DE20320020U1 - Installation for producing diesel and cement comprises a nuclear power station, a water electrolysis plant, a cement works, a reverse water gas balanced reactor and a Fischer-Tropsch reactor - Google Patents
Installation for producing diesel and cement comprises a nuclear power station, a water electrolysis plant, a cement works, a reverse water gas balanced reactor and a Fischer-Tropsch reactor Download PDFInfo
- Publication number
- DE20320020U1 DE20320020U1 DE20320020U DE20320020U DE20320020U1 DE 20320020 U1 DE20320020 U1 DE 20320020U1 DE 20320020 U DE20320020 U DE 20320020U DE 20320020 U DE20320020 U DE 20320020U DE 20320020 U1 DE20320020 U1 DE 20320020U1
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- Germany
- Prior art keywords
- cement
- reactor
- diesel
- fischer
- nuclear power
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/36—Manufacture of hydraulic cements in general
- C04B7/43—Heat treatment, e.g. precalcining, burning, melting; Cooling
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
- C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
- C10G2/33—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used
- C10G2/331—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals
- C10G2/332—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals of the iron-group
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2290/00—Organisational aspects of production methods, equipment or plants
- C04B2290/20—Integrated combined plants or devices, e.g. combined foundry and concrete plant
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
- Y02P40/121—Energy efficiency measures, e.g. improving or optimising the production methods
Abstract
Description
Die Erfindung betrifft eine Anlage zur Herstellung von Diesel und Zement. Der Diesel ist ein schwefelfreies und aromatenfreies Produkt mit hoher Zündwilligkeit und der Zement ist üblicher Portlandzement.The invention relates to a system for the production of diesel and cement. The diesel is a sulfur-free and aromatics-free product with high ignitability and the cement is more common Portland cement.
In der
Das Verfahren hat den prinzipiellen Vorteil, dass es kohlendioxidbedingte Klimaänderungen verhindert und nicht auf fossile Energieträger wie Kohle, Erdöl oder Erdgas zurückgreift.The procedure has the basic one The advantage that it prevents and does not prevent carbon dioxide-related climate changes on fossil fuels like coal, petroleum or uses natural gas.
Die Umwandlung der Kernenergie weiter in chemische Energie statt nur in Elektroenergie hat außerdem die Vorteile, dass:The conversion of nuclear energy continues in chemical energy instead of just in electrical energy also has the Advantages that:
- –die Energie leichter speicherbar wird-the Energy becomes easier to store
- –die Energie universeller (z.B. für Landwirtschaft und Verkehr) einsetzbar wird-the Energy more universal (e.g. for Agriculture and transport)
- –die geographische Lage des Kernkraftwerkes freier wählbar wird und-the geographic location of the nuclear power plant is freely selectable and
- –die Größe und damit die Wirtschaftlichkeit des Kernkraftwerke freier wählbar wird-the Size and so the economic viability of nuclear power plants can be freely selected
Es hat sich aber gezeigt, dass die Gewinnung des Kohlendioxides aus der Erdatmosphäre zu aufwendig ist.However, it has been shown that the Obtaining the carbon dioxide from the earth's atmosphere is too expensive.
So wie bei Wind, Sonne und Erdwärme die Energiedichte für eine unsubventionierte Nutzung zu gering ist, so ist die Stoffdichte von Kohlendioxid in Luft für eine wirtschaftliche Gewinnung von Kohlendioxid aus Luft zu gering.Just like wind, sun and geothermal energy density for one unsubsidized use is too low, so is the consistency of carbon dioxide in air for economic production of carbon dioxide from air is too low.
Erfindungsgemäß wird deshalb die Kohlenwasserstoffproduktion mit einem Prozess der große Mengen Kohlendioxid liefert gekoppelt.The hydrocarbon production is therefore according to the invention with a process of large quantities Carbon dioxide delivers coupled.
