FUEL CELLS

• US 20110027671A1
• Filed: 01/23/2009
• Published: 02/03/2011
• Est. Priority Date: 01/23/2008
• Status: Abandoned Application

• Current Assignee: ACAL Energy Ltd
• Original Assignee: ACAL Energy Ltd
• Inventors: Rochester, David, Knuckey, Kathryn
• Application Number:
  US12/864,498
• Publication Number:
  US 20110027671A1
• Time in Patent Office: Days
• US Class Current: 429/417
• CPC Class Codes: H01M 4/36 Selection of substances as active materials, active masses, active liquids
• CPC Class Codes: H01M 8/1016 characterised by the electrolyte material H01M8/12 takes precedence
• CPC Class Codes: H01M 8/188 by recharging of redox couples containing fluids; Redox flow type batteries
• CPC Class Codes: H01M 8/20 Indirect fuel cells, e.g. fuel cells with redox couple being irreversible H01M8/18 takes precedence
• CPC Class Codes: Y02E 60/10 Energy storage using batteries
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

A redox fuel cell comprising an anode and a cathode separated by an ion selective polymer electrolyte membrane; means for supplying a fuel to the anode region of the cell; means for supplying an oxidant to the cathode region of the cell; means for providing an electrical circuit between the anode and the cathode; a catholyte solution comprising a modified ferrocene species comprising at least one bridging unit between the cyclopentadienyl rings, the modified ferrocene species being at least partially reduced at the cathode in operation of the cell, and at least partially re-generated by reaction with the oxidant after such reduction at the cathode.

Claims

1. A redox fuel cell comprising:

an anode region comprising an anode and a cathode region comprising a cathode, said regions being separated by an ion selective polymer electrolyte membrane;

a fuel passage through which fuel is supplied to the anode region of the cell;

an oxidant inlet that supplies an oxidant to the cathode region of the cell;

an electrical circuit between the anode and the cathode;

a catholyte solution comprising at least one non-volatile catholyte component flowing in fluid communication with the cathode, the catholyte solution comprising a modified ferrocene species comprising at least one bridging unit between the cyclopentadienyl rings, the modified ferrocene species being at least partially reduced at the cathode in operation of the cell, and at least partially regenerated by reaction with the oxidant after such reduction at the cathode by direct reaction with the oxidant or by indirect reaction therewith using a redox catalyst catalysing the regeneration of the ferrocene mediator.

2. A redox fuel cell according to claim 1 wherein the modified ferrocene species is represented by the formula

3. A redox fuel cell according to claim 2 wherein the divalent heteroannular bridging group is selected from optionally substituted straight or branched chain C₁-C₂₀ alkylidene, C₂-C₂₀ alkenylidene, C₃-C₂₀ cycloalkylidene, C₆-C₂₀ arylidene, C₇-C₂₀ alkylarylidene, or a C₇-C₂₀ arylalkylidene radicals, and one or more heteroatoms.

4. A redox fuel cell according to claim 3 wherein each heteroatom present is selected from oxygen, nitrogen, phosphorus and sulphur.

5. A redox fuel cell according to claim 2 wherein A, B¹-B⁶ and C are independently selected from carbon, sulphur, oxygen, nitrogen and phosphorus and from functional groups comprising one or more of those atoms.

6. A redox fuel cell according to claim 2 wherein the number of bridging units (A-(B)_n-C) between the cyclopentadienyl rings is from 1 to 5 and the bridging units may be the same or different.

7. A redox fuel cell according to claim 2 wherein n is from 1 to 3.

8. A redox fuel cell according to claim 7 wherein n is from 1.

9. A redox fuel cell according to claim 2 wherein the or each bridging unit A-(B)_n-C may be the same or different, and -A-, -B¹-, -B²-, -B³-, -B⁴-, -B⁵-, -B⁶- and -C- are preferably independently selected from compatible combinations of substituted and unsubstituted, branched- and straight-chain —

(CH₂)—

, —

CH(alkyl)-, —

C(alkyl)₂-, —

CH(alkenyl)-, —

C(alkenyl)₂-, —

CH(alkynyl)-, —

C(alkynyl)₂-, —

CH(aryl)-, —

CH(heteroaryl)-, —

O—

, —

S—

, —

(NH)—

, —

N(alkyl)-, —

CH(OH)—

, —

CH(O-alkyl)-, —

C—

O—

C(═

O)—

or —

O—

C(═

O)—

OR—

C(═

O)—

O—

.

