Device Comprising a New Cathode and Method for Generating Electrical Energy with Use Thereof

• US 20100227203A1
• Filed: 02/13/2007
• Published: 09/09/2010
• Est. Priority Date: 02/14/2006
• Status: Abandoned Application

• Current Assignee: MAGNETO special anodes B.V. (Evoqua Water Technologies LLC)
• Original Assignee: MAGNETO special anodes B.V. (Evoqua Water Technologies LLC)
• Inventors: Ter Heijne, Annemiek, Hamelers, Hubertus Victor Marie, Buisman, Cees Jan Nico
• Application Number:
  US12/223,192
• Publication Number:
  US 20100227203A1
• Time in Patent Office: Days
• US Class Current: 429/2
• CPC Class Codes: H01M 8/16 Biochemical fuel cells, i.e. cells in which microorganisms function as catalysts
• CPC Class Codes: H01M 8/18 Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

A first embodiment is disclosed, relating to a device including an anode and a cathode. The anode and cathode are placed in a separate anode and cathode compartment. In at least one embodiment of the device, electron transfer takes place from the cathode to a terminal electron acceptor via a redox mediator. In at least one embodiment, the redox mediator includes the Fe (II)/Fe (III) redox couple. According to a further aspect, of at least one embodiment of the invention, relates to a method for generating electric energy with use of the device according to at least one embodiment of the invention.

Claims

1. Device comprising:

a number of anode compartments provided with an anode, placed in an anode fluidum comprising reagents for an oxidation reaction;

a number of cathode compartments separated from the anode compartments, provided with a cathode, placed in a cathode fluidum comprising a terminal electron acceptor, a redox mediator, suitable for transferring electrons from the cathode to the terminal electron acceptor, and a catalyst, catalyzing the electron transfer from the redox mediator to the terminal electron acceptor;

the redox mediator comprising the Pe (II)/Fe (III) redox couple and the catalyst comprising Fe(II) oxidizing catalyst.

2. Device according to claim 1, wherein Fe(II) and Fe(III) are substantially present in the cathode fluidum in soluble form.

3. Device according to claim 1, wherein the cathode fluidum has a pH value of 0-5.

4. Device according to claim 1, wherein the concentration Fe(III) ions and Fe(II) ions in soluble form is within the range of 0.05-0.2 M.

5. Device according to claim 1, wherein the terminal electron acceptor is oxygen.

6. Device according to claim 1, wherein the Fe(II) oxidizing catalyst comprises a Fe(II) oxidizing biocatalyst or a microorganism from the genus solfolobus or the genus chlorobium.

7. Device according to claim 1, wherein the cathode fluidum comprises reagents for the catalysis of the Fe(I) oxidizing catalyst.

8. Device according to claim 1, wherein the cathode compartment and anode compartment are separated by a number of ion selective membranes.

9. Device according to claim 8, wherein the number of ion selective membranes comprise an anion exchange membrane.

10. Device according to claim 8, wherein the number of ion selective membranes comprise an anion exchange membrane on the side of the anode compartment.

11. Device according to claim 8, wherein the cathode compartment is separated in an iron reduction compartment, wherein Fe(III) is reduced at the cathode and an iron oxidation compartment, wherein Fe(II) is oxidized under supply of a terminal electron acceptor, and further comprising means for transferring the cathode fluidum at least partially from the iron reduction compartment to the iron oxidation compartment and visa versa.

12. Device according to claim 11, further comprising a terminal electron acceptor removing compartment, including means for removing the terminal electron acceptor, and wherein the means for transferring the cathode fluidum at least partially from the iron oxidation compartment to the iron reduction compartment are suitable to transfer the cathode fluidum at least partially from the iron oxidation compartment to the terminal electron acceptor removing compartment, and to transfer it from there at least partially to the iron reduction compartment.

13. Device according to claim 12, wherein the means for removing the terminal electron acceptor comprise a reductor for the terminal electron acceptor.

