US20020100682A1 - Hydrogen recharging system for fuel cell hydride storage reservoir - Google Patents
Hydrogen recharging system for fuel cell hydride storage reservoir Download PDFInfo
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- US20020100682A1 US20020100682A1 US09/770,486 US77048601A US2002100682A1 US 20020100682 A1 US20020100682 A1 US 20020100682A1 US 77048601 A US77048601 A US 77048601A US 2002100682 A1 US2002100682 A1 US 2002100682A1
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- Prior art keywords
- hydrogen
- hydride storage
- fuel cell
- storage reservoir
- electrolyzer
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- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 74
- 238000003860 storage Methods 0.000 title claims abstract description 52
- 239000000446 fuel Substances 0.000 title claims abstract description 44
- 239000001257 hydrogen Substances 0.000 title claims abstract description 41
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 41
- 150000004678 hydrides Chemical class 0.000 title claims abstract description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 229910052987 metal hydride Inorganic materials 0.000 claims abstract description 18
- 150000004681 metal hydrides Chemical class 0.000 claims abstract description 16
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910001882 dioxygen Inorganic materials 0.000 claims abstract description 5
- 239000001301 oxygen Substances 0.000 claims description 9
- 229910052760 oxygen Inorganic materials 0.000 claims description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 8
- 150000002431 hydrogen Chemical class 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims 3
- 230000000717 retained effect Effects 0.000 claims 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000000463 material Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- -1 hydrogen ions Chemical class 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 239000000356 contaminant Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000002915 spent fuel radioactive waste Substances 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N O.O Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 239000002134 carbon nanofiber Substances 0.000 description 1
- 239000002041 carbon nanotube Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 229910001416 lithium ion Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/0005—Reversible uptake of hydrogen by an appropriate medium, i.e. based on physical or chemical sorption phenomena or on reversible chemical reactions, e.g. for hydrogen storage purposes ; Reversible gettering of hydrogen; Reversible uptake of hydrogen by electrodes
-
- 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
- H01M8/04201—Reactant storage and supply, e.g. means for feeding, pipes
- H01M8/04208—Cartridges, cryogenic media or cryogenic reservoirs
-
- 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
- H01M8/065—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dissolution of metals or alloys; by dehydriding metallic substances
-
- 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
- H01M8/0656—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants 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
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
-
- 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
-
- 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
- Y02E60/32—Hydrogen storage
-
- 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 in general to fuel cells, and more particularly to a system for rapidly charging hydrogen fuel to the fuel storage container.
- FIGURE is a schematic representation of a self-contained hydrogen recharging system for a fuel cell metal hydride storage canister in accordance with the invention.
- a self-contained hydrogen recharging system for a fuel cell metal hydride storage canister A water reservoir provides water to an electrolyzer, where the water is converted into hydrogen gas and oxygen gas. The hydrogen gas is stored in an accumulator, and is dried either prior to or after storing. When the metal hydride storage canister is ready to be refilled, it is connected by the user to the recharging system. A heat exchanger heats the fuel cell hydride storage canister prior to transfer of the stored hydrogen gas, and then cools the fuel cell hydride storage canister during transfer of the stored hydrogen gas. The hydrogen gas stored in the accumulator is rapidly transferred to the hydride storage canister and stowed in the canister as a metal hydride.
- a self-contained hydrogen recharging system 5 for a fuel cell metal hydride storage canister consists of several elements.
- a vessel, container or canister 10 holds a supply of water 15 that will subsequently be converted into hydrogen and oxygen.
- the container 10 can, of course, assume many forms, such as an open container, a can, a capsule, a tank, a reservoir, etc.
- a water supply line (not shown) connected to, for example, a municipal water source or other high purity water supply, can be substituted for the container 10 .
- the water supply line can be permanently connected or arranged to be removably coupled.
- the water 15 is hydrolyzed into hydrogen and oxygen in the electrolyzer 20 .
- Electrolysis also known as hydrolysis is a well known double decomposition reaction involving the splitting of water into its ions and the formation of a weak acid or base or both. This is brought about by passing a direct current through a platinum anode and a platinum cathode that are immersed in the water.
- the overall decomposition reaction is:
- hydrogen ions are produced, that combine into H 2 molecules, and are collected above the surface of the water as hydrogen gas 22 .
- oxygen ions are likewise produced and combine into O 2 molecules 24 , and are similarly collected above the surface of the water.
