Carbon dioxide removal from anode exhaust of a fuel cell by cooling/condensation

Patent metadata

Field	Value
Publication number	US-11094952-B2
Application number	US-201716094792-A
Country	US
Kind code	B2
Filing date	Apr 20, 2017
Priority date	Apr 21, 2016
Publication date	Aug 17, 2021
Grant date	Aug 17, 2021

Abstract

A system for removing carbon dioxide from anode exhaust gas that has been compressed to form pressurized anode exhaust vapor includes a feed/effluent heat exchanger configured to cool the anode exhaust vapor to a first predetermined temperature and partially condense carbon dioxide in the anode exhaust vapor; a first vapor-liquid separator configured to receive an output of the feed/effluent heat exchanger and separate liquid carbon dioxide from uncondensed anode exhaust vapor; a feed/refrigerant heat exchanger configured to receive the uncondensed anode exhaust vapor from the first vapor-liquid separator, cool the uncondensed anode exhaust vapor to a second predetermined temperature, and condense carbon dioxide in the uncondensed anode exhaust vapor; a second vapor-liquid separator configured to receive an output of the feed/refrigerant heat exchanger and separate liquid carbon dioxide to form hydrogen rich, uncondensed anode exhaust vapor.

First claim

What is claimed:

1. A system for removing carbon dioxide from anode exhaust gas that has been compressed to form pressurized anode exhaust vapor, the system comprising:
a feed/effluent heat exchanger configured to cool the anode exhaust vapor to a first predetermined temperature and partially condense carbon dioxide in the pressurized anode exhaust vapor;
a first vapor-liquid separator configured to receive an output of the feed/effluent heat exchanger and separate liquid carbon dioxide from uncondensed anode exhaust vapor;
a feed/refrigerant heat exchanger configured to receive the uncondensed anode exhaust vapor from the first vapor-liquid separator, cool the uncondensed anode exhaust vapor to a second predetermined temperature, and condense additional carbon dioxide in the uncondensed anode exhaust vapor;
a second vapor-liquid separator configured to receive an output of the feed/refrigerant heat exchanger and separate liquid carbon dioxide to form hydrogen rich, uncondensed anode exhaust vapor;
a mixer configured to receive and mix the liquid carbon dioxide separated by the first vapor-liquid separator and the liquid carbon dioxide separated by the second vapor-liquid separator; and
a pressure reduction valve configured to receive a total liquid carbon dioxide from the mixer, the total liquid carbon dioxide comprising the liquid carbon dioxide separated by the first vapor-liquid separator and the liquid carbon dioxide separated by the second vapor-liquid separator, wherein:
the pressure reduction valve is further configured to reduce a pressure of the total liquid carbon dioxide from a first pressure to a second pressure lower than the first pressure, and
the feed/effluent heat exchanger is configured to receive the total liquid carbon dioxide having the second pressure and to use the total liquid carbon dioxide as a cooling media.

2. The system of claim 1 , wherein after being used as the cooling media in the feed/effluent heat exchanger, the total liquid carbon dioxide is output from the feed/effluent heat exchanger as a reheated carbon dioxide stream, and
wherein the reheated carbon dioxide stream is further heated and sent to an expander to recover additional energy either as power or mechanical energy.

3. The system of claim 1 , wherein the first pressure is from 200 to 400 psig and the second pressure is from 65 to 100 psig.

4. The system of claim 1 , wherein the anode exhaust vapor has a pressure from 200 to 400 psig at an inlet of the feed/effluent heat exchanger.

5. The system of claim 1 , wherein the feed/refrigerant heat exchanger cools the uncondensed anode exhaust vapor to the second predetermined temperature and condenses carbon dioxide in the uncondensed anode exhaust vapor using external refrigeration.

6. The system of claim 1 , further comprising a shift unit or a water condensation unit configured to compress the anode exhaust gas to form the anode exhaust vapor upstream of the feed/effluent heat exchanger,
wherein the anode exhaust vapor has a pressure from 200 to 400 psig at an inlet of the feed/effluent heat exchanger.

