Methanation of anode exhaust gas to enhance carbon dioxide capture

Patent metadata

Field	Value
Publication number	US-11508981-B2
Application number	US-201716097165-A
Country	US
Kind code	B2
Filing date	Apr 12, 2017
Priority date	Apr 29, 2016
Publication date	Nov 22, 2022
Grant date	Nov 22, 2022

Abstract

A power production system includes a flue gas generator configured to generate a flue gas that includes carbon dioxide and oxygen; a fuel supply; a fuel cell assembly that includes: a cathode section configured to receive the flue gas generated by the flue gas generator, and output cathode exhaust, and an anode section configured to receive fuel from the fuel supply, and output anode exhaust that contains hydrogen and carbon dioxide; a methanator configured to receive the anode exhaust, convert at least a portion of the hydrogen in the anode exhaust to methane, and output methanated anode exhaust; a chiller assembly configured to cool the methanated anode exhaust to a predetermined temperature so as to liquefy carbon dioxide in the methanated anode exhaust; and a gas separation assembly configured to receive the cooled methanated anode exhaust and separate the liquefied carbon dioxide from residual fuel gas.

First claim

What is claimed is:

1. A power production system comprising:
a flue gas generator configured to generate a flue gas that includes carbon dioxide and oxygen;
a fuel supply;
a fuel cell assembly that includes:
a cathode section configured to receive the flue gas generated by the flue gas generator, and to output cathode exhaust, and
an anode section configured to receive fuel from the fuel supply, and to output anode exhaust that contains between 20 mol % and 25 mol % hydrogen and between 65 mol % and 75 mol % carbon dioxide;

a methanator configured to receive the anode exhaust, convert at least a portion of the hydrogen in the anode exhaust to methane, and output methanated anode exhaust containing between 5 mol % and 10 mol % hydrogen and between 75 mol % and 85 mol % carbon dioxide;
a chiller assembly configured to cool the methanated anode exhaust to a predetermined temperature so as to liquefy carbon dioxide in the methanated anode exhaust; and
a gas separation assembly configured to receive the cooled methanated anode exhaust and separate the liquefied carbon dioxide from residual fuel gas.

2. The power production system of claim 1 , wherein the flue gas generated by the flue gas generator includes 3-15% carbon dioxide, 1-20% water, and 3-15% oxygen, with a balance being nitrogen.

3. The power production system of claim 1 , further comprising a supplementary air source configured to provide supplementary air to the flue gas before the flue gas is received at the cathode section of the fuel cell assembly.

4. The power production system of claim 1 , further comprising a heat recovery assembly configured to receive the cathode exhaust, recover waste heat from the cathode exhaust, and provide the waste heat to drive the chiller assembly.

5. The power production system of claim 1 , wherein the cathode section of the fuel cell assembly is configured to receive exclusively all or part of the flue gas generated by the flue gas generator.

6. The power production system of claim 1 , further comprising a water removal assembly configured to receive the methanated anode exhaust, and provide water-separated methanated anode exhaust to the chiller assembly.

7. The power production system of claim 1 , further comprising a compressor configured to compress the methanated anode exhaust before the methanated anode exhaust is provided to the chiller assembly.

8. The power production system of claim 7 , wherein the compressor is configured to compress the methanated anode exhaust to at least 200 psi.

9. The power production system of claim 1 , wherein the chiller assembly is configured to cool the methanated anode exhaust to a temperature below −40° C.

10. The power production system of claim 1 , further comprising:
an oxidizer configured to:
receive the flue gas from the flue gas generator,
receive the residual fuel gas from the gas separation assembly,
oxidize the residual fuel gas to heat the flue gas, and
provide the heated flue gas to the cathode section of the fuel cell assembly.

11. The power production system of claim 10 , further comprising a heat exchanger configured to heat the flue gas from the flue gas generator using waste heat in the cathode exhaust, and provide the heated flue gas to the oxidizer.

12. The power production system of claim 1 , further comprising a heat exchanger configured to heat the flue gas from the flue gas generator using waste heat in the cathode exhaust, and provide the heated flue gas to the cathode section of the fuel cell assembly.

13. The power production system of claim 1 , further comprising a heat exchanger configured to heat fuel gas from the fuel supply using waste heat in the cathode exhaust, and provide the heated fuel gas to the anode section of the fuel cell assembly.

14. The power production system of claim 1 , where the anode section of the fuel cell assembly is configured to receive a part of the residual fuel gas from the gas separation assembly.

Assignees

• Fuelcell Energy Inc

Inventors

• Jahnke Fred C

Classifications

• B01D53/326

  in electrochemical cells · CPC title

• B01D2257/80

  Water · CPC title

• F01K23/10 Primary

  with exhaust fluid of one cycle heating the fluid in another cycle (F01K17/025 takes precedence) · CPC title

• F02C1/00

  Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid (by the use of combustion products F02C3/00, F02C5/00) · CPC title

• C01B3/586

  the reaction being a methanation reaction · CPC title