- the oxygen can either be collected or vented to the atmosphere.
- pressurized oxygen as a source of oxidant (rather than ambient air) one would collect and store the oxygen in a manner similar to that used for the hydrogen. In most cases, however, the oxygen will simply be vented to the atmosphere.
- the hydrogen gas 22 is dried by passing through a dryer 26 where any residual water vapor is removed. It is important to have a dry source of hydrogen for stable fuel cell operation.
- the gas can be dried either prior to storage in the accumulator, or during the charging of the metal hydride canister, and can be dried through any number of schemes, but we suggest that a commercial desiccant such as silica gel or 3 Angstrom molecular sieves be used, as they are easily obtainable and easily replaceable or regenerated when exhausted.
- the hydrogen gas 22 (either dried or not dried) is stored in an accumulator 30 .
- the accumulator 30 is intended to be a storage system, and as such can assume numerous configurations, such as, for example, an expandable bladder, a pressurized vessel, or a container with a piston that can store the hydrogen at or slightly above atmospheric pressure.
- the pressure generated at the electrolyzer 20 by the production of hydrogen gas 22 can be used to ‘pump’ the hydrogen gas into the accumulator 30 and store it at pressure.
- this pressure is limited, and if one wishes to store additional quantities of hydrogen gas, it needs to be compressed and stored at elevated pressures.
- the compressor (not shown) compresses the hydrogen so that it can be stored in a rigid pressurized container. Storage of pressurized hydrogen requires requisite safety considerations, and it is assumed that the skilled reader will adhere to the well-known safety precautions in the handling of pressurized hydrogen.
- the hydride storage container 100 in the user's fuel cell becomes empty and needs to be replenished, one connects it to the self-contained hydrogen recharging system 5 and the hydrogen gas 22 held in the accumulator 30 is rapidly transferred via a valve 62 to the hydride storage container 100 .
- the hydride storage container 100 is part of the user's fuel cell system, and can be integral to the fuel cell or it can be a removable component, such as a vessel with a quick disconnect.
- the hydride storage container 100 is typically filled with a material that stores the hydrogen fuel as a metal hydride, rather than as hydrogen gas.
- the hydrogen gas when the hydrogen gas is charged into the user's hydride storage container 100 , it undergoes a chemical reaction that converts the material to a metal hydride.
- a chemical reaction that converts the material to a metal hydride.
- nickel-metal hydride as the media for storing electrochemical energy, and this material is very similar to that used in the hydride storage container 100 .
- a heat exchanger 55 is provided to remove the heat of reaction. Cooling the hydride storage container 100 during charging allows for rapid recharging.
- the charging time using our invention compares rather favorably to the long charging time associated with present day batteries if examined from a recharge rate standpoint.
- a 7-volt radio battery with 1500 milliamp-hour capacity takes approximately two hours to recharge, at a recharge rate of 5.25 watt-hours per hour.
- a state of the art 7 volt fuel cell system of comparable physical size to the above battery has approximately 10 times the energy capacity, providing 15,000 milliamp-hour capacity, but can be recharged using our invention in only ten (10) minutes, thereby recharging at a rate of 630 watt-hours per hour.
- the heat exchanger 55 can also include a heating system. Over time and use, the material in the hydride storage container 100 may collect contaminants and lose some hydride storage capacity, typically ranging from 10-15% loss. The material can be purified and ‘refreshed’ using the present invention in the following way.
- the heat exchanger 55 is operated in a ‘heating’ mode, and heats the hydride canister 100 prior to charging, allowing the release of residual hydrogen and other contaminants, while an optional vacuum pump 60 evacuates the contaminant gases through purge valve 62 . Then, the hydride canister 100 is cooled and recharged as described previously above.
- a charge meter 40 monitors and measures the amount of hydrogen gas that is transferred to the spent fuel cell canister 100 .
- the charge meter is a flow meter.
- the entire system as described above is optionally contained in a housing 70 , similar to present day desktop battery chargers, typically less than or equal to one cubic foot in volume.
- the safety conscious consumer can have a small, simple, effective method for rapidly recharging spent fuel cell canisters.
