Heat generation for separate endothermic process with carbon capture

Patent metadata

Field	Value
Publication number	US-11761625-B2
Application number	US-202217990415-A
Country	US
Kind code	B2
Filing date	Nov 18, 2022
Priority date	Nov 18, 2021
Publication date	Sep 19, 2023
Grant date	Sep 19, 2023

Abstract

A method for transferring thermal energy to a separate endothermic process includes: (a) providing a carbon dioxide (CO 2 ) stream and a carbonaceous fuel to a heater; (b) reacting the carbonaceous fuel in the heater to produce a heated stream; (c) transferring heat from the heated stream to the separate endothermic process; (d) separating the CO 2 stream from the heated stream after (c); and (e) recycling the CO 2 stream to the heater after (d).

First claim

What is claimed is:

1. A method of transferring thermal energy to a separate endothermic process, the method comprising:
(a) providing a carbon dioxide (CO 2 ) stream and a carbonaceous fuel to a heater;
(b) reacting the carbonaceous fuel with an oxidantin the heater to produce a heated stream;
(c) transferring heat from the heated stream to the separate endothermic process;
(d) separating the CO 2 stream from the heated stream after (c); and
(e) recycling the CO 2 stream to the heater after (d).

2. The method of claim 1 , further comprising transferring heat from the heated stream to the CO 2 stream and the carbonaceous fuel.

3. The method of claim 2 , wherein separating the CO 2 stream from the heated stream comprises cooling the heated stream.

4. The method of claim 3 , wherein cooling the heated stream comprises contacting the heated stream with water.

5. The method of claim 4 , wherein contacting the heated stream with water comprises:
separating a supply of water from the heated stream; and
contacting the heated stream with the supply of water.

6. The method of claim 2 , further comprising:
providing an oxidant to the heater; and
transferring heat from the heated stream to the oxidant.

7. The method of claim 2 , wherein the heater comprises an oxygen ion transport membrane heater, and wherein the method further comprises:
receiving an air stream in the heater, the air stream comprising an oxidant; and
exposing the carbonaceous fuel to the oxidant within the heater.

8. The method of claim 7 , wherein the heater includes a membrane, and wherein the method further comprises:
passing the carbonaceous fuel and the CO 2 stream on a first side of the membrane;
passing the air stream on a second side of the membrane, the second side being opposite the first side; and
diffusing oxygen from the air stream across the membrane from the second side to the first side.

9. A system for transferring thermal energy to a separate endothermic process, comprising:
a heater including one or more inlets that are configured to receive a carbonaceous fuel, an oxidant, and a carbon dioxide (CO 2 ) stream, and also including an outlet, the heater configured to react the carbonaceous fuel with the oxidant in the presence of the CO 2 stream to produce a heated stream;
a heat transfer assembly fluidly coupled to the outlet, the heat transfer assembly configured to transfer heat from the heated stream to the separate endothermic process;
a separator fluidly coupled to and downstream of the heat transfer assembly, the separator configured to separate out the CO 2 stream from the heated stream, wherein the separator is further coupled to and upstream of the one or more inlets of the heater such that the CO 2 stream is to flow from the separator back toward the one or more inlets of the heater.

10. The system of claim 9 , further comprising a heat exchanger fluidly coupled between the heat transfer assembly and the separator, wherein the heat exchanger is configured to transfer heat from the heated stream to the CO 2 stream and the carbonaceous fuel.

11. The system of claim 10 , wherein the separator comprises a direct contact water cooler.

12. The system of claim 11 , wherein the separator comprises:
a second outlet that is configured to receive a supply of water that is separated from the heated stream within the separator; and
an inlet that is fluidly coupled to the second outlet that is configured to direct the supply of water back into the separator to contact the heated stream.

13. The system of claim 10 , wherein the one or more inlets of the heater are configured to receive an oxidant stream; and wherein the system further comprises:
a second heat exchanger that is configured to heat the oxidant upstream of the heater.

14. The system of claim 13 , wherein the heated stream is fluidly coupled to the second heat exchanger such that the second heat exchanger is configured to transfer heat from the heated stream to the oxidant stream.

15. The system of claim 10 , wherein the heater comprises an oxygen ion transport membrane heater including a membrane, wherein the heater is configured to pass the carbonaceous fuel and the CO 2 stream on a first side of the membrane and is configured to pass an air stream on a second side of the membrane, the second side being opposite the first side.

16. A method of generating thermal energy for a separate endothermic process, the method comprising:
(a) producing a CO 2 stream from a first outlet of a separator;
(b) flowing the CO 2 stream to a heater;
(c) reacting a carbonaceous fuel with an oxidant in the presence of the CO 2 stream within the heater;
(d) outputting a heated stream from the heater;
(e) transferring heat from the heated stream to the separate endothermic process;
(f) heating the carbonaceous fuel with the heated stream, upstream of the heater after (e); and
(g) flowing the heated stream to the separator after (f).

17. The method of claim 16 , comprising:
separating out a supply of water from the heated stream within the separator; and
recycling the supply of water back into the separator.

18. The method of claim 17 , comprising contacting the heated stream with the supply of water.

19. The method of claim 18 , wherein the heater comprises an oxygen ion transport membrane heater including a membrane, and wherein the method further comprises:
passing the carbonaceous fuel and the CO 2 stream on a first side of the membrane;
passing an air stream on a second side of the membrane, the second side being opposite the first side; and
diffusing oxygen from the air stream across the membrane from the second side to the first side.

20. The method of claim 18 , further comprising:
providing an oxidant to the heater; and
transferring heat from the heated stream to the oxidant upstream of the heater.

Assignees

• 8 Rivers Capital Llc

Inventors

• Allam Rodney John
• Brown Jr Glenn William

Classifications

• F23L2900/07005

  Injecting pure oxygen or oxygen enriched air · CPC title

• F23L2900/07001

  Injecting synthetic air, i.e. a combustion supporting mixture made of pure oxygen and an inert gas, e.g. nitrogen or recycled fumes · CPC title

• F23J2900/15061

  Deep cooling or freezing of flue gas rich of CO2 to deliver CO2-free emissions, or to deliver liquid CO2 · CPC title

• F23J2215/50

  Carbon dioxide · CPC title

• F23C2202/30

  Premixing fluegas with combustion air · CPC title