Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M16/00—Structural combinations of different types of electrochemical generators
  • H01M16/003—Structural combinations of different types of electrochemical generators of fuel cells with other electrochemical devices, e.g. capacitors, electrolysers
  • H01M16/006—Structural combinations of different types of electrochemical generators of fuel cells with other electrochemical devices, e.g. capacitors, electrolysers of fuel cells with rechargeable batteries
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
  • H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
  • H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
  • H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
  • H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
  • H01M8/0662—Treatment of gaseous reactants or gaseous residues, e.g. cleaning
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
  • H01M8/184—Regeneration by electrochemical means
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
  • H01M8/04298—Processes for controlling fuel cells or fuel cell systems
  • H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
  • H01M8/04858—Electric variables
  • H01M8/04925—Power, energy, capacity or load
  • H01M8/0494—Power, energy, capacity or load of fuel cell stacks
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
  • H01M8/249—Grouping of fuel cells, e.g. stacking of fuel cells comprising two or more groupings of fuel cells, e.g. modular assemblies
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/10—Energy storage using batteries
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/30—Hydrogen technology
  • Y02E60/50—Fuel cells

Definitions

• This invention relates generally to electrochemical cells, and more particularly, to fuel cells and ion pumps such as hydrogen pumps and oxygen pumps.
• Hydrogen is an important zero emission fuel. Recently, development of hydrogen fuel infrastructure systems has become a priority to support the use of hydrogen as a fuel.
• An important part of a hydrogen fuel infrastructure system is generation of hydrogen.
• Two methods are generally used for generating hydrogen.
• One method includes a reforming process for generating hydrogen, e.g., converting fuel such as natural gas or propane into a hydrogen-rich gas.
• Another method includes an electrolysis process which uses electrical energy to split water molecules into hydrogen and oxygen.
• the present invention provides in a first aspect, a combination fuel cell and ion pump which includes an electrochemical cell comprising an anode inlet for receiving fuel, an anode outlet for exhausting fuel, a cathode inlet for receiving oxidant, a cathode outlet for exhausting oxidant and at least one of purified oxygen and purified hydrogen, and a first electrical connector and a second electrical connector.
• a controller is operable for applying an electrical load to the first and the second electrical connectors wherein the electrochemical cell acts as a fuel cell to generate electricity, and applying an electrical potential to the first and the second electrical connectors wherein the electrochemical cell acts as at least one of a hydrogen pump to purify hydrogen and an oxygen pump to purify oxygen.
• the present invention provides in a second aspect, a combination fuel cell and hydrogen pump which includes a first electrochemical cell and a second electrochemical cell.
• the first electrochemical cell includes an anode inlet for receiving fuel, an anode outlet for exhausting fuel, a cathode inlet for receiving oxidant, a cathode outlet for exhausting oxidant, a purified hydrogen outlet for discharging purified hydrogen, and a first electrical connector and a second electrical connector.
• the second electrochemical cell includes an anode inlet for receiving fuel, an anode outlet for exhausting fuel, a cathode inlet for receiving oxidant, a cathode outlet for exhausting at least one of oxidant and purified hydrogen, and a first electrical connector and a second electrical connector.
• a valve is disposed between the first electrochemical cell and the second electrochemical cell.
• the valve includes a first passageway for transferring fuel from the first electrochemical cell to the second electrochemical cell, a second passageway for transferring exhaust fuel from the second electrochemical cell to the first electrochemical cell, a third passageway for controlling transfer of oxidant from the first electrochemical cell to the second electrochemical cell, a fourth passageway for controlling transfer of exhaust oxidant from the second electrochemical cell to the first electrochemical cell, and a fifth passageway for controlling transfer of purified hydrogen from the second electrochemical cell to the purified hydrogen outlet.
• the present invention provides in a third aspect, hydrogen infrastructure system and oxygen infrastructure systems which include the combination fuel cell and ion pump described above, a storage tank for storing purified hydrogen or purified oxygen from the combination fuel cell and ion pump, and a reformer for supplying fuel to the combination fuel cell and ion pump.
