Methods of removing contaminants from a fuel cell electrode

• US 7,858,250 B2
• Filed: 11/06/2009
• Issued: 12/28/2010
• Est. Priority Date: 02/06/2002
• Status: Active Grant

• Current Assignee: Battelle Memorial Institute
• Original Assignee: Battelle Memorial Institute
• Inventors: Hindin, Barry, Glenn, Bradley C., Markworth, Alan J., Markworth, legal representative, Saunders, James H.
• Primary Examiner(s): Cantelmo; Gregg
• Application Number:
  US12/613,637
• Publication Number:
  US 20100092816A1
• Time in Patent Office: 417 Days
• Field of Search: 429/13, 429/428, 429430-432
• US Class Current: 429/428
• CPC Class Codes: H01M 8/04238 Depolarisation
• CPC Class Codes: H01M 8/04559 of fuel cell stacks
• CPC Class Codes: H01M 8/04589 of fuel cell stacks
• CPC Class Codes: H01M 8/0488 of fuel cell stacks
• CPC Class Codes: H01M 8/04992 characterised by the implementation of mathematical or computational algorithms, e.g. feedback control loops, fuzzy logic, neural networks or artificial intelligence
• CPC Class Codes: H01M 8/0668 Removal of carbon monoxide or carbon dioxide
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

A method of optimizing a waveform of an electrical current applied to an electrode of an electrochemical device that consists of at least two electrodes separaged by an electrolyte that includes the steps of: applying an electrical current to an electrode of a device; determining a waveform of the voltage or the current of the electrical current; representing the waveform by a mathematical expression or numbers taking measurements of output voltage, current or power of the device associated with the application of the electrical current; and varying the shape and frequency of the waveform to optimize the output voltage, current or power of the device and thereby determine an optimized waveform of the electrical current to be applied to the electrode of the device.

Claims

1. A feedback control method of operating an electrochemical apparatus operated using a fuel containing an electrochemically active contaminant by applying voltage control to an electrode of the apparatus using the following algorithm the following steps:

a) determining a mathematical model that relates an instantaneous coverage of the electrode by fuel and contaminant to an overvoltage applied to the anode;

b) forming an observer that relates the instantaneous coverage of the fuel and contaminant to a single operating parameter of the apparatus;

c) forming an objective function that describes a performance parameter of the fuel cell for a discrete set of values related to the instantaneous coverage of the electrode by fuel and contaminant;

d) maximizing the objective function using optimal control techniques to maximize performance of the electrochemical apparatus by determining an optimal waveform of the single operating parameter over a specified period of time;

e) driving the contaminant coverage of the electrode to a low value by varying only the overvoltage to obtain the optimal waveform of the single operating parameter;

f) driving the fuel coverage of the electrode to a high value by varying only the overvoltage to obtain the optimal waveform of the single operating parameter; and

f) repeating steps a) through d) as necessary.

2. The feedback control method

according to claim 1 wherein step c) includes prescribing a desired trajectory of the instantaneous coverage of the electrode by fuel and contaminant as a function of time and

forming a set of mathematical relationships from steps a), b) and the desired trajectory that allows an apparatus current to be measured, the overvoltage to be prescribed for application to the electrode and instantaneous contaminant coverage of the electrode and instantaneous fuel coverage of the electrode to be predicted.

3. A feedback control method of operating a fuel cell by applying voltage control to an electrode of the fuel cell, the method comprising the following steps:

a) determining a mathematical model that relates an instantaneous coverage of the electrode by hydrogen and carbon monoxide to an overvoltage applied to the anode;

b) forming an observer that relates the instantaneous coverage of the electrode by hydrogen and carbon monoxide to a single measured operating parameter of the fuel cell;

c) forming an objective function that describes a performance parameter of the fuel cell for a discrete set of values related to the instantaneous coverage of the electrode by hydrogen and carbon monoxide;

d) maximizing the objective function using optimal control techniques to maximize performance of the fuel cell by determining an optimal waveform of the single operating parameter over a specified period of time;

e) driving the carbon monoxide coverage of the electrode to a low value by varying only the overvoltage to obtain the optimal waveform of the single operating parameter;

f) driving the hydrogen coverage of the electrode to a high value by varying only the overvoltage to obtain the optimal waveform of the single operating parameter; and

g) repeating steps a) through d) as necessary.

4. The feedback control method according to claim 3 wherein step c) includes

prescribing a desired trajectory of the instantaneous coverage of the hydrogen and carbon monoxide as a function of time and

forming a set of mathematical relationships from steps a), b) and the desired trajectory that allows fuel cell current to be measured, the overvoltage to be prescribed and instantaneous carbon monoxide coverage and instantaneous hydrogen coverage to be predicted.

5. The method according to claim 4 wherein:

in step e), the carbon monoxide coverage is driven to a low value by varying the overvoltage applied to the electrode using optimal control techniques; and

in step f), the hydrogen coverage is driven to a high value by varying the overvoltage applied to the electrode using optimal control techniques.

6. The feedback control method of claim 3 wherein the single operating parameter is fuel cell current.

7. The feedback control method of claim 3 wherein the single operating parameter is fuel cell voltage.

8. The feedback control method of claim 6 wherein the performance parameter is power delivered by the fuel cell.

9. The feedback control method of claim 6 wherein the performance parameter is an ability to follow a useful load connected to the fuel cell.

10. The feedback control method of claim 8 wherein the electrode is an anode of the fuel cell.

11. The feedback control method of claim 8 wherein the electrode is a cathode of the fuel cell.

12. The feedback control method of claim 6 wherein the optimal control techniques utilized in step d) include dynamic programming.