WO2005049498A2 - Water treatment system and method - Google Patents

Water treatment system and method Download PDF

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Publication number
WO2005049498A2
WO2005049498A2 PCT/US2004/037897 US2004037897W WO2005049498A2 WO 2005049498 A2 WO2005049498 A2 WO 2005049498A2 US 2004037897 W US2004037897 W US 2004037897W WO 2005049498 A2 WO2005049498 A2 WO 2005049498A2
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WO
WIPO (PCT)
Prior art keywords
water
point
storing
treated water
reservoir system
Prior art date
Application number
PCT/US2004/037897
Other languages
French (fr)
Other versions
WO2005049498A3 (en
Inventor
Evgeniya Freydina
Anil D. Jha
Frederick Wilkins
Aytac Sezgi
Reshma Madhusudan
Original Assignee
Usfilter Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Usfilter Corporation filed Critical Usfilter Corporation
Priority to EP04801042.5A priority Critical patent/EP1682451B1/en
Priority to ES04801042T priority patent/ES2837807T3/en
Priority to JP2006539922A priority patent/JP2007513749A/en
Publication of WO2005049498A2 publication Critical patent/WO2005049498A2/en
Publication of WO2005049498A3 publication Critical patent/WO2005049498A3/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/44Ion-selective electrodialysis
    • B01D61/52Accessories; Auxiliary operation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/44Ion-selective electrodialysis
    • B01D61/46Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/44Ion-selective electrodialysis
    • B01D61/54Controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J47/00Ion-exchange processes in general; Apparatus therefor
    • B01J47/02Column or bed processes
    • B01J47/06Column or bed processes during which the ion-exchange material is subjected to a physical treatment, e.g. heat, electric current, irradiation or vibration
    • B01J47/08Column or bed processes during which the ion-exchange material is subjected to a physical treatment, e.g. heat, electric current, irradiation or vibration subjected to a direct electric current
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/469Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/20Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/4602Treatment of water, waste water, or sewage by electrochemical methods for prevention or elimination of deposits
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/469Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
    • C02F1/4693Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis
    • C02F1/4695Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis electrodeionisation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/46115Electrolytic cell with membranes or diaphragms
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4612Controlling or monitoring
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4612Controlling or monitoring
    • C02F2201/46125Electrical variables
    • C02F2201/4613Inversing polarity
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/005Processes using a programmable logic controller [PLC]
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents

