CA2694153A1 - Steam reformation fuel cell with waste heat cogeneration turbine heat to energy pyroelectric crystals and/or thermo-coupling any and all waste heat to energy technologies and/or new macro-micros fuel cell power plant design - Google Patents
Steam reformation fuel cell with waste heat cogeneration turbine heat to energy pyroelectric crystals and/or thermo-coupling any and all waste heat to energy technologies and/or new macro-micros fuel cell power plant design Download PDFInfo
- Publication number
- CA2694153A1 CA2694153A1 CA2694153A CA2694153A CA2694153A1 CA 2694153 A1 CA2694153 A1 CA 2694153A1 CA 2694153 A CA2694153 A CA 2694153A CA 2694153 A CA2694153 A CA 2694153A CA 2694153 A1 CA2694153 A1 CA 2694153A1
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- fuel
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- fuel cell
- cathode
- heat
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- 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
- H01M8/22—Fuel cells in which the fuel is based on materials comprising carbon or oxygen or hydrogen and other elements; Fuel cells in which the fuel is based on materials comprising only elements other than carbon, oxygen or hydrogen
-
- 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
- H01M8/0637—Direct internal reforming at the anode of the fuel cell
-
- 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
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1009—Fuel cells with solid electrolytes with one of the reactants being liquid, solid or liquid-charged
- H01M8/1011—Direct alcohol fuel cells [DAFC], e.g. direct methanol fuel cells [DMFC]
- H01M8/1013—Other direct alcohol fuel cells [DAFC]
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/40—Combination of fuel cells with other energy production systems
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
Any all technologies including... MCFC and SOFC...
Note our bio fuels to energy Super Fuel Cell do not use any combustion processes and therefore do not produce any green house gases.
SUPER FUEL CELL Methane, Ethanol, Butane, Hydrogen...Any and all fuels.
Macro Upper Large Scale Fast and Mass Production per time. Probably Cheaper.
1. The nozzles that injects new unreacted fuel in the direction of the anode.
Heat produced from the reaction can be used for turbine co-generation.
2. The direction of the fuel down the channels.
3. The Anode Electrode.
4. The Cathode (where oxygen enters and reacts).
5. The Electrolyte.
Multiple Micro Scale Higher Yield per concentration of fuel left in the mixture ie. biogas is often contaminated with other gases present, therefore concentration per bulk/volume of the rest of the gases varies. By using multiple Micro Fuel Cells we 1. Maintain the same speed of throughput as the Macro part of the Super Fuel Cell Above so there is no backing up 2. Micro Fuel Cells are more efficient at reacting with the reactable fuels since the channel is thinner and therefore less fuel is exposed to more electrodes...meaning more of the reactable fuel molecules pass over the surface of the electrodes allowing for more fuel molecules access to the surface of the electrode(s) such that there is less dead space between the electrode and the outer walls of the channel...to capture the most fuel conversion, from the total mixture.
6. Cathode Outer Wall and Cathode Channel.
7. Cathode Electrode.
8. The Anode Electrode.
9. The Anode Outer Wall and Anode Channel. The bottom channel is narrowed to the optimal size for viable fuel cell stationary power plant capacity, then they feed into Multiple Micro fuel cells (possibly Proton Exchange Membrane - which are cheaper) the hot (high temperature) is run through waste heat to en energy (such as co-generation, pyroelectric crystals, thermo-coupling and any and all Heat to Energy Technologies) whereas the materials for MCFC and SOFC are expensive to replace and heavy. We might even use circular outer walls in the Multiple Micro technologies to redirect the secondary processed fuel and/or use smaller jets/sprays to get higher concentration of fuel into the depleted side facing the anode to replenish the side facing the electrode that has been depleted/spent from reacting with the anode.
We do the opposite with the cathode side of the fuel cell.
Additionally Biogas/Methane/CH4 are also steam reformed directly inside the Anode Channel by the heat produced by the reaction.
