US20100025232A1 - Recovering the compression energy in gaseous hydrogen and oxygen generated from high-pressure water electrolysis - Google Patents
Recovering the compression energy in gaseous hydrogen and oxygen generated from high-pressure water electrolysis Download PDFInfo
- Publication number
- US20100025232A1 US20100025232A1 US12/181,513 US18151308A US2010025232A1 US 20100025232 A1 US20100025232 A1 US 20100025232A1 US 18151308 A US18151308 A US 18151308A US 2010025232 A1 US2010025232 A1 US 2010025232A1
- Authority
- US
- United States
- Prior art keywords
- hydrogen gas
- pressure
- gas
- fuel cell
- expansion engine
- Prior art date
- Legal status (The legal status 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 status listed.)
- Abandoned
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/05—Pressure cells
-
- 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
-
- 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
- H01M2250/20—Fuel cells in motive systems, e.g. vehicle, ship, plane
-
- 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
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02T90/40—Application of hydrogen technology to transportation, e.g. using fuel cells
Definitions
- the field to which the disclosure relates generally to energy recovery systems and, in particular, to the recovery of compressive energy generated during a high-pressure water electrolysis process.
- Electrolyzers convert abundant, low-energy content chemicals into more valuable ones by using electricity to break down compounds into elements or simpler products.
- a water electrolyzer is a system of cells in which each cell contains two electrodes. In each cell water is oxidized at one electrode (called the cell anode), to produce oxygen gas, and reduced at the other electrode (called the cell cathode), to produce hydrogen gas.
- the oxidation-reduction reactions are driven by a direct current (DC) power source.
- Oxygen and hydrogen are generated in a stoichiometric ratio—two volume units of hydrogen for every one of oxygen—at a rate proportional to the applied cell current.
- Water electrolysis appears to be ideally suited to making and storing hydrogen needed to power fuel cells, including specifically fuel cell powered electric vehicles.
- hydrogen gas can be produced at sufficiently high-pressures (up to about 10,000 pounds per square inch, psi) for storage without the need for mechanical compression.
- Such systems require significant energy input to drive the high-pressure electrolysis process.
- oxygen that is generated in this process generally goes unutilized, and is typically vented to the atmosphere.
- One exemplary embodiment includes a method and apparatus for recovering the compression energy stored in hydrogen gas and oxygen gas generated by the electrolysis of water in a high-pressure water electrolyzer.
- the potential energy in compressed oxygen gas generated as a by-product of electrolytic hydrogen production via water electrolysis in a high-pressure electrolyzer may be used to drive a pneumatic engine.
- the pneumatic engine can then drive an electrical generator to produce electricity, and the electricity generated may be used to partially power the electrolyzer that originally made the oxygen gas and hydrogen.
- the potential energy in compressed hydrogen gas may be recovered as expansion energy that in turn may drive an electrical generator. This electrical energy may then be used to partially power the high-pressure electrolyzer that originally made the oxygen and hydrogen gas.
- the potential energy from both the compressed hydrogen gas and oxygen gas generated within the high-pressure water electrolyzer may be recovered as expansion energy that in turn may drive one or more electrical generators. This electrical energy may then be used to partially power the high-pressure water electrolyzer that originally made the oxygen and hydrogen gas.
- the expansion of hydrogen gas may also be used aboard a fuel cell electric vehicle.
- the compressed hydrogen gas may be recovered as expansion energy that in turn may drive a mechanical electrical generator. This electrical energy may be used to partially power the fuel cell.
- the expansion energy of hydrogen gas may be used directly as mechanical energy from a pneumatic engine to help propel the fuel cell electric vehicle.
- the expansion energy of hydrogen gas may both be used in a hybrid fuel cell/pneumatic vehicle as both mechanical energy from a pneumatic engine to help propel the vehicle and further may be used to drive a mechanical electrical generator and may be used to power a fuel cell electric vehicle.
- FIG. 1 is a schematic flow chart of a system used to generate high-pressure hydrogen and oxygen gases using a high-pressure water electrolyzer and using the hydrogen in a fuel cell electric vehicle or stationary fuel cell with recovery of both the chemical energy of the hydrogen and the compression energy stored in the high-pressure gases in accordance with an exemplary embodiment.
- a system 10 that may generate high-pressure hydrogen gas and oxygen gas via high-pressure water electrolysis is provided in one exemplary embodiment.
- a portion the hydrogen gas generated may be used by a fuel cell electric vehicle 11 (or stationary fuel cell) is also illustrated within the exemplary embodiment.
- the system 10 may include a high-pressure water electrolyzer 12 that may be used to generate high-pressure hydrogen gas and oxygen gas from water.
- the electrolyzer 12 may be powered by electricity from a solar system grid 14 or other conventional electrical powering devices (not shown).
- a high-pressure electrolyzer is a water-based electrolyzer that is capable of producing hydrogen gas and oxygen gas at pressures up to about 10,000 pounds per square inch.