14. Device according to claims 12, further comprising means for transferring the cathode fluidum at least partially from the iron reduction compartment to the terminal electron acceptor removing compartment.

20. Device according to claim 1, wherein the number of anode compartments provided with an anode are placed in an anode fluidum comprising reagents for an anaerobic oxidation reaction.

21. Device according to claim 20, wherein the number of anode compartments provided with an anode are placed in an anode fluidum comprising reagents for an anaerobic biological oxidation reaction.

22. Device according to claim 1, wherein the cathode compartments and anode compartments are separated by a number of ion selective membranes, and wherein the number of ion selective membranes comprise an anion exchange membrane.

23. Device according to claim 3, wherein the cathode fluidum has a pH value of 0-3.

24. Device according to claim 23, wherein the cathode fluidum has a pH value of 2-3.

25. Device according to claim 4, wherein the concentration Fe(III) ions and Fe(II) ions in soluble form is within the range of 0.01-0.1 M.

26. Device according to claim 24, wherein the concentration Fe(III) ions and Fe(II) ions in soluble form is within the range of 0.05-0.1 M.

27. Device according to claim 6, wherein the Fe(II) oxidizing biocatalyst is a Fe(II) oxidizing organism.

28. Device according to claim 27, wherein the Fe(II) oxidizing organism is a Fe(II) oxidizing microorganism.

29. Device according to claim 28, wherein the Fe(II) oxidizing microorganism is selected from the group consisting of Acidithiobacillus ferrooxidans, Leptospirillum ferrooxidans or Gallionella ferruginea.

30. Device according to claim 7, wherein the reagents for the catalysis of the Fe(I) oxidizing catalyst include nutrients for a Fe(II) oxidizing organism.

15. Method for generating electric energy comprising:

providing a device including a number of anode compartments provided with an anode, placed in an anode fluidum comprising reagents for an oxidation reaction and a number of cathode compartments separated from the anode compartments, provided with a cathode, placed in a cathode fluidum comprising a terminal electron acceptor, a redox mediator, suitable for transferring electrons from the cathode to the terminal electron acceptor, and a catalyst, catalyzing the electron transfer from the redox mediator to the terminal electron acceptor;

the redox mediator comprising the Pe (II)/Fe (III) redox couple and the catalyst comprising Fe(II) oxidizing catalyst;

electrically connecting the anode and the cathode;

at least one of forming and maintaining anaerobic conditions in the anode compartment;

performing an anaerobic oxidation reaction; and

reducing Fe(III) to Fe(II) at the cathode and oxidizing Fe(II) while reducing a terminal electron acceptor.

16. Method according to claim 15, wherein one or more substances used are replenished sufficiently.

17. method according to claim 15, wherein the cathode compartment of the device is separated in an iron reduction compartment, wherein iron (III) is reduced at the cathode and an iron oxidation compartment, wherein Fe(II) is oxidized under supply of a terminal electron acceptor, and the cathode fluidum is transferred at least partially from the iron reduction compartment to the iron oxidation compartment, and from the iron oxidation compartment to the iron reduction compartment.

18. Method according to claim 17, wherein the device further comprises a terminal electron acceptor removing compartment including means for removing the terminal electron acceptor, and wherein the at least partial transfer of the cathode fluidum from the iron oxidation compartment to the iron reduction compartment takes place by at least partially transferring the cathode fluidum from the iron oxidation compartment to the terminal electron acceptor removing compartment, and from there transferring it at least partially to the iron reduction compartment.

19. Method according to claim 18, wherein part of the cathode fluidum is transferred from the iron reduction compartment to the terminal electron acceptor removing compartment.

31. Method according to claim 15, wherein the anaerobic oxidation reaction performed includes a biological oxidation reaction in the anode compartment.

32. Method according to claim 16, wherein the one or more substances used include at least one of reagents for the anaerobic oxidation reaction, the terminal electron acceptor and the optional nutrients for the Fe(II) oxidizing organism.