Formed plate assembly for PEM fuel cell

Patent metadata

Field	Value
Publication number	US-10516167-B2
Application number	US-201514734047-A
Country	US
Kind code	B2
Filing date	Jun 9, 2015
Priority date	Apr 22, 2010
Publication date	Dec 24, 2019
Grant date	Dec 24, 2019

Abstract

A bipolar plate assembly for a fuel cell includes a cathode plate disposed adjacent an anode plate. The cathode and anode plates are formed having a first thickness of a low contact resistance, high corrosion resistance material by a deposition process. The first and second unipolar plates are formed on a removable substrate, and a first perimeter of the first unipolar plate is welded to a second perimeter of the second unipolar plate to form a hermetically sealed coolant flow path.

First claim

What is claimed is:

1. A bipolar plate assembly for a fuel cell, comprising:
a unipolar cathode plate; and
a unipolar anode plate joined with the cathode plate, at least one of the cathode plate and the anode plate having a first predetermined thickness of a first material, the first material being a low contact resistance, high corrosion resistance material formed by a deposition process on a formed substrate, the first material being generally applied to the formed substrate in a first predetermined thickness at locations defining a desired flow field pattern, the first material being locally applied to the substrate in a third predetermined thickness proximate to an alignment aperture of the at least one of the cathode plate and the anode plate such that the third predetermined thickness is greater than the first predetermined thickness; and a second material different from the first material applied to the first material at locations defining a perimeter of the at least one of the cathode plate and the anode plate, the second material being a second low contact resistance, high corrosion resistance material.

2. The bipolar plate assembly of claim 1 , wherein the low contact resistance, high corrosion resistance material is a high nickel content alloy including at least 50 percent by atom on a basis of all atoms in the low contact resistance, high corrosion resistance material.

3. The bipolar plate assembly of claim 1 , wherein the low contact resistance, high corrosion resistance material is a nanocrystalline alloy.

4. The bipolar plate assembly of claim 3 , wherein the nanocrystalline alloy is one of an FeW alloy, an FeMo alloy, an FeCr alloy, an FeTa alloy, an FeNb alloy, and mixtures thereof.

5. The bipolar plate assembly of claim 1 , wherein the low contact resistance, high corrosion resistance material is carbon.

6. The bipolar plate assembly of claim 1 , wherein at least a portion of an active area of the anode plate matingly engages at least a portion of an active area of the cathode plate to provide electrical conductivity therebetween.

7. The bipolar plate assembly of claim 1 , wherein the first predetermined thickness is between 5 and 100 microns.

8. The bipolar plate assembly of claim 1 , wherein a first perimeter of the cathode plate is integrally joined with a second perimeter of the anode plate to form a substantially hermetic seal therebetween.

9. The bipolar plate assembly of claim 1 , wherein variation of the first predetermined thickness is less than 50 nanometers.

10. A fuel cell stack comprising:
a plurality of membrane electrode assemblies arranged in a stacked configuration;
a bipolar plate assembly disposed between adjacent membrane electrode assemblies, the bipolar plate assembly including a unipolar cathode plate joined to a unipolar anode plate;
a first material forming the cathode plate and the anode plate, the first material being a first low contact resistance, high corrosion resistance material, the first material being generally applied to a substrate in a first predetermined thickness at locations defining a desired flow field pattern, the first material being locally applied to the substrate in a third predetermined thickness proximate to an alignment aperture of each of the cathode plate and the anode plate such that the third predetermined thickness is greater than the first predetermined thickness; and
a second material different from the first material applied to the first material at locations defining a first perimeter of the cathode plate and a second perimeter of the anode plate, the second material being a second low contact resistance, high corrosion resistance material,
wherein variation of the first predetermined thickness is less than 50 nanometers, and
wherein the cathode plate and the anode plate are removed from the substrate prior to assembly of the fuel cell stack.

11. The fuel cell stack of claim 10 , wherein at least a portion of an active area of the anode plate matingly engages at least a portion of an active area of the cathode plate to provide electrical conductivity therebetween.

12. The fuel cell stack of claim 10 , wherein the first predetermined thickness is between 5 and 100 microns.

13. The fuel cell stack of claim 10 , wherein the first predetermined thickness of the first material of the cathode plate abuts diffusion media of a first membrane electrode assembly, and the first predetermined thickness of the first material of the anode plate abuts diffusion media of a second membrane electrode assembly.

14. The fuel cell stack of claim 13 , wherein the substantially hermetic seal is formed by one of welding, laser welding, brazing and soldering.

15. The fuel cell stack of claim 10 , wherein the second material is generally applied in a second predetermined thickness to the locations defining the first perimeter and the second perimeter, and the second material is locally applied in a fourth predetermined thickness to locations proximate to the alignment aperture of each of the anode plate and the cathode plate such that a thickness of the second material proximate to the alignment aperture is greater than the second predetermined thickness.

16. An assembly comprising:
a substrate having a first substrate external surface corresponding to a desired cathode plate flow field pattern and a second substrate external surface corresponding to a desired anode plate flow field pattern;
a first material applied to the first substrate external surface and the second substrate external surface forming a cathode plate on the first substrate external surface and an anode plate on the second substrate external surface, the first material being a first low contact resistance, high corrosion resistance material, the first material being applied such that a first predetermined thickness is generally applied to the first substrate external surface and the second substrate external surface at locations defining a desired flow field pattern and such that a third predetermined thickness is locally applied proximate to an alignment aperture of each of the anode plate and the cathode plate such that the third predetermined thickness is greater than the first predetermined thickness; and
a second material different from the first material applied to the first material at locations to define a first perimeter of the cathode plate and a second perimeter of the anode plate, the second material being a second low contact resistance, high corrosion resistance material, the second material being applied such that a second predetermined thickness is generally applied to the locations defining the first perimeter and the second perimeter and such that a fourth predetermined thickness is locally applied proximate to the alignment aperture of each of the anode plate and the cathode plate such that a thickness of the second material proximate to the alignment aperture is greater than the second predetermined thickness,
wherein variation of each of the first predetermined thickness and the second predetermined thickness is less than 50 nanometers.

Assignees

• Gm Global Tech Operations Llc

Inventors

• Dadheech Gayatri Vyas
• Fly Gerald W

Classifications

• H01M2008/1095

  Fuel cells with polymeric electrolytes · CPC title

• H01M8/0258

  characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant · CPC title

• C25D3/562

  containing more than 50% by weight of iron or nickel or cobalt · CPC title

• H01M8/0228

  in the form of layered or coated products · CPC title

• H01M8/0208

  Alloys · CPC title