- a conventional high-pressure electrolyzer 12 that may be utilized in the exemplary embodiment is the Avalance high-pressure electrolyzer (available from Avalance LLC of Milford, Conn.), which uses a unipolar alkaline (KOH) electrolyte system with cylindrical steel electrolysis cells and includes structure for balancing the hydrogen gas and oxygen gas levels and electrolyte levels to keep the gases and electrolytes separate, as well as preventing the mixing of the hydrogen gas and oxygen gas.
- KOH unipolar alkaline
- Water may be introduced to the electrolyzer 12 from a holding tank 16 ; through the use of a high-pressure pump (not shown).
- the water may undergo a oxygen evolution reaction (oxidation reaction) at the electrolyzer anode (not shown) and may undergo a hydrogen evolution reaction (reduction reaction) at the electrolyzer cathode (not shown) according to the general formula:
- the high-pressure hydrogen gas 18 and oxygen gas 20 produced within the electrolyzer 12 may be separately removed under pressure to a hydrogen gas storage tank 22 and oxygen gas storage tank 24 , respectively.
- the pressure of hydrogen gas 18 that is removed may approach about 10,000 pounds per square inch.
- the high-pressure oxygen gas 20 may then be introduced from the storage tank 24 into an oxygen gas expansion engine 26 (pneumatic engine).
- the expanding oxygen gas within the oxygen expansion engine 26 may then drive an electrical generator 28 to produce electricity, and the electricity generated may be used to partially power the electrolyzer 12 .
- the expanded gas from the pneumatic engine 26 may then vented to the atmosphere 30 .
- the storage of high-pressure electrolytically-produced oxygen, along with recovery of the compression energy using a oxygen gas expansion engine 26 as mechanical energy, followed by conversion of the mechanical energy into electrical energy, may increase the efficiency of a solar electrolysis process by utilizing much of the energy stored in the high-pressure oxygen. It is estimated that an energy savings of up to about three percent of the lower heating value (LHV) energy of the hydrogen gas produced by electrolysis in the electrolyzer 12 may be recovered as electrical energy by using the compression energy in the stored oxygen in the exemplary embodiment described herein (10,000 psi of stored O 2 ).
- LHV lower heating value
- the hydrogen gas 18 generated in the electrolyzer 12 may be introduced from the hydrogen gas storage tank 22 to a hydrogen gas expansion engine 32 (pneumatic engine).
- the expansion of hydrogen gas within the hydrogen expansion engine 32 may then drive an electrical generator 36 to produce electricity, and the electricity generated may be used to power the electrolyzer 12 .
- the expanded hydrogen gas may then be transferred to a fuel cell electric vehicle holding tank 40 .
- the storage of high-pressure electrolytically-produced hydrogen, along with recovery of the compression energy using a hydrogen gas expansion engine 32 as mechanical energy, followed by conversion of the mechanical energy into electrical energy, may increase the efficiency of a solar electrolysis process by utilizing much of the energy stored in the high-pressure hydrogen. It is estimated that an energy savings of up to about six percent of the lower heating value (LHV) energy of the hydrogen gas produced by electrolysis in the electrolyzer 12 may be recovered as electrical energy by using the compression energy in the stored hydrogen in the exemplary embodiment described herein (10,000 psi of stored H 2 ).
- LHV lower heating value
- a fuel cell electric vehicle holding tank 40 for a fuel cell electric vehicle 11 may also be filled with expanding hydrogen gas from the hydrogen gas storage tank 22 through the gas expansion engine 32 until such time as there is an equilibrium state in hydrogen gas pressure between the hydrogen gas storage tank 22 and the holding tank 40 .
- This equilibrium state may preferably be tied to a predetermined hydrogen gas pressure within the holding tank 40 , corresponding to a predetermined quantity of hydrogen gas. In this equilibrium state, there is little conversion of compression energy to mechanical energy occurring in the hydrogen gas expansion engine 32 .
- the subsequent release of hydrogen gas from the holding tank 40 to the fuel cell 54 as described below allows additional hydrogen gas to be filled from the hydrogen gas storage tank 22 through the engine 32 to maintain the equilibrium state.
- the hydrogen gas pressure in the holding tank 40 may be maintained at about 10,000 psi.
- the holding tank 40 may hold the compressed hydrogen gas on a vehicle 11 until such time as it is needed in the fuel cell 54 to generate electric power to propel the vehicle 11 and/or provide power to a particular vehicle component.
- the compressed hydrogen gas contained in the holding tank 40 may be expanded within the second hydrogen expansion engine 50 and released to the fuel cell 54 .
- the hydrogen gas entering the fuel cell 54 is reacted with oxygen (which may enter the fuel cell 54 from a storage tank 58 or from an ambient setting), in a stoichiometric ratio, to produce water and electricity, the latter of which may be used to power an electric traction motor 62 .
