CN103261396A - Biomass production - Google Patents

Biomass production Download PDF

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Publication number
CN103261396A
CN103261396A CN2011800355944A CN201180035594A CN103261396A CN 103261396 A CN103261396 A CN 103261396A CN 2011800355944 A CN2011800355944 A CN 2011800355944A CN 201180035594 A CN201180035594 A CN 201180035594A CN 103261396 A CN103261396 A CN 103261396A
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China
Prior art keywords
reaction zone
phototroph
carbonic acid
gaseous emissions
matter
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Pending
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CN2011800355944A
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Chinese (zh)
Inventor
雅伊梅·A·冈萨雷斯
马克斯·科列斯尼克
史蒂文·C·马丁
托尼·迪彼得罗
埃米迪奥·迪彼得罗
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Pond Technologies Inc
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Pond Biofuels Inc
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Priority claimed from US12/784,181 external-priority patent/US20110287523A1/en
Priority claimed from US12/784,172 external-priority patent/US8940520B2/en
Priority claimed from US12/784,126 external-priority patent/US8889400B2/en
Priority claimed from US12/784,215 external-priority patent/US8969067B2/en
Priority claimed from US12/784,106 external-priority patent/US20110283618A1/en
Priority claimed from US12/784,141 external-priority patent/US20110287522A1/en
Priority claimed from US13/022,396 external-priority patent/US20110287405A1/en
Priority claimed from CA2738397A external-priority patent/CA2738397C/en
Priority claimed from CA2738410A external-priority patent/CA2738410C/en
Priority claimed from CA2738459A external-priority patent/CA2738459C/en
Priority claimed from CA2738461A external-priority patent/CA2738461C/en
Priority to CN201510307487.2A priority Critical patent/CN104893980A/en
Application filed by Pond Biofuels Inc filed Critical Pond Biofuels Inc
Priority to CN202210473812.2A priority patent/CN115369041A/en
Publication of CN103261396A publication Critical patent/CN103261396A/en
Pending legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N13/00—Treatment of microorganisms or enzymes with electrical or wave energy, e.g. magnetism, sonic waves
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/12—Unicellular algae; Culture media therefor
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20—Bacteria; Culture media therefor
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/80—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in fisheries management

Abstract

A process of growing a phototrophic biomass in a reaction zone, including a reaction mixture that is operative for effecting photosynthesis upon exposure to photosynthetically active light radiation, is provided. The reaction mixture includes phototrophic biomass that is operative for growth within the reaction zone. In one aspect, the carbon dioxide supply is modulated in response to detected process parameters. In another aspect, inputs to the reaction zone are modulated based on changes to the carbon dioxide supply. In another aspect, dilution of the carbon dioxide-comprising supply is effected. In another aspect, pressure of the carbon dioxide-comprising supply is increased. In another aspect, water is condensed from the carbon dioxide-comprising supply and recovered for re-use.; In another aspect, the produced phototrophic biomass is harvested at a rate which approximates a predetermined growth rate of the phototrophic biomass.

Description

The manufacturing of biomass
Related application
The application is the U.S. Patent application No.12/784 that submitted on May 20th, 2010,215 part continuation application, also be the U.S. Patent application No.12/784 that submitted on May 20th, 2010,181 part continuation application, or the U.S. Patent application No.12/784 that on May 20th, 2010 submitted to, 172 part continuation application, or the U.S. Patent application No.12/784 that on May 20th, 2010 submitted to, 141 part continuation application, or the U.S. Patent application No.12/784 that on May 20th, 2010 submitted to, 126 part continuation application, or the U.S. Patent application No.12/784 that on May 20th, 2010 submitted to, 106 part continuation application, and be the U.S. Patent application No.13/022 that submitted on February 7th, 2011,396 part continuation application.
Technical field
The present invention relates to the biomass growth method.
Background technology
In order to produce fuel source, extensively cultivate phototroph.Exhaust gas discharged also has been used to promote the growth of phototroph in the industrial production, and this is to realize by the carbonic acid gas that needs to consume in photosynthesis for the phototroph supply.By being provided for the waste gas of this type of purposes, can reducing the impact of environment and can produce potential useful fuel source.Yet, for introducing this method in the existing installation, make this method have more economic attractiveness, also there is challenge greatly.
Summary of the invention
In one aspect, provide a kind of in reaction zone the method for grow light health material (phototrophic biomass).Described reaction zone comprises and can be used for carrying out photosynthetic reaction mixture being exposed under photosynthetic effective optical radiation (photosynthetically active light radiation), and wherein said reaction mixture comprises can be used for the phototroph matter of growing in described reaction zone.Described reaction mixture is being exposed under photosynthetic effective optical radiation and is causing described phototroph matter in reaction zone, to be grown, and in described reaction zone discharging phototroph matter, when phototroph matter growth indexes (growth indicator) is different from described phototroph matter growth indexes target value, adjusting is from the molar rate of described reaction zone discharging phototroph matter, the growth that wherein causes comprises the growth that causes by photosynthesis, and wherein said phototroph matter growth indexes target value is to be placed in the reaction zone and the predetermined mole growth velocity that is exposed to the phototroph matter in the reaction mixture under photosynthetic effective optical radiation is the basis.
The method of another kind grow light health material in reaction zone is provided in one aspect of the method.Described reaction zone is included in to be exposed to and can be used for carrying out photosynthetic production purposes reaction mixture under photosynthetic effective optical radiation, and wherein said production purposes reaction mixture comprises can be for the production purposes phototroph matter of growing in reaction zone.Described reaction mixture is being exposed under photosynthetic effective optical radiation and is causing described production purposes phototroph matter in reaction zone, to be grown, and in described reaction zone discharging production purposes phototroph matter, when phototroph matter growth indexes is different from the predetermined target value of described phototroph matter growth indexes, adjusting is from the molar rate of described reaction zone discharging production purposes phototroph matter, the growth that wherein causes comprises the growth that causes by photosynthesis, and wherein said phototroph matter growth indexes target value is to be placed in the reaction zone and the predetermined mole growth velocity that is exposed to the production purposes phototroph matter in the reaction mixture under photosynthetic effective optical radiation is the basis.Being predetermined to include the described production purposes reaction mixture of supply representative and can being used for carrying out photosynthetic assessment purposes reaction mixture under photosynthetic effective optical radiation being exposed to of described target value makes the phototroph matter in the described assessment purposes reaction mixture become the assessment purposes phototroph matter of the described production purposes phototroph matter of representative.When the described assessment purposes reaction mixture in placing reaction zone is exposed under photosynthetic effective optical radiation and causes described assessment purposes phototroph matter in assessment purposes reaction mixture to be grown, at least termly detect phototroph matter growth indexes, so that a plurality of detected values that are detected the described phototroph matter growth indexes of for some time to be provided, and calculate the mole growth velocity of described assessment purposes phototroph matter according to a plurality of detected values of described phototroph matter growth indexes, determine a plurality of mole growth velocitys of described assessment purposes phototroph matter in described period thus.Based on the mole growth velocity of calculating and the detected value that is used for the described phototroph matter growth indexes of the described mole of calculating growth velocity, set up the mole growth velocity of described assessment purposes phototroph matter and the relation between the described phototroph matter growth indexes, make the relation of setting up between the mole growth velocity of described assessment purposes phototroph matter and the described phototroph matter growth indexes represent the mole growth velocity of described production purposes phototroph matter in the reaction zone and the relation between the described phototroph matter growth indexes, establish the mole growth velocity of the interior described production purposes phototroph matter of reaction zone and the relation between the described phototroph matter growth indexes thus.Select the predetermined mole growth velocity of described production purposes phototroph matter.Described phototroph matter growth indexes target value is defined as: according to the relation of establishing between the mole growth velocity of described production purposes phototroph matter in the reaction zone and the described phototroph matter growth indexes, phototroph matter growth indexes when causing described predetermined mole growth velocity makes that thus also generation is related between described phototroph matter growth indexes target value and described predetermined mole growth velocity.
The method of another kind grow light health material in reaction zone is provided in one aspect of the method.Described reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, and wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone.When the described reaction mixture in will placing described reaction zone was exposed under photosynthetic effective optical radiation and causes described phototroph matter growth in the described reaction mixture, 10% of the molar rate of growing in reaction zone with described phototroph matter was discharged described phototroph matter with interior molar rate from described reaction zone.The growth that described phototroph matter is carried out in reaction zone is to be placed in the reaction zone and at least 90% the molar rate that is exposed to the maximum growth rate of the phototroph matter in the reaction mixture under photosynthetic effective optical radiation is carried out.
The method of another kind grow light health material in reaction zone is provided in one aspect of the method.Described reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, and wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone.When described reaction mixture being exposed under photosynthetic effective optical radiation and causing placing described phototroph matter growth in the reaction mixture of reaction zone, from reaction zone discharging phototroph matter make phototroph matter the discharging molar rate molar rate that described phototroph matter is grown 10% in, the growth of the described phototroph matter that wherein causes comprises the growth that causes by photosynthesis.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: at gaseous emissions production process discharging gaseous emissions, the any described gaseous emissions defined reaction district that wherein is provided to described reaction zone is with the gaseous emissions feed time, based on the detection of at least a carbon dioxide treatment figureofmerit being regulated described reaction zone with the supply of gaseous emissions feed to described reaction zone.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: at gaseous emissions production process discharging gaseous emissions, and the described gaseous emissions of at least a portion is provided to described reaction zone, the described at least a portion gaseous emissions defined reaction district that wherein is provided to reaction zone is with the gaseous emissions feed time, be provided to the supply molar rate of the described reaction zone usefulness gaseous emissions feed of reaction zone in reduction, or when stopping described reaction zone with the supply of gaseous emissions feed, this method comprises that further startup contains the raw material of make-up gas to the supply of described reaction zone, perhaps increases the supply of raw material molar rate that contains make-up gas to described reaction zone supply.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: reaction zone is supplied to reaction zone with the gaseous emissions feed, wherein at least a portion of the gaseous emissions that produces of gaseous emissions production process limits described reaction zone gaseous emissions feed, and wherein said reaction zone comprises carbonic acid gas with the gaseous emissions feed; And replenish the aqueous substance feed from container to described reaction zone supply, wherein said additional aqueous substance feed comprises from reaction zone and is condensed with the gaseous emissions feed and is collected in aqueous materials in the container, and the condensation of wherein said aqueous materials is to realize when cooling off before reaction zone is provided to reaction zone with the gaseous emissions feed.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: at gaseous emissions production process discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone discharges with discharging carbonic acid gas feed, input at least a input thing of described reaction zone at least with the molar rate adjusting of discharging carbonic acid gas feed according to the described reaction zone that is supplied to reaction zone.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: at gaseous emissions production process discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone discharges with discharging carbonic acid gas feed, regulate at least a input thing that inputs to described reaction zone according to the reaction zone that is supplied to reaction zone with the molar rate index of discharging the carbonic acid gas feed at least.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: at gaseous emissions production process discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone discharges with discharging carbonic acid gas feed, when detecting the vicissitudinous indication of molar rate of the described reaction zone usefulness discharging carbonic acid gas feed that is provided to reaction zone, regulate at least a input thing of the described reaction zone of input.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: at gaseous emissions production process discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone discharges with discharging carbonic acid gas feed, when the molar rate that detects the described reaction zone usefulness discharging carbonic acid gas feed that is supplied to reaction zone reduces, perhaps when detecting the described reaction zone that the is supplied to reaction zone molar rate with discharging carbonic acid gas feed the indication of reduction arranged, have additional supply of to the molar rate of the additional carbonic acid gas feed of reaction zone, or begin described additional carbonic acid gas feed is supplied to reaction zone.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: with reaction zone carbonic acid gas feed to be enough to making described reaction zone carbonic acid gas feed streams before the pressure of at least 70 inches reaction zone degree of depth is supplied to reaction zone, promote the pressure of described reaction zone carbonic acid gas feed through injector (eductor) or jet-pump (jet pump) by making described reaction zone carbonic acid gas feed streams.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: with reaction zone carbonic acid gas feed to be enough to making described reaction zone carbonic acid gas feed streams before the pressure of at least 70 inches reaction zone degree of depth is supplied to reaction zone, utilize Venturi (venturi) effect to drive the described reaction zone carbonic acid gas of flow direction feed from one and shift pressure energy.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: when reaction zone feeding material is provided to described reaction zone, supply described reaction zone feeding material and additional gaseous diluent, the carbonic acid gas volumetric molar concentration of wherein said additional gaseous diluent is lower than the carbonic acid gas volumetric molar concentration that the reaction zone that is provided to reaction zone feeding material is used the gaseous emissions feed.
In one aspect of the method, provide a kind of in reaction zone the method for grow light health material, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, described method comprises: when supply concentrates the carbonic acid gas feed, to produce the carbonic acid gas feed of dilution, the carbonic acid gas volumetric molar concentration of the carbonic acid gas feed of wherein said dilution is lower than the carbonic acid gas volumetric molar concentration of described concentrated carbonic acid gas feed with described concentrated carbonic acid gas feed and additional gaseous diluent blending; And the reaction zone of the described dilution of at least a portion is supplied to reaction zone with the carbonic acid gas feed.
Description of drawings
The method of the preferred embodiment of the invention is described below with reference to following accompanying drawing.
Fig. 1 is the schema of an embodiment of the inventive method.
Fig. 2 is the schema of another embodiment of the inventive method.
Fig. 3 is the partial schematic diagram of the fluid channel in the embodiment of the inventive method.
Embodiment
In the full text of this specification sheets, its implication is when mentioning " some embodiments ": be not inevitable these embodiments that just refer in conjunction with the described special characteristic of some embodiments, structure or characteristic.In addition, can make up described special characteristic, structure or characteristic mutually according to any suitable mode.
Referring to shown in Figure 1, its provide a kind of in reaction zone 10 method of grow light health material.Described reaction zone 10 is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation.Described reaction mixture comprises phototroph raw material, carbonic acid gas and water.In some embodiments, described reaction zone comprises phototroph matter and the carbonic acid gas that places in the aqueous medium.In reaction zone, described phototroph matter is configured to can both carry out the mass transfer exchange with carbonic acid gas and water.In some embodiments, for example, described reaction mixture comprises the phototroph matter that places in the aqueous medium, and provides the phototroph that is rich in carbonic acid gas matter after phototroph matter receives carbonic acid gas.
" phototroph " is can be by the biology of phototrophy growth, for example vegetable cell and microorganism when receiving luminous energy in aqueous medium.Described phototroph can be unicellular or many cells.In some embodiments, for example, described phototroph is the biology through artificial modified or genetic modification.In some embodiments, for example, described phototroph is algae.In some embodiments, for example, described algae is microalgae (microalgae).
" phototroph matter " is at least a phototroph.In some embodiments, for example, described phototroph matter comprises more than a kind of phototroph kind.
" reaction zone 10 " limits the space of described phototroph matter growth.In some embodiments, in bioreactor 12, provide described reaction zone 10.In some embodiments, for example, the pressure in the described reaction zone is barometric point.
" bioreactor 12 " can be any structure, the zone of the suitable environment that maybe can be provided for grow light health material of disposing, level land.Thereby can utilize luminous energy when growth required space to include, but are not limited to basin, pond, groove, canal, pond, pipe, pipeline, channel and water channel as the example of the particular configuration of bioreactor 12 by providing for phototroph matter.That this type of bioreactor can be is open, closed, semi-enclosed, cover type or part cover type.In some embodiments, for example, described bioreactor 12 is open ponds, and this moment, described pond can unrestrictedly receive raw material and luminous energy from surrounding environment.In other embodiments, for example, described bioreactor 12 is ponds that cover or partly cover, and this moment, at least part of obstruction was from receiving raw material on every side.Described bioreactor 12 comprises the reaction zone 10 that contains reaction mixture.In some embodiments, described bioreactor 12 is configured to receive phototrophy reagent (and in certain embodiments, optional additional nutrient) supply, and the structure that also is configured to give off the phototroph matter of growth in the reaction zone 10.Thus, in some embodiments, described bioreactor 12 comprises for the one or more entrances that receive phototrophy reagent and additional nutrient supply, and also comprises one or more outlets of reclaiming or gathering in the crops the biomass of growth in the reaction zone 10.In some embodiments, for example, one or more entrances are configured to and can temporarily seal according to the periodic or interrupted timed interval.In some embodiments, for example, one or more outlets are configured to can be according to the temporary transient sealing of the periodic or interrupted timed interval or sealing in fact.Described bioreactor 12 is configured to contain being exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation.Described bioreactor 12 also is configured to have photosynthetic effective optical radiation of being positioned at described bioreactor 12 and being used for the described phototroph matter of irradiation (for example the wavelength that can be launched by the sun or other light sources is between the light of about 400 ~ 700nm).Described reaction mixture can make described phototroph matter produce photosynthesis and growth through the irradiation of photosynthetic effective optical radiation.In some embodiments, for example, provide the optical radiation of joining by placing the artificial light 14 in the bioreactor 12.For example, suitable artificial light comprises sunk optical fiber, photoconduction, photodiode (LED), LED band and fluorescence.Any LED band known in the art is all applicable in the described bioreactor 12.In some embodiments of using sunk LED, for example, the energy of supplying electric power for described LED comprises substitute energy for example wind, photovoltaic cell, fuel cell etc.The outside of bioreactor 12 or inside can use fluorescence as redundant system.In some embodiments, for example, the light of joining comes from lamp 16, described light be from the external emission of bioreactor 12 and pass conveying member.In some embodiments, for example, described conveying member is the part of bioreactor 12 containment structures, and it can partly see through photosynthetic effective optical radiation at least, and be configured to can with described light transmission to reaction zone 10 to be received by phototroph matter.In some embodiments, for example, natural light is received, filters, transfers to described reaction zone 10 through fiber optic materials or photoconduction then through the selective wavelength spectral filter by solar energy collector.In some embodiments, for example, these two provides the photosynthetic effective optical radiation in the described bioreactor 12 by lamp and artificial light.
" aqueous medium " is a kind of environment that comprises water.In some embodiments, for example, described aqueous medium also includes the adequate nutrients that helps the survival of phototroph matter and growth.In some embodiments, for example, additional nutrient can comprise for example NO xAnd SO xIn one or the two.Suitable aqueous medium has been specified in the following document: Rogers, L.J. with " Biochemistry of the Algae and Cyanobacteria " (biological chemistry of algae and cyanobacteria) of Gallon J.R., Oxford Clarendon press 1988; Burlew, " Algal Culture:From Laboratory to Pilot Plant " (algae culture: from the laboratory to the pilot plant) of John S., Washington press of Carnegie institute 600, Washington D.C. 1961(is " Burles1961 " hereinafter referred to as); And Round, F.E., The Biology of the Algae (algological biology), New York Sheng Mading press 1965; Above-mentioned document is incorporated this paper into way of reference respectively.Suitable the supplementing the nutrients of a kind of being called as " Bold basic medium " is specified in Bold, H.C.1949, the morphology of The morphology of Chlamydomonas chlamydogama sp.nov.Bull.Torrey Bot.Club.76:101-8(Chlamydomonas chlamydogama kind) (also can be referring to Bischoff, H.W. and Bold, H.C.1963, Phycological Studies IV.Some soil algae from Enchanted Rock and related algal species (algae research IV. is from some soil algaes of bewitched rock and relevant algae), University of Texas press, 6318:1 ~ 95; And Stein, J. (editor), Handbook of Phycological Methods, Culture methods and growth measurements (algae method, culture method and growth measurement handbook), the 7th ~ 24 page of Cambridge University Press).
" adjusting " with regard to process variable (for example inputing or outputing) refers to beginning, stops, increases, reduces or otherwise changes any in these operations of processing parameter (processing parameter that for example inputs or outputs).
In some embodiments, described method comprises carbonic acid gas is supplied to reaction zone 10.In some embodiments in these embodiments, for example, the described carbonic acid gas that is supplied to reaction zone 10 is from the gaseous emissions 18 that contains carbonic acid gas.Thus, in some embodiments, the described carbonic acid gas of gaseous emissions production process 20 supplies, therefore, described supply is realized by the gaseous emissions 18 that discharges from gaseous emissions production process 20.In some embodiments, for example, at least a portion of the carbonic acid gas that described gaseous emissions production process 20 discharges is provided to reaction zone 10, and the carbonic acid gas defined reaction district that wherein said at least a portion that is provided to reaction zone 10 is discharged is with discharging the carbonic acid gas feed.In some embodiments, for example, at least a portion of the gaseous emissions 18 that described gaseous emissions production process 20 discharges is provided to reaction zone 10, the wherein said at least a portion gaseous emissions 18 defined reaction districts that are provided to reaction zone 10 are with gaseous emissions feed 24, make described reaction zone be provided to reaction zone 10 as reaction zone with the part (together with other non-carbonic acid gas raw materials from gaseous emissions 18) of gaseous emissions feed 24 with discharging the carbonic acid gas feed.In some embodiments in these embodiments, for example, when reaction zone is provided to reaction zone 10 with gaseous emissions feed 24, make the described phototroph matter that places in the reaction zone 10 be exposed to photosynthetic effective optical radiation.
In some embodiments, for example, based on the cumulative volume calculating of gaseous emissions 18, the concentration of carbon dioxide that described gaseous emissions 18 comprises is at least 2 volume %.Thus, in some embodiments, for example, calculate based on the cumulative volume of reaction zone with gaseous emissions feed 24, described reaction zone is at least 2 volume % with the concentration of carbon dioxide that gaseous emissions feed 24 comprises.In some embodiments, for example, based on the cumulative volume calculating of gaseous emissions 18, the concentration of carbon dioxide that described gaseous emissions 18 comprises is at least 4 volume %.Thus, in some embodiments, for example, calculate based on the cumulative volume of reaction zone with gaseous emissions feed 24, described reaction zone is at least 4 volume % with the concentration of carbon dioxide that gaseous emissions feed 24 comprises.In some embodiments, for example, described reaction zone also contains NO with gaseous emissions feed 24 xAnd SO xIn one or the two.
In some embodiments, for example, at least a portion gaseous emissions 18 that is supplied to reaction zone 10 is processed before being supplied to described reaction zone 10, thereby can remove the undesirable composition in the gaseous emissions 18 effectively, and the feasible material that is provided at least a portion gaseous emissions 18 of reaction zone 10 is formed the material composition that is different from the gaseous emissions 18 that gives off from gaseous emissions production process 20.
Described gaseous emissions production process 20 comprises that effective real estate is given birth to and any process of discharging gaseous emissions 18.In some embodiments, for example, at least a portion gaseous emissions 18 that gaseous emissions production process 20 discharges is provided to described reaction zone 10.Gaseous emissions production process 20 described at least a portion gaseous emissions 18 that discharge and that be provided to reaction zone 10 contains the carbonic acid gas from gaseous emissions production process 20.In some embodiments, for example, described gaseous emissions production process 20 is a kind of combustion processeses.In some embodiments, for example, in a combustion equipment, carry out described combustion processes.In some embodiments in these embodiments, for example, for example coal, oil or Sweet natural gas carry out described combustion processes to use fossil oil.For example, described combustion equipment is any in fossil fired power plant, industrial burning facility, industrial furnace, industrial well heater or the oil engine.In some embodiments, for example, described combustion equipment is cement kiln.
Reaction zone feeding material 22 is provided to described reaction zone 10, thereby makes the carbonic acid gas that receives in the reaction zone 10 in the described reaction zone feeding material 22.At least a portion carbonic acid gas in the reaction zone feeding material 22 is from described gaseous emissions 18.In at least some operating periods of described method, the reaction zone feeding material 22 of at least a portion is to be supplied by the gaseous emissions 18 of gaseous emissions production process 20 dischargings.As mentioned above, any gaseous emissions 18 that is supplied to reaction zone 10 is supplied as reaction zone with gaseous emissions feed 24.In some embodiments in these embodiments, for example, when described reaction zone is provided to reaction zone 10 with gaseous emissions feed 24, make the phototroph matter that places in the reaction zone 10 be exposed to photosynthetic effective optical radiation.Should be appreciated that in certain embodiments, is not that whole gaseous emissions 18 all must be provided to described reaction zone 10 with gaseous emissions feed 24 as reaction zone, thereby described reaction zone feeding material 22 comprises reaction zone gaseous emissions feed 24.It is also understood that in some embodiments gaseous emissions 18 or its at least a portion are also nonessential all to be provided to described reaction zone 10 as reaction zone with gaseous emissions feed 24 in the whole time period of described method operation.Described reaction zone contains carbonic acid gas with gaseous emissions feed 24.In some embodiments in these embodiments, for example, described reaction zone is at least a portion of the gaseous emissions 18 of gaseous emissions production process 20 dischargings with gaseous emissions feed 24.In some instances, whole gaseous emissions 18 of gaseous emissions production process 20 dischargings are supplied as reaction zone gaseous emissions feed 24.
With regard to reaction zone feeding material 22, described reaction zone feeding material 22 is fluids.In some embodiments, for example, described reaction zone feeding material 22 is gaseous substances.In some embodiments, for example, described reaction zone feeding material 22 contains the gaseous substance that places in the liquid material.In some embodiments, for example, described liquid material is water-based material.In some embodiments in these embodiments, for example, the gas of at least a portion is dissolved in the described liquid material.In some embodiments in these embodiments, for example, the gas of at least a portion is configured to be scattered in the gas diffuser in the described liquid material.In some embodiments in these embodiments, for example, at least some operating periods of described method, the gas in the described reaction zone feeding material 22 contains by the carbonic acid gas of reaction zone with 24 supplies of gaseous emissions feed.In some embodiments in these embodiments, for example, described reaction zone feeding material 22 is provided to reaction zone 10 in the mode of streams.In some embodiments, for example, reaction zone feeding streams 22 comprises gaseous emissions reaction zone feeding material supply stream 24.In some embodiments, for example, reaction zone feeding streams 22 is gaseous emissions reaction zone feeding material supply stream 24.
In some embodiments, for example, described reaction zone feeding material 22 is provided to reaction zone 10 in the mode of one or more strands of reaction zone feeding streams.For example, flow through respectively separately reaction zone feeding material fluid channel of described one or more strands of reaction zone feeding streams.In some embodiments in these embodiments, when existing more than one reaction zone feeding streams, have different materials between the described reaction zone feeding streams and form.
In some embodiments, for example, the described reaction zone feeding material 22 of cooling before being supplied to reaction zone 10 makes the proper temperature of temperature convergence phototroph mass-energy growth of described reaction zone feeding material 22.In some embodiments, for example, the described reaction zone that is supplied to reaction zone feeding material 22 is set between 110 to 150 ℃ with the temperature of gaseous emissions feed 24.In some embodiments, for example, described reaction zone is about 132 ℃ with the temperature of gaseous emissions feed 24.In some embodiments, reaction zone is configured to far above described temperature with the temperature of gaseous emissions feed 24, and in some embodiments, for example uses the temperature of gaseous emissions feed 24 above 500 ℃ from the reaction zone of steelworks.In some embodiments, for example, contain reaction zone and be cooled between 20 ℃ and 50 ℃ (for example about 30 ℃) with the described reaction zone feeding material 22 of gaseous emissions feed 24.In some embodiments, described reaction zone feeding material 22 is limited with gaseous emissions feed 24 by reaction zone.The reaction zone feeding material 22 of supply comparatively high temps may hinder the growth of the phototroph matter in the reaction zone 10, perhaps even kill phototroph matter in the reaction zone 10.In some embodiments in these embodiments, when condensation reaction district feeding material 22, at interchanger 26(condenser for example) in the condensation reaction district with at least a portion of any water vapor in the gaseous emissions feed 24 and itself and reaction zone feeding material 22 are separated and become aqueous materials 70.In some embodiments, the aqueous materials 70 of formation is provided to container 28(such as following), in described container 28, aqueous materials 70 provides the additional aqueous substance feed 44 that is used for being supplied to reaction zone 10.In some embodiments, described condensation produces heat passage from reaction zone feeding material 22 to heat-transfer medium 30, therefore the temperature of heat-transfer medium 30 rises and has produced the heat-transfer medium 30 that is heated, the described heat-transfer medium that is heated 30 is provided to (for example flowing to) drying machine 32(such as following then), and carry out heat passage from the described heat-transfer medium that is heated 30 to middle concentration response district product 34, concentration response district product 34 produces final reaction zone product 36 thus in the middle of described with drying.In some embodiments, for example, after drying machine 32 dischargings, described heat-transfer medium 30 is recirculated to interchanger 26.The example of suitable heat-transfer medium 30 comprises thermal oil and ethylene glycol solution.
In some embodiments, for example, reaction zone feeding material 22 can cause the phototroph matter of at least a portion in the reaction zone 10 to be stirred to the supply of reaction zone 10.Thus, in some embodiments, for example, described reaction zone feeding material 22 is introduced into part lower in the reaction zone 10.In some embodiments, for example, introduce the below in described reaction zone feeding material 22 autoreaction districts 10, thereby can cause the content of reaction zone 10 mixed.In some embodiments in these embodiments, for example, the mixing that causes (or stirring) can make any difference of phototroph matter volumetric molar concentration any in the reaction zone 10 all be lower than 20% at 2.In some embodiments, for example, any difference of any 2 phototroph matter volumetric molar concentration is lower than 10% in the reaction zone 10.In some embodiments in these embodiments, for example, the mixing that causes can make the suspension that produce homogeneous in the reaction zone 10.Use in the embodiment of bioreactor 12 at these, for some embodiments in these embodiments, for example, the supply of described reaction zone feeding material 22 be configured to can with bioreactor 12 co-operatings, make to place at least a portion phototroph matter in the reaction zone 10 to produce required stirring.
Further those embodiments that 22 supplies to described reaction zone 10 cause placing at least a portion phototroph matter in the reaction zone 10 to be stirred at reaction zone feeding material, in some embodiments in these embodiments, for example, described reaction zone feeding material 22 before being introduced into described reaction zone 10, flow through a gas injection mechanism such as shower nozzle (sparger) 40.In some embodiments in these embodiments, for example, described shower nozzle 40 makes reaction zone feeding material 22 formation that are supplied to reaction zone 10 contain the solution-airmixture that is trapped in the microbubble in the liquid phase, (the SO for example and in some embodiments, so that the carbonic acid gas in phototroph matter and the reaction zone feeding material 22 xAnd NO xOne or both) between form maximum interface contact area.This helps described phototroph matter to absorb effectively for the required carbonic acid gas of photosynthesis (and other gaseous constituents in some embodiments), thereby can impel the growth velocity of described phototroph matter to reach optimizing.In addition, in some embodiments, for example, described shower nozzle 40 makes reaction zone feeding material 22 form bigger bubble, and it stirs the phototroph matter in the reaction zone 10, thereby promotes the mixing of each composition in the reaction zone 10.The example of suitable shower nozzle 40 is the EDI FlexAir of Colombia city, Missouri State Enviornmental Dynamics company TMThe jet pipe of T-series 91X1003 model.In some embodiments, for example, this shower nozzle 40 is placed in the bioreactor 12, described bioreactor 12 has the reaction zone 10 of 6000 liter capacities, and algae concentration is between 0.8 grams per liter to 1.5 grams per liter, and reaction zone feeding material 22 is the flow of gaseous fluid with the pressure supply of the flow velocity between 10 cubic feet/min to 20 cubic feet/min and about 68 inch of water.
About shower nozzle 40, in some embodiments, for example, the pressure head (fluid head) of considering reaction zone 10 designs described shower nozzle 40, make and supply reaction zone feeding materials 22 to reaction zone 10 by this way, described mode can promote the absorption of phototroph confrontation carbonic acid gas to reach optimizing.Thus, regulate the size of bubble, make bubble be small enough to promote that the absorption of the carbonic acid gas in the phototroph confrontation reaction zone feeding material reaches best.Simultaneously, the size of bubble will be even as big as making at least a portion bubble rise by whole height of reaction zone 10, reduces reaction zone feeding material 22 " bubbling passes " reaction zone 10 simultaneously and do not absorbed with regard to d/d situation by phototroph matter.In some embodiments, for the bubble size that promotes to reach best, utilize the pressure of pressure-regulator control reaction zone feeding material 22 in the upstream of described shower nozzle 40.
With regard to the embodiment in reaction zone 10 places bioreactor 12, in some embodiments in these embodiments, for example, described shower nozzle 40 is placed in the outside of bioreactor 12.In other embodiments, for example, described shower nozzle 40 is placed in the bioreactor 12.In some embodiments in these embodiments, for example, described shower nozzle 40 extends (and in bioreactor 12) from the bottom of bioreactor 12.
In one aspect, carbonic acid gas is provided to reaction zone 10, and the described carbonic acid gas defined reaction district carbonic acid gas feed 2402 that is supplied.Described reaction zone carbonic acid gas feed 2402 is so that reaction zone carbonic acid gas feed streams is provided to reaction zone 10 through the pressure of at least 70 inches reaction zone degree of depth.In some embodiments, for example, the described degree of depth is at least 10 feet.In some embodiments, for example, the described degree of depth is at least 20 feet.In some embodiments, for example, the described degree of depth is at least 30 feet.In some embodiments, for example, before being provided to reaction zone 10, increase the pressure of described reaction zone carbonic acid gas feed 2402.In some embodiments, when gaseous emissions production process 20 produces gaseous emissions 18, increase the pressure of described reaction zone carbonic acid gas feed 2402.In some embodiments, for example, when reaction zone carbonic acid gas feed is provided to reaction zone 10, increase the pressure of described reaction zone carbonic acid gas feed 2402.In some embodiments, for example, when reaction zone carbonic acid gas feed 2402 is provided to reaction zone 10, will place the described phototroph matter in the reaction zone 10 to be exposed under photosynthetic effective optical radiation.
In some embodiments, for example, at least part of primover (prime mover) 38 that utilizes increases described pressure.With regard to these embodiments, described pressure increase to small part owing to described primover 38.With regard to reaction zone carbonic acid gas feed 2402 was the part of reaction zone feeding material 22 and embodiment that described reaction zone feeding material 22 comprises liquid material, the example of suitable primover 38 was pump.With regard to the embodiment that increases described pressure by air-flow, the example of suitable primover 38 comprises gas blower, compressor and pneumatic pump.In other embodiments, for example, increase described pressure by jet-pump or injector.