Dieser Prozess ist die Zementproduktion. Pro Tonne Zement werden je nach Anlage mindestens 0,6 Tonnen Kohlendioxid freigesetzt und bisher als klimaschädigendes Gas in die Erdatmosphäre entlassen.This process is cement production. Per Depending on the plant, one ton of cement will produce at least 0.6 tons of carbon dioxide released and previously released as a climate-damaging gas into the earth's atmosphere.
Dass als Kohlenwasserstoff gerade Diesel produziert und als kohlendioxidliefender Prozess gerade die Zementproduktion gewählt wurde, hat folgende Gründe:That as a hydrocarbon right now Diesel produces and as a carbon dioxide-producing process just that Cement production chosen has the following reasons:
Diesel und Zement sind weltweit begehrte Produkte mit einer stabilen Nachfrage. Die jährliche Weltdieselproduktion (Diesel und Heizöl) beträgt gegenwärtig ca. 1,5 Mrd. Tonnen und die jährliche Weltzementproduktion ca. 1,7 Mrd. Tonnen.Diesel and cement are sought-after products worldwide with stable demand. The annual world diesel production (Diesel and heating oil) is currently about 1.5 billion tons and the annual World cement production approx. 1.7 billion tons.
Diesel ist von alten flüssigen und gasförmigen Energieträgern der Gesuchteste überhaupt. Er ist Wasserstoff, Erdgas, Methanol, Benzin und Kerosin aus folgenden Gründen überlegen:Diesel is from old liquid and gaseous fuels the most wanted one at all. It is hydrogen, natural gas, methanol, gasoline and kerosene from the following Consider reasons:
- –Die Weltlandwirtschaft und damit die Welternährung beruht in erster Linie auf mit Dieselkraftstoff betriebenen Maschinen-The World agriculture and thus world food is primarily based on machines powered by diesel fuel
- –Die Weltnotversorgung wie Krankenauto und Feuerwehr beruht in erster Linie auf Dieselfahrzeugen-The World emergency care such as the ambulance and fire brigade is based first Line on diesel vehicles
- –Der Weltgüterverkehr, und damit die Weltnahrungsmittelverteilung, beruht in erster Linie auf Dieselkraftstoff (LKW, Schiff, Bahn)-The World freight traffic, and thus the global food distribution, is based primarily on diesel fuel (truck, ship, train)
- –Der Weltpersonenverkehr (Bus, Bahn, Fähren) beruht in erster Linie auf Diesel-The World passenger transport (bus, train, ferries) is primarily based on diesel
- –Die Weltbauwirtschaft beruht in erster Linie auf dieselbetriebenen Maschinen-The The global construction industry is primarily based on diesel-powered machines
- –Dieselkraftstoff besitzt fast keinen Verdunstungsverlust und ist dadurch praktisch unbegrenzt ohne Aufwand lagerbar-Dieselkraftstoff has almost no loss of evaporation and is therefore practical Can be stored indefinitely without effort
- –Dieselkraftstoff ist identisch mit Heizöl und kann deshalb auch zum Heizen in bestehenden Anlagen verwendet werden-Dieselkraftstoff is identical to heating oil and can therefore also be used for heating in existing systems become
- –Durch den hohen Flammpunkt von Dieselkraftstoff besteht kaum Explosionsgefahr (z.B. durch elektrostatische Aufladung) und nur die geringste Brandgefahr von allen brennbaren Flüssigkeiten und Gasen-By The high flash point of diesel fuel means there is hardly any risk of explosion (e.g. by electrostatic charging) and only the slightest fire risk of all flammable liquids and gases
- –Dieselkraftstoff besitzt einen hohen Energieinhalt pro Volumen und Masse-Dieselkraftstoff has a high energy content per volume and mass
- –Dieselmotoren besitzen einen hohen Wirkungsgraddiesel engines have a high efficiency
- –Dieselmotoren sind robust und langlebigdiesel engines are robust and durable