- the electric traction motor 62 may convert the electrical energy to mechanical energy to propel the vehicle 11 again as shown in box 60 . Additional electrical energy for the electric traction motor 62 may be provided by the pneumatically-powered electrical generator 56 .
- the expanding hydrogen gas entering the second hydrogen expansion engine 50 from the holding tank 40 may also be used to drive an electrical generator 56 and/or may also be fed, in the form of mechanical energy, to the wheels of the fuel-cell electric vehicle to propel the vehicle 11 , as shown in box 60 .
- the exemplary embodiment illustrated herein provides a method and apparatus for increasing the efficiency of the high-pressure hydrogen generation and utilization process by recovering and utilizing the compression energy stored in high-pressure hydrogen gas and oxygen gas in ways to reduce energy costs associated with their production and end use.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- General Chemical & Material Sciences (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Fuel Cell (AREA)
Abstract
Description
- The field to which the disclosure relates generally to energy recovery systems and, in particular, to the recovery of compressive energy generated during a high-pressure water electrolysis process.
- Electrolyzers convert abundant, low-energy content chemicals into more valuable ones by using electricity to break down compounds into elements or simpler products. A water electrolyzer is a system of cells in which each cell contains two electrodes. In each cell water is oxidized at one electrode (called the cell anode), to produce oxygen gas, and reduced at the other electrode (called the cell cathode), to produce hydrogen gas. The oxidation-reduction reactions are driven by a direct current (DC) power source. Oxygen and hydrogen are generated in a stoichiometric ratio—two volume units of hydrogen for every one of oxygen—at a rate proportional to the applied cell current.
- Water electrolysis appears to be ideally suited to making and storing hydrogen needed to power fuel cells, including specifically fuel cell powered electric vehicles. In a high-pressure water electrolyzer, hydrogen gas can be produced at sufficiently high-pressures (up to about 10,000 pounds per square inch, psi) for storage without the need for mechanical compression. Such systems, however, require significant energy input to drive the high-pressure electrolysis process. In addition, oxygen that is generated in this process generally goes unutilized, and is typically vented to the atmosphere.
- One exemplary embodiment includes a method and apparatus for recovering the compression energy stored in hydrogen gas and oxygen gas generated by the electrolysis of water in a high-pressure water electrolyzer.
- In one exemplary embodiment, the potential energy in compressed oxygen gas generated as a by-product of electrolytic hydrogen production via water electrolysis in a high-pressure electrolyzer may be used to drive a pneumatic engine. The pneumatic engine can then drive an electrical generator to produce electricity, and the electricity generated may be used to partially power the electrolyzer that originally made the oxygen gas and hydrogen.
- In another exemplary embodiment, the potential energy in compressed hydrogen gas may be recovered as expansion energy that in turn may drive an electrical generator. This electrical energy may then be used to partially power the high-pressure electrolyzer that originally made the oxygen and hydrogen gas.
- In a related exemplary embodiment, the potential energy from both the compressed hydrogen gas and oxygen gas generated within the high-pressure water electrolyzer may be recovered as expansion energy that in turn may drive one or more electrical generators. This electrical energy may then be used to partially power the high-pressure water electrolyzer that originally made the oxygen and hydrogen gas.
- In yet another exemplary embodiment, the expansion of hydrogen gas may also be used aboard a fuel cell electric vehicle. In this embodiment, the compressed hydrogen gas may be recovered as expansion energy that in turn may drive a mechanical electrical generator. This electrical energy may be used to partially power the fuel cell.
- In still another exemplary embodiment, the expansion energy of hydrogen gas may be used directly as mechanical energy from a pneumatic engine to help propel the fuel cell electric vehicle.
- In a further exemplary embodiment, the expansion energy of hydrogen gas may both be used in a hybrid fuel cell/pneumatic vehicle as both mechanical energy from a pneumatic engine to help propel the vehicle and further may be used to drive a mechanical electrical generator and may be used to power a fuel cell electric vehicle.
- Other exemplary embodiments of the invention will become apparent from the detailed description provided hereinafter. It should be understood that the detailed description and specific examples, while disclosing exemplary embodiments of the invention, are intended for purposes of illustration only and are not intended to limit the scope of the invention.
- Exemplary embodiments of the invention will become more fully understood from the detailed description and the accompanying drawings, wherein:
-
FIG. 1 is a schematic flow chart of a system used to generate high-pressure hydrogen and oxygen gases using a high-pressure water electrolyzer and using the hydrogen in a fuel cell electric vehicle or stationary fuel cell with recovery of both the chemical energy of the hydrogen and the compression energy stored in the high-pressure gases in accordance with an exemplary embodiment. - The following description of the embodiment(s) is merely exemplary (illustrative) in nature and is in no way intended to limit the invention, its application, or uses.