When increasing described pressure by jet-pump or injector, in some embodiments in these embodiments, for example, described reaction zone carbonic acid gas feed 2402 is provided to jet-pump or injector, and utilize Venturi effect to transmit the pressure energy from another streaming fluid (i.e. " motive fluid stream " (motive fluid flow)) to described reaction zone carbonic acid gas feed, thereby increase the pressure in the reaction zone carbonic acid gas feed.Thus, in some embodiments, for example, referring to Fig. 3, provide motive fluid stream 700, the raw material of wherein said motive fluid stream 700 has the kinetic current pressure P M1Thus, also provide and have pressure P ELow pressure attitude reaction zone carbonic acid gas feed 2402A, the carbonic acid gas feed 2402A of wherein said low pressure attitude comprises reaction zone carbonic acid gas feed 2402.In some embodiments, described low pressure attitude reaction zone carbonic acid gas feed 2402A is limited by reaction zone carbonic acid gas feed 2402.The P of motive fluid stream M1The P that is higher than low pressure attitude carbonic acid gas feed 2402A EBy making the downstream canal part 704 of motive fluid stream 700 in the middle of flowing to from upstream canal part 702, and the pressure that makes motive fluid stream 700 is from P M1Be reduced to P M2, make P thus M2Be lower than P EBeing characterized as of middle downstream canal part 704: it is long-pending to have small cross section with respect to upstream canal part 702.By making motive fluid stream 700 flow to middle downstream canal part 704 from upstream canal part 702, make static energy be transformed into kinetic energy.When the pressure of motive fluid stream 700 is reduced to P M2The time, the generation fluid is communicated with between motive fluid stream 700 and the low pressure attitude carbonic acid gas feed 2402A, thus, in response to the pressure reduction between low pressure attitude carbonic acid gas feed 2402A and the motive fluid stream 700, make low pressure attitude carbonic acid gas feed 2402A in the downstream canal part 704 of centre, mix with described motive fluid stream 700, thereby produce the mixture 2404 that comprises reaction zone carbonic acid gas feed, it comprises described reaction zone carbonic acid gas feed 2402.The described mixture 2404 that comprises reaction zone carbonic acid gas feed of at least a portion is provided to reaction zone 10.It comprises reaction zone carbonic acid gas feed 2402 the described mixture 2404(that comprises reaction zone carbonic acid gas feed) pressure be raised to P M3, make the pressure of described reaction zone carbonic acid gas feed 2402 also be raised to P M3P M3Be higher than P EAnd also enough reaction zone carbonic acid gas feed 2402 is supplied to reaction zone 10, and, when reaction zone carbonic acid gas feed 2402 is supplied to reaction zone 10, can make flow through at least 70 inches reaction zone 10 degree of depth of described reaction zone carbonic acid gas feed 2402.In some embodiments, for example, P M3Be higher than P EAnd also be enough to described reaction zone carbonic acid gas feed 2402 is supplied to reaction zone 10, and, when reaction zone carbonic acid gas feed 2402 is supplied to reaction zone 10, can make flow through at least 10 feet reaction zone 10 degree of depth of described reaction zone carbonic acid gas feed 2402.In some embodiments, for example, P M3Be higher than PE and also be enough to described reaction zone carbonic acid gas feed 2402 is supplied to reaction zone 10, and, when reaction zone carbonic acid gas feed 2402 is supplied to reaction zone 10, can make flow through at least 20 feet reaction zone 10 degree of depth of described reaction zone carbonic acid gas feed 2402.In some embodiments, for example, P M3Be higher than P EAnd also be enough to described reaction zone carbonic acid gas feed 2402 is supplied to reaction zone 10, and, when reaction zone carbonic acid gas feed 2402 is supplied to reaction zone 10, can make flow through at least 30 feet reaction zone 10 degree of depth of described reaction zone carbonic acid gas feed 2402.In any of these embodiment, the rising of described pressure is designed to overcome the pressure head in the reaction zone 10.By making the mixture 2404 that comprises reaction zone carbonic acid gas feed flow to the downstream canal part 706 of " kinetic energy is changed to static energy " from the downstream canal part 704 of centre, pressure can raise.The cross-sectional area of the downstream canal part 706 of " kinetic energy is changed to static energy " is greater than the cross-sectional area of the downstream canal part 704 of described centre, thereby make (to have flowed to this fact of runner section with comparatively large cross-sectional area owing to the described mixture 2404 that comprises reaction zone carbonic acid gas feed) when the described mixture 2404 that comprises reaction zone carbonic acid gas feed has been arranged in the downstream canal part 706 of " kinetic energy is changed to static energy ", the kinetic energy of the mixture 2404 that comprises reaction zone carbonic acid gas feed of the downstream canal part 704 in the middle of described being positioned at is transformed into static energy.In some embodiments, for example, the converging nozzle of runner partly limits described upstream canal part 702, and the downstream canal part 706 that the divergent nozzle of runner partly limits described " kinetic energy is changed to static energy ", 704 of the downstream canal parts of described centre place the centre of described converging nozzle part and divergent nozzle part.In some embodiments, for example, the combination of the downstream canal part 706 of described upstream canal part 702 and described " kinetic energy is changed to static energy " is limited by venturi nozzles (venture nozzle).In some embodiments, for example, the combination of the downstream canal part 706 of described upstream canal part 702 and described " kinetic energy is changed to static energy " is placed in injector or the jet-pump.In some embodiments in these embodiments, for example, described motive fluid stream 700 comprises the liquid waterborne material, and thus, the described mixture 2404 that contains reaction zone carbonic acid gas feed comprises the liquids and gases raw material combination.Thus, in some embodiments, for example, the described mixture 2404 that contains reaction zone carbonic acid gas feed comprises the dispersion of gaseous state material in liquid material, and wherein said gaseous state material dispersed body comprises reaction zone carbonic acid gas feed.Perhaps, in some embodiments in these embodiments, for example, described motive fluid stream 700 is another kind of gas streams, airflow for example, and then the described mixture that contains reaction zone carbonic acid gas feed is gaseous state.The described mixture 2404 that contains reaction zone carbonic acid gas feed of at least a portion is provided to reaction zone feeding material 22, thereby the mixture that described at least a portion can be contained reaction zone carbonic acid gas feed is supplied to reaction zone 10.Thus, the carbonic acid gas in the described reaction zone feeding material 22 comprises at least a portion of reaction zone carbonic acid gas feed 2402.In some embodiments, for example, the carbonic acid gas in the described reaction zone feeding material 22 is limited by at least a portion of reaction zone carbonic acid gas feed 2402.
In some embodiments in these embodiments, for example, described reaction zone carbonic acid gas feed 2402 is that at least a portion in the gaseous emissions 18 that is discharged by described gaseous emissions production process 20 is supplied, and when described gaseous emissions production process 20 discharging gaseous emissions 18 and described reaction zone carbonic acid gas feed 2402 were provided to reaction zone 10, the described at least a portion in the gaseous emissions of having realized being discharged by described gaseous emissions production process 20 18 was supplied described reaction zone carbonic acid gas feed 2402.Thus, in some embodiments, for example, described reaction zone carbonic acid gas feed 2402 is that at least a portion in the carbonic acid gas that discharges by described gaseous emissions production process 20 is supplied, and when described gaseous emissions production process 20 discharging carbonic acid gas and described reaction zone carbonic acid gas feed 2402 were provided to reaction zone 10, the described at least a portion in the carbonic acid gas of having realized being discharged by described gaseous emissions production process 20 was supplied described reaction zone carbonic acid gas feed 2402.In some embodiments, for example, described reaction zone carbonic acid gas feed 2402 is limited with discharging carbonic acid gas feed by reaction zone.
In some embodiments, for example, described bioreactor 12 or a plurality of light light thing reactor 12 are configured to make that the carbon dioxide absorbency of phototroph matter reaches optimizing and reduces energy requirement.Thus, described bioreactor is configured to prolong the residence time of carbonic acid gas in reaction zone 10.In addition, make the movement of described carbonic acid gas on horizontal throw reach minimum, thereby reduce energy expenditure.For this purpose, described one or more bioreactors 12 are higher relatively and less area coverage (footprint) is provided, thereby the residence time that prolongs carbonic acid gas is saved energy simultaneously.
In some embodiments, for example, to described reaction zone 10 supply extra-nutrition thing feed 42.In some embodiments in these embodiments, for example, when described extra-nutrition thing feed 42 is provided to reaction zone 10, place the phototroph matter in the reaction zone 10 to be exposed under photosynthetic effective optical radiation with described.In some embodiments, for example, supply described extra-nutrition thing feed 42 by the pump such as volume pump.In other embodiments, for example, described extra-nutrition thing feed 42 manually is supplied to reaction zone 10.Nutrition in the reaction zone 10 are handled or are consumed by phototroph matter, and in some cases preferably, replenish the described processed or nutrition that consumed again.A kind of suitable nutritive compositions is " BoldShi basic medium ", it has been described in Bold, H.C.1941, the morphology of The morphology of Chlamydomonas chlamydogama sp.(Chlamydomonas chlamydogama kind), Nov.Bull.Torr.Bot.Club.76:101 ~ 8(also can be referring to Bischoff, H.W. and Bold, H.C.1963, Phycological Studies IV.Some soil algae from Enchanted Rock and related algal species (algae research IV. is from some soil algaes of bewitched rock and relevant algae), University of Texas press, 6318:1 ~ 95; And Stein, J. (editor) Handbook of Phycological Methods, Culture methods and growth measurements (algae method, culture method and growth measurement handbook), the 7th ~ 24 page of Cambridge University Press).The nutrition that described extra-nutrition thing feed 42 is used in the postreaction district is as " BoldShi basic medium ", the perhaps composition of its one or more dissolvings.Thus, in some embodiments, for example, described extra-nutrition thing feed 42 comprises " BoldShi basic medium ".In some embodiments, for example, described extra-nutrition thing feed 42 comprises the composition of one or more dissolvings of " BoldShi basic medium ", for example NaNO 3, CaCl 2, MgSO 4, KH 2PO 4, NaCl, or other materials in the moiety of its dissolving.
In some embodiments in these embodiments, the required growth velocity of phototroph matter is controlled to the delivery rate of the described extra-nutrition thing feed 42 of described reaction zone 10 supplies in the complex reaction district 10.In some embodiments, for example, by measuring pH, the NO in the reaction zone 10 3The arbitrary combination of concentration and conductivity is monitored nutrition is added the adjusting of doing.
In some embodiments, for example, described additional aqueous substance feed 44 is provided to reaction zone 10, thus the moisture in the reaction zone 10 of additional bioreactor 12.In some embodiments, for example, and as hereinafter further as described in, the supply of described additional aqueous substance feed 44 makes product discharge from described bioreactor 12.For example, described additional aqueous substance feed 44 makes product discharge from bioreactor 12 in the overflow mode.
In some embodiments, for example, described additional aqueous materials is water.
In one aspect of the method, described additional aqueous substance feed 44 comprises at least a in following: when (a) before reaction zone feeding material 22 is provided to reaction zone 10, standing to cool off, and the aqueous materials 70 that condensation goes out from described reaction zone feeding material 22; And (b) from the discharging the product that contains phototroph matter 500 isolated aqueous materials.In some embodiments, for example, described additional aqueous substance feed 44 is independently originated from one (that is, the source beyond the described technology), for example Urban water supply.
In some embodiments, for example, by the described additional aqueous substance feed 44 of pump 281 supplies.In some embodiments in these embodiments, for example, described additional aqueous substance feed 44 is continued to be supplied to reaction zone 10.
In some embodiments, for example, the described additional aqueous substance feed 44 of at least a portion is by container 28 supplies, and this will be in hereinafter being described further.At least a portion in the aqueous materials that recovery is discharged by described technology, and it the additional aqueous materials of described container 28 to provide described container 28 to hold is provided.
With reference to Fig. 2, in some embodiments, described extra-nutrition thing feed 42 and described additional aqueous substance feed 44 were provided to reaction zone feeding material 22 by shower nozzle 40 before being provided to reaction zone 10.In the embodiment in reaction zone 10 is placed in described bioreactor 12, in some embodiments in these embodiments, for example, described shower nozzle 40 is placed in the outside of described bioreactor 12.In some embodiments, preferably, in described shower nozzle 40, mix described reaction zone feeding material 22, extra-nutrition thing feed 42 and additional aqueous substance feed 44, because can make these compositions can obtain the better mixing effect when separately supplying described reaction zone feeding material 22, extra-nutrition thing feed 42 and additional aqueous substance feed 44 like this.On the other hand, the saturation limit of the gaseous state material in the described reaction zone feeding material 22 limits described reaction zone feeding material 22 to the delivery rate of reaction zone 10 in the mixture by means of blending.Because this mean method, when providing to reaction zone 10 when the required time of response of the carbonic acid gas supply of adjusting is so not urgent relatively (this depends on the biological need of employed phototroph), this type of embodiment is more suitable.
In one aspect of the method, with supplement the nutrients additional water-based mixing of materials in thing feed 42 and the described container 28 of at least a portion, be rich in nutraceutical additional aqueous substance feed 44 to provide, describedly be rich in nutraceutical additional aqueous substance feed 44 and directly be supplied to reaction zone 10 or mix mutually with reaction zone feeding material 22 in the shower nozzle 40.In some embodiments, for example, directly or indirectly supply the described nutraceutical additional aqueous substance feed that is rich in by pump.
In some embodiments, for example, the carbonic acid gas that described gaseous emissions production process 20 discharging carbonic acid gas and at least a portion are discharged be provided to reaction zone 10, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed in, regulate at least a input thing of importing to reaction zone 10 according to the described reaction zone that is provided to reaction zone 10 with the molar rate of discharging carbonic acid gas feed at least.In some embodiments in these embodiments, when described at least a input thing is regulated, will place the described phototroph matter in the reaction zone 10 to be exposed under photosynthetic effective optical radiation.
Propose as mentioned like that, the adjusting that the input thing is done is beginning, stop, increase, reduce or otherwise change any in the described input thing.The described input thing of input reaction zone 10 is such input things: it is supplied in the reaction zone 10 is essential for the growth velocity of the phototroph matter in the reaction zone 10.The exemplary input thing of input reaction zone 10 comprises: photosynthetic effective optical radiation of characteristic strength is supplied to described reaction zone, and extra-nutrition thing feed 42 is supplied to described reaction zone 10.
Thus, the adjusting that the intensity of photosynthetic effective optical radiation of being supplied to reaction zone 10 is done is any in following: start photosynthetic effective optical radiation to the supply of described reaction zone, stop photosynthetic effective optical radiation to the supply of described reaction zone, have additional supply of to the intensity of photosynthetic effective optical radiation of described reaction zone and the intensity that reduces the photosynthetic effective optical radiation that is supplied to described reaction zone 10.In some embodiments, for example, the intensity of regulating the photosynthetic effective optical radiation be supplied to described reaction zone comprises: regulate the intensity that at least a portion is rich in photosynthetic effective optical radiation that the phototroph matter of carbonic acid gas stands.
The adjusting that the molar rate of the extra-nutrition thing feed 42 that is supplied to reaction zone is done is any in following: start extra-nutrition thing feed 42 to the supply of reaction zone, stop being supplied to the extra-nutrition thing feed 42 of reaction zone supply, have additional supply of to the supply molar rate of the extra-nutrition thing feed 42 of described reaction zone or reduce the supply molar rate of the extra-nutrition thing feed 42 that is supplied to described reaction zone.
In some embodiments, for example, described adjusting is at least based on the molar rate index of the reaction zone that is provided to reaction zone 10 with discharging carbonic acid gas feed.Thus, in some embodiments, for example, the carbonic acid gas that gaseous emissions production process 20 discharging carbonic acid gas and at least a portion are discharged be provided to reaction zone 10, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed in, regulate the input thing of at least a input reaction zone 10 at least with the molar rate index of discharging the carbonic acid gas feed according to the described reaction zone that is provided to reaction zone 10.In some embodiments in these embodiments, when at least a input thing is regulated, will place the phototroph matter in the reaction zone 10 to be exposed under photosynthetic effective optical radiation.
In some embodiments, for example, the reaction zone that is supplied to reaction zone 10 is molar rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings with the molar rate index of discharging carbonic acid gas feed, thereby described adjusting is at least based on the molar rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and wherein said gaseous emissions comprises that described reaction zone is with discharging carbonic acid gas feed.Thus, in some embodiments, for example, flow sensor 78 is provided, with for detection of the molar flow rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the signal that will represent the actual measurement molar flow rate of the gaseous emissions 18 that described gaseous emissions production process 20 discharges is transferred to controller.When described controller received signal from the actual measurement molar flow rate of the described gaseous emissions 18 of the representative of flow sensor 78, the actual measurement molar flow rate of the gaseous emissions 18 that described controller discharges according to gaseous emissions production process 20 was regulated at least a input thing of input reaction zone 10.In some embodiments, for example, the adjusting that at least a input thing is done comprise following one of at least: (i) start photosynthetic effective optical radiation to the supply of described reaction zone 10; Or (ii) increase the intensity of the photosynthetic effective optical radiation be provided to reaction zone 10.In some embodiments, for example, the adjusting that at least a input thing is done comprises: (i) start extra-nutrition thing feed 42 to the supply of described reaction zone; Or (ii) have additional supply of to the supply molar rate of the extra-nutrition thing feed 42 of described reaction zone 10.In some embodiments, the adjusting that at least a input thing is done comprise following one of at least: (i) stop being supplied to the supply of photosynthetic effective optical radiation of described reaction zone 10; Or (ii) reduce the intensity of the photosynthetic effective optical radiation be provided to reaction zone 10.In some embodiments, for example, the adjusting that at least a input thing is done comprise following one of at least: (i) stop being supplied to the supply of the extra-nutrition thing feed 42 of described reaction zone; Or (ii) reduce the supply molar rate of the extra-nutrition thing feed 42 be supplied to described reaction zone 10.
In some embodiments, for example, the reaction zone that is supplied to reaction zone 10 is carbonic acid gas volumetric molar concentration by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings with the molar rate index of discharging carbonic acid gas feed, thereby described adjusting is at least based on the carbonic acid gas volumetric molar concentration by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and wherein said gaseous emissions 18 comprises that described reaction zone is with discharging carbonic acid gas feed.Thus, in some embodiments, for example, carbon dioxide sensor 781 is provided, with for detection of by the carbonic acid gas volumetric molar concentration in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the signal that will represent the carbonic acid gas volumetric molar concentration of the gaseous emissions 18 that described gaseous emissions production process 20 discharges is transferred to controller.When described controller received from the representative of carbon dioxide sensor 781 in the described gaseous emissions 18 signal of the actual measurement volumetric molar concentration of carbonic acid gas, described controller was regulated at least a input thing of input reaction zone 10 according to the actual measurement volumetric molar concentration of carbonic acid gas in the described gaseous emissions 18.In some embodiments, for example, the adjusting that at least a input thing is done comprise following one of at least: (i) start photosynthetic effective optical radiation to the supply of described reaction zone 10; Or (ii) increase the intensity of the photosynthetic effective optical radiation be provided to reaction zone 10.In some embodiments, for example, the adjusting that at least a input thing is done comprises: (i) start extra-nutrition thing feed 42 to the supply of described reaction zone; Or (ii) have additional supply of to the supply molar rate of the extra-nutrition thing feed 42 of described reaction zone 10.In some embodiments, the adjusting that at least a input thing is done comprise following one of at least: (i) stop being supplied to the supply of photosynthetic effective optical radiation of described reaction zone 10; Or (ii) reduce the intensity of the photosynthetic effective optical radiation be provided to reaction zone 10.In some embodiments, for example, the adjusting that at least a input thing is done comprise following one of at least: (i) stop being supplied to the supply of the extra-nutrition thing feed 42 of described reaction zone; Or (ii) reduce the supply molar rate of the extra-nutrition thing feed 42 be supplied to described reaction zone 10.
In some embodiments, for example, the reaction zone that is supplied to reaction zone 10 is molar rate by the carbonic acid gas of described gaseous emissions production process 20 dischargings with the molar rate index of discharging carbonic acid gas feed, thereby described adjusting is at least based on the molar rate by the carbonic acid gas of described gaseous emissions production process 20 dischargings, and wherein said gaseous emissions 18 comprises that described reaction zone is with discharging carbonic acid gas feed.In some embodiments, for example, based on by the actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings and by the combination of the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, calculate the molar rate by the carbonic acid gas of described gaseous emissions production process 20 dischargings.Described (i) by the actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings and (ii) by the combination of the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the basis of the molar rate of calculating the carbonic acid gas that described gaseous emissions production process 20 discharges is provided.Thus, flow sensor 78 is provided, with for detection of the molar flow rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the signal that will represent the actual measurement molar flow rate of the gaseous emissions 18 that is discharged by described gaseous emissions production process 20 is transferred to controller.Thus, carbon dioxide sensor 781 also is provided, with the carbonic acid gas volumetric molar concentration for detection of the gaseous emissions 18 that is discharged by described gaseous emissions production process 20, and the signal that will represent by the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings is transferred to controller.Receive representative by the sensing flux signal of the actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings at described controller from flow sensor 78, also receive representative by the carbonic acid gas sensing signal of the actual measurement volumetric molar concentration of carbonic acid gas the gaseous emissions 18 of described gaseous emissions production process 20 dischargings from carbon dioxide sensor 781, and calculate the molar rate of the carbonic acid gas that is discharged by gaseous emissions production process 20 according to the sensing flux signal that receives and the carbonic acid gas sensing signal that receives after, described controller is regulated at least a input thing of importing reaction zone 10 according to the molar rate calculated value of the carbonic acid gas that gaseous emissions production process 20 discharges, and wherein the molar flow rate of the gaseous emissions 18 that the actual measurement volumetric molar concentration of carbonic acid gas and described process 20 are discharged in the gaseous emissions 18 (described sensing flux signal is based on it) is to be detected simultaneously or in fact simultaneously.In some embodiments, for example, the adjusting that at least a input thing is done comprise following one of at least: (i) start photosynthetic effective optical radiation to the supply of described reaction zone 10; Or (ii) increase the intensity of the photosynthetic effective optical radiation be provided to reaction zone 10.In some embodiments, for example, the adjusting that at least a input thing is done comprises: (i) start extra-nutrition thing feed 42 to the supply of described reaction zone; Or (ii) have additional supply of to the supply molar rate of the extra-nutrition thing feed 42 of described reaction zone 10.In some embodiments, the adjusting that at least a input thing is done comprise following one of at least: (i) stop being supplied to the supply of photosynthetic effective optical radiation of described reaction zone 10; Or (ii) reduce the intensity of the photosynthetic effective optical radiation be provided to reaction zone 10.In some embodiments, for example, the adjusting that at least a input thing is done comprise following one of at least: (i) stop being supplied to the supply of the extra-nutrition thing feed 42 of described reaction zone; Or (ii) reduce the supply molar rate of the extra-nutrition thing feed 42 be supplied to described reaction zone 10.
In one aspect of the method, the carbonic acid gas that gaseous emissions production process 20 discharging carbonic acid gas and at least a portion are discharged be provided to reaction zone 10, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed in, when detecting the described reaction zone that is provided to reaction zone 10 molar rate with discharging carbonic acid gas feed and change, regulate at least a input thing of input reaction zone 10.Thus, described at least a input thing to input reaction zone 10 is regulated to be in response to and is detected the reaction zone that is provided to reaction zone 10 and change with the supply molar rate of discharging the carbonic acid gas feed and implement.In some embodiments in these embodiments, for example, when at least a input thing is regulated, will place the described phototroph matter in the reaction zone 10 to be exposed under photosynthetic effective optical radiation.
In one aspect of the method, the carbonic acid gas that gaseous emissions production process 20 discharging carbonic acid gas and at least a portion are discharged be provided to reaction zone 10, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed in, when detecting the vicissitudinous indication of molar rate of the reaction zone usefulness discharging carbonic acid gas feed that is provided to reaction zone 10, regulate at least a input thing of input reaction zone 10.Thus, described at least a input thing to input reaction zone 10 is regulated to be in response to and is detected the reaction zone that is provided to reaction zone 10 and implement with the vicissitudinous indication of supply molar rate of discharging the carbonic acid gas feed.In some embodiments in these embodiments, for example, when at least a input thing is regulated, will place the described phototroph matter in the reaction zone 10 to be exposed under photosynthetic effective optical radiation.
As mentioned above, the adjusting done is to begin, stop, increase or reduce any in the described input thing to the input thing.The exemplary input thing of input reaction zone 10 comprises that the photosynthetic effective optical radiation with characteristic strength is supplied to described reaction zone 10, and the extra-nutrition thing feed 42 of certain molar rate is supplied to described reaction zone 10.
Similarly, as described above, the adjusting that the intensity of photosynthetic effective optical radiation of being supplied to reaction zone 10 is done is any in following: start photosynthetic effective optical radiation to the supply of described reaction zone, stop photosynthetic effective optical radiation to the supply of described reaction zone, have additional supply of to the intensity of photosynthetic effective optical radiation of described reaction zone and the intensity that reduces the photosynthetic effective optical radiation that is supplied to described reaction zone 10.In some embodiments, for example, the intensity of regulating the photosynthetic effective optical radiation be supplied to described reaction zone comprises: regulate the intensity that at least a portion is rich in photosynthetic effective optical radiation that the phototroph matter of carbonic acid gas stands.
In addition, as mentioned above, the adjusting that the molar rate of the extra-nutrition thing feed 42 that is supplied to reaction zone is done is any in following: start extra-nutrition thing feed 42 to the supply of reaction zone, stop being supplied to the extra-nutrition thing feed 42 of reaction zone supply, have additional supply of to the supply molar rate of the extra-nutrition thing feed 42 of described reaction zone or reduce the supply molar rate of the extra-nutrition thing feed 42 that is supplied to described reaction zone.
In some embodiments, for example, and also as indicated above, the intensity of regulating described photosynthetic effective optical radiation by controller.In some embodiments, for example, the controller change exports the power of light source to strengthen or to weaken the light intensity of described light source from power supply, and this can realize by any one in control voltage or the electric current.In addition, in some embodiments, for example, also regulate the supply molar rate of described extra-nutrition thing feed 42 by controller.In order to regulate the supply molar rate of described extra-nutrition thing feed 42, described controller can be controlled volume pump 421 so that the extra-nutrition thing feed 42 of predetermined molar flow rate to be provided.
In some embodiments, for example, at gaseous emissions production process 20 discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone 10, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed, when detecting the reaction zone that is provided to reaction zone 10 molar rate with discharging carbonic acid gas feed and increase, the adjusting that at least a input thing is done comprise following one of at least: (i) start photosynthetic effective optical radiation to the supply of described reaction zone 10; Or (ii) increase the intensity of the photosynthetic effective optical radiation be provided to reaction zone 10.Thus, described adjusting is in response to and detects the reaction zone that is provided to reaction zone 10 and implement with the increase of the supply molar rate of discharging carbonic acid gas feed.In some embodiments, for example, the increase of intensity of described photosynthetic effective optical radiation that is provided to reaction zone 10 is proportional with the increase of the supply molar rate of discharging carbonic acid gas feed with the described reaction zone that is provided to reaction zone 10.
In some embodiments, for example, at gaseous emissions production process 20 discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone 10, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed, when detecting the reaction zone that is provided to reaction zone 10 molar rate with discharging carbonic acid gas feed the indication of increase arranged, the adjusting that at least a input thing is done comprise following one of at least: (i) start photosynthetic effective optical radiation to the supply of described reaction zone 10; Or (ii) increase the intensity of the photosynthetic effective optical radiation be provided to reaction zone 10.Thus, described adjusting is in response to and detects the reaction zone that is provided to reaction zone 10 and have the indication of increase to implement with the molar rate of discharging carbonic acid gas feed.In some embodiments, for example, the increase of intensity of described photosynthetic effective optical radiation that is provided to reaction zone 10 is proportional with the increase of discharging carbonic acid gas feed molar rate with the described reaction zone that is provided to reaction zone 10.
In some embodiments, for example, when startup is provided to the supply of photosynthetic effective optical radiation of described reaction zone or when having additional supply of intensity to photosynthetic effective optical radiation of described reaction zone, improves and place in the reaction zone 10 and the rate of cooling of supplying the light source of described photosynthetic effective optical radiation to reaction zone.Described light source is supplied photosynthetic effective optical radiation to reaction zone when, cool off to alleviate any heat energy of being produced by described light source to the heat effect of reaction zone.Can improve the temperature of described reaction zone to the heat effect of described reaction zone 10.To damage described phototroph matter when in some embodiments, temperature is too high in the reaction zone 10.In some embodiments, for example, described light source is placed in the liquid light guide, and conductive fluid is placed in the described liquid light guide, improves rate of cooling by the exchange rate that increases described conductive fluid in the liquid light guide.
In some embodiments, for example, the carbonic acid gas that gaseous emissions production process 20 discharging carbonic acid gas and at least a portion are discharged be provided to reaction zone 10, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed in, when detecting the reaction zone that is provided to reaction zone 10 molar rate with discharging carbonic acid gas feed and increase, the adjusting that at least a input thing is done comprise following one of at least: (i) start extra-nutrition thing feed 42 to the supply of reaction zone 10; Or (ii) increase the molar rate of the described extra-nutrition thing feed 42 be provided to reaction zone 10.Thus, described adjusting is in response to and detects the reaction zone that is provided to reaction zone 10 and implement with the increase of the supply molar rate of discharging carbonic acid gas feed.
In some embodiments, for example, at gaseous emissions production process 20 discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone 10, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed, when detecting the reaction zone that the is provided to reaction zone 10 supply molar rate with discharging carbonic acid gas feed the indication of increase arranged, the adjusting that at least a input thing is done comprise following one of at least: (i) start extra-nutrition thing feed 42 to the supply of reaction zone 10; Or (ii) increase the supply molar rate of the described extra-nutrition thing feed 42 be provided to reaction zone 10.Thus, described adjusting is in response to and detects the reaction zone that is provided to reaction zone 10 and have the indication of increase to implement with the supply molar rate of discharging carbonic acid gas feed.
In some embodiments, for example, detecting the reaction zone that is provided to reaction zone 10 has the indication of increase to be with the supply molar rate of discharging carbonic acid gas feed: the molar rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings increases, and wherein said gaseous emissions 18 comprises that described reaction zone is with discharging carbonic acid gas feed.Thus, in some embodiments, for example, provide flow sensor 78, with for detection of the molar flow rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the signal that will represent the actual measurement molar flow rate of described gaseous emissions 18 is transferred to controller.The reception signal of the actual measurement molar flow rate of the gaseous emissions 18 that will discharge from the described gaseous emissions production process 20 of the representative of flow sensor 78 at described controller, compare with the signal of the molar flow rate of the previous gaseous emissions 18 that is discharged by described gaseous emissions production process 20 that detects of the representative that had before received, and confirm after the molar flow rate increase of the gaseous emissions 18 that described gaseous emissions production process 20 discharges, described controller carry out following one of at least: (a) start photosynthetic effective optical radiation to the supply of described reaction zone 10, or increase the intensity of the photosynthetic effective optical radiation that is provided to reaction zone 10; And (b) startup extra-nutrition thing feed 42 supplies to described reaction zone 10, or have additional supply of to the supply molar rate of the extra-nutrition thing feed 42 of described reaction zone 10.
In some embodiments, for example, detecting the reaction zone that is provided to reaction zone 10 has the indication of increase to be with the supply molar rate of discharging the carbonic acid gas feed: the volumetric molar concentration by carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings increases, and wherein said gaseous emissions 18 comprises that described reaction zone is with discharging the carbonic acid gas feed.Thus, in some embodiments, for example, carbon dioxide sensor 781 is provided, with the volumetric molar concentration for detection of carbonic acid gas in the gaseous emissions 18 that is discharged by described gaseous emissions production process 20, and the signal that will represent by the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings is transferred to controller.The reception signal of the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 that described controller will be discharged by described gaseous emissions production process 20 from the representative of carbon dioxide sensor 781, compare with the signal of carbonic acid gas volumetric molar concentration in the previous gaseous emissions 18 that is discharged by described gaseous emissions production process 20 that detects of the representative that had before received, and after confirming that carbonic acid gas volumetric molar concentration in the described gaseous emissions 18 increases, described controller carry out following one of at least: (a) start photosynthetic effective optical radiation to the supply of described reaction zone 10, or increase the intensity of the photosynthetic effective optical radiation that is provided to reaction zone 10; And (b) startup extra-nutrition thing feed 42 supplies to described reaction zone 10, or have additional supply of to the supply molar rate of the extra-nutrition thing feed 42 of described reaction zone 10.
In some embodiments, for example, the described reaction zone that is supplied to reaction zone 10 has the indication of increase to be with the supply molar rate of discharging carbonic acid gas feed: the molar rate by the carbonic acid gas of described gaseous emissions production process 20 dischargings increases.Thus, in some embodiments, for example, be based on following (i) and (ii) contrast by the molar rate increase of the carbonic acid gas of described gaseous emissions production process 20 dischargings: (i) by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings, the combination of the actual measurement volumetric molar concentration of carbonic acid gas in the actual measurement molar flow rate of the gaseous emissions 18 that wherein said calculating is discharged based on described gaseous emissions production process 20, the gaseous emissions 18 that discharges with described gaseous emissions production process 20; And (ii) before by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings, wherein said calculating based on before by the previous actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, with before by the combination of the previous actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings.Thus, flow sensor 78 is provided, with for detection of the molar flow rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the signal that will represent the actual measurement molar flow rate of the gaseous emissions 18 that is discharged by described gaseous emissions production process 20 is transferred to controller.Thus, carbon dioxide sensor 781 also is provided, with the volumetric molar concentration for detection of carbonic acid gas in the gaseous emissions 18 that is discharged by described gaseous emissions production process 20, and the signal that will represent by the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings is transferred to controller.Receive representative by the sensing flux signal of the actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings at described controller from flow sensor 78, also receive representative by the carbonic acid gas sensing signal (wherein the actual measurement molar flow rate of the gaseous emissions 18 that the actual measurement volumetric molar concentration of carbonic acid gas and described process 20 are discharged in the gaseous emissions 18 (described sensing flux signal is based on it) is to be detected simultaneously or in fact simultaneously) of the actual measurement volumetric molar concentration of carbonic acid gas the gaseous emissions 18 of described gaseous emissions production process 20 dischargings from carbon dioxide sensor 781, and calculate the molar rate of the carbonic acid gas that is discharged by gaseous emissions production process 20 according to the sensing flux signal that receives and the carbonic acid gas sensing signal that receives, and will by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings with before compared by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings, and after the molar rate increase of affirmation by the carbonic acid gas of described gaseous emissions production process 20 dischargings, described controller carry out following one of at least: (a) start photosynthetic effective optical radiation to the supply of described reaction zone 10, or increase the intensity of the photosynthetic effective optical radiation that is provided to reaction zone 10; And (b) startup extra-nutrition thing feed 42 supplies to described reaction zone 10, or have additional supply of to the supply molar rate of the extra-nutrition thing feed 42 of described reaction zone 10, wherein, before by the molar rate calculated value of the carbonic acid gas of gaseous emissions production process 20 dischargings based on the representative of previous reception before by the sensing flux signal of the previous actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the previous representative that receives is before by the combination of the carbonic acid gas sensing signal of the previous actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the previous actual measurement molar flow rate of the previous actual measurement volumetric molar concentration of wherein said carbonic acid gas and the gaseous emissions 18 of described previous discharging (the sensing flux signal of described previous reception is based on it) is the while or is detected in fact simultaneously.
In some embodiments, for example, (a) by the increase of the actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings; (b) by the increase of the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings; Or (c) by the increase of the supply molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings, any one among this three is the index that the reaction zone that is supplied to reaction zone 10 increases with the supply molar rate of discharging carbonic acid gas feed.When the described reaction zone that is supplied to reaction zone 10 increases with the supply molar rate of discharging the carbonic acid gas feed, the supply molar rate of at least a growth conditions of phototroph matter increases (namely, the carbonic acid gas supply molar rate that improves), correspondingly start or increase other the input things relevant with this type of growth delivery rate so that the phototroph matter in the reaction zone 10 by expectedly growing.
In some embodiments, for example, at gaseous emissions production process 20 discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone 10, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed, when detecting the reaction zone that the is supplied to reaction zone 10 supply molar rate with discharging carbonic acid gas feed and reduce, the adjusting that at least a input thing is done comprise following one of at least: (i) stop being supplied to the supply of photosynthetic effective optical radiation of described reaction zone 10; Or (ii) reduce the intensity of the photosynthetic effective optical radiation be provided to reaction zone 10.Thus, described adjusting is in response to and detects the reaction zone that is provided to reaction zone 10 and implement with the reduction of the supply molar rate of discharging carbonic acid gas feed.In some embodiments, for example, be provided to the reduction and the be lowered into ratio of the described reaction zone that is provided to reaction zone 10 with the supply molar rate of discharging the carbonic acid gas feed of intensity of described photosynthetic effective optical radiation of reaction zone.
In some embodiments, for example, at gaseous emissions production process 20 discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone 10, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed, when detecting the reaction zone that is provided to reaction zone 10 molar rate with discharging carbonic acid gas feed the indication of reduction arranged, the adjusting that at least a input thing is done comprise following one of at least: (i) stop being supplied to the supply of photosynthetic effective optical radiation of described reaction zone 10; Or (ii) reduce the intensity of the photosynthetic effective optical radiation be provided to reaction zone 10.Thus, described adjusting is in response to and detects the reaction zone that is provided to reaction zone 10 and have the indication of reduction to implement with the supply molar rate of discharging carbonic acid gas feed.In some embodiments, for example, be provided to the reduction and the be lowered into ratio of the described reaction zone that is provided to reaction zone 10 with the supply molar rate of discharging the carbonic acid gas feed of intensity of described photosynthetic effective optical radiation of reaction zone.
