Fuel cell thermal management system and method

• US 6,649,290 B2
• Filed: 05/11/2001
• Issued: 11/18/2003
• Est. Priority Date: 05/11/2001
• Status: Expired due to Fees

• Current Assignee: Cellex Power Products, Inc. (Plug Power Inc.)
• Original Assignee: Cellex Power Products, Inc. (Plug Power Inc.)
• Inventors: Corless, Adrian J., Leboe, David
• Primary Examiner(s): Bell, Bruce F.
• Application Number:
  US09/854,409
• Publication Number:
  US 20020168556A1
• Time in Patent Office: 921 Days
• Field of Search: 429/13, 429/17, 429/20, 429/22, 429/24, 429/26
• US Class Current: 429/423
• CPC Class Codes: B60L 3/0053 relating to fuel cells
• CPC Class Codes: B60L 58/33 by cooling
• CPC Class Codes: H01M 10/613 Cooling or keeping cold
• CPC Class Codes: H01M 10/615 Heating or keeping warm
• CPC Class Codes: H01M 10/625 Vehicles
• CPC Class Codes: H01M 10/627 Stationary installations, e.g. power plant buffering or backup power supplies
• CPC Class Codes: H01M 10/6563 with forced flow, e.g. by blowers
• CPC Class Codes: H01M 10/66 Heat-exchange relationships between the cells and other systems, e.g. central heating systems or fuel cells
• CPC Class Codes: H01M 10/667 the system being an electronic component, e.g. a CPU, an inverter or a capacitor
• CPC Class Codes: H01M 16/006 of fuel cells with rechargeable batteries
• CPC Class Codes: H01M 2250/20 Fuel cells in motive systems, e.g. vehicle, ship, plane
• CPC Class Codes: H01M 8/04007 related to heat exchange
• CPC Class Codes: H01M 8/04014 Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
• CPC Class Codes: Y02E 60/10 Energy storage using batteries
• CPC Class Codes: Y02E 60/50 Fuel cells
• CPC Class Codes: Y02T 90/40 Application of hydrogen technology to transportation, e.g. using fuel cells

Abstract

This application relates to a system and method for regulating the temperature of a self-contained fuel cell apparatus preferably comprising a fuel reformer. The invention maintains the various components of the fuel cell apparatus within preferred operating temperature ranges while ensuring that exhaust gases and external surfaces of the apparatus do not exceed safe temperature levels. The invention is particularly suited for self-contained hybrid power supply applications, for example for non-road electric vehicles. The various components of the apparatus are strategically configured relative to air flow paths to fully utilize the cooling capacity of the process stream and minimize parasitic loads. In some embodiments the inlet air is pre-heated to enable operation of the apparatus in low temperature environments, such as industrial freezers.

Claims

1. A method of regulating the thermal characteristics of a self-contained fuel cell apparatus having external surfaces and a plurality of heat-generating components housed within said apparatus, said components having different preferred operating temperature ranges, said method comprising:

(a) introducing a heat transfer gas into said apparatus;

(b) moving said heat transfer gas within said apparatus in one or more flow paths between said components to maintain said components within said preferred operating temperature ranges, whereby said flow paths are configured such that said heat transfer gas has sufficient cooling capacity to accept waste heat from each of said components located downstream therefrom; and

(c) exhausting said gas from said apparatus to the environment surrounding said apparatus,

wherein the temperature of said external surfaces and said gas exhausted from said apparatus is maintained below 70°

C.

2. The method of claim 1, further comprising the step of transferring heat from said heat transfer gas moving through a first one of said flow paths to said heat transfer gas moving through a second one of said flow paths.

3. The method of claim 1, wherein said method comprises providing a plurality of said gas flow paths and further comprises merging at least some of said flow paths prior to exhausting said heat transfer gas from said apparatus.

4. The method of claim 1, wherein at least some of said heat transfer gas is recirculated within said apparatus.

5. The method of claim 1, wherein an exhaust portion of said heat transfer gas is recirculated to pre-heat an intake portion of said heat transfer gas at a location upstream from at least some of said components, wherein said exhaust portion does not comprise contaminated emissions.

6. The method of claim 1, further comprising transferring heat from said heat transfer gas to a fuel storage chamber of said apparatus.

