US20020100682A1 - Hydrogen recharging system for fuel cell hydride storage reservoir - Google Patents

Hydrogen recharging system for fuel cell hydride storage reservoir Download PDF

Info

Publication number
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
Authority
US
United States
Prior art keywords
hydrogen
hydride storage
fuel cell
storage reservoir
electrolyzer
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
Application number
US09/770,486
Inventor
Ronald Kelley
Steven Pratt
Sivakumar Muthuswamy
Robert Pennisi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Motorola Solutions Inc
Original Assignee
Motorola Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Motorola Inc filed Critical Motorola Inc
Priority to US09/770,486 priority Critical patent/US20020100682A1/en
Assigned to MOTOROLA, INC. reassignment MOTOROLA, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: KELLEY, RONALD J., PENNISI, ROBERT W., PRATT, STEVEN D.
Assigned to MOTOROLA, INC. reassignment MOTOROLA, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MUTHUSWAMY, SIVAKUMAR
Priority to PCT/US2002/001388 priority patent/WO2002084771A1/en
Priority to CNA02804293XA priority patent/CN1489798A/en
Publication of US20020100682A1 publication Critical patent/US20020100682A1/en
Priority to ZA2003/05589A priority patent/ZA200305589B/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/0005Reversible 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
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04201Reactant storage and supply, e.g. means for feeding, pipes
    • H01M8/04208Cartridges, cryogenic media or cryogenic reservoirs
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/065Combination 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
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0656Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by electrochemical means
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel 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.

Landscapes

  • 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

    TECHNICAL FIELD
  • This invention relates in general to fuel cells, and more particularly to a system for rapidly charging hydrogen fuel to the fuel storage container. [0001]
  • BACKGROUND
  • 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. [0002]
  • 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[0003] 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.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • 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.[0004]
  • DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
  • 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. [0005]
  • Referring now to the single drawing FIGURE, a self-contained hydrogen recharging system [0006] 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. 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 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:
    Figure US20020100682A1-20020801-C00001
  • At the cathode, hydrogen ions are produced, that combine into H[0007] 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. 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. 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 the accumulator 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 [0008] 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. For purposes of clarity, it should be noted that 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. Thus, 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. 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 the hydride storage container 100. Since the hydrogen-metal hydride reaction is exothermic (produces heat), 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. 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 [0009] 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.
  • In an alternative embodiment, a [0010] charge meter 40 monitors and measures the amount of hydrogen gas that is transferred to the spent fuel 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 a housing 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. [0011]

Claims (14)

What is claimed is:
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.
US09/770,486 2001-01-29 2001-01-29 Hydrogen recharging system for fuel cell hydride storage reservoir Abandoned US20020100682A1 (en)

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
PCT/US2002/001388 WO2002084771A1 (en) 2001-01-29 2002-01-16 Hydrogen recharging system for fuel cell hydride storage reservoir
CNA02804293XA CN1489798A (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)