Excess heat can be used for:
1. Co-Generation.
2. Pyroelectric Crystals.
3. Thermo-Coupling.
4. Any and All Heat Waste to Energy Technologies.
To deal with the problem of carbon deposits we could scrub biogas to remove the tar before entering the fuel cell, use cleanable electrodes and/or replaceable electrodes; we could also configure the each of the anode and cathode each in layers, an outer shield (made of less expensive materials) to allow deposit of carbon on its surface, and thick back (inner) anode that could produce a stronger current to increase efficiency (perhaps made of a more conductive material).
Note our bio fuels to energy Super Fuel Cell do not use any combustion processes and therefore do not produce any green house gases.
SUPER FUEL CELL Methane, Ethanol, Butane, Hydrogen...Any and all fuels.
Macro Upper Large Scale Fast and Mass Production per time. Probably Cheaper.
1. The nozzles that injects new unreacted fuel in the direction of the anode.
Heat produced from the reaction can be used for turbine co-generation.
2. The direction of the fuel down the channels.
3. The Anode Electrode.
4. The Cathode (where oxygen enters and reacts).
5. The Electrolyte.
Multiple Micro Scale Higher Yield per concentration of fuel left in the mixture ie. biogas is often contaminated with other gases present, therefore concentration per bulk/volume of the rest of the gases varies. By using multiple Micro Fuel Cells we 1. Maintain the same speed of throughput as the Macro part of the Super Fuel Cell Above so there is no backing up 2. Micro Fuel Cells are more efficient at reacting with the reactable fuels since the channel is thinner and therefore less fuel is exposed to more electrodes...meaning more of the reactable fuel molecules pass over the surface of the electrodes allowing for more fuel molecules access to the surface of the electrode(s) such that there is less dead space between the electrode and the outer walls of the channel...to capture the most fuel conversion, from the total mixture.
6. Cathode Outer Wall and Cathode Channel.
7. Cathode Electrode.
8. The Anode Electrode.
9. The Anode Outer Wall and Anode Channel. The bottom channel is narrowed to the optimal size for viable fuel cell stationary power plant capacity, then they feed into Multiple Micro fuel cells (possibly Proton Exchange Membrane - which are cheaper) the hot (high temperature) is run through waste heat to en energy (such as co-generation, pyroelectric crystals, thermo-coupling and any and all Heat to Energy Technologies) whereas the materials for MCFC and SOFC are expensive to replace and heavy. We might even use circular outer walls in the Multiple Micro technologies to redirect the secondary processed fuel and/or use smaller jets/sprays to get higher concentration of fuel into the depleted side facing the anode to replenish the side facing the electrode that has been depleted/spent from reacting with the anode.
We do the opposite with the cathode side of the fuel cell.
Additionally Biogas/Methane/CH4 are also steam reformed directly inside the Anode Channel by the heat produced by the reaction.
Excess heat can be used for:
1. Co-Generation.
2. Pyroelectric Crystals.
3. Thermo-Coupling.
4. Any and All Heat Waste to Energy Technologies.
To deal with the problem of carbon deposits we could scrub biogas to remove the tar before entering the fuel cell, use cleanable electrodes and/or replaceable electrodes; we could also configure the each of the anode and cathode each in layers, an outer shield (made of less expensive materials) to allow deposit of carbon on its surface, and thick back (inner) anode that could produce a stronger current to increase efficiency (perhaps made of a more conductive material).
Description
Description Any all technologies including... MCFC and SOFC...
Note our bio fuels to energy Super Fuel Cell do not use any combustion processes and therefore do not produce any green house gases.
SUPER FUEL CELL Methane, Ethanol, Butane, Hydrogen...Any and all fuels.
Macro Upper Large Scale Fast and Mass Production per time. Probably Cheaper.
1. The nozzles that injects new unreacted fuel in the direction of the anode.
Heat produced from the reaction can be used for turbine co-generation.
Note our bio fuels to energy Super Fuel Cell do not use any combustion processes and therefore do not produce any green house gases.