In some embodiments, for example, at gaseous emissions production process 20 discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone 10, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed, when detecting the reaction zone that the is provided to reaction zone 10 supply molar rate with discharging carbonic acid gas feed and reduce, the adjusting that at least a input thing is done comprise following one of at least: (i) stop being supplied to the supply of the extra-nutrition thing feed 42 of described reaction zone; Or (ii) reduce the supply molar rate of the extra-nutrition thing feed 42 be supplied to described reaction zone 10.Thus, described adjusting is in response to and detects the reaction zone that is provided to reaction zone 10 and reduce with the supply molar rate of discharging carbonic acid gas feed and implement.
In some embodiments, for example, at gaseous emissions production process 20 discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone 10, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed, when detecting the reaction zone that the is provided to reaction zone 10 supply molar rate with discharging carbonic acid gas feed the indication of reduction arranged, the adjusting that at least a input thing is done comprise following one of at least: (i) stop being supplied to the supply of the extra-nutrition thing feed 42 of described reaction zone; Or (ii) reduce the supply molar rate of the extra-nutrition thing feed 42 be supplied to described reaction zone 10.Thus, described adjusting is in response to and detects the reaction zone that is provided to reaction zone 10 and have the indication of reduction to implement with the supply molar rate of discharging carbonic acid gas feed.
In some embodiments, for example, detecting the reaction zone that is supplied to reaction zone 10 has the indication of reduction to be with the supply molar rate of discharging carbonic acid gas feed: the molar rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings reduces.Thus, in some embodiments, for example, provide flow sensor 78, with for detection of the molar flow rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the signal that will represent the actual measurement molar flow rate of described gaseous emissions 18 is transferred to controller.Will be from the representative of the flow sensor 78 reception signal by the actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings at described controller, before compared by the signal of the previous actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings with the representative of previous reception, and after the molar flow rate reduction of affirmation by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, described controller carry out following one of at least: (a) reduce the intensity of the photosynthetic effective optical radiation that is supplied to reaction zone 10, or stop its supply; And the supply molar rate that (b) reduces the extra-nutrition thing feed 42 that is supplied to reaction zone 10, or stop its supply.
In some embodiments, for example, detecting the reaction zone that is supplied to reaction zone 10 has the indication of reduction to be with the supply molar rate of discharging carbonic acid gas feed: the carbonic acid gas volumetric molar concentration by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings reduces.Thus, in some embodiments, for example, carbon dioxide sensor 781 is provided, with the volumetric molar concentration for detection of carbonic acid gas in the gaseous emissions 18 that is discharged by described gaseous emissions production process 20, and the signal that will represent by the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings is transferred to controller.The reception signal of the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 that described controller will be discharged by described gaseous emissions production process 20 from the representative of carbon dioxide sensor 781, before compared by the signal of the previous actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings with the representative of previous reception, and confirm after the volumetric molar concentration reduction of carbonic acid gas in the described gaseous emissions 18, described controller carry out following one of at least: (a) reduce the intensity of the photosynthetic effective optical radiation that is supplied to reaction zone 10, or stop its supply; And the supply molar rate that (b) reduces the extra-nutrition thing feed 42 that is supplied to reaction zone 10, or stop its supply.
In some embodiments, for example, the reaction zone that is supplied to reaction zone 10 has the indication of reduction to be with the supply molar rate of discharging carbonic acid gas feed: the molar rate by the carbonic acid gas of described gaseous emissions production process 20 dischargings reduces.Thus, in some embodiments, for example, reduced by the molar rate of the carbonic acid gas of described gaseous emissions production process 20 dischargings and to be based on following (i) and (ii) contrast: (i) by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings, the combination of the actual measurement volumetric molar concentration of carbonic acid gas in the actual measurement molar flow rate of the gaseous emissions 18 that wherein said calculating is discharged based on described gaseous emissions production process 20, the gaseous emissions 18 that discharges with described gaseous emissions production process 20; And (ii) before by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings, wherein said calculating based on before by the previous actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, with before by the combination of the previous actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings.Thus, flow sensor 78 is provided, with for detection of the molar flow rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the signal that will represent the actual measurement molar flow rate of the gaseous emissions 18 that is discharged by described gaseous emissions production process 20 is transferred to controller.Thus, carbon dioxide sensor 781 also is provided, with the volumetric molar concentration for detection of carbonic acid gas in the gaseous emissions 18 that is discharged by described gaseous emissions production process 20, and the signal that will represent by the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings is transferred to controller.Receive representative by the sensing flux signal of the actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings at described controller from flow sensor 78, also receive representative by the carbonic acid gas sensing signal (wherein the actual measurement molar flow rate of the gaseous emissions 18 that the actual measurement volumetric molar concentration of carbonic acid gas and described process 20 are discharged in the gaseous emissions 18 (described sensing flux signal is based on it) is to be detected simultaneously or in fact simultaneously) of the actual measurement volumetric molar concentration of carbonic acid gas the gaseous emissions 18 of described gaseous emissions production process 20 dischargings from carbon dioxide sensor 781, and calculate the molar rate of the carbonic acid gas that is discharged by gaseous emissions production process 20 according to the sensing flux signal that receives and the carbonic acid gas sensing signal that receives, and will by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings with before compared by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings, and after the molar rate reduction of affirmation by the carbonic acid gas of described gaseous emissions production process 20 dischargings, described controller carry out following one of at least: (a) reduce the intensity of the photosynthetic effective optical radiation that is supplied to reaction zone 10, or stop its supply; And the supply molar rate that (b) reduces the extra-nutrition thing feed 42 that is supplied to reaction zone 10, or stop its supply, wherein, before by the molar rate calculated value of the carbonic acid gas of gaseous emissions production process 20 dischargings based on the representative of previous reception before by the sensing flux signal of the previous actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the previous representative that receives is before by the combination of the carbonic acid gas sensing signal of the previous actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, the previous actual measurement volumetric molar concentration of wherein said carbonic acid gas with before were whiles or were detected in fact simultaneously by the previous actual measurement molar flow rate (the sensing flux signal of described previous reception is based on it) of the gaseous emissions 18 of described process 20 dischargings.
In some embodiments, for example, (a) molar flow rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings reduces; (b) the carbonic acid gas volumetric molar concentration by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings reduces; Or (c) reduced by the molar rate of the carbonic acid gas of described gaseous emissions production process 20 dischargings, any one among this three is the index that the reaction zone that is supplied to reaction zone 10 reduces with the supply molar rate of discharging carbonic acid gas feed.Because the reaction zone that is supplied to reaction zone 10 reduces with the supply molar rate of discharging carbonic acid gas feed, thus correspondingly reduction or termination relevant with the growth of phototroph matter one or more other import the delivery rate of thing to save described input thing.
In one aspect of the method, at gaseous emissions production process 20 discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone 10, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed, when the supply molar rate that detects the reaction zone usefulness discharging carbonic acid gas feed that is provided to reaction zone 10 reduces, perhaps when detecting the reaction zone that the is provided to reaction zone 10 supply molar rate with discharging carbonic acid gas feed the indication of reduction arranged, have additional supply of to the supply molar rate of the additional carbonic acid gas feed 92 of reaction zone 10, or start additional carbonic acid gas feed 92 to the supply of reaction zone 10.Thus, have additional supply of to the supply molar rate of the additional carbonic acid gas feed 92 of described reaction zone 10 or start and replenish carbonic acid gas feed 92 and be in response to the supply of described reaction zone 10 and detect the reaction zone that is provided to reaction zone 10 with the supply molar rate reduction of discharging carbonic acid gas feed or have the indication of reduction to implement.In some embodiments, for example, the source of described additional carbonic acid gas feed 92 is dioxide bottles.In some embodiments, for example, the source of described additional carbonic acid gas feed 92 is air supplies.In some embodiments, for example, detected reduction is: detect the described reaction zone that is supplied to reaction zone 10 and stop with the supply molar rate of discharging the carbonic acid gas feed.In some embodiments, for example, the indication of detected reduction is: detect the indication that termination is arranged with the supply molar rate of discharging carbonic acid gas feed to the described reaction zone of reaction zone 10.In some embodiments, for example, it is above-mentioned any indication that the described reaction zone that is supplied to reaction zone 10 has the indication of reduction with the supply molar rate of discharging carbonic acid gas feed.
In some embodiments in these embodiments, having additional supply of to the supply molar rate of the additional carbonic acid gas feed 92 of reaction zone 10 or when starting its supply, will place the described phototroph matter in the reaction zone 10 to be exposed under photosynthetic effective optical radiation.
In some embodiments, for example, keep the constant growth velocity of essence in order to make phototroph matter, provide described additional carbonic acid gas feed 92 to be supplied to the reduction of supply molar rate of the carbonic acid gas of reaction zone 10 with compensation by gaseous emissions production process 20, if to be considered to only be temporary words (for example being less than for two weeks) in described reduction (for example stopping).Thus, in some embodiments, the time that feed 92 continues after the supply self-starting of reaction zone 10 was shorter than for two (2) weeks, for example be shorter than a week, as further example, be shorter than five (5) days, as further example, be shorter than three (3) days, as further example, be shorter than one (1) day.In some embodiments, for example, the time that feed 92 continues after the supply self-starting of reaction zone 10 was greater than 15 minutes, for example greater than 30 minutes, as further example, greater than one (1) hour, as further example, greater than six (6) hours, as further example, greater than 24 hours.
In following these embodiments, increase and replenish carbonic acid gas feed 92 to the supply molar rate of reaction zone 10, or start its supply and be in response to and detect the described reaction zone that is provided to reaction zone 10 and have the indication of reduction to implement with the supply molar rate of discharging carbonic acid gas feed, and it is that molar flow rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings reduces that the detected described reaction zone that is provided to reaction zone 10 has the indication of reduction with the supply molar rate of discharging carbonic acid gas feed, in some embodiments in these embodiments, for example, flow sensor 78 is provided, with for detection of the molar flow rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the signal that will represent the actual measurement molar flow rate of the gaseous emissions 18 that is discharged by described gaseous emissions production process 20 is transferred to controller.Will be from the representative of the flow sensor 78 reception signal by the current actual measurement molar flow rate of the gaseous emissions 18 of gaseous emissions production process 20 dischargings at described controller, before compared by the signal of the previous actual measurement molar flow rate of the gaseous emissions 18 of gaseous emissions production process 20 dischargings with the representative of previous reception, and after the molar flow rate reduction of affirmation by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, described controller drives the opening of flow control element, for example valve 921, replenish carbonic acid gas feed 92 to start by additional carbonic acid gas feed 92 sources to reaction zone 10 supplies, or increase the supply molar rate of the described additional carbonic acid gas feed 92 that is provided to reaction zone 10.
In following these embodiments, increase and replenish carbonic acid gas feed 92 to the supply molar rate of reaction zone 10, or start its supply and be in response to and detect the described reaction zone that is provided to reaction zone 10 and have the indication of reduction to implement with the supply molar rate of discharging carbonic acid gas feed, and it is that volumetric molar concentration by carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings reduces that the detected described reaction zone that is provided to reaction zone 10 has the indication of reduction with the supply molar rate of discharging carbonic acid gas feed, in some embodiments in these embodiments, for example, carbon dioxide sensor 781 is provided, with the volumetric molar concentration for detection of carbonic acid gas in the gaseous emissions 18 that is discharged by described gaseous emissions production process 20, and the signal that will represent by the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings is transferred to controller.The reception signal of the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 that described controller will be discharged by described gaseous emissions production process 20 from the representative of carbon dioxide sensor 781, before compared by the signal of the previous actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings with the representative of previous reception, and after the volumetric molar concentration of carbonic acid gas reduces in the gaseous emissions of confirming to be discharged by described gaseous emissions production process 20 18, described controller drives the opening of flow control element, for example valve 921, replenish carbonic acid gas feed 92 to the supply of reaction zone 10 to start, or increase the supply molar rate of the described additional carbonic acid gas feed 92 that is provided to reaction zone 10.
In following these embodiments, increase and replenish carbonic acid gas feed 92 to the supply molar rate of reaction zone 10, or start to replenish carbonic acid gas feed 92 and be in response to the supply of reaction zone 10 and detect the described reaction zone that is provided to reaction zone 10 and have the indication of reduction to implement with the supply molar rate of discharging the carbonic acid gas feed, be that molar rate by the carbonic acid gas of described gaseous emissions production process 20 dischargings reduces when the detected described reaction zone that is provided to reaction zone 10 has the indication of reduction with the supply molar rate of discharging carbonic acid gas feed, in some embodiments in these embodiments, for example, reduced by the molar rate of the carbonic acid gas of described gaseous emissions production process 20 dischargings and to be based on following (i) and (ii) contrast: (i) by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings, the actual measurement molar flow rate of the gaseous emissions 18 that wherein said calculating is discharged based on described gaseous emissions production process 20, the combination of the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 that discharges with described gaseous emissions production process 20; And (ii) before by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings, wherein said calculating based on before by the previous actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, with before by the combination of the previous actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings.Thus, flow sensor 78 is provided, with for detection of the molar flow rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the signal that will represent the actual measurement molar flow rate of the gaseous emissions 18 that is discharged by described gaseous emissions production process 20 is transferred to controller.Thus, carbon dioxide sensor 781 also is provided, with the volumetric molar concentration for detection of carbonic acid gas in the gaseous emissions 18 that is discharged by described gaseous emissions production process 20, and the signal that will represent by the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings is transferred to controller.Receive representative by the sensing flux signal of the actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings at described controller from flow sensor 78, also receive representative by the carbonic acid gas sensing signal (wherein the actual measurement molar flow rate of the gaseous emissions 18 that the actual measurement volumetric molar concentration of carbonic acid gas and described process 20 are discharged in the gaseous emissions 18 (described sensing flux signal is based on it) is to be detected simultaneously or in fact simultaneously) of the actual measurement volumetric molar concentration of carbonic acid gas the gaseous emissions 18 of described gaseous emissions production process 20 dischargings from carbon dioxide sensor 781, and calculate the molar rate of the carbonic acid gas that is discharged by gaseous emissions production process 20 according to the sensing flux signal that receives and the carbonic acid gas sensing signal that receives, and to by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings with before compared by the molar rate calculated value of the carbonic acid gas of described gaseous emissions production process 20 dischargings, and after the molar rate reduction of affirmation by the carbonic acid gas of described gaseous emissions production process 20 dischargings, described controller drives the opening of flow control element, for example valve 921, replenish carbonic acid gas feed 92 to the supply of described reaction zone 10 to start, or increase is provided to the supply molar rate of the described additional carbonic acid gas feed of reaction zone 10, wherein before by the molar rate calculated value of the carbonic acid gas of gaseous emissions production process 20 dischargings based on the representative of previous reception before by the sensing flux signal of the previous actual measurement molar flow rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, and the previous representative that receives is before by the combination of the carbonic acid gas sensing signal of the previous actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, the previous actual measurement volumetric molar concentration of wherein said carbonic acid gas with before were whiles or were detected in fact simultaneously by the previous actual measurement molar flow rate (the sensing flux signal of described previous reception is based on it) of the gaseous emissions 18 of described process 20 dischargings.
In following these embodiments, detecting the described reaction zone that the is provided to reaction zone 10 supply molar rate reduction (or termination) of discharging carbonic acid gas feed, or when detecting the reaction zone that is provided to reaction zone 10 and with the supply molar rate of discharging carbonic acid gas feed the indication of reduction (or termination) being arranged, in response, increase described additional carbonic acid gas feed 92 to the supply molar rate of reaction zone 10, or start described additional carbonic acid gas feed 92 to the supply of reaction zone 10, in some embodiments in these embodiments, described technology comprises that in addition startup contains the raw material 48 of make-up gas to the supply of reaction zone 10, or increases the described supply molar rate that contains the raw material 48 of make-up gas that is provided to reaction zone 10.
In some embodiments, for example, although in response to the reduction of the reaction zone that is provided to reaction zone 10 with the supply molar rate of discharging carbonic acid gas feed, or the termination of its supply and started additional carbonic acid gas feed 92 to the supply of reaction zone 10, or increased the supply molar rate of the additional carbonic acid gas feed 92 that is provided to reaction zone 10, still start the described raw material 48 of make-up gas that contains to the supply of reaction zone 10, or increase the described supply molar rate that contains the raw material 48 of make-up gas that is provided to reaction zone 10, use the supply molar rate of discharging carbonic acid gas feed to reduce with at least part of compensation owing to be provided to the reaction zone of reaction zone 10, or its supply stops and the reduction of the mole delivery rate of the raw material that is provided to reaction zone 10 (for example raw material of reaction zone feeding material 22) that causes or the termination that raw material (for example raw material of reaction zone feeding material 22) is supplied.
In some embodiments, for example, the mole delivery rate of the raw material (reaction zone feeding material 22) that is supplied to reaction zone 10 is reduced or the supply of raw material (reaction zone feeding material 22) stops being compensated, can make the supply molar rate of the raw material (reaction zone feeding material 22) that is supplied to reaction zone 10 not change in fact.
In some embodiments, mole delivery rate to the raw material (reaction zone feeding material 22) that is supplied to reaction zone 10 reduces, or the supply of raw material (reaction zone feeding material 22) stops being compensated, can alleviate the degree that stirring dies down in the reaction zone 10, otherwise, because being provided to the reaction zone of reaction zone 10 reduces with the supply molar rate of discharging the carbonic acid gas feed, or its supply stops, the reaction zone that can cause being provided to reaction zone 10 uses the supply molar rate of gaseous emissions feed 24 to reduce, or its supply termination, thereby cause the stirring in the reaction zone 10 to die down.
In some embodiments, for example, any reaction zone with gaseous emissions feed 24, the raw material combination of replenishing carbonic acid gas feed 92 and containing make-up gas limit be provided to reaction zone, as the combined operation feedstream of at least a portion of reaction zone feeding material 22, described reaction zone feeding material 22 is provided to reaction zone 10 and the material in the reaction zone is produced agitaion, thereby makes that the volumetric molar concentration difference of any phototroph matter is lower than 20% in the reaction zone 10 at 2.In some embodiments, for example, the agitaion that produces can make the volumetric molar concentration difference of phototroph matter any in the reaction zone 10 be lower than 10% at 2.Thus, the supply raw material 48 that contains make-up gas can reduce to produce between the phototroph matter any 2 in the reaction zone and is higher than required maximum concentration gradient.
Contain in the raw material 48 of make-up gas if there is carbonic acid gas, then the volumetric molar concentration of its carbonic acid gas is lower than the carbonic acid gas volumetric molar concentration of the additional carbonic acid gas feed 92 that is provided to reaction zone 10.In some embodiments, for example, based on the integral molar quantity of make-up gas raw material 48, the carbonic acid gas volumetric molar concentration of described make-up gas raw material 48 is lower than 3 moles of %.In some embodiments, for example, based on the integral molar quantity of make-up gas raw material 48, the carbonic acid gas volumetric molar concentration of described make-up gas raw material 48 is lower than one (1) mole of %.
In some embodiments, for example, the raw material 48 that contains make-up gas is gaseous substances.In some embodiments in these embodiments, for example, the raw material 48 that contains make-up gas comprises the dispersion of gaseous state material in liquid material.In some embodiments in these embodiments, for example, the raw material 48 that contains make-up gas comprises air.In some embodiments in these embodiments, for example, provide the raw material 48 that contains make-up gas with the form of fluid.The raw material 48 that contains make-up gas is provided to reaction zone 10 as the part of reaction zone feeding material 22.
In some embodiments, for example, start the described raw material 48 that contains make-up gas to the supply of reaction zone 10 or increase the described supply molar rate that contains the raw material 48 of make-up gas that is provided to reaction zone 10 and also be in response to and detect the reaction zone that is provided to reaction zone 10 and reduce (or termination) or detect the reaction zone that is provided to reaction zone 10 with the supply molar rate of discharging carbonic acid gas feed and have the indication of reduction (or termination) to implement with the supply molar rate of discharging the carbonic acid gas feed.The example of suitable indication and as indicated above for detection of suitable sensor and the control scheme of this type of indication, and in some embodiments, start the described raw material 48 that contains make-up gas to the supply of reaction zone 10 or increase the described supply molar rate that contains the raw material 48 of make-up gas that is provided to reaction zone 10 be the opening by controller turn-on flow rate controlling elements (as valve 50) or increase as described in opening be communicated with and realize to produce fluid with the source of the raw material 48 that contains make-up gas.
In some embodiments, start the described raw material 48 that contains make-up gas to the supply of reaction zone 10 or increase the described supply molar rate that contains the raw material 48 of make-up gas that is provided to reaction zone 10 and be in response to the supply molar rate that detects the reaction zone feeding material 22 that is provided to reaction zone 10 and reduce or have the indication of reduction to implement, described additional carbonic acid gas feed 92 is provided to reaction zone 10 simultaneously.In some embodiments, for example, provide flow sensor, with the molar flow rate for detection of reaction zone feeding material 22, and the signal that will represent the actual measurement molar flow rate of described reaction zone feeding material 22 is transferred to controller.Will be from the reception signal of the current actual measurement molar flow rate of the described reaction zone feeding of the representative of flow sensor material 22 at described controller, compare with the signal of the previous actual measurement molar flow rate of the described reaction zone feeding of the representative of previous reception material 22, and confirm after the molar flow rate reduction of described reaction zone feeding material 22, described controller drives the opening of flow control element, valve (for example valve 50) for example, starting the supply to reaction zone 10 from the source of the raw material 48 that contains make-up gas of the described raw material 48 that contains make-up gas, or increase from the source of the raw material 48 that contains make-up gas to the described supply molar rate that contains the raw material 48 of make-up gas of reaction zone 10 supplies.
In one aspect of the method, at gaseous emissions production process 20 discharging gaseous emissions 18, wherein any gaseous emissions 18 defined reaction districts that are provided to described reaction zone 10 with gaseous emissions feed 24 in, regulate the reaction zone that is supplied to described reaction zone 10 according to the detection of at least a carbon dioxide treatment figureofmerit with the supply of gaseous emissions feed 24.In some embodiments, for example, described gaseous emissions 18 is that the form with air-flow is discharged.In some embodiments, for example, described reaction zone is that form with air-flow provides with gaseous emissions feed 24.In some embodiments, for example, when the conditioned reaction district is with gaseous emissions feed 24, will place the described phototroph matter in the reaction zone 10 to be exposed under photosynthetic effective optical radiation.
When regulating described reaction zone according at least a carbon dioxide treatment figureofmerit with gaseous emissions feed 24 during to the supply of reaction zone 10, in some embodiments, for example, described technology comprises that further the part branch of the gaseous emissions 18 that adjusting is discharged flows to the supply of another operating unit.The supply that the part branch of the gaseous emissions 18 that discharges flows to another operating unit limits shunting gaseous emissions 60.Described shunting gaseous emissions 60 comprises carbonic acid gas.Described another operating unit transforms shunting gaseous emissions 60, thereby reduces it to the influence of environment.
Propose as mentioned like that, regulate described reaction zone and be beginnings, stop, increase, reduce or otherwise change described reaction zone gaseous emissions feed 24 any in the supply of reaction zone 10 to the supply of reaction zone 10 with gaseous emissions feed 24.Equally, the part shunting (being described shunting gaseous emissions 60) of regulating the gaseous emissions 18 discharge is beginning, stops, increases, reduces or otherwise change described shunting gaseous emissions 60 any in the supply of another operating unit to the supply of another operating unit.
Described carbon dioxide treatment figureofmerit is any feature that represents the capacity of reaction zone 10, and the capacity of wherein said reaction zone 10 is that the capacity that transforms takes place for photosynthetic response that the phototroph matter of carbonic acid gas in placing described reaction zone that described reaction zone will receive carbonic acid gas and at least a portion is received is carried out.
In some embodiments, for example, described carbon dioxide treatment figureofmerit is any technology characteristics that represents the capacity of reaction zone 10, the photosynthetic response that the phototroph matter of carbonic acid gas in placing described reaction zone that wherein said reaction zone 10 is used for receiving carbonic acid gas and at least a portion is received is carried out transforms, thereby makes the described growth of the phototroph matter that described photosynthesis realization response district 10 is interior.Thus, the detection of described carbon dioxide treatment figureofmerit for determining whether need to regulate described reaction zone with the supply of gaseous emissions feed 24 so that the growth of the interior phototroph matter of reaction zone 10 reaches for the predetermined molar rate is vital.
In some embodiments, for example, described carbon dioxide treatment figureofmerit is any technology characteristics that represents the capacity of reaction zone 10, the photosynthetic response that the phototroph matter of carbonic acid gas in placing described reaction zone that wherein said reaction zone 10 is used for receiving carbonic acid gas and at least a portion is received is carried out transforms, thereby makes any carbonic acid gas from reaction zone 10 dischargings be lower than predetermined molar rate.Thus, carbonic acid gas that described reaction zone discharges to the supply of reaction zone 10 so that from reaction zone 10 with gaseous emissions feed 24 reaches for the predetermined molar rate is vital for determining whether need to regulate in the detection of described carbon dioxide treatment figureofmerit.
In some embodiments, for example, the carbon dioxide treatment figureofmerit that detects is the pH in the reaction zone 10.In some embodiments, for example, the carbon dioxide treatment figureofmerit that detects is the volumetric molar concentration of phototroph matter in the reaction zone 10.Because any product 500 that contains phototroph matter by reaction zone 10 dischargings comprises from a part of material in the reaction zone 10 (namely, be material supply in the origin autoreaction district 10 by the product that contains phototroph matter 500 of reaction zone 10 discharging), so the detection of carbon dioxide treatment figureofmerit (for example volumetric molar concentration of the pH in the reaction zone or the phototroph matter in the described reaction zone) comprises the detection of the carbon dioxide treatment figureofmerit in the described product 500 that contains phototroph matter that reaction zone 10 is discharged.
In some embodiments, for example, the adjusting that described reaction zone is done to the supply of reaction zone 10 with gaseous emissions feed 24 is the detection based on interior two kinds or multiple carbon dioxide treatment figureofmerit of reaction zone 10.
In some embodiments, for example, at described gaseous emissions production process 20 discharging gaseous emissions 18, the any gaseous emissions 18 defined reaction districts that wherein are provided to reaction zone 10 are with gaseous emissions feed 24 time, when detecting the carbon dioxide treatment figureofmerit represent reaction zone 10 and will receive the such capacity of carbonic acid gas supply that molar rate increases in reaction zone 10, the adjusting that described reaction zone is done to the supply of reaction zone 10 with gaseous emissions feed 24 comprises: start described reaction zone usefulness gaseous emissions feed 24 to the supply of reaction zone 10, or have additional supply of to the supply molar rate of the described reaction zone usefulness gaseous emissions feed 24 of reaction zone 10.Thus, described adjusting is in response to the carbon dioxide treatment figureofmerits that detect in the reaction zone 10 and represent the such capacity of carbonic acid gas supply that reaction zone 10 will receive the molar rate increase and implement.In following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, and when described shunting gaseous emissions 60 is provided to described another operating unit, in some embodiments in these embodiments, described technology further comprises the supply molar rate that reduces the shunting gaseous emissions 60 that is provided to another operating unit, or stops described supply.Should described understanding, in some embodiments, detect the treatment capacity index and represent the such capacity of carbonic acid gas supply that reaction zone 10 will receive the molar rate increase and when reaction zone is provided to reaction zone 10 with gaseous emissions feed 24, take place.Also should described understanding, in other embodiments, detect the treatment capacity index and represent the such capacity of carbonic acid gas supply that reaction zone 10 will receive the molar rate increase and when reaction zone is provided to reaction zone 10 with gaseous emissions feed 24, do not take place.
In some embodiments, for example, at described gaseous emissions production process 20 discharging gaseous emissions 18, and the described gaseous emissions 18 of at least a portion is provided to reaction zone 10, the described at least a portion gaseous emissions 18 defined reaction districts that wherein are provided to reaction zone 10 are with gaseous emissions feed 24 time, when in reaction zone 10, detecting the carbon dioxide treatment figureofmerit and represent reaction zone 10 and will receive the such capacity of carbonic acid gas supply that molar rate reduces, the adjusting that described reaction zone is done to the supply of reaction zone 10 with gaseous emissions feed 24 comprises: reduce the reaction zone supply molar rate of gaseous emissions feed 24 that is provided to reaction zone 10, or stop described supply.Thus, described adjusting is in response to the carbon dioxide treatment figureofmerits that detect in the reaction zone 10 and represent the such capacity of carbonic acid gas supply that reaction zone 10 will receive the molar rate reduction and implement.In following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, in some embodiments in these embodiments, described technology further comprises the described shunting gaseous emissions 60 of startup to the supply of another operating unit, or increases the supply molar rate of the shunting gaseous emissions 60 that is provided to another operating unit.
In some embodiments, for example, described carbon dioxide treatment figureofmerit is the pH in the reaction zone 10.When the operation pH in reaction zone 10 is higher than the high value (having indicated the supply molar rate deficiency of the carbonic acid gas that is supplied to reaction zone 10) of predetermined pH or is lower than predetermined pH low value (indicated the supply molar rate of the carbonic acid gas that is supplied to reaction zone 10 excessive), to cause the growth of phototroph matter to be lower than required growth velocity, even under extreme case, may cause the death of described phototroph matter.In some embodiments, for example, the pH in the reaction zone 10 that detects detects with pH sensor 46 in reaction zone 10.PH sensor 46 is provided, and with for detection of the pH in the reaction zone, and the signal that will represent the actual measurement pH in the described reaction zone transfers to controller.
In some embodiments, for example, at described gaseous emissions production process 20 discharging gaseous emissions 18, the any gaseous emissions 18 defined reaction districts that wherein are provided to described reaction zone 10 are with gaseous emissions feed 24 time, when in reaction zone 10, detecting the pH that is higher than the high value of predetermined pH, the adjusting that described reaction zone is done to the supply of reaction zone 10 with gaseous emissions feed 24 comprises: start described reaction zone and use gaseous emissions feed 24 to the supply of reaction zone 10, or increase the supply molar rate that the reaction zone that is provided to reaction zone 10 is used gaseous emissions feed 24.In following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, and when described shunting gaseous emissions 60 is provided to described another operating unit, in some embodiments in these embodiments, described technology further comprises the supply molar rate that reduces the shunting gaseous emissions 60 that is provided to another operating unit, or stops described supply.Should described understanding, in some embodiments, detect pH in the reaction zone 10 and be higher than the high value of predetermined pH and when described reaction zone is provided to reaction zone 10 with gaseous emissions feed 24, take place.Also should described understanding, in other embodiments, detect pH in the reaction zone 10 and be higher than the high value of predetermined pH and when reaction zone is provided to reaction zone 10 with gaseous emissions feed 24, do not take place.
In following these embodiments, when the pH in the reaction zone is higher than predetermined pH high value, in some embodiments in these embodiments, to compare from reception signal and the target value (i.e. the high value of the pH that is scheduled to) of the actual measurement pH in the representative reaction zone 10 of pH sensor 47 at controller, and confirm that the actual measurement pH in the described reaction zone 10 is higher than after the high value of described predetermined pH, described controller uses gaseous emissions feed 24 to the supply of reaction zone 10 by starting described reaction zone, or increase the reaction zone be provided to reaction zone 10 and respond with the supply molar rate of gaseous emissions feed 24.In some embodiments, for example, described controller starts described reaction zone by the opening of opening described flow control element 50 and uses gaseous emissions feed 24 to the supply of reaction zone 10.In some embodiments, for example, described controller increases the mole delivery rate that the reaction zone that is provided to reaction zone 10 is used gaseous emissions feed 24 by the opening that makes described flow control element 50.Provide and dispose described flow control element 50, in order to optionally control the molar rate that the reaction zone of supplying to reaction zone 10 is used the supply stream of gaseous emissions feed 24 with the supply stream of gaseous emissions feed 24 (comprise by making and produce the pressure-losses to the reaction zone of reaction zone 10 supplies with the supply stream of gaseous emissions feed 24) by optionally disturbing to the reaction zone of reaction zone 10 supply.Thus, start described reaction zone usefulness gaseous emissions feed 24 to the supply of reaction zone 10 by driving described flow control element 50, or increase its supply molar rate.Described predetermined pH is high, and value is decided on the phototroph of described biomass.In some embodiments, for example, the high value of described predetermined pH can be up to 10.
In following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, and when described shunting gaseous emissions 60 is provided to described another operating unit, in some embodiments in these embodiments, for example, when the pH in controller is confirmed reaction zone 10 was higher than predetermined pH high value, described controller further was provided to the supply molar rate of the shunting gaseous emissions 60 of another operating unit by reduction, or stop described supply and respond.In some embodiments, for example, described controller is by the supply molar rate of the shunting gaseous emissions 60 that makes the opening that places the valve between described gaseous emissions production process 20 and another operating unit reduce to reduce to be provided to another operating unit, and wherein said valve is configured for the fluid that disturbs between gaseous emissions production process 20 and another operating unit and is communicated with.In some embodiments, for example, described controller is by stopping the valve closes that places between described gaseous emissions production process 20 and another operating unit to be provided to the supply of the shunting gaseous emissions 60 of another operating unit, and wherein said valve is configured for the fluid that disturbs between gaseous emissions production process 20 and another operating unit and is communicated with.
Equally, in following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, and when described shunting gaseous emissions 60 is provided to described another operating unit, in other embodiments in these embodiments, for example, when the pressure of the gaseous emissions 18 of described another operating unit upstream is lower than predetermined pressure, reduce the supply molar rate of the shunting gaseous emissions 60 that is provided to another operating unit, or stop described supply, wherein the reduction of pressure is in response to and starts described reaction zone usefulness gaseous emissions feed 24 to the supply of reaction zone 10, or increase the reaction zone be provided to reaction zone 10 and produce with the supply molar rate of gaseous emissions feed 24, wherein any one reactions that to be described controllers make in response to confirming actual measurement pH in the reaction zone to be higher than predetermined pH high value.In this type of embodiment, when the actual measurement pH in described controller is confirmed reaction zone is higher than the high value of described predetermined pH, as mentioned above, described controller starts described reaction zone is provided to the reaction zone usefulness gaseous emissions feed 24 of reaction zone 10 to the supply of reaction zone 10 or increase with gaseous emissions feed 24 supply molar rate.Start described reaction zone with gaseous emissions feed 24 to the supply of reaction zone 10 or increase its supply molar rate and correspondingly cause the pressure of described gaseous emissions 18 to reduce, be lower than predetermined pressure thereby make the pressure of gaseous emissions 18 of described another operating unit upstream become.When the pressure of the gaseous emissions 18 of described another operating unit upstream is lower than predetermined pressure, making for example valve of closing element 64() the biasing power of closing can surpass the hydrodynamicpressure that described closing element 64 is opened, and wherein said closing element 64 places between gaseous emissions production process 20 and another operating unit and is configured for the described gaseous emissions production process 20 of interference and is communicated with fluid between another operating unit.In some embodiments, reduce the opening of described closing element 64, thereby reduce the supply molar rate of the shunting gaseous emissions 60 that is provided to described another operating unit.In other embodiments, close described closing element 64, thereby termination is provided to the supply of the shunting gaseous emissions 60 of another operating unit.
Equally, in following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, and when described shunting gaseous emissions 60 is provided to described another operating unit, in other embodiments in these embodiments, for example, when the pressure of the described gaseous emissions 18 of another operating unit upstream reduces, reduce the supply molar rate of the shunting gaseous emissions 60 that is provided to described another operating unit, the reduction of wherein said gaseous emissions 18 pressure is in response to the described reaction zone of driving and uses gaseous emissions feed 24 to the supply of reaction zone 10, or increase the reaction zone be provided to reaction zone 10 and produce with the supply molar rate of gaseous emissions feed 24, wherein any one reactions that to be described controllers make in response to confirming actual measurement pH in the reaction zone to be higher than predetermined pH high value.The supply molar rate that the pressure of the gaseous emissions 18 of described another operating unit upstream reduces the shunting gaseous emissions 60 that causes being provided to described another operating unit reduces.