• the present invention provides in a fourth aspect, a method for generating electricity and purifying at least one of hydrogen and oxygen in which the method includes providing an electrochemical cell having an anode inlet for receiving fuel, an anode outlet for exhausting fuel, a cathode inlet for receiving oxidant, and a cathode outlet for exhausting oxidant and at least one of purified hydrogen and purified oxygen, and operating the electrochemical cell to generate electricity and at least one of purify hydrogen and purified oxygen.
• FIG. 1 is a diagrammatic illustration of a combination fuel cell and hydrogen pump in accordance with the present invention
• FIG. 2 is a diagrammatic illustration of the combination fuel cell and hydrogen pump of FIG. 1 configured as a fuel cell;
• FIG. 3 is a diagrammatic illustration of the combination fuel cell and hydrogen pump of FIG. 1 configured as a hydrogen pump;
• FIG. 4 is a diagrammatic illustration of an alternative embodiment of a combination fuel cell and hydrogen pump in accordance with the present invention configured as a fuel cell;
• FIG. 5 is a diagrammatic illustration of the combination fuel cell and hydrogen pump of FIG. 4 configured as a fuel cell and hydrogen pump;
• FIG. 6 is a flowchart of a method for generating electricity and purifying hydrogen in accordance with the present invention.
• FIG. 7 is a diagrammatic illustration of a hydrogen fuel infrastructure system in accordance with the present invention.
• FIG. 8 is a diagrammatic illustration of a combination fuel cell and oxygen pump in accordance with the present invention.
• FIG. 9 is a diagrammatic illustration of the combination fuel cell and oxygen pump of FIG. 8 configured as a fuel cell
• FIG. 10 is a diagrammatic illustration of the combination fuel cell and oxygen pump of FIG. 8 configured as an oxygen pump;
• FIG. 11 is a flowchart of a method for generating electricity and purifying oxygen in accordance with the present invention.
• FIG. 12 is a diagrammatic illustration of an oxygen infrastructure system in accordance with the present invention.
• FIG. 1 illustrates a combination fuel cell and ion pump 10 which may be configured in a fuel cell mode for generating electricity and in a hydrogen pump mode for purifying and/or compressing hydrogen, and which may be suitably employed in a hydrogen fuel infrastructure system.
• Hydrogen fuel infrastructure systems such as refueling stations may have multiple functions, e.g., hydrogen production, electricity production, and heat generation.
• the present invention overcomes the drawback of having to provide two separate devices such as a fuel cell for generating electricity and a hydrogen pump for purifying and/or compressing hydrogen. Such a combination also reduces the costs and also the space required compared to providing two separate devices.
• Combination 10 generally includes at least one electrochemical cell, for example which may be a stack 20 of electrochemical cells as illustrated in FIG. 1, having an anode inlet 22 for receiving a fuel such as reformate, an anode outlet 24 for exhausting fuel such as reformate, a cathode inlet 26 for receiving an oxidant such as air, a cathode outlet 28 for exhausting oxidant such as air or purified hydrogen, and a first electrical connector 32 and a second electrical connector 34 for applying an electrical load or an electrical potential to stack 20.
• electrochemical cell for example which may be a stack 20 of electrochemical cells as illustrated in FIG. 1, having an anode inlet 22 for receiving a fuel such as reformate, an anode outlet 24 for exhausting fuel such as reformate, a cathode inlet 26 for receiving an oxidant such as air, a cathode outlet 28 for exhausting oxidant such as air or purified hydrogen, and a first electrical connector 32 and a second electrical connector 34 for applying an electrical load or an electrical potential to
• a first valve 46 is attached to cathode inlet 26 for controlling oxidant to stack 20.
• a second valve 48 is attached to cathode outlet 28 for either exhausting oxidant from stack 20 in a first direction or exhausting purified hydrogen in a second direction different from the first direction.
• a controller 50 is attached to first electrical connector 32 and second electrical connector 34 for applying either an electrical load to stack 20 for generating electricity, or an electrical potential to stack 20 for purifying hydrogen.