7. The system of claim 1 , further comprising a flow path configured to receive a portion of the carbon dioxide separated from the anode exhaust vapor and to export the portion of the carbon dioxide separated from the anode exhaust vapor for sequestration or other uses.

8. A fuel cell system comprising:
a fuel cell comprising a cathode, an anode, and an electrolyte matrix provided between the cathode and the anode;
the system of claim 1 for removing carbon dioxide from anode exhaust gas to form hydrogen rich, uncondensed anode exhaust vapor; and
a pressure swing adsorption system configured to separate carbon dioxide and other impurities from the hydrogen rich, uncondensed anode exhaust vapor to purify hydrogen or syngas from the anode exhaust gas.

9. A method of removing carbon dioxide from anode exhaust gas, the method comprising:
compressing the anode exhaust gas to form anode exhaust vapor;
cooling the anode exhaust vapor to a first predetermined temperature and partially condensing carbon dioxide in the anode exhaust vapor in a first heat exchanger;
receiving an output of the first heat exchanger in a first vapor-liquid separator;
separating liquid carbon dioxide from uncondensed anode exhaust vapor in the first vapor-liquid separator;
receiving the uncondensed anode exhaust vapor from the first vapor-liquid separator in a second heat exchanger;
cooling the uncondensed anode exhaust vapor to a second predetermined temperature and condensing carbon dioxide in the uncondensed anode exhaust vapor in the second heat exchanger;
receiving an output of the second heat exchanger in a second vapor-liquid separator;
separating, in the second vapor-liquid separator, liquid carbon dioxide from the output of the second heat exchanger to form hydrogen rich, uncondensed anode exhaust vapor;
receiving and mixing the liquid carbon dioxide separated by the first vapor-liquid separator and the liquid carbon dioxide separated by the second vapor-liquid separator to form a total liquid carbon dioxide;
reducing a pressure of the total liquid carbon dioxide from a first pressure to a second pressure lower than the first pressure by passing the total liquid carbon dioxide through a pressure reduction valve;
feeding the total liquid carbon dioxide having the second pressure to the first heat exchanger; and
cooling the first heat exchanger using the total liquid carbon dioxide.

10. The method of claim 9 , wherein the cooling step reheats the total liquid carbon dioxide such that a reheated carbon dioxide stream is output from the first heat exchanger, and
the method further comprises:
further heating the reheated carbon dioxide stream; and
recovering additional energy from the further heated reheated carbon dioxide stream using an expander.

11. The method of claim 9 , wherein the first pressure is from 200 to 400 psig and the second pressure is from 65 to 100 psig.

12. The method of claim 9 , wherein the step of compressing the anode exhaust gas to form the anode exhaust vapor comprises compressing the anode exhaust gas to a pressure from 200 to 400 psig.

13. The method of claim 9 , wherein the step of cooling the uncondensed anode exhaust vapor to the second predetermined temperature and condensing carbon dioxide in the uncondensed anode exhaust vapor in the second heat exchanger is performed using external refrigeration.

14. The method of claim 9 , further comprising purifying the hydrogen rich, uncondensed anode exhaust vapor by separating carbon dioxide and other impurities therefrom.

15. The method of claim 14 , wherein the step of purifying the hydrogen rich, uncondensed anode exhaust vapor comprises feeding the hydrogen rich, uncondensed anode exhaust vapor output from the second vapor-liquid separator to a pressure swing adsorption system.

Assignees

• Fuelcell Energy Inc

Inventors

• Jahnke Fred C
• Leo Anthony M

Classifications

• Y02E60/50

  Fuel cells · CPC title

• F25J3/067

  separation of carbon dioxide (production of carbon dioxide in general C01B32/00) · CPC title

• C01B2203/066

  with fuel cells · CPC title

• B01D53/62

  Carbon oxides · CPC title

• C01B2203/043

  Regenerative adsorption process in two or more beds, one for adsorption, the other for regeneration · CPC title