In some embodiments, for example, at described gaseous emissions production process 20 discharging gaseous emissions 18, and the described gaseous emissions 18 of at least a portion is provided to reaction zone 10, the described at least a portion gaseous emissions 18 defined reaction districts that wherein are provided to reaction zone 10 are with gaseous emissions feed 24 time, when the actual measurement pH in the reaction zone 10 is lower than predetermined pH low value, the adjusting that described reaction zone is done to the supply of reaction zone 10 with gaseous emissions feed 24 comprises: reduce the reaction zone supply molar rate of gaseous emissions feed 24 that is provided to reaction zone 10, or stop described supply.In following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, in some embodiments in these embodiments, for example, described technology further comprises the described shunting gaseous emissions 60 of startup to the supply of another operating unit, or increases the supply molar rate of the shunting gaseous emissions 60 that is provided to another operating unit.
In following these embodiments, pH in the reaction zone is lower than predetermined pH low value, in some embodiments in these embodiments, for example, will be from the representative of pH sensor 46 after the reception signal of the actual measurement pH in the described reaction zone 10 and target value (i.e. Yu Ding pH low value) compare and confirm that actual measurement pH in the described reaction zone 10 is lower than described predetermined pH low value at described controller, described controller is provided to reaction zone 10 by reduction reaction zone is with the supply molar rate of gaseous emissions feed 24 or stop described supply and respond.In some embodiments, for example, described controller is by making for example valve of described flow control element 50() opening reduce to reduce the reaction zone that is provided to reaction zone 10 with the supply molar rate of gaseous emissions feed 24.In some embodiments, for example, described controller is by making for example valve of described flow control element 50() close and stop described reaction zone with the supply of gaseous emissions feed 24 to reaction zone 10.Described predetermined pH low value is decided on the phototroph of described biomass.In some embodiments, for example, described predetermined pH low value can be low to moderate 4.0.
In following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, in some embodiments in these embodiments, for example, when the pH in controller is confirmed reaction zone 10 was lower than predetermined pH low value, described controller further responded to the supply molar rate that the supply of another operating unit or increase are provided to the shunting gaseous emissions 60 of another operating unit by starting described shunting gaseous emissions 60.In some embodiments, for example, described controller places valve between described gaseous emissions production process 20 and another operating unit to start described shunting gaseous emissions 60 to the supply of another operating unit by driving or increases the supply molar rate of the shunting gaseous emissions 60 that is provided to another operating unit, and wherein said valve is configured for the fluid that disturbs between described process 20 and another operating unit and is communicated with.In some embodiments, for example, described controller places the opening of the valve between described gaseous emissions production process 20 and another operating unit to start described shunting gaseous emissions 60 to the supply of another operating unit by unlatching.In some embodiments, for example, described controller is by the supply molar rate of the shunting gaseous emissions 60 that the opening that places the valve between described gaseous emissions production process 20 and another operating unit increased be provided to another operating unit.
Equally, in following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, in other embodiments in these embodiments, for example, when the pressure of the described gaseous emissions 18 of described another operating unit upstream is higher than predetermined pressure, start described shunting gaseous emissions 60 to the supply of another operating unit, or increase is provided to the supply molar rate of the shunting gaseous emissions 60 of another operating unit, the pressure of the gaseous emissions 18 of wherein said another operating unit upstream increases to and is higher than the supply molar rate reduction that predetermined pressure is in response to the reaction zone usefulness gaseous emissions feed 24 that is provided to reaction zone 10, or described supply stops and produces, wherein any one reactions that to be described controllers make in response to confirming actual measurement pH in the reaction zone to be lower than predetermined pH low value.In this type of embodiment, when the pH that records by pH sensor 46 in described controller is confirmed reaction zone is lower than predetermined pH low value, as mentioned above, described controller makes the reaction zone be provided to reaction zone 10 reduce with the supply molar rate of gaseous emissions feed 24 or makes described supply termination.The reaction zone that is provided to reaction zone 10 reduces with the supply molar rate of gaseous emissions feed 24 or described supply stops causing the pressure of the gaseous emissions 18 of described another operating unit upstream correspondingly to increase, and is higher than predetermined pressure thereby make the pressure of gaseous emissions 18 of described another operating unit upstream become.When the pressure of the gaseous emissions 18 of described another operating unit upstream is higher than predetermined pressure, the hydrodynamicpressure of the gaseous emissions 18 that closing element 64 opens is surpassed makes for example valve of closing element 64() the biasing power of closing, wherein said closing element 64 places between gaseous emissions production process 20 and another operating unit and is used for the described gaseous emissions production process 20 of interference and is communicated with fluid between another operating unit.In some embodiments, in response to the increase of described hydrodynamicpressure, start the opening of described closing element 64, thereby cause starting described shunting gaseous emissions 60 to the supply of another operating unit.In other embodiments, in response to the increase of described hydrodynamicpressure, increase the opening of described closing element 64, thereby cause increasing the supply molar rate of the shunting gaseous emissions 60 that is provided to another operating unit.
Equally, in following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, in other embodiments in these embodiments, for example, pressure in response to the described gaseous emissions 18 of described another operating unit upstream increases, and increase is provided to the supply molar rate of the shunting gaseous emissions 60 of another operating unit, described pressure increase is in response to the reaction zone that is provided to reaction zone 10 and uses the supply molar rate of gaseous emissions feed 24 to reduce, or described supply stops and produces, wherein any one reactions that to be described controllers make in response to confirming actual measurement pH in the reaction zone to be lower than predetermined pH low value.In this type of embodiment, when the pH that records by pH sensor 47 in described controller is confirmed reaction zone is lower than predetermined pH low value, as mentioned above, described controller makes the reaction zone be provided to reaction zone 10 reduce with the supply molar rate of gaseous emissions feed 24 or makes described supply termination.The reaction zone that is provided to reaction zone 10 reduces with the supply molar rate of gaseous emissions feed 24 or described supply stops causing the pressure of the gaseous emissions 18 of described another operating unit upstream correspondingly to increase.The supply molar rate that the pressure increase of the gaseous emissions 18 of described another operating unit upstream causes being provided to the shunting gaseous emissions 60 of another operating unit increases.
In some embodiments, for example, described carbon dioxide treatment figureofmerit is the volumetric molar concentration of the phototroph matter in the reaction zone 10.In some embodiments, for example, it is desirable to, when the volumetric molar concentration of the phototroph matter in the reaction zone 10 was maintained in predetermined concentration or the predetermined concentration scope, the volumetric molar concentration of the phototroph matter in the described reaction zone 10 was controlled as the volumetric molar concentration that the phototroph matter that for example makes results has higher total recovery.In some embodiments, the volumetric molar concentration by phototroph matter in the cell counter 47 assaying reaction districts 10.For example, a kind of suitable cell counter is the AS-16F single passage absorption probe of the optek-Danulat company supply in the hot state of University of Wisconsin-Madison Germany city.Other proper device that are used for the volumetric molar concentration of mensuration phototroph matter comprise other light scattering sensors, for example spectrophotometer.In addition, but the volumetric molar concentration of the described phototroph matter of labor measurement, then with described value manually in the described controller of input to produce required response.
Thus, in some embodiments, for example, at described gaseous emissions production process 20 discharging gaseous emissions 18, and at least a portion gaseous emissions 18 is provided to described reaction zone 10, the gaseous emissions 18 defined reaction districts that wherein said at least a portion is provided to described reaction zone 10 are with gaseous emissions feed 24 time, when the concentration that detects phototroph matter in reaction zone 10 is higher than the high value of predetermined volumetric molar concentration (" the high value of intended target concentration ") of phototroph matter, the adjusting that described reaction zone is done to the supply of reaction zone 10 with gaseous emissions feed 24 comprises: reduce the reaction zone supply molar rate of gaseous emissions feed 24 that is provided to reaction zone 10, or stop described supply.In following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, described technology further comprises the described shunting gaseous emissions 60 of startup to the supply of another operating unit, or increases the supply molar rate of the shunting gaseous emissions 60 that is provided to another operating unit.
In following these embodiments, phototroph matter concentration in the described reaction zone is higher than the high value of predetermined concentration target, in some embodiments in these embodiments, to compare from reception signal and the high value of described predetermined concentration target of the actual measurement volumetric molar concentration of the phototroph matter in the representative reaction zone 10 of described cell counter 47 at described controller, and the volumetric molar concentration of confirming the phototroph matter in the reaction zone 10 is when being higher than the high value of predetermined concentration target, and described controller is provided to reaction zone 10 by reduction reaction zone responds with the supply molar rate of gaseous emissions feed 24.In some embodiments, for example, the reaction zone that makes the opening of described flow control element 50 reduce to reduce to be provided to reaction zone 10 by controller is with the supply molar rate of gaseous emissions feed 24.In some embodiments, for example, make described flow control element 50 close to stop described reaction zone by controller and use gaseous emissions feed 24 to the supply of reaction zone 10.
In following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, in some embodiments in these embodiments, for example, the high value of the reception signal of the volumetric molar concentration of phototroph matter and described predetermined concentration target compares in described controller will be from the representative reaction zone 10 of described cell counter 47, and the volumetric molar concentration of confirming the phototroph matter in the reaction zone 10 is when being higher than the high value of predetermined concentration target, and described controller is further by the supply of the described shunting gaseous emissions 60 of startup to another operating unit, or increase the supply molar rate of the shunting gaseous emissions 60 be provided to another operating unit and respond.In some embodiments, for example, described controller places valve between described gaseous emissions production process 20 and another operating unit to start described shunting gaseous emissions 60 to the supply of another operating unit by driving or increases the supply molar rate of the shunting gaseous emissions 60 that is provided to another operating unit, and wherein said valve is configured for the fluid that disturbs between described process 20 and another operating unit and is communicated with.In some embodiments, for example, described controller places the opening of the valve between described gaseous emissions production process 20 and another operating unit to start described shunting gaseous emissions 60 to the supply of another operating unit by driving.In some embodiments, for example, described controller is by the supply molar rate of the shunting gaseous emissions 60 that the opening that places the valve between described gaseous emissions production process 20 and another operating unit increased be provided to another operating unit.
Equally, in following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, in other embodiments in these embodiments, for example, when the pressure of the described gaseous emissions 18 of described another operating unit upstream is higher than predetermined pressure, start described shunting gaseous emissions 60 to the supply of another operating unit, or increase is provided to the supply molar rate of the shunting gaseous emissions 60 of another operating unit, the pressure of the gaseous emissions 18 of wherein said another operating unit upstream increases to and is higher than predetermined pressure and is in response to that the reaction zone that is provided to reaction zone 10 reduces with the supply molar rate of gaseous emissions feed 24 or described supply stops and produces, and wherein any one is reactions that described controller is made in response to the actual measurement volumetric molar concentration of confirming phototroph matter in the reaction zone is higher than the high value of predetermined concentration target.In this type of embodiment, when described controller confirms that by cell counter 47 the actual measurement volumetric molar concentration of phototroph matter in the reaction zones is higher than the high value of described predetermined concentration target, as mentioned above, described controller makes the reaction zone be provided to reaction zone 10 reduce with the supply molar rate of gaseous emissions feed 24 or makes described supply termination.Reduce the reaction zone be provided to reaction zone 10 with the supply molar rate of gaseous emissions feed 24 or stop described supply and cause the pressure of the gaseous emissions 18 of described another operating unit upstream correspondingly to increase, be higher than predetermined pressure thereby make the pressure of described gaseous emissions 18 become.When the pressure of described gaseous emissions 18 is higher than predetermined pressure, the hydrodynamicpressure that closing element 64 is opened surpasses makes for example valve of closing element 64() the biasing power of closing, wherein said closing element 64 places between gaseous emissions production process 20 and another operating unit and is configured for the described gaseous emissions production process 20 of interference and is communicated with fluid between another operating unit.In some embodiments, open the opening of described closing element 64, thereby start described shunting gaseous emissions 60 to the supply of described another operating component.In some embodiments, increase the opening of described closing element 64, thereby increase the supply molar rate of the shunting gaseous emissions 60 that is provided to another operating unit.
Equally, in following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, in other embodiments in these embodiments, for example, pressure in response to the gaseous emissions 18 of described another operating unit upstream increases, and increase is provided to the supply molar rate of the shunting gaseous emissions 60 of another operating unit, described pressure increase is in response to the reaction zone that is provided to reaction zone 10 and uses the supply molar rate of gaseous emissions feed 24 to reduce, or described supply stops and produces, and wherein any one is that described controller is higher than the reaction that the high value of predetermined concentration target is made in response to the actual measurement volumetric molar concentration of confirming the phototroph matter in the reaction zone.In this type of embodiment, when the phototroph matter volumetric molar concentration that records by cell counter 47 in described controller is confirmed reaction zone is higher than predetermined concentration target high value, as mentioned above, described controller makes the reaction zone be provided to reaction zone 10 reduce with the supply molar rate of gaseous emissions feed 24 or makes described supply termination.Reducing the reaction zone be provided to reaction zone 10 with the supply molar rate of gaseous emissions feed 24 or stopping described supply causes the pressure of the gaseous emissions 18 of described another operating unit upstream correspondingly to increase.The supply molar rate that the pressure increase of the gaseous emissions 18 of described another device upstream causes being provided to the described shunting gaseous emissions 60 of another operating unit increases.
In some embodiments, for example, at described gaseous emissions production process 20 discharging gaseous emissions 18, the any gaseous emissions 18 defined reaction districts that wherein are provided to described reaction zone 10 are with gaseous emissions feed 24 time, when detecting the phototroph matter volumetric molar concentration that is lower than the predetermined volumetric molar concentration low value (" predetermined concentration target low value ") of phototroph matter in the reaction zone 10, the adjusting that described reaction zone is done to the supply of reaction zone 10 with gaseous emissions feed 24 comprises: start described reaction zone and use gaseous emissions feed 24 to the supply of reaction zone 10, or increase the supply molar rate that the reaction zone that is provided to reaction zone 10 is used gaseous emissions feed 24.In following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, and when described shunting gaseous emissions 60 is provided to described another operating unit, in some embodiments in these embodiments, described technology further comprises the supply molar rate that reduces the shunting gaseous emissions 60 that is provided to another operating unit, or stops described supply.
In following these embodiments, phototroph matter volumetric molar concentration in the described reaction zone is lower than described predetermined concentration target low value, in some embodiments in these embodiments, reception signal and the described predetermined concentration target low value of the actual measurement volumetric molar concentration of phototroph matter compare in described controller will be from the representative reaction zone 10 of described cell counter 47, and the actual measurement volumetric molar concentration of confirming the phototroph matter in the reaction zone 10 is when being lower than predetermined concentration target low value, and described controller is by starting described reaction zone with the supply of gaseous emissions feed 24 to reaction zone 10, or increase the reaction zone be provided to reaction zone 10 and respond with the supply molar rate of gaseous emissions feed 24.In some embodiments, for example, start described flow control element 50 by controller and reach this purpose.In some embodiments, the opening of opening described flow control element 50 by controller starts described reaction zone with the supply of gaseous emissions feed 24 to reaction zone 10.In some embodiments, the reaction zone that the opening of described flow control element 50 is increased be provided to reaction zone 10 by controller is with the mole delivery rate of gaseous emissions feed 24.
In following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, and when described shunting gaseous emissions 60 is provided to described another operating unit, in some embodiments in these embodiments, for example, reception signal and the described concentration target low value of phototroph matter volumetric molar concentration compare in described controller will be from the representative reaction zone 10 of cell counter 47, and the volumetric molar concentration of confirming the phototroph matter in the described reaction zone 10 is when being lower than described predetermined concentration target low value, and described controller further is provided to the supply molar rate of the shunting gaseous emissions 60 of another operating unit by reduction, or stop described supply and respond.In some embodiments, for example, described controller places the valve between gaseous emissions production process 20 and another operating unit to reduce described shunting gaseous feed 60 to the supply molar rate of another operating unit or stop described supply by startup, and wherein said valve is configured to disturb described gaseous emissions production process 20 to be communicated with fluid between another operating unit.In some embodiments, for example, described controller is by the supply molar rate of the shunting gaseous emissions 60 that makes the opening that places the valve between gaseous emissions production process 20 and another operating unit reduce to reduce to be provided to another operating unit.In some embodiments, for example, described controller is by stopping the valve closes that places between gaseous emissions production process 20 and another operating unit to be provided to the supply of the shunting gaseous emissions 60 of another operating unit.
Equally, in following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, and when described shunting gaseous emissions 60 is provided to described another operating unit, in other embodiments in these embodiments, for example, pressure in response to the gaseous emissions 18 of another operating unit upstream reduces, and reduction is provided to the supply molar rate of the shunting gaseous emissions 60 of another operating unit, or termination is provided to the supply of the shunting gaseous emissions 60 of another operating unit, wherein the pressure reduction is in response to and starts described reaction zone usefulness gaseous emissions feed 24 to the supply of reaction zone 10, or increase the reaction zone be provided to reaction zone 10 and produce with the supply molar rate of gaseous emissions feed 24, wherein any one to be described controllers be lower than the reaction that predetermined concentration target low value is made in response to the actual measurement volumetric molar concentration of the phototroph matter in the affirmation reaction zone.The pressure that described pressure reduces the gaseous emissions 18 that causes described another operating unit upstream is lower than predetermined minimum pressure, and making for example valve of closing element 64() the biasing power of closing can surpass the hydrodynamicpressure that makes the gaseous emissions 18 that described closing element 64 opens, and wherein said closing element 64 places between gaseous emissions production process 20 and another operating unit and is configured for the described gaseous emissions production process 20 of interference and is communicated with fluid between another operating unit.In some embodiments, reduce the opening of described closing element 64 in response to the pressure of the gaseous emissions 18 of another operating unit upstream reduces, this supply molar rate that can cause being provided to the shunting gaseous emissions 60 of another operating unit reduces.In other embodiments, close described closing element 64 in response to the pressure of the gaseous emissions 18 of another operating unit upstream reduces, this supply that can cause being provided to the shunting gaseous emissions 60 of another operating unit stops.
Equally, in following these embodiments, the outlet of described gaseous emissions production process 20 and another operating unit are collaborative to be arranged so that described shunting gaseous emissions 60 is supplied to another operating unit, and when described shunting gaseous emissions 60 is provided to described another operating unit, in other embodiments in these embodiments, for example, pressure in response to the gaseous emissions 18 of another operating unit upstream reduces, and reduction is provided to the supply molar rate of the shunting gaseous emissions 60 of another operating unit, wherein the pressure reduction is in response to and starts described reaction zone usefulness gaseous emissions feed 24 to the supply of reaction zone 10, or increase the reaction zone be provided to reaction zone 10 and produce with the supply molar rate of gaseous emissions feed 24, wherein any one to be described controllers be lower than the reaction that described predetermined concentration target low value is made in response to the actual measurement volumetric molar concentration of the phototroph matter in the affirmation reaction zone.The supply molar rate that the pressure of the gaseous emissions 18 of described another operating unit upstream reduces the shunting gaseous emissions 60 that causes being provided to another operating unit reduces.
In some embodiments, for example, it is to carry out with reaction zone is regulated simultaneously to the supply of reaction zone 10 with gaseous emissions feed 24 that the shunting gaseous emissions 60 that is supplied to another operating unit is regulated.Thus, in some embodiments, for example, the reaction zone that is provided to reaction zone 10 when reduction is with the supply molar rate of gaseous emissions feed 24 or when stopping described supply, start described shunting gaseous emissions 60 to the supply of another operating unit, or increase the supply molar rate of the shunting gaseous emissions 60 that is provided to another operating unit.In addition, thus, when start described reaction zone with gaseous emissions feed 24 to the supply of reaction zone 10 or when increasing the supply molar rate of the reaction zone usefulness gaseous emissions feed 24 that is provided to reaction zone 10, reduce described shunting gaseous emissions 60 to the supply molar rate of another operating unit or stop described supply.
In some embodiments, for example, described flow control element 50 is flow control valves.In some embodiments, for example, described flow control element 50 is three-way valves, and it also can regulate the supply of the raw material 48 that contains make-up gas, and this will further describe hereinafter.
In some embodiments, for example, described closing element 64 is any in valve, air-lock or the stack cover (stack cap).
In some embodiments, for example, when described reaction zone was provided to reaction zone 10 with gaseous emissions feed 24 in the mode of fluid, described reaction zone was realized by primover 38 with the small part that flows to of gaseous emissions feed 24.With regard to this type of embodiment, the example of suitable primover 38 comprises gas blower, compressor, pump (being used for comprising the liquid pressurization that reaction zone is used gaseous emissions feed 24) and pneumatic pump.In some embodiments, for example, described primover 38 is a kind of variable-speed blowers, and described primover 38 also can be used as the flow control element 50 that is configured to optionally to control the flow rate of described reaction zone feeding material 22 and limits described flow rate.
In some embodiments, for example, described another operating unit is chimney 62.Described chimney 62 is configured to accept the shunting gaseous emissions 60 by the export supply of described gaseous emissions production process 20.When operation, described shunting gaseous emissions 60 is set at sufficiently high pressure, the described chimney 62 so that it can be flowed through.In some embodiments in these embodiments, for example, the space that the shunting gaseous exhaust logistics 60 of the described chimney 62 of flowing through is directed to away from the outlet of described gaseous emissions production process 20.Equally, in some embodiments in these embodiments, for example, when the pressure of described gaseous emissions 18 surpasses predetermined peak pressure, from the described shunting gaseous emissions 60 of described export supply.In this type of embodiment, for example, when the pressure of described gaseous emissions 18 surpasses predetermined peak pressure, can cause described closing element 64 to be opened, thereby carry out the supply of described shunting gaseous emissions 60.
In some embodiments, for example, represent described reaction zone 10 will receive the molar rate reduction from described reaction zone with gaseous emissions feed 24 the such capacity of carbonic acid gas supply in response to detecting the carbon dioxide treatment figureofmerit, chimney 62 is set so that the by-passing portions of gaseous emissions 18 is directed to the space away from the outlet of described gaseous emissions production process 20 discharging gaseous emissions 18, is disposed to environment thereby can reduce the gaseous emissions with unacceptable gas concentration lwevel.
In some embodiments, for example, described chimney 62 is existing chimneys 62, its be adjusted to adapt to by described shunting gaseous emissions 60 provide than the low-flow flux.Thus, in some embodiments, for example, insert liner in the chimney 62 to adapt to described lower flux.
In some embodiments, for example, described another operating unit is the separator that can remove carbonic acid gas from described shunting gaseous emissions 60.In some embodiments, for example, described separator is gas absorber.
In some embodiments, for example, at described gaseous emissions production process 20 discharging gaseous emissions 18, and the described gaseous emissions 18 of at least a portion is provided to reaction zone 10, the described at least a portion gaseous emissions 18 defined reaction districts that wherein are provided to reaction zone 10 are with gaseous emissions feed 24 time, represent reaction zone 10 and will receive the such capacity of carbonic acid gas supply that molar rate reduces (pH that for example detects in the reaction zone is lower than predetermined pH low value when in reaction zone 10, detecting the carbon dioxide treatment figureofmerit, or detect the high value of predetermined volumetric molar concentration that phototroph matter volumetric molar concentration in the reaction zone is higher than phototroph matter) time, represent reaction zone 10 in response to the carbon dioxide treatment figureofmerit that detects and to receive the such capacity of carbonic acid gas supply that molar rate reduces, the adjusting that described reaction zone is done with gaseous emissions feed 24 comprises: reduce the supply molar rate that the reaction zone that is provided to reaction zone 10 is used gaseous emissions feed 24, or stop described supply, in this case, described technology comprises that further startup contains the raw material 48 of make-up gas to the supply of described reaction zone 10, or increases the supply molar rate of the raw material that contains make-up gas 48 that is provided to reaction zone 10.
Contain in the raw material 48 of make-up gas if there is carbonic acid gas, then the volumetric molar concentration of its carbonic acid gas is lower than the carbonic acid gas volumetric molar concentration that is provided to described at least a portion gaseous emissions 18 of reaction zone 10 from described gaseous emissions production process 20.In some embodiments, for example, based on the integral molar quantity of described make-up gas raw material 48, the carbonic acid gas volumetric molar concentration of described make-up gas raw material 48 is lower than 3 moles of %.In some embodiments, for example, based on the integral molar quantity of described make-up gas raw material 48, the carbonic acid gas volumetric molar concentration of described make-up gas raw material 48 is lower than one (1) mole of %.In some embodiments, for example, the raw material 48 that contains make-up gas is provided to described reaction zone 10 as the part of described reaction zone feeding material 22.In some embodiments, for example, described reaction zone feeding material 22 is gaseous state materials.In some embodiments, for example, described reaction zone feeding material 22 comprises the dispersion of gaseous state material in liquid material.
In some embodiments, for example, by regulating described reaction zone is provided to reaction zone 10 with reduction to the supply of reaction zone with gaseous emissions feed 24 reaction zone with the mole delivery rate of gaseous emissions feed 24 or to stop the supply molar rate of described supply and the carbonic acid gas that is provided to described reaction zone 10 to the described raw material 48 that contains make-up gas of reaction zone 10 supplies with reduction or stop described supply be crew-served.In some embodiments, for example,, start shunting gaseous emissions 60 to the supply of another operating unit or increase to the supply molar rate of the shunting gaseous emissions 60 of another operating unit supply with the supply molar rate of gaseous emissions feed 24 or stop described supply and start the raw material 48 that contains make-up gas when the supply of reaction zone 10 or increasing the supply molar rate of the raw material that contains make-up gas 48 that is provided to reaction zone 10 at reaction zone that reduction is provided to reaction zone 10.
In some embodiments in these embodiments, and as mentioned above, described flow control element 50 is three-way valves, and can regulate the raw material 48 that contains make-up gas to the supply of reaction zone, it combines with the adjusting of gaseous emissions feed 24 to the supply of reaction zone 10 with reaction zone, and described carbon dioxide treatment figureofmerit is responded.Thus, represent described reaction zone and will receive the such capacity of carbonic acid gas supply that molar rate reduces (pH that for example detects in the reaction zone is lower than predetermined pH low value when in reaction zone 10, detecting the carbon dioxide treatment figureofmerit, or detect the high value of predetermined volumetric molar concentration that phototroph matter volumetric molar concentration in the reaction zone is higher than phototroph matter) time, described controller contains the raw material 48 of make-up gas to the supply of reaction zone by driving described valve 50 with startup, or increase be provided to reaction zone 10 described contain make-up gas raw material 48 the supply molar rate and respond.In some embodiments, when the raw material 48 that contains make-up gas is provided to reaction zone 10, represent described reaction zone and will receive the such capacity of carbonic acid gas supply that molar rate increases (pH that for example detects reaction zone in is higher than predetermined pH high value when in reaction zone 10, detecting the carbon dioxide treatment figureofmerit, or detect the predetermined volumetric molar concentration low value that phototroph matter volumetric molar concentration in the reaction zone is lower than phototroph matter) time, described controller by the described raw material 48 that contains make-up gas that drives described valve 50 and be provided to reaction zone 10 with reduction the supply molar rate or stop its supply and respond.
In one aspect of the method, at gaseous emissions production process 20 discharging gaseous emissions 18, and the described gaseous emissions 18 of at least a portion is provided to reaction zone 10, the described at least a portion gaseous emissions 18 defined reaction districts that wherein are provided to reaction zone 10 are with gaseous emissions feed 24 time, and the operation of implementing is to make the described reaction zone that is supplied to reaction zone 10 use the supply molar rate of gaseous emissions feed 24 to reduce, or described supply is stopped, in this case, described technology comprises that further startup contains the raw material 48 of make-up gas to the supply of reaction zone 10, or increase contains the raw material 48 of make-up gas to the supply molar rate of described reaction zone 10.
In some embodiments, for example, starting the raw material 48 contain make-up gas is in response to the supply of described reaction zone 10 or the supply molar rate that increases the raw material that contains make-up gas 48 that is provided to reaction zone 10 and detects that the reaction zone that is provided to reaction zone 10 reduces with the supply molar rate of gaseous emissions feed 24 or described supply termination or detect the reaction zone that is provided to reaction zone 10 and have the indication of reduction or the described indication that is supplied with termination to implement with the supply molar rate of gaseous emissions feed 24.For example, as mentioned above, the reaction zone that is provided to reaction zone 10 reduces with the supply molar rate of gaseous emissions feed 24 or described supply stops being in response to and detects the carbon dioxide treatment figureofmerit and represent the such capacity of carbonic acid gas supply that reaction zone 10 will receive the molar rate reduction and implement.In some embodiments, for example, provide flow sensor, with for detection of the described reaction zone molar flow rate with gaseous emissions feed 24, and will represent described reaction zone and be transferred to controller with the signal of the actual measurement molar flow rate of gaseous emissions feed 24.Will be from the reception signal of the described reaction zone of the representative of described flow sensor with the current actual measurement molar flow rate of gaseous emissions feed 24 at described controller, compare with the signal of the previous described reaction zone of representative that receives of representative with the previous actual measurement molar flow rate of gaseous emissions feed 24, and confirm after the molar flow rate reduction of described reaction zone with gaseous emissions feed 24, described controller drives the opening of flow control element, valve (for example valve 50) for example, starting source from the raw material 48 that contains make-up gas to the described raw material 48 that contains make-up gas of reaction zone 10 supplies, or increase from the source of the raw material 48 that contains make-up gas to the described supply molar rate that contains the raw material 48 of make-up gas of reaction zone 10 supplies.
In other embodiments in these embodiments, reduce the reaction zone that is provided to reaction zone 10 with the supply molar rate of gaseous emissions feed 24 or stop described supply by reducing molar rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings.In some embodiments in these embodiments, for example, reduce or detect the indication that reduction is arranged by the molar rate of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings in response to detecting molar rate by the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, correspondingly start the raw material 48 that contains make-up gas to the supply of described reaction zone 10 or correspondingly increase the supply molar rate of the raw material that contains make-up gas 48 that is provided to reaction zone 10.In some embodiments, for example, provide flow sensor, with the molar flow rate for detection of described gaseous emissions 18, and the signal that will represent the actual measurement molar flow rate of described gaseous emissions 18 is transferred to controller.Will be from the reception signal of the current actual measurement molar flow rate of the described gaseous emissions 18 of the representative of described flow sensor at described controller, compare with the signal of the previous actual measurement molar flow rate of the described gaseous emissions 18 of the representative of previous reception, and confirm after the molar flow rate reduction of described gaseous emissions 18, described controller drives the opening of flow control element, valve (for example valve 50) for example, starting source from the raw material 48 that contains make-up gas to the described raw material 48 that contains make-up gas of reaction zone 10 supplies, or increase from the source of the raw material 48 that contains make-up gas to the described supply molar rate that contains the raw material 48 of make-up gas of reaction zone 10 supplies.
In some embodiments, for example, the raw material 48 that contains make-up gas when startup is exposed to the phototroph matter that places reaction zone 10 under photosynthetic effective optical radiation to the supply of reaction zone 10 or when increasing be provided to reaction zone 10 described and contain the supply molar rate of raw material 48 of make-up gas.In some embodiments, for example, for example driving the back by controller by flow control element 50() regulate the described raw material 48 of make-up gas that contains to the supply of reaction zone 10.In some embodiments, the previous actual measurement molar flow rate of the gaseous emissions 18 that discharges at actual measurement molar flow rate and the described gaseous emissions production process 20 of the gaseous emissions 18 that described gaseous emissions production process 20 is discharged compares, and when confirming that molar flow rate by the gaseous emissions 18 of gaseous emissions production process 20 dischargings has reduced, controller is implemented described driving.
With regard to any this above-mentioned implementation of processes scheme, wherein reduce the reaction zone be provided to reaction zone 10 with the supply molar rate of gaseous emissions feed 24 or stop its supply, and startup contains the raw material 48 of make-up gas to the supply of reaction zone 10, or increase is provided to the described supply molar rate that contains the raw material 48 of make-up gas of reaction zone 10, in some embodiments in these embodiments, for example, start and contain the raw material 48 of make-up gas to the supply of reaction zone 10, or increase the described supply molar rate that contains the raw material 48 of make-up gas be provided to reaction zone 10, at least part of compensation because the reaction zone that is provided to reaction zone 10 reduces with the supply molar rate of gaseous emissions feed 24 or the mole delivery rate reduction of the raw material that is provided to reaction zone 10 (for example raw material of described reaction zone feeding material 22) that its supply termination causes, or the supply of described raw material (for example raw material of described reaction zone feeding material 22) stops.In some embodiments, for example, for described owing to the reaction zone that is provided to reaction zone 10 reduces with the supply molar rate of gaseous emissions feed 24 or its supply stops the mole delivery rate reduction of the raw material that is provided to reaction zone 10 (for example raw material of described reaction zone feeding material 22) that causes, or the supply of described raw material (for example raw material of described reaction zone feeding material 22) stops the compensation do, for example contain the supply of the raw material 48 of make-up gas by startup, or increase that the described supply molar rate that contains the raw material 48 of make-up gas realizes like that, can make to the mole delivery rate not variation in fact of the raw material (for example raw material of described reaction zone feeding material 22) of reaction zone 10 supplies.
In some embodiments, (a) below and combination (b): (a) reduce the reaction zone be provided to reaction zone 10 with the supply molar rate of gaseous emissions feed 24 or stop described supply; And (b) start the raw material 48 contain make-up gas to the supply of reaction zone 10 or increase its supply molar rate, can alleviate because the degree that the reaction zone that is provided to reaction zone 10 dies down with stirring in the reaction zone 10 that the supply molar rate reduces or its supply termination causes of gaseous emissions feed 24.In some embodiments, for example, contain the raw material of make-up gas and any described reaction zone and be provided to reaction zone with the combination of gaseous emissions feed 24 as at least a portion of described reaction zone feeding material 22, and described reaction zone feeding material 22 is supplied to reaction zone 10 and the material in the reaction zone is produced agitaion, thereby make that the volumetric molar concentration difference of any phototroph matter is lower than 20% in the reaction zone 10 at 2.In some embodiments, for example, the agitaion that produces can make the volumetric molar concentration difference of phototroph matter any in the reaction zone 10 be lower than 10% at 2.The purpose that supply contains the raw material 48 of make-up gas is to reduce to produce between the phototroph matter any 2 in the reaction zone to be higher than required maximum concentration gradient.
In some embodiments, for example, contain the raw material 48 gaseous state materials of make-up gas.In some embodiments in these embodiments, for example, the raw material 48 that contains make-up gas comprises the dispersion of gaseous state material in liquid material.In some embodiments in these embodiments, for example, the raw material 48 that contains make-up gas comprises air.In some embodiments in these embodiments, for example, provide the raw material 48 that contains make-up gas with the form of fluid.
In some cases, preferably, utilization makes the growth of phototroph matter by the carbonic acid gas in the gaseous emissions 18 of described gaseous emissions production process 20 dischargings, but the carbonic acid gas volumetric molar concentration in the described discharging gaseous emissions 18 is superfluous for the required growth velocity of described phototroph matter.Thus, be provided to described reaction zone 10 at reaction zone feeding material 22, and described reaction zone feeding material 22 is to be supplied with gaseous emissions feed 24 by the reaction zone of gaseous emissions production process 20 dischargings, make when described reaction zone limits at least a portion of described reaction zone feeding material 22 with gaseous emissions feed 24, if the gas concentration lwevel in the described reaction zone feeding material 22 too high (described gas concentration lwevel is at least part of owing to being used for obtaining the carbonic acid gas volumetric molar concentration that reaction zone is used the described gaseous emissions 18 of gaseous emissions feed 24), then when being exposed to described reaction zone feeding material 22, disadvantageous reaction may appear in phototroph matter.
