Utilization of dead channel to improve temperature uniformity on thermal interface material

Patent metadata

Field	Value
Publication number	US-11996533-B2
Application number	US-201916972536-A
Country	US
Kind code	B2
Filing date	Jun 7, 2019
Priority date	Jun 8, 2018
Publication date	May 28, 2024
Grant date	May 28, 2024

Abstract

A heat exchanger includes first and second plates joined together with portions of the inner surfaces spaced apart to define a plurality of fluid flow passages for flow of a heat transfer fluid. A dividing rib separates the heat exchanger into an inlet section and an outlet section, each of which includes a plurality of fluid flow passages. Inlet and outlet ports are located near a first end of the heat exchanger, on opposite sides of the dividing rib. The heat transfer surface area of the inlet section is less than that of the outlet section due to the presence of one or more flow obstructions between the inlet port and first ends of the fluid flow passages in the inlet section. Each flow obstruction may be a dead channel including a continuous outer rib completely surrounding a depressed middle region.

First claim

What is claimed is:

1. A heat exchanger, comprising:
a first plate having an inner surface and an outer surface;
a second plate having an inner surface and an outer surface, wherein the first and second plates are joined together with the inner surface of the first plate and the inner surface of the second plate in opposed facing relation to one another, and with portions of the respective inner surfaces of the first and second plates being spaced apart from one another;
a plurality of fluid flow passages adapted for flow of a heat transfer fluid, and located between the spaced apart portions of the inner surfaces of the first and second plates;
a dividing rib which separates the heat exchanger into an inlet section and an outlet section, each of the inlet section and the outlet section including a plurality of the fluid flow passages;
an inlet port located in the inlet section for supplying the heat transfer fluid to the plurality of fluid flow passages; and
an outlet port in the outlet section for discharging the heat transfer fluid from the plurality of fluid flow passages;
wherein both the inlet port and the outlet port are located proximate to a first end of the heat exchanger, on opposite sides of the dividing rib;
wherein the portions of the inner surfaces of the first and second plates which are spaced apart from one another define a total heat transfer surface area of the heat exchanger, and wherein the total heat transfer surface area is a sum of a heat transfer surface area of the inlet section and a heat transfer surface area of the outlet section; and
wherein the heat transfer surface area of the inlet section is less than the heat transfer surface area of the outlet section.

2. The heat exchanger according to claim 1 , wherein the dividing rib has a first end and a second end and extends along a central longitudinal axis of the heat exchanger, wherein the second end of the dividing rib is spaced from a second end of the heat exchanger to provide a gap through which flow communication is provided between the inlet section and the outlet section.

3. The heat exchanger according to claim 1 , wherein the outer surface of the first plate is adapted for thermal contact with bottom surfaces of plurality of battery cells arranged in side-by-side relation along a central longitudinal axis of the heat exchanger;
wherein the heat exchanger comprises a plurality of zones, each of the zones having an area corresponding to an area of the bottom surface of one of the battery cells;
each of the zones having an inlet portion lying in the inlet section of the heat exchanger and an outlet portion lying in the outlet section of the heat exchanger; and
each of the zones having a heat transfer surface area which is a portion of the total heat transfer surface area, with the heat transfer surface area of each of the zones being divided between the inlet section and the outlet section of the heat exchanger.

4. The heat exchanger according to claim 3 , wherein one of the plurality of zones comprises a proximal zone which is immediately adjacent to the inlet and outlet ports at the first end of the heat exchanger,
wherein the heat transfer surface area of the proximal zone is unevenly divided between the inlet and outlet sections of the heat exchanger, with a portion of the proximal zone heat transfer surface area lying in the outlet section being greater than a portion of the proximal zone heat transfer surface area lying in the inlet section.

5. The heat exchanger according to claim 4 , wherein one of the zones of the plurality of zones comprises a distal zone which is proximate to a second end of the heat exchanger and farthest from the inlet and outlet ports;
wherein the heat transfer surface area of the distal zone is evenly divided between the inlet and outlet sections of the heat exchanger.

