Carbon-oxygen battery and method of use thereof

Patent metadata

Field	Value
Publication number	US-2024274847-A1
Application number	US-202418631919-A
Country	US
Kind code	A1
Filing date	Apr 10, 2024
Priority date	Oct 11, 2022
Publication date	Aug 15, 2024
Grant date	—

Abstract

A carbon-oxygen battery system, including: a Boudouard reactor in fluid communication with an electrochemical cell, wherein the electrochemical cell has a CO/CO 2 inlet, a CO/CO 2 outlet, and an oxygen outlet, and wherein the CO/CO 2 outlet is fluidly connected by a first stream to an inlet of the Boudouard reactor, and wherein the CO/CO 2 inlet is fluidly connected by a second stream to an outlet of the Boudouard reactor, and a CO/CO 2 tank fluidly connected to at least one of the first stream or the second stream.

First claim

1 . A carbon-oxygen battery system, comprising:
a Boudouard reactor comprising a carbon store and in fluid communication with an electrochemical cell,
wherein the electrochemical cell comprises a CO/CO 2 inlet, a CO/CO 2 outlet, and an oxygen inlet/outlet,
wherein the CO/CO 2 outlet is fluidly connected by a first stream to an inlet of the Boudouard reactor, and
wherein the CO/CO 2 inlet is fluidly connected by a second stream to an outlet of the Boudouard reactor,
a CO/CO 2 tank fluidly configured to store CO, CO 2 , or a combination thereof and connected to at least one of the first stream or the second stream; and a fuel gauge configured to determine a state of charge based on a pressure drop through the Boudouard reactor.

2 . The carbon-oxygen battery system of claim 1 , wherein the pressure drop is determined between the inlet and the outlet of the Boudouard reactor.

3 . The carbon-oxygen battery system of claim 1 , wherein the carbon store is configured to provide carbon.

4 . The carbon-oxygen battery system of claim 1 , further comprising an external carbon source.

5 . The carbon-oxygen battery system of claim 1 , further comprising a carbon store fuel gauge configured to sense a mass of carbon in the carbon store, a volume of carbon in the carbon store, or a combination thereof.

6 . The carbon-oxygen battery system of claim 1 , further comprising a CO/CO 2 tank fuel gauge, wherein the CO/CO 2 tank fuel gauge is configured to sense a mass of CO/CO 2 in the CO/CO 2 tank, a pressure of CO/CO 2 in the CO/CO 2 tank, or a combination thereof.

7 . The carbon-oxygen battery system of claim 1 , further comprising an O 2 tank fluidly configured to store a gas comprising O 2 and connected to the electrochemical cell.

8 . The carbon-oxygen battery system of claim 7 , further comprising an O 2 tank fuel gauge, wherein the O 2 tank fuel gauge is configured to sense a mass of the gas comprising O 2 in the O 2 tank, a pressure of the gas comprising O 2 in the O 2 tank, or a combination thereof.

9 . The carbon-oxygen battery system of claim 1 , wherein the electrochemical cell comprises a positive electrode, a negative electrode, and an electrolyte, wherein the electrolyte comprises a solid oxide electrolyte, a molten carbonate electrolyte, or a combination thereof and wherein the positive electrode and the negative electrode are connected to an external circuit.

10 . The carbon-oxygen battery system of claim 1 , further comprising a heat exchanger configured to exchange heat between the Boudouard reactor and the electrochemical cell.

11 . The carbon-oxygen battery system of claim 1 , wherein at least one of the Boudouard reactor or the electrochemical cell is disposed in a thermal chamber.

12 . The carbon-oxygen battery system of claim 1 , wherein the electrochemical cell comprises a plurality of electrochemical cells, wherein each electrochemical cell of the plurality of electrochemical cells is in electrical contact with the external circuit.

13 . The carbon-oxygen battery system of claim 12 , wherein at least one electrochemical cell of the plurality of electrochemical cells is a removable electrochemical cell.

14 . The carbon-oxygen battery system of claim 13 , wherein the removable electrochemical cell is configured to be selectively isolated from the carbon-oxygen battery system, preferably wherein the removable electrochemical cell is configured to be selectively isolated from the carbon-oxygen battery system.

