Hydrogen recycling apparatus and method of operation

1. A method of operating an electrochemical cell stack comprising:

setting a maximum voltage on a power supply;

feeding a reactant gas to the cell stack;

halting the flow of the reactant gas to at least one cell in the cell stack;

increasing the voltage applied to the at least one cell to the maximum voltage in response to the halting of the flow of reactant gas to the at least one cell; and

initiating the flow of reactant gas to the at least one cell in response to the voltage increasing above a threshold for a predetermined amount of time.

2. The method of claim 1 wherein the reactant gas includes a mixture of hydrogen and carbon monoxide.

3. The method of claim 2 wherein the cell stack includes an anode and a cathode, the reactant gas being supplied to the anode.

4. The method of claim 3 further comprising generating hydrogen gas at the cathode in response to feeding reactant gas to the cell stack.

5. The method of claim 4 further comprising generating carbon dioxide at the anode in response to feeding reactant gas to the cell stack.

6. The method of claim 1 wherein the cell stack includes a plurality of cells, the plurality of cells including a first cell and a second cell.

7. The method of claim 6 wherein:

the step of halting the flow of reactant includes halting the flow of reactant to the first cell; and

the step of increasing the voltage includes reversing the polarity of the first cell.

8. The method of claim 7 further comprising:

initiating the flow of reactant gas to the first cell;

halting the flow of the reactant gas to the second cell;

reversing the polarity of the second cell; and

initiating the flow of reactant gas to the second cell in response to the voltage being a predetermined voltage.

9. A system comprising:

a source of reactant gas including hydrogen and carbon monoxide;

a power supply having a maximum voltage setting;

an electrochemical cell electrically coupled to the power supply and having an anode and a cathode, the anode having a catalyst configured to convert during operation at least a first portion of the reactant gas to carbon dioxide, the cathode having a catalyst configured to convert during operation at least a second portion of the reactant gas to hydrogen gas; and

a controller operably coupled to the source of reactant gas, the controller configured to halt the flow of reactant gas to the electrochemical cell, increasing the voltage applied to the electrochemical cell to the maximum voltage setting in response to the halt of the flow of reactant gas, and reinitiating the flow of reactant gas in response to the voltage increasing above a threshold for a predetermined amount of time.

10. The system of claim 9 further comprising a phase separator fluidly coupled to the cathode.

11. The system of claim 10 wherein the source of reactant gas is a process furnace.

12. The system of claim 11 further comprising a vent fluidly coupled to the anode to receive a third portion of said reactant gas and the carbon dioxide.

13. The system of claim 12 further comprising a source of nitrogen gas fluidly coupled to the process furnace and a source of hydrogen gas fluidly coupled to the process furnace.

14. The system of claim 9 wherein the cell stack includes a plurality of cells, each of the plurality of cells having an anode and cathode, the plurality of cells including a first cell and a second cell.

15. The system of claim 14 wherein the controller is further responsive to halting the flow of reactant includes halting the flow of reactant to the first cell and increasing the voltage includes reversing the polarity of the first cell in response to halting the flow of reactant.