SUPER FUEL CELL Methane, Ethanol, Butane, Hydrogen...Any and all fuels.
Macro Upper Large Scale Fast and Mass Production per time. Probably Cheaper.
1. The nozzles that injects new unreacted fuel in the direction of the anode.
Heat produced from the reaction can be used for turbine co-generation.
2. The direction of the fuel down the channels.
3. The Anode Electrode.
4. The Cathode (where oxygen enters and reacts).
5. The Electrolyte.
Multiple Micro Scale Higher Yield per concentration of fuel left in the mixture ie. biogas is often contaminated with other gases present, therefore concentration per bulk/volume of the rest of the gases varies. By using multiple Micro Fuel Cells we 1. Maintain the same speed of throughput as the Macro part of the Super Fuel Cell Above so there is no backing up 2. Micro Fuel Cells are more efficient at reacting with the reactable fuels since the channel is thinner and therefore less fuel is exposed to more electrodes... meaning more of the reactable fuel molecules pass over the surface of the electrodes allowing for more fuel molecules access to the surface of the electrode(s) such that there is less dead space between the electrode and the outer walls of the channel...to capture the most fuel conversion, from the total mixture.
Multiple Micro Scale Higher Yield per concentration of fuel left in the mixture ie. biogas is often contaminated with other gases present, therefore concentration per bulk/volume of the rest of the gases varies. By using multiple Micro Fuel Cells we 1. Maintain the same speed of throughput as the Macro part of the Super Fuel Cell Above so there is no backing up 2. Micro Fuel Cells are more efficient at reacting with the reactable fuels since the channel is thinner and therefore less fuel is exposed to more electrodes... meaning more of the reactable fuel molecules pass over the surface of the electrodes allowing for more fuel molecules access to the surface of the electrode(s) such that there is less dead space between the electrode and the outer walls of the channel...to capture the most fuel conversion, from the total mixture.
6. Cathode Outer Wall and Cathode Channel.
7. Cathode Electrode.
8. The Anode Electrode.
9. The Anode Outer Wall and Anode Channel. The bottom channel is narrowed to the optimal size for viable fuel cell stationary power plant capacity, then they feed into Multiple Micro fuel cells (possibly Proton Exchange Membrane - which are cheaper) the hot (high temperature) is run through waste heat to en energy (such as co-generation, pyroelectric crystals, thermo-coupling and any and all Heat to Energy Technologies) whereas the materials for MCFC and SOFC are expensive to replace and heavy. We might even use circular outer walls in the Multiple Micro technologies to redirect the secondary processed fuel and/or use smaller jets/sprays to get higher concentration of fuel into the depleted side facing the anode to replenish the side facing the electrode that has been depleted/spent from reacting with the anode.
We do the opposite with the cathode side of the fuel cell.
Additionally Biogas/Methane/CH4 are also steam reformed directly inside the Anode Channel by the heat produced by the reaction.
Excess heat can be used for:
1. Co-Generation.
2. Pyroelectric Crystals.
3. Thermo-Coupling.
4. Any and All Heat Waste to Energy Technologies.
To deal with the problem of carbon deposits we could scrub biogas to remove the tar before entering the fuel cell, use cleanable electrodes and/or replaceable electrodes; we could also configure the each of the anode and cathode each in layers, an outer shield (made of less expensive materials) to allow deposit of carbon on its surface, and thick back (inner) anode that could produce a stronger current to increase efficiency (perhaps made of a more conductive material).
We do the opposite with the cathode side of the fuel cell.
Additionally Biogas/Methane/CH4 are also steam reformed directly inside the Anode Channel by the heat produced by the reaction.
Excess heat can be used for:
1. Co-Generation.
2. Pyroelectric Crystals.
3. Thermo-Coupling.
4. Any and All Heat Waste to Energy Technologies.
To deal with the problem of carbon deposits we could scrub biogas to remove the tar before entering the fuel cell, use cleanable electrodes and/or replaceable electrodes; we could also configure the each of the anode and cathode each in layers, an outer shield (made of less expensive materials) to allow deposit of carbon on its surface, and thick back (inner) anode that could produce a stronger current to increase efficiency (perhaps made of a more conductive material).
