Granted Patent B2

US 12,509,785 · App. 17/652,255 · Granted Dec 30, 2025

Inventors: Shuai Zhao (Santa Clara, CA); Sichao Ma (Dublin, CA); Edward Izett (Berkeley, CA); Timothy A. Bekkedahl (Fremont, CA); Kendra P. Kuhl (Oakland, CA)

Assignee: Twelve Benefit Corporation

C25B15/02C25B3/26C25B9/19C25B13/08

Abstract

Claims (19)

1 . A method of operating an electrolyzer for carbon oxide reduction, the method comprising:

performing normal operation at the electrolyzer, wherein normal operation comprises inletting a reactant gas comprising a carbon oxide to a cathode of the electrolyzer and applying an electrical current to the electrolyzer at a first current density, to thereby produce an operating electrical potential between the cathode and an anode of the electrolyzer and reduce the carbon oxide and produce a carbon-containing reduction product;

performing a scheduled recovery process comprising: (i) transitioning the electrolyzer to a state in which there is an open circuit voltage between the cathode and the anode of the electrolyzer, and (ii) while the electrolyzer maintains the open circuit voltage, flowing a recovery gas to the cathode; and

resuming normal operation at the electrolyzer, wherein resuming normal operation comprises returning to the operating electrical potential.

2 . The method of claim 1 , wherein normal operation comprises flowing the reactant gas to the cathode at first flow rate and at a first pressure.

3 . The method of claim 1 , wherein the carbon oxide is CO 2 and/or CO and the carbon-containing reduction product comprises CO, a hydrocarbon, or an organic oxygen-containing compound.

4 . The method of claim 1 , wherein normal operation comprises periodically pausing and/or pulsing the electrical current to the electrolyzer.

5 . The method of claim 1 , wherein performing normal operation at the electrolyzer comprises performing normal operation for a period of at least about 100 hours.

6 . The method of claim 1 , further comprising, after resuming normal operation at the electrolyzer, continuing to perform normal operation at the electrolyzer for at least about 100 hours before again performing the scheduled recovery process or terminating operation of the electrolyzer.

7 . The method of claim 1 , wherein the recovery gas has a different composition than the reactant gas.

8 . The method of claim 1 , further comprising determining that an event that is likely to harm performance of the electrolyzer is occurring or is likely to occur, and performing a protection process.

9 . The method of claim 1 , wherein normal operation comprises stopping or modifying flow of the recovery gas to the cathode.

10 . The method of claim 1 , wherein the recovery gas is the reactant gas.

11 . The method of claim 10 , wherein the recovery process comprises maintaining the reactant gas flow to the cathode while open circuit voltage is maintained.

12 . The method of claim 1 , wherein normal operation comprises a pulsed voltage profile.

13 . The method of claim 1 , wherein performing normal operation at the electrolyzer comprises performing normal operation for a period of at least about 500 hours.

14 . The method of claim 1 , further comprising, after resuming normal operation at the electrolyzer, continuing to perform normal operation at the electrolyzer for at least about 500 hours before again performing a scheduled recovery process or terminating operation of the electrolyzer.

15 . The method of claim 1 , wherein performing normal operation at the electrolyzer comprises performing normal operation for a period of at least about 1000 hours.

16 . The method of claim 1 , further comprising, after resuming normal operation at the electrolyzer, continuing to perform normal operation at the electrolyzer for at least about 2000 hours before again performing the scheduled recovery process or terminating operation of the electrolyzer.

Assignments (3)

Continuity (2)

References Cited (139)