- –Im Falle eines Transportunglückes (LKW, Bahn, Schiff) ist bei synthetischem Diesel mit den geringsten Schäden zu rechnen, denn es gibt keine dauerhafte Verseuchung, da synthetischer Diesel einerseits ganz langsam verdunstet und andererseits durch die Aromatenfreiheit sehr gut biologisch abgebaut wird-In the In the event of a transport accident (Truck, train, ship) has the lowest for synthetic diesel damage to count, because there is no permanent contamination, because of synthetic Diesel evaporates very slowly on the one hand and on the other hand through the absence of aromatics is biodegraded very well
- –Es existiert eine bewährte und hochentwickelte Infrastruktur für Transport, Lagerung, Verteilung und Lagerung beim Endverbraucher (ca. 100 Jahre Weltentwicklung)-It there is a proven one and sophisticated infrastructure for transportation, storage, distribution and Storage at the end consumer (approx. 100 years of world development)
- –Es existiert eine bewährte und hochentwickelte Dieselmotorentechnik (ca. 100 Jahre Weltentwicklung) und Heizanlagentechnik (ca. 50 Jahre Weltentwicklung)-It there is a proven one and highly developed diesel engine technology (approx. 100 years of world development) and heating system technology (approx. 50 years of world development)
Die Gründe für die Wahl der Zementproduktion und nicht der Brandkalkproduktion, der Kohle-, Erdöl- oder Erdgasverbrennung als kohlendioxidliefenden Prozess sind folgende:The reasons for choosing cement production and not fire lime production, coal, petroleum or Natural gas combustion as a carbon dioxide-producing process is as follows:
- –Der Markt und die Verwendungsmöglichkeit für Zement ist viel größer als der Markt und die Verwendungsmöglichkeit für Brandkalk-The Market and the possible use for cement is much larger than the market and its uses for quicklime
- –Kalksteinvorkommen sind viel weiter verbreitet und leichter abbaubar als Kohle-, Erdöl- oder Erdgasvorkommen-Kalksteinvorkommen are much more common and more easily degradable than coal, petroleum or gas resources
- –Kohlendioxid in großen Mengen über weite Strecken zu transportieren ist unwirtschaftlich, denn man transportiert vor allem nutzlosen Sauerstoff (Für nur 14 Tonnen Diesel müssen 44 Tonnen Kohlendioxid transportiert werden)-Kohlendioxid in large Amounts over Transporting long distances is uneconomical because you primarily transports useless oxygen (for just 14 tons of diesel, 44 Tons of carbon dioxide are transported)
- –Da das Zementklinkerbrennen mit einem Teil des durch Elektrolyse erzeugten Sauerstoffes statt mit Luft erfolgen kann, wird das anfallende Kohlendioxid stickstofffrei, was Synthese- sowie energetische Vorteile hat–As the cement clinker burning with part of the Oxygen generated by electrolysis instead of air, the resulting carbon dioxide is nitrogen-free, which has synthetic and energetic advantages
- –Die Zementproduktion bietet die Möglichkeit, Nebenprodukte wie gebrauchten Fischer-Tropsch-Katalysator (kohlenwasserstoffhaltiges Eisenoxid), gebrauchten Reversen-Wassergas-Gleichgewichts-Katalysator (Aluminiumoxid) und höhere und niedriger siedende Abfallkohlenwasserstoffe der Fischer-Tropsch-Synthese stofflich und energetisch zu verwerten.-The Cement production offers the opportunity By-products such as used Fischer-Tropsch catalyst (containing hydrocarbons Iron oxide), used reverse water gas equilibrium catalyst (Alumina) and higher and lower-boiling waste hydrocarbons from the Fischer-Tropsch synthesis and utilize it energetically.
Erfindungsgemäß besteht die Anlage zur Herstellung von Diesel und Zement aus folgenden Teilanlagen mit folgenden Funktionen:According to the invention there is the plant for production of diesel and cement from the following subsystems with the following functions:
Teilanlage 1Unit 1
Ein Stand-der-Technik-Kernkraftwerk (z.B. analog KKW Isar 2) erzeugt Strom.A state-of-the-art nuclear power plant (e.g. analogue to Isar 2) generates electricity.
