Temperature control apparatus and method for high energy electrochemical cells

• US 20050089750A1
• Filed: 12/19/2002
• Published: 04/28/2005
• Est. Priority Date: 02/19/2002
• Status: Abandoned Application

• Current Assignee: 3M Innovative Properties Company (3M Company)
• Original Assignee: 3M Innovative Properties Company (3M Company)
• Inventors: Gullicks, Scott D., Ng, Chin-Yee
• Application Number:
  US10/502,443
• Publication Number:
  US 20050089750A1
• Time in Patent Office: Days
• US Class Current: 429/120
• CPC Class Codes: F28D 7/08 the conduits being otherwise bent, e.g. in a serpentine or zig-zag F28D7/10 takes precedenceF28D7/0016 and F28D7/0033 take precedence
• CPC Class Codes: F28F 3/12 Elements constructed in the shape of a hollow panel, e.g. with channels F28D1/02, F28D1/03 take precedence
• CPC Class Codes: H01M 10/613 Cooling or keeping cold
• CPC Class Codes: H01M 10/625 Vehicles
• CPC Class Codes: H01M 10/647 Prismatic or flat cells, e.g. pouch cells
• CPC Class Codes: H01M 10/6557 arranged between the cells
• CPC Class Codes: H01M 10/6567 Liquids
• CPC Class Codes: H01M 50/112 Monobloc comprising multiple compartments
• CPC Class Codes: Y02E 60/10 Energy storage using batteries

Abstract

An apparatus and method provides cooling for electrochemical cells of an energy storage device. A number of electrochemical cells are arranged in a spaced apart relationship, each having opposing first and second planar surfaces and being subject to volumetric changes during charge and discharge cycling. A cooling bladder provides temperature control for the energy storage device. The cooling bladder is formed of a conformable thermally conducting material and includes inlet and outlet ports. The cooling bladder conforms to maintain contact with at least the first planar surface or the second planar surface of each cell during volumetric changes of the cells. A heat transfer medium passes between the inlet and outlet ports of the cooling bladder to control an operating temperature of the cells. The cooling bladder can be pressurized to maintain the cells of the energy storage device in a state of compression during charge and discharge cycling.

Claims

1. An electrochemical storage device, comprising:

a plurality of electrochemical cells arranged in a spaced apart relationship, each of he electrochemical cells comprising opposing first and second planar surfaces and subject to volumetric changes during charge amd discharge cycling; and

a cooling bladder formed of a conformable thermally conducting material and having an inlet port and an outlet port, the cooling bladder conformable to maintain contact with at least the first planar surface or the second planar surface of each of the electrochemical cells during the volumetric changes, a heat transfer medium passing between the inlet and outlet port to control au operating temperature of the electrochemical cells.

2. The device of claim 1, wherein the cooling bladder compprises a continuous hollowed interior within which the heat transfer medium passes.

3. The device of claim 1, wherein the cooling bladder comprises a plurality of flow channels within which the heat transfer medium passes.

4. The device of claim 1, wherein the cooling bladder covers substantially all of a surface area of each of the cells.

5. The device of claim 1, wherein the cooling bladder comprises a support arrangement that inhibits restriction of heat fer medium flow at cooling bladder bend locaions.

6. The device of claim 5, wherein the support arrangement is located on an outer surface of the cooling bladder at the cooling bladder bend locations.

7. The device of claim 5, wherein tbe support arrangement is located within the cooling bladder at the cooling bladder bend locations.

8. The device of claim 1, wherein the cooling bladder comprises a porous filler material disposed within tbe cooling bladder.

9. The device of claim 1. wherein the cooling bladder comprises a porous filler material disposed at cooling bladder locations subject to bending.

10. The device of claim 1, wherein the cooling bladder comprises thickened sections provided at cooling bladder locations subject to bending.

11. The device of claim 1, wherein the cooling bladder comprises an interior compartment within which the heat transfer medium passes between the inlet port and the outlet port in a unidirectionl manner.

