Method of running-in operation of fuel cell

Patent metadata

Field	Value
Publication number	US-10957925-B2
Application number	US-201715420998-A
Country	US
Kind code	B2
Filing date	Jan 31, 2017
Priority date	May 20, 2016
Publication date	Mar 23, 2021
Grant date	Mar 23, 2021

Abstract

First, a reaction gas is supplied to a fuel cell stack including a laminate of solid polymer electrolyte fuel cells and power generation is performed so that a temperature of the fuel cell stack reaches 65° C. or higher (heating power generation step). Next, the reaction gas is supplied to the fuel cell stack and the power generation is performed under a condition in which relative humidity is 100% or more (cleaning power generation step). Cooling water of room temperature may be supplied to the fuel cell stack from the outside before the cleaning power generation step is performed after the heating power generation step is completed, or after the cleaning power generation step is completed (quenching step).

First claim

What is claimed is:

1. A method of running-in operation of a fuel cell, consisting of:
a single heating power generation step of supplying a reaction gas to a fuel cell stack including a laminate of solid polymer electrolyte fuel cells and performing power generation so that a temperature of the fuel cell stack reaches 65° C. or higher and thereby promoting desorption of a poisonous substance from a surface of a catalyst, wherein during the single heating power generation step, air is provided and relative humidity of less than 100% is maintained;
and after completion of the single heating power generation step,
a single cleaning power generation step of supplying the reaction gas to the fuel cell stack and performing power generation under a condition in which relative humidity is 100% or more and thereby discharging the poisonous substance desorbed from the catalyst surface during the single heating power generation step to outside of the fuel cell together with liquid water before the poisonous substance desorbed from the catalyst surface during the single heating power generation step is reabsorbed to the catalyst surface.

2. The method according to claim 1 , wherein the single heating power generation step performs power generation so that the temperature of the fuel cell stack reaches 80° C. or higher.

3. The method according to claim 1 , further comprising a quenching step of supplying cooling water of room temperature to the fuel cell stack from the outside (a) before the single cleaning power generation step is performed after the single heating power generation step is completed, or (b) after the single cleaning power generation step is completed.

4. The method according to claim 1 , wherein performing the power generation in the single heating power generation step includes is at least one selected from the group consisting of:
(a) performing the power generation under a condition in which a stoichiometric ratio of air becomes lower than that in steady operation;
(b) performing the power generation under a condition in which an air utilization factor becomes higher than that in the steady operation; and
(c) performing the power generation under a condition in which a cell voltage becomes a desorption potential of a poisonous substance.

5. The method according to claim 1 ,
wherein each of the single heating power generation step and the single cleaning power generation step includes performing the power generation while circulating cooling water between the fuel cell stack and a heat exchanger, and
an amount of the cooling water in the single heating power generation step is smaller than an amount of the cooling water in the single cleaning power generation step.

6. The method according to claim 1 , wherein the single heating power generation step includes performing the power generation without allowing cooling water to flow in the fuel cell stack.

7. The method according to claim 1 , wherein during the single heating power generation step, cooling water is circulated by alternately repeating normal circulation for circulating the cooling water in one direction between the fuel cell stack and a heat exchanger and reverse circulation for reversing a flow direction of the cooling water.

8. The method according to claim 1 , wherein the single cleaning power generation step includes performing the power generation under a condition in which a current density is 1 A/cm 2 or more.

9. The method according to claim 1 , wherein during the single cleaning power generation step, alternately repeating normal supply of oxidant gas for allowing the oxidant gas to flow in one direction within the fuel cell stack and reverse supply of oxidant gas for reversing a flow direction of the oxidant gas within the fuel cell stack.

10. The method according to claim 1 , wherein the single cleaning power generation step includes performing the power generation under a condition in which a back pressure of a cathode gas channel is higher than that in steady operation.

Assignees

• Toyota Chuo Kenkyusho Kk
• Toyota Motor Co Ltd

Inventors

• Murata Hajime
• Kodama Kensaku
• Kato Manabu
• Kusakari Toshiaki

Classifications

• H01M8/0491

  of fuel cell stacks · CPC title

• H01M8/04029

  Heat exchange using liquids · CPC title

• H01M2008/1095

  Fuel cells with polymeric electrolytes · CPC title

• Y02P70/50

  Manufacturing or production processes characterised by the final manufactured product · CPC title

• H01M8/04828

  Humidity; Water content · CPC title