6. The heat exchanger according to claim 3 , wherein the plurality of zones comprises a proximal zone which is immediately adjacent to the inlet and outlet ports at the first end of the heat exchanger, wherein one or more of the zones, including the proximal zone, has a respective heat transfer surface area unevenly divided between the inlet and outlet sections of the heat exchanger, with a portion of the heat transfer surface area lying in the outlet section being greater than a portion of the heat transfer surface area lying in the inlet section; and
wherein the one or more of the zones have a total length which is about 10-50 percent of a length of the heat exchanger.

7. The heat exchanger according to claim 6 , wherein two or more of the zones have the respective heat transfer surface areas unevenly divided between the inlet and outlet sections, and wherein the two or more zones are contiguous.

8. The heat exchanger according to claim 6 , wherein, in each of the zones having the respective heat transfer surface area unevenly divided between the inlet and outlet sections of the heat exchanger, the portion of the heat transfer surface area lying in the inlet section is about 10-80 percent smaller than the portion of the heat transfer surface area lying in the outlet section.

9. The heat exchanger according to claim 8 , wherein the portion of the heat transfer surface area lying in the inlet section is about 25-60 percent smaller than the portion of the heat transfer surface area lying in the outlet section.

10. The heat exchanger according to claim 6 , wherein each of the zones having the respective heat transfer surface area unevenly divided between the inlet and outlet sections of the heat exchanger has at least one flow obstruction provided in the respective inlet portion;
wherein the one or more flow obstructions occupy from about 50-90 percent of a width of the inlet portion of the zone in which the flow obstruction is provided, and from about 50-90 percent of a length of the zone.

11. The heat exchanger according to claim 1 , wherein the inlet section includes one or more flow obstructions located between the inlet port and first ends of the plurality of fluid flow passages in the inlet section.

12. The heat exchanger according to claim 11 , wherein each of the flow obstructions comprises a dead channel including a continuous outer rib structure completely surrounding a depressed middle region.

13. The heat exchanger according to claim 12 , wherein each of the flow obstructions has a pair of side edges, a leading edge and a trailing edge, all of which partly define regions of fluid flow, such that each of the flow obstructions is completely surrounded by the regions of fluid flow.

14. The heat exchanger according to claim 13 , wherein the side edges of each of the flow obstructions are parallel to each other and to the fluid flow passages in the inlet section.

15. The heat exchanger according to claim 13 , wherein one or more ribs or dimples are provided between the inlet port and the flow obstruction.

16. The heat exchanger according to claim 1 , wherein a thickness of the first plate in a portion of the inlet section is greater than a thickness of the plate in the outlet section.

17. The heat exchanger according to claim 16 , wherein the portion of greater thickness in the first plate is provided in an area of the inlet section which is proximate to the inlet port.

18. The heat exchanger according to claim 17 , wherein the portion of greater thickness in the first plate is provided by a sheet of metal secured to the inner surface of the first plate.

19. The heat exchanger according to claim 1 , wherein the heat exchanger is a cold plat

Assignees

• Dana Canada Corp

Inventors

• Rahim Noman
• Yu jiang feng
• Kenney Benjamin A
• Nayeemullah Mohammed Anush
• Vakilimoghaddam Farbod

Classifications

• H01M10/6556 Primary

  Solid parts with flow channel passages or pipes for heat exchange (closed pipes H01M10/6552) · CPC title

• B60L50/64 Primary

  Constructional details of batteries specially adapted for electric vehicles · CPC title

• B60L58/26

  by cooling · CPC title

• F28D1/035

  with U-flow or serpentine-flow inside the conduits (F28D1/0341 takes precedence) · CPC title

• F28F3/12

  Elements constructed in the shape of a hollow panel, e.g. with channels {(F28D1/02, F28D1/03 take precedence)} · CPC title