12. The device of claim 1, wherein the cooling bladder comprises a plurality of compartments through which the heat transfer medium passes.

13. The device of claim 1. wherein the cooling bladder comprises a first interior compartment and a second interior compartment, the transfer medium passing within the first interior compartment in a direction opposing that of the trasfer medium passing widtwi the second interior compartment.

14. The device of claim 1, wherein the conformable thermally conductive material comprises a single material layer.

15. The device of claim 1, whorein the conformable thermally conductive material comprises a plurality of material layers.

16. The device of claim 1, wherein the conformable thermally conductive material comprises a metallic layer disposed between a first polymer layer and a second polymer layer.

17. Tha device of claim 1, wherein the conformable thermally conductive material of the cooling bladder has a thickness of less than about 150 mils.

18. The device of claim 1, wherein the cooling bladder and the heat transfer medium constitute less than about 50% by weight or volume of a total aggregate weight or volume of the cells, cooling bladder, and heat transfer modium.

19. The device of claim 1, when the plurality of electrochemical cells are arranged to form a plurality of cell sets, each of the cell sets provided with one of a plurality of the cooling bladders, sudh tiat an operating temperature of electrochemical cells of each of the cell sets is controlled by at least one of tbe plurality of cooling bladders.

20. The device of claim 1, wherein the plurality of electrochemical cells are arranged to forn a cell stack, and the cooling bladder controls the operating temperature of the cell stack such that a temperature difference as measured between auy two cells of fte cell stack does not exceed 5 degrees Celsius.

21. The device of claim 1, wherein the plurality of electrochemical cells are arranged to form a cell stack, and the cooling bladder controls the operating temperature of the cell stack such that a tamperature difference as measured between any two points on either the first or second planar surface of an individual cell does not exceed 5 degrees Celsius.

22. The deice of claim 1, wherein the plurality of electrochemical cells are arranged to form a cell stack, and the cooling bladder controls the operating temperature of the cell stack such that a temperature difference as measured between any two cells of the cell stack or between any two point on either the first or second planar surface of an individual cell does not exceed 2 degrees Celsius.

23. The devic of claim 1, wherein the cooling bladder conforms to a serpentine configuration to contact the respective first and sctond planar surfaces of each of the electrochemical cells.

24. The device of claim 1, wherein:

each of the plurality electrochemical cells comprises first, second, third, and fourth edges, thP first edge opposing the second edge and the third edge the fourth edge;

the first and second edges of euch oleetrochemical cell electrically couples to respective electrical conductors for conducting current into and out of euch of the electrochemical cells; and

the cooling bladder contacts respective third and fourth edges and respective first and second planar surfaces of each of the electrochemical cells.

25. The device of claim 1, wherein the heat transfer medium comprises water.

26. The device of claim 1, wberein the heat transfer medium comprises a mixture of water and ethylene glycol.

27. The device of claim 1, wherein a temperature of the heat transfer medium entering the inlet port of the cooling bladder is substantially constant.

28. The device of claim 1, wherein the operating temperature of the elctrochemical cells ranges between about 20 degrees Celsius and about 130 degrees Celsius.

29. The device of claim 1, further comprising a houing within which the plurality of electrochemical cells and the cooling bladder are situated the housing comprising a positive terminal and a negative terminal each coupled to the electrochemical cells, the housing of comnprising an inlet aperture for providing access to the inlet port of the cooling bladder and an outlet aperture for providing access to the outlet port of the cooling bladder.

30. The device of claim 1, further comprsing a housing within which the plurality of electrochemical cells and a plurality of the cooling bladders are situated, the housing comprising a positive terminal and a negative terminal each coupled to the electrochemical cells, the housing further comprising at least one inlet aperture for providing access to an inlet port of each of the cooling bladders and at least one outlet aperture for providing access to an outlet port of each of the cooling bladders.