- Referring now to
FIG. 1 , asystem 10 that may generate high-pressure hydrogen gas and oxygen gas via high-pressure water electrolysis is provided in one exemplary embodiment. A portion the hydrogen gas generated may be used by a fuel cell electric vehicle 11 (or stationary fuel cell) is also illustrated within the exemplary embodiment. - The
system 10 may include a high-pressure water electrolyzer 12 that may be used to generate high-pressure hydrogen gas and oxygen gas from water. Theelectrolyzer 12 may be powered by electricity from asolar system grid 14 or other conventional electrical powering devices (not shown). - By definition, a high-pressure electrolyzer is a water-based electrolyzer that is capable of producing hydrogen gas and oxygen gas at pressures up to about 10,000 pounds per square inch. One example of a conventional high-
pressure electrolyzer 12 that may be utilized in the exemplary embodiment is the Avalance high-pressure electrolyzer (available from Avalance LLC of Milford, Conn.), which uses a unipolar alkaline (KOH) electrolyte system with cylindrical steel electrolysis cells and includes structure for balancing the hydrogen gas and oxygen gas levels and electrolyte levels to keep the gases and electrolytes separate, as well as preventing the mixing of the hydrogen gas and oxygen gas. - Water may be introduced to the
electrolyzer 12 from aholding tank 16; through the use of a high-pressure pump (not shown). The water may undergo a oxygen evolution reaction (oxidation reaction) at the electrolyzer anode (not shown) and may undergo a hydrogen evolution reaction (reduction reaction) at the electrolyzer cathode (not shown) according to the general formula: -
H2O→H2+½O2 - The high-
pressure hydrogen gas 18 andoxygen gas 20 produced within theelectrolyzer 12 may be separately removed under pressure to a hydrogengas storage tank 22 and oxygengas storage tank 24, respectively. In one exemplary embodiment, the pressure ofhydrogen gas 18 that is removed may approach about 10,000 pounds per square inch. - The high-
pressure oxygen gas 20 may then be introduced from thestorage tank 24 into an oxygen gas expansion engine 26 (pneumatic engine). The expanding oxygen gas within theoxygen expansion engine 26 may then drive anelectrical generator 28 to produce electricity, and the electricity generated may be used to partially power theelectrolyzer 12. The expanded gas from thepneumatic engine 26 may then vented to theatmosphere 30. - The storage of high-pressure electrolytically-produced oxygen, along with recovery of the compression energy using a oxygen
gas expansion engine 26 as mechanical energy, followed by conversion of the mechanical energy into electrical energy, may increase the efficiency of a solar electrolysis process by utilizing much of the energy stored in the high-pressure oxygen. It is estimated that an energy savings of up to about three percent of the lower heating value (LHV) energy of the hydrogen gas produced by electrolysis in theelectrolyzer 12 may be recovered as electrical energy by using the compression energy in the stored oxygen in the exemplary embodiment described herein (10,000 psi of stored O2). - The
hydrogen gas 18 generated in theelectrolyzer 12 may be introduced from the hydrogengas storage tank 22 to a hydrogen gas expansion engine 32 (pneumatic engine). The expansion of hydrogen gas within thehydrogen expansion engine 32 may then drive anelectrical generator 36 to produce electricity, and the electricity generated may be used to power theelectrolyzer 12. The expanded hydrogen gas may then be transferred to a fuel cell electricvehicle holding tank 40. - The storage of high-pressure electrolytically-produced hydrogen, along with recovery of the compression energy using a hydrogen
gas expansion engine 32 as mechanical energy, followed by conversion of the mechanical energy into electrical energy, may increase the efficiency of a solar electrolysis process by utilizing much of the energy stored in the high-pressure hydrogen. It is estimated that an energy savings of up to about six percent of the lower heating value (LHV) energy of the hydrogen gas produced by electrolysis in theelectrolyzer 12 may be recovered as electrical energy by using the compression energy in the stored hydrogen in the exemplary embodiment described herein (10,000 psi of stored H2). - A fuel cell electric
vehicle holding tank 40 for a fuel cellelectric vehicle 11 may also be filled with expanding hydrogen gas from the hydrogengas storage tank 22 through thegas expansion engine 32 until such time as there is an equilibrium state in hydrogen gas pressure between the hydrogengas storage tank 22 and theholding tank 40. This equilibrium state may preferably be tied to a predetermined hydrogen gas pressure within theholding tank 40, corresponding to a predetermined quantity of hydrogen gas. In this equilibrium state, there is little conversion of compression energy to mechanical energy occurring in the hydrogengas expansion engine 32. The subsequent release of hydrogen gas from theholding tank 40 to thefuel cell 54 as described below allows additional hydrogen gas to be filled from the hydrogengas storage tank 22 through theengine 32 to maintain the equilibrium state. In the exemplary embodiment shown herein, the hydrogen gas pressure in theholding tank 40 may be maintained at about 10,000 psi. - The
holding tank 40 may hold the compressed hydrogen gas on avehicle 11 until such time as it is needed in thefuel cell 54 to generate electric power to propel thevehicle 11 and/or provide power to a particular vehicle component. When needed, the compressed hydrogen gas contained in theholding tank 40 may be expanded within the secondhydrogen expansion engine 50 and released to thefuel cell 54. - In fuel-cell conversion, the hydrogen gas entering the
fuel cell 54 is reacted with oxygen (which may enter thefuel cell 54 from astorage tank 58 or from an ambient setting), in a stoichiometric ratio, to produce water and electricity, the latter of which may be used to power anelectric traction motor 62. Theelectric traction motor 62 may convert the electrical energy to mechanical energy to propel thevehicle 11 again as shown inbox 60. Additional electrical energy for theelectric traction motor 62 may be provided by the pneumatically-poweredelectrical generator 56. - The expanding hydrogen gas entering the second
hydrogen expansion engine 50 from theholding tank 40 may also be used to drive anelectrical generator 56 and/or may also be fed, in the form of mechanical energy, to the wheels of the fuel-cell electric vehicle to propel thevehicle 11, as shown inbox 60. - Thus, the exemplary embodiment illustrated herein provides a method and apparatus for increasing the efficiency of the high-pressure hydrogen generation and utilization process by recovering and utilizing the compression energy stored in high-pressure hydrogen gas and oxygen gas in ways to reduce energy costs associated with their production and end use.
