IP Library Granted Patent US 11,738,996
Granted Patent B2
US 11,738,996 · App. 17/397,512 · Granted Aug 29, 2023

Power generation using hydrogen fuel with economical carbon dioxide capture

Inventors: Ganesan Subbaraman (Bell Canyon, CA); Jeffrey A. Mays (Woodland, CA); Ronald J. Stanis (Des Plaines, IL)
Assignee: GAS TECHNOLOGY INSTITUTE
C01B3/38B01D53/48B01D53/62B01D53/82B01D53/83B01D53/96C01B3/44F01K23/10F01K23/106F02C3/205F02C7/22B01D2251/404B01D2251/602B01D2256/16B01D2257/504C01B2203/0233C01B2203/043C01B2203/0425C01B2203/0475C01B2203/1241C01B2203/1258C01B2203/84Y02C20/40Y02E20/18
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Quick Facts
Patent No.
US 11,738,996
App. No.
17/397,512
Granted
Aug 29, 2023
Kind
B2
Abstract

Systems and methods for generating power using hydrogen fuel, such as derived from natural gas, are provided. Feed materials are introduced into a compact hydrogen generator to produce carbon dioxide, hydrogen gas and steam. Sorbent material within the compact hydrogen generator acts to absorb carbon dioxide, forming a used sorbent. Hydrogen gas and steam are separated from the used sorbent and passed to a power generator such as a hydrogen turbine to produce power. The used sorbent is introduced into a calciner and heated to desorb carbon dioxide and form a regenerated sorbent which can be recycled to the compact hydrogen generator.

Claims (38)

1. A system for power generation, the system comprising:

a compact hydrogen generator, the compact hydrogen generator containing a quantity of a sorbent material and a reforming catalyst, wherein the compact hydrogen generator comprises a fluidized bed configured to fluidize both the reforming catalyst and the sorbent material in combination with a feed material, wherein the feed material comprises natural gas and steam, and wherein the feed material in contact with the reforming catalyst produces H 2 product and carbon dioxide and the sorbent material absorbs carbon dioxide and forms a used sorbent;

a gas/solids separator connected to the compact hydrogen generator to separate the H 2 product and the used sorbent, wherein the reforming catalyst and the sorbent material are both fluidized in the bed and each of the reforming catalyst and the sorbent material has a corresponding size configured for the reforming catalyst to remain in the fluidized bed while the H 2 product and used sorbent are conveyed by elutriation from the fluidized bed to the gas/solids separator;

a calciner connected to the gas/solids separator to heat the used sorbent to desorb carbon dioxide from the used sorbent to produce regenerated sorbent;

a recycle line to introduce at least a portion of the regenerated sorbent from the calciner to the compact hydrogen generator; and

at least one power generator to receive and utilize at least a portion of the H 2 product from the gas/solids separator to produce power.

2. The system of claim 1 wherein the feed material fluidizes the regenerated sorbent in the recycle line and delivers the regenerated sorbent to a bottom of the fluidized bed reactor.

3. The system of claim 1 wherein the compact hydrogen generator containing the sorbent material comprises a bubbling fluidized bed of the sorbent material and the reforming catalyst for catalytic conversion of methane to the H 2 product.

4. The system of claim 1 wherein the natural gas comprises sulfur, said system additionally comprises:

a desulfurizer to remove sulfur from the natural gas prior to passage to the compact hydrogen generator.

5. The system of claim 1 wherein the calciner is an indirect heating calciner.

6. The system of claim 1 wherein the at least one power generator comprises a gas turbine or a hydrogen turbine and produces a flue gas, wherein said system additionally comprises a heat recovery steam generator connected to the at least one power generator to accept at least a portion of the flue gas, recover heat from the flue gas and generate steam.

7. The system of claim 1 wherein the compact hydrogen generator operates at a pressure of at least 35 psia to produce the H 2 product and carbon dioxide.

8. The system of claim 1 wherein the calciner operates at atmospheric pressure to heat the used sorbent to desorb carbon dioxide from the used sorbent to produce regenerated sorbent.

9. The system of claim 1 wherein the calciner heats the used sorbent to desorb carbon dioxide from the used sorbent.

10. The system of claim 1 additionally comprising:

a H 2 purifier to purify at least a portion of the H 2 product from the gas/solids separator to form purified H 2 product;

a storage vessel to temporarily store at least a portion of the purified H 2 product; and

a first process line to selectively pass a portion of the temporarily stored H 2 product from the storage vessel to the at least one power generator.

11. The system of claim 1 wherein the at least one power generator is a turbine.

12. The system of claim 11 wherein the-turbine is a hydrogen turbine.

13. The system of claim 1 wherein the at least one power generator is a reciprocating engine.

14. The system of claim 1 wherein the feed material produces generator products including H 2 , the carbon dioxide, and steam, the gas/solids separator separates the used sorbent from the H 2 and steam, and the at least one power generator receives and utilizes at least a portion of the H 2 and steam from the gas/solids separator to produce power.

15. The system of claim 14 wherein the compact hydrogen generator has a steam to carbon ratio operating range between 2.5:1 to 4:1.

16. The system of claim 14 wherein the compact hydrogen generator produces generator products having a steam to hydrogen ratio, on a volume basis, of between 1:8 and 1:2.

17. A method for producing power via hydrogen gas with the system of claim 1 , said method comprising:

introducing the feed material into the compact hydrogen generator to produce the H 2 product and carbon dioxide, the compact hydrogen generator containing a quantity of the sorbent material to absorb carbon dioxide and form the used sorbent;

introducing the H 2 product and used sorbent from the sorbent enhanced reformer to the gas/solids separator to separate the H 2 product from the used sorbent;

introducing at least a portion of the separated H 2 product to the at least one power generator to produce the power;

introducing at least a portion of the separated used sorbent to the calciner to heat the used sorbent to desorb carbon dioxide from the used sorbent to produce the regenerated sorbent and CO 2 ; and

recycling the at least a portion of the regenerated sorbent to the sorbent enhanced reformer.

18. A method for producing power via hydrogen gas with the system of claim 14 , said method comprising:

introducing the feed material into the compact hydrogen generator to produce the products including H 2 , carbon dioxide, and steam, the compact hydrogen generator containing the quantity of a sorbent material to absorb carbon dioxide and form a used sorbent;

introducing the H 2 , steam and used sorbent from the sorbent enhanced reformer to the gas/solids separator to separate the H 2 and steam from the used sorbent;

introducing at least a portion of the separated H 2 and steam to the at least one power generator to produce power;

introducing at least a portion of the separated used sorbent to the calciner to heat the used sorbent to desorb carbon dioxide from the used sorbent to produce regenerated sorbent and CO 2 ; and

recycling at least a portion of the regenerated sorbent to the sorbent enhanced reformer,

wherein the sorbent enhanced reformer has a steam to carbon ratio operating range between 2.5:1 to 4:1 or produces products having a steam to hydrogen ratio, on a volume basis, of between 1:8 and 1:2.

Continuity (7)
Continuation 16220946 · Dec 14, 2018
Continuation In Part 15892616 · Feb 9, 2018
Continuation In Part 15165521 · May 26, 2016
Provisional Application 62697285 · Jul 12, 2018
Provisional Application 62456993 · Feb 9, 2017
Provisional Application 62167871 · May 28, 2015
Related Publication 20210363006A1 · Nov 25, 2021