Claims (4)
Note our bio fuels to energy Super Fuel Cell do not use any combustion processes and therefore do not produce any green house gases.
SUPER FUEL CELL Methane, Ethanol, Butane, Hydrogen...Any and all fuels.
Macro Upper Large Scale Fast and Mass Production per time. Probably Cheaper.
1. The nozzles that injects new unreacted fuel in the direction of the anode.
Heat produced from the reaction can be used for turbine co-generation.
2. The direction of the fuel down the channels.
3. The Anode Electrode.
4. The Cathode (where oxygen enters and reacts).
5. The Electrolyte.
Multiple Micro Scale Higher Yield per concentration of fuel left in the mixture ie. biogas is often contaminated with other gases present, therefore concentration per bulk/volume of the rest of the gases varies. By using multiple Micro Fuel Cells we 1. Maintain the same speed of throughput as the Macro part of the Super Fuel Cell Above so there is no backing up 2. Micro Fuel Cells are more efficient at reacting with the reactable fuels since the channel is thinner and therefore less fuel is exposed to more electrodes...meaning more of the reactable fuel molecules pass over the surface of the electrodes allowing for more fuel molecules access to the surface of the electrode(s) such that there is less dead space between the electrode and the outer walls of the channel...to capture the most fuel conversion, from the total mixture.
6. Cathode Outer Wall and Cathode Channel.
7. Cathode Electrode.
8. The Anode Electrode.
9. The Anode Outer Wall and Anode Channel. The bottom channel is narrowed to the optimal size for viable fuel cell stationary power plant capacity, then they feed into Multiple Micro fuel cells (possibly Proton Exchange Membrane - which are cheaper) the hot (high temperature) is run through waste heat to en energy (such as co-generation, pyroelectric crystals, thermo-coupling and any and all Heat to Energy Technologies) whereas the materials for MCFC and SOFC are expensive to replace and heavy. We might even use circular outer walls in the Multiple Micro technologies to redirect the secondary processed fuel and/or use smaller jets/sprays to get higher concentration of fuel into the depleted side facing the anode to replenish the side facing the electrode that has been depleted/spent from reacting with the anode.
We do the opposite with the cathode side of the fuel cell.
Additionally Biogas/Methane/CH4 are also steam reformed directly inside the Anode Channel by the heat produced by the reaction.
Excess heat can be used for:
1. Co-Generation.
2. Pyroelectric Crystals.
3. Thermo-Coupling.
4. Any and All Heat Waste to Energy Technologies.
To deal with the problem of carbon deposits we could scrub biogas to remove the tar before entering the fuel cell, use cleanable electrodes and/or replaceable electrodes; we could also configure the each of the anode and cathode each in layers, an outer shield (made of less expensive materials) to allow deposit of carbon on its surface, and thick back (inner) anode that could produce a stronger current to increase efficiency (perhaps made of a more conductive material).