- The above description of embodiments of the invention is merely exemplary in nature and, thus, variations thereof are not to be regarded as a departure from the spirit and scope of the invention.
Claims (34)
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/181,513 US20100025232A1 (en) | 2008-07-29 | 2008-07-29 | Recovering the compression energy in gaseous hydrogen and oxygen generated from high-pressure water electrolysis |
| DE102009034572A DE102009034572A1 (en) | 2008-07-29 | 2009-07-24 | Recovery of the compression energy in gaseous hydrogen and oxygen from the production by means of high-pressure water electrolysis |
| CN200910164682A CN101638792A (en) | 2008-07-29 | 2009-07-29 | Recovering the compression energy in gaseous hydrogen and oxygen generated from high-pressure water electrolysis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/181,513 US20100025232A1 (en) | 2008-07-29 | 2008-07-29 | Recovering the compression energy in gaseous hydrogen and oxygen generated from high-pressure water electrolysis |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20100025232A1 true US20100025232A1 (en) | 2010-02-04 |
Family
ID=41528351
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/181,513 Abandoned US20100025232A1 (en) | 2008-07-29 | 2008-07-29 | Recovering the compression energy in gaseous hydrogen and oxygen generated from high-pressure water electrolysis |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US20100025232A1 (en) |
| CN (1) | CN101638792A (en) |
| DE (1) | DE102009034572A1 (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140377167A1 (en) * | 2012-01-18 | 2014-12-25 | H-Tec Systems Gmbh | Method for starting up an electrolyzer |
| WO2016001155A1 (en) * | 2014-07-01 | 2016-01-07 | Siemens Aktiengesellschaft | Method for operating an electrolytic system and electrolytic system |
| GB2556077A (en) * | 2016-11-17 | 2018-05-23 | Linde Ag | Oxygen generation system and method of generating oxygen gas |
| WO2018136508A1 (en) * | 2017-01-17 | 2018-07-26 | Ivys Inc. | Hydrogen gas dispensing systems and methods |
| WO2020011748A1 (en) * | 2018-07-12 | 2020-01-16 | Haldor Topsøe A/S | Expander for soec applications |
| CN114875424A (en) * | 2022-04-24 | 2022-08-09 | 宁波大学 | Large-scale underground compressed hydrogen energy storage system |
| CN115234308A (en) * | 2022-08-22 | 2022-10-25 | 清华四川能源互联网研究院 | Pressure energy recovery and utilization system for hydrogen production by electrolysis of water |
| US20230128698A1 (en) * | 2020-03-19 | 2023-04-27 | Airbus Operations Gmbh | Energy recovery assembly, fuel cell system and vehicle with energy recovery assembly |
| EP4424873A1 (en) * | 2023-02-28 | 2024-09-04 | Siemens Energy Global GmbH & Co. KG | Energy recovery system and related method of recovering energy |
Families Citing this family (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2961756B1 (en) * | 2010-06-29 | 2014-03-07 | Michelin Soc Tech | SYSTEM FOR PRODUCING AND SUPPLYING HYDROGEN AND SODIUM CHLORATE HAVING SODIUM CHLORIDE ELECTROLYSER FOR PRODUCING SODIUM CHLORATE |
| CN102174703A (en) * | 2010-12-20 | 2011-09-07 | 苏州竞立制氢设备有限公司 | Water electrolysis hydrogen preparation gas-liquid separation and oxygen purification all-in-one machine |
| CN102965686A (en) * | 2011-08-31 | 2013-03-13 | 本田技研工业株式会社 | Water electrolysis system and method for operating the same |
| CN104228596A (en) * | 2014-10-10 | 2014-12-24 | 郭金武 | Solar hydrogen energy automobile |
| DE202015106668U1 (en) | 2014-12-08 | 2016-01-29 | Michael Bergmann | Autonomous and self-sufficient plant for hydrogen production and storage |
| CN104819074B (en) * | 2015-04-30 | 2018-06-22 | 吉林省中涵科技有限公司 | fuel supply device based on water electrolysis |