- Our invention provides recharging times for fuel cells up to 100 times faster than present day electrochemical battery charging methods. Since water and electricity are the only raw materials needed to replenish the system, our invention can be used virtually anywhere with minimal cost.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Fuel Cell (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
A self-contained hydrogen recharging system (5) for a fuel cell metal hydride storage canister (100). A water reservoir (10) provides water (15) to an electrolyzer (20), where the water is converted into hydrogen gas (22) and oxygen gas (24). The hydrogen gas is dried (26) and then stored in an accumulator (30). When the metal hydride storage canister is ready to be refilled, it is connected by the user to the recharging system. A heat exchanger (55) heats the fuel cell hydride storage canister prior to transfer of the stored hydrogen gas, and then cools the fuel cell hydride storage canister during transfer of the stored hydrogen gas. The hydrogen gas stored in the accumulator is rapidly transferred to the hydride storage canister by means of a pump (60) and stowed in the canister as a metal hydride.
Description
- This invention relates in general to fuel cells, and more particularly to a system for rapidly charging hydrogen fuel to the fuel storage container.
- In recent years, nearly all electronic devices have been reduced in size and made lightweight, in particular portable electronic devices. This advancement has been made possible, in part, by the development of new battery chemistries such as nickel-metal hydride, lithium ion, zinc-air, and lithium polymer that enable larger amounts of power to be packaged in a smaller container. However, since these are secondary or rechargeable batteries, they need to be recharged upon depletion of their electrical capacity. This is typically performed by connecting the battery to a battery charger that converts alternating current (typically 110 volts AC) to a low level direct current (typically 2-12 volts DC). The charging cycle typically lasts a minimum of 1-2 hours, and more commonly 4-14 hours. Although the new batteries are a tremendous advancement over the previous generations of batteries, they still suffer from the need for sophisticated charging regimens and the slow charging rates.
- Some have sought to replace electrolytic batteries with small fuel cells. Simply put, fuel cells catalytically convert a hydrogen molecule to hydrogen ions and electrons, and then extract the electrons through a membrane as electrical power, while oxidizing the hydrogen ions to H 2O and extracting the byproduct water. The tremendous advantage of fuel cells is the potential ability to provide significantly larger amounts of power in a small package (as compared to a battery). However, the problem of how to replenish the supply of hydrogen fuel to the spent fuel cell still seeks an elegant and practical solution before widespread consumer acceptance occurs. Some have sought to use methanol as the source of hydrogen, by catalytically converting or ‘reforming’ the methanol using exotic schemes. At the current state of the art, fuel cells directly powered by methanol are still a laboratory curiosity, and significant technical obstacles remain to be overcome. Even with seven decades behind us since the Hindenberg disaster, consumers remain wary of hydrogen gas, and thus there is no infrastructure to provide hydrogen to refill exhausted fuel cells. Thus, even though the energy conversion portion of the fuel cell has been refined to the point where it is commercially viable for small devices, the problem of how to safely provide hydrogen to consumers in small quantities remains to be commercially implemented.
- The sole drawing FIGURE is a schematic representation of a self-contained hydrogen recharging system for a fuel cell metal hydride storage canister in accordance with the invention.
- A self-contained hydrogen recharging system for a fuel cell metal hydride storage canister. A water reservoir provides water to an electrolyzer, where the water is converted into hydrogen gas and oxygen gas. The hydrogen gas is stored in an accumulator, and is dried either prior to or after storing. When the metal hydride storage canister is ready to be refilled, it is connected by the user to the recharging system. A heat exchanger heats the fuel cell hydride storage canister prior to transfer of the stored hydrogen gas, and then cools the fuel cell hydride storage canister during transfer of the stored hydrogen gas. The hydrogen gas stored in the accumulator is rapidly transferred to the hydride storage canister and stowed in the canister as a metal hydride. While the specification concludes with claims defining the features of the invention that are regarded as novel, it is believed that the construction, method of operation and advantages of the invention will be better understood from a consideration of the following description in conjunction with the drawing FIGURE.