• Controller 50 may include electrical output terminals 62 and 64 for applying an electrical load to stack 20.
• a rechargeable battery may be connected to electrical output terminals 62 and 64.
• Controller 50 may also include electrical input terminals 72 and 74 for applying an electrical potential to stack 20.
• Controller 50 may include mechanical switch or switches or may be automated and include a microprocessor or microcontroller.
• Stack 20 may be categorized according to the type of electrolyte (for example, solid polymer, polybenzimidazole (PBI) based membrane, alkaline, or phosphoric acid) used to accommodate ion transfer during operation.
• PBI polybenzimidazole
• combination 10 may include a solid polymer electrochemical cell comprising a membrane electrode assembly (MEA).
• MEA typically includes a solid polymer membrane or proton exchange membrane (PEM) sandwiched between and in contact with two electrodes: one electrode commonly referred to as the anode and the other electrode commonly referred to as the cathode.
• the membrane is typically made of a porous, electrically-conducting sheet material.
• the electrodes are typically made from carbon-fiber paper or cloth.
• a catalyst layer may be provided to facilitate the electrochemical reaction.
• the MEA is placed between two electrically conductive graphite plates, which have one or more reactant flow passages impressed on the surface.
• the reactant flow passages direct the flow of reactants (e.g., reformate or air) to the membrane electrode assembly.
• reactants e.g., reformate or air
• a plurality of electrochemical cells may be formed into a stack with suitable manifolds therein for transferring the reactants to and from each of the plurality of cells.
• FIG. 2 illustrates combination 10 configured in a fuel cell mode for generating electricity.
• fuel is supplied to anode inlet 22 and exhausted via anode outlet 24, first valve 46 is operated to allow a supply of oxidant to cathode inlet 26, and second valve 48 is operated to exhaust oxidant from cathode outlet 28 in a first direction, e.g., to a vent.
• Electrical output terminals 62 and 64 of controller 50 are connected to an electrical load which load is applied across stack 20 via electrical connectors 32 and 34.
• a catalyst coating on the anode helps to separate the gas into protons (hydrogen ions) and electrons.
• the electrolyte membrane in the center allows only the protons to pass through the membrane to the cathode side of the electrochemical cell.
• the electrons cannot pass through this membrane and flow through an external circuit in the form of electric current.
• oxidant e.g., oxygen in air
• another catalyst coating helps the oxygen, protons, and electrons combine to produce pure water and heat.
• FIG. 3 illustrates combination 10 configured in a hydrogen pump mode for purifying and/or compressing hydrogen.
• fuel such as reformate is supplied to anode inlet 22 and exhausted via anode outlet 24
• first valve 46 is operated to close or block the supply of oxidant to cathode inlet 26
• second valve 48 is operated to direct purified hydrogen in a second direction (e.g., the first direction for directing exhaust oxidant as shown in FIG. 2 is closed or blocked).
• Electrical input terminals 72 and 74 of controller 50 may be connected to a power supply for providing an electrical potential across stack 20 via electrical connectors 32 and 34.
• combination 10 in a hydrogen pump mode, fuel flows into the electrochemical cell anode, electrical energy is supplied between the electrodes to overcome the internal resistance of the electrochemical cell, dissociate the hydrogen in the gas-to-be treated to protons, and drive the protons through the membrane to the opposite side for recovery as purified and/or pressurized hydrogen at the cathode outlet.
• the hydrogen stream may be stored or may be humidified by introduction of water and then stored.
• a humidified purified hydrogen may also be produced using an electrochemical cell which includes NAFION which allows the transfer of water as well as hydrogen.
• FIGS. 4 and 5 illustrate an alternative embodiment of a combination fuel cell and hydrogen pump 100 which may be configured in a fuel cell mode for generating electricity and in a hydrogen pump mode for purifying and/or compressing hydrogen.
• Combination 100 may also be suitably employed in a hydrogen fuel infrastructure system.
• combination 100 is partitioned or includes two portions which may be suitably configured and operated so that combination 100 may operate in fuel cell mode, or in both a fuel cell mode and a hydrogen pump mode.
