Claims
- 1. A process for reversibly sorbing hydrogen gas comprising bringing a hydrogen-containing gas into contact with a carbon-metal hybrid material under conditions of temperature and partial pressure of hydrogen whereby the carbon-metal hybrid material sorbs said hydrogen gas, and subsequently adjusting the temperature and/or pressure to cause desorption of said hydrogen gas from the carbon-metal hybrid material; said process characterized in that the carbon-metal hybrid material comprises a substantially graphitic carbon component and a metal or metal alloy component which reversibly reacts with the hydrogen.
- 2. A process in accordance with claim 1 wherein said substantially graphitic carbon component of the carbon-metal hybrid material is selected from the group consisting of graphite, exfoliated graphite, single wall carbon nanotubes, single wall carbon nanocones, carbon nanocells, multi-wall carbon nanotubes, carbon nanofilm, mesoporous and microporous carbon microbeads, substantially graphitized carbon soot, and mixtures thereof.
- 3. A process in accordance with claim 2 wherein said substantially graphitic carbon component of the carbon-metal hybrid material is a single-sheet graphitic structure.
- 4. A process in accordance with claim 1 wherein said metal component of the carbon-metal hybrid material is a metal or an alloy containing a metal selected from the group consisting of Pt, Pd, Ir, Rh, Ru, Os, Ni, Co, Ti, Zr, Hf, V, Nb, Ta, and mixtures thereof.
- 5. A process in accordance with claim 1 wherein the said metal or metal alloy components of the carbon-metal hybrid material has been reacted with hydrogen to form a metal hydride prior to combination with the substantially graphitic carbon component to form the carbon-metal hybrid.
- 6. A process in accordance with claim 1 wherein the hydrogen-containing gas is brought into contact with said carbon-metal hybrid material in a vessel at a pressure from between 14 psia to 2000 psia of hydrogen partial pressure whereby said hybrid material sorbs said hydrogen gas, and the pressure in the vessel is subsequently reduced without adjusting the temperature, thereby desorbing the hydrogen gas from the carbon-metal hybrid material.
- 7. A process in accordance with claim 6 wherein said pressure in the vessel is reduced to about 1 psia to 200 psia to desorb said hydrogen gas.
- 8. A process in accordance with claim 1 wherein the hydrogen-containing gas is brought into contact with said carbon-metal hybrid material in a vessel at a temperature from between 253 K to 473 K whereby said hybrid material sorbs said hydrogen gas, and the temperature in the vessel is subsequently increased without adjusting the pressure, thereby desorbing the hydrogen gas from the carbon-metal hybrid material.
- 9. A process in accordance with claim 8 wherein said temperature in the vessel is increased to about 273 K to 573 K to desorb said hydrogen gas.
- 10. A process in accordance with claim 1 wherein said hydrogen-containing gas is contacted with said carbon-metal hybrid material for about 0.5 to 120 minutes.
- 11. A process in accordance with claim 1 wherein said carbon-metal hybrid material can store between 0.1 and 10 wt % hydrogen at ambient or near-ambient conditions of temperature and pressure.
- 12. A process in accordance with claim 1 wherein said carbon-metal hybrid material contains a bulk concentration of metal or metal alloy, which comprises from 1 to 80% on a weight basis of the carbon-metal hybrid material.
- 13. A process for reversibly storing hydrogen using a carbon-metal hybrid material, which hybrid material comprises a substantially graphitic carbon component and a metal or metal alloy component capable of reversibly reacting with hydrogen, said process comprising bringing a hydrogen-containing gas into contact with said carbon-metal hybrid material within a storage vessel at a hydrogen partial pressure from about 14 psia to 2000 psia and a temperature from about 253 K to 473 K whereby said carbon-metal hybrid material sorbs, thereby storing said hydrogen gas, and subsequently reducing the hydrogen partial pressure to between about 1 psia to 200 psia and increasing the temperature to between about 273 k to 573 K to desorb said hydrogen gas from said carbon-metal hybrid material.
- 14. A process in accordance with claim 13 wherein the hydrogen-containing gas is contacted with the carbon-metal hybrid material within the storage vessel at a hydrogen partial pressure from about 20 psia to 500 psia and a temperature from about 273 K to 323 K.
- 15. A process in accordance with claim 14 wherein after said carbon-metal hybrid material sorbs said hydrogen, the hydrogen partial pressure is reduced to between 14 psia to 50 psia and the temperature is increased to between about 293 K to 363 K to desorb the hydrogen gas from the carbon-metal hybrid material.
- 16. A process in accordance with claim 13 wherein said substantially graphitic carbon component of the carbon-metal hybrid material is selected from the group consisting of graphite, exfoliated graphite, single wall carbon nanotubes, single wall carbon nanocones, carbon nanocells, multi-wall carbon nanotubes, carbon nanofilm, mesoporous and microporous carbon microbeads, substantially graphitized carbon soot, and mixtures thereof.
- 17. A process in accordance with claim 13 wherein said metal component of the carbon-metal hybrid material is a metal or an alloy containing a metal selected from the group consisting of Pt, Pd, Ir, Rh, Ru, Os, Ni, Co, Ti, Zr, Hf, V, Nb, Ta, and mixtures thereof.
- 18. A process in accordance with claim 13 wherein said hydrogen can be stored within said carbon-metal hybrid material for an indefinite period of time before it is desorbed.
- 19. A process in accordance with claim 18 wherein said carbon-metal hybrid material stores between 0.1 and 10 wt % hydrogen at ambient conditions.
- 20. A process in accordance with claim 13 wherein the hydrogen stored in the carbon-metal hybrid material can be desorbed and recovered on demand by adjusting conditions of temperature and/or pressure to provide a readily available supply of hydrogen.
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] The present application is a continuation-in-part of Provisional Patent Application No. 60/252,751 filed Nov. 22, 2000.
Provisional Applications (1)
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Number |
Date |
Country |
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60252751 |
Nov 2000 |
US |