- Referring now to the single drawing FIGURE, a self-contained hydrogen recharging system 5 for a fuel cell metal hydride storage canister consists of several elements. A vessel, container or
canister 10 holds a supply ofwater 15 that will subsequently be converted into hydrogen and oxygen. Thecontainer 10 can, of course, assume many forms, such as an open container, a can, a capsule, a tank, a reservoir, etc. Additionally, a water supply line (not shown) connected to, for example, a municipal water source or other high purity water supply, can be substituted for thecontainer 10. The water supply line can be permanently connected or arranged to be removably coupled. Thewater 15 is hydrolyzed into hydrogen and oxygen in theelectrolyzer 20. Electrolysis (also known as hydrolysis) is a well known double decomposition reaction involving the splitting of water into its ions and the formation of a weak acid or base or both. This is brought about by passing a direct current through a platinum anode and a platinum cathode that are immersed in the water. The overall decomposition reaction is: - At the cathode, hydrogen ions are produced, that combine into H 2 molecules, and are collected above the surface of the water as
hydrogen gas 22. At the anode, oxygen ions are likewise produced and combine into O2 molecules 24, and are similarly collected above the surface of the water. The oxygen can either be collected or vented to the atmosphere. In fuel cell systems that utilize pressurized oxygen as a source of oxidant (rather than ambient air) one would collect and store the oxygen in a manner similar to that used for the hydrogen. In most cases, however, the oxygen will simply be vented to the atmosphere. Thehydrogen gas 22 is dried by passing through adryer 26 where any residual water vapor is removed. It is important to have a dry source of hydrogen for stable fuel cell operation. The gas can be dried either prior to storage in the accumulator, or during the charging of the metal hydride canister, and can be dried through any number of schemes, but we suggest that a commercial desiccant such as silica gel or 3 Angstrom molecular sieves be used, as they are easily obtainable and easily replaceable or regenerated when exhausted. The hydrogen gas 22 (either dried or not dried) is stored in anaccumulator 30. Theaccumulator 30 is intended to be a storage system, and as such can assume numerous configurations, such as, for example, an expandable bladder, a pressurized vessel, or a container with a piston that can store the hydrogen at or slightly above atmospheric pressure. The pressure generated at theelectrolyzer 20 by the production ofhydrogen gas 22 can be used to ‘pump’ the hydrogen gas into theaccumulator 30 and store it at pressure. Of course, this pressure is limited, and if one wishes to store additional quantities of hydrogen gas, it needs to be compressed and stored at elevated pressures. This can be accomplished by incorporating a mechanical compressor into theaccumulator 30. The compressor (not shown) compresses the hydrogen so that it can be stored in a rigid pressurized container. Storage of pressurized hydrogen requires requisite safety considerations, and it is assumed that the skilled reader will adhere to the well-known safety precautions in the handling of pressurized hydrogen. - When the
hydride storage container 100 in the user's fuel cell becomes empty and needs to be replenished, one connects it to the self-contained hydrogen recharging system 5 and thehydrogen gas 22 held in theaccumulator 30 is rapidly transferred via avalve 62 to thehydride storage container 100. For purposes of clarity, it should be noted that thehydride storage container 100 is part of the user's fuel cell system, and can be integral to the fuel cell or it can be a removable component, such as a vessel with a quick disconnect. Thehydride storage container 100 is typically filled with a material that stores the hydrogen fuel as a metal hydride, rather than as hydrogen gas. Thus, when the hydrogen gas is charged into the user'shydride storage container 100, it undergoes a chemical reaction that converts the material to a metal hydride. Those skilled in the art will appreciate that large quantities of hydrogen can be safely stored in the metal hydride form. For example, many modern electrochemical rechargeable batteries use nickel-metal hydride as the media for storing electrochemical energy, and this material is very similar to that used in thehydride storage container 100. Since the hydrogen-metal hydride reaction is exothermic (produces heat), aheat exchanger 55 is provided to remove the heat of reaction. Cooling thehydride storage container 100 during charging allows for rapid recharging. The charging time using our invention compares rather favorably to the long charging time associated with present day batteries if examined from a recharge rate standpoint. As an example, a 7-volt radio battery with 1500 milliamp-hour capacity takes approximately two hours to recharge, at a recharge rate of 5.25 watt-hours per hour. A state of the art 7 volt fuel cell system of comparable physical size to the above battery has approximately 10 times the energy capacity, providing 15,000 milliamp-hour capacity, but can be recharged using our invention in only ten (10) minutes, thereby recharging at a rate of 630 watt-hours per hour. - The