Teilanlage 2Unit 2
Mit dem Strom von Teilanlage 1 wird
mit Stand-der-Technik-Wasserelektrolyseanlagen (z.B. von Norsk Hydro
Electrolysers AS) Wasser in Wasserstoff und Sauerstoff zerlegt:
Teilanlage 3Part 3
Ein Stand-der-Technik-Zementwerk
erzeugt Zement und Kohlendioxid:
Teilanlage 4Unit 4
Ein Reverse-Wassergas-Gleichgewichts-Reaktor
wandelt das Kohlendioxid von Teilanlage 3 mit dem Wasserstoff von
Teilanlage 2 in Kohlenmonoxid um:
Ein geeigneter Katalysator wurde kürzlich zur Ausbeuteerhöhung für die Methanolsynthese nach dem CAMERE-Verfahren entwickelt.A suitable catalyst became recently to yield increase for the Methanol synthesis developed using the CAMERE process.
(Oh-Shim Joo and Kwang-Deog Jung in Bull. Korean Chem. Soc. 2003, Vol. 24, No 1, 86–90)(Oh-Shim Joo and Kwang-Deog Jung in Bull. Korean Chem. Soc. 2003, Vol. 24, No 1, 86-90)
Teilanlage 5Unit 5
Ein Stand-der-Technik-Fischer-Tropsch-Reaktor
setzt das Kohlenmonoxid von Teilanlage 4 mit Wasserstoff von Teilanlage
2 zu synthetischem Diesel um:
Geeignete Reaktoren sind von Firmen wie Syntroleum Corporation, ANGTL Company, Rentech Inc., Ivanhoe Energy, Shell oder Sasol Synthetic Fuels verfügbar, da dieser Prozess ein Teilprozess des GTL(gas to liquid)-Verfahrens ist.Suitable reactors are from companies such as Syntroleum Corporation, ANGTL Company, Rentech Inc., Ivanhoe Energy, Shell or Sasol Synthetic Fuels are available because of this process Sub-process of the GTL (gas to liquid) process is.
Bei der Verbrennung von 1 kg Diesel zu Kohlendioxid und Wasser wird eine Energie von 42 MJ frei. Das bedeutet, dass man zum Aufbau von 1 kg Diesel aus Kohlendioxid und Wasser auch 42 MJ benötigt. Da 1 kWh auch 3,6 MJ sind, benötigt man zum Aufbau von 1 kg Diesel aus Kohlendioxid und Wasser 11,7 kWh. Bei Kernkraftstromherstellungskosten von 2 Eurocent pro kWh errechnen sich Dieselherstellungskosten von 23,4 Eurocent pro kg Diesel.When burning 1 kg of diesel an energy of 42 MJ is released to carbon dioxide and water. The means that to build 1 kg of diesel from carbon dioxide and Water also needed 42 MJ. Since 1 kWh is also 3.6 MJ needed to build 1 kg of diesel from carbon dioxide and water 11.7 kWh. At nuclear power generation costs of 2 euro cents per kWh Diesel production costs are calculated at 23.4 euro cents per kg Diesel.
Da ein 1400-MW-Kernkraftwerk (wie Isar 2) jährlich 12,2 Mrd. kWh liefert, könnte man theoretisch mit einer solchen Anlage jährlich 1,04 Mio. Tonnen Diesel und 5,6 Mio. Tonnen Zement herstellen. Da der Wirkungsgrad der Wasserelektrolyse aber nur bei ca. 70% liegt und die Zementproduktion auch ca. 4 GJ pro Tonne Zement benötigt, sind jährlich ca. 600 000 Tonnen Diesel und ca. 3 Mio. Tonnen Zement realistisch.Because a 1400 MW nuclear power plant (like Isar 2) annually 12.2 billion kWh one theoretically produces 1.04 million tons of diesel annually with such a system and produce 5.6 million tons of cement. Because the efficiency of water electrolysis but is only around 70% and cement production is also around 4 GJ needed per ton of cement are yearly approx. 600,000 tons of diesel and approx. 3 million tons of cement realistic.
