Wet state control device for fuel cell

Patent metadata

Field	Value
Publication number	US-9620797-B2
Application number	US-201214123868-A
Country	US
Kind code	B2
Filing date	Apr 19, 2012
Priority date	Jun 6, 2011
Publication date	Apr 11, 2017
Grant date	Apr 11, 2017

Abstract

A wet state control device for fuel cell includes a priority control unit for preferentially controlling either one of a pressure and a flow rate of cathode gas when a wet state of a fuel cell is adjusted, a water temperature control unit for controlling a temperature of cooling water when the wet state of the fuel cell is not completely adjustable by a control of the priority control unit, and a complementary control unit for controlling the other of the pressure and the flow rate of the cathode gas to complement a response delay of the water temperature control unit.

First claim

The invention claimed is:

1. A wet state control device configured to control a wet state of a membrane in a fuel cell, the wet state control device comprising:
a priority control unit configured to control either one of a pressure or a flow rate of cathode gas when the wet state of the membrane is adjusted;
a water temperature control unit configured to control a temperature of cooling water when the wet state of the membrane is not completely adjustable by a control of the priority control unit; and
a complementary control unit configured to control the other of the pressure or the flow rate of the cathode gas to complement a response delay of the water temperature control unit;
wherein the fuel cell is dried by decreasing the wet state of the membrane, and during the drying:
the priority control unit decreases the pressure of the cathode gas;
the water temperature control unit increases the temperature of the cooling water when the wet state of the membrane is not completely adjustable by the control of the priority control unit; and
the complementary control unit controls the flow rate of the cathode gas to complement the response delay of the water temperature control unit.

2. The wet state control device according to claim 1 , wherein the fuel cell is dried by decreasing the wet state of the membrane, and during the drying:
the priority control unit decreases the pressure of the cathode gas based on a flow rate of the cathode gas that is to be supplied when the membrane is set in a wetter state than a present wet state and the temperature of the cooling water when the membrane is set in a wetter state than the present wet state;
the water temperature control unit increases the temperature of the cooling water based on an actual pressure of the cathode gas and the flow rate of the cathode gas that is to be supplied when the wetter state than the present wet state is set; and
the complementary control unit controls the flow rate of the cathode gas based on the actual pressure of the cathode gas and an actual temperature of the cooling water.

3. The wet state control device according to claim 2 , wherein:
the flow rate of the cathode gas that is to be supplied when the wetter state than the present wet state is set is a lowest flow rate in a range where the performance of the fuel cell is ensured; and
the temperature of the cooling water that is to be supplied when the wetter state than the present wet state is set is a lowest temperature in a range where the performance of the fuel cell is ensured.

4. The wet state control device according to claim 2 , wherein:
the priority control unit uses the actual temperature of the cooling water instead of the temperature of the cooling water supplied when the wetter state than the present wet state is set if the water temperature control unit is not operating and the fuel cell is dried by decreasing the wet state of the membrane.

5. The wet state control device according to claim 2 , wherein:
the priority control unit and the water temperature control unit use an actual flow rate of the cathode gas instead of the flow rate of the cathode gas supplied when the wetter state than the present wet state is set if the complementary control unit is not operating and the fuel cell is dried by decreasing the wet state of the membrane.

6. The wet state control device according to claim 1 , wherein the fuel cell is dried by decreasing the wet state of the membrane, and during the drying:
the priority control unit decreases the pressure of the cathode gas based on an actual flow rate of the cathode gas and an actual temperature of the cooling water;
the water temperature control unit increases the temperature of the cooling water based on the actual flow rate of the cathode gas and a pressure of the cathode gas supplied when the membrane is set in a drier state than a present wet state; and
the complementary control unit controls the flow rate of the cathode gas based on a pressure of the cathode gas supplied when the membrane is set in the drier state than the present wet state and a temperature between a temperature of the cooling water supplied when the membrane is set in the drier state than the present wet state and an actual temperature of the cooling water.

7. The wet state control device according to claim 6 , wherein:
the pressure of the cathode gas supplied when the drier state than the present wet state is set is a lowest pressure in a range where the performance of the fuel cell is ensured; and
the temperature of the cooling water supplied when the drier state than the present wet state is set is a highest temperature in a range where the performance of the fuel cell is ensured.

Assignees

• Aoki Tetsuya
• Matsumoto Michihiko
• Nissan Motor

Inventors

• Aoki Tetsuya
• Matsumoto Michihiko

Classifications

• H01M8/04119 Primary

  with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying · CPC title

• H01M2008/1095

  Fuel cells with polymeric electrolytes · CPC title

• H01M8/04358

  of the coolant · CPC title

• H01M8/04029

  Heat exchange using liquids · CPC title

• H01M8/04723 Primary

  of the coolant · CPC title