Electrochemical cell, and particularly a cell with electrodeposited fuel
View Patent ↗The present invention relates to an electrochemical cell for generating electrical power that includes an anode, a cathode, a charging electrode and an ionically conductive medium containing at least metal fuel ions and poly(ethylene glycol)tetrahydrofurfuryl. The present invention also relates to a method for charging the cell by electrodeposition of metal fuel on the anode thereof.
1. A method for operating an electrochemical cell, wherein the cell comprises:
a first electrode for oxidizing a metal fuel during discharging and reducing reducible ions of the metal fuel during recharging;
a second electrode spaced apart from the first electrode for at least reducing an oxidizer during discharging;
a charging electrode for oxidizing oxidizable ions of the oxidizer during recharging;
an ionically conductive medium communicating the electrodes, the ionically conductive medium comprising the reducible metal fuel ions and an additive comprising poly(ethylene glycol)tetrahydrofurfuryl,
wherein the method comprises recharging the electrochemical cell by:
i. applying an electrical current between the charging electrode and the first electrode with the charging electrode functioning as an anode and the first electrode functioning as a cathode, such that the reducible metal fuel ions are reduced and electrodeposited as the metal fuel in oxidizable form on the first electrode; and
ii. removing the electrical current to discontinue the charging.
2. A method according to claim 1 , further comprising generating electrical current using the electrochemical cell by oxidizing the metal fuel at the first electrode functioning as an anode and reducing the oxidizer at the second electrode functioning as a cathode whereby electrons are generated for conduction from the first electrode to the second electrode via a load, and the oxidized metal fuel ions and reduced oxidizer ions react to form a by-product.
3. A method according to claim 1 , wherein the charging electrode is selected from the group consisting of (a) the second electrode, (b) a third electrode spaced from both the first and second electrodes, and (c) one or more bodies of the first electrode wherein the first electrode comprises a plurality of spaced apart permeable bodies for receiving the metal fuel.
4. A method according to claim 2 , wherein the ionically conductive medium is an aqueous electrolyte solution.
5. A method according to claim 4 , wherein the aqueous electrolyte solution is alkaline.
6. A method according to claim 5 , wherein the aqueous electrolyte solution comprises potassium hydroxide.
7. A method according to claim 1 , wherein the poly(ethylene glycol)tetrahydrofurfuryl is in a concentration of 0.5 mL/L to 4.0 mL/L.
8. A method according to claim 4 , wherein the poly(ethylene glycol)tetrahydrofurfuryl is in a concentration of 0.5 mL/L to 4.0 mL/L.
9. A method according to claim 5 , wherein the poly(ethylene glycol)tetrahydrofurfuryl is in a concentration of 0.5 mL/L to 4.0 mL/L.
10. A method according to claim 6 , wherein the poly(ethylene glycol)tetrahydrofurfuryl is in a concentration of 0.5 mL/L to 4.0 mL/L.
11. A method according to claim 1 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
12. A method according to claim 4 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
13. A method according to claim 5 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
14. A method according to claim 6 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
15. A method according to claim 7 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
16. A method according to claim 8 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
17. A method according to claim 9 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
18. A method according to claim 10 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
19. A method according to claim 1 , wherein at least the recharging is performed between about 20° C. and 60° C.
20. A method according to claim 1 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
21. A method according to claim 5 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
22. A method according to claim 7 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
23. A method according to claim 9 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
24. A method according to claim 11 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
25. A method according to claim 13 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
26. A method according to claim 15 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
27. A method according to claim 17 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
28. A method according to claim 1 , wherein the first electrode comprises a series of permeable bodies arranged in spaced apart relation;
wherein during charging the electrochemical cell:
the electrochemical current is applied between the charging electrode and at least one of the permeable electrode bodies with the charging electrode functioning as the anode and the at least one permeable electrode body functioning as the cathode, such that the reducible metal fuel ions are reduced and electrodeposited as metal fuel in oxidizable form on the at least one permeable electrode body;
said electrodeposition causing growth among the permeable electrode bodies such that the electrodeposited metal fuel establishes an electrical connection between the permeable electrode bodies.