| CN104819075B (en) * | 2015-04-30 | 2018-04-27 | 吉林省中涵科技有限公司 | fuel supply device based on water electrolysis |
| DE102015007732A1 (en) * | 2015-06-16 | 2016-12-22 | Linde Aktiengesellschaft | Oxygen expander (electrolysis) for cooling the production and compression process |
| DE102015013072A1 (en) * | 2015-10-08 | 2017-04-27 | Linde Aktiengesellschaft | Reuse of the fuel cell process water for the electrolysis process |
| CN105576803A (en) * | 2016-02-17 | 2016-05-11 | 陆玉正 | Distributed new energy charging pile and hydrogen refueling station |
| JP6801599B2 (en) * | 2017-07-26 | 2020-12-16 | トヨタ自動車株式会社 | Fuel cell system and control device |
| CN107634245A (en) * | 2017-09-22 | 2018-01-26 | 北京理工大学 | A kind of hydrogen cell automobile pressure energy drives hydrogen gas circulating pump device |
| CN110566806B (en) * | 2019-09-30 | 2024-04-12 | 长江勘测规划设计研究有限责任公司 | Compression energy recycling system of hydrogen production energy storage system |
| CN110792479B (en) * | 2019-11-07 | 2020-07-28 | 安徽伯华氢能源科技有限公司 | Hydrogen power generation system |
| EP3882375B8 (en) | 2020-03-17 | 2023-07-26 | Hymeth ApS | Method of compressing carbon dioxide using high-pressure electrolysis |
| CN112567979A (en) * | 2020-12-31 | 2021-03-30 | 盐城万洋农副产品有限公司 | Power device for applying solar hydrogen new energy to gardening mower |
| CN115602882A (en) * | 2022-09-16 | 2023-01-13 | 北京市煤气热力工程设计院有限公司(Cn) | System and method for integrated production-storage-use hydrogen energy storage based on electricity-hydrogen-gas conversion |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6182717B1 (en) * | 1998-10-22 | 2001-02-06 | Honda Giken Kogyo Kabushiki Kaisha | Process for filling hydrogen into a hydrogen storage tank in automobile |
| US6610193B2 (en) * | 2000-08-18 | 2003-08-26 | Have Blue, Llc | System and method for the production and use of hydrogen on board a marine vessel |
| US20080119975A1 (en) * | 2006-11-16 | 2008-05-22 | Ford Global Technologies, Llc | Hybrid Electric Vehicle Powertrain with Engine Start and Transmission Shift Arbitration |
| US20080257751A1 (en) * | 2006-04-25 | 2008-10-23 | Smola Matthew M | Enhanced device for generating hydrogen for use in internal combustion engines |
-
2008
- 2008-07-29 US US12/181,513 patent/US20100025232A1/en not_active Abandoned
-
2009
- 2009-07-24 DE DE102009034572A patent/DE102009034572A1/en not_active Withdrawn
- 2009-07-29 CN CN200910164682A patent/CN101638792A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6182717B1 (en) * | 1998-10-22 | 2001-02-06 | Honda Giken Kogyo Kabushiki Kaisha | Process for filling hydrogen into a hydrogen storage tank in automobile |
| US6610193B2 (en) * | 2000-08-18 | 2003-08-26 | Have Blue, Llc | System and method for the production and use of hydrogen on board a marine vessel |
| US20080257751A1 (en) * | 2006-04-25 | 2008-10-23 | Smola Matthew M | Enhanced device for generating hydrogen for use in internal combustion engines |
| US20080119975A1 (en) * | 2006-11-16 | 2008-05-22 | Ford Global Technologies, Llc | Hybrid Electric Vehicle Powertrain with Engine Start and Transmission Shift Arbitration |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9790092B2 (en) * | 2012-01-18 | 2017-10-17 | H-Tec Systems Gmbh | Method for starting up an electrolyzer |
| US20140377167A1 (en) * | 2012-01-18 | 2014-12-25 | H-Tec Systems Gmbh | Method for starting up an electrolyzer |
| US10351962B2 (en) | 2014-07-01 | 2019-07-16 | Siemens Aktiengesellschaft | Method for operating an electrolytic system and electrolytic system |
| WO2016001155A1 (en) * | 2014-07-01 | 2016-01-07 | Siemens Aktiengesellschaft | Method for operating an electrolytic system and electrolytic system |