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Priority Applications (1)
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DE20320020U DE20320020U1 (en) | 2003-12-24 | 2003-12-24 | Installation for producing diesel and cement comprises a nuclear power station, a water electrolysis plant, a cement works, a reverse water gas balanced reactor and a Fischer-Tropsch reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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DE20320020U DE20320020U1 (en) | 2003-12-24 | 2003-12-24 | Installation for producing diesel and cement comprises a nuclear power station, a water electrolysis plant, a cement works, a reverse water gas balanced reactor and a Fischer-Tropsch reactor |
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DE20320020U1 true DE20320020U1 (en) | 2004-05-06 |
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DE20320020U Expired - Lifetime DE20320020U1 (en) | 2003-12-24 | 2003-12-24 | Installation for producing diesel and cement comprises a nuclear power station, a water electrolysis plant, a cement works, a reverse water gas balanced reactor and a Fischer-Tropsch reactor |
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Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006099573A1 (en) * | 2005-03-16 | 2006-09-21 | Fuelcor Llc | Systems, methods, and compositions for production of synthetic hydrocarbon compounds |
WO2007108014A1 (en) * | 2006-03-20 | 2007-09-27 | Cri Ehf | Process for producing liquid fuel from carbon dioxide and water |
DE102006034712A1 (en) * | 2006-07-27 | 2008-01-31 | Steag Saar Energie Ag | Method for reducing the CO2 emission of fossil-fired power plants |
GB2459430A (en) * | 2007-12-10 | 2009-10-28 | Neutral Carbon Ltd | Production of hydrocarbons from carbon dioxide |
EP2206762A1 (en) * | 2009-01-13 | 2010-07-14 | Areva | A system and a process for producing at least one hydrocarbon fuel from a carbonaceous material |
FR2947832A1 (en) * | 2009-07-09 | 2011-01-14 | Areva | PROCESS FOR THE PRODUCTION OF SYNTHETIC HYDROCARBONS FROM CARBONACEOUS MATERIALS |
WO2011070124A2 (en) | 2009-12-10 | 2011-06-16 | Fruitful Innovations B.V. | Improved catalytic process for reacting carbon dioxide with hydrogen |
US9249064B2 (en) | 2009-11-20 | 2016-02-02 | Cri, Ehf | Storage of intermittent renewable energy as fuel using carbon containing feedstock |
EP3196177A1 (en) | 2016-01-21 | 2017-07-26 | HeidelbergCement AG | Hydrogen as fuel in the manufacture of concrete |
DE102016209027A1 (en) * | 2016-05-24 | 2017-11-30 | Thyssenkrupp Ag | Plant network for the production of mineral building materials and a process for operating the plant network |
DE102016209028A1 (en) * | 2016-05-24 | 2017-11-30 | Thyssenkrupp Ag | Plant network for the production of mineral building materials and a process for operating the plant network |
EP3839015A1 (en) * | 2019-12-20 | 2021-06-23 | Holcim Technology Ltd | Method of processing exhaust gas |
US11738317B2 (en) | 2021-01-15 | 2023-08-29 | CRI, hf | Reactor for synthesizing methanol or other products |
-
2003
- 2003-12-24 DE DE20320020U patent/DE20320020U1/en not_active Expired - Lifetime
Cited By (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006099573A1 (en) * | 2005-03-16 | 2006-09-21 | Fuelcor Llc | Systems, methods, and compositions for production of synthetic hydrocarbon compounds |
US8168143B2 (en) * | 2005-03-16 | 2012-05-01 | Fuelcor, Llc | Systems, methods, and compositions for production of synthetic hydrocarbon compounds |
US8114916B2 (en) | 2005-03-16 | 2012-02-14 | Fuelcor, Llc | Systems, methods, and compositions for production of synthetic hydrocarbon compounds |
US8093305B2 (en) | 2005-03-16 | 2012-01-10 | Fuelcor, Llc | Systems, methods, and compositions for production of synthetic hydrocarbon compounds |
CN103059899A (en) * | 2005-03-16 | 2013-04-24 | 弗尔科有限责任公司 | Systems, methods, and compositions for production of synthetic hydrocarbon compounds |
KR101318966B1 (en) * | 2005-03-16 | 2013-10-17 | 퓨얼코어 엘엘씨 | System, methods, and compositions for production of synthetic hydrocarbon compounds |
US7863340B2 (en) | 2005-03-16 | 2011-01-04 | Fuelcor Llc | Systems, methods, and compositions for production of synthetic hydrocarbon compounds |
US8506910B2 (en) | 2006-03-20 | 2013-08-13 | Cri Ehf | Process and system for producing liquid fuel from carbon dioxide and water |
WO2007108014A1 (en) * | 2006-03-20 | 2007-09-27 | Cri Ehf | Process for producing liquid fuel from carbon dioxide and water |
US8198338B2 (en) | 2006-03-20 | 2012-06-12 | Cri Ehf | Process for producing liquid fuel from carbon dioxide and water |
DE102006034712A1 (en) * | 2006-07-27 | 2008-01-31 | Steag Saar Energie Ag | Method for reducing the CO2 emission of fossil-fired power plants |
GB2459430A (en) * | 2007-12-10 | 2009-10-28 | Neutral Carbon Ltd | Production of hydrocarbons from carbon dioxide |
WO2010081829A1 (en) * | 2009-01-13 | 2010-07-22 | Areva | A system and a process for producing at least one hydrocarbon fuel from a carbonaceous material |
EP2206762A1 (en) * | 2009-01-13 | 2010-07-14 | Areva | A system and a process for producing at least one hydrocarbon fuel from a carbonaceous material |
US8184763B2 (en) | 2009-01-13 | 2012-05-22 | Areva Sa | System and a process for producing at least one hydrocarbon fuel from a carbonaceous material |
FR2947832A1 (en) * | 2009-07-09 | 2011-01-14 | Areva | PROCESS FOR THE PRODUCTION OF SYNTHETIC HYDROCARBONS FROM CARBONACEOUS MATERIALS |
WO2011004122A3 (en) * | 2009-07-09 | 2011-04-07 | Areva | Process for producing synthetic hydrocarbons from carbonaceous materials |
US9000055B2 (en) | 2009-07-09 | 2015-04-07 | Areva | Process for producing synthetic hydrocarbons from carbonaceous materials |
US9249064B2 (en) | 2009-11-20 | 2016-02-02 | Cri, Ehf | Storage of intermittent renewable energy as fuel using carbon containing feedstock |
WO2011070124A2 (en) | 2009-12-10 | 2011-06-16 | Fruitful Innovations B.V. | Improved catalytic process for reacting carbon dioxide with hydrogen |
US8754269B2 (en) | 2009-12-10 | 2014-06-17 | Antecy B.V. | Catalytic process for reacting carbon dioxide with hydrogen |
EP3196177A1 (en) | 2016-01-21 | 2017-07-26 | HeidelbergCement AG | Hydrogen as fuel in the manufacture of concrete |
DE102016209027A1 (en) * | 2016-05-24 | 2017-11-30 | Thyssenkrupp Ag | Plant network for the production of mineral building materials and a process for operating the plant network |
DE102016209028A1 (en) * | 2016-05-24 | 2017-11-30 | Thyssenkrupp Ag | Plant network for the production of mineral building materials and a process for operating the plant network |
DE102016209027A9 (en) * | 2016-05-24 | 2018-01-18 | Thyssenkrupp Ag | Plant network for the production of mineral building materials and a process for operating the plant network |
EP3839015A1 (en) * | 2019-12-20 | 2021-06-23 | Holcim Technology Ltd | Method of processing exhaust gas |
WO2021124231A1 (en) * | 2019-12-20 | 2021-06-24 | Holcim Technology Ltd | Method of processing exhaust gas |
US11738317B2 (en) | 2021-01-15 | 2023-08-29 | CRI, hf | Reactor for synthesizing methanol or other products |
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