• Combination 100 generally includes at least one first electrochemical cell, for example a first stack 120 of electrochemical cells, and at least one second electrochemical cell, for example a second stack 121 of electrochemical cells.
• a valve 140 may be sandwiched between first stack 120 and second stack 121.
• Valve 140 may include a housing 141 having a first passageway 142, and a second passageway 143, and a chamber 144. Disposed in chamber 144 is a slidable member 145 having a third passageway 146, a fourth passageway 147, and a fifth passageway 148.
• Combination 100 may also include an anode inlet 122 for receiving fuel such as reformate for first stack 120 and second stack 121, an anode outlet 124 for exhausting fuel from first stack 120 and second stack 121, a cathode inlet 126 for receiving oxidant such as air for first stack 120 and second stack 121, a cathode outlet 127 for exhausting oxidant from first stack 120 and second stack 121, and a purified hydrogen outlet 129 for discharging purified hydrogen from second stack 121.
• Stack 120 may further include a first electrical connector 132 and a second electrical connector 134 for applying an electrical load to first stack 120.
• Stack 121 may further include a first electrical connector 136 and a second electrical connector 138 for applying an electrical load or an electrical potential to second stack 121.
• a controller 150 is attached to electrical connectors 132, 134, 136, and 138 for applying an electrical load to first stack 120 and second stack 121 for generating electricity, or applying an electrical load to first stack 120 for generating electricity and applying an electrical potential to stack 121 for purifying hydrogen.
• Controller 150 may include a mechanical switch or switches, or may be automated and include a microprocessor or microcontroller.
• FIG. 4 illustrates the configuration of combination 100 wherein both first stack 120 and second stack 121 are operated in a fuel cell mode for generating electricity. For example, fuel such as reformate is supplied to anode inlet 122 for both stack 120 and stack 121, and exhausted via anode outlet 124 from both stack 120 and stack 121.
• Oxidant such as air is supplied to a cathode inlet 126.
• Valve 140 is positioned (e.g., using a suitable actuator under control of controller 150) so that oxidant is directed to the electrochemical cells of both stack 120 and stack 121, and also exhausted from the electrochemical cells of both stack 120 and stack 121.
• valve 140 is positioned so that the supply of oxidant passes through first passageway 146 to second stack 121, and exhaust oxidant from second stack passes through passageway 147.
• a load applied across electrical output terminals 162 and 164 of controller 150 may be operably applied across stack 120 and stack 121.
• the load maybe applied across electrical connector 132 of stack 120 and electrical connector 138 of stack 121, with electrical connector 134 of stack 120 connected to electrical connector 136 of stack 121. Accordingly, both stacks contribute to the generation of electrical power.
• FIG. 4 illustrates the wiring of the two stacks in series, it will be appreciated that parallel wiring, or separate wiring of the two stacks may also be employed.
• FIG. 5 illustrates the configuration of combination 100 wherein first stack 120 is operated in a fuel cell mode for generating electricity, and second stack 121 is operated in a hydrogen pump mode for purifying hydrogen.
• fuel such as reformate is supplied to anode inlet 122 for both stack 120 and stack 121, and exhausted via anode outlet 124 from stack 120 and stack 121.
• Oxidant such as air is supplied to cathode inlet 126.
• Valve 140 is positioned (e.g., using a suitable actuator under control of controller 150) so that oxidant via passageway 146 to stack 121 is blocked, exhaust from stack 121 via passageway 147 is blocked, and purified hydrogen from stack 121 is directed via passageway 148 to purified hydrogen outlet 129.
• a load applied across electrical output terminals 162 and 164 of controller 150 is operably applied across electrical connector 132 and electrical connector 134 of stack 120, while a direct current power supply attached to electrical input terminals 172 and 174 is electrically connected to electrical connector 136 and electrical connector 138 of stack 121. Accordingly, stack 120 contributes to the generation of electrical power, while stack 121 contributes to the purification of hydrogen.