heat exchanger 55 can also include a heating system. Over time and use, the material in thehydride storage container 100 may collect contaminants and lose some hydride storage capacity, typically ranging from 10-15% loss. The material can be purified and ‘refreshed’ using the present invention in the following way. Theheat exchanger 55 is operated in a ‘heating’ mode, and heats thehydride canister 100 prior to charging, allowing the release of residual hydrogen and other contaminants, while anoptional vacuum pump 60 evacuates the contaminant gases throughpurge valve 62. Then, thehydride canister 100 is cooled and recharged as described previously above. - In an alternative embodiment, a
charge meter 40 monitors and measures the amount of hydrogen gas that is transferred to the spentfuel cell canister 100. In its simplest form, the charge meter is a flow meter. In order to provide a package that is commercially viable, the entire system as described above is optionally contained in ahousing 70, similar to present day desktop battery chargers, typically less than or equal to one cubic foot in volume. Thus, the safety conscious consumer can have a small, simple, effective method for rapidly recharging spent fuel cell canisters. Our invention provides recharging times for fuel cells up to 100 times faster than present day electrochemical battery charging methods. Since water and electricity are the only raw materials needed to replenish the system, our invention can be used virtually anywhere with minimal cost. - While the preferred embodiments of the invention have been illustrated and described, it will be clear that the invention is not so limited. Numerous modifications, changes, variations, substitutions and equivalents will occur to those skilled in the art without departing from the spirit and scope of the present invention as defined by the appended claims. For example, the instant invention as shown and described can also be used with other hydrogen based fuel cell storage systems, such as carbon nanofiber or nanotube storage systems, and additionally, pressurized hydrogen storage vessels.
Claims (14)
1. A hydrogen recharging system for fuel cell hydride storage reservoirs, comprising:
an electrolyzer to hydrolyze liquid water to hydrogen gas and oxygen gas, said electrolyzer connected to a water supply;
a hydrogen gas accumulator;
a dryer situated between and connected to the electrolyzer and the accumulator; and
wherein hydrogen gas produced by the electrolyzer is dried in the dryer and then stored in the accumulator such that when a user connects the fuel cell hydride storage reservoir to the hydrogen recharging system, the stored hydrogen gas is rapidly transferred from the accumulator to the hydride storage reservoir, to be retained in the hydride storage reservoir in the form of a metal hydride.
2. The system as described in claim 1 , further comprising a heat exchanger to cool the connected fuel cell hydride storage reservoir during transfer of the stored hydrogen.
3. The system as described in claim 1 , further comprising a heat exchanger to heat the connected fuel cell hydride storage reservoir prior to transfer of the stored hydrogen, and wherein a pump is used to evacuate the fuel cell hydride storage reservoir during heating.
4. The system as described in claim 1 , wherein a pump is used to evacuate the fuel cell hydride storage reservoir.
5. The system as described in claim 4 , further comprising a heat exchanger to heat the connected fuel cell hydride storage reservoir during evacuation of the reservoir, and then to cool the connected fuel cell hydride storage reservoir during transfer of the stored hydrogen.
6. The system as described in claim 1 , further comprising a vent on the electrolyzer to vent oxygen produced by the electrolyzer to the surrounding environment.
7. The system as described in claim 1 , wherein the accumulator further comprises a compressor.
8. The system as described in claim 1 , further comprising a charge meter for measuring the amount of hydrogen transferred to the fuel cell hydride storage reservoir.
9. The system as described in claim 1 , wherein the system is contained in a desktop housing less than or equal to one cubic foot in volume.
10. A self-contained hydrogen recharging system for a fuel cell metal hydride storage reservoir, comprising:
a water supply connected to an electrolyzer for converting liquid water to hydrogen and oxygen gas;
hydrogen storage means comprising an accumulator and a compressor;
a dryer situated after the electrolyzer; and
wherein hydrogen gas produced by the electrolyzer is stored in the hydrogen storage means;
a heat exchanger to heat the fuel cell hydride storage reservoir prior to transfer of the stored hydrogen gas, and then to cool the fuel cell hydride storage reservoir during transfer of the stored hydrogen gas; and
wherein upon connection of the fuel cell hydride storage reservoir to the hydrogen recharging system by a user, the stored hydrogen gas is rapidly transferred to the hydride storage reservoir and stowed in the reservoir as a metal hydride.
11. The system as described in claim 7 , further comprising a vent on the electrolyzer to vent oxygen produced by the electrolyzer to the surrounding environment.
12. The system as described in claim 7 , further comprising a charge meter for measuring the amount of hydrogen transferred to the fuel cell hydride storage reservoir.