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040018095A1 (en) * 2002-07-25 2004-01-29 Smekal Thomas J. Fluidic pump
US20040253494A1 (en) * 2001-09-13 2004-12-16 Ryuichiro Maruyama Hydrogen gas manufacturing and filling equipment and electrochemical equipment
WO2005023709A2 (en) * 2003-03-19 2005-03-17 Lund And Company Invention, L.L.C. Power driven equipment utilizing hydrogen from the electrolysis of water
US20050229977A1 (en) * 2004-04-16 2005-10-20 Yang Li Flow regulating valve assembly
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
WO2007008891A2 (en) * 2005-07-12 2007-01-18 Honeywell International Inc. Fuel cell recharger
US20070084879A1 (en) * 2005-09-30 2007-04-19 Mclean Gerard F Hydrogen supplies and related methods
US7241521B2 (en) 2003-11-18 2007-07-10 Npl Associates, Inc. Hydrogen/hydrogen peroxide fuel cell
US20070160887A1 (en) * 2006-01-10 2007-07-12 Honeywell International Inc. Power generator having multiple layers of fuel cells
US20070178340A1 (en) * 2006-01-31 2007-08-02 Honeywell International Inc. Fuel cell power generator with micro turbine
US20070184312A1 (en) * 2005-07-12 2007-08-09 Honeywell International Inc. Power generator shut-off valve
US20070227899A1 (en) * 2006-03-29 2007-10-04 Mcclaine Andrew W Storing and transporting energy
US20070287059A1 (en) * 2006-06-12 2007-12-13 Honeywell International Inc. Fuel cell recharger
US20080127411A1 (en) * 2006-09-08 2008-06-05 Airbus Deutschland Gmbh Self-sustaining washroom for mobile use
FR2913417A1 (en) * 2007-03-06 2008-09-12 Ceram Hyd Soc Par Actions Simp HYDROGEN STORAGE PROCESS AND UNIT
US20090297899A1 (en) * 2008-05-27 2009-12-03 Samsung Electro-Mechanics Co., Ltd. Housing, apparatus for generating hydrogen and fuel cell power generation system having the same
US20100196199A1 (en) * 2007-03-01 2010-08-05 Andritz Separation Inc. System and method for treatment of pathogens in dried sewage sludge
US20100280138A1 (en) * 2007-05-28 2010-11-04 Arash Mofakhami Method of activating boron nitride
FR2968462A1 (en) * 2010-12-06 2012-06-08 Michelin Soc Tech DEVICE FOR GENERATING ELECTRICITY BY FUEL CELL.
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
US9105907B2 (en) 2008-03-06 2015-08-11 Ceram Hyd Material for an electrochemical device
US9233847B2 (en) 2006-03-29 2016-01-12 Safe Hydrogen, Llc Methods and systems for making metal hydride slurries

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100460746C (en) * 2004-08-10 2009-02-11 孔德凯 Hollow isothermal electric heating storage cylinder for solid hydrogen and hydrogen charging device
CN101162782B (en) * 2006-10-09 2010-08-25 比亚迪股份有限公司 Fuel battery hydrogen storing device and hydrogen storing and charging system
KR100957373B1 (en) * 2007-12-13 2010-05-11 현대자동차주식회사 Reservor tank of coolant for fuel cell vehicle
CA3017431C (en) * 2011-02-28 2022-04-05 Nicolas Kernene Energy unit with safe and stable hydrogen storage
CN102800877B (en) * 2011-05-27 2014-09-17 中国地质大学(武汉) Parallel direct fuel cell energy storage and supply system based on liquid hydrogen storage material
EP3428317A1 (en) * 2017-07-12 2019-01-16 Airbus Defence and Space System for producing and dispensing pressurized hydrogen

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4108605A (en) * 1976-05-04 1978-08-22 Billings Energy Corporation Hydrogen purification and storage system
US4211537A (en) * 1978-07-24 1980-07-08 Teitel Robert J Hydrogen supply method
US4302217A (en) * 1978-07-24 1981-11-24 Teitel Robert J Hydrogen supply system
US4376373A (en) * 1981-02-18 1983-03-15 Roy Weber Energy recovery system
US5813222A (en) * 1994-10-07 1998-09-29 Appleby; Anthony John Method and apparatus for heating a catalytic converter to reduce emissions

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5346778A (en) * 1992-08-13 1994-09-13 Energy Partners, Inc. Electrochemical load management system for transportation applications
US5510202A (en) * 1994-02-24 1996-04-23 Rockwell International Corporation Quasi-passive variable pressure regenerative fuel cell system
US5512145A (en) * 1994-10-07 1996-04-30 The Cooper Union For The Advancement Of Science And Art Energy conversion system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4108605A (en) * 1976-05-04 1978-08-22 Billings Energy Corporation Hydrogen purification and storage system
US4211537A (en) * 1978-07-24 1980-07-08 Teitel Robert J Hydrogen supply method
US4302217A (en) * 1978-07-24 1981-11-24 Teitel Robert J Hydrogen supply system
US4376373A (en) * 1981-02-18 1983-03-15 Roy Weber Energy recovery system
US5813222A (en) * 1994-10-07 1998-09-29 Appleby; Anthony John Method and apparatus for heating a catalytic converter to reduce emissions

