# US 5,700,595 A · Ion exchange membrane fuel cell power plant with water management pressure differentials

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- Number: US 5,700,595 A
- Document ID: US5700595A
- Status: Granted
- Kind: A
- Application number: 08/494,132
- Filed: 1995-06-23
- Granted: 1997-12-23
- Earliest claimed: 1995-06-23
- Assignees: International Fuel Cells Corporation
- Inventors: Carl Reiser
- Web page: https://patentgrep.com/patent/US5700595A

## CPC

- H01M 8/04156: {with product water removal}
- H01M 8/04029: Heat exchange using liquids
- H01M 2300/0082: Organic polymers
- Y02E 60/50: Fuel cells
- H01M: PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION

## Abstract

A proton exchange membrane fuel cell device with an internal water management and transfer system includes a plurality of adjacently arranged proton exchange membrane assemblies including a proton exchange membrane component; a pair of porous anode and cathode catalyst layers situated on either side of the proton exchange membrane; and porous plate assemblies interposed between and in contact with each of the adjacent proton exchange membrane assemblies. Oxidant gas is supplied to oxidant gas supply channels, and fuel gas to fuel gas supply channels formed in the porous plate assemblies for distribution to the cathode and anode catalyst layers, respectively. A water coolant circulating system is formed in each of the porous plate assemblies and causes each of the porous plate assemblies to become saturated with coolant water. The reactant flow fields are pressurized to a pressure which exceeds the coolant water circulating pressure by a selected .DELTA.P so as to ensure that product water formed on the cathode side of each membrane assembly will be pumped through the porous plates into the coolant water flow field and become entrained in the circulating coolant water stream.

## Claims

### Claim 1

A method for operating a solid polymer electrolyte membrane fuel cell power plant, said method comprising the steps of
a) providing oxidant and fuel reactant gas streams on opposite cathode and anode sides of the solid polymer electrolyte membrane;
b) providing a circulating water coolant stream on said cathode side of the electrolyte membrane;
c) providing a fine pore plate between said oxidant gas stream and said circulating water coolant stream; and
d) pressurizing said oxidant reactant gas stream to a first predetermined pressure;
e) pressurizing said water coolant stream to a second predetermined pressure which is less than said first predetermined pressure so as to create a positive target pressure differential (.DELTA.P) between said oxidant reactant gas stream and said water coolant stream, which .DELTA.P is operative to pump product water formed on the cathode side of the electrolyte membrane through said fine pore plate and into said circulating water coolant stream.

### Claim 2 (depends on 1)

The method of claim 1 wherein said oxidant reactant gas stream is pressurized to a pressure which is above ambient pressure.

### Claim 3 (depends on 1)

The method of claim 1 further comprising the step of periodically releasing product water from said water coolant stream.

### Claim 4

A solid polymer electrolyte membrane fuel cell power plant assembly comprising:
a) oxidant and fuel reactant gas streams on opposite cathode and anode sides of the solid polymer electrolyte membrane;
b) a circulating water coolant stream on said cathode side of the electrolyte membrane;
c) a fine pore plate between said oxidant gas stream and said circulating water coolant stream;
d) means for pressurizing said oxidant reactant gas stream to a first predetermined pressure; and
e) means for pressurizing said water coolant stream to a second predetermined pressure which is less than said first predetermined pressure so as to create a positive target pressure differential (.DELTA.P) between said oxidant reactant gas stream and said water coolant stream, which .DELTA.P is operative to pump product water formed on the cathode side of the electrolyte membrane through said fine pore plate and into said circulating water coolant stream.

### Claim 5 (depends on 4)

The assembly of claim 4 comprising means for pressurizing said oxidant reactant gas stream to a pressure which is above ambient pressure.

### Claim 6 (depends on 4)

The assembly of claim 4 further comprising means for periodically releasing product water from said water coolant stream.