• stack 121 and valve 140 are similar to stack 20 and valves 46 and 48, e.g., valve 140 is comparable to valves 46 and 48. It will also be appreciated that other valve configuration and valving devices may be suitably employed for effecting the various gas flows.
• FIG. 6 illustrates a method 200 for generating electricity and purifying hydrogen.
• the method includes a step 210 of providing an electrochemical cell having an anode inlet for receiving fuel, an anode outlet for exhausting fuel, a cathode inlet for receiving oxidant, and a cathode outlet for exhausting at least one of oxidant and purified hydrogen, and a step 220 of operating the electrochemical cell to generate electricity and purify hydrogen.
• operating the electrochemical cell to generate electricity may include applying an electrical load to the electrochemical cell.
• Operating the electrochemical cell to purify hydrogen may include applying an electrical potential to the electrochemical cell.
• a combination in accordance with the present invention may also be partitioned into more than two portions or include more than two electrochemical cell stacks.
• the amount of power generation and hydrogen purification may be variably controlled.
• the stacks may be wired such that direct current power generated by one portion of the stack (e.g., operating in a fuel cell mode) may provide the direct current power supply for another part of the stack (e.g., operating in a hydrogen pump mode).
• the combinations may be operated in the hydrogen pump mode periodically to remove contaminants from the electrode/catalyst structures of the electrochemical cells to improve long-life performance of the electrochemical cells in the power generation and/or the hydrogen purification modes.
• the combinations may also be designed with the stacks formed of electrochemical cells that can withstand pressurization of at least the cathode side of the cell so that in the hydrogen pump mode, hydrogen can be compressed as well as purified.
• the combinations may further be fitted with additional valves and piping such that nitrogen or another inert gas may be used as a purge flow when switching operations of the stack (or portions thereof) between power generation and hydrogen purification modes.
• FIG. 7 is an example of one embodiment of a hydrogen fuel infrastructure system 300 in accordance with the present invention which may include a reformer 310 such as a catalytic partial oxidation (CPO) reformer, a steam reformer, or an autothermal reformer for converting a hydrocarbon such as methane or methanol into a hydrogen-rich stream, a carbon monoxide cleanup device 320 for reducing the amount of carbon monoxide in the reformate, a combination fuel cell and hydrogen pump system 330 such as described above for generating electricity and purifying hydrogen, a hydrogen storage unit 340, and an electrical storage unit 350 such as a battery.
• the system may also include a furnace 360.
• the system may be disposed in a service station for providing a supply of hydrogen for use in motor vehicles. It will be appreciated that the system may also be disposed in a building or home for generation of electricity, and purifying hydrogen which may be stored for later use.
• FIG. 8 illustrates a combination fuel cell and oxygen pump 400 which may be configured in a fuel cell mode for generating electricity and in an oxygen pump mode for purifying and/or compressing oxygen, and which may be suitably employed in an oxygen infrastructure system.
• This type of device may be valuable in the medical field such as in hospitals or on submarines where there exists a need for both electrical generation and pure oxygen generation.
• Combination 400 generally includes at least one electrochemical cell, for example which may be a stack 420 of electrochemical cells as illustrated in FIG. 8, having an anode inlet 422 for receiving a fuel such as reformate, an anode outlet 424 for exhausting fuel such as reformate, a cathode inlet 26 for receiving an oxidant such as air, a cathode outlet 428 for exhausting oxidant such as air or purified hydrogen, and a first electrical connector 432 and a second electrical connector 434 for applying an electrical load or an electrical potential to stack 420.
• a fuel such as reformate
• an anode outlet 424 for exhausting fuel such as reformate
• a cathode inlet 26 for receiving an oxidant such as air
• a cathode outlet 428 for exhausting oxidant such as air or purified hydrogen
• a first electrical connector 432 and a second electrical connector 434 for applying an electrical load or an electrical potential to stack 420.
• a first valve 446 is attached to anode inlet 422 for controlling fuel to stack 420.
• a second valve 448 is attached to cathode outlet 428 for either exhausting oxidant from stack 420 in a first direction or exhausting purified oxygen in a second direction different from the first direction.
