ELECTRODES AND METHODS FOR MICROBIAL FUEL CELLS

• US 20080292912A1
• Filed: 07/23/2008
• Published: 11/27/2008
• Est. Priority Date: 05/02/2006
• Status: Abandoned Application

• Current Assignee: Penn State Research Foundation (Pennsylvania State University)
• Original Assignee: Penn State Research Foundation (Pennsylvania State University)
• Inventors: Cheng, Shaoan, Logan, Bruce
• Application Number:
  US12/177,962
• Publication Number:
  US 20080292912A1
• Time in Patent Office: Days
• US Class Current: 429/2
• CPC Class Codes: C02F 3/005 Combined electrochemical biological processes aeration by electrolytically produced oxygen bubbles C02F3/202
• CPC Class Codes: H01M 4/8657 layered
• CPC Class Codes: H01M 4/8878 Treatment steps after deposition of the catalytic active composition or after shaping of the electrode being free-standing body
• CPC Class Codes: H01M 4/8882 Heat treatment, e.g. drying, baking
• CPC Class Codes: H01M 4/90 Selection of catalytic material
• CPC Class Codes: H01M 8/16 Biochemical fuel cells, i.e. cells in which microorganisms function as catalysts
• CPC Class Codes: Y02E 60/50 Fuel cells
• CPC Class Codes: Y02W 10/37 using solar energy

Abstract

Methods of improving a performance parameter of a microbial fuel cell are provided according to embodiments of the present invention which include heating an electrode and exposing the heated electrode to ammonia gas to produce a treated electrode characterized by an increased positive surface charge on the electrode surface. Improved performance parameters include increased maximum power density, increased coulombic efficiency, increased volumetric power density and decreased microbial fuel cell operation time to achieve maximum power density

Claims

1. A method of improving a performance parameter of a microbial fuel cell, comprising:

heating an electrode having an electrode surface to produce a heated electrode;

exposing the heated electrode to ammonia gas to produce a treated electrode characterized by an increased positive surface charge on the electrode surface;

connecting the treated electrode and a cathode to produce an electrode assembly wherein the treated electrode and the cathode are in electrical communication; and

disposing the electrode assembly at least partially in a reaction chamber, the reaction chamber containing a bioxidizable substrate for exoelectrogen microorganisms and a plurality of exoelectrogen microorganisms, thereby providing a microbial filet cell having an improved performance parameter compared to a microbial fuel cell without the treated electrode.

2. The method of claim 1 wherein the improved performance parameter is increased maximum power density.

3. The method of claim 1 wherein the improved performance parameter is increased coulombic efficiency.

4. The method of claim 1 wherein the improved performance parameter is increased volumetric power density.

5. The method of claim 1 wherein the improved performance parameter is decreased time to achieve maximum power density.

6. The method of claim 1 wherein the electrode is a carbon electrode.

7. The method of claim 6 wherein the carbon electrode comprises a carbon material selected from the group consisting of:

carbon cloth, carbon paper, carbon felt, carbon wool, carbon foam, graphite, porous graphite, graphite powder, graphite granules, graphite fiber, and reticulated vitreous carbon.

8. The method of claim 1 wherein the electrode is a graphite fiber brush electrode.

9. The method of claim 1 wherein the electrode has a specific surface area greater than 100 m²/m³.

10. The method of claim 1 wherein a separator or ion exchange membrane partitions the reaction chamber to form an anode compartment and a cathode compartment, wherein the treated electrode is an anode and is disposed in the anode compartment and the cathode is disposed in the cathode compartment.

11. The method of claim 1 wherein no separator or ion exchange membrane partitions the reaction chamber such that the reaction chamber is a single chamber reactor.

12. The method of claim 1, further comprising a power source disposed in electrical communication with the electrode assembly to enhance a potential between the treated electrode and the cathode, thereby generating hydrogen gas.

13. The method of claim 12, wherein the power source is selected from the group consisting of:

grid power, a solar power source, a wind power source, a DC power source, an electrochemical cell and a microbial fuel cell.

14. The method of claim 1 wherein the cathode is a tube cathode.

15. The method of claim 1, further comprising a second treated electrode.

16. The method of claim 1, further comprising a second cathode.

17. A microbial fuel cell, comprising:

an anode treated with ammonia gas, the anode characterized by increased positive surface charge compared to an untreated anode, the microbial fuel cell having an improved performance parameter compared to a microbial fuel cell without the treated electrode.

18. The microbial fuel cell of claim 17 wherein the improved performance parameter is increased maximum power density.

19. The microbial fuel cell of claim 17 wherein the improved performance parameter is increased coulombic efficiency.

20. The microbial fuel cell of claim 17 wherein the improved performance parameter is increased volumetric power density.

21. The microbial fuel cell of claim 17 wherein the improved performance parameter is decreased time to achieve maximum power density.

22. The microbial fuel cell of claim 17, further comprising a power source disposed in electrical communication with an electrode assembly including the anode and a cathode to enhance a potential between the anode and the cathode, thereby generating hydrogen gas.

23. The microbial fuel cell of claim 22, wherein the power source is selected from the group consisting of:

grid power, a solar power source, a wind power source, a DC power source, an electrochemical cell and a microbial fuel cell.

24. The microbial fuel cell of claim 17 wherein the microbial fuel cell comprises a reaction chamber, wherein a separator or ion exchange membrane partitions the reaction chamber to form an anode compartment and a cathode compartment, wherein the anode is disposed in the anode compartment and a cathode is disposed in the cathode compartment.

25. The microbial fuel cell of claim 17 wherein the microbial fuel cell comprises a reaction chamber and no separator or ion exchange membrane partitions the reaction chamber.

26. The microbial fuel cell of claim 17 wherein the anode is a carbon anode.

27. The microbial fuel cell of claim 26 wherein the carbon anode comprises a carbon material selected from the group consisting of:

carbon cloth, carbon paper, carbon felt, carbon wool, carbon foam, graphite, porous graphite, graphite powder, graphite granules, graphite fiber, and reticulated vitreous carbon.

28. The microbial fuel cell of claim 17 wherein the anode is a graphite fiber brush electrode.

29. The microbial fuel cell of claim 17 wherein the anode has a specific surface area greater than 100 m²/m³.

30. A method of increasing positive surface charge on an electrode surface, comprising:

heating an electrode to produce a heated electrode; and

exposing the heated electrode to ammonia gas, thereby producing an electrode having an increased positive surface charge on an electrode surface.

31. An electrode treated by the method of claim 30, the electrode characterized by an increased positive surface charge compared to an untreated electrode.