31. The device of claim 1, wherein the electrochemical cells comprise lithium cells or nickel metal hydride cells.

32. An electrochemical storage device, comprising:

a plurality of electrochemiical cells arranged in a spaced apart relationship, the electrochemical cells comprising opposing first and second planr surfaces, the electrochemical cells subject to volumetric changes during charge and discharge cycling; and

a cooling bladder formed of a conformable thermally conductive material, the cooling bladder conformable to contact at least the repective first planar surface or second planar surface of each of the electrochemical cells, a heat transfer medium passing within the cooling bladder to control an operating temperature of the electrochemical cells, the cooling bladder pressurized to maintain the electrochemical cells in a state of compression during charge and discharge cycling.

33. The dcvice of claim 32, wherein the cooling bladder comprises a plurality of flow channels within which the heat transfer medium passes.

34. The device of claim 32, wherein the cooling bladder comprises a support arrangememt that inhibits restriction of heat transfer medium flow at cooling bladder bend Iocations.

35. The device of claim 34, wherein the support arrangement is located on an outer surface of the cooling bladder at the cooling bladder bend locations.

36. The device of claim 34, wherein the support arrangement is located within tbo cooling bladder at the cooling bladder bend locations.

37. The device of claim 32, wherein the cooling bladder comprises a porous filler material disposed within the cooling bladder.

38. The device of claim 32, wherein the cooling bladder comprises thickend sections provided at cooling bladder locations subject to bending.

39. The device of claim 32, wherein the cooling bladder comprises a plurality of compartments through which the haat medium posses.

40. The device of claim 32, wberein the conformable thermally conductive material comprises a single material layer.

41. The device of claim 32, wharein the conformable thermally conductive material comnrises a plurality of material layer.

42. The device of claim 32, wherein the conformable thermally conductive material of the cooling bladder has a thickness of less than about 150 mils.

43. The device of claim 32, wherein the plurality of electrochemical cells are arranged to form a plurality of cell sets, each of the cell sets provided with one of a plurality of the cooling bladders, such that an operating teperature of electrochemical cells of each of the cell sets is controlled by at least one of the plurality of cooling bladders.

44. The device of claim 32, wherein the plurality of eletochemical cells are arranged to form a cell stack, and the cooling bladder controls the operating temperature of the cell stack such that a temperature differece as measured between any two cells of the cell stack does not exceed 5 degrees Celsius.

45. The device of claim 32, wherein the plurality of electrochemical cells are arranged to form a cell stack, and the cooling bladder controls the operating temperature of th cell stack such that a tenperature diffenrce as measured between any two points on either the first or second planar surface of an individual cell does not exceed 5 degrees Celsius.

46. The device of claim 32, wherein the cooling bladder conforms to a serpentine configuration to contact the respective first and second planar surfaces of each of the electrochemical cells.

47. The device of claim 32, wherein:

each of the plurality of electrochemical cells comprises first, second, third, and fourth edges, the first edge opposing the second edge and the third edge opposing the fourth edge;

the first and second edges of each electrochemical cell electrially couples to respective electrical conductors for conducting current into and out of each of the electrochemical cells; and

the cooling bladder contacts respective third and fourth edges and respective first and second planar surfaces of each of the electrochemical cells.

48. The device of claim 32, wherein the operating temperature of the electrochemical cells ranges between about 20 degrees Celsius and about 130 degrees Celsius.

49. The device of claim 32. further comprising a housing within which the plurality of electrochemical cells and the cooling bladder are sitated, the housing comprising a positve terminal and a negative terminal each coupled to the eletrochemical cells, the housing further comprising an inlet aperture for providing access to the inlet port of the cooling bladder and an outlet aperture for providing access to the outlet port of the cooling bladder.

50. The device of claim 32, further comprising a housing within which the plurality of electrochemical cells and a plurality of the cooling bladders are situated, the housing comprising a positive terminal and a negative terminal each coupled to the electrochemical cells, the housing furthier comprising at least one inlet aperture for providing access to an inlet port of each of the cooling bladder and at least one outlet aperture for providing access to an outlet port of each of the cooling bladders.

