Sorbent-enhanced processes for the reaction of fuel to produce hydrogen and related systems
US-11999620-B2 · Jun 4, 2024 · US
US12434966B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12434966-B2 |
| Application number | US-202418642429-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 22, 2024 |
| Priority date | Nov 7, 2019 |
| Publication date | Oct 7, 2025 |
| Grant date | Oct 7, 2025 |
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Methods of using sorbents to enhance the production of hydrogen from fuel, and related systems, are generally described. In some embodiments, the production of hydrogen from the fuel involves a reforming reaction and/or a gasification reaction combined with a water-gas shift reaction.
Opening claim text (preview).
What is claimed is: 1. A system, comprising: a reactor configured to react carbon monoxide (CO) in a water-gas shift reaction (WGSR) that generates (i) hydrogen and (ii) carbon dioxide (CO 2 ), and a separator in fluid communication with said reactor, wherein said separator comprises a molten sorbent comprising a salt in molten form, wherein said molten sorbent is configured to capture at least a portion of said CO 2 , thereby obtaining captured CO 2 . 2. The system of claim 1 , wherein said CO is produced by reacting a fuel and steam. 3. The system of claim 2 , wherein said fuel comprises methane. 4. The system of claim 2 , wherein said fuel comprises a hydrocarbon of the form C n H 2n+2 , where n is an integer number. 5. The system of claim 1 , wherein said reactor further comprises a catalyst. 6. The system of claim 1 , wherein said separator comprises a CO 2 permeable membrane. 7. The system of claim 1 , further comprising a desorber in fluid communication with said separator, wherein said desorber is configured to release at least a portion of said captured CO 2 from said molten sorbent. 8. The system of claim 1 , wherein said salt in molten form comprises boron and oxygen. 9. The system of claim 1 , wherein said salt in molten form comprises an alkali metal borate, A x B 1-x O 1.5-x , where A is an alkali metal, B is Boron, O is Oxygen, and x is a number such that 0<x<1. 10. The system of claim 1 , wherein said reactor and said separator are located in a single vessel. 11. A method, comprising: directing carbon monoxide (CO) into a reactor; in said reactor, reacting said CO in a water gas shift reaction (WGSR) that generates (i) hydrogen and (ii) carbon dioxide (CO 2 ); and directing a stream comprising said CO 2 from said reactor to a separator in fluid communication with said reactor, wherein said separator comprises a molten sorbent comprising a salt in molten form that captures at least a portion of said CO 2 , thereby obtaining captured CO 2 . 12. The method of claim 11 , wherein said CO is produced by reacting a fuel and steam. 13. The method of claim 12 , wherein said fuel comprises methane. 14. The method of claim 12 , wherein said fuel comprises a hydrocarbon of the form C n H 2n+2 , where n is an integer number. 15. The method of claim 11 , wherein said reactor further comprises a catalyst. 16. The method of claim 11 , wherein said separator comprises a CO 2 permeable membrane. 17. The method of claim 11 , further comprising directing said captured CO 2 to a desorber, and in said desorber, releasing at least a portion of said captured CO 2 from said molten sorbent. 18. The method of claim 11 , wherein said salt in molten form comprises boron and oxygen. 19. The method of claim 11 , wherein said salt in molten form comprises an alkali metal borate, A x B 1-x O 1.5-x , where A is an alkali metal, B is Boron, O is Oxygen, and x is a number such that 0<x<1. 20. The method of claim 11 , wherein said reactor and said separator are located in a single vessel.
by reaction of hydrocarbons with gasifying agents · CPC title
Carbon dioxide sequestration · CPC title
Natural gas or methane · CPC title
by combustion of fuel · CPC title
containing a CO-shift step, i.e. a water gas shift step · CPC title
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