Definitions

  • the present invention relates generally to a system and method for treating a fluid and, more particularly, to a water treatment system incorporating an electrochemical device and a reservoir system with sensors and baffle plates for tailoring delivery of treated water to a point of use.
  • Water that contains hardness species such as calcium and magnesium may be undesirable for some uses in industrial, commercial and household applications.
  • the typical guidelines for a classification of water hardness are: zero to 60 milligrams per liter (mg/1) as calcium carbonate is classified as soft; 61 to 120 mg/1 as moderately hard; 121 to 180 mg/1 as hard; and more than 180 mg 1 as very hard.
  • Hard water can be softened or treated by removing the hardness ion species. Examples of systems that remove such species include those that use ion exchange beds. In such systems, the hardness ions become ionically bound to oppositely charged ionic species that are mixed on the surface of the ion exchange resin.
  • the ion exchange resin eventually becomes saturated with ionically bound hardness ion species and must be regenerated. Regeneration typically involves replacing the bound hardness species with more soluble ionic species, such as sodium chloride. The hardness species bound on the ion exchange resin are replaced by the sodium ions and the ion exchange resins are ready again for a subsequent water softening step.
  • Other systems have been disclosed. For example, Dosch, in U.S. Patent No. 3,148,687 teaches a washing machine including a water softening anangement using ion exchange resins. Similarly, Gadini et al., in International Application Publication No. WO00/64325, disclose a household appliance using water with an improved device for reducing the water hardness.
  • Electrodeionization is one process that may be used to soften water.
  • EDI is a process that removes ionizable species from liquids using electrically active media and an electrical potential to influence ion transport.
  • the electrically active media may function to alternately collect and discharge ionizable species, or to facilitate the transport of ions continuously by ionic or electronic substitution mechanisms.
  • EDI devices can include media having permanent or temporary charge and can be operated to cause electrochemical reactions designed to achieve or enhance performance. These devices also include electrically active membranes such as semi-permeable ion exchange or bipolar membranes.
  • Continuous electrodeionization is a process wherein the primary sizing parameter is the transport through the media, not the ionic capacity of the media.
  • a typical CEDI device includes alternating electroactive semi-permeable anion and cation exchange membranes. The spaces between the membranes are configured to create liquid flow compartments with inlets and outlets.
  • a transverse DC electrical field is imposed by an external power source using electrodes at the bounds of the membranes and compartments. Often, electrode compartments are provided so that reaction product from the electrodes can be separated from the other flow compartments. Upon imposition of the electric field, ions in the liquid are attracted to their respective counter-electrodes.
  • the volume within the ion-depleting compartments and, in some embodiments, within the ion-concentrating compartments also includes electrically active media.
  • the media may include intimately mixed anion and cation exchange resins.
  • the ion-exchange media typically enhances the transport of ions within the compartments and may participate as substrates for controlled electrochemical reactions.
  • Electrodeionization devices have been described by, for example, Giuffrida et al. in U.S. Patent Nos. 4,632,745, 4,925,541 and 5,211,823, by Ganzi in U.S. Patent Nos. 5,259,936 and 5,316,637, by Oren et al. in U.S. Patent No. 5,154,809 and by Kedem in U.S. Patent No. 5,240,579.
  • Giuffrida et al. in U.S. Patent Nos. 4,632,745, 4,925,541 and 5,211,823, by Ganzi in U.S. Patent Nos. 5,259,936 and 5,316,637, by Oren et al. in U.S. Patent No. 5,154,809 and by Kedem in U.S. Patent No. 5,240,579.
  • the present invention provides a storage system comprising a pressurized reservoir system having a first inlet fluidly connected to a point of entry and a second inlet fluidly connected to an electrochemical device, at least one conductivity sensor in the pressurized reservoir system and a distribution system fluidly connected to the pressurized reservoir system and to a point of use.
  • the present invention provides a water treatment system comprising a reservoir system fluidly connected to a point of entry and having a first baffle plate, a water treatment device fluidly connected to the reservoir system and a water distribution system fluidly connected to the reservoir system and a point of use.
  • the present invention provides a method for providing treated water.
  • the method can comprise storing water from a point of entry, removing at least a portion of any undesired species from the water in an electrochemical device to produce treated water, measuring at least one water property of the treated water, and transferring at least a portion of the treated water to a point of use according to the measured property.
  • the present invention provides an electrodeionization system comprising a reservoir system fluidly connected to a point of entry and having a water property sensor, an electrodeionization device fluidly connected to the reservoir system and a controller connected to the water property sensor for regulating a water flow from the reservoir system to a point of use.
  • the present invention provides a method for providing treated water.
  • the method can comprise storing water from a point of entry under a pressure that is above atmospheric pressure, removing at least a portion of any undesired species from the water in a water treatment device to produce treated water, measuring a property of the treated water, determining a difference between the property of the treated water to a set point and controlling an operating parameter of the electrochemical device based on the difference between the property of the treated water and the set point.
  • the present invention provides a method for facilitating water treatment.
  • the method can comprise providing a water treatment system comprising an electrochemical device that is fluidly connected to a reservoir system having a water property sensor and a controller that is connected to the water property sensor for regulating a water flow from the reservoir system to a point of use.
  • the treatment system is fluidly connectable to a point of entry and to the point of use.
  • the present invention provides a method for facilitating water treatment.
  • the method can comprise providing a water treatment system comprising a reservoir system having a baffle plate and an electrochemical device.
  • the reservoir system is fluidly connectable to a point of entry and to a water distribution system.
  • the present invention provides a water treatment system comprising means for storing water that is fluidly connected to a point of entry and an electrochemical device, means for determining a water property in the means for storing water and means for delivering the water to a point of use based on the water property.
  • the present invention provides a method for providing treated water.
  • the method can comprise storing water from a point of entry, removing at least a portion of any undesirable species from the water to produce treated water, storing at least a portion of the treated water and minimizing any mixing of the water from the point of entry and the treated water.
  • the present invention provides a method for providing treated water. The method can comprise storing water from a point of entry in a first zone of a reservoir system, removing at least a portion of any undesirable species from the water to produce treated water, and storing at least a portion of the treated water in a second zone of the reservoir system.
  • the present invention provides a method for purifying water.
  • the method can comprise storing water from a point of use, releasing any volatilizable material from the stored water, removing at least a portion of any undesirable species from the water in water treatment device to produce treated water, and storing at least a portion of the treated water.
  • the present invention provides a method for purifying water. The method can comprise storing water from a point of use, aerating the stored water, removing at least a portion of any undesirable species from the water in an electrodeionization device to produce treated water, and storing at least a portion of the treated water.
  • the present invention provides a water treatment system comprising a reservoir system fluidly connected to a point of entry and comprising a ventilation system, an electrodeionization device fluidly connected to the reservoir system, and a point of use fluidly connected to the reservoir system.
  • the present invention provides a water treatment system comprising a reservoir system fluidly connected to a point of entry and comprising an aeration system, a water treatment device fluidly connected to the reservoir system, and a point of use fluidly connected to the reservoir system.
  • FIG. 1 is a process flow diagram of a water treatment system showing a reservoir system having a set of sensors and a treatment device, such as an electrochemical treatment device, in accordance with one or more embodiments of the present invention
  • FIG. 2 is a schematic, sectional view through a typical electrodeionization device, illustrating the fluid and ion flow directions through depleting and concentrating compartments in accordance with one or more embodiments of the present invention
  • FIG. 3 is a schematic, sectional view through a vessel illustrating the use of baffle plates and sensors in accordance with one or more embodiments of the invention.
  • the present invention is directed to a fluid treatment system and methods for providing treated fluids in industrial, commercial and residential applications.
  • the present invention will be described using water as the fluid but should not be limited as such.
  • treated water it is believed that other fluids that can be treated according to the present invention.
  • a component of the system, or to a step of the method, of the present invention that adjusts, modifies, measures or operates on water or water property the present invention is believed to be applicable as well.
  • the fluid to be treated may be a fluid that is a mixture comprising water.
  • the fluid can be a liquid that comprises water.
  • the treatment system can provide purified, treated or softened water to a point of use by reducing a concentration of or removing at least a portion of any hardness-causing species contained in water from a water source, such as municipal water, well water, brackish water and water containing foulants.
  • a water source such as municipal water, well water, brackish water and water containing foulants.
  • Other applications of the system would be in the treatment and processing of foods and beverages, sugars, various industries, such as the chemical, pharmaceutical, food and beverage, wastewater treatments and power-generating industries.
  • the water treatment system typically includes at least one baffle plate in a reservoir system.
  • the water treatment system comprises at least one water property sensor for measuring at least one water property.
  • the water treatment system of the present invention typically receives water from the water source or a point of entry and treats the water containing at least some undesirable species before delivering the treated water to a point of use.
  • the treatment system typically has a reservoir system in line with a treatment device, which can comprise an electrochemical treatment device such as an electrodeionization device.
  • the treatment system in accordance with some embodiments of the present invention further comprises a sensor for measuring at least one property of the water or an operating condition of the treatment system.
  • the treatment system also includes a controller for adjusting or regulating at least one operating parameter of the treatment system or a component of the treatment system.
  • FIG. 1 shows a schematic flow diagram of a water treatment system according to one embodiment of the present invention.
  • the water treatment system 10 includes a reservoir system 12 fluidly connected, typically at an upstream end, to a water source or a point of entry 14 and to a treatment device such as an electrochemical device which can comprise an electrodeionization device 16, typically at a downstream end.
  • Water treatment system 10 typically includes a point of use 18, which is typically fluidly connected downstream of reservoir system 12.
  • water treatment system 10 also has a sensor 20 and a controller 22 for controlling or regulating power source 24 which provides power to electrodeionization device 16.
  • Electrodeionization device 16 typically removes undesirable species from water to be treated flowing from point of entry 14 to produce treated water for storage into reservoir system 12 and ultimate delivery to point of use 18.
  • Water treatment system 10 in certain embodiments further includes pretreatment system 28, which is typically fluidly connected upstream of reservoir system 12 or electrodeionization device 16. Moreover, water treatment system 10 typically also includes fluid control components, such as pump 30 and valve 32.
  • pressurized refers to a system or component that has a pressure, internal or applied, that is above atmospheric pressure. For example, a pressurized reservoir system has an internal pressure that is greater than atmospheric pressure.
  • Pressure in the pressurized reservoir system can be created by various methods and techniques, for example, by pressurizing the water with a water pump or by elevating the water source, thus creating head pressure.
  • the components, systems, or techniques of the present invention can incorporate or utilize any suitable water treatment or purification device or apparatus or technique that removes or at least reduces a concentration of any undesirable species in a fluid to be treated and is not necessarily limited to purifying or treating water with an electrodeionization device.
  • the treatment system can comprise a treatment device comprising at least one of a reverse osmosis device, a electrochemical device, an ultrafiltration device, a microfiltration device, and, in some cases, a distillation device.
  • FIG. 2 schematically shows a cross-sectional view of fluid and ion flow paths through one embodiment of an electrodeionization device in accordance with the present invention.
  • the electrodeionization module or device 16 includes ion-depleting (depleting) compartments 34 and ion-concentrating (concentrating) compartments 36, positioned between ion-depleting compartments 34.
  • Depleting compartments 34 are typically bordered by an anolyte compartment 38 and a catholyte compartment 40.
  • end blocks (not shown) are positioned adjacent to end plates (not shown) to house an anode 42 and a cathode 44 in their respective compartments.
  • the compartments include cation-selective membranes 46 and anion-selective membranes 48, which are typically peripherally sealed to the periphery of both sides of the compartments.
  • the cation-selective membranes and anion-selective membranes are typically comprised of an ion exchange powder, a polyethylene powder binder and a glycerin lubricant.
  • the cation- and anion-selective membranes are typically heterogeneous polyolefin-based membranes, which are typically extruded by a thermoplastic process using heat and pressure to create a composite sheet.
  • the present invention contemplates the use of homogenous membranes as well as combinations of homogeneous and heterogeneous membranes.
  • Suitable ion-selective membranes include, for example, web supported using styrene-divinyl benzene with sulphonic acid or quaternary ammonium functional groups, web supported using styrene-divinyl benzene in a polyvinylidene fluoride binder, and unsupported-sulfonated styrene and quarternized vinyl benzyl amine grafts on polyethylene sheet.
  • Concentrating compartments 36 are typically filled with cation exchange resin 50 and depleting compartments 34 are typically filled with cation exchange resin 50 and anion exchange resin 52.
  • the cation exchange and anion exchange resins can be ananged in layers within any of the depleting, concentrating and electrode compartments so that a number of layers in a variety of anangements can be assembled.
  • Other embodiments are believed to be within the scope of the invention including, for example, the use of mixed bed ion exchange resins in any of the ion-depleting, concentrating and electrode compartments, the use of inert resin between layer beds of anionic and cationic exchange resins, the use of various types and anangements of anionic and cationic resins including, but not limited to, those described by DiMascio et al., in U.S. Patent No. 5,858,191.
  • a liquid to be treated 54 typically from an upstream water source entering the treatment system at point of entry 14, having dissolved cationic and anionic components, including hardness ion species, is introduced into ion-depleting compartments 34 through manifold 60, wherein the cationic components are attracted to the cation exchange resin 50 and the anionic components are attracted to the anion exchange resin 52.
  • Cationic components can migrate through cation-selective membrane 46 into adjacent concentrating compartment 36.
  • Anion-selective membrane 48 positioned on the opposite side of concentrating compartment 36, can prevent migration into adjacent compartments, thereby trapping the cationic components in the concentrating compartment.
  • anionic components can migrate through the ion-selective membranes, but in a direction that is typically opposite or counter relative to the migration direction of the cationic components.
  • Anionic components can migrate through anion-selective membrane 48, from ion-depleting compartment 34, into adjacent concentrating compartment 36.
  • Cation-selective membrane 46 positioned on the other side of concentrating compartment 36, can prevent further migration, thus effectively trapping anionic components in the ion-concentrating compartment.
  • the applied electric field on electrodeionization device 16 can create a polarization phenomenon, which leads to the dissociation of water into hydrogen and hydroxyl ions.
  • the hydrogen and hydroxyl ions regenerate the ion exchange resins 50 and 52 in depleting compartments 34, so that removal of dissolved ionic components can occur continuously and without a separate step for regenerating exhausted ion exchange resins because of the ionic species migration.
  • the applied electric field across electrodeionization device 16 is typically a direct cunent.
  • an alternating cunent may be used, provided that there is a potential difference between electrodes that is sufficient to attract cationic and anionic species to the respective attracting electrodes.
  • an alternating cunent may be rectified, for example, by using a diode or a bridge rectifier, to convert an alternating cunent to a pulsating direct cunent that provides a potential gradient across the electrodeionization device.
  • the electroactive media, the ion exchange resins 50 and 52, typically utilized in depleting compartments 34, can have a variety of functional groups on their surface regions, such as tertiary, alkyl amino groups and dimethyl ethanolamine. These materials can also be used in combinations with ion exchange resin materials having various functional groups on their surface regions, such as quaternary ammonium groups. Other types of electroactive media can also be utilized. Examples of such include, but are not limited to, electroactive fibers.
  • Reservoir system 12 can store or accumulate water from point of entry 14 or a water source and can also serve to store treated water from product stream 56 from electrodeionization device 16 and provide water, typically treated water or treated water mixed with water from point of entry 14 to point of use 18 through a distribution system.
  • reservoir system 12 can be pressurized with a pressure that is above atmospheric pressure.
  • reservoir system 12 comprises a vessel or a vessel that has inlets and outlets for fluid flow such as an inlet 62 and an outlet 64.
  • Inlet 62 is typically fluidly connected to point of entry 14 and outlet 64 is typically fluidly connected to a water distribution system or a point of use 18.
  • Reservoir system 12 can have several vessels or vessels having several inlets positioned at various locations on each vessel.
  • outlet 64 may be positioned on each vessel at various locations depending on, among other things, demand or flow rate to point of use 18, capacity or efficiency of electrodeionization device 16 and capacity or hold-up of reservoir system 12.
  • Reservoir system 12 can further comprise various components or elements that perform desirable functions or avoid undesirable consequences.
  • reservoir system 12 can have a plurality of vessels having internal components, such as baffle plates, generally refened to as baffles, that are positioned to disrupt any internal fluid flow cunents within the vessels of reservoir system 12.
  • reservoir system 12 has a heat exchanger for heating or cooling the fluid.
  • reservoir system 12 can comprise a vessel with a heating coil, which can have a heating fluid at an elevated temperature relative to the temperature of the fluid in the vessel.
  • the heating fluid may be hot water in closed-loop flow with a heating unit operation such as a furnace so that the heating fluid temperature is raised in the furnace and the heating fluid temperature is lowered in the vessel because of heat transfer to the vessel fluid.
  • auxiliary or additional components include, but are not limited to, pressure relief valves designed to relieve internal pressure of any vessels and avoid or at least reduce the likelihood of vessel rupture and thermal expansion tanks that are suitable for maintaining a desired operating pressure.
  • the size and capacity of a thermal expansion tank will depend on one or more factors including, but not limited to, the total volume of water, the operating temperature and pressure of the reservoir system.
  • reservoir system 12 is typically comiected downstream of point of entry
  • Electrode 14 and fluidly connected in-line, such as in a recirculation loop, with electrodeionization device 16.
  • water from point of entry 14 can flow into inlet 62 and can mix with the bulk water contained within reservoir system 12.
  • Bulk water can exit reservoir system 12 through outlet 64 and can be directed to point of use 18 or through pump 30 into electrodeionization device 16 for treatment or removal of any undesirable species.
  • Treated water leaving electrodeionization device 16 may mix with water from point of entry 14 and enter reservoir system 12 through inlet 62. In this way, a loop can be formed or defined between reservoir system 12 and electrodeionization device 16 and feedwater from point of entry 14 can replenish water demand created by and flowing to point of use 18.
  • Point of entry 14 typically provides water from a water source or connects the water source to the water treatment system.
  • the water source can be a potable water source, such as municipal water or well water or it can be from a brackish or saltwater source.
  • a pretreatment system purifies the water so that it is suitable for human consumption before reaching point of entry 14.
  • the water typically contains dissolved salts or ionic or ionizable species including sodium, chloride, calcium ions, magnesium ions, carbonates, sulfates or other insoluble or semi-soluble species or dissolved gases, such as silica and carbon dioxide.
  • the water can contain additives, such as fluoride, chlorate and bromate species.
  • point of entry 14 maybe the point of entry for an industrial, commercial or household setting.
  • the treatment system can comprise at least two vessels or two zones in one or more vessels, each of which can be, at least partially, fluidly isolated from the other.
  • the treatment system can comprise two vessels fluidly connected to a point of entry and to one or more treatment devices.
  • the two vessels can be fluidly isolated from each other by conduits and valves so that a first vessel can be placed in service with one or more treatment devices while a second vessel can be removed from service for, for example, maintenance or cleaning.
  • water treatment system 10 can include a water distribution system, which in turn can connect to a point of use.
  • the water distribution system may comprise components that are fluidly connected to provide water, typically treated water, from reservoir system 12 to point of use 18.
  • the water distribution system may comprise any anangement of pipes, valves, tees, pumps and manifolds to provide water from reservoir system 12 to one or several points of use 18 or to any component of water treatment system 10.
  • the water distribution system is a water distribution system in a commercial, industrial or household setting that provides potable water to several points of use.
  • Point of use 18 is typically any device or appliance that requires or demands water.
  • point of use 18 can be an appliance, such as a washing machine or a dishwasher, or can be a faucet serving to provide water to a kitchen sink or a showerhead.
  • point of use 18 comprises a system for providing water suitable for household or residential use.
  • water treatment system 10 also comprises a sensor, typically a water property sensor, which measures at least one physical property of the water in water treatment system 10.
  • sensor 20 can be a device that can measure turbidity, water conductivity, pH, temperature, pressure, flow rate or composition.
  • Sensor 20 can be installed or positioned within water treatment system 10, or any component thereof, to measure a water property or used in combination with one or more sensors to indicate the water quality in water treatment system 10.
  • sensor 20 can be a water conductivity sensor installed in reservoir system 12 so that sensor 20 measures the conductivity of the water, which can indicate the quality of the water available for service in point of use 18.
  • water treatment system 10 has multiple sensors, for example, a combination of any of pH, temperature, pressure and flow rate sensors.
  • sensor 20 may comprise a series or a set of sensors in reservoir system 12. The series or set of sensors may be ananged and connected to controller 22 so that the water quality is monitored, intennittently or continuously, through controller 22, and, in some embodiments, the operation of water treatment system 10 can be optimized as described below.
  • Other embodiments of the present invention can comprise a combination of sets of sensors in various locations throughout water treatment system 10.
  • sensor 20 can be a flow sensor measuring a flow rate to a point of use 18 and further include any of a nephelometer, pH, temperature and pressure sensor monitoring the operating condition of water treatment system 10.
  • water treatment system 10 may further comprise a pretreatment system 28 designed to remove a portion of any undesirable species from the water before the water is introduced to, for example, reservoir system 12 or the electrodeionization device 16.
  • pretreatment systems include, but are not limited to, reverse osmosis devices, which are typically used to desalinate brackish or salt water. Carbon or charcoal filter may be necessary to remove at least a portion of any chlorine, including active chlorine, or any species that may foul or interfere with the operation of electrodeionization device 16.
  • pretreatment system 28 can comprise any apparatus or device that removes or at least renders inactive any microorganism such as bacteria that may be present in one or more components of the treatment system.
  • a pretreatment apparatus may be disposed upstream of the electrochemical device and/or the reservoir.
  • suitable devices that can render bacteria at least partially inactive include devices that utilize ozone and/or actinic radiation.
  • bacterial inactivating devices be installed or utilized at or near a point of use so that fluids such as water delivered to a point of use can be essentially disinfected.
  • Other types of pre and/or post treatment systems can utilize microfiltration and/or ultrafiltration techniques.
  • Pretreatment system 28 may be positioned anywhere within water treatment system
  • pretreatment system 28 can be positioned upstream of reservoir system 12 or downstream of system 12 but upstream of electrodeionization device 16 so that at least some chlorine species are retained in reservoir system 12 but are removed before the water enters electrodeionization device 16.
  • the treatment system can comprise systems and techniques that permit disinfection of any component of the treatment system.
  • the treatment system can be exposed to a disinfecting solution or a disinfectant.
  • the disinfectant can be any material that can destroy or at least renders inactive a portion of any microorganisms, such as bacteria, present in any component or subsystem of the treatment system.
  • Examples of a disinfectant can include any base, acid or sanitizer, such as a halogen or halogen-donating compounds, peroxygen or peroxygen-donating compounds that destroys or renders bacteria inactive.
  • the disinfectant can be introduced into the treatment system by any suitable device or technique.
  • the disinfectant can be ' introduced into a water treatment system by introducing chlorine into the reservoir system. Introducing chlorine can be performed by injection of a hypochlorate species from a disinfectant reservoir fluidly connectable to any suitable portion of the treatment system.
  • the chlorinated water can be further circulated through at least a portion of the treatment system thereby exposing wetted portions of the system to the disinfectant.
  • water treatment system 10 further comprises a controller 22 that is capable of monitoring and regulating the operating conditions of water treatment system 10 and its components.
  • Controller 22 typically comprises a microprocessor-based device, such as a programmable logic controller (PLC) or a distributed control system that receives or sends input and output signals to components of water treatment system 10.
  • PLC programmable logic controller
  • controller 22 can be a PLC that sends a signal to power source 24, which supplies power to electrodeionization device 16 or can provide a signal to a motor control center that provides power to pumps 30.
  • controller 22 regulates the operating conditions of water treatment system 10 in open-loop or closed-loop control scheme.
  • controller 22 in open-loop control, can provide signals to the water treatment system such that water is treated without measuring any operating condition.
  • controller 22 may control the operating conditions in closed-loop control so that operating parameters may be adjusted depending on an operating condition measured by, for example, sensor 20.
  • controller 22 may further comprise a communication system such as a remote communication device for transmitting or sending any of measured operating condition or operating parameter to a remote station.
  • Controller 22 can provide a signal that actuates any valves 32 in water treatment system 10 so that fluid flow in water treatment system 10 can be adjusted based on a variety of parameters including, but not limited to, the quality of water from point of entry 14, the quality of water to point of use 18, the demand or quantity of water to point of use 18, the operating efficiency or capacity of electrodeionization device 16, or any of a variety of operating conditions, such as the water conductivity, composition, pH, turbidity, alkalinity, temperature, pressure and flow rate.
  • controller 22 can receive a signal from sensor 20, or a set of signals from a combination of sensors or sets of sensors, so that controller 22 can be capable of monitoring the operating parameters of water treatment system 10.
  • sensor 20 can be a water conductivity sensor positioned within reservoir system 12 so that the water conductivity in reservoir system 12 can be monitored by controller 22.
  • Controller 22 can, based on the signals from, for example, sensor 20, control power source 24, which provides an electric field to electrodeionization device 16. In operation, controller 22 can increase, decrease or otherwise adjust the voltage, cunent, or both, supplied to electrodeionization device 16. In another embodiment of the present invention, controller 22 may reverse the direction of the applied field from power source 24 to electrodeionization device 16 according to a predetermined schedule or according to an operating condition, such as the water quality or any other operating parameter measured by sensor 20.
  • controller 22 can be configured to reverse the polarity of the electric field applied to electrodeionization device 16 when a measured parameter reaches a set point.
  • the present invention provides a controller that is capable of increasing, decreasing or otherwise adjusting a cycle time based on, for example, the measured water properties, such as but not limited to, total dissolved solids, water quality, including conductivity.
  • the cycle of electrodeionization device 16 includes the period between reversals in the electric field, along with the associated changes, reversals or substitution of fluid flows within electrodeionization device 16.
  • Polarity reversal which has been described by, for example, Giuffrida et al., in U.S. Patent No. 4,956,071, is considered to be within the scope of the present invention.
  • Controller 22 may be configured or configurable by programming or maybe self-adjusting such that it is capable of maximizing any of the service life and the efficiency of or reducing the operating cost of water treatment system 10.
  • controller 22 can comprise a microprocessor having user-selectable set points or self-adjusting set points that adjusts the applied voltage and cunent or both to electrodeionization device 16, the flow rate through the ion-concentrating and ion-depleting compartments of the electrodeionization device or the flow rate to discharge to drain 26 from the electrodeionization device or the pretreatment system or both.
  • the water treatment system stores water from point of entry 18, which is typically connected to a water source and typically at a pressure that is above atmospheric pressure, in a first zone of reservoir system 12.
  • Reservoir system 12 can be fluidly connected to a water distribution system that supplies treated water to point of use 18.
  • Water treatment system 10 can have an electrochemical device such as an electrodeionization device 16 that purifies or treats water from point of entry 14 by removing at least a portion of any undesirable species to produce treated water that is introduced into reservoir system 12 in a second zone of reservoir system 12.
  • First and second zones of reservoir system 12 can be monitored by at least one water quality sensor, more preferably, a set of water quality sensors connected to controller 22, which, in turn, can adjust an operating parameter of the electrochemical device.
  • controller 22 can monitor the first and second zones of reservoir system 12 and regulate the operation of the electrochemical device depending on any of the properties measured by a sensor or a set of sensors 20 which measures the water properties of the water in the first and second zones.
  • the term "zone" refers to a volume, typically a volume of liquid in the reservoir system.
  • a reservoir system can have one container or vessel having two or more zones defined as portions of the vessel containing conesponding volumes.
  • the reservoir system can have two or more zones wherein each zone is defined by a conesponding, separate vessel.
  • controller 22 through sensor or set of sensors 20 or combinations thereof, can monitor or measure at least one water property of the water in the first and second zones of reservoir system 12 and also measure a flow rate flowing into at least one point of use 18 and can adjust an operating parameter of electrodeionization device 16 based on the measured properties.
  • sensor 20 measures at least one property of at least one of the water from the point of entry and the treated water. For example, when an increased flow rate is measured to point of use 18, controller 22 can adjust an operating parameter, such as an applied voltage or cunent, of electrodeionization device 16 to treat water to compensate for any additional demand flowing into point of use 18.
  • controller 22 can adjust an operating parameter of electrodeionization device 16 depending on the volume in the first and second zones of reservoir system 12 and the historical demand, e.g. water demand, required by point of use 18.
  • reservoir system 12 has partitions that separate freated water from untreated water or mixtures of treated water with untreated water.
  • Controller 22 through measurement sensors 20 and valves 32, can control the flow of treated, raw or mixed water to a particular point of use, depending on specific needs of that point of use. For example, if point of use 18 requires softened water, then controller 22 can open one or more valves 32 in the water distribution system so that only treated water is provided to point of use 18.
  • controller 22 would isolate treated water in reservoir system 12 and allow raw water to flow through the water distribution system to point of use 18 by opening the appropriate valves.
  • reservoir system 12 is capable of isolating purified or treated water from raw water into zones by use of techniques or structures such as partitions or baffles or by utilizing separate vessels which may be isolated from each other.
  • controller 22 can control one or more valves 32 so that raw water can be introduced into electrodeionization device 16 and treated water from the electrodeionization device can be transfened to the zone or vessel of treated water.
  • controller 22 can supply water to point of use 18 depending on the requirements of point of use 18 in a similar fashion as described above.
  • the fluid volumes of the first and second zones can be adjusted depending on several factors including, for example, the demand by a point of use, the operating efficiency of the electrodeionization device and the water property of the water in the zones.
  • the system can also comprise aeration devices, which can introduce a gas, such as air, and ventilation devices, to effect dissolution of air and/or to volatilize or purge undesirable species, such as compounds that can affect the taste of water. Any unit operation that permits mass transfer to and from the fluid, such as water, can be utilized in accordance with the techniques of the present invention.
  • aerating device examples include, but are not limited to bubblers and perforated tubes or lines submerged in fluid to be aerated, such as treated water or water from a point of use.
  • aeration can be performed by exposing the fluid to be aerated in an open air channel having, preferably, features such as
  • controller 22 can calculate a control parameter that can be used to adjust or vary a control signal to a component of the water treatment system. For example, controller 22 can calculate a
  • LSI Langelier Saturation Index
  • Calculated LSI can then be used in another or the same control loop, in the same or another controller, as an input variable that can be compared to a set-point and generate an output signal that actuates, adjusts or otherwise regulates a component of the water treatment system.
  • LSI can be calculated according to, for example, ASTM D 3739.
  • the treated water such as the softened water, has a low LSI so that it has a low tendency to form scale.
  • low LSI water has a LSI of about less than 2, preferably, less than about 1, and more preferably, less than about zero, hi another embodiment of the present invention, the treated water has a low conductivity that is less than about 300 ⁇ S/cm, preferably less than about 220 ⁇ S/cm and more preferably, less than about 200 ⁇ S/cm.
  • controller 22 can regulate the operation of the water treatment system by incorporating adaptive or predictive algorithms, which are capable of monitoring demand and water quality and can adjust the operation of the electrochemical device, such as increasing or decreasing the applied voltage or the period between electric field reversals of electrodeionization device 16.
  • controller 22 can be predictive in anticipating higher demand for treated water during early morning hours in a residential application to supply point of use 18 serving as a showerhead. Controller 22 can incorporate dead band control to reduce the likelihood of unstable on/off control or chattering.
  • Dead band refers to the range of signal outputs that a sensor provides without necessarily triggering a responsive control signal. The dead band may reside, in some embodiments of the invention, intrinsically in the sensor or may be programmed as part of the control system, or both. Dead band control can avoid unnecessary intermittent operation by smoothing out any measurement excursions. Such control techniques can prolong the operating life or mean time before failure of the components of water treatment system 10. Other techniques that can be used include the use of voting, time-smoothing or time-averaging measurements or combinations thereof.
  • stream 58 to auxiliary use can provide additional or secondary benefits.
  • stream 58 rather than going to drain 26, may be used to provide irrigating water to any residential, commercial or industrial use, such as for irrigating, for recycling or for recovery of collected or concentrated salts.
  • the present invention can provide a vessel, or a plurality of vessels, having a plurality of outlet ports, each of which can be connected to a water distribution system.
  • the plurality of outlets can permit the selective delivery of water to any point of use.
  • the plurality of outlets can permit the system to deliver water having a specific or predetermined water quality to a specific point of use.
  • water having low conductivity can be delivered to a point of use, such as a shower, that does requires higher quality water.
  • a point of use such as a shower
  • Such a system can also accommodate delivery of hard water to a point of use that is insensitive to water hardness.
  • Sensors can measure the water conductivity as an indication of water quality.
  • the control system can regulate valves or pumps, or both, in, for example, the distribution system, to provide water having the appropriate or closest water quality that conesponds to the water quality requirement of the point of use.
  • FIG. 3 is a schematic illustration of a reservoir system that can be used in the water treatment system of the present invention.
  • the reservoir system 12 has a vessel 13 with an inlet 62, typically fluidly connected to a point of entry (not shown), and an outlet 64, typically fluidly connected to a point of use (not shown).
  • Vessel 13 has a second inlet 63 that is fluidly connected to an electrodeionization device (not shown).
  • Vessel 13 has at least one baffle 66, which can be ananged in a variety of configuration including, for example, offset and rotated anangements or combinations thereof.
  • baffle 66 can be single, double or triple segmental baffles or combinations thereof.
  • At least one water property sensor 20 can be installed on vessel 13 for measuring a water property such as, pressure, temperature, pH and conductivity.
  • Sensor 20 can be installed in a variety of configurations. As illustrated, three sensors 20a, 20b and 20c that measure the conductivity of the water are installed along the height of vessel 13. In operation, each sensor 20a, 20b and 20c provides a signal to a controller (not shown), which conesponds to the measured water conductivity.
  • the controller can be configured to average the measurements or can monitor any difference in water conductivity. In the former, the controller regulates the operating parameters of the electrodeionization device, which softens the water flowing from outlet 64 to produce treated water returning into second inlet 63 based on the average measured conductivity.
  • the controller monitors the interface between the treated and raw water in vessel 13 and regulates the operation of the electrodeionization device as necessary to provide treated water to the point of use. For example, before the interface 68 between raw and treated water, as measured by the difference in conductivity, reaches sensor 20b, the controller regulates the operation of the electrodeionization device to treat water at a first operating condition. If demand for treated water results in bringing interface 68 between sensor 20b and 20c, then the controller can regulate the electrodeionization device at a second operating condition that treats water at a faster rate or removes undesirable species at a faster rate. In this way, constructive use of baffles and sensor anangement can optimize the operation of the water treatment system and components thereof.