In other cases, be provided to described reaction zone 10 at reaction zone feeding material 22, and described reaction zone feeding material 22 is by additional carbonic acid gas feed 92 supplies, make when described additional carbonic acid gas feed 92 limits at least a portion of described reaction zone feeding material 22, described additional carbonic acid gas feed 92 may contain the carbonic acid gas (being the carbonic acid gas that is higher than 90 moles of % based on the integral molar quantity that replenishes carbonic acid gas feed 92 for example) of relative higher concentration, like this, when being exposed to described reaction zone feeding material 22, disadvantageous reaction may appear in phototroph matter.
Thus, in one aspect of the method, carbonic acid gas is provided to described reaction zone 10, and the carbonic acid gas of supplying limits described reaction zone carbonic acid gas feed.Provide to concentrate carbonic acid gas feed 25A, wherein said concentrated carbonic acid gas feed 25A comprises described reaction zone carbonic acid gas feed.Described concentrated carbonic acid gas feed 25A and 90 blending of additional gaseous diluent.Described ooze to mix can produce the carbonic acid gas feed 25B of dilution, the carbonic acid gas volumetric molar concentration of the carbonic acid gas feed 25B of wherein said dilution is lower than the carbonic acid gas volumetric molar concentration of described concentrated carbonic acid gas feed 25A.The carbonic acid gas feed 25B of the described dilution of at least a portion is provided to reaction zone 10.The carbonic acid gas volumetric molar concentration of described additional gaseous diluent 90 is lower than the carbonic acid gas volumetric molar concentration of described concentrated carbonic acid gas feed 25A.In some embodiments, for example, described reaction zone carbonic acid gas feed comprises by the carbonic acid gas of described gaseous emissions production process 20 dischargings or is limited by it.In some embodiments, for example, described reaction zone carbonic acid gas feed comprises described additional carbonic acid gas feed 92 or is limited by it.
In one aspect of the method, when gaseous emissions production process 20 discharging gaseous emissions 18, to concentrate carbonic acid gas feed 25A and 90 blending of additional gaseous diluent, wherein said concentrated carbonic acid gas feed 25A comprises for the feed 24A that obtains gaseous emissions, and at least a portion of the wherein said gaseous emissions 18 that is discharged by described gaseous emissions production process 20 for the feed 24A that obtains gaseous emissions is limited.Described blending effect has produced the carbonic acid gas feed 25B of dilution, and the carbonic acid gas volumetric molar concentration of the carbonic acid gas feed 25B of wherein said dilution is lower than the carbonic acid gas volumetric molar concentration of described concentrated carbonic acid gas feed 25A.The carbonic acid gas feed 25B of the described dilution of at least a portion is provided to reaction zone 10.The carbonic acid gas volumetric molar concentration of described additional gaseous diluent 90 is lower than the carbonic acid gas volumetric molar concentration of described concentrated carbonic acid gas feed 25A.In some embodiments in these embodiments, for example, in described concentrated carbonic acid gas feed 25A and described additional gaseous diluent 90 blending, will place the phototroph matter in the reaction zone 10 to be exposed under photosynthetic effective optical radiation.In some embodiments, for example, described concentrated carbonic acid gas feed 25A is limited for the feed 24A that obtains gaseous emissions by described.In some embodiments, for example, described concentrated carbonic acid gas feed 25A comprises described additional carbonic acid gas feed 92.In some embodiments in these embodiments, for example, described additional carbonic acid gas feed 92 is supplied to described concentrated carbonic acid gas feed 25A, carries out blending simultaneously.
In some embodiments, for example, the carbonic acid gas feed 25B of described dilution contains and is lower than the predetermined peaked carbonic acid gas volumetric molar concentration of carbonic acid gas volumetric molar concentration.In some embodiments, for example, based on the integral molar quantity of the carbonic acid gas feed 25B of described dilution, described predetermined carbonic acid gas volumetric molar concentration maximum value is at least 30 moles of %.In some embodiments, for example, based on the integral molar quantity of the carbonic acid gas feed 25B of described dilution, described predetermined carbonic acid gas volumetric molar concentration maximum value is at least 20 moles of %.In some embodiments, for example, based on the integral molar quantity of the carbonic acid gas feed 25B of described dilution, described predetermined carbonic acid gas volumetric molar concentration maximum value is at least 10 moles of %.
In some embodiments, for example, the blending of described additional gaseous diluent 90 and described concentrated carbonic acid gas feed 25A is in response to the carbonic acid gas volumetric molar concentrations that detect by in the gaseous emissions 18 of carbon dioxide generating process 20 dischargings and implements greater than predetermined carbonic acid gas volumetric molar concentration maximum value.In some embodiments, for example, based on the integral molar quantity of described gaseous emissions 18, described predetermined carbonic acid gas volumetric molar concentration maximum value is at least 10 moles of %.In some embodiments, for example, based on the integral molar quantity of described gaseous emissions 18, described predetermined carbonic acid gas volumetric molar concentration maximum value is at least 20 moles of %.In some embodiments, for example, based on the integral molar quantity of described gaseous emissions 18, described predetermined carbonic acid gas volumetric molar concentration maximum value is at least 30 moles of %.Thus, in some embodiments, for example, carbon dioxide sensor 781 is provided, with the carbonic acid gas volumetric molar concentration for detection of the gaseous emissions 18 that is discharged, and the signal that will represent by the carbonic acid gas volumetric molar concentration of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings is transferred to controller.To compare and the carbonic acid gas volumetric molar concentration of confirming described gaseous emissions 18 during greater than described predetermined carbonic acid gas volumetric molar concentration maximum value from the reception signal of the actual measurement carbonic acid gas volumetric molar concentration of the described gaseous emissions 18 of the representative of described carbon dioxide sensor 781 and predetermined carbonic acid gas volumetric molar concentration maximum value at described controller, the opening of described controller opening controlling valve door 901 or its opening is increased, thus supply replenishes gaseous diluent 90 to be used for and described concentrated carbonic acid gas feed 25A blending.
In some embodiments, for example, at described gaseous emissions production process 20 discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to reaction zone 10, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of reaction zone 10 discharges with discharging carbonic acid gas feed, when detecting the reaction zone that the is supplied to reaction zone 10 supply molar rate with discharging carbonic acid gas feed the indication of reduction arranged, increase the supply molar rate of the additional carbonic acid gas feed 92 that is provided to reaction zone 10, or start additional carbonic acid gas feed 92 to the supply of reaction zone 10.In response to detecting described reaction zone the indication of reduction is being arranged to the supply molar rate of reaction zone 10 with discharging carbonic acid gas feed, and described additional carbonic acid gas feed 92 is supplied to described concentrated carbonic acid gas feed 25A, thereby make that the described concentrated carbonic acid gas feed 25A of at least a portion is limited by described additional carbonic acid gas feed 92, and when the described concentrated carbonic acid gas feed 25A of at least a portion is provided to reaction zone 10, described concentrated carbonic acid gas feed 25A and described additional gaseous diluent 90 blending and produced the carbonic acid gas feed 25B of dilution.In some embodiments, for example, the source of described additional carbonic acid gas feed 92 is dioxide bottles.In some embodiments, for example, the source of described additional carbonic acid gas feed 92 is air supplies.In some embodiments in these embodiments, when the carbonic acid gas feed 25B that produces the carbonic acid gas feed 25B of described dilution and the described dilution of at least a portion in described concentrated carbonic acid gas feed 25A and described additional carbonic acid gas feed 92 blending is provided to reaction zone 10, will place the described phototroph matter in the reaction zone 10 to be exposed under photosynthetic effective optical radiation.In some embodiments, for example, described concentrated carbonic acid gas feed 25A and described additional carbonic acid gas feed 92 blending to be producing the carbonic acid gas feed 25B of described dilution, are lower than the peaked carbonic acid gas volumetric molar concentration of described predetermined gas concentration lwevel thereby make the carbonic acid gas feed 25B of described dilution contain.In some embodiments, for example, blending is in response to and detects described concentrated carbonic acid gas feed 25A(it comprises described additional carbonic acid gas feed 92) in the carbonic acid gas volumetric molar concentration be higher than predetermined carbonic acid gas volumetric molar concentration maximum value and implement.In some embodiments, for example, it is any indication mentioned above that described reaction zone has the indication of reduction with discharging carbonic acid gas feed to the supply molar rate of reaction zone 10.In some embodiments, for example, keep constant growth velocity in order to make phototroph matter, provide the reduction with the supply molar rate of gaseous emissions feed 24 of reaction zone that described additional carbonic acid gas feed 92 is provided to reaction zone 10 with compensation, if to be considered to only be temporary words (for example being less than for two weeks) in described reduction.
In following these embodiments, described concentrated carbonic acid gas feed 25A comprises additional carbonic acid gas feed 92, and described concentrated carbonic acid gas feed 25A and described additional gaseous diluent 90 blending are to produce the carbonic acid gas feed 25B of described dilution, the carbonic acid gas feed 25B of the described dilution of at least a portion is provided to reaction zone, in this case, blending to described concentrated carbonic acid gas feed 25A and described additional gaseous diluent 90 is designed, and makes to produce the dilution carbonic acid gas feed 25B that contains the carbonic acid gas of being scheduled to volumetric molar concentration.
In some embodiments, for example, described additional gaseous diluent 90 is gaseous state materials.In some embodiments, for example, described additional gaseous diluent 90 comprises air.In some embodiments, for example, described additional gaseous diluent 90 is provided to described concentrated carbonic acid gas feed 25A with the form of fluid.
Place the described reaction mixture in the reaction zone 10 to be exposed under photosynthetic effective optical radiation, thereby can carry out photosynthesis.Described photosynthesis can make the growth of phototroph matter.In some embodiments, for example, provide the phototroph matter that is rich in carbonic acid gas that places in the aqueous medium, and place the phototroph matter that is rich in carbonic acid gas in the aqueous medium to be exposed under photosynthetic effective optical radiation to carry out photosynthesis with described.
In some embodiments, for example, described optical radiation is characterised in that wavelength is between 400 ~ 700nm.In some embodiments, for example, described optical radiation is the form of natural daylight.In some embodiments, for example, provide described optical radiation by artificial light 14.In some embodiments, for example, described optical radiation comprises natural daylight and artificial light.
In some embodiments, for example, the intensity of the light that control provides is to meet the required growth velocity of described phototroph matter in the reaction zone 10.In some embodiments, the intensity of regulating the light that provides according to the mensuration of described phototroph matter growth velocity in the reaction zone 10.In some embodiments, the intensity of regulating the light that provides according to the supply molar rate that is provided to the carbonic acid gas in the described reaction zone feeding material 22.
In some embodiments, for example, the condition in visual response district 10 provides the light of predetermined wavelength.Said that usually, described light was to provide with the blue-light source of 1:4 and red light source.This ratio is looked employed phototroph and difference.In addition, when needs simulation circulation pattern every day, can change described ratio.For example, when simulation dawn or dusk, provide more red light, more blue light then is provided when simulation situation at noon.In addition, can change this ratio by providing more blue light to simulate the manual recovery circulation time.
Find that blue light can stimulate the reconstruction of alga cells internal structure, its internal structure may become impaired after one section is grown fast, and ruddiness then promotes algae grows.Equally, find, as long as enough carbonic acid gas (and in some embodiments, providing other nutrition) are provided, from spectrum, get rid of green glow can in addition surpass and still make algae growth constantly in reaction zone 10 under the situation that before has been confirmed as its " saturation point " in water.
With regard to artificial light, for example, suitable artificial light 14 comprises sunk optical fiber, photodiode, LED band and fluorescence.Any LED band known in the art can be used in this technology.In the situation of sunk LED, its design comprises uses solar cell to supply electric power.In the situation of sunk LED, in some embodiments, for example, the energy comprises and substitutes the formula energy, and for example wind-force, photovoltaic cell, fuel cell etc. are in order to supply electric power for LED.
With regard to the embodiment in described reaction zone 10 is placed in the bioreactor 12 that comprises storage tank, in some embodiments in these embodiments, for example, provide described luminous energy by the combination of following light source.The lamp 16 of sunlight form is caught by solar energy collector and utilized and can provide the conventional lenses of the light of required wavelength to filter to reaction zone 10.Then, be transferred in the bioreactor 12 by photoconduction or fiber optic materials from the light through filtering of solar energy collector, in bioreactor 12, described light becomes and is scattered in the reaction zone 10.In some embodiments, except sunlight, fluorescent tubes in the bioreactor 12 also comprise the high-capacity LED array, and its light that specific wavelength can be provided is to be replenished sunlight as required or to be that reaction zone 10 provides whole required light in dark period (for example night).In some embodiments, with regard to photoconduction, for example, make in the photoconduction of transparent heat-transfer medium (for example ethylene glycol solution) in described bioreactor 12 and circulate, to regulate the temperature in the photoconduction, and in some cases, provide described heat-transfer medium so that the heat of described photoconduction controllably dissipates and enters in the described reaction zone 10.In some embodiments, for example, therefore can be according to the power demand of predicting described LED at gaseous emissions 18 observed trend and controlled, this is because these observed trend help to predict the growth velocity of described phototroph matter in the time afterwards.
In some embodiments, in the described reaction zone feeding material 22 of supply, described reaction mixture is exposed under photosynthetic effective optical radiation.
In some embodiments, for example, the growth velocity of described phototroph matter depends on that available reaction zone limits and be provided to reaction zone 10 with gaseous emissions feed 24(by at least a portion of the gaseous emissions 18 of described gaseous emissions production process 20 dischargings).It defines nutrition, water and light intensity required when making the maximization of phototroph matter growth velocity then.In some embodiments, for example, provide controller, for example computer implemented system to be used for monitoring and controlling the operation of the various elements of technology described herein, comprises light, valve, sensor, gas blower, fan, air-lock, pump etc.
Give off reaction zone product 500 by described reaction zone.Described reaction zone product 500 comprises phototroph matter 58.In some embodiments, for example, described reaction zone product 500 comprises at least a portion in the content of described reaction zone 10.Thus, can collect phototroph matter from the reaction zone product 500 of described discharging.In some embodiments, for example, reaction zone gaseous exhaust product 80 is also discharged by described reaction zone 10.
In one aspect of the method, provide a kind of in reaction zone 10 technology of grow light health material, it comprises the molar rate of regulating the described phototroph matter of discharging according to the detection of phototroph matter growth indexes.
Being used for carrying out photosynthetic reaction mixture (form of production purposes reaction mixture) under being exposed to photosynthetic effective optical radiation is placed in the described reaction zone 10.Described production purposes reaction mixture comprise can in reaction zone 10, grow for the production of purposes phototroph matter.The production purposes phototroph matter of one reaction zone concentration is provided in reaction zone 10 thus.Described reaction mixture in placing reaction zone 10 is exposed under photosynthetic effective optical radiation, and in reaction zone, carry out the growth of production purposes phototroph matter, and when giving off described production purposes phototroph matter from reaction zone 10, when variant between the phototroph matter growth indexes in detecting reaction zone and the predetermined phototroph matter growth indexes target value, described technology comprises the discharging molar rate of described production purposes phototroph matter in the conditioned reaction district 10, wherein said predetermined phototroph matter growth indexes target value with place reaction zone 10 in and predetermined mole of growth velocity being exposed to the production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation be associated.The growth that described production purposes phototroph matter is carried out comprises the growth of being undertaken by photosynthesis.In some embodiments, for example, described growth comprises the growth that places the metabolic process of the extra-nutrition thing in the reaction mixture to carry out by consumption.
Described predetermined phototroph matter growth indexes target value is the phototroph matter growth indexes target value during for the mole growth velocity of being scheduled to corresponding to the mole growth velocity that places in the reaction zone 10 and be exposed to the production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation.
In some embodiments, for example, with place in the reaction zone 10 and be exposed to the production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation predetermined growth velocity 10% with the interior growth of carrying out described production purposes phototroph matter.In some embodiments, with place in the reaction zone 10 and be exposed to the production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation predetermined growth velocity 5% with the interior growth of carrying out described production purposes phototroph matter.In some embodiments, for example, with place in the reaction zone 10 and be exposed to the production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation predetermined growth velocity 1% with the interior growth of carrying out described production purposes phototroph matter.
In some embodiments, for example, described adjusting is in response to the comparison of measured light health material growth indexes and described predetermined phototroph matter growth indexes target value and implements.
In some embodiments, for example, described technology comprises that further detection phototroph matter growth indexes is to provide described measured light health material growth indexes.
In some embodiments, for example, described phototroph matter growth indexes is the volumetric molar concentration of the phototroph matter in the reaction mixture that places in the described reaction zone 10.
In some embodiments, for example, described measured light health material growth indexes representative places the volumetric molar concentration of the interior production purposes phototroph matter of the reaction mixture in the described reaction zone 10.Thus, in some embodiments in these embodiments, for example, described measured light health material growth indexes is the volumetric molar concentration of the production purposes phototroph matter in the reaction mixture that places in the reaction zone 10.In other embodiments in these embodiments, for example, described measured light health material growth indexes is the volumetric molar concentration of described production purposes phototroph matter in the reaction zone product 500.In some embodiments, for example, detect described concentration by cell counter 47.For example, a kind of suitable cell counter is the AS-16F single passage absorption probe by the optek-Danulat company supply in the hot state of University of Wisconsin-Madison Germany city.Other proper device that are used for the volumetric molar concentration of mensuration phototroph matter index comprise other light scattering sensors, for example spectrophotometer.In addition, but the volumetric molar concentration of the described phototroph matter of labor measurement manually inputs to described value described controller then to produce required response.
In some embodiments, for example, described phototroph matter is grown comprise to reaction zone 10 supplying carbon dioxides and with production purposes reaction mixture to be exposed under photosynthetic effective optical radiation.In some embodiments, for example, the carbonic acid gas of supplying is to be supplied by the gaseous emissions 18 of described gaseous emissions production process 20.In some embodiments, for example, described gaseous emissions production process 20 gives off gaseous emissions 18, and the described gaseous emissions 18 of at least a portion is provided to reaction zone feeding material 22(as reaction zone gaseous emissions feed 24), and described reaction zone feeding material 22 is provided to reaction zone 10, at this moment, the carbonic acid gas of supplying is to be supplied by the gaseous emissions 18 of described gaseous emissions production process 20.Thus, in some embodiments, for example, when growing, carbonic acid gas is fed to described reaction zone 10, wherein when described gaseous emissions 18 was discharged by gaseous emissions production process 20, at least a portion was provided to the carbonic acid gas of reaction zone 10 by described gaseous emissions 18 supplies.
In some embodiments, for example, described production purposes reaction mixture also contains water and carbonic acid gas.
In some embodiments in these embodiments, for example, as mentioned above, the predetermined molar rate of described phototroph matter growth is based on being placed in the reaction zone 10 and being exposed to the maximum molar rate of the described phototroph matter growth in the reaction mixture under photosynthetic effective optical radiation.
In some embodiments, for example, the predetermined mole growth velocity of described production purposes phototroph matter be place in the reaction zone 10 and be exposed to the production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation maximum mole growth velocity at least 90%.In some embodiments, for example, described predetermined mole growth velocity be place in the reaction zone 10 and be exposed to the production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation maximum mole growth velocity at least 95%.In some embodiments, for example, described predetermined mole growth velocity be place in the reaction zone 10 and be exposed to the production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation maximum mole growth velocity at least 99%.In some embodiments, for example, described predetermined mole growth velocity equals to place in the reaction zone 10 and is exposed to the maximum mole growth velocity of the production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation.
In some embodiments, for example, when the molar rate of regulating by the described production purposes phototroph matter of reaction zone 10 dischargings, with constant or constant in fact for some time that reaches at least one (1) hour of the volume maintenance that places the described reaction mixture in the reaction zone.In some embodiments, for example, described period is at least six (6) hours.In some embodiments, for example, described period is at least 24 hours.In some embodiments, for example, described period is at least seven (7) days.In some embodiments, for example, when carrying out described adjusting, in order to reach the optimum economic benefit of described technology, reach for some time with the volume maintenance that places the described reaction mixture in the reaction zone is constant or constant in fact, make the predetermined molar rate of described predetermined phototroph matter growth indexes value and described phototroph matter growth in described period, keep constant or constant in fact.
In some embodiments, for example, described reaction zone 10 is placed in the bioreactor 12, and described production purposes phototroph matter be by to the substitute mode of reaction zone 10 supply water-based feeding materials 4 from described bioreactor 12(and reaction zone 10) discharge.In other words, can be from bioreactor 12(and reaction zone 10 to described reaction zone 10 supply water-based feeding materials 4) displace described production purposes phototroph matter, thereby by described bioreactor 12(and reaction zone 10) give off described production purposes phototroph matter.In some embodiments, for example, described production purposes phototroph matter is that the overflow substitute mode by bioreactor 12 is discharged from described bioreactor 12.
In some embodiments, for example, described water-based feeding material 4 does not contain phototroph matter in fact.In other embodiments, for example, described water-based feeding material contains the phototroph matter that volumetric molar concentration is lower than the volumetric molar concentration of the phototroph matter in the reaction mixture in the reaction zone 10.
In some embodiments, for example, described water-based feeding material 4 is with from the form supply of the fluid in the source 6 of water-based feeding material 4.For example, described fluid is by prime mover driven, and described primover for example is pump.In some embodiments, for example, described water-based feeding material comprises additional aqueous substance feed 44.As mentioned above, in some embodiments, for example, the described additional aqueous substance feed 44 of at least a portion is by container 28 supplies.Thus, contain in the embodiment of described additional aqueous substance feed 44 at water-based feeding material 4, described container is as the source 6 of described water-based feeding material 4.
In some embodiments, for example, described water-based feeding material 4 comprises extra-nutrition thing feed 42 and additional aqueous substance feed 44.In some embodiments in these embodiments, described water-based feeding material 4 is provided to the reaction zone feeding material 22 of described reaction zone 10 upstreams.Thus, as mentioned above and with reference to Fig. 2, in some embodiments in these embodiments, described extra-nutrition thing feed 42 and additional aqueous substance feed 44 are provided to reaction zone feeding material 22 by the shower nozzle 40 of reaction zone 10 upstreams.
In some embodiments, for example, when measured light health material growth indexes is the actual measurement volumetric molar concentration of the volumetric molar concentration of the phototroph matter in the reaction mixture that places in the reaction zone 10 and the phototroph matter in the described reaction mixture that places in the reaction zone 10 when being lower than predetermined phototroph matter volumetric molar concentration target value, described adjusting comprises the molar rate of the production purposes phototroph matter that reduces by 10 dischargings of autoreaction district.In some embodiments in these embodiments, for example, by discharging described production purposes phototroph matter to the substitute mode of reaction zone 10 supply water-based feeding materials 4 from reaction zone 10, and by reducing described water-based feeding material 4 to the supply molar rate of reaction zone 10 or stopping described supply, to reduce from the molar rate of the described production purposes phototroph matter of reaction zone 10 dischargings.Thus, when discharging described production purposes phototroph matter by this type of substitute mode, in some embodiments, for example, when described measured light health material growth indexes is the volumetric molar concentration of the phototroph matter in the reaction mixture that places in the reaction zone 10, phototroph matter in the described reaction mixture that places in the reaction zone 10 is being compared by cell counter 47 detected actual measurement volumetric molar concentrations and predetermined phototroph matter volumetric molar concentration target value, and when confirming that described actual measurement volumetric molar concentration is lower than described predetermined phototroph matter volumetric molar concentration target value, described controller responds by reducing described water-based feeding material 4 to the supply molar rate of reaction zone 10 or stopping described supply, reduces described production purposes phototroph matter thus from the molar rate of reaction zone 10 dischargings or stops its discharging.In some embodiments, for example, described controller reduces to reduce the molar rate that described water-based feeding material 4 is supplied to reaction zone 10 by the opening that makes control valve 441, and described control valve 441 places and helps to be supplied in the runner of reaction zone 10 from 6 fluids with water-based feeding material 4 of originating.In some embodiments, for example, described controller stops described water-based feeding material 4 to the supply of reaction zone 10 by control valve 441 is closed, and described control valve 441 places and helps to be supplied in the runner of reaction zone 10 from 6 fluids with water-based feeding material 4 of originating.In some embodiments, for example, the fluid of described water-based feeding material 4 is by prime mover driven, and described primover for example is pump 281.In some embodiments, for example, the fluid of described water-based feeding material 4 is by segregation drive.In some embodiments, for example, described water-based feeding material 4 comprises the additional aqueous substance feed 44 by container 28 supplies.In some embodiments, described water-based feeding material 4 is the additional aqueous substance feed 44 by container 28 supplies.In some embodiments in these embodiments, for example, described additional aqueous substance feed 44 is supplied by container 28 by means of pump 281, and in other embodiments in these embodiments, for example, described additional aqueous substance feed 44 is supplied by container 28 by means of gravity.In some embodiments, for example, when providing primover (for example pump 281) that described water-based feeding material 4 is flowed to reaction zone 10, controller is by making for example pump 281 of described primover 281() power of hydrotropisms's feeding material 4 supply reduces, for example by reducing the speed of described primover 281, make described water-based feeding material 4 reduce to the supply molar rate of reaction zone 10.In some embodiments, for example, when providing primover (for example pump 281) that described water-based feeding material 4 is flowed to reaction zone 10, controller stops by making described primover 38, makes described water-based feeding material 4 stop to the supply of reaction zone 10.
In some embodiments, for example, when described measured light health material growth indexes is the actual measurement volumetric molar concentration of the volumetric molar concentration of the phototroph matter in the reaction mixture that places in the reaction zone 10 and the phototroph matter in the described reaction mixture that places in the reaction zone 10 when being higher than predetermined phototroph matter volumetric molar concentration target value, described adjusting comprises the molar rate of the production purposes phototroph matter that increases by 10 dischargings of autoreaction district.In some embodiments in these embodiments, for example, by discharging described production purposes phototroph matter to the substitute mode of reaction zone 10 supply water-based feeding materials 4 from reaction zone 10, and by starting described water-based feeding material 4 to the supply of reaction zone 10 or increasing its supply molar rate, to increase from the molar rate of the described production purposes phototroph matter of reaction zone 10 dischargings.Thus, when discharging described production purposes phototroph matter by this type of substitute mode, in some embodiments, for example, when described measured light health material growth indexes is the volumetric molar concentration of the phototroph matter in the reaction zone 10, phototroph matter in the described reaction mixture that places in the reaction zone 10 is being compared by cell counter 47 detected actual measurement volumetric molar concentrations and predetermined phototroph matter volumetric molar concentration target value, and when confirming that described actual measurement volumetric molar concentration is higher than described predetermined phototroph matter volumetric molar concentration target value, described controller responds by starting described water-based feeding material 4 to the supply of reaction zone 10 or increasing its supply molar rate, increases described production purposes phototroph matter thus from the molar rate of reaction zone 10 dischargings.In some embodiments, for example, described controller starts described water-based feeding material 4 to the supply of reaction zone 10 by making control valve 441, and described control valve 441 places and helps to be supplied in the runner of reaction zone 10 from 6 fluids with water-based feeding material 4 of originating.In some embodiments, for example, described controller increases described water-based feeding material 4 to the supply molar rate of reaction zone 10 by the opening that makes control valve 441, and described control valve 441 places and helps to be supplied in the runner of reaction zone 10 from 6 fluids with water-based feeding material 4 of originating.In some embodiments, for example, the fluid of described water-based feeding material 4 is by prime mover driven, and described primover for example is pump 281.In some embodiments, for example, the fluid of described water-based feeding material 4 is by segregation drive.In some embodiments, for example, described water-based feeding material comprises the additional aqueous substance feed 44 by container 28 supplies.In some embodiments, for example, described water-based feeding material is the additional aqueous substance feed 44 by container 28 supplies.In some embodiments in these embodiments, for example, described additional aqueous substance feed 44 is supplied by container 28 by means of pump 281, in other embodiments in these embodiments, for example, described additional aqueous substance feed 44 is supplied by container 28 by means of gravity.In some embodiments, for example, when providing primover (for example pump 281) that described water-based feeding material 4 is flowed to reaction zone 10, controller starts described water-based feeding material 4 to the supply of reaction zone 10 by driving described primover.In some embodiments, for example, when providing primover (for example pump 281) that described water-based feeding material 4 is flowed to reaction zone 10, controller increases by the power that makes described primover hydrotropisms feeding material 4 supplies makes described water-based feeding material 4 increase to the supply molar rate of reaction zone 10.
In some embodiments, for example, give off described phototroph matter 58 by the primover that is communicated with reaction zone 10 fluids from reaction zone 10.Thus, in some embodiments, for example, the adjusting of discharging the molar rate of described phototroph matter from reaction zone comprises:
(i) there are differences in response to detecting between measured light health material growth indexes (placing in the reaction mixture in the reaction zone) and the predetermined phototroph matter growth indexes target value, regulated from the supply of electric power that reaction zone 10 is discharged primover of phototroph matter being used for, wherein said predetermined phototroph matter growth indexes target value with place reaction zone 10 in and predetermined mole of growth velocity being exposed to the phototroph matter in the described reaction mixture under photosynthetic effective optical radiation be associated; And
(ii) when the supply of electric power of primover is regulated, in response to there are differences between the actual measurement volume index that detects the reaction mixture in the reaction zone and the predetermined reaction mixture volume index value, supply molar rate to the described additional aqueous substance feed 44 in supply response district 10 is regulated, wherein said predetermined reaction mixture volume index value represents the volume of the reaction mixture in the described reaction zone 10, wherein in described reaction zone 10, phototroph matter growth indexes in the reaction mixture is arranged on predetermined phototroph matter growth indexes target value, simultaneously, the phototroph matter in the reaction mixture is grown with predetermined phototroph matter mole growth velocity.
In some embodiments, for example, the reaction mixture volume index in the described reaction zone 10 (or abbreviate as " reaction mixture volume index ") is the last liquid level of the reaction mixture in the reaction zone 10.In some embodiments, for example, measure liquid level on this by liquid level sensor.Thus, in some embodiments, for example, provide liquid level sensor, with the liquid level of the reaction mixture in the detection reaction district 10, and the signal that will represent described actual measurement liquid level is transferred to controller.Described controller compares described reception signal and predetermined fluid level value (the reaction mixture volume index value that representative is predetermined).When if the reception signal is lower than the predetermined fluid level value, described controller responds by starting described additional aqueous substance feed 48 to the supply of reaction zone 10 or increasing its supply molar rate, for example implements by making to be configured to disturb described additional aqueous substance feed 48 to the valve open (starting the situation of supply) of the supply of reaction zone 10 or to increase its opening (having additional supply of the situation of molar rate).When if described reception signal is higher than the predetermined fluid level value, described controller be provided to by reduction reaction zone 10 described additional aqueous substance feed 48 the supply molar rate or stop described supply and respond, for example be configured to disturb described additional aqueous substance feed 48 to reduce (reducing the situation of supply molar rate) or make described valve closes (stopping the situation of supply) to the opening of the valve of the supply of reaction zone 10 by making.In making reaction zone 10, the supply of reaction zone 10 maintains required liquid level by regulating described additional aqueous substance feed 48, to the water of reaction zone 10 supply make up water to replace discharging from reaction zone 10 in company with phototroph matter, so that the growth molar rate optimizing of the described phototroph matter in the reaction zone 10, and make the molar rate optimizing of the phototroph matter of discharging from reaction zone 10 thus.
In some embodiments, for example, when the molar rate that described phototroph matter is discharged from reaction zone 10 was regulated, described technology further comprised: in response to detecting one or more nutrition in the reaction zone 10 (as NO 3) measured concentration and corresponding intended target concentration value between there are differences, the supply molar rate of the extra-nutrition thing feed in supply response district is regulated.
In some embodiments, for example, when the molar rate that described phototroph matter is discharged from reaction zone 10 is regulated, described technology further comprises: in response to the detection of at least a carbon dioxide treatment figureofmerit, the molar rate of the carbon-dioxide flow in supply response district 10 is regulated.In some embodiments, for example, in reaction zone 10, carry out the detection of described at least a carbon dioxide treatment figureofmerit.The carbon dioxide treatment figureofmerit that detects is any feature that represents the capacity of reaction zone 10, and the capacity of wherein said reaction zone 10 is that the capacity that transforms takes place for photosynthetic response that the phototroph matter of carbonic acid gas in placing described reaction zone that described reaction zone will receive carbonic acid gas and at least a portion is received is carried out.In some embodiments, for example, the carbon dioxide treatment figureofmerit that detects is the pH in the reaction zone 10.In some embodiments, for example, the carbon dioxide treatment figureofmerit that detects is the volumetric molar concentration of phototroph matter in the reaction zone 10.
In some embodiments, for example, when the molar rate that described phototroph matter is discharged from reaction zone 10 is regulated, described technology further comprises: the molar rate in response to the carbonic acid gas that detects supply response district 10 changes, and the intensity of photosynthetic effective optical radiation that described reaction mixture is stood is regulated.
In one aspect of the method, described technology further comprises predetermined described phototroph matter growth indexes target value.Thus, the described production purposes reaction mixture of representative is provided and can be used for carrying out photosynthetic assessment purposes reaction mixture under photosynthetic effective optical radiation being exposed to, make the phototroph matter in the described assessment purposes reaction mixture become the assessment purposes phototroph matter of the described production purposes phototroph matter of representative.In some embodiments, for example, described production purposes reaction mixture also contains water and carbonic acid gas, and described assessment purposes reaction mixture also contains water and carbonic acid gas.Described assessment purposes reaction mixture in placing reaction zone 10 is exposed to photosynthetic effective optical radiation and when causing described assessment purposes phototroph matter in assessment purposes reaction mixture to be grown, described technology further comprises:
(i) detect described phototroph matter growth indexes at least termly so that a plurality of detected values of (" at least termly " refers to detect off and on or detect serially with the identical or different timed interval) the phototroph matter growth indexes that is detected for some time to be provided;
(ii) calculate the mole growth velocity of described assessment purposes phototroph matter according to a plurality of detected values of described phototroph matter growth indexes, determine a plurality of mole growth velocitys of described assessment purposes phototroph matter in described period thus; And
(iii) based on the mole growth velocity of calculating and the detected value that is used for the described phototroph matter growth indexes of the described mole of calculating growth velocity, set up the mole growth velocity of described assessment purposes phototroph matter and the relation between the described phototroph matter growth indexes, make the relation of setting up between the mole growth velocity of described assessment purposes phototroph matter and the described phototroph matter growth indexes represent the mole growth velocity of described production purposes phototroph matter in the reaction zone 10 and the relation between the described phototroph matter growth indexes, establish the mole growth velocity of reaction zone 10 interior described production purposes phototroph matter and the relation between the described phototroph matter growth indexes thus.
Select predetermined mole growth velocity from the described mole growth velocity that calculates.Described phototroph matter growth indexes target value is defined as: according to the relation of establishing between the mole growth velocity of described production purposes phototroph matter in the reaction zone and the described phototroph matter growth indexes, and the phototroph matter growth indexes when causing described predetermined mole growth velocity.Thus, make thus between described phototroph matter growth indexes target value and described predetermined mole growth velocity, also produce related.
In some embodiments, for example, when reaction zone has the feature of at least a assessment purposes growth conditions, described assessment purposes phototroph matter in the reaction zone 10 are grown, the feature of each in the wherein said at least a assessment purposes growth conditions all the represents described production purposes phototroph matter production purposes growth conditions that described reaction zone 10 has when growing in reaction zone 10.In some embodiments, for example, described production purposes growth conditions is any in the multiple production purposes growth conditions, and described multiple production purposes growth conditions comprises: the composition of reaction mixture, reaction zone temperature, reaction zone pH, reaction zone light intensity, reaction zone illumination mode (for example intensity variableization), reaction zone illumination circulation (for example illumination circulation ON/OFF time length) and reaction zone temperature.In some embodiments, for example, provide one or more assessment purposes growth conditionss to promote the production of phototroph matter to reach optimizing, in wherein said one or more assessment purposes growth conditionss each all represents production purposes phototroph matter in the reaction zone 10 when growing, the production purposes growth conditions that production purposes reaction mixture stands.