• a controller 450 is attached to first electrical connector 432 and second electrical connector 434 for applying either an electrical load to stack 420 for generating electricity, or an electrical potential to stack 420 for purifying oxygen.
• Controller 450 may include electrical output terminals 462 and 464 for applying an electrical load to stack 420.
• a rechargeable battery may be connected to electrical output terminals 462 and 464.
• Controller 450 may also include electrical input terminals 472 and 474 for applying an electrical potential to stack 420.
• Controller 450 may include mechanical switch or switches, or may be automated and include a microprocessor or microcontroller.
• Combination 400 may include a solid oxide electrochemical cell having a hard ceramic electrolyte which is operated at temperatures up to about 1,000 degrees C (about 1,800 degrees F).
• a mixture of zirconium oxide and calcium oxide may form a crystal lattice, though other oxide combinations may be used as electrolytes.
• the solid electrolyte may also be coated on both sides with specialized porous electrode materials.
• FIG. 9 illustrates combination 10 configured in a fuel cell mode for generating electricity.
• first valve 446 is operated to allow a supply of fuel to anode inlet 422 and exhausted via anode outlet 424
• oxidant is supplied to cathode inlet 426
• second valve 448 is operated to exhaust oxidant from cathode outlet 428 in a first direction, e.g., to a vent.
• Electrical output terminals 462 and 464 of controller 450 are connected to an electrical load which load is applied across stack 420 via electrical connectors 432 and 434.
• FIG. 10 illustrates combination 400 configured in an oxygen pump mode for purifying and/or compressing oxygen.
• first valve 446 is operated to close or block the supply of fuel such as reformate to anode inlet 422
• a supply of oxidant is provided to cathode inlet 426
• second valve 448 is operated to direct purified oxygen in a second direction (e.g., the first direction for directing exhaust oxidant as shown in FIG. 9 is closed or blocked).
• Electrical input terminals 472 and 474 of controller 450 may be connected to a power supply for providing an electrical potential across stack 420 via electrical connectors 432 and 434.
• oxidant such as air flows into the electrochemical cell anode, electrical energy is supplied between the electrodes to overcome the internal resistance of the electrochemical cell, dissociate the oxygen in the gas-to-be treated to protons, and drive the protons through the solid oxide to the opposite side for recovery as purified and/or pressurized oxygen at the cathode outlet.
• the oxygen stream may be stored.
• FIG. 11 illustrates a method 500 for generating electricity and purifying oxygen.
• the method includes a step 510 of providing an electrochemical cell having an anode inlet for receiving fuel, an anode outlet for exhausting fuel, a cathode inlet for receiving oxidant such as air, and a cathode outlet for exhausting at least one of oxidant and purified oxygen, and a step 520 of operating the electrochemical cell to generate electricity and purify oxygen.
• operating the electrochemical cell to generate electricity may include applying an electrical load to the electrochemical cell.
• Operating the electrochemical cell to purify oxygen may include applying an electrical potential to the electrochemical cell.
• FIG. 12 is an example of one embodiment of a oxygen infrastructure system 600 in accordance with the present invention which may include a reformer 610 such as a catalytic partial oxidation (CPO) reformer, a steam reformer, or an autothermal reformer for converting a hydrocarbon such as methane or methanol into a hydrogen-rich stream, a carbon monoxide cleanup device 620 for reducing the amount of carbon monoxide in the reformate, a combination fuel cell and oxygen pump 630 such as described above for generating electricity and purifying oxygen, an oxygen storage unit 640, and an electrical storage unit 650 such as a battery.
• the system may also include a furnace 660.

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• 2003
  • 2003-09-09 US US10/658,123 patent/US7252900B2/en not_active Expired - Fee Related
• 2004
  • 2004-09-08 JP JP2006526245A patent/JP4589925B2/ja not_active Expired - Fee Related
  • 2004-09-08 WO PCT/US2004/029198 patent/WO2005024975A2/en not_active Ceased
• 2007
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