13. The system as described in claim 7 , further comprising a vacuum pump.
14. A hydrogen recharging system for fuel cell hydride storage reservoirs, comprising:
an electrolyzer to hydrolyze liquid water to hydrogen gas and oxygen gas, said electrolyzer connected to a water supply;
a hydrogen gas accumulator; and
wherein hydrogen gas produced by the electrolyzer is stored in the accumulator such that when a user connects the fuel cell hydride storage reservoir to the hydrogen recharging system, the stored hydrogen gas is rapidly transferred from the accumulator to the hydride storage reservoir, to be retained in the hydride storage reservoir in the form of a metal hydride.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/770,486 US20020100682A1 (en) | 2001-01-29 | 2001-01-29 | Hydrogen recharging system for fuel cell hydride storage reservoir |
| CNA02804293XA CN1489798A (en) | 2001-01-29 | 2002-01-16 | Hydrogen charging system for fuel cell hydride storage container |
| PCT/US2002/001388 WO2002084771A1 (en) | 2001-01-29 | 2002-01-16 | Hydrogen recharging system for fuel cell hydride storage reservoir |
| ZA2003/05589A ZA200305589B (en) | 2001-01-29 | 2003-07-18 | Hydrogen recharging system for fuel cell hydride storage reservoir |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/770,486 US20020100682A1 (en) | 2001-01-29 | 2001-01-29 | Hydrogen recharging system for fuel cell hydride storage reservoir |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20020100682A1 true US20020100682A1 (en) | 2002-08-01 |
Family
ID=25088709
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US09/770,486 Abandoned US20020100682A1 (en) | 2001-01-29 | 2001-01-29 | Hydrogen recharging system for fuel cell hydride storage reservoir |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US20020100682A1 (en) |
| CN (1) | CN1489798A (en) |
| WO (1) | WO2002084771A1 (en) |
| ZA (1) | ZA200305589B (en) |
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| US20060051638A1 (en) * | 2004-09-03 | 2006-03-09 | Gross Karl J | Hydrogen storage and integrated fuel cell assembly |
| US20060117831A1 (en) * | 2004-11-30 | 2006-06-08 | Honeywell International, Inc. | Nano-crystalline and/or metastable metal hydrides as hydrogen source for sensor calibration and self-testing |
| US20070084879A1 (en) * | 2005-09-30 | 2007-04-19 | Mclean Gerard F | Hydrogen supplies and related methods |
| WO2007008891A3 (en) * | 2005-07-12 | 2007-04-26 | Honeywell Int Inc | Fuel cell recharger |
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| WO2005023709A3 (en) * | 2003-03-19 | 2007-08-16 | Lund And Company Inv L L C | Power driven equipment utilizing hydrogen from the electrolysis of water |
| US20070227899A1 (en) * | 2006-03-29 | 2007-10-04 | Mcclaine Andrew W | Storing and transporting energy |
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| FR2913417A1 (en) * | 2007-03-06 | 2008-09-12 | Ceram Hyd Soc Par Actions Simp | HYDROGEN STORAGE PROCESS AND UNIT |
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| CN104791603A (en) * | 2014-01-20 | 2015-07-22 | 上海华捷视医疗设备有限公司 | Hydrogen energy storage and supply system, and hydrogen energy storage and supply method |
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| US20040018095A1 (en) * | 2002-07-25 | 2004-01-29 | Smekal Thomas J. | Fluidic pump |
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| US20080014477A1 (en) * | 2003-11-18 | 2008-01-17 | Nie Luo | Hydrogen/hydrogen peroxide fuel cell |
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| US20050229977A1 (en) * | 2004-04-16 | 2005-10-20 | Yang Li | Flow regulating valve assembly |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN1489798A (en) | 2004-04-14 |
| ZA200305589B (en) | 2005-02-23 |
| WO2002084771A1 (en) | 2002-10-24 |
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| AS | Assignment |
Owner name: MOTOROLA, INC., ILLINOIS Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:KELLEY, RONALD J.;PRATT, STEVEN D.;PENNISI, ROBERT W.;REEL/FRAME:011500/0592 Effective date: 20010124 |
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Owner name: MOTOROLA, INC., ILLINOIS Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:MUTHUSWAMY, SIVAKUMAR;REEL/FRAME:011696/0963 Effective date: 20010323 |
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