In one aspect of the method, when described phototroph matter is grown in reaction zone 10 with a maximum mole growth velocity (or comparatively approaching with it), carry out the discharging of phototroph matter with the discharging molar rate that is close with the mole growth velocity of described phototroph matter in reaction zone at least.
Can be placed in the reaction zone 10 for the reaction mixture that under being exposed to photosynthetic effective optical radiation, carries out photosynthetic production purposes reaction mixture form.Described production purposes reaction mixture comprises the phototroph matter that can be used for the production purposes phototroph matter form of growth in reaction zone 10.Described reaction mixture in placing reaction zone 10 is exposed under photosynthetic effective optical radiation and when causing production purposes phototroph matter in the reaction mixture to be grown, the molar rate of in reaction zone 10, growing with described production purposes phototroph matter 10% with interior molar rate from the described production purposes phototroph matter of described reaction zone 10 dischargings.The growth that described production purposes phototroph matter is carried out in reaction zone 10 is to place in the reaction zone 10 and at least 90% the molar rate that is exposed to the maximum growth rate of the production purposes phototroph matter in the reaction mixture under photosynthetic effective optical radiation is carried out.In some embodiments, for example, the mole growth velocity of the discharging molar rate of described production purposes phototroph matter described production purposes phototroph matter in reaction zone 10 5% in.In some embodiments, for example, the mole growth velocity of the discharging molar rate of described production purposes phototroph matter described production purposes phototroph matter in reaction zone 10 1% in.In some embodiments, for example, the growth that described production purposes phototroph matter is carried out in reaction zone 10 is to place in the reaction zone 10 and at least 95% the growth molar rate that is exposed to the maximum growth rate of the production purposes phototroph matter in the reaction mixture under photosynthetic effective optical radiation is carried out, in some embodiments in these embodiments, for example, the discharging molar rate of described production purposes phototroph matter be set at described production purposes phototroph matter in the reaction zone 10 the mole growth velocity 5% with interior (for example 1% in).In some embodiments, for example, the growth that described production purposes phototroph matter is carried out in reaction zone 10 is to place in the reaction zone 10 and at least 99% the growth molar rate that is exposed to the maximum growth rate of the production purposes phototroph matter in the reaction mixture under photosynthetic effective optical radiation is carried out, in some embodiments in these embodiments, for example, the discharging molar rate of described production purposes phototroph matter be set at described production purposes phototroph matter in the reaction zone 10 the mole growth velocity 5% with interior (for example 1% in).
In some embodiments, for example, described production purposes phototroph matter is grown comprise carbonic acid gas to be supplied to described reaction zone 10 and production purposes reaction mixture is exposed under photosynthetic effective optical radiation.In some embodiments, for example, the carbonic acid gas of supplying is to be supplied by the gaseous emissions 18 of gaseous emissions production process 20.In some embodiments, for example, described gaseous emissions production process 20 gives off gaseous emissions 18, and the described gaseous emissions 18 of at least a portion is provided to reaction zone feeding material 22(as reaction zone gaseous emissions feed 24), and described reaction zone feeding material 22 is provided to reaction zone 10, at this moment, the carbonic acid gas of supplying is to be supplied by the gaseous emissions 18 of gaseous emissions production process 20.Thus, in some embodiments, for example, when growing, carbonic acid gas is fed to described reaction zone 10, wherein when the gaseous emissions production process discharged described gaseous emissions, at least a portion was provided to the carbonic acid gas of reaction zone and is supplied by described gaseous emissions.
In some embodiments, for example, described reaction zone 10 is placed in the bioreactor 12, and the substitute mode by being supplied to described reaction zone 10 in response to water-based feeding material 4 is from described bioreactor 12(and described reaction zone 10) give off production purposes phototroph matter.In other words, can be from described bioreactor 12(and described reaction zone 10 to described reaction zone 10 supply water-based feeding materials 4) displace production purposes phototroph matter, make that thus described production purposes phototroph matter is from bioreactor 12(and described reaction zone 10) discharge.In some embodiments, for example, described production purposes phototroph matter product is discharged from bioreactor in the overflow mode.
In some embodiments, for example, described water-based feeding material 4 is provided to reaction zone 10 and from the described production purposes phototroph matter of reaction zone 10 displacements, makes described production purposes phototroph matter discharge from reaction zone 10 thus.In some embodiments in these embodiments, for example, described water-based feeding material 4 does not comprise production purposes phototroph matter in fact.In the other embodiment in these embodiments, for example, described water-based feeding material 4 comprises the production purposes phototroph matter that concentration is lower than the reaction zone concentration of described production purposes phototroph matter.
In some embodiments, for example, with regard to described water-based feeding material 4, described water-based feeding material 4 is with from the form supply of the fluid in the source 6 of water-based feeding material 4.For example, described fluid is by prime mover driven, and described primover for example is pump.In some embodiments, for example, described water-based feeding material comprises additional aqueous substance feed 44.As mentioned above, in some embodiments, for example, the described additional aqueous substance feed 44 of at least a portion is by container 28 supplies.Thus, contain in the embodiment of described additional aqueous substance feed 44 at water-based feeding material 4, described container is as the source 6 of described water-based feeding material 4.
In some embodiments, for example, described water-based feeding material 4 comprises extra-nutrition thing feed 42 and additional aqueous substance feed 44.In some embodiments in these embodiments, for example, described water-based feeding material 4 is provided to the reaction zone feeding material 22 of described reaction zone 10 upstreams.Thus, as mentioned above and with reference to Fig. 2, in some embodiments in these embodiments, described extra-nutrition thing feed 42 and additional aqueous substance feed 44 are provided to reaction zone feeding material 22 by the shower nozzle 40 of reaction zone 10 upstreams.
In some embodiments in these embodiments, for example, and as mentioned above, give off described phototroph matter 58 by the primover that is communicated with reaction zone 10 fluids from reaction zone 10.In some embodiments, for example, as mentioned above, described additional aqueous substance feed 44 is provided to reaction zone 10, thereby makes the reaction mixture in the reaction zone 10 maintain predetermined volume.
In one aspect of the method, the speed discharging phototroph matter that is complementary with the mole growth velocity with reaction zone 10 interior described phototroph matter.In some embodiments, for example, can alleviate the suffered impact of phototroph matter in the reaction zone 10 like this.With regard to some embodiments, for example, control the discharging of described phototroph matter by the supply molar rate of described additional aqueous substance feed 44, this can influence the product that contains phototroph matter 500 in the described bioreactor 12 of bioreactor 12 displacements.For example, discharge the described product 500 that comprises phototroph matter in the overflow mode.In some embodiments in these embodiments, the higher part of the phototroph matter suspension in the reaction zone 10 is from bioreactor 12 overflows (for example described phototroph matter is discharged via the overflow port of bioreactor 12), thereby obtains the described product 500 that contains phototroph matter.In other embodiments, for example, utilize the valve control that places in the runner that links to each other with described bioreactor 12 outlet fluids described by the discharging of product 500.
In some embodiments, for example, discharge described product 500 continuously.In other embodiments, for example, discharge described product termly.In some embodiments, for example, be designed to make the volumetric molar concentration of the biomass in the described product to maintain relatively low concentration the described discharging that contains the product 500 of phototroph matter.Comprise in the embodiment of algae in phototroph matter, with regard to some embodiments, preferably, discharge described product 500 with the degree of the mole growth velocity generation flip-flop that alleviates the algae in the reaction zone 10 with lower volumetric molar concentration.This flip-flop may cause algae to be impacted, thereby causes in the long time yield lower.In some embodiments, when described phototroph matter is algae, when more specifically being scenedesmus obliquus (scenedesmus obliquus), the concentration of this algae can be between every liter 0.5 to 3 gram in the product 500 that contains phototroph matter.The desired concn of the algae product 500 that is discharged is decided on different algae strains, thereby its concentration range changes along with algae strain difference.Thus, in some embodiments, preferably, in reaction zone, keep predetermined water-content to promote the optimal growth of described phototroph matter, also can influence this effect by controlling the supply that replenishes aqueous substance feed 44.
The described product 500 that contains phototroph matter comprises water.In some embodiments, for example, the described product 500 that contains phototroph matter is provided to separator 52, removing the water of at least a portion from the described product 500 that contains phototroph matter, thereby obtain the product that contains phototroph matter 34 of intermediate concentration and the aqueous materials 72(that reclaims is essentially water in some embodiments).In some embodiments, for example, described separator 52 is high speed centrifugation separators 52.Other suitable examples of separator 52 comprise decanting vessel, settling vessel or pond, flocculation plant or flotation unit.In some embodiments, the aqueous materials 72 of recovery is provided to container 28, for example is used for the container for described technology recycling.
In some embodiments, for example, after discharging described product 500 and before it being supplied to described separator 52, the described product 500 that contains phototroph matter is provided to collecting tank 54.Described collecting tank 54 had both played the effect of the snubber between bioreactor 12 and the separator 52, and also played the effect of mixing vessel at collecting tank 54 when a plurality of bioreactors receive different biomass strains.With regard to latter event, the predetermined feature of a cover that the fuel type that the employing basis will be prepared by the mixture of biomass strain or grade design, the mixture of customizable biomass strain.
As mentioned above, container 28 is provided for the source of the additional aqueous substance feed 44 of reaction zone 10, and plays the effect of holding described additional aqueous substance feed 44 before additional aqueous substance feed 44 is provided to reaction zone 10.In some embodiments, owing to containing moisture and the evaporation in drying machine 32 in the end product 36 that contains phototroph matter, can produce moisture loss.The additional aqueous materials that is installed in the container 28 of collecting from described technology can be provided to reaction zone 10, and the aqueous substance feed 44 as a supplement.In some embodiments, for example, described additional aqueous substance feed 44 is provided to reaction zone 10 by pump 281.In other embodiments, allow if implement the processing unit configuration of the system of described technology, can carry out described supply by gravity.As mentioned above, the additional aqueous materials of collecting from described technology comprises at least a following: (a) before reaction zone feeding material 22 is provided to reaction zone 10 during with its condensation, and the aqueous materials 70 that condensation goes out from described reaction zone feeding material 22; And (b) isolated aqueous materials 72 from the product 500 that contains phototroph matter.In some embodiments, for example, described additional aqueous substance feed 44 is provided to reaction zone 10 to replace described product 500 from reaction zone.In some embodiments, for example, described product 500 cements out from bioreactor 12 in the overflow mode.In some embodiments, for example, described additional aqueous substance feed 44 is provided to reaction zone 10, thereby places the reaction mixture in the reaction zone to make the phototroph matter in the reaction zone reach required predetermined concentration by dilution.
As mentioned above, can be used as container 28(and can hold the aqueous materials of collecting from described technology) the example of concrete structure including, but not limited to basin, pond, groove, canal, pond, pipe, pipeline, channel and water channel.
In some embodiments, for example, when gaseous emissions production process 20 gives off described gaseous emissions 18 and described reaction zone when being provided to described reaction zone feeding material 22 with gaseous emissions feed 24, implement described additional aqueous substance feed 44 to the supply of reaction zone 10.In some embodiments, for example, when implementing described additional aqueous substance feed to the supply of reaction zone 10, will place the phototroph matter that is rich in carbonic acid gas in the aqueous medium to be exposed under photosynthetic effective optical radiation.
In some embodiments, for example, based on detecting the predetermined target value that phototroph matter growth indexes value departs from described processing parameter, regulate and replenish aqueous substance feed 44 to the supply of reaction zone 10, the predetermined target value of wherein said phototroph matter growth indexes is based on the predetermined mole growth velocity of phototroph matter in the described reaction zone.Described phototroph matter growth indexes departs from the detection of phototroph matter growth indexes target value and the adjusting described additional aqueous substance feed 44 done to the supply of reaction zone 10 in response to described detection has been described in above.
In some embodiments, for example, described additional aqueous substance feed 44 depends on the volumetric molar concentration of phototroph matter to the supply of reaction zone 10.Thus, come the volumetric molar concentration of the phototroph matter in the detection reaction district 10 or the volumetric molar concentration index of the phototroph matter in the reaction zone 10 by cell counter (for example above-mentioned cell counter).The actual measurement volumetric molar concentration index of the actual measurement volumetric molar concentration of described phototroph matter or described phototroph matter is transferred to controller, when described controller confirmed that described actual measurement volumetric molar concentration surpasses the high value of predetermined volumetric molar concentration, described controller was supplied molar rate and is responded by starting described additional aqueous substance feed 44 to the supply of reactor 10 or increasing it.In some embodiments, for example, start described additional aqueous substance feed 44 to the supply of reactor 10 or increase its supply molar rate comprise driving primover, for example pump 281, with start described additional aqueous substance feed 44 to the supply of reactor 10 or increase its supply molar rate.In some embodiments, for example, implement described additional aqueous substance feed 44 to the supply of reactor 10 or increase its supply molar rate to comprise and make opening from container 28 to reaction zone that be configured to disturb described additional aqueous substance feed 44 valves of 10 supplies from open or described opening is increased.
In some embodiments, for example, when the last liquid level of reaction zone 10 contents in the described bioreactor 12 becomes when being lower than predetermined minimum liquid level, start that described additional aqueous substance feed 44(reclaimed from described technology) to the supply of reactor 10 or increase its supply molar rate.In some embodiments in these embodiments, for example, liquid level sensor 76 is provided, and with the position for detection of the last liquid level of reaction zone 10 contents in the described bioreactor, and the signal that will represent the last liquid level of described reaction zone 10 contents is transferred to controller.The reception signal of liquid level compares with predetermined low level value and when confirming in the actual measurement of described reaction zone content that liquid level is lower than described predetermined low level value, described controller starts the supply of described additional aqueous substance feed 44 or increases its supply molar rate on described controller will be from representative reaction zone 10 contents of liquid level sensor 76.When by pump 281 described additional aqueous substance feed 44 being supplied to reaction zone 10, described controller drives described pump 281, thereby starts described additional aqueous substance feed 44 to the supply of reaction zone 10 or increase its delivery rate.When realizing described additional aqueous substance feed 44 to the supply of reaction zone 10 by gravity, described controller drives the opening of valve, thereby starts described additional aqueous substance feed 44 to the supply of reaction zone 10 or increase its supply molar rate.For example, to the control of the position of liquid level on reaction zone 10 contents and those from the operation of carrying out some embodiments the embodiment of the discharging of phototroph matter 58 in the reaction zone 10 than lower part of reaction zone 10 (for example, as indicated above, when by primover of being communicated with reaction zone 10 fluids during from the described phototroph matter 58 of described reaction zone 10 dischargings) relevant.For the embodiment of discharging described phototroph matter 58 by overflow from reaction zone 10, in some embodiments in these embodiments, relevant with the operating process in " sowing time " of described bioreactor 12 to the control of the position of liquid level on reaction zone 10 contents.
In some embodiments, for example, when the valve in utilization places the runner that is communicated with the outlet fluid of bioreactor 12 is controlled the discharging of described product 500, can be by cell counter 47(above-mentioned cell counter for example) come the volumetric molar concentration of phototroph matter in the detection reaction district.The actual measurement volumetric molar concentration of described phototroph matter is transferred to controller, when described controller confirms that described measured light health material volumetric molar concentration surpasses the high value of the predetermined volumetric molar concentration of described phototroph matter, described controller responds by the opening that makes valve open or increase described valve, and the molar rate that makes described product 500 discharge from reaction zone 10 increases.
In some embodiments, for example, provide extra make up water source 68 to alleviate the situation that described additional aqueous substance feed 44 is not enough to remedy the moisture loss during the technological operation.Thus, in some embodiments, for example, described additional aqueous substance feed 44 mixes mutually with reaction zone feeding material 22 in shower nozzle 40.On the contrary, in some embodiments, for example, the facility that is provided for 66 dischargings to the waterways of described container 28 surpasses the situation of replenishing aequum to alleviate the aqueous materials that reclaims from described technology.
In some embodiments, for example, from described reaction zone 10 discharging reaction zone gaseous exhaust products 80.Reclaim the described reaction zone gaseous exhaust of at least a portion product 80 and it is supplied to the reaction zone 110 of combustion processes operating unit 100.As carrying out photosynthetic result in the reaction zone 10, with respect to described reaction zone gaseous emissions feed 24, described reaction zone gaseous exhaust product 80 is rich in oxygen.The combustion zone 110(that described gaseous exhaust product 80 is provided to process of combustion operating unit 100 for example places the combustion zone 110 in the retort), thereby play the effect of effecting reaction thing in its combustion processes that can in process of combustion operating unit 100, carry out.Combustiblematerials (for example carbonaceous material) in the described reaction zone gaseous exhaust product 80 catalytic combustion districts 100 also reacts, thereby makes described combustiblematerials burning.The example of suitable process of combustion operating unit 100 comprises those that adopt in fossil fired power plant, industrial burning facility, industrial furnace, industrial well heater, oil engine and the cement kiln.
In some embodiments, for example, when the gaseous emissions production process 20 described gaseous emissions 18 of discharging and described reaction zone are provided to reaction zone feeding material 22 with gaseous emissions feed 24, make the reaction zone gaseous exhaust product 80 of described recovery contact combustiblematerialss.In some embodiments, for example, when described reaction zone is provided to reaction zone feeding material 22 with gaseous emissions feed 24, make the reaction zone gaseous exhaust product contact combustiblematerials of described recovery.In some embodiments, for example, when described reaction zone feeding material is provided to reaction zone, make the reaction zone gaseous exhaust product contact combustiblematerials of described recovery.In some embodiments, for example, when the reaction zone gaseous exhaust product of described recovery contacts combustiblematerials, the phototroph matter that is rich in carbonic acid gas that places in the aqueous medium is exposed under photosynthetic effective optical radiation.
The product 34 that contains the phototroph matter of intermediate concentration is provided to drying machine 32, thereby described drying machine 32 provides the water in the product 34 of the described phototroph matter that contains intermediate concentration of heat evaporation at least a portion for the described product 34 that contains the phototroph matter of intermediate concentration, obtains containing the end product 36 of phototroph matter thus.As mentioned above, in some embodiments, the heat of product 34 that supply contains the phototroph matter of intermediate concentration is provided by heat-transfer medium 30, and described heat-transfer medium 30 has been used to before reaction zone feeding material 22 is provided to reaction zone 10 described reaction zone feeding material 22 be cooled off.By carrying out this cooling, heat is passed to heat-transfer medium 30 from described reaction zone feeding material 22, thereby the temperature of described heat-transfer medium 30 is raise.In this type of embodiment, the described product 34 that contains the phototroph matter of intermediate concentration is in relatively warm temperature, and not many from the heat that product 34 transpiring moistures of the described phototroph matter that contains intermediate concentration are required, thereby to use heat-transfer medium 30 to come the dry described product 34 that contains the phototroph matter of intermediate concentration as thermal source be feasible.As mentioned above, after the product 34 of the described phototroph matter that contains intermediate concentration of heating, some energy have been lost thereby the heat-transfer medium 30 that is in lesser temps that becomes is recycled to interchanger 26, to cool off described reaction zone feeding material 22.Described drying machine 32 required heats are decided according to the delivery rate of the product 34 of the phototroph matter that contains intermediate concentration that is supplied to drying machine 32.Adjust cooling requirement (described interchanger 26) and demand for heat (described drying machine 32) by controller, so that the flow rate by monitoring reaction zone feeding material 22 and temperature and come these two kinds of operations of balance by the throughput rate of the product 500 resulting products 500 of bioreactor discharge.
In some embodiments, when changing, the delivery rate of reaction zone feeding material 22 beginning to experience significant time-delay (for example in some cases for above three (3) hours from described reaction zone with gaseous emissions feed 24, sometimes in addition be the longer time) afterwards, realized being changed and the change of the phototroph matter growth velocity that causes to the delivery rate of reaction zone feeding material 22 with gaseous emissions feed 24 by described reaction zone.Comparatively speaking, change and the calorific value of the described heat-transfer medium 30 that causes changes and can realize quickly to the delivery rate of reaction zone feeding material 22 with gaseous emissions feed 24 based on described reaction zone.Thus, in some embodiments, thermal buffer is provided, be used for storing any excessive heat energy (be the form of heat-transfer medium 30), and is producing one section time-delay of response introducing at reaction zone aspect the heat transfer performance with the variation of gaseous emissions feed 24 for described drying machine 32.In some embodiments, for example, described thermal buffer is the heat-transfer medium storagetank.Perhaps, described reaction zone is being supplied in the transitional period of reaction zone feeding material 22 with gaseous emissions feed 24, can providing external heat source to replenish the required heat energy of described drying machine 32.In order to adapt to the variation of described phototroph matter growth velocity, perhaps for the startup that adapts to described technology or close, may need to use thermal buffer or extra heat.For example, if the growth of described phototroph matter reduces or stops, described drying machine 32 can be stored in heat energy in the snubber by use and remain in operation depletedly until it, perhaps, in some embodiments, uses second thermal source.
Further describe other embodiments now with reference to following non-limiting examples.
Embodiment 1
A predictive embodiment will be described now, it illustrates such embodiment: the target value of determining phototroph matter growth indexes (for example concentration of algae in the reaction zone of bioreactor), and the operation of carrying out implementation of processes scheme mentioned above, comprise according to the deviation between described parameter measure value and the target value and regulate the molar rate that contains the product of phototroph matter from the reaction zone discharging.
At first, in the reaction zone of bioreactor, provide and be in algae in the aqueous medium, that contain the initial concentration of proper nutrition thing.Gaseous carbon dioxide is supplied to reaction zone, and described reaction zone is exposed in the light that light source (for example LED) sends, so that described algae grows.When the concentration of algae in the reaction zone reaches every liter 0.5 when gram, water is introduced in the reaction zone of described bioreactor, in order to collect described algae by the overflow of reactor content, and the initial target concentration of algae is set in every liter 0.5 gram.At first, introduce described supply water with moderate and constant relatively speed, thereby make described bioreactor have the volume of half (1/2) to change every day, but help the growth of described algae and reach target value within a short period of time with the water yield that fresh water is changed in the reaction zone termly because found.If the growth velocity of described algae is lower than dilution rate and any moment during measurement operation records concentration of algae with respect to concentration of algae setting point decline at least 2%, described Controlling System will stop or reducing dilution rate, to avoid the concentration of algae in the described reaction zone further thinning.If the growth velocity of described algae is higher than dilution rate, then concentration of algae can raise and surpass initial concentration of algae setting point, and described Controlling System will improve the concentration of algae setting point so that it is synchronous with the concentration of algae that increases, and keeps identical dilution rate simultaneously.For example, concentration of algae may be increased to every liter 0.52 gram, and described Controlling System will make the concentration of algae setting point be increased to 0.51 this moment.Described Controlling System continues the increase of monitoring concentration of algae, improves the target concentration of algae simultaneously.When the growth velocity that records described algae reaches the variation of maximum, the target concentration of algae is locked as currency, thereby make it become target value, regulate dilution rate then, thereby when concentration of algae is target value, collect described algae with the speed identical with algae growth velocity in the bioreactor.
The algae growth velocity is corresponding with concentration of algae.When recording the algae growth velocity and take place significantly to change, the described algae in the expression reaction zone just grows with (or close to) its maximum rate, and described growth velocity is corresponding to the concentration of algae of target value.Thus, by the control dilution rate concentration of algae in the reaction zone is maintained described target value, the growth of described algae is maintained (or close to) maximum value, its result must be the drainage rate optimizing that makes described algae along with the prolongation of time.
In order to help the complete understanding to content of the present invention, many details have been mentioned in the above-mentioned explanation that is used for task of explanation.Yet, it will be apparent to one skilled in the art that these concrete details are also nonessential for implementing the present invention.Though described some size and material at the enforcement of described exemplary, also can use other size and/or materials that are fit within the scope of the present invention.All these adjustment and variation, comprise all technically suitable at present and suitable variation in the future, all should be considered to be in the field of the invention and the scope.Intactly incorporate all mentioned reference in this mode by reference.
Claims (according to the modification of the 19th of treaty)
1. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, and described method comprises:
Described reaction mixture is being exposed under photosynthetic effective optical radiation and is causing described phototroph matter in described reaction zone, to be grown, and in described reaction zone discharging phototroph matter, when phototroph matter growth indexes is different from phototroph matter growth indexes target value, adjusting is from the speed of described reaction zone discharging phototroph matter, the growth that wherein causes comprises the growth that causes by photosynthesis, and wherein said phototroph matter growth indexes target value is to be placed in the described reaction zone and the predetermined growth velocity that is exposed to the described phototroph matter in the described reaction mixture under photosynthetic effective optical radiation is the basis.
2. method according to claim 1 wherein, makes described phototroph matter growth indexes target value be associated with the predetermined growth velocity of described phototroph matter.
3. method according to claim 1, wherein, described adjusting is in response to detect to there are differences between described phototroph matter growth indexes and the described phototroph matter growth indexes target value and implements.
4. method according to claim 3 further comprises and detects phototroph matter growth indexes so that measured light health material growth indexes to be provided.
5. method according to claim 4, wherein, described measured light health material growth indexes represents the concentration of the described phototroph matter in the described reaction mixture.
6. method according to claim 4, wherein, described measured light health material growth indexes is the concentration of the described phototroph matter in the described reaction mixture.
7. method according to claim 4, wherein, described measured light health material growth indexes is the concentration of the phototroph matter in the reaction zone product of described reaction zone discharging, wherein said reaction zone product also contains water.
8. method according to claim 1, wherein, described phototroph matter growth indexes target value is scheduled to.
9. method according to claim 1, wherein, the growth of the described phototroph matter that causes is to carry out with interior growth velocity with 10% of described predetermined growth velocity.
10. method according to claim 1, wherein, the growth of the described phototroph matter that causes is to carry out with interior growth velocity with 5% of described predetermined growth velocity.
11. method according to claim 1, wherein, the growth of the described phototroph matter that causes is to carry out with interior growth velocity with 1% of described predetermined growth velocity.
12. method according to claim 1, wherein, described reaction zone is placed in the bioreactor, and the phototroph matter of wherein discharging is contained in the overflow of described bioreactor discharge, and described overflow is by producing water-based feeding material supply to described reaction zone.
13. method according to claim 12 wherein, implements described reaction zone is discharged the adjusting of the speed of phototroph matter by regulating described water-based feeding material to the delivery rate of described reaction zone.
14. method according to claim 4, wherein, when measured light health material growth indexes was lower than described phototroph matter growth indexes target value, described adjusting comprises reduced the speed of described reaction zone discharging phototroph matter.
15. method according to claim 14, wherein, described reaction zone is placed in the bioreactor, and the phototroph matter of wherein discharging is contained in the overflow of described bioreactor discharge, and described overflow is by producing water-based feeding material supply to described reaction zone.
16. method according to claim 15, wherein, described adjusting is by making described water-based feeding material reduce to implement to the delivery rate of described reaction zone.
17. method according to claim 1, wherein, when described phototroph matter growth indexes during greater than described phototroph matter growth indexes target value, described adjusting comprises increases the speed of described reaction zone discharging phototroph matter.
18. method according to claim 17, wherein, described reaction zone is placed in the bioreactor, and the phototroph matter of wherein discharging is contained in the overflow of described bioreactor discharge, and described overflow is by producing water-based feeding material supply to described reaction zone.
19. method according to claim 18, wherein, described adjusting is by described water-based feeding material is implemented to the delivery rate increase of described reaction zone.
20. method according to claim 12, wherein, described water-based feeding material does not contain phototroph matter in fact.
21. method according to claim 1 wherein, grows described phototroph matter to comprise carbonic acid gas to be supplied to described reaction zone and described production purposes reaction mixture is exposed under photosynthetic effective optical radiation.
22. method according to claim 21 wherein, is supplied described carbonic acid gas when growing.
23. method according to claim 22, wherein, at least a portion that is provided to the described carbonic acid gas of described reaction zone is supplied by described gaseous emissions when gaseous emissions production process discharging gaseous emissions.
24. method according to claim 1, wherein, described reaction mixture also contains water and carbonic acid gas.
25. method according to claim 1, wherein, the predetermined growth velocity of described production purposes phototroph matter be placed in the described reaction zone and be exposed to the described production purposes phototroph matter in the described reaction mixture under described photosynthetic effective optical radiation maximum growth rate at least 90%.
26. the method for a growth production purposes phototroph matter in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic production purposes reaction mixture under photosynthetic effective optical radiation, wherein said production purposes reaction mixture comprises can be for the production purposes phototroph matter of growing in described reaction zone, and described method comprises:
Described reaction mixture is being exposed under photosynthetic effective optical radiation and is causing described production purposes phototroph matter in described reaction zone, to be grown, and in described reaction zone discharging production purposes phototroph matter, when phototroph matter growth indexes is different from predetermined phototroph matter growth indexes target value, adjusting is from the speed of described reaction zone discharging production purposes phototroph matter, the growth that wherein causes comprises the growth that causes by photosynthesis, and wherein said phototroph matter growth indexes target value is to be placed in the described reaction zone and the predetermined growth velocity that is exposed to the described production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation is the basis;
Being predetermined to include of wherein said target value:
The described production purposes reaction mixture of supply representative and can be used for carrying out photosynthetic assessment purposes reaction mixture under photosynthetic effective optical radiation being exposed to makes the phototroph matter in the described assessment purposes reaction mixture become the assessment purposes phototroph matter of the described production purposes phototroph matter of representative;
When the described assessment purposes reaction mixture in placing described reaction zone is exposed under photosynthetic effective optical radiation and causes described assessment purposes phototroph matter in described assessment purposes reaction mixture to be grown, at least termly detect phototroph matter growth indexes, so that a plurality of detected values that are detected the described phototroph matter growth indexes of for some time to be provided; And
Calculate the growth velocity of described assessment purposes phototroph matter according to a plurality of detected values of described phototroph matter growth indexes, determine a plurality of growth velocitys of described assessment purposes phototroph matter in described period thus;
Based on the growth velocity of calculating and the detected value that is used for the described phototroph matter growth indexes of the described growth velocity of calculating, set up the growth velocity of described assessment purposes phototroph matter and the relation between the described phototroph matter growth indexes, make the relation of setting up between the growth velocity of described assessment purposes phototroph matter and the described phototroph matter growth indexes represent the growth velocity and the relation between the described phototroph matter growth indexes of the described production purposes phototroph matter in the described reaction zone, establish the growth velocity of the interior described production purposes phototroph matter of described reaction zone and the relation between the described phototroph matter growth indexes thus;
Select the predetermined growth velocity of described production purposes phototroph matter; And
Described phototroph matter growth indexes target value is defined as: according to the relation of establishing between the growth velocity of the described production purposes phototroph matter in the described reaction zone and the described phototroph matter growth indexes, phototroph matter growth indexes when causing described predetermined growth velocity, make thus between described phototroph matter growth indexes target value and described predetermined growth velocity, also produce related.
27. method according to claim 26, wherein, when described reaction zone has the feature of at least a assessment purposes growth conditions, make described assessment purposes phototroph matter carry out described growth, the feature of each in the wherein said at least a assessment purposes growth conditions all the represents described production purposes phototroph matter production purposes growth conditions that described reaction zone has when growing in described reaction zone.
28. method according to claim 27, wherein, described production purposes growth conditions is any in the multiple production purposes growth conditions, and described multiple production purposes growth conditions comprises: reaction zone composition, reaction zone temperature, reaction zone pH, reaction zone light intensity, reaction zone illumination mode, reaction zone illumination circulation and reaction zone temperature.
29. method according to claim 26, wherein, the predetermined growth velocity of described production purposes phototroph matter be placed in the described reaction zone and be exposed to the described production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation maximum growth rate at least 90%.
30. method according to claim 26, wherein, the predetermined growth velocity of described production purposes phototroph matter be placed in the described reaction zone and be exposed to the described production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation maximum growth rate at least 99%.
31. method according to claim 26, wherein, described production purposes reaction mixture also contains water and carbonic acid gas; And wherein said assessment purposes reaction mixture also contains water and carbonic acid gas.
32. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, and described method comprises:
When the described reaction mixture in will placing described reaction zone was exposed under photosynthetic effective optical radiation and causes described phototroph matter growth in the described reaction mixture, 10% of the speed of growing in described reaction zone with described phototroph matter was discharged described phototroph matter with interior speed from described reaction zone;
The growth that wherein said phototroph matter is carried out in described reaction zone is to be placed in the described reaction zone and at least 90% the speed that is exposed to the maximum growth rate of the described phototroph matter in the described reaction mixture under photosynthetic effective optical radiation is carried out.
33. method according to claim 32, wherein, described reaction zone is placed in the bioreactor, and the phototroph matter of wherein discharging is contained in the overflow of described bioreactor discharge.
34. method according to claim 32, wherein, the growth of described production purposes phototroph matter comprises and carbonic acid gas is supplied to described reaction zone and described production purposes reaction mixture is exposed under photosynthetic effective optical radiation.
35. method according to claim 32, wherein, the described growth of the described phototroph matter in the described reaction zone is to be placed in the described reaction zone and at least 95% the speed that is exposed to the maximum growth rate of the described phototroph matter in the described reaction mixture under photosynthetic effective optical radiation is carried out.
36. method according to claim 32, wherein, the described growth of the described phototroph matter in the described reaction zone is to be placed in the described reaction zone and at least 99% the speed that is exposed to the maximum growth rate of the described phototroph matter in the described reaction mixture under photosynthetic effective optical radiation is carried out.
37. method according to claim 32, wherein, 5% of the speed of growing with the described phototroph matter that places in the described reaction zone is discharged described phototroph matter with interior speed from described reaction zone.
38. method according to claim 32, wherein, 1% of the speed of growing with the described phototroph matter that places in the described reaction zone is discharged described phototroph matter with interior speed from described reaction zone.
39. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, and described method comprises:
When described reaction mixture being exposed under photosynthetic effective optical radiation and causing placing described phototroph matter in the described reaction mixture of described reaction zone to be grown, from described reaction zone discharging phototroph matter, make described phototroph matter drainage rate speed that described phototroph matter is grown 10% in, the growth of the described phototroph matter that wherein causes comprises the growth that causes by photosynthesis.
40. according to the described method of claim 39, wherein, the drainage rate of described phototroph matter speed that described phototroph matter is grown 5% in.
41. according to the described method of claim 39, wherein, the drainage rate of described phototroph matter speed that described phototroph matter is grown 1% in.
42. according to the described method of claim 39, wherein, the drainage rate of described phototroph matter equals the speed that described phototroph matter is grown.
43. according to the described method of claim 39, wherein, the speed that described phototroph matter is grown equals to be placed in the described reaction zone and is exposed to the maximum growth rate of the described phototroph matter in the described reaction mixture under photosynthetic effective optical radiation.
44. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
At gaseous emissions production process discharging gaseous emissions, wherein any described gaseous emissions defined reaction district that is provided to described reaction zone with the gaseous emissions feed in, based on the detection of at least a carbon dioxide treatment figureofmerit being regulated described reaction zone with the supply of gaseous emissions feed to described reaction zone.
45. according to the described method of claim 44, wherein, in described reaction zone, carry out at least one the detection in the described at least a carbon dioxide treatment figureofmerit.
46. according to the described method of claim 44, comprise that further the part branch of the gaseous emissions that adjusting is discharged flows to the supply of another operating unit, the part branch current limit shunting gaseous emissions of the described gaseous emissions of another operating unit of supply that wherein discharges.
47. according to the described method of claim 46, wherein, when described reaction zone is regulated to the supply of described reaction zone with the gaseous emissions feed, the described shunting gaseous emissions of supplying with described another operating unit is regulated.
48. according to the described method of claim 46, wherein, reduce it to the impact of environment thereby described another operating unit transforms described shunting gaseous emissions.
49. according to the described method of claim 48, wherein, described another operating unit is the separator that can remove carbonic acid gas from described shunting gaseous emissions.