| GB2556077A (en) * | 2016-11-17 | 2018-05-23 | Linde Ag | Oxygen generation system and method of generating oxygen gas |
| US10236522B2 (en) | 2017-01-17 | 2019-03-19 | Ivys Inc. | Hydrogen gas dispensing systems and methods |
| WO2018136508A1 (en) * | 2017-01-17 | 2018-07-26 | Ivys Inc. | Hydrogen gas dispensing systems and methods |
| US11196062B2 (en) | 2017-01-17 | 2021-12-07 | Ivys Inc. | Hydrogen gas dispensing systems and methods |
| US12021280B2 (en) | 2017-01-17 | 2024-06-25 | Ivys Inc. | Hydrogen gas dispensing systems and methods |
| WO2020011748A1 (en) * | 2018-07-12 | 2020-01-16 | Haldor Topsøe A/S | Expander for soec applications |
| US20230128698A1 (en) * | 2020-03-19 | 2023-04-27 | Airbus Operations Gmbh | Energy recovery assembly, fuel cell system and vehicle with energy recovery assembly |
| CN114875424A (en) * | 2022-04-24 | 2022-08-09 | 宁波大学 | Large-scale underground compressed hydrogen energy storage system |
| CN115234308A (en) * | 2022-08-22 | 2022-10-25 | 清华四川能源互联网研究院 | Pressure energy recovery and utilization system for hydrogen production by electrolysis of water |
| EP4424873A1 (en) * | 2023-02-28 | 2024-09-04 | Siemens Energy Global GmbH & Co. KG | Energy recovery system and related method of recovering energy |
| WO2024179725A1 (en) * | 2023-02-28 | 2024-09-06 | Siemens Energy Global GmbH & Co. KG | Energy recovery system and related method of recovering energy |
Also Published As
| Publication number | Publication date |
|---|---|
| DE102009034572A1 (en) | 2010-02-18 |
| CN101638792A (en) | 2010-02-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US20100025232A1 (en) | Recovering the compression energy in gaseous hydrogen and oxygen generated from high-pressure water electrolysis | |
| US8840764B2 (en) | Electrolysis apparatus for the production of electricity and hydrogen | |
| US3829368A (en) | Oxygen-hydrogen generation and sewage treatment method and system | |
| CN108604695B (en) | Energy storage with engine REP | |
| CN106945560B (en) | Energy recovery structure of exhaust system of fuel cell vehicle | |
| KR20110114816A (en) | CO2 capture device and method using fuel cell power generation system | |
| US10840572B1 (en) | Solar hydrogen generation and off-peak storage | |
| JP6815415B2 (en) | Regenerative fuel cell system and water electrolysis system | |
| WO2012073383A1 (en) | Natural energy storage system | |
| AU2020222393A1 (en) | Hydrogen based renewable energy storage system | |
| CN101220481A (en) | Preparation method of solar water-based high-pressure high-purity hydrogen-oxygen fuel for space vehicles | |
| KR20220004507A (en) | Methanol fuel energy conversion system | |
| KR102257467B1 (en) | Platform and method for producing ammonia | |
| KR102358856B1 (en) | Rechargeable electrochemical device for producing electrical energy | |
| TWI463731B (en) | Fuel cell power generation system with oxygen inlet instead of air | |
| JP2009224293A (en) | Fuel cell system | |
| AU2023366065B2 (en) | A process and apparatus for sustainable water fuelled vehicle | |
| JP2000054173A (en) | Water electrolytic storage battery | |
| US20240332579A1 (en) | Fuel cell as an electrolyzer in fuel cell electric vehicles for onboard hydrogen production | |
| KR102925018B1 (en) | Hybrid water electrolysis system | |
| EP4557412A1 (en) | Method for generating electric power or producing hydrogen, and energy conversion system | |
| GB2634787A (en) | Electrolysis of water | |
| Lejda | Fuel Cells as Source of Ecological Energy for Automotive Vehicles | |
| JP5497265B2 (en) | Discharge system for fuel cell inspection | |