Abstract

A water treatment system provides treated or softened water to a point of use by removing a portion of any hardness-causing species contained in water from a point of entry coming from a water source, such as municipal water, well water, brackish water and water containing foulants. The water treatment system typically treats the water containing at least some undesirable species before delivering the treated water to a point of use. The water treatment system has a reservoir system in line with an electrochemical device such as an electrodeionization device. The water treatment system has a sensor or a set of sensors for measuring at least one property of the water or an operating condition of the treatment system. The water treatment system also has a controller for adjusting or regulating at least one operating parameter of the treatment system or a component of the water treatment system to optimize the operation and performance of the system or components of the system to supply water tailored to quality requirements.

Description

WATER TREATMENT SYSTEM AND METHOD
BACKGROUND OF THE INVENTION
1. Field of the Invention The present invention relates generally to a system and method for treating a fluid and, more particularly, to a water treatment system incorporating an electrochemical device and a reservoir system with sensors and baffle plates for tailoring delivery of treated water to a point of use.
2. Description of Related Art Water that contains hardness species such as calcium and magnesium may be undesirable for some uses in industrial, commercial and household applications. The typical guidelines for a classification of water hardness are: zero to 60 milligrams per liter (mg/1) as calcium carbonate is classified as soft; 61 to 120 mg/1 as moderately hard; 121 to 180 mg/1 as hard; and more than 180 mg 1 as very hard. Hard water can be softened or treated by removing the hardness ion species. Examples of systems that remove such species include those that use ion exchange beds. In such systems, the hardness ions become ionically bound to oppositely charged ionic species that are mixed on the surface of the ion exchange resin. The ion exchange resin eventually becomes saturated with ionically bound hardness ion species and must be regenerated. Regeneration typically involves replacing the bound hardness species with more soluble ionic species, such as sodium chloride. The hardness species bound on the ion exchange resin are replaced by the sodium ions and the ion exchange resins are ready again for a subsequent water softening step. Other systems have been disclosed. For example, Dosch, in U.S. Patent No. 3,148,687 teaches a washing machine including a water softening anangement using ion exchange resins. Similarly, Gadini et al., in International Application Publication No. WO00/64325, disclose a household appliance using water with an improved device for reducing the water hardness. Gadini et al. teach of a household appliance having a control system, a water supply system from an external source and a softening system with an electrochemical cell. Electrodeionization (EDI) is one process that may be used to soften water. EDI is a process that removes ionizable species from liquids using electrically active media and an electrical potential to influence ion transport. The electrically active media may function to alternately collect and discharge ionizable species, or to facilitate the transport of ions continuously by ionic or electronic substitution mechanisms. EDI devices can include media having permanent or temporary charge and can be operated to cause electrochemical reactions designed to achieve or enhance performance. These devices also include electrically active membranes such as semi-permeable ion exchange or bipolar membranes. Continuous electrodeionization (CEDI) is a process wherein the primary sizing parameter is the transport through the media, not the ionic capacity of the media. A typical CEDI device includes alternating electroactive semi-permeable anion and cation exchange membranes. The spaces between the membranes are configured to create liquid flow compartments with inlets and outlets. A transverse DC electrical field is imposed by an external power source using electrodes at the bounds of the membranes and compartments. Often, electrode compartments are provided so that reaction product from the electrodes can be separated from the other flow compartments. Upon imposition of the electric field, ions in the liquid are attracted to their respective counter-electrodes. The adjoining compartments, bounded by the electroactive anion permeable membrane facing the anode and the electroactive cation membrane facing the cathode, typically become ionically depleted and the compartments, bounded by the electroactive cation permeable membrane facing the anode and the electroactive anion membrane facing the cathode, typically become ionically concentrated. The volume within the ion-depleting compartments and, in some embodiments, within the ion-concentrating compartments, also includes electrically active media. In CEDI devices, the media may include intimately mixed anion and cation exchange resins. The ion-exchange media typically enhances the transport of ions within the compartments and may participate as substrates for controlled electrochemical reactions. Electrodeionization devices have been described by, for example, Giuffrida et al. in U.S. Patent Nos. 4,632,745, 4,925,541 and 5,211,823, by Ganzi in U.S. Patent Nos. 5,259,936 and 5,316,637, by Oren et al. in U.S. Patent No. 5,154,809 and by Kedem in U.S. Patent No. 5,240,579. SUMMARY OF THE INVENTION
In one aspect, the present invention provides a storage system comprising a pressurized reservoir system having a first inlet fluidly connected to a point of entry and a second inlet fluidly connected to an electrochemical device, at least one conductivity sensor in the pressurized reservoir system and a distribution system fluidly connected to the pressurized reservoir system and to a point of use. In another embodiment, the present invention provides a water treatment system comprising a reservoir system fluidly connected to a point of entry and having a first baffle plate, a water treatment device fluidly connected to the reservoir system and a water distribution system fluidly connected to the reservoir system and a point of use. In another embodiment, the present invention provides a method for providing treated water. The method can comprise storing water from a point of entry, removing at least a portion of any undesired species from the water in an electrochemical device to produce treated water, measuring at least one water property of the treated water, and transferring at least a portion of the treated water to a point of use according to the measured property. In another embodiment, the present invention provides an electrodeionization system comprising a reservoir system fluidly connected to a point of entry and having a water property sensor, an electrodeionization device fluidly connected to the reservoir system and a controller connected to the water property sensor for regulating a water flow from the reservoir system to a point of use. In another aspect, the present invention provides a method for providing treated water. The method can comprise storing water from a point of entry under a pressure that is above atmospheric pressure, removing at least a portion of any undesired species from the water in a water treatment device to produce treated water, measuring a property of the treated water, determining a difference between the property of the treated water to a set point and controlling an operating parameter of the electrochemical device based on the difference between the property of the treated water and the set point. In another embodiment, the present invention provides a method for facilitating water treatment. The method can comprise providing a water treatment system comprising an electrochemical device that is fluidly connected to a reservoir system having a water property sensor and a controller that is connected to the water property sensor for regulating a water flow from the reservoir system to a point of use. The treatment system is fluidly connectable to a point of entry and to the point of use. In another embodiment, the present invention provides a method for facilitating water treatment. The method can comprise providing a water treatment system comprising a reservoir system having a baffle plate and an electrochemical device. The reservoir system is fluidly connectable to a point of entry and to a water distribution system. In another embodiment, the present invention provides a water treatment system comprising means for storing water that is fluidly connected to a point of entry and an electrochemical device, means for determining a water property in the means for storing water and means for delivering the water to a point of use based on the water property. In another aspect, the present invention provides a method for providing treated water. The method can comprise storing water from a point of entry, removing at least a portion of any undesirable species from the water to produce treated water, storing at least a portion of the treated water and minimizing any mixing of the water from the point of entry and the treated water. In yet another embodiment, the present invention provides a method for providing treated water. The method can comprise storing water from a point of entry in a first zone of a reservoir system, removing at least a portion of any undesirable species from the water to produce treated water, and storing at least a portion of the treated water in a second zone of the reservoir system. In another aspect, the present invention provides a method for purifying water. The method can comprise storing water from a point of use, releasing any volatilizable material from the stored water, removing at least a portion of any undesirable species from the water in water treatment device to produce treated water, and storing at least a portion of the treated water. In another aspect, the present invention provides a method for purifying water. The method can comprise storing water from a point of use, aerating the stored water, removing at least a portion of any undesirable species from the water in an electrodeionization device to produce treated water, and storing at least a portion of the treated water. In another aspect, the present invention provides a water treatment system comprising a reservoir system fluidly connected to a point of entry and comprising a ventilation system, an electrodeionization device fluidly connected to the reservoir system, and a point of use fluidly connected to the reservoir system. In another aspect, the present invention provides a water treatment system comprising a reservoir system fluidly connected to a point of entry and comprising an aeration system, a water treatment device fluidly connected to the reservoir system, and a point of use fluidly connected to the reservoir system. Other advantages, novel features and objects of the invention will become apparent from the following detailed description of the invention when considered in conjunction with the accompanying drawings, which are schematic and are not intended to be drawn to scale. In the figures, each identical or substantially similar component that is illustrated in various figures is represented by a single numeral or notation. For purposes of clarity, not every component is labeled in every figure, nor is every component of each embodiment of the invention shown where illustration is not necessary to allow those of ordinary skill in the art to understand the invention.
BRIEF DESCRIPTION OF THE DRAWINGS
Prefened, non-limiting embodiments of the present invention will be described by way of example and with reference to the accompanying drawings, in which: FIG. 1 is a process flow diagram of a water treatment system showing a reservoir system having a set of sensors and a treatment device, such as an electrochemical treatment device, in accordance with one or more embodiments of the present invention; FIG. 2 is a schematic, sectional view through a typical electrodeionization device, illustrating the fluid and ion flow directions through depleting and concentrating compartments in accordance with one or more embodiments of the present invention; and FIG. 3 is a schematic, sectional view through a vessel illustrating the use of baffle plates and sensors in accordance with one or more embodiments of the invention.
DETAILED DESCRIPTION OF THE INVENTION
The present invention is directed to a fluid treatment system and methods for providing treated fluids in industrial, commercial and residential applications. The present invention will be described using water as the fluid but should not be limited as such. For example, where reference is made to treated water, it is believed that other fluids that can be treated according to the present invention. Moreover, where reference is made to a component of the system, or to a step of the method, of the present invention that adjusts, modifies, measures or operates on water or water property, the present invention is believed to be applicable as well. For example, the fluid to be treated may be a fluid that is a mixture comprising water. Accordingly, the fluid can be a liquid that comprises water. The treatment system can provide purified, treated or softened water to a point of use by reducing a concentration of or removing at least a portion of any hardness-causing species contained in water from a water source, such as municipal water, well water, brackish water and water containing foulants. Other applications of the system would be in the treatment and processing of foods and beverages, sugars, various industries, such as the chemical, pharmaceutical, food and beverage, wastewater treatments and power-generating industries. The water treatment system typically includes at least one baffle plate in a reservoir system. Alternatively, or in combination, the water treatment system comprises at least one water property sensor for measuring at least one water property. The water treatment system of the present invention typically receives water from the water source or a point of entry and treats the water containing at least some undesirable species before delivering the treated water to a point of use. The treatment system typically has a reservoir system in line with a treatment device, which can comprise an electrochemical treatment device such as an electrodeionization device. The treatment system, in accordance with some embodiments of the present invention further comprises a sensor for measuring at least one property of the water or an operating condition of the treatment system. In other embodiments of the present invention, the treatment system also includes a controller for adjusting or regulating at least one operating parameter of the treatment system or a component of the treatment system. FIG. 1 shows a schematic flow diagram of a water treatment system according to one embodiment of the present invention. The water treatment system 10 includes a reservoir system 12 fluidly connected, typically at an upstream end, to a water source or a point of entry 14 and to a treatment device such as an electrochemical device which can comprise an electrodeionization device 16, typically at a downstream end. Water treatment system 10 typically includes a point of use 18, which is typically fluidly connected downstream of reservoir system 12. In certain embodiments of the invention, water treatment system 10 also has a sensor 20 and a controller 22 for controlling or regulating power source 24 which provides power to electrodeionization device 16. Electrodeionization device 16 typically removes undesirable species from water to be treated flowing from point of entry 14 to produce treated water for storage into reservoir system 12 and ultimate delivery to point of use 18. Undesirable species removed by electrodeionization device 16 is typically transfened to an auxiliary use or a drain 26. Water treatment system 10, in certain embodiments further includes pretreatment system 28, which is typically fluidly connected upstream of reservoir system 12 or electrodeionization device 16. Moreover, water treatment system 10 typically also includes fluid control components, such as pump 30 and valve 32. The present invention will be further understood in light of the following definitions. As used herein, "pressurized" refers to a system or component that has a pressure, internal or applied, that is above atmospheric pressure. For example, a pressurized reservoir system has an internal pressure that is greater than atmospheric pressure. Pressure in the pressurized reservoir system can be created by various methods and techniques, for example, by pressurizing the water with a water pump or by elevating the water source, thus creating head pressure. The components, systems, or techniques of the present invention can incorporate or utilize any suitable water treatment or purification device or apparatus or technique that removes or at least reduces a concentration of any undesirable species in a fluid to be treated and is not necessarily limited to purifying or treating water with an electrodeionization device. Thus, in accordance with one or more embodiments of the present invention, the treatment system can comprise a treatment device comprising at least one of a reverse osmosis device, a electrochemical device, an ultrafiltration device, a microfiltration device, and, in some cases, a distillation device. Further, although the phrase "electrodionization device" is used herein with reference to treating water, other treatment devices, including electrochemical devices, which can treat or purify water to remove one or more undesirable species from a fluid, can be used. Examples of such electrochemical devices include, but are not limited to, devices that incorporate principles of electrodialysis and/or capacitive deionization. FIG. 2 schematically shows a cross-sectional view of fluid and ion flow paths through one embodiment of an electrodeionization device in accordance with the present invention. The electrodeionization module or device 16 includes ion-depleting (depleting) compartments 34 and ion-concentrating (concentrating) compartments 36, positioned between ion-depleting compartments 34. Depleting compartments 34 are typically bordered by an anolyte compartment 38 and a catholyte compartment 40. Typically, end blocks (not shown) are positioned adjacent to end plates (not shown) to house an anode 42 and a cathode 44 in their respective compartments. In certain embodiments of the present invention, the compartments include cation-selective membranes 46 and anion-selective membranes 48, which are typically peripherally sealed to the periphery of both sides of the compartments. The cation-selective membranes and anion-selective membranes are typically comprised of an ion exchange powder, a polyethylene powder binder and a glycerin lubricant. In some embodiments, the cation- and anion-selective membranes are typically heterogeneous polyolefin-based membranes, which are typically extruded by a thermoplastic process using heat and pressure to create a composite sheet. However, the present invention contemplates the use of homogenous membranes as well as combinations of homogeneous and heterogeneous membranes. Representative suitable ion-selective membranes include, for example, web supported using styrene-divinyl benzene with sulphonic acid or quaternary ammonium functional groups, web supported using styrene-divinyl benzene in a polyvinylidene fluoride binder, and unsupported-sulfonated styrene and quarternized vinyl benzyl amine grafts on polyethylene sheet. Concentrating compartments 36 are typically filled with cation exchange resin 50 and depleting compartments 34 are typically filled with cation exchange resin 50 and anion exchange resin 52. In some embodiments of the present invention, the cation exchange and anion exchange resins can be ananged in layers within any of the depleting, concentrating and electrode compartments so that a number of layers in a variety of anangements can be assembled. Other embodiments are believed to be within the scope of the invention including, for example, the use of mixed bed ion exchange resins in any of the ion-depleting, concentrating and electrode compartments, the use of inert resin between layer beds of anionic and cationic exchange resins, the use of various types and anangements of anionic and cationic resins including, but not limited to, those described by DiMascio et al., in U.S. Patent No. 5,858,191. In operation, a liquid to be treated 54, typically from an upstream water source entering the treatment system at point of entry 14, having dissolved cationic and anionic components, including hardness ion species, is introduced into ion-depleting compartments 34 through manifold 60, wherein the cationic components are attracted to the cation exchange resin 50 and the anionic components are attracted to the anion exchange resin 52. An electric field applied across electrodeionization device 16, through anode 42 and cathode 44, which are typically positioned on opposite ends of electrodeionization device 16, typically passes perpendicularly relative to the fluid flow direction such that cationic and anionic components in the liquid tend to migrate in a direction conesponding to their attracting electrodes. Cationic components can migrate through cation-selective membrane 46 into adjacent concentrating compartment 36. Anion-selective membrane 48, positioned on the opposite side of concentrating compartment 36, can prevent migration into adjacent compartments, thereby trapping the cationic components in the concentrating compartment. Similarly, anionic components can migrate through the ion-selective membranes, but in a direction that is typically opposite or counter relative to the migration direction of the cationic components. Anionic components can migrate through anion-selective membrane 48, from ion-depleting compartment 34, into adjacent concentrating compartment 36. Cation-selective membrane 46, positioned on the other side of concentrating compartment 36, can prevent further migration, thus effectively trapping anionic components in the ion-concentrating compartment. In net effect, ionic components are removed or depleted from the liquid 54 depleting compartments 34 and collected in concentrating compartments 36 resulting in a treated water product stream 56 and a concentrate or waste stream 58. In accordance with some embodiments of the present invention, the applied electric field on electrodeionization device 16 can create a polarization phenomenon, which leads to the dissociation of water into hydrogen and hydroxyl ions. The hydrogen and hydroxyl ions regenerate the ion exchange resins 50 and 52 in depleting compartments 34, so that removal of dissolved ionic components can occur continuously and without a separate step for regenerating exhausted ion exchange resins because of the ionic species migration. The applied electric field across electrodeionization device 16 is typically a direct cunent. However, any applied electric field that creates a bias or a potential difference between one electrode and another can be used to promote migration of ionic species. Therefore, an alternating cunent may be used, provided that there is a potential difference between electrodes that is sufficient to attract cationic and anionic species to the respective attracting electrodes. In yet another embodiment in accordance with the systems and techniques of the present invention, an alternating cunent may be rectified, for example, by using a diode or a bridge rectifier, to convert an alternating cunent to a pulsating direct cunent that provides a potential gradient across the electrodeionization device. The electroactive media, the ion exchange resins 50 and 52, typically utilized in depleting compartments 34, can have a variety of functional groups on their surface regions, such as tertiary, alkyl amino groups and dimethyl ethanolamine. These materials can also be used in combinations with ion exchange resin materials having various functional groups on their surface regions, such as quaternary ammonium groups. Other types of electroactive media can also be utilized. Examples of such include, but are not limited to, electroactive fibers. Reservoir system 12 can store or accumulate water from point of entry 14 or a water source and can also serve to store treated water from product stream 56 from electrodeionization device 16 and provide water, typically treated water or treated water mixed with water from point of entry 14 to point of use 18 through a distribution system. In one embodiment, reservoir system 12 can be pressurized with a pressure that is above atmospheric pressure. In accordance with some embodiments of the present invention, reservoir system 12 comprises a vessel or a vessel that has inlets and outlets for fluid flow such as an inlet 62 and an outlet 64. Inlet 62 is typically fluidly connected to point of entry 14 and outlet 64 is typically fluidly connected to a water distribution system or a point of use 18. Reservoir system 12 can have several vessels or vessels having several inlets positioned at various locations on each vessel. Similarly, outlet 64 may be positioned on each vessel at various locations depending on, among other things, demand or flow rate to point of use 18, capacity or efficiency of electrodeionization device 16 and capacity or hold-up of reservoir system 12. Reservoir system 12 can further comprise various components or elements that perform desirable functions or avoid undesirable consequences. For example, reservoir system 12 can have a plurality of vessels having internal components, such as baffle plates, generally refened to as baffles, that are positioned to disrupt any internal fluid flow cunents within the vessels of reservoir system 12. In some embodiments of the present invention, reservoir system 12 has a heat exchanger for heating or cooling the fluid. For example, reservoir system 12 can comprise a vessel with a heating coil, which can have a heating fluid at an elevated temperature relative to the temperature of the fluid in the vessel. The heating fluid may be hot water in closed-loop flow with a heating unit operation such as a furnace so that the heating fluid temperature is raised in the furnace and the heating fluid temperature is lowered in the vessel because of heat transfer to the vessel fluid. Other examples of auxiliary or additional components include, but are not limited to, pressure relief valves designed to relieve internal pressure of any vessels and avoid or at least reduce the likelihood of vessel rupture and thermal expansion tanks that are suitable for maintaining a desired operating pressure. The size and capacity of a thermal expansion tank will depend on one or more factors including, but not limited to, the total volume of water, the operating temperature and pressure of the reservoir system. In operation, reservoir system 12 is typically comiected downstream of point of entry
14 and fluidly connected in-line, such as in a recirculation loop, with electrodeionization device 16. For example, water from point of entry 14 can flow into inlet 62 and can mix with the bulk water contained within reservoir system 12. Bulk water can exit reservoir system 12 through outlet 64 and can be directed to point of use 18 or through pump 30 into electrodeionization device 16 for treatment or removal of any undesirable species. Treated water leaving electrodeionization device 16 may mix with water from point of entry 14 and enter reservoir system 12 through inlet 62. In this way, a loop can be formed or defined between reservoir system 12 and electrodeionization device 16 and feedwater from point of entry 14 can replenish water demand created by and flowing to point of use 18. Point of entry 14 typically provides water from a water source or connects the water source to the water treatment system. The water source can be a potable water source, such as municipal water or well water or it can be from a brackish or saltwater source. In some embodiments, a pretreatment system purifies the water so that it is suitable for human consumption before reaching point of entry 14. The water typically contains dissolved salts or ionic or ionizable species including sodium, chloride, calcium ions, magnesium ions, carbonates, sulfates or other insoluble or semi-soluble species or dissolved gases, such as silica and carbon dioxide. Moreover, the water can contain additives, such as fluoride, chlorate and bromate species. Thus, for example, point of entry 14 maybe the point of entry for an industrial, commercial or household setting. In accordance with further embodiments of the invention, the treatment system can comprise at least two vessels or two zones in one or more vessels, each of which can be, at least partially, fluidly isolated from the other. For example, the treatment system can comprise two vessels fluidly connected to a point of entry and to one or more treatment devices. The two vessels can be fluidly isolated from each other by conduits and valves so that a first vessel can be placed in service with one or more treatment devices while a second vessel can be removed from service for, for example, maintenance or cleaning. In accordance with another embodiment of the present invention, water treatment system 10 can include a water distribution system, which in turn can connect to a point of use. The water distribution system may comprise components that are fluidly connected to provide water, typically treated water, from reservoir system 12 to point of use 18. The water distribution system may comprise any anangement of pipes, valves, tees, pumps and manifolds to provide water from reservoir system 12 to one or several points of use 18 or to any component of water treatment system 10. And, according to one embodiment of the invention, the water distribution system is a water distribution system in a commercial, industrial or household setting that provides potable water to several points of use. Point of use 18 is typically any device or appliance that requires or demands water. For example, point of use 18 can be an appliance, such as a washing machine or a dishwasher, or can be a faucet serving to provide water to a kitchen sink or a showerhead. In another embodiment of the invention, point of use 18 comprises a system for providing water suitable for household or residential use. In accordance with another embodiment of the present invention , water treatment system 10 also comprises a sensor, typically a water property sensor, which measures at least one physical property of the water in water treatment system 10. For example, sensor 20 can be a device that can measure turbidity, water conductivity, pH, temperature, pressure, flow rate or composition. Sensor 20 can be installed or positioned within water treatment system 10, or any component thereof, to measure a water property or used in combination with one or more sensors to indicate the water quality in water treatment system 10. For example, sensor 20 can be a water conductivity sensor installed in reservoir system 12 so that sensor 20 measures the conductivity of the water, which can indicate the quality of the water available for service in point of use 18. In another aspect of the present invention, water treatment system 10 has multiple sensors, for example, a combination of any of pH, temperature, pressure and flow rate sensors. And in another embodiment, sensor 20 may comprise a series or a set of sensors in reservoir system 12. The series or set of sensors may be ananged and connected to controller 22 so that the water quality is monitored, intennittently or continuously, through controller 22, and, in some embodiments, the operation of water treatment system 10 can be optimized as described below. Other embodiments of the present invention can comprise a combination of sets of sensors in various locations throughout water treatment system 10. For example, sensor 20 can be a flow sensor measuring a flow rate to a point of use 18 and further include any of a nephelometer, pH, temperature and pressure sensor monitoring the operating condition of water treatment system 10. In accordance with another embodiment of the present invention, water treatment system 10 may further comprise a pretreatment system 28 designed to remove a portion of any undesirable species from the water before the water is introduced to, for example, reservoir system 12 or the electrodeionization device 16. Examples of pretreatment systems include, but are not limited to, reverse osmosis devices, which are typically used to desalinate brackish or salt water. Carbon or charcoal filter may be necessary to remove at least a portion of any chlorine, including active chlorine, or any species that may foul or interfere with the operation of electrodeionization device 16. In accordance with further embodiments of the present invention, pretreatment system 28 can comprise any apparatus or device that removes or at least renders inactive any microorganism such as bacteria that may be present in one or more components of the treatment system. For example, a pretreatment apparatus may be disposed upstream of the electrochemical device and/or the reservoir. Examples of such suitable devices that can render bacteria at least partially inactive include devices that utilize ozone and/or actinic radiation. Further, in other embodiments of the present invention, such bacterial inactivating devices be installed or utilized at or near a point of use so that fluids such as water delivered to a point of use can be essentially disinfected. Other types of pre and/or post treatment systems can utilize microfiltration and/or ultrafiltration techniques. Pretreatment system 28 may be positioned anywhere within water treatment system
10. For example, pretreatment system 28 can be positioned upstream of reservoir system 12 or downstream of system 12 but upstream of electrodeionization device 16 so that at least some chlorine species are retained in reservoir system 12 but are removed before the water enters electrodeionization device 16. In accordance with further embodiments of the invention, the treatment system can comprise systems and techniques that permit disinfection of any component of the treatment system. For example, the treatment system can be exposed to a disinfecting solution or a disinfectant. The disinfectant can be any material that can destroy or at least renders inactive a portion of any microorganisms, such as bacteria, present in any component or subsystem of the treatment system. Examples of a disinfectant can include any base, acid or sanitizer, such as a halogen or halogen-donating compounds, peroxygen or peroxygen-donating compounds that destroys or renders bacteria inactive. The disinfectant can be introduced into the treatment system by any suitable device or technique. For example, the disinfectant can be ' introduced into a water treatment system by introducing chlorine into the reservoir system. Introducing chlorine can be performed by injection of a hypochlorate species from a disinfectant reservoir fluidly connectable to any suitable portion of the treatment system. The chlorinated water can be further circulated through at least a portion of the treatment system thereby exposing wetted portions of the system to the disinfectant. In accordance with one or more embodiments of the present invention, water treatment system 10 further comprises a controller 22 that is capable of monitoring and regulating the operating conditions of water treatment system 10 and its components. Controller 22 typically comprises a microprocessor-based device, such as a programmable logic controller (PLC) or a distributed control system that receives or sends input and output signals to components of water treatment system 10. For example, controller 22 can be a PLC that sends a signal to power source 24, which supplies power to electrodeionization device 16 or can provide a signal to a motor control center that provides power to pumps 30. In certain embodiments of the present invention, controller 22 regulates the operating conditions of water treatment system 10 in open-loop or closed-loop control scheme. In accordance with one embodiment of the invention, controller 22, in open-loop control, can provide signals to the water treatment system such that water is treated without measuring any operating condition. In contrast, controller 22 may control the operating conditions in closed-loop control so that operating parameters may be adjusted depending on an operating condition measured by, for example, sensor 20. In yet another embodiment of the invention, controller 22 may further comprise a communication system such as a remote communication device for transmitting or sending any of measured operating condition or operating parameter to a remote station. Controller 22 can provide a signal that actuates any valves 32 in water treatment system 10 so that fluid flow in water treatment system 10 can be adjusted based on a variety of parameters including, but not limited to, the quality of water from point of entry 14, the quality of water to point of use 18, the demand or quantity of water to point of use 18, the operating efficiency or capacity of electrodeionization device 16, or any of a variety of operating conditions, such as the water conductivity, composition, pH, turbidity, alkalinity, temperature, pressure and flow rate. Thus, in one or more embodiments of the present invention, controller 22 can receive a signal from sensor 20, or a set of signals from a combination of sensors or sets of sensors, so that controller 22 can be capable of monitoring the operating parameters of water treatment system 10. For example, sensor 20 can be a water conductivity sensor positioned within reservoir system 12 so that the water conductivity in reservoir system 12 can be monitored by controller 22. Controller 22 can, based on the signals from, for example, sensor 20, control power source 24, which provides an electric field to electrodeionization device 16. In operation, controller 22 can increase, decrease or otherwise adjust the voltage, cunent, or both, supplied to electrodeionization device 16. In another embodiment of the present invention, controller 22 may reverse the direction of the applied field from power source 24 to electrodeionization device 16 according to a predetermined schedule or according to an operating condition, such as the water quality or any other operating parameter measured by sensor 20. For example, controller 22 can be configured to reverse the polarity of the electric field applied to electrodeionization device 16 when a measured parameter reaches a set point. In another embodiment, the present invention provides a controller that is capable of increasing, decreasing or otherwise adjusting a cycle time based on, for example, the measured water properties, such as but not limited to, total dissolved solids, water quality, including conductivity. The cycle of electrodeionization device 16 includes the period between reversals in the electric field, along with the associated changes, reversals or substitution of fluid flows within electrodeionization device 16. Polarity reversal, which has been described by, for example, Giuffrida et al., in U.S. Patent No. 4,956,071, is considered to be within the scope of the present invention. Controller 22 may be configured or configurable by programming or maybe self-adjusting such that it is capable of maximizing any of the service life and the efficiency of or reducing the operating cost of water treatment system 10. For example, controller 22 can comprise a microprocessor having user-selectable set points or self-adjusting set points that adjusts the applied voltage and cunent or both to electrodeionization device 16, the flow rate through the ion-concentrating and ion-depleting compartments of the electrodeionization device or the flow rate to discharge to drain 26 from the electrodeionization device or the pretreatment system or both. Accordingly, in accordance with one or more embodiment, the water treatment system stores water from point of entry 18, which is typically connected to a water source and typically at a pressure that is above atmospheric pressure, in a first zone of reservoir system 12. Reservoir system 12 can be fluidly connected to a water distribution system that supplies treated water to point of use 18. Water treatment system 10 can have an electrochemical device such as an electrodeionization device 16 that purifies or treats water from point of entry 14 by removing at least a portion of any undesirable species to produce treated water that is introduced into reservoir system 12 in a second zone of reservoir system 12. First and second zones of reservoir system 12 can be monitored by at least one water quality sensor, more preferably, a set of water quality sensors connected to controller 22, which, in turn, can adjust an operating parameter of the electrochemical device. In this way, controller 22 can monitor the first and second zones of reservoir system 12 and regulate the operation of the electrochemical device depending on any of the properties measured by a sensor or a set of sensors 20 which measures the water properties of the water in the first and second zones. As used herein, the term "zone" refers to a volume, typically a volume of liquid in the reservoir system. For example, a reservoir system can have one container or vessel having two or more zones defined as portions of the vessel containing conesponding volumes. However, in accordance with some embodiments of invention, the reservoir system can have two or more zones wherein each zone is defined by a conesponding, separate vessel. In accordance with another embodiment of the present invention, controller 22, through sensor or set of sensors 20 or combinations thereof, can monitor or measure at least one water property of the water in the first and second zones of reservoir system 12 and also measure a flow rate flowing into at least one point of use 18 and can adjust an operating parameter of electrodeionization device 16 based on the measured properties. Thus, in one or more embodiments of the present invention, sensor 20 measures at least one property of at least one of the water from the point of entry and the treated water. For example, when an increased flow rate is measured to point of use 18, controller 22 can adjust an operating parameter, such as an applied voltage or cunent, of electrodeionization device 16 to treat water to compensate for any additional demand flowing into point of use 18. In another embodiment, controller 22 can adjust an operating parameter of electrodeionization device 16 depending on the volume in the first and second zones of reservoir system 12 and the historical demand, e.g. water demand, required by point of use 18. In accordance with another embodiment of the present invention, reservoir system 12 has partitions that separate freated water from untreated water or mixtures of treated water with untreated water. Controller 22, through measurement sensors 20 and valves 32, can control the flow of treated, raw or mixed water to a particular point of use, depending on specific needs of that point of use. For example, if point of use 18 requires softened water, then controller 22 can open one or more valves 32 in the water distribution system so that only treated water is provided to point of use 18. Or, if point of use 18 does not require softened water, then controller 22 would isolate treated water in reservoir system 12 and allow raw water to flow through the water distribution system to point of use 18 by opening the appropriate valves. In accordance with another embodiment of the present invention, reservoir system 12 is capable of isolating purified or treated water from raw water into zones by use of techniques or structures such as partitions or baffles or by utilizing separate vessels which may be isolated from each other. In this way, controller 22 can control one or more valves 32 so that raw water can be introduced into electrodeionization device 16 and treated water from the electrodeionization device can be transfened to the zone or vessel of treated water. Moreover, controller 22 can supply water to point of use 18 depending on the requirements of point of use 18 in a similar fashion as described above. Thus, in another embodiment of the invention, the fluid volumes of the first and second zones can be adjusted depending on several factors including, for example, the demand by a point of use, the operating efficiency of the electrodeionization device and the water property of the water in the zones. The system can also comprise aeration devices, which can introduce a gas, such as air, and ventilation devices, to effect dissolution of air and/or to volatilize or purge undesirable species, such as compounds that can affect the taste of water. Any unit operation that permits mass transfer to and from the fluid, such as water, can be utilized in accordance with the techniques of the present invention. Examples of aerating device include, but are not limited to bubblers and perforated tubes or lines submerged in fluid to be aerated, such as treated water or water from a point of use. In accordance with another example, aeration can be performed by exposing the fluid to be aerated in an open air channel having, preferably, features such as In accordance with another embodiment of the present invention, controller 22 can calculate a control parameter that can be used to adjust or vary a control signal to a component of the water treatment system. For example, controller 22 can calculate a
Langelier Saturation Index (LSI) based on the measured operating conditions of the streams of the water treatment system. Calculated LSI can then be used in another or the same control loop, in the same or another controller, as an input variable that can be compared to a set-point and generate an output signal that actuates, adjusts or otherwise regulates a component of the water treatment system. LSI can be calculated according to, for example, ASTM D 3739. In some embodiments of the present invention, the treated water, such as the softened water, has a low LSI so that it has a low tendency to form scale. As used herein, low LSI water has a LSI of about less than 2, preferably, less than about 1, and more preferably, less than about zero, hi another embodiment of the present invention, the treated water has a low conductivity that is less than about 300 μS/cm, preferably less than about 220 μS/cm and more preferably, less than about 200 μS/cm. In accordance with another embodiment of the present invention, controller 22 can regulate the operation of the water treatment system by incorporating adaptive or predictive algorithms, which are capable of monitoring demand and water quality and can adjust the operation of the electrochemical device, such as increasing or decreasing the applied voltage or the period between electric field reversals of electrodeionization device 16. For example, controller 22 can be predictive in anticipating higher demand for treated water during early morning hours in a residential application to supply point of use 18 serving as a showerhead. Controller 22 can incorporate dead band control to reduce the likelihood of unstable on/off control or chattering. Dead band refers to the range of signal outputs that a sensor provides without necessarily triggering a responsive control signal. The dead band may reside, in some embodiments of the invention, intrinsically in the sensor or may be programmed as part of the control system, or both. Dead band control can avoid unnecessary intermittent operation by smoothing out any measurement excursions. Such control techniques can prolong the operating life or mean time before failure of the components of water treatment system 10. Other techniques that can be used include the use of voting, time-smoothing or time-averaging measurements or combinations thereof. In accordance with another embodiment of the present invention, stream 58 to auxiliary use can provide additional or secondary benefits. For example, stream 58, rather than going to drain 26, may be used to provide irrigating water to any residential, commercial or industrial use, such as for irrigating, for recycling or for recovery of collected or concentrated salts. In accordance with another embodiment, the present invention can provide a vessel, or a plurality of vessels, having a plurality of outlet ports, each of which can be connected to a water distribution system. The plurality of outlets can permit the selective delivery of water to any point of use. The plurality of outlets can permit the system to deliver water having a specific or predetermined water quality to a specific point of use. For example, water having low conductivity can be delivered to a point of use, such as a shower, that does requires higher quality water. Such a system can also accommodate delivery of hard water to a point of use that is insensitive to water hardness. Sensors can measure the water conductivity as an indication of water quality. The control system can regulate valves or pumps, or both, in, for example, the distribution system, to provide water having the appropriate or closest water quality that conesponds to the water quality requirement of the point of use. The present invention will be further illustrated through the following example, which is illustrative in nature and is not intended to limit the scope of the invention.
Example This prophetic example describes a water treatment system that can be designed according to the present invention. FIG. 3 is a schematic illustration of a reservoir system that can be used in the water treatment system of the present invention. The reservoir system 12 has a vessel 13 with an inlet 62, typically fluidly connected to a point of entry (not shown), and an outlet 64, typically fluidly connected to a point of use (not shown). Vessel 13 has a second inlet 63 that is fluidly connected to an electrodeionization device (not shown). Vessel 13 has at least one baffle 66, which can be ananged in a variety of configuration including, for example, offset and rotated anangements or combinations thereof. Moreover, baffle 66 can be single, double or triple segmental baffles or combinations thereof. At least one water property sensor 20 can be installed on vessel 13 for measuring a water property such as, pressure, temperature, pH and conductivity. Sensor 20 can be installed in a variety of configurations. As illustrated, three sensors 20a, 20b and 20c that measure the conductivity of the water are installed along the height of vessel 13. In operation, each sensor 20a, 20b and 20c provides a signal to a controller (not shown), which conesponds to the measured water conductivity. The controller can be configured to average the measurements or can monitor any difference in water conductivity. In the former, the controller regulates the operating parameters of the electrodeionization device, which softens the water flowing from outlet 64 to produce treated water returning into second inlet 63 based on the average measured conductivity. In the latter anangement, the controller monitors the interface between the treated and raw water in vessel 13 and regulates the operation of the electrodeionization device as necessary to provide treated water to the point of use. For example, before the interface 68 between raw and treated water, as measured by the difference in conductivity, reaches sensor 20b, the controller regulates the operation of the electrodeionization device to treat water at a first operating condition. If demand for treated water results in bringing interface 68 between sensor 20b and 20c, then the controller can regulate the electrodeionization device at a second operating condition that treats water at a faster rate or removes undesirable species at a faster rate. In this way, constructive use of baffles and sensor anangement can optimize the operation of the water treatment system and components thereof. Those skilled in the art would appreciate that all parameters and configurations described herein are meant to be exemplary and that actual parameters and configurations will depend upon the specific application for which the systems and methods of the present invention are used. Those skilled in the art will also recognize, or be able to ascertain using no more than routine experimentation, many equivalents to the specific embodiments of the invention described herein. For example, those skilled in the art can recognize that the present invention can be configured to minimize mixing between untreated water and treated water as well as to maximize such mixing when desirable or to control the degree of mixing according to need. Moreover, those of ordinary skill would be able to select materials of construction of the components or the system of the present invention using no more than routine experimentation. It is, therefore, to be understood that the foregoing embodiments are presented by way of example only and that, within the scope of the appended claims and equivalents thereto, the invention may be practiced otherwise than as specifically described. The present invention is directed to each individual feature, system, or method described herein. In addition, any combination of two or more such features, systems or methods, if such features, systems or methods are not mutually inconsistent, is considered to be within the scope of the present invention. What is claimed is:

Claims

1. A storage system comprising: a pressurized reservoir system having a first inlet fluidly connected to a point of entry and a second inlet fluidly connected to an electrochemical device; at least one conductivity sensor in the pressurized reservoir system; and a distribution system fluidly connected to the pressurized reservoir system and to a point of use.
2. The storage system of claim 1, wherein the pressurized reservoir system has at least one baffle plate positioned proximate the first inlet.
3. The storage system of claim 2, wherein the pressurized reservoir system has at least one baffle plate positioned proximate the second inlet.
4. The storage system of claim 3 further comprising a controller regulating at least one operating parameter of the electrochemical device.
5. The storage system of claim 4, wherein the controller regulates at least one operating parameter of the electrochemical device based on a signal from the conductivity sensor.
6. The storage system of claim 5 further comprising a pretreatment device fluidly connected upstream of the electrochemical device.
7. The storage system of claim 6 wherein at least three conductivity sensors are in the pressurized reseivoir system.
8. The storage system of claim 7 wherein the distribution system is a household water distribution system.
9. The storage system of claim 1 further comprising at least one sensor selected from the group consisting of a nephelometer, a composition analyzer, a pH, temperature and pressure sensor.
10. The storage system of claim 1, comprising at least three conductivity sensors installed along a water flow direction.
11. The storage system of claim 1 further comprising a post-treatment system comprising at least one of a ultraviolet device, a microfiltration device and an ultrafiltration device disposed downstream of the electrochemical device and upstream of the point of use.
12. The storage system of claim 1 further comprising a disinfectant source fluidly connected to at least one of the pressurized reservoir system, the electrochemical device, and the distribution system.
13. A water treatment system comprising: a reservoir system fluidly connected to a point of entry and having a first baffle plate; a water treatment device fluidly connected to the reservoir system; and a water distribution system fluidly connected to the reservoir system and a point of use.
14. The system of claim 13 wherein the reservoir system is pressurized.
15. The system of claim 14 further comprising a set of water property sensors for measuring at least one water property.
16. The system of claim 15 further comprising a controller for adjusting an operating parameter of the water treatment device based on the measured water property.
17. The water storage system of claim 14 further comprising a vent in the pressurized reservoir system.
18. The water storage system of claim 14 further comprising an aeration system in the pressurized reservoir system.
19. The water storage system of claim 14 further comprising a post treatment device fluidly connected to the water distribution system and upstream of the point of use.
20. The water storage system of claim 14 further comprising a disinfectant source fluidly connectable to at least one of the reservoir system and the water treatment device.
21. A method for providing treated water comprising: storing water from a point of entry; removing at least a portion of any undesired species from the water in an electrochemical device to produce treated water; measuring at least one water property of the treated water; and transferring at least a portion of the treated water to a point of use according to the measured property.
22. The method of claim 21 further comprising storing the treated water.
23. The method of claim 22 wherein storing the treated water comprises storing the treated water under a pressure that is above atmospheric pressure.
24. The method of claim 21 further comprising storing the treated water with the water from the point of entry.
25. The method of claim 24 wherein storing the treated water is performed while minimizing any mixing with the water from the point of entry.
26. The method of claim 21 further comprising calculating a desired property of the treated water based on at least one measured water property.
27. The method of claim 26 further comprising adjusting an operating parameter of the electrochemical device based upon the calculated desired property.
28. The method of claim 27 wherein the measured water property is LSI.
29. The method of claim 27 wherein the operating parameter is a cycle time of the electrochemical device.
30. The method of claim 21 further comprising disinfecting at least a portion of the electrochemical device.
31. The method of claim 21 further comprising post treating the water prior to transferring to a point of use.
32. An electrodeionization system comprising: a reservoir system fluidly connected to a point of entry and having a water property sensor; an electrodeionization device fluidly connected to the reservoir system; and a controller connected to the water property sensor for regulating a water flow from the reservoir system to a point of use.
33. The electrodeionization system of claim 32 further comprising a household water distribution system fluidly connected to the reservoir system.
34. The electrodeionization system of claim 33 wherein the reservoir system has at least one baffle plate.
35. The electrodeionization system of claim 32 wherein the reservoir system is a pressurized reservoir system.
36. A method for providing treated water comprising: storing water from a point of entry under a pressure that is above atmospheric pressure; removing at least a portion of any undesired species from the water in a water treatment device to produce treated water; measuring a property of the treated water; determining a difference between the property of the treated water to a set point; and controlling an operating parameter of the water treatment device based on the difference between the property of the treated water and the set point.
37. The method of claim 36 further comprising pre-treating the water prior to removing any undesired species.
38. The method of claim 36 further comprising controlling a flow to a point of use based on the difference between the property of the treated water and the set point.
39. The method of claim 36 further comprising minimizing any mixing of the water from the point of entry with the treated water.
40. The method of claim 36 further comprising mixing the water from the point of entry with the treated water.
41. The method of claim 36 wherein the water treatment device comprises an electrodeionization device.
I 42. A method for facilitating water treatment comprising providing a water treatment system comprising an electrochemical device that is fluidly connected to a reservoir system having a water property sensor and a controller that is connected to the water property sensor for regulating a water flow from the reservoir system to a point of use, the treatment system is fluidly connectable to a point of entry and to the point of use.
43. A method for facilitating water treatment comprising providing a water treatment system comprising a reservoir system having a baffle plate and an electrodeionization device, the reservoir system is fluidly connectable to a point of entry and to a water distribution system.
44. A water treatment system comprising: means for storing water that is fluidly connected to a point of entry and an electrochemical device; means for determining a water property in the means for storing water; and means for delivering water to a point of use based on the water property.
45. The water treatment system of claim 44 further comprising means for pretreating the water from a water source.
46. The water treatment system of claim 44 further comprising means for adjusting an operating parameter of the electrochemical device based on the water property.
47. The water treatment system of claim 44 further comprising means for minimizing mixing in the means for storing water.
48. A method for providing treated water comprising: storing water from a point of entry; removing at least a portion of any undesirable species from the water to produce treated water; storing at least a portion of the treated water; and minimizing any mixing of the water from the point of entry and the treated water.
49. The method of claim 48 further comprising minimizing any mixing of the treated water while storing the treated water.
50. The method of claim 49 wherein storing the at least a portion of the treated water comprises storing at least a portion of the treated water in a reservoir system.
51. The method of claim 48 wherein removing at least a portion of any undesirable species comprises purifying the water in an electrodeionization device.
52. The method of claim 48 wherein storing water from the point of entry comprises storing water at a pressure that is above atmospheric pressure.
53. The method of claim 48 wherein storing at least a portion of the treated water comprises storing at least a portion of the treated water at a pressure that is above atmospheric pressure.
54. The method of claim 48 further comprising measuring at least one water property.
55. The method of claim 48 wherein storing water from a point of entry comprises storing water in a first vessel of a reservoir system and storing at least a portion of the treated water comprises storing at least a portion of the treated water in a second vessel of the reservoir system.
56. A method for providing treated water comprising: storing water from a point of entry in a first zone of a reservoir system; removing at least a portion of any undesirable species from the water to produce treated water; and storing at least a portion of the treated water in a second zone of the reservoir system.
57. The method of claim 56 further comprising adjusting at least one of a first zone volume and a second zone volume based on a water demand by a point of use.
58. The method of claim 56 further comprising adjusting at least one of a first zone volume and a second zone volume based on a treated water property.
59. The method of claim 56 further comprising delivering water from any of the first and second zones to a point of use.
60. The method of claim 56 wherein the reservoir system is pressurized.
61. The method of claim 56 wherein the first zone comprises a first vessel of the reservoir system and the second zone comprises a second vessel of the reservoir system.
62. A method for purifying water comprising: storing water from a point of use; releasing any volatilizable material from the stored water; removing at least a portion of any undesirable species from the water in a water treatment device to produce treated water; and storing at least a portion of the treated water.
63. The method of claim 62 wherein the water treatment device comprises an electrochemical device.
64. The method of claim 63 wherein the electrochemical device comprises an electrodeionization device.
65. A method for purifying water comprising: storing water from a point of use; aerating the stored water; removing at least a portion of any undesirable species from the water in an electrodeionization device to produce treated water; and storing at least a portion of the treated water.
66. The method of claim 65 wherein storing the at least a portion of the treated water comprises storing the treated water at a pressure that is above atmospheric pressure.
67. A water treatment system comprising a reservoir system fluidly connected to a point of entry and comprising a ventilation system; and an electrodeionization device fluidly connected to the reservoir system; and a point of use fluidly connected to the reservoir system.
68. A water treatment system comprising: a reservoir system fluidly connected to a point of entry and comprising an aeration system; a water treatment device fluidly connected to the reservoir system; and a point of use fluidly connected to the reservoir system.
69. The water treatment system of claim 68 further comprising at least one water property sensor.
70. The water treatment system of claim 68 further comprising a controller for regulating at least one operating parameter of the water treatment system based on a measured water property.
71. The water treatment system of claim 68 wherein the water treatment device comprises an electrochemical device.
72. The water treatment system of claim 71 wherein the electrochemical device comprises an electrodeionization device.
PCT/US2004/037897 2003-11-13 2004-11-12 Water treatment system and method WO2005049498A2 (en)

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Families Citing this family (106)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2639642C (en) 1996-12-20 2013-01-15 Siemens Water Technologies Corp. Scouring method
US7147785B2 (en) * 2000-09-28 2006-12-12 Usfilter Corporation Electrodeionization device and methods of use
AUPR421501A0 (en) 2001-04-04 2001-05-03 U.S. Filter Wastewater Group, Inc. Potting method
AUPR692401A0 (en) 2001-08-09 2001-08-30 U.S. Filter Wastewater Group, Inc. Method of cleaning membrane modules
US7572359B2 (en) * 2001-10-15 2009-08-11 Siemens Water Technologies Holding Corp. Apparatus for fluid purification and methods of manufacture and use thereof
AUPS300602A0 (en) 2002-06-18 2002-07-11 U.S. Filter Wastewater Group, Inc. Methods of minimising the effect of integrity loss in hollow fibre membrane modules
JP4282598B2 (en) 2002-10-10 2009-06-24 シーメンス・ウォーター・テクノロジーズ・コーポレーション Filtration device and method for cleaning the filtration device
US7501061B2 (en) * 2002-10-23 2009-03-10 Siemens Water Technologies Holding Corp. Production of water for injection using reverse osmosis
AU2002953111A0 (en) 2002-12-05 2002-12-19 U. S. Filter Wastewater Group, Inc. Mixing chamber
JP4611982B2 (en) 2003-08-29 2011-01-12 シーメンス・ウォーター・テクノロジーズ・コーポレーション Backwash method
US7273561B1 (en) * 2003-10-21 2007-09-25 Waitaki Research Corporation Method for determining the chemical dosage required to reduce sulfides in wastewater to acceptable levels
US8377279B2 (en) 2003-11-13 2013-02-19 Siemens Industry, Inc. Water treatment system and method
US7563351B2 (en) 2003-11-13 2009-07-21 Siemens Water Technologies Holding Corp. Water treatment system and method
US7083733B2 (en) * 2003-11-13 2006-08-01 Usfilter Corporation Water treatment system and method
US7846340B2 (en) * 2003-11-13 2010-12-07 Siemens Water Technologies Corp. Water treatment system and method
JP4569096B2 (en) * 2003-11-13 2010-10-27 日産自動車株式会社 Fuel cell cooling system
US20050103717A1 (en) 2003-11-13 2005-05-19 United States Filter Corporation Water treatment system and method
KR20070003783A (en) 2003-11-14 2007-01-05 유.에스. 필터 웨이스트워터 그룹, 인크. Improved module cleaning method
US8758621B2 (en) 2004-03-26 2014-06-24 Evoqua Water Technologies Llc Process and apparatus for purifying impure water using microfiltration or ultrafiltration in combination with reverse osmosis
JP2007535398A (en) 2004-04-22 2007-12-06 シーメンス ウォーター テクノロジース コーポレイション Filtration device including membrane bioreactor and treatment tank for digesting organic substances, and waste liquid treatment method
CN100572646C (en) * 2004-05-05 2009-12-23 荷兰联合利华有限公司 Cleaning method
EP1598470A1 (en) * 2004-05-17 2005-11-23 The Procter & Gamble Company Method and system for washing
US7329358B2 (en) * 2004-05-27 2008-02-12 Siemens Water Technologies Holding Corp. Water treatment process
WO2006017911A1 (en) 2004-08-20 2006-02-23 Siemens Water Technologies Corp. Square mbr manifolding system
US20060049105A1 (en) * 2004-09-07 2006-03-09 Marine Desalination Systems, L.L.C. Segregated flow, continuous flow deionization
US8790515B2 (en) 2004-09-07 2014-07-29 Evoqua Water Technologies Llc Reduction of backwash liquid waste
NZ553742A (en) 2004-09-14 2010-09-30 Siemens Water Tech Corp Methods and apparatus for removing solids from a membrane module
CA2579894A1 (en) 2004-09-15 2006-03-23 Siemens Water Technologies Corp. Continuously variable aeration
WO2006066350A1 (en) 2004-12-24 2006-06-29 Siemens Water Technologies Corp. Simple gas scouring method and apparatus
EP2394731A1 (en) 2004-12-24 2011-12-14 Siemens Industry, Inc. Cleaning in membrane filtration systems
WO2006100937A1 (en) * 2005-03-18 2006-09-28 Kurita Water Industries Ltd. Apparatus for producing pure water
US7658828B2 (en) * 2005-04-13 2010-02-09 Siemens Water Technologies Holding Corp. Regeneration of adsorption media within electrical purification apparatuses
US20060231406A1 (en) * 2005-04-13 2006-10-19 Usfilter Corporation Regeneration of adsorption media within electrical purification apparatuses
CA2605757A1 (en) 2005-04-29 2006-11-09 Siemens Water Technologies Corp. Chemical clean for membrane filter
EP1885655B1 (en) * 2005-06-01 2014-12-17 Evoqua Water Technologies LLC Water treatment process by intermittent sanitization
US20060283802A1 (en) * 2005-06-21 2006-12-21 Water Standard Company, Llc Methods and systems for producing electricity and desalinated water
CN101287538B (en) 2005-08-22 2013-03-06 西门子工业公司 An assembly for water filtration using a tube manifold to minimise backwash
US20070138090A1 (en) * 2005-10-05 2007-06-21 Jordan Edward J Method and apparatus for treating wastewater
US10252923B2 (en) 2006-06-13 2019-04-09 Evoqua Water Technologies Llc Method and system for water treatment
US8114259B2 (en) * 2006-06-13 2012-02-14 Siemens Industry, Inc. Method and system for providing potable water
US8277627B2 (en) 2006-06-13 2012-10-02 Siemens Industry, Inc. Method and system for irrigation
US10213744B2 (en) 2006-06-13 2019-02-26 Evoqua Water Technologies Llc Method and system for water treatment
US20080067069A1 (en) 2006-06-22 2008-03-20 Siemens Water Technologies Corp. Low scale potential water treatment
SG174801A1 (en) * 2006-06-22 2011-10-28 Siemens Water Tech Corp Electrodeionization apparatus and low scale potential water treatment
US7820024B2 (en) * 2006-06-23 2010-10-26 Siemens Water Technologies Corp. Electrically-driven separation apparatus
US7744760B2 (en) 2006-09-20 2010-06-29 Siemens Water Technologies Corp. Method and apparatus for desalination
WO2009051612A1 (en) * 2007-10-18 2009-04-23 Kinetico Incorporated Electroregeneration apparatus and water treatment method
WO2008048656A2 (en) 2006-10-18 2008-04-24 Kinetico Incorporated Electroregeneration apparatus and water treatment method
WO2008051546A2 (en) 2006-10-24 2008-05-02 Siemens Water Technologies Corp. Infiltration/inflow control for membrane bioreactor
EP2129629A1 (en) 2007-04-02 2009-12-09 Siemens Water Technologies Corp. Improved infiltration/inflow control for membrane bioreactor
US9764288B2 (en) 2007-04-04 2017-09-19 Evoqua Water Technologies Llc Membrane module protection
KR101239780B1 (en) 2007-05-29 2013-03-06 지멘스 인더스트리 인코포레이티드 Membrane cleaning with pulsed airlift pump
US8999173B2 (en) * 2007-06-04 2015-04-07 Global Water Holdings, Llc Aqueous treatment apparatus utilizing precursor materials and ultrasonics to generate customized oxidation-reduction-reactant chemistry environments in electrochemical cells and/or similar devices
WO2009073175A2 (en) 2007-11-30 2009-06-11 Siemens Water Technologies Corp. Systems and methods for water treatment
US8562839B2 (en) * 2008-03-13 2013-10-22 Drexel University Desalination system and process
WO2010009518A1 (en) 2008-07-24 2010-01-28 Siemens Water Technologies Corp. Frame system for membrane filtration modules
KR20110044312A (en) 2008-08-20 2011-04-28 지멘스 워터 테크놀로지스 코포레이션 Improved membrane system backwash energy efficiency
JP4978593B2 (en) * 2008-09-01 2012-07-18 三浦工業株式会社 Pure water production system
KR101059564B1 (en) * 2008-12-02 2011-08-26 삼성전자주식회사 Water softening device and washing machine having same
AU2010257526A1 (en) 2009-06-11 2012-01-12 Siemens Industry, Inc Methods for cleaning a porous polymeric membrane and a kit for cleaning a porous polymeric membrane
US9346689B2 (en) * 2009-12-22 2016-05-24 Hellenbrand, Inc. Method of water discharge management
WO2011136888A1 (en) 2010-04-30 2011-11-03 Siemens Industry, Inc Fluid flow distribution device
EP2618916A4 (en) 2010-09-24 2016-08-17 Evoqua Water Technologies Llc Fluid control manifold for membrane filtration system
CN102600726B (en) * 2011-01-25 2014-12-10 通用电气公司 Ionic substance removal system
KR20120132324A (en) * 2011-05-26 2012-12-05 웅진코웨이주식회사 Method of active regeneration of deionization module and apparatus for treating water using thereof
KR20140097140A (en) 2011-09-30 2014-08-06 에보쿠아 워터 테크놀로지스 엘엘씨 Isolation valve
US9604166B2 (en) 2011-09-30 2017-03-28 Evoqua Water Technologies Llc Manifold arrangement
US8961770B2 (en) 2011-10-27 2015-02-24 Pentair Residential Filtration, Llc Controller and method of operation of a capacitive deionization system
US9695070B2 (en) 2011-10-27 2017-07-04 Pentair Residential Filtration, Llc Regeneration of a capacitive deionization system
US9010361B2 (en) 2011-10-27 2015-04-21 Pentair Residential Filtration, Llc Control valve assembly
US8671985B2 (en) 2011-10-27 2014-03-18 Pentair Residential Filtration, Llc Control valve assembly
US9637397B2 (en) 2011-10-27 2017-05-02 Pentair Residential Filtration, Llc Ion removal using a capacitive deionization system
US20130116994A1 (en) * 2011-11-03 2013-05-09 International Business Machines Corporation Water management
BR112014013734A8 (en) 2011-12-06 2017-06-13 Masco Corp ozone distribution on a tap
US9724645B2 (en) 2012-02-02 2017-08-08 Tangent Company Llc Electrochemically regenerated water deionization
KR101380406B1 (en) * 2012-04-05 2014-04-10 주식회사 포스코 Boron recovering device, method for recovering boron and boron recovering system
EP2866922B1 (en) 2012-06-28 2018-03-07 Evoqua Water Technologies LLC A potting method
DE102012212638C5 (en) * 2012-07-18 2020-07-30 Premark Feg L.L.C. Dishwasher and method for operating a dishwasher
CN103626266B (en) * 2012-08-27 2015-12-02 侯梦斌 A kind of take active carbon fiber fabrics as electro-adsorption water treating equipment and the technique of electrode
WO2014045668A1 (en) * 2012-09-20 2014-03-27 三菱電機株式会社 Humidifier and method of hydrophilization processing for humidification material
GB2520871B (en) 2012-09-26 2020-08-19 Evoqua Water Tech Llc Membrane securement device
US9962865B2 (en) 2012-09-26 2018-05-08 Evoqua Water Technologies Llc Membrane potting methods
AU2013323934A1 (en) 2012-09-27 2015-02-26 Evoqua Water Technologies Llc Gas scouring apparatus for immersed membranes
WO2014052769A1 (en) 2012-09-28 2014-04-03 Hydronovation, Inc. Devices and methods for storing, processing, and delivering a processed liquid
US10131553B2 (en) 2013-01-30 2018-11-20 3M Innovative Properties Company Electrochemical cells for supply of acid water
US10160670B2 (en) 2013-06-26 2018-12-25 Evoqua Water Technologies Llc Methods and systems for polarization control
HUE061765T2 (en) 2013-10-02 2023-08-28 Rohm & Haas Electronic Mat Singapore Pte Ltd Device for repairing a membrane filtration module
JP5884065B2 (en) * 2013-11-18 2016-03-15 パナソニックIpマネジメント株式会社 Liquid processing unit, toilet seat, washing machine and liquid processing apparatus
JP5884066B2 (en) * 2013-11-18 2016-03-15 パナソニックIpマネジメント株式会社 Liquid processing unit, toilet seat, washing machine and liquid processing apparatus
JP5866501B1 (en) * 2014-03-03 2016-02-17 パナソニックIpマネジメント株式会社 Water treatment support system, program
WO2016033598A1 (en) * 2014-08-29 2016-03-03 Ecoclean Usa Inc Water adjustment techniques for creation of disinfectant
DE102015110155B4 (en) * 2015-06-24 2019-06-19 Océ Printing Systems GmbH & Co. KG Method and device for carrying out an electrophoretic printing process and device for preparing a liquid therefor
US10767270B2 (en) 2015-07-13 2020-09-08 Delta Faucet Company Electrode for an ozone generator
US10322375B2 (en) 2015-07-14 2019-06-18 Evoqua Water Technologies Llc Aeration device for filtration system
CA2946465C (en) 2015-11-12 2022-03-29 Delta Faucet Company Ozone generator for a faucet
CN105481163A (en) * 2015-12-02 2016-04-13 于加全 Water treatment device and water treatment system
CN108463437B (en) 2015-12-21 2022-07-08 德尔塔阀门公司 Fluid delivery system comprising a disinfection device
WO2018097875A1 (en) 2016-09-12 2018-05-31 Aecom (Delaware Corporation) Use of electrochemical oxidation for treatment of per-and polyfluoroalkyl substances (pfas) in waste generated from sorbent and resin regeneration processes
EP3672916A4 (en) 2017-08-21 2021-05-19 Evoqua Water Technologies LLC Treatment of saline water for agricultural and potable use
US10273165B1 (en) * 2017-10-12 2019-04-30 Evoqua Water Technologies Llc Method and apparatus to monitor and control a water system
US10837895B2 (en) 2018-01-08 2020-11-17 A. O. Smith Corporation Electrochemical analysis device for reagentless detection
CA3106069A1 (en) 2018-08-08 2020-02-13 Evoqua Water Technologies Llc System and method of deionization of water
WO2020247029A1 (en) * 2019-06-07 2020-12-10 Evoqua Water Technologies Llc Pfas treatment scheme using separation and electrochemical elimination
CN114599611A (en) * 2019-08-26 2022-06-07 晶体公司 Periodic UVC dosing
EP4108329A4 (en) * 2020-02-18 2023-11-29 Kabushiki Kaisha F.C.C. Ion exchange equipment
AU2022282382A1 (en) * 2021-05-27 2023-12-07 Evoqua Water Technologies Llc Enhancing water treatment recovery from retention pond at fertilizer plants

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3630378A (en) * 1968-05-24 1971-12-28 Dow Chemical Co Novel water treating and storage apparatus
US4655909A (en) * 1983-12-20 1987-04-07 Nippon Paint Co., Ltd. Water-deionizing system
USH1206H (en) * 1991-01-24 1993-07-06 The United States Of America As Represented By The Secretary Of The Air Force Cascade crossflow tower
US20020092769A1 (en) * 2000-07-13 2002-07-18 Benny Garcia Electrodeionization system
US20030089609A1 (en) * 2001-10-15 2003-05-15 United States Filter Corporation Apparatus for fluid purification and methods of manufacture and use thereof

Family Cites Families (312)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2535035A (en) 1945-04-30 1950-12-26 Robert E Briggs Method of electrolytic water softening and ph adjustment
US2514415A (en) * 1946-02-27 1950-07-11 Carl H Rasch Storage battery paste with ion exchange expander
NL96481C (en) 1950-07-21
US2681320A (en) * 1950-12-23 1954-06-15 Rohm & Haas Permselective films of cationexchange resins
US2681319A (en) * 1951-01-10 1954-06-15 Rohm & Haas Permselective films of anionexchange resins
US2815320A (en) 1953-10-23 1957-12-03 Kollsman Paul Method of and apparatus for treating ionic fluids by dialysis
GB776469A (en) 1953-12-17 1957-06-05 Tno Process and apparatus for the electrolytic deionisation of salt-containing liquids
US2854394A (en) 1954-11-01 1958-09-30 Kollsman Paul Method of and apparatus for fractionation by electrodialysis
US2777814A (en) 1954-12-02 1957-01-15 Gen Electric Water heating and demineralizing apparatus
US2912372A (en) 1955-05-12 1959-11-10 Gen Electric Water treatment methods
NL95176C (en) 1955-07-30
US2906684A (en) 1956-01-30 1959-09-29 Gen Electric Water demineralizing units
US2788319A (en) * 1956-02-07 1957-04-09 Clayton Manufacturing Co Ion exchange method and apparatus
US2794777A (en) * 1956-08-27 1957-06-04 Clayton Manufacturing Co Electrolytic deionization
US3296112A (en) * 1957-07-16 1967-01-03 Kollsman Paul Method of modifying the chemical composition of substances by ion transfer
GB877239A (en) 1957-12-24 1961-09-13 Permutit Co Ltd Improvements relating to electrodialytic cells
GB879181A (en) * 1958-02-03 1961-10-04 Permutit Co Ltd Improvements relating to the removal of dissolved solids from liquids
GB882601A (en) 1958-05-07 1961-11-15 Permutit Co Ltd Improvements relating to the treatment of aqueous liquids by electro-dialysis
GB880344A (en) 1958-06-19 1961-10-18 Permutit Co Ltd Improvements relating to electrodialytic cells
US3074864A (en) * 1959-04-21 1963-01-22 Gen Electric Methods of and apparatus for demineralizing raw water
GB893051A (en) 1959-04-30 1962-04-04 John Thompson Kennicott Ltd Improvements in or relating to an electrodialysis apparatus
US3091583A (en) 1959-10-27 1963-05-28 Aqua Ionics Inc Electrodialysis cell
GB942762A (en) 1960-05-13 1963-11-27 John Thompson Kennicott Ltd A method of packing a receptacle with comminuted material
US3099615A (en) * 1961-02-13 1963-07-30 Kollsman Paul Electrodialysis involving periodic current reversal
DE1225569B (en) 1961-05-20 1966-09-22 Paul Dosch Method and device for water softening for washing machines and dishwashers
NL288721A (en) 1962-02-19
US3165460A (en) * 1962-04-11 1965-01-12 American Mach & Foundry Electrolytic acid generator
DE1494902A1 (en) 1962-05-04 1969-06-26 American Mach & Foundry Polymeric products and processes for their manufacture
NL294289A (en) * 1962-06-20
DE1201055B (en) 1962-09-27 1965-09-16 Wolfen Filmfab Veb Process for the production of heterogeneous ion exchange membranes
US3341441A (en) 1964-01-07 1967-09-12 Ionics Method for preventing scale buildup during electrodialysis operation
US3291713A (en) 1964-05-27 1966-12-13 Ionics Removal of weakly basic substances from solution by electrodeionization
GB1137679A (en) 1965-02-24 1968-12-27 Wallace Tiernan Inc Procedures and apparatus for electrodialytic treatment of liquids
FR1547493A (en) 1967-07-25 1968-11-29 Improvements to the means for removing ions from a solution
US3375208A (en) * 1967-07-26 1968-03-26 Esb Inc Method for preparing a microporous thermoplastic resin material
US3627703A (en) 1968-10-31 1971-12-14 Mitsubishi Petrochemical Co Polypropylene resin composites and production thereof
US3645884A (en) * 1969-07-10 1972-02-29 Edwin R Gilliland Electrolytic ion exchange apparatus
GB1318036A (en) 1969-10-29 1973-05-23 Permutit Co Ltd Ion-exchange treatment of liquids and apparatus for use therein
US3679055A (en) 1970-07-15 1972-07-25 Polymetrics Inc Reverse osmosis water purifier
JPS4916189B1 (en) * 1970-12-23 1974-04-20
US3755135A (en) 1971-01-20 1973-08-28 A Johnson Electric demineralizing apparatus
US3989615A (en) 1971-07-06 1976-11-02 Nippon Soda Company Limited Diaphragm process electrolytic cell
US3786924A (en) 1971-07-22 1974-01-22 Delro Inc Water purification system
JPS545888Y2 (en) 1971-12-16 1979-03-16
BE794634A (en) 1972-01-28 1973-07-26 Rhone Poulenc Sa DIAPHRAGM SEPARATOR
US4359789A (en) 1972-01-31 1982-11-23 Monogram Industries, Inc. Sewerless disposal system
JPS5112313B2 (en) * 1972-09-01 1976-04-17
US3869376A (en) * 1973-05-14 1975-03-04 Alvaro R Tejeda System for demineralizing water by electrodialysis
JPS532160B2 (en) 1973-08-17 1978-01-25
US3870033A (en) * 1973-11-30 1975-03-11 Aqua Media Ultra pure water process and apparatus
US4089758A (en) * 1974-05-24 1978-05-16 Imperial Chemical Industries Limited Electrolytic process
US4167551A (en) 1974-10-21 1979-09-11 Mitsubishi Petrochemical Company Limited Process for the production of an ion exchange membrane
CH586059A5 (en) * 1974-11-29 1977-03-31 Yeda Res & Dev
JPS5247580A (en) 1975-10-14 1977-04-15 Mitsubishi Heavy Ind Ltd Desalting method by electrodialysis
US4032452A (en) * 1975-11-13 1977-06-28 Sybron Corporation Electrically regenerated ion exchange system
US4130473A (en) 1976-03-05 1978-12-19 Eddleman William L Electrode structure for use in metal in exchange apparatus useful in purifying spent acids and the like
US4102752A (en) 1976-07-09 1978-07-25 Rugh Ii John L Municipal water supply system
US4116889A (en) 1976-08-19 1978-09-26 Allied Chemical Corporation Bipolar membranes and method of making same
US4119581A (en) 1977-02-23 1978-10-10 California Institute Of Technology Membrane consisting of polyquaternary amine ion exchange polymer network interpenetrating the chains of thermoplastic matrix polymer
US4191811A (en) * 1977-03-01 1980-03-04 Ionics, Incorported Ion exchange membranes based upon polyphenylene sulfide and fluorocarbon polymeric binder
US4162218A (en) 1977-06-27 1979-07-24 Mccormick Gerald L Water reuse system
IL52758A0 (en) 1977-08-16 1977-10-31 Yeda Res & Dev Improved device for electrodialysis
IL52757A0 (en) 1977-08-16 1977-10-31 Yeda Res & Dev Dimensionally stable ion exchange membranes for electrodialysis
US4153761A (en) * 1978-04-21 1979-05-08 The United States Of America As Represented By The Secretary Of The Army Method of removing foulants from ion exchange resins
JPS5512141A (en) 1978-07-13 1980-01-28 Mitsubishi Petrochem Co Ltd Manufacturing of ion exchange membrane
US4197206A (en) * 1978-09-13 1980-04-08 Karn William S Heat sealable ion permeable membranes
US4228000A (en) 1979-01-08 1980-10-14 Hoeschler Frank A Water treatment apparatus with means for automatic disinfection thereof
US4374232A (en) * 1979-01-26 1983-02-15 Gelman Sciences Inc. Graft copolymer membrane and processes of manufacturing and using the same
US4216073A (en) 1979-05-29 1980-08-05 Ionics Inc. Ion exchange resin containing activated carbon
US4330654A (en) * 1980-06-11 1982-05-18 The Dow Chemical Company Novel polymers having acid functionality
US4358545A (en) 1980-06-11 1982-11-09 The Dow Chemical Company Sulfonic acid electrolytic cell having flourinated polymer membrane with hydration product less than 22,000
US4321145A (en) * 1980-06-11 1982-03-23 Carlson Lee G Ion exchange treatment for removing toxic metals and cyanide values from waste waters
US4298442A (en) 1980-08-04 1981-11-03 Ionics, Incorporated Electrodialysis process for silica removal
US4430226A (en) * 1981-03-09 1984-02-07 Millipore Corporation Method and apparatus for producing ultrapure water
US4465573A (en) 1981-05-12 1984-08-14 Hare Harry M O Method and apparatus for the purification of water
SU990256A1 (en) 1981-08-05 1983-01-23 Институт Твердого Тела И Переработки Минерального Сырья Со Ан Ссср Ion-exchange membrane
WO1983003984A1 (en) 1982-05-13 1983-11-24 Gerhard Kunz Method for the treatment of a liquid phase, particularly method for desalting aqueous solutions, as well as device for its implementation
SU1118389A1 (en) 1982-10-05 1984-10-15 Предприятие П/Я М-5885 Electric dialyzer
DE3238280A1 (en) 1982-10-15 1984-04-19 Hans-Wilhelm Prof. Dr.-Ing. 1000 Berlin Lieber Process for desalting solutions
US4505797A (en) * 1983-03-24 1985-03-19 Ionics, Incorporated Ion-exchange membranes reinforced with non-woven carbon fibers
US4473450A (en) 1983-04-15 1984-09-25 Raychem Corporation Electrochemical method and apparatus
US4636296A (en) * 1983-08-18 1987-01-13 Gerhard Kunz Process and apparatus for treatment of fluids, particularly desalinization of aqueous solutions
US4610790A (en) 1984-02-10 1986-09-09 Sterimatics Company Limited Partnership Process and system for producing sterile water and sterile aqueous solutions
US4574049B1 (en) * 1984-06-04 1999-02-02 Ionpure Filter Us Inc Reverse osmosis system
DE3423653A1 (en) 1984-06-27 1986-01-09 Gerhard K. Dipl.-Chem. Dr.-Ing. 5628 Heiligenhaus Kunz Method and device for metering in ions into liquids, in particular aqueous solutions
US4956071A (en) 1984-07-09 1990-09-11 Millipore Corporation Electrodeionization apparatus and module
US4931160A (en) * 1987-05-11 1990-06-05 Millipore Corporation Electrodeionization method and apparatus
US4925541B1 (en) * 1984-07-09 1994-08-02 Millipore Corp Electrodeionization apparatus and method
USRE35741E (en) * 1984-07-09 1998-03-10 Millipore Corporation Process for purifying water
US5154809A (en) 1984-07-09 1992-10-13 Millipore Corporation Process for purifying water
EP0170895B1 (en) 1984-07-09 1989-03-22 Millipore Corporation Improved electrodeionization apparatus and method
GB8513114D0 (en) * 1985-05-23 1985-06-26 Ici Plc Membranes
US4614576A (en) 1985-10-22 1986-09-30 Ionics, Incorporated Microliter scale electrodialysis apparatus
US4671863A (en) * 1985-10-28 1987-06-09 Tejeda Alvaro R Reversible electrolytic system for softening and dealkalizing water
ZA87553B (en) 1986-01-31 1988-03-30 Water Res Commission Dewatering slurries
US4661411A (en) * 1986-02-25 1987-04-28 The Dow Chemical Company Method for depositing a fluorocarbonsulfonic acid polymer on a support from a solution
EP0253119A3 (en) 1986-06-13 1989-07-19 Asahi Glass Company Ltd. Ion exchange membrane for electrolysis
JPH07106350B2 (en) 1986-07-31 1995-11-15 バブコツク日立株式会社 Operating method of electrodialysis desalination equipment
US4707240A (en) 1986-09-15 1987-11-17 Ionics Incorporated Method and apparatus for improving the life of an electrode
US4753681A (en) * 1986-09-30 1988-06-28 Millipore Corporation Method for defouling electrodeionization apparatus
US4747929A (en) * 1986-10-01 1988-05-31 Millipore Corporation Depletion compartment and spacer construction for electrodeionization apparatus
US4804451A (en) * 1986-10-01 1989-02-14 Millipore Corporation Depletion compartment for deionization apparatus and method
US4751153A (en) * 1987-01-02 1988-06-14 Continental Can Company, Inc. Frame for a cell construction
IT1202425B (en) 1987-01-26 1989-02-09 Giuseppe Bianchi ELECTROCHEMICAL DEOXYGENATION PROCESS FOR THE CONTROL OF CORROSION IN DEIONIZED WATERS
US4747955A (en) * 1987-04-13 1988-05-31 The Graver Company Purification of liquids with treated polyester fibers
US4808287A (en) 1987-12-21 1989-02-28 Hark Ernst F Water purification process
US4849102A (en) * 1988-05-31 1989-07-18 Filtron Technology Corporation Bidirectional ultrafiltration apparatus
US4871431A (en) 1988-07-11 1989-10-03 Ionics, Incorporated Apparatus for the removal of dissolved solids from liquids using bipolar membranes
US4969983A (en) 1988-07-11 1990-11-13 Ionics, Incorporated Apparatus and process for the removal of acidic and basic gases from fluid mixtures using bipolar membranes
US4915803A (en) * 1988-09-26 1990-04-10 The Dow Chemical Company Combination seal and frame cover member for a filter press type electrolytic cell
US4964970A (en) 1988-10-05 1990-10-23 Hoh Water Technology Corp. Compact low volume water purification apparatus
US4983267A (en) * 1988-10-18 1991-01-08 Innova/Pure Water, Inc. Water deionization and contaminants removal or degradation
CN1021828C (en) 1989-01-24 1993-08-18 上海市合成树脂研究所 Continuous prepn. of ion exchange membrane used for different phase
US5489370A (en) * 1989-05-08 1996-02-06 Ionex Removal of ions from a bulk source by electropotential ion transport using a host receptor matrix
US5254227A (en) 1989-06-16 1993-10-19 Olin Corporation Process for removing catalyst impurities from polyols
US5026465A (en) * 1989-08-03 1991-06-25 Ionics, Incorporated Electrodeionization polarity reversal apparatus and process
US5116509A (en) 1989-09-08 1992-05-26 Millipore Corporation Electrodeionization and ultraviolet light treatment method for purifying water
JPH0647105B2 (en) 1989-12-19 1994-06-22 株式会社荏原総合研究所 Purification method and device for pure water or ultrapure water
US5106465A (en) * 1989-12-20 1992-04-21 Olin Corporation Electrochemical process for producing chlorine dioxide solutions from chlorites
US5092970A (en) * 1989-12-20 1992-03-03 Olin Corporation Electrochemical process for producing chlorine dioxide solutions from chlorites
US5084148A (en) * 1990-02-06 1992-01-28 Olin Corporation Electrochemical process for producing chloric acid - alkali metal chlorate mixtures
US5203976A (en) * 1990-03-19 1993-04-20 Ionics, Incorporated Introducing and removing ion-exchange and other particulates rom an assembled electrodeionization stack
US5066375A (en) 1990-03-19 1991-11-19 Ionics, Incorporated Introducing and removing ion-exchange and other particulates from an assembled electrodeionization stack
US5120416A (en) * 1990-03-19 1992-06-09 Ionics, Incorporated Introducing and removing ion-exchange and other particulates from an assembled electrodeionization stack
US5059330A (en) 1990-04-02 1991-10-22 Burkhardt Donald O Gray water reclamation method and apparatus
US5196115A (en) * 1990-04-23 1993-03-23 Andelman Marc D Controlled charge chromatography system
US5192432A (en) 1990-04-23 1993-03-09 Andelman Marc D Flow-through capacitor
DE4016000C2 (en) 1990-05-18 1993-10-21 Hager & Elsaesser Device for the treatment of metal-containing liquids by ion exchange and simultaneous or periodic regeneration of the ion exchange resin by electrodialysis
US5032265A (en) 1990-06-20 1991-07-16 Millipore Corporation Method and system for producing sterile aqueous solutions
AU658845B2 (en) 1990-08-20 1995-05-04 Abbott Laboratories Medical drug formulation and delivery system
FR2666245B1 (en) 1990-08-31 1992-10-23 Lyonnaise Eaux METHOD FOR CONTROLLING THE OPERATING MODES OF AN AUTOMATIC WATER FILTRATION APPARATUS ON TUBULAR MEMBRANES.
US5126026A (en) * 1990-09-28 1992-06-30 Allied-Signal Inc. Guard membranes for use in electrodialysis cells
US5064097A (en) 1990-10-10 1991-11-12 Water Center International Ltd. Compact water purification and beverage dispensing apparatus
FR2668077B1 (en) 1990-10-22 1992-12-04 Commissariat Energie Atomique REVERSE OSMOSIS OR NANOFILTRATION MEMBRANE AND MANUFACTURING METHOD THEREOF.
US5082472A (en) * 1990-11-05 1992-01-21 Mallouk Robert S Composite membrane for facilitated transport processes
WO1992011089A1 (en) * 1990-12-17 1992-07-09 Ionpure Technologies Corporation Electrodeionization apparatus
US5176828A (en) * 1991-02-04 1993-01-05 Millipore Corporation Manifold segment stack with intermediate feed manifold
US5128043A (en) 1991-02-13 1992-07-07 Wildermuth Glen W Method and apparatus for purifying liquids
DE69204187T2 (en) * 1991-03-13 1996-01-25 Ebara Corp Electrically regenerable demineralization device.
IL97543A (en) 1991-03-14 1994-11-11 Yeda Res & Dev Electrodialysis reversal process and apparatus with bipolar membranes for hard-water softening
US5211823A (en) * 1991-06-19 1993-05-18 Millipore Corporation Process for purifying resins utilizing bipolar interface
US5259936A (en) 1991-06-19 1993-11-09 Millipore Corporation Purified ion exchange resins and process
US5107896A (en) 1991-07-09 1992-04-28 John J. Gianfrancesco Multi-functional valve
JPH05134094A (en) 1991-07-09 1993-05-28 Ebara Corp Elimination method and system of organic impurities in condensate
EP0531999A1 (en) 1991-09-11 1993-03-17 Asahi Glass Company Ltd. Method for producing an acid and/or alkali metal hydroxide
JPH05262902A (en) 1992-03-23 1993-10-12 Tanaka Kikinzoku Kogyo Kk Preparation of ion-exchange membrane
US5316740A (en) * 1992-03-26 1994-05-31 Los Alamos Technical Associates, Inc. Electrolytic cell for generating sterilization solutions having increased ozone content
EP0570341B1 (en) 1992-05-15 1996-09-18 Christ AG Apparatus for the continuous electrochemical desalination of aqueous solutions
US5166220A (en) 1992-06-01 1992-11-24 Mcmahon John M Water softening process
FR2692882B1 (en) 1992-06-29 1994-10-07 Trailigaz Process for treating, in particular drinking water, with ozone. Installation for the implementation of the process.
US5358640A (en) 1992-07-20 1994-10-25 Nalco Chemical Company Method for inhibiting scale formation and/or dispersing iron in reverse osmosis systems
US5292422A (en) * 1992-09-15 1994-03-08 Ip Holding Company Modules for electrodeionization apparatus
US5346924B1 (en) 1992-09-23 2000-04-25 Ionpure Techn Corp Heterogenous ion exchange materials comprising polyethylene of linear low density or high density high molecular weight
DE4238532A1 (en) 1992-11-14 1994-05-19 Kunz Gerhard K Method and device for desalting aqueous solutions using ion exchange materials
US5286354A (en) 1992-11-30 1994-02-15 Sachem, Inc. Method for preparing organic and inorganic hydroxides and alkoxides by electrolysis
US5346624A (en) 1993-01-11 1994-09-13 The Graver Company Method and apparatus for treatment of aqueous solutions
IN181196B (en) 1993-01-20 1998-04-25 Raju Manjarabad Venkataramanas
US5356849A (en) 1993-01-21 1994-10-18 Calgon Carbon Corporation Catalytic carbon
US5444031A (en) 1993-01-21 1995-08-22 Calgon Carbon Corporation Process for making catalytic carbon
JP2751090B2 (en) 1993-04-21 1998-05-18 日本錬水株式会社 Pure water production equipment
US5538611A (en) 1993-05-17 1996-07-23 Marc D. Andelman Planar, flow-through, electric, double-layer capacitor and a method of treating liquids with the capacitor
US6402916B1 (en) * 1993-10-27 2002-06-11 Richard L. Sampson Electrolytic process and apparatus controlled regeneration of modified ion exchangers to purify aqueous solutions and adjust ph
US5434020A (en) 1993-11-15 1995-07-18 The Regents Of The University Of California Continuous-feed electrochemical cell with nonpacking particulate electrode
