Electrochemical cell system

Patent metadata

Field	Value
Publication number	US-12080926-B2
Application number	US-202117444279-A
Country	US
Kind code	B2
Filing date	Aug 2, 2021
Priority date	Nov 6, 2018
Publication date	Sep 3, 2024
Grant date	Sep 3, 2024

Abstract

An electrochemical cell system and a method of controlling water imbalance is provided. The electrochemical cell system and the method both include determining a present water imbalance in the electrochemical cell by summing a waterin and a watercreated less a waterout; tracking a cumulative water imbalance during operation of the electrochemical cell by repeatedly determining the present water imbalance and continuing to sum the results during operation; and adjusting a flow rate of the oxidant feed gas entering the electrochemical cell based on the cumulative water imbalance.

First claim

What is claimed is:

1. An electrochemical cell system, comprising:
an electrochemical cell;
a plurality of oxidant gas inlet sensors, an oxidant gas exhaust sensor, a coolant inlet sensor, a coolant exhaust sensor, and current transducer;
a controller configured to:
determine a present water imbalance in the electrochemical cell by summing a water in and a water created less a water out , wherein:
water in is an amount of water introduced into the electrochemical cell by an oxidant feed gas;
water created is an amount of water created by the electrochemical cell from the electrochemical reaction; and
water out is an amount of water discharged from the electrochemical cell by an oxidant exhaust gas;

track a cumulative water imbalance during operation of the electrochemical cell by repeatedly determining the present water imbalance and continuing to sum the results during operation;
adjust a flow rate of the oxidant feed gas entering the electrochemical cell based on the cumulative water imbalance; and

wherein the controller is configured to recalibrate the cumulative water imbalance to zero by:
increasing the flow rate of the oxidant feed gas to the electrochemical cell temporarily in order to dry out the electrochemical cell;
measuring a resistance of the electrochemical cell;
stopping flow of the oxidant feed gas once the resistance measured is about equal to a target resistance that corresponds to the cumulative water imbalance being equal to zero; and
resetting the cumulative water imbalance to zero when the resistance measured is about equal to the target resistance.

2. The electrochemical cell system of claim 1 , wherein the controller is configured to use a PID loop to adjust the flow rate of the oxidant feed gas; and
wherein the controller is configured to adjust the flow rate of the oxidant feed gas when the cumulative water imbalance deviates from zero in order to bring the cumulative water imbalance to zero.

3. The electrochemical cell system of claim 1 , wherein the controller is configured to adjust the flow rate of the oxidant gas when the cumulative water balance deviates from zero beyond a set threshold;
wherein the controller is configured to repeat the determination of the present water imbalance at least every 30 seconds; and
wherein the controller is configured to adjust the flow rate of the oxidant feed gas repeatedly at a frequency of at least 1 Hz.

4. The electrochemical cell of claim 1 , further comprising a coolant pump configured to supply a coolant to the electrochemical cell at a generally fixed inlet coolant temperature and to operate at a generally fixed speed.

5. The electrochemical cell of claim 1 , wherein the resistance is measured using a current-interrupt method;
wherein the target resistance is determined during initial startup testing of the electrochemical cell; and
wherein the target resistance is between about 50 to about 100 mΩ-cm 2 .

6. The electrochemical cell of claim 1 , wherein the controller is configured to recalibrate the cumulative water imbalance at least once per day during a shutdown sequence for the electrochemical cell.

7. The electrochemical cell of claim 1 ,
wherein the controller is configured to determine water in based on a humidity of the oxidant feed gas, a pressure of the oxidant feed gas, and the flow rate of the oxidant feed gas;
wherein the controller is configured to determine water created based a current generated by the electrochemical cell and anode stoichiometric ratio; and
wherein the controller is configured to determine water out based on a humidity of an oxidant exhausted gas and a pressure of the oxidant exhausted gas.

8. The electrochemical cell of claim 1 , wherein the increase in the flow rate is determined based on at least one of the cumulative water imbalance at time of shutdown and a predetermined shutdown time.

9. The electrochemical cell of claim 1 , further comprising a second increase in the flow rate of the oxidant feed gas if the cumulative water imbalance is not reset to zero within a predetermined shutdown time.

10. An electrochemical cell system, comprising:
an electrochemical cell;
a plurality of oxidant gas inlet sensors, an oxidant gas exhaust sensor, a coolant inlet sensor, a coolant exhaust sensor, and current transducer;
a controller configured to:
determine a present water imbalance in the electrochemical cell by summing a water in and a water created less a water out , wherein:
water in is an amount of water introduced into the electrochemical cell by an oxidant feed gas;
water created is an amount of water created by the electrochemical cell from the electrochemical reaction; and
water out is an amount of water discharged from the electrochemical cell by an oxidant exhaust gas;

track a cumulative water imbalance during operation of the electrochemical cell by repeatedly determining the present water imbalance and continuing to sum the results during operation;
adjust a flow rate of the oxidant feed gas entering the electrochemical cell based on the cumulative water imbalance; and

wherein the controller is configured to recalibrate the cumulative water imbalance to zero by:
increasing the flow rate of the oxidant feed gas to the electrochemical cell temporarily in order to dry out the electrochemical cell;
measuring a humidity of the oxidant exhaust gas;
stopping flow of the oxidant feed gas once the humidity of the oxidant exhaust gas is below a target humidity that corresponds to a cumulative water imbalance of zero; and
resetting the cumulative water imbalance to zero.

11. The electrochemical cell system of claim 10 , wherein the controller is configured to use a PID loop to adjust the flow rate of the oxidant feed gas; and
wherein the controller is configured to adjust the flow rate of the oxidant feed gas when the cumulative water imbalance deviates from zero in order to bring the cumulative water imbalance to zero.

12. The electrochemical cell system of claim 10 , wherein the controller is configured to adjust the flow rate of the oxidant gas when the cumulative water balance deviates from zero beyond a set threshold;
wherein the controller is configured to repeat the determination of the present water imbalance at least every 30 seconds; and
wherein the controller is configured to adjust the flow rate of the oxidant feed gas repeatedly at a frequency of at least 1 Hz.

13. The electrochemical cell of claim 10 , further comprising a coolant pump configured to supply a coolant to the electrochemical cell at a generally fixed inlet coolant temperature and to operate at a generally fixed speed.

14. The electrochemical cell of claim 10 , wherein the resistance is measured using a current-interrupt method;
wherein the target resistance is determined during initial startup testing of the electrochemical cell; and
wherein the target resistance is between about 50 to about 100 mΩ-cm 2 .

15. The electrochemical cell of claim 10 , wherein the controller is configured to recalibrate the cumulative water imbalance at least once per day during a shutdown sequence for the electrochemical cell.

16. The electrochemical cell of claim 10 ,
wherein the controller is configured to determine water in based on a humidity of the oxidant feed gas, a pressure of the oxidant feed gas, and the flow rate of the oxidant feed gas;
wherein the controller is configured to determine water created based a current generated by the electrochemical cell and anode stoichiometric ratio; and
wherein the controller is configured to determine water o

Assignees

• Nuvera Fuel Cells Llc

Inventors

• Blanchet Scott

Classifications

• H01M8/04514

  of anode exhausts · CPC title

• H01M8/04843

  of fuel cell exhausts · CPC title

• H01M8/04753

  of fuel cell reactants · CPC title

• H01M8/04723

  of the coolant · CPC title

• H01M8/04402

  of anode exhausts · CPC title