To deal with the problem of carbon deposits we could scrub biogas to remove the tar before entering the fuel cell, use cleanable electrodes and/or replaceable electrodes; we could also configure the each of the anode and cathode each in layers, an outer shield (made of less expensive materials) to allow deposit of carbon on its surface, and thick back (inner) anode that could produce a stronger current to increase efficiency (perhaps made of a more conductive material).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA2694153A CA2694153A1 (en) | 2010-03-18 | 2010-03-18 | Steam reformation fuel cell with waste heat cogeneration turbine heat to energy pyroelectric crystals and/or thermo-coupling any and all waste heat to energy technologies and/or new macro-micros fuel cell power plant design |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA2694153A CA2694153A1 (en) | 2010-03-18 | 2010-03-18 | Steam reformation fuel cell with waste heat cogeneration turbine heat to energy pyroelectric crystals and/or thermo-coupling any and all waste heat to energy technologies and/or new macro-micros fuel cell power plant design |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2694153A1 true CA2694153A1 (en) | 2011-09-18 |
Family
ID=44671756
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2694153A Abandoned CA2694153A1 (en) | 2010-03-18 | 2010-03-18 | Steam reformation fuel cell with waste heat cogeneration turbine heat to energy pyroelectric crystals and/or thermo-coupling any and all waste heat to energy technologies and/or new macro-micros fuel cell power plant design |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA2694153A1 (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015055173A1 (en) * | 2013-10-17 | 2015-04-23 | Technische Universität Bergakademie Freiberg | Device and method for converting thermal energy into chemical energy and chemical energy into electrical energy with intermediate chemical storage |
| US9077006B2 (en) | 2013-03-15 | 2015-07-07 | Exxonmobil Research And Engineering Company | Integrated power generation and carbon capture using fuel cells |
| US9556753B2 (en) | 2013-09-30 | 2017-01-31 | Exxonmobil Research And Engineering Company | Power generation and CO2 capture with turbines in series |
| US9755258B2 (en) | 2013-09-30 | 2017-09-05 | Exxonmobil Research And Engineering Company | Integrated power generation and chemical production using solid oxide fuel cells |
| US9819042B2 (en) | 2013-09-30 | 2017-11-14 | Exxonmobil Research And Engineering Company | Fuel cell integration within a heat recovery steam generator |
| US11211621B2 (en) | 2018-11-30 | 2021-12-28 | Exxonmobil Research And Engineering Company | Regeneration of molten carbonate fuel cells for deep CO2 capture |
| US11335937B2 (en) | 2019-11-26 | 2022-05-17 | Exxonmobil Research And Engineering Company | Operation of molten carbonate fuel cells with high electrolyte fill level |
| US11424469B2 (en) | 2018-11-30 | 2022-08-23 | ExxonMobil Technology and Engineering Company | Elevated pressure operation of molten carbonate fuel cells with enhanced CO2 utilization |
| US11476486B2 (en) | 2018-11-30 | 2022-10-18 | ExxonMobil Technology and Engineering Company | Fuel cell staging for molten carbonate fuel cells |
| US11664519B2 (en) | 2019-11-26 | 2023-05-30 | Exxonmobil Research And Engineering Company | Fuel cell module assembly and systems using same |
| US11695122B2 (en) | 2018-11-30 | 2023-07-04 | ExxonMobil Technology and Engineering Company | Layered cathode for molten carbonate fuel cell |
| US11742508B2 (en) | 2018-11-30 | 2023-08-29 | ExxonMobil Technology and Engineering Company | Reforming catalyst pattern for fuel cell operated with enhanced CO2 utilization |
| US11888187B2 (en) | 2018-11-30 | 2024-01-30 | ExxonMobil Technology and Engineering Company | Operation of molten carbonate fuel cells with enhanced CO2 utilization |
| US11978931B2 (en) | 2021-02-11 | 2024-05-07 | ExxonMobil Technology and Engineering Company | Flow baffle for molten carbonate fuel cell |
-
2010
- 2010-03-18 CA CA2694153A patent/CA2694153A1/en not_active Abandoned