Cited By (53)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040253494A1 (en) * 2001-09-13 2004-12-16 Ryuichiro Maruyama Hydrogen gas manufacturing and filling equipment and electrochemical equipment
US6793462B2 (en) * 2002-07-25 2004-09-21 Motorola, Inc. Fluidic pump
US20040018095A1 (en) * 2002-07-25 2004-01-29 Smekal Thomas J. Fluidic pump
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
WO2005023709A2 (en) * 2003-03-19 2005-03-17 Lund And Company Invention, L.L.C. Power driven equipment utilizing hydrogen from the electrolysis of water
US7781083B2 (en) 2003-11-18 2010-08-24 Npl Associates, Inc. Hydrogen/hydrogen peroxide fuel cell
US20080014477A1 (en) * 2003-11-18 2008-01-17 Nie Luo Hydrogen/hydrogen peroxide fuel cell
US7241521B2 (en) 2003-11-18 2007-07-10 Npl Associates, Inc. Hydrogen/hydrogen peroxide fuel cell
US20050229977A1 (en) * 2004-04-16 2005-10-20 Yang Li Flow regulating valve assembly
US7781109B2 (en) 2004-09-03 2010-08-24 Gross Karl J Hydrogen storage and integrated fuel cell assembly
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
US7152458B2 (en) 2004-11-30 2006-12-26 Honeywell International Inc. Nano-crystalline and/or metastable metal hydrides as hydrogen source for sensor calibration and self-testing
WO2007008891A3 (en) * 2005-07-12 2007-04-26 Honeywell Int Inc Fuel cell recharger
US20070184312A1 (en) * 2005-07-12 2007-08-09 Honeywell International Inc. Power generator shut-off valve
US8404395B2 (en) 2005-07-12 2013-03-26 Honeywell International Inc. Ring of fuel cells with a hydrogen generator
WO2007008891A2 (en) * 2005-07-12 2007-01-18 Honeywell International Inc. Fuel cell recharger
US20070084879A1 (en) * 2005-09-30 2007-04-19 Mclean Gerard F Hydrogen supplies and related methods
US8522835B2 (en) 2005-09-30 2013-09-03 SOCIéTé BIC Hydrogen supplies and related methods
US8215342B2 (en) 2005-09-30 2012-07-10 Societé BIC Hydrogen supplies and related methods
US20070160887A1 (en) * 2006-01-10 2007-07-12 Honeywell International Inc. Power generator having multiple layers of fuel cells
US8043736B2 (en) 2006-01-10 2011-10-25 Honeywell International Inc. Power generator having multiple layers of fuel cells
US20070178340A1 (en) * 2006-01-31 2007-08-02 Honeywell International Inc. Fuel cell power generator with micro turbine
US9580308B2 (en) 2006-03-29 2017-02-28 Safe Hydrogen, Llc Storing and transporting energy
US9233847B2 (en) 2006-03-29 2016-01-12 Safe Hydrogen, Llc Methods and systems for making metal hydride slurries
WO2007117858A3 (en) * 2006-03-29 2008-12-31 Safe Hydrogen Llc Storing and transporting energy
US8715583B2 (en) 2006-03-29 2014-05-06 Safe Hydrogen, Llc Storing and transporting energy
US10077190B2 (en) 2006-03-29 2018-09-18 Safe Hydrogen, Llc Methods and systems for making metal hydride slurries
US10549990B2 (en) 2006-03-29 2020-02-04 Safe Hydrogen, Llc Storing and transporting energy
US7790013B2 (en) * 2006-03-29 2010-09-07 Safe Hydrogen, Llc Storing and transporting energy
US20100252423A1 (en) * 2006-03-29 2010-10-07 Safe Hydrogen, Llc Storing and Transporting Energy
US10570012B2 (en) 2006-03-29 2020-02-25 Safe Hydrogen, Llc Methods and systems for making metal hydride slurries
US11192784B2 (en) 2006-03-29 2021-12-07 Safe Hydrogen, Llc Methods and systems for making metal hydride slurries
AU2007235120B2 (en) * 2006-03-29 2011-08-04 Safe Hydrogen, Llc Storing and transporting energy
US20070227899A1 (en) * 2006-03-29 2007-10-04 Mcclaine Andrew W Storing and transporting energy
AU2007235120C1 (en) * 2006-03-29 2012-01-19 Safe Hydrogen, Llc Storing and transporting energy
US7727647B2 (en) 2006-06-12 2010-06-01 Honeywell International Inc. Portable hydrogen fuel container charger
US20070287059A1 (en) * 2006-06-12 2007-12-13 Honeywell International Inc. Fuel cell recharger
US8141185B2 (en) * 2006-09-08 2012-03-27 Airbus Operations Gmbh Self-sustaining washroom for mobile use
US20080127411A1 (en) * 2006-09-08 2008-06-05 Airbus Deutschland Gmbh Self-sustaining washroom for mobile use
US20100196199A1 (en) * 2007-03-01 2010-08-05 Andritz Separation Inc. System and method for treatment of pathogens in dried sewage sludge
WO2008129182A3 (en) * 2007-03-06 2009-03-12 Ceram Hyd Hydrogen storing method and unit
FR2913417A1 (en) * 2007-03-06 2008-09-12 Ceram Hyd Soc Par Actions Simp HYDROGEN STORAGE PROCESS AND UNIT
WO2008129182A2 (en) * 2007-03-06 2008-10-30 Ceram Hyd Hydrogen storing method and unit
US8383692B2 (en) 2007-05-28 2013-02-26 Ceram Hyd Method of activating boron nitride
US8507147B2 (en) 2007-05-28 2013-08-13 Ceram Hyd Proton exchange membrane and cell comprising such a membrane
US20100280138A1 (en) * 2007-05-28 2010-11-04 Arash Mofakhami Method of activating boron nitride
US9105907B2 (en) 2008-03-06 2015-08-11 Ceram Hyd Material for an electrochemical device
US7833394B2 (en) * 2008-05-27 2010-11-16 Samsung Electro-Mechanics Co., Ltd. Housing, apparatus for generating hydrogen and fuel cell power generation system having the same
US20090297899A1 (en) * 2008-05-27 2009-12-03 Samsung Electro-Mechanics Co., Ltd. Housing, apparatus for generating hydrogen and fuel cell power generation system having the same
FR2968462A1 (en) * 2010-12-06 2012-06-08 Michelin Soc Tech DEVICE FOR GENERATING ELECTRICITY BY FUEL CELL.
WO2012076445A1 (en) * 2010-12-06 2012-06-14 Societe De Technologie Michelin Device for generating electricity using a fuel cell
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