50. according to the described method of claim 48, wherein, described another operating unit is chimney.
51. according to the described method of claim 44, wherein, the carbon dioxide treatment figureofmerit that detects is any feature of capacity of the described reaction zone of representative, and the capacity of wherein said reaction zone is that the capacity that transforms takes place for photosynthetic response that the described phototroph matter of carbonic acid gas in placing described reaction zone that described reaction zone will receive carbonic acid gas and at least a portion is received is carried out.
52. according to the described method of claim 44, wherein, the carbon dioxide treatment figureofmerit that detects is any feature of described method of the capacity of the described reaction zone of representative, the capacity of wherein said reaction zone is that the capacity that transforms takes place for photosynthetic response that described reaction zone will receive carbonic acid gas and the described phototroph matter in the described reaction mixture of carbonic acid gas in placing described reaction zone that at least a portion receives is carried out, thereby makes described photosynthesis realize the predetermined growth velocity of the described phototroph matter in the described reaction zone.
53. according to the described method of claim 44, wherein, the carbon dioxide treatment figureofmerit that detects is any feature of described method of the capacity of the described reaction zone of representative, the capacity of wherein said reaction zone is that the capacity that transforms takes place for photosynthetic response that the described phototroph matter of carbonic acid gas in placing described reaction zone that described reaction zone will receive carbonic acid gas and at least a portion is received is carried out, thereby makes any carbonic acid gas from described reaction zone discharging all be lower than acceptable molar rate.
54. according to the described method of claim 44, wherein, the carbon dioxide treatment figureofmerit that detects is at least a in the concentration of pH and phototroph matter.
55. according to the described method of claim 44, wherein, discharge described gaseous emissions at described gaseous emissions production process, the any described gaseous emissions defined reaction district that wherein is provided to described reaction zone is with the gaseous emissions feed time, when detected carbon dioxide treatment figureofmerit in described reaction zone represented described reaction zone and will receive the such capacity of carbonic acid gas supply that molar rate increases, the adjusting that described reaction zone is done to the supply of described reaction zone with the gaseous emissions feed comprised: start described reaction zone usefulness gaseous emissions feed to the supply of described reaction zone, or have additional supply of to the supply molar rate of the described reaction zone usefulness gaseous emissions feed of described reaction zone.
56. according to the described method of claim 55, further comprise: arrange when will shunt gaseous emissions and be supplied to described another operating unit and described shunting gaseous emissions and be provided to described another operating unit in that described gaseous emissions production process and another operating unit are collaborative, the supply molar rate of the described shunting gaseous emissions that is provided to described another operating unit is reduced or make described supply termination.
57. according to the described method of claim 44, wherein, at described gaseous emissions production process discharging gaseous emissions, and the described gaseous emissions of at least a portion is provided to described reaction zone, the described at least a portion gaseous emissions defined reaction district that wherein is provided to described reaction zone is with the gaseous emissions feed time, when detected carbon dioxide treatment figureofmerit in described reaction zone represented described reaction zone and will receive the such capacity of carbonic acid gas supply that molar rate reduces, the adjusting that described reaction zone is done to the supply of described reaction zone with the gaseous emissions feed comprised: the supply molar rate that reduces the described reaction zone usefulness gaseous emissions feed that is provided to described reaction zone, or stop its supply.
58. according to the described method of claim 57, wherein, arrange to shunt under the situation that gaseous emissions is supplied to described another operating unit in that described gaseous emissions production process and another operating unit are collaborative, described method further comprises: start described shunting gaseous emissions to the supply of described another operating unit, or increase the supply molar rate of the described shunting gaseous emissions that is provided to described another operating unit.
59. according to the described method of claim 44, wherein, when detected carbon dioxide treatment figureofmerit in described reaction zone represents described reaction zone and will receive the such capacity of carbonic acid gas supply that molar rate reduces, represent described reaction zone in response to the carbon dioxide treatment figureofmerit that detects and to receive the such capacity of carbonic acid gas supply that molar rate reduces, the adjusting that described reaction zone is done with the gaseous emissions feed comprises the supply molar rate that reduces the described reaction zone usefulness gaseous emissions feed that is provided to described reaction zone, or stop its supply, in this case, described method further comprises: startup contains the raw material of make-up gas to the supply of described reaction zone, or increases the supply of raw material molar rate that contains make-up gas that is provided to described reaction zone.
60. according to the described method of claim 59, wherein, if there is carbonic acid gas, then the volumetric molar concentration of its carbonic acid gas is lower than the carbonic acid gas volumetric molar concentration that is supplied to described at least a portion gaseous emissions of described reaction zone from described gaseous emissions production process in the described raw material that contains make-up gas.
61. according to the described method of claim 60, wherein, make the described reaction zone that is provided to described reaction zone reduce with the mole delivery rate of gaseous emissions feed or make its supply stop and contain the raw material of make-up gas to be provided to that the supply molar rate of the carbonic acid gas of described reaction zone reduces or make it supply termination be crew-served to described reaction zone supply is described to the supply of described reaction zone with the gaseous emissions feed by regulating described reaction zone.
62. according to the described method of claim 59, wherein, start the described raw material that contains make-up gas to the supply of described reaction zone or increase that the described supply of raw material molar rate that contains make-up gas that is provided to described reaction zone has compensated at least in part because the described reaction zone that is provided to described reaction zone reduces with the supply molar rate of gaseous emissions feed or it supplies the reduction of mole delivery rate of the material that is provided to described reaction zone that termination causes or the termination of described raw material supply.
63. according to the described method of claim 62, wherein, below (a) and combination (b): (a) reduce described reaction zone with the gaseous emissions feed to the supply molar rate of described reaction zone or stop its supply; And (b) start the described raw material that contains make-up gas to the supply of described reaction zone or increase its supply molar rate, alleviated because the degree that the described reaction zone that is provided to described reaction zone dies down with stirring in the described reaction zone that the supply molar rate reduces or its supply termination causes of gaseous emissions feed.
64. according to the described method of claim 63, wherein, the described raw material that contains make-up gas and any described reaction zone are provided to described reaction zone with the combination of gaseous emissions feed as at least a portion of reaction zone feeding material, and described reaction zone feeding material supply produced agitaion to described reaction zone and to the material in the described reaction zone, thereby make that the volumetric molar concentration difference of any phototroph matter is lower than 20% in the described reaction zone at 2.
65. according to the described method of claim 44, wherein, when described reaction zone is regulated to the supply of described reaction zone with the gaseous emissions feed, will place the described reaction mixture in the described reaction zone to be exposed under photosynthetic effective optical radiation.
66. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
At gaseous emissions production process discharging gaseous emissions, and the described gaseous emissions of at least a portion is provided to described reaction zone, the described at least a portion gaseous emissions defined reaction district that wherein is provided to described reaction zone is with the gaseous emissions feed time, be provided to the supply molar rate of the described reaction zone usefulness gaseous emissions feed of described reaction zone in reduction, or when stopping described reaction zone with the supply of gaseous emissions feed, described method further comprises: startup contains the raw material of make-up gas to the supply of described reaction zone, perhaps increases the supply of raw material molar rate that contains make-up gas to described reaction zone supply.
67. according to the described method of claim 66, wherein, the described startup raw material that contains make-up gas is to the supply of described reaction zone or increase the supply of raw material molar rate that contains make-up gas that is provided to described reaction zone and be in response to and detect that the reaction zone that is provided to reaction zone reduces with the supply molar rate of gaseous emissions feed or its supply termination or detect the reaction zone that is provided to reaction zone and have the indication of reduction or its indication that is supplied with termination to implement with the supply molar rate of gaseous emissions feed.
68. according to the described method of claim 67, wherein, if there is carbonic acid gas, then the volumetric molar concentration of its carbonic acid gas is lower than the carbonic acid gas volumetric molar concentration that is supplied to described at least a portion gaseous emissions of described reaction zone from described gaseous emissions production process in the described raw material that contains make-up gas.
69. according to the described method of claim 68, wherein, make the described reaction zone that is provided to described reaction zone reduce with the mole delivery rate of gaseous emissions feed or make its supply stop and contain the raw material of make-up gas to be provided to that the supply molar rate of the carbonic acid gas of described reaction zone reduces or make it supply termination be crew-served to described reaction zone supply is described to the supply of described reaction zone with the gaseous emissions feed by regulating described reaction zone.
70. according to the described method of claim 66, wherein, start the described raw material that contains make-up gas to the supply of described reaction zone or increase that the described supply of raw material molar rate that contains make-up gas that is provided to described reaction zone has compensated at least in part because the described reaction zone that is provided to described reaction zone reduces with the supply molar rate of gaseous emissions feed or it supplies the reduction of mole delivery rate of the material that is provided to described reaction zone that termination causes or the termination of described raw material supply.
71. according to the described method of claim 70, wherein, below (a) and combination (b): (a) reduce described reaction zone with the gaseous emissions feed to the supply molar rate of described reaction zone or stop its supply; And (b) start the described raw material that contains make-up gas to the supply of described reaction zone or increase its supply molar rate, alleviated because the degree that the described reaction zone that is provided to described reaction zone dies down with stirring in the described reaction zone that the supply molar rate reduces or its supply termination causes of gaseous emissions feed.
72. according to the described method of claim 70, wherein, the described raw material that contains make-up gas and any described reaction zone are provided to described reaction zone with the combination of gaseous emissions feed as at least a portion of reaction zone feeding material, and described reaction zone feeding material supply produced agitaion to described reaction zone and to the material in the described reaction zone, thereby make that the concentration difference of any phototroph matter is lower than 20% in the described reaction zone at 2.
73. according to the described method of claim 66, wherein, the raw material that contains make-up gas when startup will place the described reaction mixture in the described reaction zone to be exposed under photosynthetic effective optical radiation to the supply of described reaction zone or when increasing the described supply of raw material molar rate that contains make-up gas.
74. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
Described reaction zone is supplied to reaction zone with the gaseous emissions feed, at least a portion defined reaction district gaseous emissions feed of the gaseous emissions that produces of gaseous emissions production process wherein, wherein said reaction zone comprises carbonic acid gas with the gaseous emissions feed; And
Replenish the aqueous substance feed from container to described reaction zone supply, wherein said additional aqueous substance feed comprises from described reaction zone with condensation the gaseous emissions feed and be collected in aqueous materials in the described container, and the condensation of wherein said aqueous materials is to realize when cooling off before described reaction zone is provided to described reaction zone with the gaseous emissions feed.
75. according to the described method of claim 74, wherein, the aqueous materials that is condensed is water.
76. according to the described method of claim 74, wherein, described additional aqueous substance feed further comprises aqueous materials.
77. according to the described method of claim 74, wherein, described reaction zone is to be lower than 50 ℃ temperature from being cooled to greater than 110 ℃ temperature with the cooling of gaseous emissions feed.
78. according to the described method of claim 77, wherein, in interchanger, carry out the cooling that described reaction zone is used the gaseous emissions feed.
79. according to the described method of claim 78, wherein, described condensation produces and is fed into the heat passage of heat-transfer medium from described reaction zone with gaseous emissions, thereby produce the heat-transfer medium that is heated, and the described heat-transfer medium that is heated is supplied to drying machine to evaporate moisture from the phototroph matter of described reaction zone discharging.
80. according to the described method of claim 79, wherein, described evaporation is to carry out heat passage the realization by the described biomass product in from the described heat-transfer medium that is heated to described drying machine, thereby produce the heat-transfer medium of cooling, and the heat-transfer medium of described cooling is recycled to described interchanger to carry out described condensation.
81. according to the described method of claim 74, wherein, when described reaction zone is provided to described reaction zone with the gaseous emissions feed, carry out the supply of described additional aqueous materials.
82. 1 described method wherein, when described gaseous emissions production process produces described reaction zone with the gaseous emissions feed, is carried out the supply of described additional aqueous materials according to Claim 8.
83. 2 described methods wherein, when carrying out the supply of described additional aqueous materials, will place the described reaction zone mixture in the described reaction zone to be exposed under photosynthetic effective optical radiation according to Claim 8.
84. according to the described method of claim 79, wherein, in response to by described reaction zone with the gaseous emissions feed to changing with the rate of heat transfer that gaseous emissions is fed into described heat-transfer medium from described reaction zone that the supply molar rate of described reaction zone changes and causes, thermal buffer is provided, with delay described reaction zone with the gaseous emissions feed to the influence that rate of heat transfer to the described biomass product in from the described heat-transfer medium that is heated to described drying machine produces that changes of the supply molar rate of described reaction zone.
85. according to the described method of claim 79, wherein, in response to reducing from described reaction zone with rate of heat transfer that gaseous emissions be fed into described heat-transfer medium reducing of causing with the gaseous emissions feed to the supply molar rate of described reaction zone by described reaction zone, provide with described drying machine in the extra heat source of biomass product thermal communication, so that the rate of heat transfer of the described biomass product in from the described heat-transfer medium that is heated to described drying machine is replenished.
86. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
The carbonic acid gas that gaseous emissions production process discharging carbonic acid gas and at least a portion are discharged be provided to described reaction zone, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of described reaction zone discharges with discharging carbonic acid gas feed in, regulate at least a input thing of importing described reaction zone according to the described reaction zone that is provided to described reaction zone with the molar rate of discharging carbonic acid gas feed at least.
87. 6 described methods wherein, when described at least a input thing is regulated, will place the described phototroph matter in the described reaction zone to be exposed under photosynthetic effective optical radiation according to Claim 8.
88. 6 described methods according to Claim 8, wherein, each that import in the described at least a input thing of described reaction zone is such input thing: it is essential for the growth velocity of the described phototroph matter in the described reaction zone that described input thing is supplied in the described reaction zone.
89. 6 described methods according to Claim 8, wherein, described at least a input thing comprise following one of at least: (i) photosynthetic effective optical radiation of supply characteristic strength; And (ii) supply extra-nutrition thing feed.
90. 9 described methods according to Claim 8, wherein, comprise the supply that starts the photosynthetic effective optical radiation that is provided to described reaction zone when the adjusting that described at least a input thing is done, or when increasing the intensity of the photosynthetic effective optical radiation be provided to described reaction zone, be provided to the supply of photosynthetic effective optical radiation of described reaction zone in described startup, or after increasing the intensity of the photosynthetic effective optical radiation that is provided to described reaction zone, improve the rate of cooling of light source, wherein said light source is arranged in the described reaction zone and to described reaction zone and supplies described photosynthetic effective optical radiation.
91. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
The carbonic acid gas that gaseous emissions production process discharging carbonic acid gas and at least a portion are discharged be provided to described reaction zone, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of described reaction zone discharges with discharging carbonic acid gas feed in, regulate at least a input thing that inputs to described reaction zone according to the described reaction zone that is provided to described reaction zone with the molar rate index of discharging the carbonic acid gas feed at least.
92. according to the described method of claim 91, wherein, when described at least a input thing is regulated, will place the described phototroph matter in the described reaction zone to be exposed under photosynthetic effective optical radiation.
93. according to the described method of claim 91, wherein, each that import in the described at least a input thing of described reaction zone is such input thing: it is essential for the growth velocity of the described phototroph matter in the described reaction zone that described input thing is supplied in the described reaction zone.
94. according to the described method of claim 91, wherein, described at least a input thing comprise following one of at least: (i) photosynthetic effective optical radiation of supply characteristic strength; And (ii) supply extra-nutrition thing feed.
95. according to the described method of claim 91, wherein, the described reaction zone that is provided to described reaction zone is the molar rate of described gaseous emissions production process discharging gaseous emissions with the index of the supply molar rate of discharging carbonic acid gas feed, thereby the described adjusting molar rate of discharging described gaseous emissions based on described gaseous emissions production process at least, wherein said gaseous emissions comprises that described reaction zone is with discharging carbonic acid gas feed.
96. according to the described method of claim 91, wherein, the described reaction zone that is provided to described reaction zone is carbonic acid gas volumetric molar concentration by the gaseous emissions of described gaseous emissions production process discharging with the index of the supply molar rate of discharging carbonic acid gas feed, thereby described adjusting is at least based on the carbonic acid gas volumetric molar concentration by the described gaseous emissions of described gaseous emissions production process discharging, and wherein said gaseous emissions comprises that described reaction zone is with discharging carbonic acid gas feed.
97. according to the described method of claim 91, wherein, the described reaction zone that is provided to described reaction zone is the molar rate of described gaseous emissions production process discharging carbonic acid gas with the index of the supply molar rate of discharging carbonic acid gas feed, thereby described adjusting is at least based on the molar rate of described gaseous emissions production process discharging carbonic acid gas, and wherein said gaseous emissions comprises that described reaction zone is with discharging carbonic acid gas feed.
98. according to the described method of claim 97, wherein, based on by the actual measurement molar flow rate of the gaseous emissions of described gaseous emissions production process discharging and by the combination of the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions of described gaseous emissions production process discharging, calculate the molar rate of described gaseous emissions production process discharging carbonic acid gas.
99. according to the described method of claim 94, wherein, comprise the supply that starts the photosynthetic effective optical radiation that is provided to described reaction zone when the adjusting that described at least a input thing is done, or when increasing the intensity of the photosynthetic effective optical radiation be provided to described reaction zone, be provided to the supply of photosynthetic effective optical radiation of described reaction zone in described startup, or after increasing the intensity of the photosynthetic effective optical radiation that is provided to described reaction zone, improve the rate of cooling of light source, wherein said light source is arranged in the described reaction zone and to described reaction zone and supplies described photosynthetic effective optical radiation.
100. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
The carbonic acid gas that gaseous emissions production process discharging carbonic acid gas and at least a portion are discharged be provided to described reaction zone, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of described reaction zone discharges with discharging carbonic acid gas feed in, when detecting the vicissitudinous indication of supply molar rate of the described reaction zone usefulness discharging carbonic acid gas feed that is provided to described reaction zone, regulate at least a input thing that inputs to described reaction zone.
101. according to the described method of claim 100, wherein, when described at least a input thing is regulated, will place the described phototroph matter in the described reaction zone to be exposed under photosynthetic effective optical radiation.
102. according to the described method of claim 100, wherein, each that import in the described at least a input thing of described reaction zone is such input thing: it is essential for the growth velocity of the described phototroph matter in the described reaction zone that described input thing is supplied in the described reaction zone.
103. according to the described method of claim 100, wherein, described at least a input thing comprise following one of at least: (i) photosynthetic effective optical radiation of supply characteristic strength; And (ii) supply extra-nutrition thing feed.
104. according to the described method of claim 103, wherein, comprise the supply that starts the photosynthetic effective optical radiation that is provided to described reaction zone when the adjusting that described at least a input thing is done, or when increasing the intensity of the photosynthetic effective optical radiation be provided to described reaction zone, be provided to the supply of photosynthetic effective optical radiation of described reaction zone in described startup, or after increasing the intensity of the photosynthetic effective optical radiation that is provided to described reaction zone, improve the rate of cooling of light source, wherein said light source is arranged in the described reaction zone and to described reaction zone and supplies described photosynthetic effective optical radiation.
105. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
At gaseous emissions production process discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to described reaction zone, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of described reaction zone discharges with discharging carbonic acid gas feed, when the supply molar rate that detects the described reaction zone usefulness discharging carbonic acid gas feed that is provided to described reaction zone reduces, perhaps when detecting the described reaction zone that the is provided to described reaction zone supply molar rate with discharging carbonic acid gas feed the indication of reduction arranged, increase the supply molar rate of the additional carbonic acid gas feed that is provided to described reaction zone, or start described additional carbonic acid gas feed to the supply of described reaction zone.
106. according to the described method of claim 105, wherein, reducing or detecting the described reaction zone that is provided to described reaction zone has reduction with the supply molar rate of discharging the carbonic acid gas feed indication in response to detecting the described reaction zone that the is provided to described reaction zone supply molar rate with discharging carbonic acid gas feed, and when starting described additional carbonic acid gas feed to the supply of described reaction zone, described additional carbonic acid gas feed continues the time greater than 30 minutes after the supply self-starting of described reaction zone.
107. according to the described method of claim 105, further comprise starting and contain the raw material of make-up gas to the supply of described reaction zone, or increase is provided to the supply of raw material molar rate that contains make-up gas of described reaction zone, if there is carbonic acid gas, then the volumetric molar concentration of its carbonic acid gas is lower than the carbonic acid gas volumetric molar concentration of the described additional carbonic acid gas feed that is provided to described reaction zone in the wherein said raw material that contains make-up gas.
108. according to the described method of claim 107, wherein, any described reaction zone with discharging carbonic acid gas feed, described additional carbonic acid gas feed and the described raw material combination that contains make-up gas limit be provided to described reaction zone, as the combined operation feedstream of at least a portion of described reaction zone feeding material, described reaction zone feeding material is provided to described reaction zone and the material in the described reaction zone is produced agitaion, thereby makes that the concentration difference of any phototroph matter is lower than 20% in the described reaction zone at 2.
109. according to the described method of claim 107, wherein, the described startup raw material that contains make-up gas is to the supply of described reaction zone or increase the supply of raw material molar rate that contains make-up gas that is provided to described reaction zone and be in response to the supply molar rate that detects the described reaction zone feeding material that is provided to described reaction zone and reduce or have the indication of reduction to implement.
110. according to the described method of claim 109, wherein, when described additional carbonic acid gas feed was provided to described reaction zone, startup contained the raw material of make-up gas to the supply of described reaction zone, or increased the supply of raw material molar rate that contains make-up gas that is provided to described reaction zone.
111. according to the described method of claim 107, wherein, start the described raw material that contains make-up gas to the supply of described reaction zone or increase that the described supply of raw material molar rate that contains make-up gas that is provided to described reaction zone has compensated at least in part because the described reaction zone that is provided to described reaction zone reduces with the supply molar rate of discharging carbonic acid gas feed or it supplies the reduction of mole delivery rate of the raw material that is provided to described reaction zone that termination causes or the termination of described raw material supply.
112. according to the described method of claim 105, wherein, when increasing described additional carbonic acid gas feed to the supply molar rate of described reaction zone or starting described additional carbonic acid gas feed to the supply of described reaction zone, will place the described phototroph matter in the described reaction zone to be exposed under photosynthetic effective optical radiation.
113. according to the described method of claim 107, wherein, the raw material that contains make-up gas in startup will place the phototroph matter in the reaction zone to be exposed under photosynthetic effective optical radiation to the supply of described reaction zone or when increasing the described raw material that contains make-up gas to the supply molar rate of described reaction zone.
114. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
With reaction zone carbonic acid gas feed to be enough to making described reaction zone carbonic acid gas feed streams before the pressure of at least 70 inches reaction zone degree of depth is supplied to described reaction zone, promote the pressure of described reaction zone carbonic acid gas feed through injector or jet-pump by making described reaction zone carbonic acid gas feed streams.
115. according to the described method of claim 114, wherein, described pressure is enough to make described reaction zone carbonic acid gas feed streams through at least 10 feet the reaction zone degree of depth.
116. according to the described method of claim 114, wherein, described pressure is enough to make described reaction zone carbonic acid gas feed streams through at least 20 feet the reaction zone degree of depth.
117. according to the described method of claim 114, wherein, described reaction zone carbonic acid gas feed produces agitaion to the supply of described reaction zone at least a portion content of described reaction zone, thereby makes that the concentration difference of any phototroph matter is lower than 20% in the described reaction zone at 2.
118. according to the described method of claim 114, wherein, described reaction zone carbonic acid gas feed is to be supplied by the gaseous emissions that the gaseous emissions production process produces.
119. according to the described method of claim 118, wherein, when described gaseous emissions production process is supplied described reaction zone carbonic acid gas feed to described reaction zone, carry out the lifting of described pressure.
120. according to the described method of claim 114, wherein, when carrying out described reaction zone carbonic acid gas feed to the supply of described reaction zone, will place the described reaction mixture in the described reaction zone to be exposed under photosynthetic effective optical radiation.
121. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
With reaction zone carbonic acid gas feed to be enough to making described reaction zone carbonic acid gas feed streams before the pressure of at least 70 inches reaction zone degree of depth is supplied to described reaction zone, utilize Venturi effect to shift pressure energy from driving the described reaction zone carbonic acid gas of flow direction feed.
122. according to the described method of claim 121, wherein, described pressure is enough to make described reaction zone carbonic acid gas feed streams through at least 10 feet the reaction zone degree of depth.
123. according to the described method of claim 121, wherein, described pressure is enough to make described reaction zone carbonic acid gas feed streams through at least 20 feet the reaction zone degree of depth.
124. according to the described method of claim 123, wherein, described reaction zone carbonic acid gas feed produces agitaion to the supply of described reaction zone at least a portion content of described reaction zone, thereby makes that the concentration difference of any phototroph matter is lower than 20% in the described reaction zone at 2.
125. according to the described method of claim 121, wherein, described reaction zone carbonic acid gas feed is to be supplied by the gaseous emissions that the gaseous emissions production process produces.
126. according to the described method of claim 125, wherein, when described gaseous emissions production process is supplied described reaction zone carbonic acid gas feed to described reaction zone, carry out the lifting of described pressure.
127. according to the described method of claim 121, wherein, when carrying out described reaction zone carbonic acid gas feed to the supply of described reaction zone, will place the described reaction mixture in the described reaction zone to be exposed under photosynthetic effective optical radiation.
128. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
When reaction zone feeding material is provided to described reaction zone, supply described reaction zone feeding material and additional gaseous diluent, the carbonic acid gas volumetric molar concentration of wherein said additional gaseous diluent is lower than the carbonic acid gas volumetric molar concentration that the reaction zone that is provided to described reaction zone feeding material is used the gaseous emissions feed.
129. according to the described method of claim 128, wherein, described additional gaseous diluent makes the reaction zone feeding material that is provided to described reaction zone have to the supply of described reaction zone feeding material to be lower than the predetermined peaked carbonic acid gas volumetric molar concentration of carbonic acid gas volumetric molar concentration.
130. according to the described method of claim 128, wherein, described additional gaseous diluent makes that to the supply of described reaction zone feeding material described reaction zone feeding material is thinning with regard to the carbonic acid gas volumetric molar concentration.
131. according to the described method of claim 128, wherein, described additional gaseous diluent makes the carbonic acid gas volumetric molar concentration in the described reaction zone feeding material reduce to the supply of described reaction zone feeding material.
132. according to the described method of claim 128, wherein, described reaction zone feeding material comprises reaction zone gaseous emissions feed, and wherein said reaction zone is that at least a portion of the gaseous emissions that discharged by the gaseous emissions production process limits with the gaseous emissions feed.
133. according to the described method of claim 132, wherein, when described reaction zone is provided to described reaction zone feeding material and described gaseous emissions production process and discharges described reaction zone with the gaseous emissions feed with the gaseous emissions feed, with described reaction zone feeding material supply to described reaction zone.
134. according to the described method of claim 133, wherein, described additional gaseous diluent is in response to the carbonic acid gas volumetric molar concentration that detects by in the gaseous emissions of carbon dioxide generating process discharging to the supply of described reaction zone feeding material and implements greater than predetermined carbonic acid gas volumetric molar concentration maximum value.
135. according to the described method of claim 134, wherein, based on the integral molar quantity of described gaseous emissions, described predetermined carbonic acid gas volumetric molar concentration maximum value is at least 10 moles of %.
136. according to the described method of claim 128, wherein, when the described reaction mixture in placing described reaction zone is exposed to photosynthetic effective optical radiation, described additional gaseous diluent is supplied to described reaction zone feeding material.
137. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
When supply concentrates the carbonic acid gas feed, to produce the carbonic acid gas feed of dilution, the carbonic acid gas volumetric molar concentration of the carbonic acid gas feed of wherein said dilution is lower than the carbonic acid gas volumetric molar concentration of described concentrated carbonic acid gas feed with described concentrated carbonic acid gas feed and additional gaseous diluent blending; And
The reaction zone that at least a portion is diluted is supplied to described reaction zone with the carbonic acid gas feed.
138. according to the described method of claim 137, wherein, the feasible reaction zone that is provided to the described dilution of described reaction zone of described blending has to be lower than with the carbonic acid gas feed is scheduled to the peaked carbonic acid gas volumetric molar concentration of carbonic acid gas volumetric molar concentration.
139. according to the described method of claim 138, wherein, described concentrated carbonic acid gas feed comprises reaction zone carbonic acid gas feed, wherein said reaction zone carbonic acid gas feed is limited by at least a portion of the gaseous emissions that the gaseous emissions production process produces, and wherein, when being provided to, described reaction zone carbonic acid gas feed implements described blending when described concentrated carbonic acid gas feed and described gaseous emissions production process produce described reaction zone with the gaseous emissions feed.
140. according to the described method of claim 139, wherein, described blending is in response to the carbonic acid gas volumetric molar concentration that detects by in the gaseous emissions of described gaseous emissions production process discharging and implements greater than predetermined carbonic acid gas volumetric molar concentration maximum value.
141. according to the described method of claim 140, wherein, based on the integral molar quantity of described gaseous emissions, described predetermined carbonic acid gas volumetric molar concentration maximum value is at least 10 moles of %.
142. according to the described method of claim 137, wherein, implement described blending when the described reaction mixture in placing described reaction zone is exposed to photosynthetic effective optical radiation.

Claims (142)

1. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, and described method comprises:
Described reaction mixture is being exposed under photosynthetic effective optical radiation and is causing described phototroph matter in described reaction zone, to be grown, and in described reaction zone discharging phototroph matter, when phototroph matter growth indexes is different from phototroph matter growth indexes target value, adjusting is from the molar rate of described reaction zone discharging phototroph matter, the growth that wherein causes comprises the growth that causes by photosynthesis, and wherein said phototroph matter growth indexes target value is to be placed in the described reaction zone and the predetermined mole growth velocity that is exposed to the described phototroph matter in the described reaction mixture under photosynthetic effective optical radiation is the basis.
2. method according to claim 1 wherein, makes described phototroph matter growth indexes target value be associated with the predetermined mole growth velocity of described phototroph matter.
3. method according to claim 1, wherein, described adjusting is in response to detect to there are differences between described phototroph matter growth indexes and the described phototroph matter growth indexes target value and implements.
4. method according to claim 3 further comprises and detects phototroph matter growth indexes so that measured light health material growth indexes to be provided.
5. method according to claim 4, wherein, described measured light health material growth indexes represents the volumetric molar concentration of the described phototroph matter in the described reaction mixture.
6. method according to claim 4, wherein, described measured light health material growth indexes is the volumetric molar concentration of the described phototroph matter in the described reaction mixture.
7. method according to claim 4, wherein, described measured light health material growth indexes is the volumetric molar concentration of the phototroph matter in the reaction zone product of described reaction zone discharging, wherein said reaction zone product also contains water.
8. method according to claim 1, wherein, described phototroph matter growth indexes target value is scheduled to.
9. method according to claim 1, wherein, the growth of the described phototroph matter that causes is to carry out with interior growth molar rate with 10% of described predetermined mole growth velocity.
10. method according to claim 1, wherein, the growth of the described phototroph matter that causes is to carry out with interior growth molar rate with 5% of described predetermined mole growth velocity.
11. method according to claim 1, wherein, the growth of the described phototroph matter that causes is to carry out with interior growth molar rate with 1% of described predetermined mole growth velocity.
12. method according to claim 1, wherein, described reaction zone is placed in the bioreactor, and the phototroph matter of wherein discharging is contained in the overflow of described bioreactor discharge, and described overflow is by producing water-based feeding material supply to described reaction zone.
13. method according to claim 12 wherein, implements described reaction zone is discharged the adjusting of the molar rate of phototroph matter by regulating described water-based feeding material to the supply molar rate of described reaction zone.
14. method according to claim 4, wherein, when measured light health material growth indexes was lower than described phototroph matter growth indexes target value, described adjusting comprises reduced the molar rate of described reaction zone discharging phototroph matter.
15. method according to claim 14, wherein, described reaction zone is placed in the bioreactor, and the phototroph matter of wherein discharging is contained in the overflow of described bioreactor discharge, and described overflow is by producing water-based feeding material supply to described reaction zone.
16. method according to claim 15, wherein, described adjusting is by making described water-based feeding material reduce to implement to the supply molar rate of described reaction zone.
17. method according to claim 1, wherein, when described phototroph matter growth indexes during greater than described phototroph matter growth indexes target value, described adjusting comprises increases the molar rate of described reaction zone discharging phototroph matter.
18. method according to claim 17, wherein, described reaction zone is placed in the bioreactor, and the phototroph matter of wherein discharging is contained in the overflow of described bioreactor discharge, and described overflow is by producing water-based feeding material supply to described reaction zone.
19. method according to claim 18, wherein, described adjusting is by described water-based feeding material is implemented to the delivery rate increase of described reaction zone.
20. method according to claim 12, wherein, described water-based feeding material does not contain phototroph matter in fact.
21. method according to claim 1 wherein, grows described production purposes phototroph matter to comprise carbonic acid gas to be supplied to described reaction zone and described production purposes reaction mixture is exposed under photosynthetic effective optical radiation.
22. method according to claim 21 wherein, is supplied described carbonic acid gas when growing.
23. method according to claim 22, wherein, at least a portion that is provided to the described carbonic acid gas of described reaction zone is supplied by described gaseous emissions when gaseous emissions production process discharging gaseous emissions.
24. method according to claim 1, wherein, described production purposes reaction mixture also contains water and carbonic acid gas.
25. method according to claim 1, wherein, the predetermined mole growth velocity of described production purposes phototroph matter be placed in the described reaction zone and be exposed to the described production purposes phototroph matter in the described reaction mixture under described photosynthetic effective optical radiation maximum mole growth velocity at least 90%.
26. the method for a growth production purposes phototroph matter in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic production purposes reaction mixture under photosynthetic effective optical radiation, wherein said production purposes reaction mixture comprises can be for the production purposes phototroph matter of growing in described reaction zone, and described method comprises:
Described reaction mixture is being exposed under photosynthetic effective optical radiation and is causing described production purposes phototroph matter in described reaction zone, to be grown, and in described reaction zone discharging production purposes phototroph matter, when phototroph matter growth indexes is different from predetermined phototroph matter growth indexes target value, adjusting is from the molar rate of described reaction zone discharging production purposes phototroph matter, the growth that wherein causes comprises the growth that causes by photosynthesis, and wherein said phototroph matter growth indexes target value is to be placed in the described reaction zone and the predetermined mole growth velocity that is exposed to the described production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation is the basis;
Being predetermined to include of wherein said target value:
The described production purposes reaction mixture of supply representative and can be used for carrying out photosynthetic assessment purposes reaction mixture under photosynthetic effective optical radiation being exposed to makes the phototroph matter in the described assessment purposes reaction mixture become the assessment purposes phototroph matter of the described production purposes phototroph matter of representative;
When the described assessment purposes reaction mixture in placing described reaction zone is exposed under photosynthetic effective optical radiation and causes described assessment purposes phototroph matter in described assessment purposes reaction mixture to be grown, at least termly detect phototroph matter growth indexes, so that a plurality of detected values that are detected the described phototroph matter growth indexes of for some time to be provided; And
Calculate the mole growth velocity of described assessment purposes phototroph matter according to a plurality of detected values of described phototroph matter growth indexes, determine a plurality of mole growth velocitys of described assessment purposes phototroph matter in described period thus;
Based on the mole growth velocity of calculating and the detected value that is used for the described phototroph matter growth indexes of the described mole of calculating growth velocity, set up the mole growth velocity of described assessment purposes phototroph matter and the relation between the described phototroph matter growth indexes, make the relation of setting up between the mole growth velocity of described assessment purposes phototroph matter and the described phototroph matter growth indexes represent the mole growth velocity of the described production purposes phototroph matter in the described reaction zone and the relation between the described phototroph matter growth indexes, establish the mole growth velocity of the interior described production purposes phototroph matter of described reaction zone and the relation between the described phototroph matter growth indexes thus;
Select the predetermined mole growth velocity of described production purposes phototroph matter; And
Described phototroph matter growth indexes target value is defined as: according to the relation of establishing between the mole growth velocity of the described production purposes phototroph matter in the described reaction zone and the described phototroph matter growth indexes, phototroph matter growth indexes when causing described predetermined mole growth velocity makes that thus also generation is related between described phototroph matter growth indexes target value and described predetermined mole growth velocity.