29. A method according to claim 1 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharging.
30. A method according to claim 2 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharging.
31. A method according to claim 3 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharging.
32. A method according to claim 4 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharging.
33. A method according to claim 5 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharging.
34. A method according to claim 6 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharging.
35. An electrochemical cell comprising:
a first electrode for oxidizing a metal fuel during discharging and reducing reducible ions of the metal fuel during recharging;
a second electrode spaced apart from the first electrode for at least reducing an oxidizer during discharging;
a charging electrode for oxidizing oxidizable ions of the oxidizer during recharging;
an ionically conductive medium communicating the electrodes, the ionically conductive medium comprising reducible metal fuel ions and an additive comprising poly(ethylene glycol)tetrahydrofurfuryl.
36. An electrochemical cell according to claim 35 , wherein the charging electrode is selected from the group consisting of (a) the second electrode, (b) a third electrode spaced apart from the first and second electrodes, and (c) one or more bodies of the first electrode wherein the first electrode comprises a plurality of spaced apart permeable bodies for receiving the metal fuel.
37. An electrochemical cell according to claim 36 , wherein the ionically conductive medium is an aqueous electrolyte solution.
38. An electrochemical cell according to claim 37 , wherein the aqueous electrolyte solution is alkaline.
39. An electrochemical cell according to claim 38 , wherein the aqueous electrolyte solution comprises potassium hydroxide.
40. An electrochemical cell according to claim 36 , wherein the poly(ethylene glycol)tetrahydrofurfuryl is in a concentration of 0.5 mL/L to 4.0 mL/L.
41. An electrochemical cell according to claim 37 , wherein the poly(ethylene glycol)tetrahydrofurfuryl is in a concentration of 0.5 mL/L to 4.0 mL/L.
42. An electrochemical cell according to claim 38 , wherein the poly(ethylene glycol)tetrahydrofurfuryl is in a concentration of 0.5 mL/L to 4.0 mL/L.
43. An electrochemical cell according to claim 39 , wherein the poly(ethylene glycol)tetrahydrofurfuryl is in a concentration of 0.5 mL/L to 4.0 mL/L.
44. An electrochemical cell according to claim 36 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
45. An electrochemical cell according to claim 37 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
46. An electrochemical cell according to claim 38 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
47. An electrochemical cell according to claim 39 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
48. An electrochemical cell according to claim 40 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
49. An electrochemical cell according to claim 41 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
50. An electrochemical cell according to claim 42 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
51. An electrochemical cell according to claim 43 , wherein the poly(ethylene glycol)tetrahydrofurfuryl has 2-5 ethylene oxide units.
52. An electrochemical cell according to claim 36 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
53. An electrochemical cell according to claim 38 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
54. An electrochemical cell according to claim 40 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
55. An electrochemical cell according to claim 42 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
56. An electrochemical cell according to claim 44 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
57. An electrochemical cell according to claim 46 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
58. An electrochemical cell according to claim 48 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
59. An electrochemical cell according to claim 50 , wherein the metal fuel is zinc and the reducible metal fuel ions are reducible zinc ions.
60. An electrochemical cell according to claim 35 , wherein the first electrode comprises a series of permeable electrode bodies arranged in spaced apart relation,
wherein the spaced apart relation of the permeable electrode bodies enables the electrical current to be applied between the charging electrode and at least one of the permeable electrode bodies with the charging electrode functioning as the anode and the at least permeable electrode body functioning as the cathode, such that the reducible fuel ions are reduced and electrodeposited as fuel in oxidizable from on the at least one permeable electrode body, whereby the electrodeposition causes growth of the fuel among the permeable electrode bodies such that the electrodeposited fuel establishes an electrical connection between the permeable electrode bodies.
61. An electrochemical cell according to claim 35 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharge.
62. An electrochemical cell according to claim 36 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharge.
63. An electrochemical cell according to claim 37 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharge.
64. An electrochemical cell according to claim 38 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharge.
65. An electrochemical cell according to claim 39 , wherein the second electrode is an air electrode for absorbing and reducing oxygen during discharge.