Avoiding fuel starvation of anode end fuel cell

Patent metadata

Field	Value
Publication number	US-9966612-B2
Application number	US-201214378314-A
Country	US
Kind code	B2
Filing date	Feb 24, 2012
Priority date	Feb 24, 2012
Publication date	May 8, 2018
Grant date	May 8, 2018

Abstract

The fuel flow channels ( 20 a ) of the end fuel cell ( 9 a ) at the anode end ( 34 ) of a fuel cell stack are significantly deeper than the fuel flow field channels ( 20 ) of the remaining fuel cells ( 9 ) in the stack, whereby fuel starvation caused by ice in the fuel flow channels is avoided during cold startup. The fuel flow field channels of the end cell ( 9 ) at the anode end of the stack is between about 0.15 mm and about 1.5 mm deeper than the fuel flow field channels in the remaining fuel cells of the stack, or between about 35% and about 65% deeper than the fuel flow field channels in the remaining fuel cells of the stack.

First claim

The invention claimed is:

1. An apparatus, comprising:
a fuel cell stack including a plurality of contiguous fuel cells compressed between a pair of end plates, each of said fuel cells comprising an electrolyte with an anode catalyst layer on a first surface of the electrolyte and a cathode catalyst layer on a second surface of the electrolyte, an anode gas diffusion layer adjacent the anode catalyst layer and a cathode gas diffusion layer adjacent the cathode catalyst layer, an anode water transport plate having a fuel flow field including fuel flow field channels adjacent the anode gas diffusion layer and a cathode water transport plate having an oxidant flow field adjacent the cathode gas diffusion layer;
wherein each of the fuel flow field channels in the fuel flow field of the fuel cell at an anode end of the fuel cell stack have a respective depth measured perpendicularly to the first and second surfaces of the electrolyte, and each of the fuel flow field channels in the fuel flow fields of other fuel cells in the fuel cell stack have a respective depth measured perpendicularly to the first and second surfaces of the electrolyte;
wherein each of the depths of the fuel flow field channels in the fuel flow field of the fuel cell at an anode end of the fuel cell stack are deeper than each of the depths of the fuel flow field channels in the fuel flow fields of the other fuel cells in the fuel cell stack; and
wherein the fuel flow field channels in the fuel flow fields of the other fuel cells in the fuel cell stack are the fuel flow field channels in the fuel flow fields of all other fuel cells in the fuel cell stack.

2. The apparatus of claim 1 wherein each of the depths of the fuel flow field channels in the fuel flow fields of the other fuel cells in the fuel cell stack are between about 0.3 mm and about 0.5 mm.

3. The apparatus of claim 2 wherein each of the depths of the fuel flow field channels in the fuel flow field of the fuel cell at the anode end of the fuel cell stack are deeper than each of the depths of the fuel flow field channels in the fuel flow fields of the other fuel cells in the fuel cell stack by between about 0.15 mm and about 0.25 mm.

4. The apparatus of claim 1 wherein each of the depths of the fuel flow field channels in the fuel flow fields of the other fuel cells in the fuel cell stack are about 0.4 mm.

5. The apparatus of claim 1 wherein each of the depths of the fuel flow field channels in the fuel flow field of the fuel cell at the anode end of the fuel cell stack are at least twice as deep as each of the depths of the fuel flow field channels in the fuel flow fields of the other fuel cells in the fuel cell stack.

6. The apparatus of claim 1 wherein each of the depths of the fuel flow field channels in the fuel flow field of the fuel cell at the anode end of the fuel cell stack are deeper than each of the depths of the fuel flow field channels in the fuel flow fields of the other fuel cells in the fuel cell stack by between about 0.15 mm and about 1.5 mm.

7. The apparatus of claim 1 wherein each of the depths of the fuel flow field channels in the fuel flow field of the fuel cell at the anode end of the fuel cell stack are deeper than each of the depths of the fuel flow field channels in the fuel flow fields of the other fuel cells in the fuel cell stack by between about 0.15 mm and about 0.5 mm.

8. The apparatus of claim 1 wherein each of the depths of the fuel flow field channels in the fuel flow field of the fuel cell at the anode end of the fuel cell stack are deeper than each of the depths of the fuel flow field channels in the fuel flow fields of the other fuel cells in the fuel cell stack by between about 0.15 mm and about 0.25 mm.

9. The apparatus of claim 1 wherein each of the fuel flow field channels in the fuel flow field of the fuel cell at the anode end of the fuel cell stack have a common first depth measured perpendicularly to the first and second surfaces of the electrolyte, and each of the fuel flow field channels in the fuel flow fields of other fuel cells in the fuel cell stack have a common second depth measured perpendicularly to the first and second surfaces of the electrolyte, and the first depth is deeper than the second depth.

10. The apparatus of claim 9 wherein the first depth is deeper than the second depth by between about 35% and about 65% of the second depth.

11. The apparatus of claim 9 wherein the first depth is deeper than the second depth by between about 45% and about 65% of the second depth.

12. The apparatus of claim 9 wherein the first depth is deeper than the second depth by about 55% of the second depth.

Assignees

• Patterson Jr Timothy W
• Darling Robert M
• Audi Ag

Inventors

• Patterson Jr Timothy W
• Darling Robert M

Classifications

• H01M8/026 Primary

  characterised by grooves, e.g. their pitch or depth · CPC title

• H01M8/10

  Fuel cells with solid electrolytes · CPC title

• H01M8/2465

  Details of groupings of fuel cells · CPC title

• H01M8/241

  with solid or matrix-supported electrolytes · CPC title

• H01M8/04225

  during start-up · CPC title