10. A redox fuel cell according to claim 2 wherein the ferrocene bridging units A, B, and C, may carry further substituent groups which are independently selected from hydrogen and from functional groups comprising halogen, hydroxy, amino, protonated amino, imino, nitro, cyano, acyl, acyloxy, sulphate, sulphonyl, sulphinyl, alkylamino, protonated alkylamino, quaternary alkylammonium, carboxy, carboxylic acid, ester, ether, amido, sulphonate, sulphonic acid, sulphonamide, phosphonic acid, phosphonate, phosphate, alkylsulphonyl, arylsulphonyl, alkoxycarbonyl, alkylsulphinyl, alkylthio, arylthio, alkyl, alkoxy, oxyester, oxyamido, aryl, arylamino, aryloxy, heterocycloalkyl, heteroaryl, (C2-C5)alkenyl, (C2-C5)alkynyl, azido, phenylsulphonyloxy o amino acid conjugates having the formula —

CO—

W—

OH, where W is an amino acid-, and from alkyl, alkenyl, aryl, cycloalkyl, alkaryl, alkenaryl, aralkyl, aralkenyl groups substituted with one or more of the aforesaid functional groups.

11. A redox fuel cell according to claim 2 wherein each bridging unit is at least one of branched and extended at any bridging atom on any bridge by any suitable number of one of more of spacer and functional groups.

12. A redox fuel cell according to claim 11 wherein each spacer group is independently selected from straight or branched chain, substituted or unsubstituted alkyl, alkenyl, aryl, heteroaryl, cycloalkyl, alkaryl, alkenaryl, acetylene, and suitable combinations of the aforesaid units.

13. A redox fuel cell according to claim 2 wherein at least one ferrocene site without a bridging substituent is independently substituted with hydrogen or with functional groups comprising halogen, hydroxy, amino, imino, nitro, cyano, acyl, acyloxy, sulphate, sulphonyl, sulphinyl, alkylamino, carboxy, carboxylic acid, ester, ether, amido, sulphonate, sulphonic acid, sulphonamide, phosphonic acid, phosphonate, phosphonic acid, phosphate, alkylsulphonyl, arylsulphonyl, alkoxycarbonyl, alkylsulphinyl, arylsulphinyl, alkylthio, arylthio, alkyl, alkoxy, oxyester, oxyamido, aryl, arylamino, aryloxy, heterocycloalkyl, heteroaryl, (C₂-C₅)alkenyl, (C₂-C₅)alkynyl, azido phenylsulphonyloxy or amino acid conjugates having the formula —

CO—

W—

OH, where W is an amino acid, and from alkyl, alkenyl, aryl, cycloalkyl, alkaryl alkenaryl, aralkyl, aralkenyl groups substituted with one or more of the aforesaid functional groups.

14. A redox fuel cell according to claim 1 wherein the modified ferrocene species is selected from:

15. A redox fuel cell according to claim 1 wherein the ion selective polymer electrode membrane is at least one of cation and proton selective.

16. A redox fuel cell according to claim 1 wherein the catholyte is acidic.

17. A redox fuel cell according to claim 16 wherein the modified ferrocene species is non-ionic or anionic in its oxidised form.

18. A redox fuel cell according to claim 17 wherein the modified ferrocene species is anionic in its oxidised form.

19. A redox fuel cell according to claim 1 wherein the ion selective polymer electrode membrane is anion selective.

20. A redox fuel cell according to claim 19 wherein the catholyte is alkali.

21. A redox fuel cell according to claim 20 wherein the modified ferrocene species is non-ionic or cationic in its reduced form.

22. A redox fuel cell according to claim 1 wherein the ion selective polymer electrode membrane is a bi-membrane.

23. A redox fuel cell according to claim 1 wherein the modified ferrocene species is present in the catholyte at a concentration of at least 0.0001M.

24. A redox fuel cell according to claim 1 wherein the modified ferrocene species is present in the catholyte at a concentration of at least 0.005M.

25. A redox fuel cell according to claim 1 wherein the modified ferrocene species is present in the catholyte at a concentration of at least 0.001M.

26. A redox fuel cell according to claim 1 wherein the catholyte additionally comprises a catalyst redox species.

27. A redox fuel cell according to claim 26 wherein the catalyst redox species is selected from ligated transition metal complexes, polyoxometallate species, and combinations thereof.

28. A redox fuel cell according to claim 27 wherein the transition metal(s) in the transition metal complexes are selected from manganese (II-V), iron (I-IV), copper (I-III), cobalt (I-III), nickel (I-III), chromium (II-VII), titanium (II-IV), tungsten (IV-VI), vanadium (II-V) and molybdenum (II-VI).

29. A redox fuel cell according to claim 26 wherein the catalyst redox species comprises a multidentate N-donor ligand.

30. A redox fuel cell according to claim 29 wherein the N-donor ligand comprises one or more pyridine substituents.

31. A redox fuel cell according to claim 30 wherein the catalyst redox species is an iron complex of N4Py, pydien, trilen or derivatives thereof.

32. A catholyte solution for use in a redox fuel cell according to claim 1.