US5411641A (en) * 1993-11-22 1995-05-02 E. I. Du Pont De Nemours And Company Electrochemical conversion of anhydrous hydrogen halide to halogen gas using a cation-transporting membrane
JPH07155750A (en) 1993-12-07 1995-06-20 Mitsubishi Rayon Co Ltd Hot-water sterilization method for water purifier
JP3187629B2 (en) 1993-12-16 2001-07-11 オルガノ株式会社 Reverse osmosis membrane treatment method
US5460728A (en) 1993-12-21 1995-10-24 Shell Oil Company Method for inhibiting the plugging of conduits by gas hydrates
US5518626A (en) * 1993-12-23 1996-05-21 United Technologies Corporation Process employing thermally sterilizable aqueous polishing agents
DE69522483T2 (en) * 1994-03-01 2002-04-25 Mitsubishi Chem Corp Method of demineralizing water or an aqueous liquid
JP3090841B2 (en) 1994-03-29 2000-09-25 オルガノ株式会社 Electric deionized water production equipment
WO1995026821A1 (en) 1994-03-30 1995-10-12 Tingsheng Wang Process and apparatus for regeneration of resins in fixed double-bed type
IL109240A (en) * 1994-04-07 1998-02-22 Yeda Res & Dev Ion exchange membranes
US5503729A (en) * 1994-04-25 1996-04-02 Ionics Incorporated Electrodialysis including filled cell electrodialysis (electrodeionization)
EP0683136A3 (en) 1994-05-06 1998-05-13 AEA Technology plc Silver removal
US5584981A (en) 1994-05-06 1996-12-17 United Kingdom Atomic Energy Authority Electrochemical deionization
EP0680932B1 (en) 1994-05-06 2001-08-08 AEA Technology plc Electrochemical deionisation
US5451309A (en) 1994-05-09 1995-09-19 B&W Nuclear Technologies, Inc. Ion exchange resin regeneration apparatus
US5425858A (en) * 1994-05-20 1995-06-20 The Regents Of The University Of California Method and apparatus for capacitive deionization, electrochemical purification, and regeneration of electrodes
US6309532B1 (en) 1994-05-20 2001-10-30 Regents Of The University Of California Method and apparatus for capacitive deionization and electrochemical purification and regeneration of electrodes
DE69532281T2 (en) 1994-05-20 2004-09-30 United States Filter Corp., Palm Desert METHOD AND DEVICE FOR ELECTRICAL DEIONIZATION WITH POLARITY SWITCHING AND DOUBLE REVERSE
DE4418812C2 (en) 1994-05-30 1999-03-25 Forschungszentrum Juelich Gmbh Single and multiple electrolysis cells and arrangements thereof for the deionization of aqueous media
US5538746A (en) 1994-06-17 1996-07-23 Levy; Ehud Process for filtering water prior to carbonation
US6241893B1 (en) 1994-06-17 2001-06-05 Ehud Levy Water filtration media, apparatus and processes
US20030038089A1 (en) 1994-06-17 2003-02-27 Ehud Levy Method of reducing contaminants in drinking water
US5460725A (en) 1994-06-21 1995-10-24 The Dow Chemical Company Polymeric adsorbents with enhanced adsorption capacity and kinetics and a process for their manufacture
US5538655A (en) 1994-06-29 1996-07-23 Arthur D. Little, Inc. Molecular complexes for use as electrolyte components
US5520816A (en) * 1994-08-18 1996-05-28 Kuepper; Theodore A. Zero waste effluent desalination system
US5458787A (en) 1994-10-27 1995-10-17 Uop Extraction of certain metal cations from aqueous solutions
US5599614A (en) * 1995-03-15 1997-02-04 W. L. Gore & Associates, Inc. Integral composite membrane
US5547551A (en) 1995-03-15 1996-08-20 W. L. Gore & Associates, Inc. Ultra-thin integral composite membrane
WO1997046492A1 (en) 1994-11-29 1997-12-11 Organo Corporation Process for producing deionized water by electrical deionization technique
WO1997046491A1 (en) 1994-11-29 1997-12-11 Organo Corporation Process for producing deionized water by electrical deionization technique
MY113226A (en) 1995-01-19 2001-12-31 Asahi Glass Co Ltd Porous ion exchanger and method for producing deionized water
CA2215977A1 (en) * 1995-03-23 1996-09-26 Arthur L. Goldstein Improvements in membrane processes including electrodialysis
US5783050A (en) 1995-05-04 1998-07-21 Eltech Systems Corporation Electrode for electrochemical cell
US5670053A (en) 1995-08-07 1997-09-23 Zenon Environmental, Inc. Purification of gases from water using reverse osmosis
US5766479A (en) * 1995-08-07 1998-06-16 Zenon Environmental Inc. Production of high purity water using reverse osmosis
DE19542475C2 (en) 1995-11-15 1999-10-28 Ballard Power Systems Polymer electrolyte membrane fuel cell and method for producing a distributor plate for such a cell
JP3518112B2 (en) 1995-12-06 2004-04-12 東京瓦斯株式会社 Fuel cell water treatment equipment
GB9600633D0 (en) 1996-01-12 1996-03-13 Glegg Water Conditioning Inc Elecrodeionization apparatus having geometric arrangement of ion exchange material
GB9602625D0 (en) * 1996-02-09 1996-04-10 Clegg Water Conditioning Inc Modular apparatus for the demineralisation of liquids
US5868937A (en) 1996-02-13 1999-02-09 Mainstream Engineering Corporation Process and system for recycling and reusing gray water
KR100441461B1 (en) * 1996-03-21 2004-10-02 그레그 워터 콘디셔닝 인코오포레이티드 Method and Apparatus for Producing Deionized Water
JP3468259B2 (en) 1996-03-22 2003-11-17 栗田工業株式会社 Deionized water production method
US5593563A (en) * 1996-04-26 1997-01-14 Millipore Corporation Electrodeionization process for purifying a liquid
US6248226B1 (en) * 1996-06-03 2001-06-19 Organo Corporation Process for producing deionized water by electrodeionization technique
RO114874B1 (en) 1996-06-21 1999-08-30 Sc Ind Etans Srl Process for making support boards for filter cells, fluid distribution system of micro- and ultrafiltration filter and mould for manufacturing the same
US5763774A (en) * 1996-08-01 1998-06-09 Millipore Corporation Fluid flow meter with reduced orientation sensitivity
US5868915A (en) 1996-09-23 1999-02-09 United States Filter Corporation Electrodeionization apparatus and method
WO1998017590A1 (en) 1996-10-23 1998-04-30 Aquatronics, Inc. Electrodialyzer and process for desalination
JPH10128338A (en) 1996-10-29 1998-05-19 Ebara Corp Method and device for preventing scale from being deposited in electric regeneration type continuous desalting apparatus
JP2000504273A (en) 1996-11-12 2000-04-11 ユナイテッド・ステイツ・フィルター・コーポレーション Electrodeionization apparatus and method
US5762774A (en) 1996-12-20 1998-06-09 Glegg Water Conditioning, Inc. Apparatus for the purification of liquids and a method of manufacturing and of operating same
US5788826A (en) 1997-01-28 1998-08-04 Pionetics Corporation Electrochemically assisted ion exchange
US6258278B1 (en) 1997-03-03 2001-07-10 Zenon Environmental, Inc. High purity water production
US6267891B1 (en) 1997-03-03 2001-07-31 Zenon Environmental Inc. High purity water production using ion exchange
JPH10277557A (en) 1997-04-10 1998-10-20 Asahi Glass Co Ltd Deionized water making apparatus
US5925240A (en) * 1997-05-20 1999-07-20 United States Filter Corporation Water treatment system having dosing control
US5868944A (en) * 1997-06-19 1999-02-09 Oxygen8, Inc. Oxygenated water cooler
US6780328B1 (en) 1997-06-20 2004-08-24 Li Zhang Fluid purification devices and methods employing deionization followed by ionization followed by deionization
WO1998058727A1 (en) 1997-06-20 1998-12-30 Ionics, Incorporated Fluid purification devices and methods employing deionization followed by ionization followed by deionization
JPH1142483A (en) 1997-07-28 1999-02-16 Sharp Corp Mineral water regulator
US6146524A (en) * 1997-09-15 2000-11-14 Story; Craig W. Multi-stage ozone injection water treatment system
CN1136153C (en) * 1997-10-23 2004-01-28 星崎电机株式会社 Electrolyzed water production apparatus
US5971368A (en) * 1997-10-29 1999-10-26 Fsi International, Inc. System to increase the quantity of dissolved gas in a liquid and to maintain the increased quantity of dissolved gas in the liquid until utilized
US6017433A (en) 1997-11-12 2000-01-25 Archer Daniels Midland Company Desalting aqueous streams via filled cell electrodialysis
KR100299139B1 (en) 1997-12-31 2001-11-14 윤종용 Decimation filter and method for the same
GB9802732D0 (en) 1998-02-09 1998-04-08 Elga Ltd Electrodialysis apparatus
US6402917B1 (en) * 1998-02-09 2002-06-11 Otv Societe Anonyme Electrodialysis apparatus
US6190528B1 (en) * 1998-03-19 2001-02-20 Xiang Li Helical electrodeionization apparatus
US6398965B1 (en) 1998-03-31 2002-06-04 United States Filter Corporation Water treatment system and process
US6099716A (en) 1998-05-26 2000-08-08 Proton Energy Systems, Inc. Electrochemical cell frame
US6171374B1 (en) * 1998-05-29 2001-01-09 Ballard Power Systems Inc. Plate and frame fluid exchanging assembly with unitary plates and seals
US6056878A (en) * 1998-08-03 2000-05-02 E-Cell Corporation Method and apparatus for reducing scaling in electrodeionization systems and for improving efficiency thereof
US6149788A (en) 1998-10-16 2000-11-21 E-Cell Corporation Method and apparatus for preventing scaling in electrodeionization units
US6197174B1 (en) 1998-11-25 2001-03-06 E-Cell Corporation Method and apparatus for electrodeionization of water using mixed bed and single phase ion exchange materials in the diluting compartment
US6190553B1 (en) * 1998-12-01 2001-02-20 Sangeul Lee Purification system for disposal of polluted or waste water using water plants
US6315886B1 (en) 1998-12-07 2001-11-13 The Electrosynthesis Company, Inc. Electrolytic apparatus and methods for purification of aqueous solutions
US6458257B1 (en) 1999-02-09 2002-10-01 Lynntech International Ltd Microorganism control of point-of-use potable water sources
US6428689B1 (en) 1999-01-27 2002-08-06 Sanyo Electric Co., Ltd. Water purifying and dispensing apparatus, and method of purifying chlorine-containing water
US6284124B1 (en) 1999-01-29 2001-09-04 United States Filter Corporation Electrodeionization apparatus and method
US6190558B1 (en) * 1999-04-01 2001-02-20 Nimbus Water Systems, Inc. Reverse osmosis purification system
IT1309792B1 (en) 1999-04-22 2002-01-30 Eltek Spa HOUSEHOLD APPLIANCES USING WATER, IN PARTICULAR A WASHING MACHINE, WITH PERFECTED DEVICE FOR BLAST CHILLING
AU4600400A (en) 1999-04-22 2001-05-08 Eltek S.P.A. Household appliance using water, namely a washing machine, with improved device for softening the water
US6482304B1 (en) 1999-05-07 2002-11-19 Otv Societe Anonyme Apparatus and method of recirculating electrodeionization
US6235166B1 (en) * 1999-06-08 2001-05-22 E-Cell Corporation Sealing means for electrically driven water purification units
EP1196353B1 (en) 1999-06-08 2011-02-09 E-Cell Corporation Sealing means for electrically driven water purification units and method of manufacturing thereof
JP3389889B2 (en) 1999-07-13 2003-03-24 栗田工業株式会社 Electric deionizer
US6254741B1 (en) 1999-08-05 2001-07-03 Stuart Energy Systems Corporation Electrolytic cells of improved fluid sealability
US6379518B1 (en) 1999-08-11 2002-04-30 Kurita Water Industries Ltd. Electrodeionization apparatus and pure water producing apparatus
JP3570304B2 (en) 1999-08-11 2004-09-29 栗田工業株式会社 Sterilization method of deionized water production apparatus and method of producing deionized water
US6214204B1 (en) * 1999-08-27 2001-04-10 Corning Incorporated Ion-removal from water using activated carbon electrodes
DE19942347B4 (en) 1999-09-04 2004-07-22 Dechema Gesellschaft Für Chemische Technik Und Biotechnologie E.V. Electrochemically regenerable ion exchanger
US6187162B1 (en) * 1999-09-13 2001-02-13 Leon Mir Electrodeionization apparatus with scaling control
US6296751B1 (en) 1999-09-13 2001-10-02 Leon Mir Electrodeionization apparatus with scaling control
JP2001079553A (en) 1999-09-16 2001-03-27 Kurita Water Ind Ltd Method for packing ion exchanger in electric deionizer, and electric deionizer
US6284399B1 (en) 1999-09-17 2001-09-04 Plug Power Llc Fuel cell system having humidification membranes
JP4197380B2 (en) 1999-09-17 2008-12-17 オルガノ株式会社 Electrodeionization equipment
JP3508647B2 (en) 1999-10-07 2004-03-22 栗田工業株式会社 Electrodeionization equipment
JP4172117B2 (en) 1999-10-14 2008-10-29 栗田工業株式会社 Electrodeionization equipment
JP4110689B2 (en) 1999-10-14 2008-07-02 栗田工業株式会社 Electrodeionization equipment
US6258265B1 (en) 1999-10-15 2001-07-10 James Phillip Jones Water purifying apparatus having a plurality of purifying stages and modular ion exchange media containers
JP3593932B2 (en) 1999-10-18 2004-11-24 栗田工業株式会社 High-purity water production apparatus and high-purity water production method
JP3801821B2 (en) 1999-10-29 2006-07-26 株式会社荏原製作所 Electric desalination equipment
US6503957B1 (en) 1999-11-19 2003-01-07 Electropure, Inc. Methods and apparatus for the formation of heterogeneous ion-exchange membranes
EP1106241A1 (en) * 1999-12-10 2001-06-13 Asahi Glass Company Ltd. Electro-regenerating type apparatus for producing deionized water
US6627073B2 (en) * 1999-12-16 2003-09-30 Sanyo Electric Co, Ltd. Water treatment device
FR2803284B1 (en) 2000-01-03 2002-04-12 Michel Bernard AUTOMATIC DRINKING WATER PURIFICATION DEVICE
EP1129765A1 (en) 2000-03-02 2001-09-05 Asahi Glass Company Ltd. Method for producing deionized water
US6274019B1 (en) * 2000-03-08 2001-08-14 Organo Corporation Electrodeionization apparatus
US6375812B1 (en) * 2000-03-13 2002-04-23 Hamilton Sundstrand Corporation Water electrolysis system
US6365023B1 (en) 2000-06-22 2002-04-02 Millipore Corporation Electrodeionization process
GB0016846D0 (en) 2000-07-10 2000-08-30 United States Filter Corp Electrodeionisation Apparatus
KR100465580B1 (en) 2000-07-13 2005-01-13 쿠리타 고교 가부시키가이샤 Electro-deionization device and method for operating the same
EP1307406A4 (en) 2000-08-11 2007-02-21 Ionics Device and method for electrodialysis
US6495014B1 (en) 2000-08-17 2002-12-17 University Of Chicago Electrodeionization substrate, and device for electrodeionization treatment
US6645383B1 (en) 2000-08-25 2003-11-11 Usf Consumer & Commercial Watergroup, Inc. Process and apparatus for blending product liquid from different TFC membranes
US20020144954A1 (en) 2000-09-28 2002-10-10 Arba John W. Electrodeionization device and methods of use
US7147785B2 (en) 2000-09-28 2006-12-12 Usfilter Corporation Electrodeionization device and methods of use
US20020103724A1 (en) 2000-12-01 2002-08-01 Stephen Huxter Courier independent system and method for the delivery of goods ordered by the internet
JP3794268B2 (en) 2001-01-05 2006-07-05 栗田工業株式会社 Electrodeionization apparatus and operation method thereof
US6607647B2 (en) 2001-04-25 2003-08-19 United States Filter Corporation Electrodeionization apparatus with expanded conductive mesh electrode and method
US6649037B2 (en) 2001-05-29 2003-11-18 United States Filter Corporation Electrodeionization apparatus and method
US6579445B2 (en) * 2001-06-01 2003-06-17 Sartorius Ag System for the production of laboratory grade ultrapure water
JP4507270B2 (en) * 2001-06-26 2010-07-21 三浦工業株式会社 Water softening device and regeneration control method thereof
US6607668B2 (en) 2001-08-17 2003-08-19 Technology Ventures, Inc. Water purifier
US6795298B2 (en) 2001-09-07 2004-09-21 Luxon Energy Devices Corporation Fully automatic and energy-efficient deionizer
JP4997678B2 (en) 2001-09-27 2012-08-08 栗田工業株式会社 Electrodeionization equipment
CA2464416C (en) 2001-11-05 2012-01-03 Bionomics Ltd. Apparatus and method for producing purified water having high microbiological purity
WO2003053859A1 (en) 2001-12-20 2003-07-03 Aquatech International Corporation Fractional deionization process
US20030155243A1 (en) 2002-02-21 2003-08-21 Eet Corporation Multi-path split cell spacer and electrodialysis stack design
US6808608B2 (en) * 2002-03-13 2004-10-26 Dionex Corporation Water purifier and method
US6758954B2 (en) 2002-04-11 2004-07-06 U.S. Filter Corporation Electrodeionization apparatus with resilient endblock
US20040188258A1 (en) 2002-05-17 2004-09-30 Yohei Takahashi Electric demineralizer
US7501061B2 (en) * 2002-10-23 2009-03-10 Siemens Water Technologies Holding Corp. Production of water for injection using reverse osmosis
US20040118780A1 (en) 2002-12-20 2004-06-24 Barnstead/Thermolyne Corporation Water purification system and method
US6929748B2 (en) * 2003-03-28 2005-08-16 Chemitreat Pte Ltd Apparatus and method for continuous electrodeionization
JP4384444B2 (en) 2003-05-29 2009-12-16 株式会社荏原製作所 Electric demineralizer and electrodialyzer
JP2005007348A (en) 2003-06-20 2005-01-13 Matsushita Electric Ind Co Ltd Electric deionizer
JP2005007347A (en) 2003-06-20 2005-01-13 Matsushita Electric Ind Co Ltd Electrodialysis type water purifier
US7604725B2 (en) 2003-11-13 2009-10-20 Siemens Water Technologies Holding Corp. Water treatment system and method
US7582198B2 (en) 2003-11-13 2009-09-01 Siemens Water Technologies Holding Corp. Water treatment system and method
US7862700B2 (en) 2003-11-13 2011-01-04 Siemens Water Technologies Holding Corp. Water treatment system and method
US20050103717A1 (en) * 2003-11-13 2005-05-19 United States Filter Corporation Water treatment system and method
US7083733B2 (en) 2003-11-13 2006-08-01 Usfilter Corporation Water treatment system and method
US8377279B2 (en) 2003-11-13 2013-02-19 Siemens Industry, Inc. Water treatment system and method
US7338595B2 (en) * 2003-11-13 2008-03-04 Culligan International Company Flow-through tank for water treatment
US7846340B2 (en) 2003-11-13 2010-12-07 Siemens Water Technologies Corp. Water treatment system and method
US7563351B2 (en) 2003-11-13 2009-07-21 Siemens Water Technologies Holding Corp. Water treatment system and method
US7329358B2 (en) 2004-05-27 2008-02-12 Siemens Water Technologies Holding Corp. Water treatment process
US7459088B2 (en) 2004-09-13 2008-12-02 The University Of South Carolina Water desalination process and apparatus
US20060231403A1 (en) 2005-04-14 2006-10-19 Riviello John M Chambered electrodeionization apparatus with uniform current density, and method of use

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3630378A (en) * 1968-05-24 1971-12-28 Dow Chemical Co Novel water treating and storage apparatus
US4655909A (en) * 1983-12-20 1987-04-07 Nippon Paint Co., Ltd. Water-deionizing system
USH1206H (en) * 1991-01-24 1993-07-06 The United States Of America As Represented By The Secretary Of The Air Force Cascade crossflow tower
US20020092769A1 (en) * 2000-07-13 2002-07-18 Benny Garcia Electrodeionization system
US20030089609A1 (en) * 2001-10-15 2003-05-15 United States Filter Corporation Apparatus for fluid purification and methods of manufacture and use thereof

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US8894834B2 (en) 2014-11-25
EP1682451A2 (en) 2006-07-26
WO2005049498A3 (en) 2006-11-09
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US20050103722A1 (en) 2005-05-19
US20060157422A1 (en) 2006-07-20

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