7. The method of claim 1, wherein said heat transfer gas is air introduced into said apparatus through an inlet in communication with said environment.

8. The method of claim 7, wherein said components comprise a fuel cell, a reformer, a DC/DC converter and an energy storage device, said method further comprising:

(a) moving said heat transfer gas in a first one of said flow paths from said inlet past said energy storage device and said DC/DC converter;

(b) moving said heat transfer gas in a second one of said flow paths from said inlet through said reformer; and

(c) moving said heat transfer gas in a third one of said flow paths from said inlet through said fuel cell.

9. The method of claim 8, further comprising mixing said heat transfer gas from said second and third flow paths downstream from said reformer to dilute exhaust expelled from said reformer.

10. The method of claim 8, wherein said heat transfer gas is moved through said first flow path downstream from said DC/DC converter to accept radiant heat from said reformer.

11. The method of claim 8, further comprising transferring heat from said heat transfer gas to a source of fuel for said apparatus prior to introduction of said fuel into said reformer.

12. The method of claim 8, wherein said heat transfer gas is introduced into said apparatus through a single inlet and is exhausted from said apparatus through a single outlet.

13. The method of claim 8, wherein said heat transfer gas moving in said third flow path comprises oxidant gas reactedin said fuel cell.

14. The method of claim 1, wherein the temperature of said external surfaces and said gas exhausted from said apparatus is maintained below 50°

C.

17. The system of claim 14, wherein said means for moving said heat transfer gas through said apparatus comprises:

(a) a plurality of conduits within said apparatus defining said flow paths for holding volumes of said heat transfer gas, each of said conduits being in communication with said inlet and said outlet;

(b) a plurality of air diverters for diverting said heat transfer gas into said conduits; and

(c) at least one active air flow control element for actuating movement of said heat transfer gas through said conduits.

15. A system for regulating the thermal characteristics of a self-contained fuel cell apparatus having external surfaces and a plurality of heat-generating components housed within said apparatus, said components having different preferred operating temperature ranges, said system comprising:

(a) an inlet for introducing a heat transfer gas into said apparatus;

(b) means for moving said heat transfer gas within said apparatus in one or more flow paths between said components to maintain said components within said preferred operating temperature ranges, whereby said flow paths are configured such that said heat transfer gas has sufficient cooling capacity to accept waste heat from any of said components located downstream therefrom; and

(c) an outlet for exhausting said gas from said apparatus to the environment surrounding said apparatus,

wherein the temperature of said external surfaces and said gas exhausted from said apparatus is maintained below 70°

C.

16. The system of claim 15, wherein said heat transfer gas is air introduced into said apparatus from the environment surrounding said apparatus through said inlet.

18. A method of regulating the thermal characteristics of a self-contained fuel cell apparatus comprising a fuel reformer, said apparatus having external surfaces and a plurality of heat-generating components including the fuel cell and the fuel reformer housed within said apparatus, said components having different preferred operating temperature ranges, said method comprising:

(a) introducing air into said apparatus from the environment surrounding said apparatus;

(b) moving said air within said apparatus in one or more flow paths between said components to maintain said components within said preferred operating temperature ranges, whereby said flow paths are configured such that said air has sufficient cooling capacity at any location within said flow paths to accept waste heat from any of said components located downstream therefrom; and

(c) exhausting said air from said apparatus to said environment surrounding said apparatus.

19. The method of claim 18, wherein the temperature of said external surfaces and said air exhausted from said apparatus is maintained below 70°

C.

20. The method of claim 18, wherein the temperature of said external surfaces and said air exhausted from said apparatus is maintained below 50°

C.

21. The method of claim 18, comprising a plurality of said flow paths and wherein at least some of said flow paths are merged prior to exhausting said air from said apparatus.

22. The method of claim 21, wherein said air is introduced into said apparatus through a single inlet and exhausted from said apparatus from a single outlet, wherein said inlet and said outlet are located on a common one of said external surfaces.

23. The method of claim 18, wherein a first portion of said air is recirculated within said flow paths after it has been heated within said apparatus.

24. The method of claim 23, wherein said first portion of said air is substantially free of reformer exhaust.