51. The device of claim 32, wherein the electrochemical colls comprise lithium cells or nickel metal hydride cells.

52. A method of providing cooling within an electrochemical storage davice, comprising:

providing a plurality of electrocemical cells arranged in a spaced apart relationship, each of the electrochemical cells comprising opposing first and second planar surface and subject to volumetric changes during charge and discharge cycling;

providing a conformable, the conductive cooling bladder such that the cooling bladder maintains contact with at least the first planar suface or the second planar surface of each of the electrochemical cells during the volumetric changes; and

passing heat transfer medium through the cooling bladder to control an operating temperature of the electochemical cells.

53. The method of claim 52. further comprising pressurising the cooling bladder to maintain the eleclochemical cells in a state of compression during call charge and discharge cycling.

54. The method of claim 52, wherein passing the heat transfer medium further comprises passing the heat transfer medium through the cooling bladder in a unidirectional manner.

55. The method of claim 52, wherein passing te heat transfer medium furtber comprises passing the heat transfer medium through a plurality of oompartments provided within the cooling bladder.

56. The method of claim 52, further comprising supporting the cooling bladder at cooling bladder bend locations to inhibit restriction of heat transfer medium flow at the cooling bladder bend locations.

58. The method of claim 52, wherein the plurality of electrochemical cells are arranged to form a plurality of cell sets, each of the cell sets provided with one of a plurality of the cooling bladders, further wherein passing the heat transfer medium comprises passing the heat transfer medium through each of the cooling bladder to control an operating temperature of the electrochemical cells of each of the cell sets.

59. The method of claim 52, wherein the plurality of clectrochemical cells are arranged to form a cell stack, further wherein passing the heat transfer medium comprises passing the heat transfer medium through the cooling bladder to control the operating temperature of the cell stack such that a temperature difference as measured between any two cells of the cell stack does not exceed 5 degrees Celsius,

60. The method of claim 52, wherein the plurality of electrochemical cells are arranged to form a cell stack, wherein passing the heat transfer medium comprises passing the heat transfer medium through the cooling bladder to control the operatiog temperature of the cell stack such that a temperature difference as measured between any two points on either the first or second planar surface of an individual cell does not exceed 5 degree Celsius.

61. The method of claim 52, wherein the heat transfer medium comprises water or a mixture of water and ethylene glycol.

62. The method of claim 52, wherein passing the heat transfer medium comprises passing the heat transfer medium at a substantally constant temperature into the cooling bladder.

63. The method of claim 52, wherein the operating tunperature of the electrochemical cells ranges between about 20 degrees Celsius and about 130 degrees Celsius.

64. The method of claim 52, wherein the electrochemical cells comprise lithium cells or nickel metal hydride cells.

65. The method of claim 52, further comprising providing a housing within which the plurality of electochemical cels and the cooling bladder are situated, the housing comprising a positive terminal and a negative terminal each coupled to the electrochemical cells, the housing further comprising an inlet aperture for providing access to the inlet port of the cooling bladder and an outet aperture for providing access to the outlet port of the cooling bladder, further wherein passing the heat transfer medium comprises passing the heat transfer the heat medium through the inlet aperture of the housing, the inlet and outlet ports of the cooling bladder, and the outlet aperture of the housing.

66. The method of claim 52, further comprising providing a housing within which the plurality of electrochemical cells and a plurality of the cooling bladders are situated, the housing comprising a positive terminal and a negative terminal each coupled to the electrochemical cells, the housing further comprising at least one inlet aperture for providing access to an inlet port of each of the cooling bladders and at lenst one outlet aperture for providing access to an outlet port of each of the cooling bladders, further wherein passing the heat transfer medium comprises passing the heat transfer medium through the at least one inlet aperture of the housing, the inlet and outlet ports of the respective cooling bladders, and the at least one outlet aperture of the housing.

57. The method of claim 57, wherein supporting the cooling bladder further comprises using a porous filler material within the cooling bladder to support the cooling bladder at the cooling bladder bend locations.