Cited By (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9077006B2 (en) | 2013-03-15 | 2015-07-07 | Exxonmobil Research And Engineering Company | Integrated power generation and carbon capture using fuel cells |
| US9178234B2 (en) | 2013-03-15 | 2015-11-03 | Exxonmobil Research And Engineering Company | Integrated power generation using molten carbonate fuel cells |
| US9419295B2 (en) | 2013-03-15 | 2016-08-16 | Exxonmobil Research And Engineering Company | Integrated power generation and chemical production using fuel cells at a reduced electrical efficiency |
| US9647284B2 (en) | 2013-03-15 | 2017-05-09 | Exxonmobil Research And Engineering Company | Integration of molten carbonate fuel cells in Fischer-Tropsch synthesis |
| US9650246B2 (en) | 2013-03-15 | 2017-05-16 | Exxonmobil Research And Engineering Company | Integration of molten carbonate fuel cells in fischer-tropsch synthesis |
| US9786939B2 (en) | 2013-03-15 | 2017-10-10 | Exxonmobil Research And Engineering Company | Integrated power generation and chemical production using fuel cells |
| US10676799B2 (en) | 2013-03-15 | 2020-06-09 | Exxonmobil Research And Engineering Company | Integrated electrical power and chemical production using fuel cells |
| US9556753B2 (en) | 2013-09-30 | 2017-01-31 | Exxonmobil Research And Engineering Company | Power generation and CO2 capture with turbines in series |
| US9755258B2 (en) | 2013-09-30 | 2017-09-05 | Exxonmobil Research And Engineering Company | Integrated power generation and chemical production using solid oxide fuel cells |
| US9819042B2 (en) | 2013-09-30 | 2017-11-14 | Exxonmobil Research And Engineering Company | Fuel cell integration within a heat recovery steam generator |
| US10283802B2 (en) | 2013-09-30 | 2019-05-07 | Exxonmobil Research And Engineering Company | Fuel cell integration within a heat recovery steam generator |
| WO2015055173A1 (en) * | 2013-10-17 | 2015-04-23 | Technische Universität Bergakademie Freiberg | Device and method for converting thermal energy into chemical energy and chemical energy into electrical energy with intermediate chemical storage |
| US11211621B2 (en) | 2018-11-30 | 2021-12-28 | Exxonmobil Research And Engineering Company | Regeneration of molten carbonate fuel cells for deep CO2 capture |
| US11424469B2 (en) | 2018-11-30 | 2022-08-23 | ExxonMobil Technology and Engineering Company | Elevated pressure operation of molten carbonate fuel cells with enhanced CO2 utilization |
| US11476486B2 (en) | 2018-11-30 | 2022-10-18 | ExxonMobil Technology and Engineering Company | Fuel cell staging for molten carbonate fuel cells |
| US11616248B2 (en) | 2018-11-30 | 2023-03-28 | ExxonMobil Technology and Engineering Company | Elevated pressure operation of molten carbonate fuel cells with enhanced CO2 utilization |
| US11695122B2 (en) | 2018-11-30 | 2023-07-04 | ExxonMobil Technology and Engineering Company | Layered cathode for molten carbonate fuel cell |
| US11742508B2 (en) | 2018-11-30 | 2023-08-29 | ExxonMobil Technology and Engineering Company | Reforming catalyst pattern for fuel cell operated with enhanced CO2 utilization |
| US11843150B2 (en) | 2018-11-30 | 2023-12-12 | ExxonMobil Technology and Engineering Company | Fuel cell staging for molten carbonate fuel cells |
| US11888187B2 (en) | 2018-11-30 | 2024-01-30 | ExxonMobil Technology and Engineering Company | Operation of molten carbonate fuel cells with enhanced CO2 utilization |
| US12095129B2 (en) | 2018-11-30 | 2024-09-17 | ExxonMobil Technology and Engineering Company | Reforming catalyst pattern for fuel cell operated with enhanced CO2 utilization |
| US11335937B2 (en) | 2019-11-26 | 2022-05-17 | Exxonmobil Research And Engineering Company | Operation of molten carbonate fuel cells with high electrolyte fill level |
| US11664519B2 (en) | 2019-11-26 | 2023-05-30 | Exxonmobil Research And Engineering Company | Fuel cell module assembly and systems using same |
| US11888199B2 (en) | 2019-11-26 | 2024-01-30 | ExxonMobil Technology and Engineering Company | Operation of molten carbonate fuel cells with high electrolyte fill level |
| US11978931B2 (en) | 2021-02-11 | 2024-05-07 | ExxonMobil Technology and Engineering Company | Flow baffle for molten carbonate fuel cell |
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