| CN117265561A (en) | Proton exchange membrane electrolytic water system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: GM GLOBAL TECHNOLOGY OPERATIONS, INC.,MICHIGAN Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:KELLY, NELSON A.;GIBSON, THOMAS L.;OUWERKERK, DAVID B.;SIGNING DATES FROM 20080718 TO 20080724;REEL/FRAME:021306/0818 |
|
| AS | Assignment |
Owner name: UNITED STATES DEPARTMENT OF THE TREASURY,DISTRICT Free format text: SECURITY AGREEMENT;ASSIGNOR:GM GLOBAL TECHNOLOGY OPERATIONS, INC.;REEL/FRAME:022201/0448 Effective date: 20081231 Owner name: UNITED STATES DEPARTMENT OF THE TREASURY, DISTRICT Free format text: SECURITY AGREEMENT;ASSIGNOR:GM GLOBAL TECHNOLOGY OPERATIONS, INC.;REEL/FRAME:022201/0448 Effective date: 20081231 |
|
| AS | Assignment |
Owner name: CITICORP USA, INC. AS AGENT FOR BANK PRIORITY SECU Free format text: SECURITY AGREEMENT;ASSIGNOR:GM GLOBAL TECHNOLOGY OPERATIONS, INC.;REEL/FRAME:022554/0538 Effective date: 20090409 Owner name: CITICORP USA, INC. AS AGENT FOR HEDGE PRIORITY SEC Free format text: SECURITY AGREEMENT;ASSIGNOR:GM GLOBAL TECHNOLOGY OPERATIONS, INC.;REEL/FRAME:022554/0538 Effective date: 20090409 |
|
| AS | Assignment |
Owner name: GM GLOBAL TECHNOLOGY OPERATIONS, INC.,MICHIGAN Free format text: RELEASE BY SECURED PARTY;ASSIGNOR:UNITED STATES DEPARTMENT OF THE TREASURY;REEL/FRAME:023126/0914 Effective date: 20090709 Owner name: GM GLOBAL TECHNOLOGY OPERATIONS, INC.,MICHIGAN Free format text: RELEASE BY SECURED PARTY;ASSIGNORS:CITICORP USA, INC. AS AGENT FOR BANK PRIORITY SECURED PARTIES;CITICORP USA, INC. AS AGENT FOR HEDGE PRIORITY SECURED PARTIES;REEL/FRAME:023155/0769 Effective date: 20090814 Owner name: GM GLOBAL TECHNOLOGY OPERATIONS, INC., MICHIGAN Free format text: RELEASE BY SECURED PARTY;ASSIGNOR:UNITED STATES DEPARTMENT OF THE TREASURY;REEL/FRAME:023126/0914 Effective date: 20090709 Owner name: GM GLOBAL TECHNOLOGY OPERATIONS, INC., MICHIGAN Free format text: RELEASE BY SECURED PARTY;ASSIGNORS:CITICORP USA, INC. AS AGENT FOR BANK PRIORITY SECURED PARTIES;CITICORP USA, INC. AS AGENT FOR HEDGE PRIORITY SECURED PARTIES;REEL/FRAME:023155/0769 Effective date: 20090814 |
|
| AS | Assignment |
Owner name: UNITED STATES DEPARTMENT OF THE TREASURY,DISTRICT Free format text: SECURITY AGREEMENT;ASSIGNOR:GM GLOBAL TECHNOLOGY OPERATIONS, INC.;REEL/FRAME:023156/0313 Effective date: 20090710 Owner name: UNITED STATES DEPARTMENT OF THE TREASURY, DISTRICT Free format text: SECURITY AGREEMENT;ASSIGNOR:GM GLOBAL TECHNOLOGY OPERATIONS, INC.;REEL/FRAME:023156/0313 Effective date: 20090710 |
|
| AS | Assignment |
Owner name: UAW RETIREE MEDICAL BENEFITS TRUST,MICHIGAN Free format text: SECURITY AGREEMENT;ASSIGNOR:GM GLOBAL TECHNOLOGY OPERATIONS, INC.;REEL/FRAME:023162/0237 Effective date: 20090710 Owner name: UAW RETIREE MEDICAL BENEFITS TRUST, MICHIGAN Free format text: SECURITY AGREEMENT;ASSIGNOR:GM GLOBAL TECHNOLOGY OPERATIONS, INC.;REEL/FRAME:023162/0237 Effective date: 20090710 |
|
| AS | Assignment |
Owner name: GM GLOBAL TECHNOLOGY OPERATIONS, INC., MICHIGAN Free format text: RELEASE BY SECURED PARTY;ASSIGNOR:UNITED STATES DEPARTMENT OF THE TREASURY;REEL/FRAME:025245/0909 Effective date: 20100420 |
|
| AS | Assignment |
Owner name: GM GLOBAL TECHNOLOGY OPERATIONS, INC., MICHIGAN Free format text: RELEASE BY SECURED PARTY;ASSIGNOR:UAW RETIREE MEDICAL BENEFITS TRUST;REEL/FRAME:025315/0046 Effective date: 20101026 |
|
| AS | Assignment |
Owner name: WILMINGTON TRUST COMPANY, DELAWARE Free format text: SECURITY AGREEMENT;ASSIGNOR:GM GLOBAL TECHNOLOGY OPERATIONS, INC.;REEL/FRAME:025324/0475 Effective date: 20101027 |
|
| AS | Assignment |
Owner name: GM GLOBAL TECHNOLOGY OPERATIONS LLC, MICHIGAN Free format text: CHANGE OF NAME;ASSIGNOR:GM GLOBAL TECHNOLOGY OPERATIONS, INC.;REEL/FRAME:025781/0211 Effective date: 20101202 |
|
| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |