Fuel cell separator and fuel cell stack and reactant gas control method thereof

Patent metadata

Field	Value
Publication number	US-10074858-B2
Application number	US-201615067474-A
Country	US
Kind code	B2
Filing date	Mar 11, 2016
Priority date	Aug 24, 2006
Publication date	Sep 11, 2018
Grant date	Sep 11, 2018

Abstract

A fuel cell separator, a fuel cell stack having the fuel cell separator, and a reactant gas control method of the fuel cell stack are provided. That is, even when the fuel cell stack operates under the low load operation condition, a reactant gas is supplied to the reactant gas passages of the fuel cell separator, and thus, the length of the passage can be shortened by 50% as compared with the prior art having only one reactant gas passage. Therefore, the reactant gas can be effectively supplied without experiencing pressure loss. Further, in the high load operation of the fuel cell stack, the reactant gas is introduced into the first reactant gas passage of the fuel cell separator and utilized in half of the whole electrode area. Subsequently, the reactant gas is introduced into the second reactant gas passage and utilized in the remaining half of the electrode area. The flow rate of the reactant gas flowing along the passage channels is increased by two times, even when the reactant gas utilizing rate is identical as compared with the reactant gas flow in the low load operation. As a result, the moisture existing in the passage channels can be more effectively discharged and the flooding phenomenon occurring in the high load operation can be prevented. By controlling the reactant gas supply in accordance with an operation condition of the fuel cell stack without experiencing pressure loss and deterioration of the utilizing rate, the flooding phenomenon and concentration polarization phenomenon that occur in the fuel cell stack can be prevented.

First claim

What is claimed is:

1. A method of controlling reactant gas of a fuel cell stack, the method comprising:
determining if a performance deterioration cause, such as a flooding phenomenon or concentration polarization phenomenon, occurs in the fuel cell stack; and
controlling, when it is determined that the performance deterioration cause does not occur in the fuel cell stack, a reactant gas supply to the fuel cell stack in accordance with a low load operation condition, and, when it is determined that the performance deterioration cause occurs in the fuel cell stack, the reactant gas supply to the fuel cell stack in accordance with a high load operation condition,
wherein, in the low load operation condition, a reactant gas inlet valve and a reactant gas outlet valve are opened and a reactant gas intermediate valve is closed so that the reactant gas is supplied through first and second reactant gas inlet ports and discharged through first and second reactant gas outlet ports, and
in the high load operation condition, the reactant gas inlet valve and the reactant gas outlet valve are closed and the reactant gas intermediate valve is opened so that the reactant gas is supplied only through the first reactant gas inlet port and discharged only through the second reactant gas outlet port.

2. The method of claim 1 , wherein the reactant gas includes an oxidizing gas, and
in the low load operation condition, the oxidizing gas is supplied through a first oxidizing agent inlet port and a second oxidizing agent inlet port and passes along oxidizing agent inlet manifolds, in the course of which the oxidizing gas is introduced into oxidizing agent passages through a first oxidizing agent inlet through hole and a second oxidizing agent inlet through hole and is used for an electrochemical reaction, after which the oxidizing gas is discharged to oxidizing agent outlet manifolds through a first oxidizing agent outlet through hole and a second oxidizing agent outlet through hole to be finally discharged to an external side through a first oxidizing agent outlet port and a second oxidizing agent outlet port.

3. The method of claim 2 , wherein, in the high load operation condition, the oxidizing gas is supplied only to the first oxidizing agent inlet port and passes along a first oxidizing agent inlet manifold, in the course of which the oxidizing gas is introduced into a first oxidizing agent passage through the first oxidizing agent inlet through hole and is used for the electrochemical reaction, after which the oxidizing gas is discharged to a first oxidizing agent outlet manifold through the first oxidizing agent outlet through hole, directed to a third oxidizing agent outlet port, introduced again to a second oxidizing agent inlet manifold through a third oxidizing agent inlet port, introduced into a second oxidizing agent passage through the second oxidizing agent inlet through hole of a fuel cell separator, used again for the electrochemical reaction, discharged to a second oxidizing agent outlet manifold through the second oxidizing agent outlet through hole, directed to the second oxidizing agent outlet port, and finally discharged to the external side through the second oxidizing agent outlet port.

4. The method of claim 1 , wherein the reactant gas includes a fuel gas, and
in the low load operation condition, the fuel gas is supplied through a first fuel inlet port and a second fuel inlet port and passes along fuel inlet manifolds, in the course of which the fuel gas is introduced into fuel passages through a first fuel inlet through hole and a second fuel inlet through hole and is used for an electrochemical reaction, after which the fuel gas is discharged to fuel outlet manifolds through a first fuel outlet through hole and a second fuel outlet through hole to be finally discharged to an external side through a first fuel outlet port and a second fuel outlet port.

5. The method of claim 4 , wherein in the high load operation condition, the fuel gas is supplied only to the first fuel inlet port and passes along a first fuel inlet manifold, in the course of which the fuel gas is introduced into a first fuel passage through the first fuel inlet through hole and is used for the electrochemical reaction, after which the fuel gas is discharged to a first fuel outlet manifold through the first fuel outlet through hole, directed to a third fuel outlet port, introduced again to a second fuel inlet manifold through a third fuel inlet port, introduced into a second fuel passage through the second fuel inlet through hole of a fuel cell separator, used again for the electrochemical reaction, discharged to a second fuel outlet manifold through the second fuel outlet through hole, and finally discharged to the external side through the second fuel outlet port.

Assignees

• Doosan Corp

Inventors

• Oh Sung-Jin
• Lee Kyoung-Hwang
• Baek Seung-Ho
• Lee Sung-Hoon
• Park Il-Tae
• Hong Byung-Sun
• Shinn Mee-Nam

Classifications

• H01M8/1039

  halogenated, e.g. sulfonated polyvinylidene fluorides · CPC title

• H01M8/04753

  of fuel cell reactants · CPC title

• H01M8/2483

  characterised by internal manifolds · CPC title

• H01M8/2457

  with both reactants being gaseous or vaporised · CPC title

• H01M8/04679

  of fuel cell stacks · CPC title