27. method according to claim 26, wherein, when described reaction zone has the feature of at least a assessment purposes growth conditions, make described assessment purposes phototroph matter carry out described growth, the feature of each in the wherein said at least a assessment purposes growth conditions all the represents described production purposes phototroph matter production purposes growth conditions that described reaction zone has when growing in described reaction zone.
28. method according to claim 27, wherein, described production purposes growth conditions is any in the multiple production purposes growth conditions, and described multiple production purposes growth conditions comprises: reaction zone composition, reaction zone temperature, reaction zone pH, reaction zone light intensity, reaction zone illumination mode, reaction zone illumination circulation and reaction zone temperature.
29. method according to claim 26, wherein, the predetermined mole growth velocity of described production purposes phototroph matter be placed in the described reaction zone 10 and be exposed to the described production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation maximum mole growth velocity at least 90%.
30. method according to claim 26, wherein, the predetermined mole growth velocity of described production purposes phototroph matter be placed in the described reaction zone and be exposed to the described production purposes phototroph matter in the described reaction mixture under photosynthetic effective optical radiation maximum mole growth velocity at least 99%.
31. method according to claim 26, wherein, described production purposes reaction mixture also contains water and carbonic acid gas; And wherein said assessment purposes reaction mixture also contains water and carbonic acid gas.
32. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, and described method comprises:
When the described reaction mixture in will placing described reaction zone was exposed under photosynthetic effective optical radiation and causes described phototroph matter growth in the described reaction mixture, 10% of the molar rate of growing in described reaction zone with described phototroph matter was discharged described phototroph matter with interior molar rate from described reaction zone;
The growth that wherein said phototroph matter is carried out in described reaction zone is to be placed in the described reaction zone and at least 90% the molar rate that is exposed to the maximum growth rate of the described phototroph matter in the described reaction mixture under photosynthetic effective optical radiation is carried out.
33. method according to claim 32, wherein, described reaction zone is placed in the bioreactor, and the phototroph matter of wherein discharging is contained in the overflow of described bioreactor discharge.
34. method according to claim 32, wherein, the growth of described production purposes phototroph matter comprises and carbonic acid gas is supplied to described reaction zone and described production purposes reaction mixture is exposed under photosynthetic effective optical radiation.
35. method according to claim 32, wherein, the described growth of the described phototroph matter in the described reaction zone is to be placed in the described reaction zone and at least 95% the molar rate that is exposed to the maximum growth rate of the described phototroph matter in the described reaction mixture under photosynthetic effective optical radiation is carried out.
36. method according to claim 32, wherein, the described growth of the described phototroph matter in the described reaction zone is to be placed in the described reaction zone and at least 99% the molar rate that is exposed to the maximum growth rate of the described phototroph matter in the described reaction mixture under photosynthetic effective optical radiation is carried out.
37. method according to claim 32, wherein, 5% of the molar rate of growing with the described phototroph matter that places in the described reaction zone is discharged described phototroph matter with interior molar rate from described reaction zone.
38. method according to claim 32, wherein, 1% of the molar rate of growing with the described phototroph matter that places in the described reaction zone is discharged described phototroph matter with interior molar rate from described reaction zone.
39. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, and described method comprises:
When described reaction mixture being exposed under photosynthetic effective optical radiation and causing placing described phototroph matter in the described reaction mixture of described reaction zone to be grown, from described reaction zone discharging phototroph matter, make described phototroph matter the discharging molar rate molar rate that described phototroph matter is grown 10% in, the growth of the described phototroph matter that wherein causes comprises the growth that causes by photosynthesis.
40. according to the described method of claim 39, wherein, the discharging molar rate of described phototroph matter molar rate that described phototroph matter is grown 5% in.
41. according to the described method of claim 39, wherein, the discharging molar rate of described phototroph matter molar rate that described phototroph matter is grown 1% in.
42. according to the described method of claim 39, wherein, the discharging molar rate of described phototroph matter equals the molar rate that described phototroph matter is grown.
43. according to the described method of claim 39, wherein, the described phototroph matter molar rate of growing equals to be placed in the described reaction zone and is exposed to the maximum mole growth velocity of the described phototroph matter in the described reaction mixture under photosynthetic effective optical radiation.
44. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
At gaseous emissions production process discharging gaseous emissions, wherein any described gaseous emissions defined reaction district that is provided to described reaction zone with the gaseous emissions feed in, based on the detection of at least a carbon dioxide treatment figureofmerit being regulated described reaction zone with the supply of gaseous emissions feed to described reaction zone.
45. according to the described method of claim 44, wherein, in described reaction zone, carry out at least one the detection in the described at least a carbon dioxide treatment figureofmerit.
46. according to the described method of claim 44, comprise that further the part branch of the gaseous emissions that adjusting is discharged flows to the supply of another operating unit, the part branch current limit shunting gaseous emissions of the described gaseous emissions of another operating unit of supply that wherein discharges.
47. according to the described method of claim 46, wherein, when described reaction zone is regulated to the supply of described reaction zone with the gaseous emissions feed, the described shunting gaseous emissions of supplying with described another operating unit is regulated.
48. according to the described method of claim 46, wherein, reduce it to the impact of environment thereby described another operating unit transforms described shunting gaseous emissions.
49. according to the described method of claim 48, wherein, described another operating unit is the separator that can remove carbonic acid gas from described shunting gaseous emissions.
50. according to the described method of claim 48, wherein, described another operating unit is chimney.
51. according to the described method of claim 44, wherein, the carbon dioxide treatment figureofmerit that detects is any feature of capacity of the described reaction zone of representative, and the capacity of wherein said reaction zone is that the capacity that transforms takes place for photosynthetic response that the described phototroph matter of carbonic acid gas in placing described reaction zone that described reaction zone will receive carbonic acid gas and at least a portion is received is carried out.
52. according to the described method of claim 44, wherein, the carbon dioxide treatment figureofmerit that detects is any feature of described method of the capacity of the described reaction zone of representative, the capacity of wherein said reaction zone is that the capacity that transforms takes place for photosynthetic response that described reaction zone will receive carbonic acid gas and the described phototroph matter in the described reaction mixture of carbonic acid gas in placing described reaction zone that at least a portion receives is carried out, thereby makes described photosynthesis realize the predetermined mole growth velocity of the described phototroph matter in the described reaction zone.
53. according to the described method of claim 44, wherein, the carbon dioxide treatment figureofmerit that detects is any feature of described method of the capacity of the described reaction zone of representative, the capacity of wherein said reaction zone is that the capacity that transforms takes place for photosynthetic response that the described phototroph matter of carbonic acid gas in placing described reaction zone that described reaction zone will receive carbonic acid gas and at least a portion is received is carried out, thereby makes any carbonic acid gas from described reaction zone discharging all be lower than acceptable molar rate.
54. according to the described method of claim 44, wherein, the carbon dioxide treatment figureofmerit that detects is at least a in the volumetric molar concentration of pH and phototroph matter.
55. according to the described method of claim 44, wherein, discharge described gaseous emissions at described gaseous emissions production process, the any described gaseous emissions defined reaction district that wherein is provided to described reaction zone is with the gaseous emissions feed time, when detected carbon dioxide treatment figureofmerit in described reaction zone represented described reaction zone and will receive the such capacity of carbonic acid gas supply that molar rate increases, the adjusting that described reaction zone is done to the supply of described reaction zone with the gaseous emissions feed comprised: start described reaction zone usefulness gaseous emissions feed to the supply of described reaction zone, or have additional supply of to the supply molar rate of the described reaction zone usefulness gaseous emissions feed of described reaction zone.
56. according to the described method of claim 55, further comprise: arrange when described shunting gaseous emissions being supplied to described another operating unit and described shunting gaseous emissions and being provided to described another operating unit in that described gaseous emissions production process and another operating unit are collaborative, the supply molar rate of the described shunting gaseous emissions that is provided to described another operating unit is reduced or described supply is stopped.
57. according to the described method of claim 44, wherein, at described gaseous emissions production process discharging gaseous emissions, and the described gaseous emissions of at least a portion is provided to described reaction zone, the described at least a portion gaseous emissions defined reaction district that wherein is provided to described reaction zone is with the gaseous emissions feed time, when detected carbon dioxide treatment figureofmerit in described reaction zone represented described reaction zone and will receive the such capacity of carbonic acid gas supply that molar rate reduces, the adjusting that described reaction zone is done to the supply of described reaction zone with the gaseous emissions feed comprised: the supply molar rate that reduces the described reaction zone usefulness gaseous emissions feed that is provided to described reaction zone, or stop its supply.
58. according to the described method of claim 57, wherein, work in coordination with setting so that described shunting gaseous emissions is supplied under the situation of described another operating unit at described gaseous emissions production process and another operating unit, described method further comprises: start described shunting gaseous emissions to the supply of described another operating unit, or increase the supply molar rate of the described shunting gaseous emissions that is provided to described another operating unit.
59. according to the described method of claim 44, wherein, when detected carbon dioxide treatment figureofmerit in described reaction zone represents described reaction zone and will receive the such capacity of carbonic acid gas supply that molar rate reduces, represent described reaction zone in response to the carbon dioxide treatment figureofmerit that detects and to receive the such capacity of carbonic acid gas supply that molar rate reduces, the adjusting that described reaction zone is done with the gaseous emissions feed comprises the supply molar rate that reduces the described reaction zone usefulness gaseous emissions feed that is provided to described reaction zone, or stop its supply, in this case, described method further comprises: startup contains the raw material of make-up gas to the supply of described reaction zone, or increases the supply of raw material molar rate that contains make-up gas that is provided to described reaction zone.
60. according to the described method of claim 59, wherein, if there is carbonic acid gas, then the volumetric molar concentration of its carbonic acid gas is lower than the carbonic acid gas volumetric molar concentration that is supplied to described at least a portion gaseous emissions of described reaction zone from described gaseous emissions production process in the described raw material that contains make-up gas.
61. according to the described method of claim 60, wherein, make the described reaction zone that is provided to described reaction zone reduce with the mole delivery rate of gaseous emissions feed or make its supply stop and contain the raw material of make-up gas to be provided to that the supply molar rate of the carbonic acid gas of described reaction zone reduces or make it supply termination be crew-served to described reaction zone supply is described to the supply of described reaction zone with the gaseous emissions feed by regulating described reaction zone.
62. according to the described method of claim 59, wherein, start the described raw material that contains make-up gas to the supply of described reaction zone or increase that the described supply of raw material molar rate that contains make-up gas that is provided to described reaction zone has compensated at least in part because the described reaction zone that is provided to described reaction zone reduces with the supply molar rate of gaseous emissions feed or it supplies the reduction of mole delivery rate of the raw material that is provided to described reaction zone that termination causes or the termination of described raw material supply.
63. according to the described method of claim 62, wherein, below (a) and combination (b): (a) reduce described reaction zone with the gaseous emissions feed to the supply molar rate of described reaction zone or stop its supply; And (b) start the described raw material that contains make-up gas to the supply of described reaction zone or increase its supply molar rate, alleviated because the degree that the described reaction zone that is provided to described reaction zone dies down with stirring in the described reaction zone that the supply molar rate reduces or its supply termination causes of gaseous emissions feed.
64. according to the described method of claim 63, wherein, the described raw material that contains make-up gas and any described reaction zone are provided to described reaction zone with the combination of gaseous emissions feed as at least a portion of reaction zone feeding material, and described reaction zone feeding material supply produced agitaion to described reaction zone and to the material in the described reaction zone, thereby make that the volumetric molar concentration difference of any phototroph matter is lower than 20% in the described reaction zone at 2.
65. according to the described method of claim 44, wherein, when described reaction zone is regulated to the supply of described reaction zone with the gaseous emissions feed, will place the described reaction mixture in the described reaction zone to be exposed under photosynthetic effective optical radiation.
66. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
At gaseous emissions production process discharging gaseous emissions, and the described gaseous emissions of at least a portion is provided to described reaction zone, the described at least a portion gaseous emissions defined reaction district that wherein is provided to described reaction zone is with the gaseous emissions feed time, be provided to the supply molar rate of the described reaction zone usefulness gaseous emissions feed of described reaction zone in reduction, or when stopping described reaction zone with the supply of gaseous emissions feed, described method further comprises: startup contains the raw material of make-up gas to the supply of described reaction zone, perhaps increases the supply of raw material molar rate that contains make-up gas to described reaction zone supply.
67. according to the described method of claim 66, wherein, the described startup raw material that contains make-up gas is to the supply of described reaction zone or increase the supply of raw material molar rate that contains make-up gas that is provided to described reaction zone and be in response to and detect that the reaction zone that is provided to reaction zone reduces with the supply molar rate of gaseous emissions feed or its supply termination or detect the reaction zone that is provided to reaction zone and have the indication of reduction or its indication that is supplied with termination to implement with the supply molar rate of gaseous emissions feed.
68. according to the described method of claim 67, wherein, if there is carbonic acid gas, then the volumetric molar concentration of its carbonic acid gas is lower than the carbonic acid gas volumetric molar concentration that is supplied to described at least a portion gaseous emissions of described reaction zone from described gaseous emissions production process in the described raw material that contains make-up gas.
69. according to the described method of claim 68, wherein, make the described reaction zone that is provided to described reaction zone reduce with the mole delivery rate of gaseous emissions feed or make its supply stop and contain the raw material of make-up gas to be provided to that the supply molar rate of the carbonic acid gas of described reaction zone reduces or make it supply termination be crew-served to described reaction zone supply is described to the supply of described reaction zone with the gaseous emissions feed by regulating described reaction zone.
70. according to the described method of claim 66, wherein, start the described raw material that contains make-up gas to the supply of described reaction zone or increase that the described supply of raw material molar rate that contains make-up gas that is provided to described reaction zone has compensated at least in part because the described reaction zone that is provided to described reaction zone reduces with the supply molar rate of gaseous emissions feed or it supplies the reduction of mole delivery rate of the raw material that is provided to described reaction zone that termination causes or the termination of described raw material supply.
71. according to the described method of claim 70, wherein, below (a) and combination (b): (a) reduce described reaction zone with the gaseous emissions feed to the supply molar rate of described reaction zone or stop its supply; And (b) start the described raw material that contains make-up gas to the supply of described reaction zone or increase its supply molar rate, alleviated because the degree that the described reaction zone that is provided to described reaction zone dies down with stirring in the described reaction zone that the supply molar rate reduces or its supply termination causes of gaseous emissions feed.
72. according to the described method of claim 70, wherein, the described raw material that contains make-up gas and any described reaction zone are provided to described reaction zone with the combination of gaseous emissions feed as at least a portion of reaction zone feeding material, and described reaction zone feeding material supply produced agitaion to described reaction zone and to the material in the described reaction zone, thereby make that the volumetric molar concentration difference of any phototroph matter is lower than 20% in the described reaction zone at 2.
73. according to the described method of claim 66, wherein, the raw material that contains make-up gas when startup will place the described reaction mixture in the described reaction zone to be exposed under photosynthetic effective optical radiation to the supply of described reaction zone or when increasing the described supply of raw material molar rate that contains make-up gas.
74. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
Described reaction zone is supplied to reaction zone with the gaseous emissions feed, at least a portion defined reaction district gaseous emissions feed of the gaseous emissions that produces of gaseous emissions production process wherein, wherein said reaction zone comprises carbonic acid gas with the gaseous emissions feed; And
Replenish the aqueous substance feed from container to described reaction zone supply, wherein said additional aqueous substance feed comprises from described reaction zone with condensation the gaseous emissions feed and be collected in aqueous materials in the described container, and the condensation of wherein said aqueous materials is to realize when cooling off before described reaction zone is provided to described reaction zone with the gaseous emissions feed.
75. according to the described method of claim 74, wherein, the aqueous materials that is condensed is water.
76. according to the described method of claim 74, wherein, described additional aqueous substance feed further comprises aqueous materials.
77. according to the described method of claim 74, wherein, described reaction zone is to be lower than 50 ℃ temperature from being cooled to greater than 110 ℃ temperature with the cooling of gaseous emissions feed.
78. according to the described method of claim 77, wherein, in interchanger, carry out the cooling that described reaction zone is used the gaseous emissions feed.
79. according to the described method of claim 78, wherein, described condensation produces and is fed into the heat passage of heat-transfer medium from described reaction zone with gaseous emissions, thereby produce the heat-transfer medium that is heated, and the described heat-transfer medium that is heated is supplied to drying machine to evaporate moisture from the biomass product of described reaction zone discharging.
80. according to the described method of claim 79, wherein, described evaporation is to carry out heat passage the realization by the described biomass product in from the described heat-transfer medium that is heated to described drying machine, thereby produce the heat-transfer medium of cooling, and the heat-transfer medium of described cooling is recycled to described interchanger to carry out described condensation.
81. according to the described method of claim 74, wherein, when described reaction zone is provided to described reaction zone with the gaseous emissions feed, carry out the supply of described additional aqueous materials.
82. 1 described method wherein, when described gaseous emissions production process produces described reaction zone with the gaseous emissions feed, is carried out the supply of described additional aqueous materials according to Claim 8.
83. 2 described methods wherein, when carrying out the supply of described additional aqueous materials, will place the described reaction zone mixture in the described reaction zone to be exposed under photosynthetic effective optical radiation according to Claim 8.
84. according to the described method of claim 79, wherein, in response to by described reaction zone with the gaseous emissions feed to changing with the rate of heat transfer that gaseous emissions is fed into described heat-transfer medium from described reaction zone that the supply molar rate of described reaction zone changes and causes, thermal buffer is provided, with delay described reaction zone with the gaseous emissions feed to the influence that rate of heat transfer to the described biomass product in from the described heat-transfer medium that is heated to described drying machine produces that changes of the supply molar rate of described reaction zone.
85. according to the described method of claim 79, wherein, in response to reducing from described reaction zone with rate of heat transfer that gaseous emissions be fed into described heat-transfer medium reducing of causing with the gaseous emissions feed to the supply molar rate of described reaction zone by described reaction zone, provide with described drying machine in the extra heat source of biomass product thermal communication, so that the rate of heat transfer of the described biomass product in from the described heat-transfer medium that is heated to described drying machine is replenished.
86. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
The carbonic acid gas that gaseous emissions production process discharging carbonic acid gas and at least a portion are discharged be provided to described reaction zone, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of described reaction zone discharges with discharging carbonic acid gas feed in, regulate at least a input thing of importing described reaction zone according to the described reaction zone that is provided to described reaction zone with the molar rate of discharging carbonic acid gas feed at least.
87. 6 described methods wherein, when described at least a input thing is regulated, will place the described phototroph matter in the described reaction zone to be exposed under photosynthetic effective optical radiation according to Claim 8.
88. 6 described methods according to Claim 8, wherein, each that import in the described at least a input thing of described reaction zone is such input thing: it is essential for the mole growth velocity of the described phototroph matter in the described reaction zone that described input thing is supplied in the described reaction zone.
89. 6 described methods according to Claim 8, wherein, described at least a input thing comprise following one of at least: (i) photosynthetic effective optical radiation of supply characteristic strength; And (ii) supply extra-nutrition thing feed.
90. 9 described methods according to Claim 8, wherein, comprise the supply that starts the photosynthetic effective optical radiation that is provided to described reaction zone when the adjusting that described at least a input thing is done, or when increasing the intensity of the photosynthetic effective optical radiation be provided to described reaction zone, be provided to the supply of photosynthetic effective optical radiation of described reaction zone in described startup, or after increasing the intensity of the photosynthetic effective optical radiation that is provided to described reaction zone, improve the rate of cooling of light source, wherein said light source is arranged in the described reaction zone and to described reaction zone and supplies described photosynthetic effective optical radiation.
91. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
The carbonic acid gas that gaseous emissions production process discharging carbonic acid gas and at least a portion are discharged be provided to described reaction zone, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of described reaction zone discharges with discharging carbonic acid gas feed in, regulate at least a input thing that inputs to described reaction zone according to the described reaction zone that is provided to described reaction zone with the molar rate index of discharging the carbonic acid gas feed at least.
92. according to the described method of claim 91, wherein, when described at least a input thing is regulated, will place the described phototroph matter in the described reaction zone to be exposed under photosynthetic effective optical radiation.
93. according to the described method of claim 91, wherein, each that import in the described at least a input thing of described reaction zone is such input thing: it is essential for the growth velocity of the described phototroph matter in the described reaction zone that described input thing is supplied in the described reaction zone.
94. according to the described method of claim 91, wherein, described at least a input thing comprise following one of at least: (i) photosynthetic effective optical radiation of supply characteristic strength; And (ii) supply extra-nutrition thing feed.
95. according to the described method of claim 91, wherein, the described reaction zone that is provided to described reaction zone is the molar rate of described gaseous emissions production process discharging gaseous emissions with the index of the supply molar rate of discharging carbonic acid gas feed, thereby the described adjusting molar rate of discharging described gaseous emissions based on described gaseous emissions production process at least, wherein said gaseous emissions comprises that described reaction zone is with discharging carbonic acid gas feed.
96. according to the described method of claim 91, wherein, the described reaction zone that is provided to described reaction zone is carbonic acid gas volumetric molar concentration by the gaseous emissions of described gaseous emissions production process discharging with the index of the supply molar rate of discharging carbonic acid gas feed, thereby described adjusting is at least based on the carbonic acid gas volumetric molar concentration by the described gaseous emissions of described gaseous emissions production process discharging, and wherein said gaseous emissions comprises that described reaction zone is with discharging carbonic acid gas feed.
97. according to the described method of claim 91, wherein, the described reaction zone that is provided to described reaction zone is the molar rate of described gaseous emissions production process discharging carbonic acid gas with the index of the supply molar rate of discharging carbonic acid gas feed, thereby described adjusting is at least based on the molar rate of described gaseous emissions production process discharging carbonic acid gas, and wherein said gaseous emissions comprises that described reaction zone is with discharging carbonic acid gas feed.
98. according to the described method of claim 97, wherein, based on by the actual measurement molar flow rate of the gaseous emissions of described gaseous emissions production process discharging and by the combination of the actual measurement volumetric molar concentration of carbonic acid gas in the gaseous emissions of described gaseous emissions production process discharging, calculate the molar rate of described gaseous emissions production process discharging carbonic acid gas.
99. according to the described method of claim 94, wherein, comprise the supply that starts the photosynthetic effective optical radiation that is provided to described reaction zone when the adjusting that described at least a input thing is done, or when increasing the intensity of the photosynthetic effective optical radiation be provided to described reaction zone, be provided to the supply of photosynthetic effective optical radiation of described reaction zone in described startup, or after increasing the intensity of the photosynthetic effective optical radiation that is provided to described reaction zone, improve the rate of cooling of light source, wherein said light source is arranged in the described reaction zone and to described reaction zone and supplies described photosynthetic effective optical radiation.
100. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
The carbonic acid gas that gaseous emissions production process discharging carbonic acid gas and at least a portion are discharged be provided to described reaction zone, wherein be provided to carbonic acid gas defined reaction district that described at least a portion of described reaction zone discharges with discharging carbonic acid gas feed in, when detecting the vicissitudinous indication of supply molar rate of the described reaction zone usefulness discharging carbonic acid gas feed that is provided to described reaction zone, regulate at least a input thing that inputs to described reaction zone.
101. according to the described method of claim 100, wherein, when described at least a input thing is regulated, will place the described phototroph matter in the described reaction zone to be exposed under photosynthetic effective optical radiation.
102. according to the described method of claim 100, wherein, each that import in the described at least a input thing of described reaction zone is such input thing: it is essential for the growth velocity of the described phototroph matter in the described reaction zone that described input thing is supplied in the described reaction zone.
103. according to the described method of claim 100, wherein, described at least a input thing comprise following one of at least: (i) photosynthetic effective optical radiation of supply characteristic strength; And (ii) supply extra-nutrition thing feed.
104. according to the described method of claim 103, wherein, comprise the supply that starts the photosynthetic effective optical radiation that is provided to described reaction zone when the adjusting that described at least a input thing is done, or when increasing the intensity of the photosynthetic effective optical radiation be provided to described reaction zone, be provided to the supply of photosynthetic effective optical radiation of described reaction zone in described startup, or after increasing the intensity of the photosynthetic effective optical radiation that is provided to described reaction zone, improve the rate of cooling of light source, wherein said light source is arranged in the described reaction zone and to described reaction zone and supplies described photosynthetic effective optical radiation.
105. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
At gaseous emissions production process discharging carbonic acid gas, and the carbonic acid gas that at least a portion is discharged is provided to described reaction zone, when wherein being provided to carbonic acid gas defined reaction district that described at least a portion of described reaction zone discharges with discharging carbonic acid gas feed, when the supply molar rate that detects the described reaction zone usefulness discharging carbonic acid gas feed that is provided to described reaction zone reduces, perhaps when detecting the described reaction zone that the is provided to described reaction zone supply molar rate with discharging carbonic acid gas feed the indication of reduction arranged, increase the supply molar rate of the additional carbonic acid gas feed that is provided to described reaction zone, or start described additional carbonic acid gas feed to the supply of described reaction zone.
106. according to the described method of claim 105, wherein, reducing or detecting the described reaction zone that is provided to described reaction zone has reduction with the supply molar rate of discharging the carbonic acid gas feed indication in response to detecting the described reaction zone that the is provided to described reaction zone supply molar rate with discharging carbonic acid gas feed, and when starting described additional carbonic acid gas feed to the supply of described reaction zone, described additional carbonic acid gas feed continues the time greater than 30 minutes after the supply self-starting of described reaction zone.
107. according to the described method of claim 105, further comprise starting and contain the raw material of make-up gas to the supply of described reaction zone, or increase is provided to the supply of raw material molar rate that contains make-up gas of described reaction zone, if there is carbonic acid gas, then the volumetric molar concentration of its carbonic acid gas is lower than the carbonic acid gas volumetric molar concentration of the described additional carbonic acid gas feed that is provided to described reaction zone in the wherein said raw material that contains make-up gas.
108. according to the described method of claim 107, wherein, any described reaction zone with discharging carbonic acid gas feed, described additional carbonic acid gas feed and the described raw material combination that contains make-up gas limit be provided to described reaction zone, as the combined operation feedstream of at least a portion of described reaction zone feeding material, described reaction zone feeding material is provided to described reaction zone and the material in the described reaction zone is produced agitaion, thereby makes that the volumetric molar concentration difference of any phototroph matter is lower than 20% in the described reaction zone at 2.
109. according to the described method of claim 107, wherein, the described startup raw material that contains make-up gas is to the supply of described reaction zone or increase the supply of raw material molar rate that contains make-up gas that is provided to described reaction zone and be in response to the supply molar rate that detects the described reaction zone feeding material that is provided to described reaction zone and reduce or have the indication of reduction to implement.
110. according to the described method of claim 109, wherein, when described additional carbonic acid gas feed was provided to described reaction zone, startup contained the raw material of make-up gas to the supply of described reaction zone, or increased the supply of raw material molar rate that contains make-up gas that is provided to described reaction zone.
111. according to the described method of claim 107, wherein, start the described raw material that contains make-up gas to the supply of described reaction zone or increase that the described supply of raw material molar rate that contains make-up gas that is provided to described reaction zone has compensated at least in part because the described reaction zone that is provided to described reaction zone reduces with the supply molar rate of discharging carbonic acid gas feed or it supplies the reduction of mole delivery rate of the raw material that is provided to described reaction zone that termination causes or the termination of described raw material supply.
112. according to the described method of claim 105, wherein, when increasing described additional carbonic acid gas feed to the supply molar rate of described reaction zone or starting described additional carbonic acid gas feed to the supply of described reaction zone, will place the described phototroph matter in the described reaction zone to be exposed under photosynthetic effective optical radiation.
113. according to the described method of claim 107, wherein, the raw material that contains make-up gas in startup will place the phototroph matter in the reaction zone to be exposed under photosynthetic effective optical radiation to the supply of described reaction zone or when increasing the described raw material that contains make-up gas to the supply molar rate of described reaction zone.
114. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
With reaction zone carbonic acid gas feed to be enough to making described reaction zone carbonic acid gas feed streams before the pressure of at least 70 inches reaction zone degree of depth is supplied to described reaction zone, promote the pressure of described reaction zone carbonic acid gas feed through injector or jet-pump by making described reaction zone carbonic acid gas feed streams.
115. according to the described method of claim 114, wherein, described pressure is enough to make described reaction zone carbonic acid gas feed streams through at least 10 feet the reaction zone degree of depth.
116. according to the described method of claim 114, wherein, described pressure is enough to make described reaction zone carbonic acid gas feed streams through at least 20 feet the reaction zone degree of depth.
117. according to the described method of claim 114, wherein, described reaction zone carbonic acid gas feed produces agitaion to the supply of described reaction zone at least a portion content of described reaction zone, thereby makes that the volumetric molar concentration difference of any phototroph matter is lower than 20% in the described reaction zone at 2.
118. according to the described method of claim 114, wherein, described reaction zone carbonic acid gas feed is to be supplied by the gaseous emissions that the gaseous emissions production process produces.
119. according to the described method of claim 118, wherein, when described gaseous emissions production process is supplied described reaction zone carbonic acid gas feed to described reaction zone, carry out the lifting of described pressure.
120. according to the described method of claim 114, wherein, when carrying out described reaction zone carbonic acid gas feed to the supply of described reaction zone, will place the described reaction mixture in the described reaction zone to be exposed under photosynthetic effective optical radiation.
121. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
With reaction zone carbonic acid gas feed to be enough to making described reaction zone carbonic acid gas feed streams before the pressure of at least 70 inches reaction zone degree of depth is supplied to described reaction zone, utilize Venturi effect to shift pressure energy from driving the described reaction zone carbonic acid gas of flow direction feed.
122. according to the described method of claim 121, wherein, described pressure is enough to make described reaction zone carbonic acid gas feed streams through at least 10 feet the reaction zone degree of depth.
123. according to the described method of claim 121, wherein, described pressure is enough to make described reaction zone carbonic acid gas feed streams through at least 20 feet the reaction zone degree of depth.
124. according to the described method of claim 123, wherein, described reaction zone carbonic acid gas feed produces agitaion to the supply of described reaction zone at least a portion content of described reaction zone, thereby makes that the volumetric molar concentration difference of any phototroph matter is lower than 20% in the described reaction zone at 2.
125. according to the described method of claim 121, wherein, described reaction zone carbonic acid gas feed is to be supplied by the gaseous emissions that the gaseous emissions production process produces.
126. according to the described method of claim 125, wherein, when described gaseous emissions production process is supplied described reaction zone carbonic acid gas feed to described reaction zone, carry out the lifting of described pressure.
127. according to the described method of claim 121, wherein, when carrying out described reaction zone carbonic acid gas feed to the supply of described reaction zone, will place the described reaction mixture in the described reaction zone to be exposed under photosynthetic effective optical radiation.
128. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
When reaction zone feeding material is provided to described reaction zone, supply described reaction zone feeding material and additional gaseous diluent, the carbonic acid gas volumetric molar concentration of wherein said additional gaseous diluent is lower than the carbonic acid gas volumetric molar concentration that the reaction zone that is provided to described reaction zone feeding material is used the gaseous emissions feed.
129. according to the described method of claim 128, wherein, described additional gaseous diluent makes the reaction zone feeding material that is provided to described reaction zone have to the supply of described reaction zone feeding material to be lower than the predetermined peaked carbonic acid gas volumetric molar concentration of carbonic acid gas volumetric molar concentration.
130. according to the described method of claim 128, wherein, described additional gaseous diluent makes that to the supply of described reaction zone feeding material described reaction zone feeding material is thinning with regard to the carbonic acid gas volumetric molar concentration.
131. according to the described method of claim 128, wherein, described additional gaseous diluent makes the carbonic acid gas volumetric molar concentration in the described reaction zone feeding material reduce to the supply of described reaction zone feeding material.
132. according to the described method of claim 128, wherein, described reaction zone feeding material comprises reaction zone gaseous emissions feed, and wherein said reaction zone is that at least a portion of the gaseous emissions that discharged by the gaseous emissions production process limits with the gaseous emissions feed.
133. according to the described method of claim 132, wherein, when described reaction zone is provided to described reaction zone feeding material and described gaseous emissions production process and discharges described reaction zone with the gaseous emissions feed with the gaseous emissions feed, with described reaction zone feeding material supply to described reaction zone.
134. according to the described method of claim 133, wherein, described additional gaseous diluent is in response to the carbonic acid gas volumetric molar concentration that detects by in the gaseous emissions of carbon dioxide generating process discharging to the supply of described reaction zone feeding material and implements greater than predetermined carbonic acid gas volumetric molar concentration maximum value.
135. according to the described method of claim 134, wherein, based on the integral molar quantity of described gaseous emissions, described predetermined carbonic acid gas volumetric molar concentration maximum value is at least 10 moles of %.
136. according to the described method of claim 128, wherein, when the described reaction mixture in placing described reaction zone is exposed to photosynthetic effective optical radiation, described additional gaseous diluent is supplied to described reaction zone feeding material.
137. the method for a grow light health material in reaction zone, wherein said reaction zone is included in to be exposed to and can be used for carrying out photosynthetic reaction mixture under photosynthetic effective optical radiation, wherein said reaction mixture comprises can be for the phototroph matter of growing in described reaction zone, the growth of wherein said phototroph matter comprises the growth that causes by photosynthesis, and described method comprises:
When supply concentrates the carbonic acid gas feed, to produce the carbonic acid gas feed of dilution, the carbonic acid gas volumetric molar concentration of the carbonic acid gas feed of wherein said dilution is lower than the carbonic acid gas volumetric molar concentration of described concentrated carbonic acid gas feed with described concentrated carbonic acid gas feed and additional gaseous diluent blending; And
The reaction zone that at least a portion is diluted is supplied to described reaction zone with the carbonic acid gas feed.
138. according to the described method of claim 137, wherein, the feasible reaction zone that is provided to the described dilution of described reaction zone of described blending has to be lower than with the carbonic acid gas feed is scheduled to the peaked carbonic acid gas volumetric molar concentration of carbonic acid gas volumetric molar concentration.
139. according to the described method of claim 138, wherein, described concentrated carbonic acid gas feed comprises reaction zone carbonic acid gas feed, wherein said reaction zone carbonic acid gas feed is limited by at least a portion of the gaseous emissions that the gaseous emissions production process produces, and wherein, when being provided to, described reaction zone carbonic acid gas feed implements described blending when described concentrated carbonic acid gas feed and described gaseous emissions production process produce described reaction zone with the gaseous emissions feed.
140. according to the described method of claim 139, wherein, described blending is in response to the carbonic acid gas volumetric molar concentration that detects by in the gaseous emissions of described gaseous emissions production process discharging and implements greater than predetermined carbonic acid gas volumetric molar concentration maximum value.
141. according to the described method of claim 140, wherein, based on the integral molar quantity of described gaseous emissions, described predetermined carbonic acid gas volumetric molar concentration maximum value is at least 10 moles of %.
142. according to the described method of claim 137, wherein, implement described blending when the described reaction mixture in placing described reaction zone is exposed to photosynthetic effective optical radiation.
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US12/784,106 US20110283618A1 (en) 2010-05-20 2010-05-20 Supplying bioreactor gaseous effluent to combustion process
US12/784,141 US20110287522A1 (en) 2010-05-20 2010-05-20 Producing biomass using pressurized exhaust gas
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US12/784,126 US8889400B2 (en) 2010-05-20 2010-05-20 Diluting exhaust gas being supplied to bioreactor
US12/784,181 US20110287523A1 (en) 2010-05-20 2010-05-20 Recovering make-up water during biomass production
US12/784,215 US8969067B2 (en) 2010-05-20 2010-05-20 Process for growing biomass by modulating supply of gas to reaction zone
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