15 . The carbon-oxygen battery system of claim 13 , wherein each removable electrochemical cell of the plurality of removable electrochemical cells is electrically connected to the external circuit in parallel.

16 . The carbon-oxygen battery system of claim 13 ,
wherein each removable electrochemical cell is configured to be independently isolated from the system, and wherein the carbon-oxygen battery system is configured to operate when one or more of the removable electrochemical cells is isolated from the system and at least one electrochemical cell is not isolated from the system.

17 . The carbon-oxygen battery system of claim 1 , wherein the battery system comprises a plurality of electrochemical cells,
wherein the battery system further comprises a plurality of thermal chambers, and wherein the Boudouard reactor is disposed in a first thermal chamber of the plurality of thermal chambers, and at least one electrochemical cell of the plurality of electrochemical cells is disposed in a second thermal chamber of the plurality of thermal chambers.

18 . A method of operating the carbon-oxygen battery system of claim 1 , the method comprising:
supplying electricity and a CO/CO 2 stream comprising CO, CO 2 , or a combination thereof to the carbon-oxygen battery system to charge the battery system, wherein
the CO/CO 2 stream is provided by the CO/CO 2 tank,
carbon dioxide from the CO/CO 2 stream is converted to carbon monoxide and oxygen by the electrochemical cell,
the carbon monoxide from the electrochemical cell is converted to carbon dioxide and carbon by the Boudouard reactor, and
the carbon produced by the charging is stored in the carbon store; and
discharging the battery system to convert the carbon to carbon dioxide and produce electricity, wherein
the carbon and carbon dioxide are converted in the Boudouard reactor to carbon monoxide,
the carbon monoxide and oxygen are converted to carbon dioxide by the electrochemical cell, the carbon dioxide is added to the CO/CO 2 stream, and
the CO/CO 2 produced by the discharging is stored in the CO/CO 2 tank.

19 . The method of claim 18 , further comprising determining the state of charge of the carbon-oxygen battery system using the fuel gauge, which senses the pressure drop across the Boudouard reactor.

20 . The method of claim 19 , wherein the determining is during the discharging of the battery system, during the charging of the battery system, or a combination thereof.

21 . The method of claim 19 , wherein the determining comprises determining the pressure drop between the inlet and the outlet of the Boudouard reactor.

22 . The method of claim 19 , further comprising accumulating the carbon dioxide in the CO/CO 2 tank.

23 . The method of claim 18 , wherein the CO/CO 2 stream comprises CO, CO 2 , N 2 , He, Ar, or a combination thereof.

24 . A method of operating a carbon-oxygen battery system, the method comprising:
providing the carbon-oxygen battery system of claim 1 ; and wherein the electrochemical cell is a plurality of electrochemical cells, wherein at least one electrochemical cell of the plurality is a removable electrochemical cell, and further comprising installing the removable electrochemical cell to operate the system.

25 . The method of claim 24 , wherein the installing occurs while charging or discharging at least one electrochemical cell of the plurality of electrochemical cells.

26 . A method of operating a carbon-oxygen battery system, the method comprising:
providing the carbon-oxygen battery system of claim 13 ; and isolating the removable electrochemical cell, wherein the isolating comprises closing a first valve at a position downstream of the CO/CO 2 tank and upstream of the removable electrochemical cell, closing a second valve at a position downstream of the Boudouard reactor, and disconnecting the removable electrochemica

Assignees

• Form Energy Inc

Inventors

• Woodford William Henry
• Grandahl Tyler
• Moon Hwan

Classifications

• H01M8/04089

  of gaseous reactants · CPC title

• H01M8/0631 Primary

  Reactor construction specially adapted for combination reactor/fuel cell (hydrogen C01B3/00; reactors for physicochemical processes B01J19/00) · CPC title

• H01M8/0668

  Removal of carbon monoxide or carbon dioxide · CPC title

• H01M8/04067

  Heat exchange or temperature measuring elements, thermal insulation, e.g. heat pipes, heat pumps, fins · CPC title

• H01M8/04753

  of fuel cell reactants · CPC title