Also Published As

Publication number Publication date
ZA200305589B (en) 2005-02-23
WO2002084771A1 (en) 2002-10-24
CN1489798A (en) 2004-04-14

Similar Documents

Publication Publication Date Title
US20020100682A1 (en) Hydrogen recharging system for fuel cell hydride storage reservoir
US7727647B2 (en) Portable hydrogen fuel container charger
EP2976803B1 (en) Metal/oxygen battery with oxygen pressure management
US10312562B2 (en) Metal-oxygen battery system having a suction function and a blowing function
JPH08507830A (en) Electrochemical fullerene system
JP6178871B2 (en) Metal oxygen battery with multistage oxygen compressor
JP2746751B2 (en) Method and apparatus for charging and discharging electrical energy
EP1661199A2 (en) Hydrogen storage-based rechargeable fuel cell system
US7700214B1 (en) Metal hydride fuel cell cartridge and electrolyzer electrode
US8246796B2 (en) Fuel cell recharger
US20090226776A1 (en) Hydrogen charging apparatus
JP6178870B2 (en) Metal oxygen battery with multistage oxygen compressor
CN104577167B (en) Fuel cell recharger
JP5563443B2 (en) Method for generating hydrogen molecules from silicon hydride
KR102358856B1 (en) Rechargeable electrochemical device for producing electrical energy
CN101263625A (en) Fuel cell recharger
US20110003225A1 (en) Recharging valve for a fuel cell

Legal Events

Date Code Title Description
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

AS Assignment

Owner name: MOTOROLA, INC., ILLINOIS

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:MUTHUSWAMY, SIVAKUMAR;REEL/FRAME:011696/0963

Effective date: 20010323

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION