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Dual-electrode plates of fuel cell

A fuel cell and bipolar plate technology, applied to battery electrodes, fuel cell components, circuits, etc., can solve problems such as battery performance degradation, battery internal resistance increase, and electrical conductivity decline, so as to reduce production difficulty and production costs , Simplify the difficulty of assembly and improve the service life

Inactive Publication Date: 2009-04-22
BEIJING UNIV OF CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Studies have shown that the proton exchange membrane is very easy to adsorb metal cations and cause a decrease in conductivity, especially after the adsorption of ferric ions, the loss of the conductivity of the proton exchange membrane is greater than that of the adsorption of divalent nickel ions and divalent copper ions (M.J.Kelly, G. Fafilek, J.O. Besenhard, H. Kronberger, G.E. Nauer. J. Power Sources 145 (2005) 249-252)
During the long-term use of fuel cells, corrosion of metal materials is inevitable, and the metal cations produced by corrosion enter the proton exchange membrane, which will increase the internal resistance of the battery and reduce the performance of the battery.
In addition, the H that may be generated in the battery 2 o 2 Decomposition produces OH or 00H free radicals to attack the end group of the polymer segment in the proton exchange membrane, reducing the chemical stability of the proton exchange membrane (D.E.Curtin, R.D.Lousenberg, T.J.Henry, P.C.Tangeman, M.E.Tisack.J.Power Sources 131(2004)41-48), while the presence of metal ions aggravates the degradation rate of the proton exchange membrane (W.Schmittinger, A.Vahidi.J.PowerSources 180(2008)1-14), which is not conducive to the long-term use of fuel cells
Considering the assembly of the battery stack, the structure of the bridge plate is very unfavorable to the assembly of the fuel cell, and it is difficult to realize an automated assembly line

Method used

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  • Dual-electrode plates of fuel cell
  • Dual-electrode plates of fuel cell
  • Dual-electrode plates of fuel cell

Examples

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Embodiment 1

[0027] Such as Figure 7 As shown, the fuel cell includes an anode plate 1, a cooling plate 2, a cathode plate 3 and a membrane electrode 4, the membrane electrode 4 is arranged between the cathode plate 3 and the anode plate 1, and the cooling plate 2 is arranged between the anode plate 1 and the cathode plate between 3. The main channel 7 for feeding and discharging fuel, the main channel 8 for feeding and discharging cooling liquid and cooling gas, and the main channel 9 for feeding and discharging oxidant run through each pole plate. Attached below Figure 1~6 The structure of each pole plate in this embodiment will be described in detail.

[0028] In this embodiment, the feed or discharge main channel through holes of each plate are connected with the flow channels on the respective plate through the ectopic through holes, the ectopic through holes run through the plates, and the main channel through holes are connected to the ectopic channels. The connection channel o...

Embodiment 2

[0040] The structure of this embodiment is basically the same as that of Embodiment 1, the only difference is that: the connecting channel 10 of the cooling air, cooling liquid feed and discharge main channel and the ectopic through hole is arranged on the cooling plate, and the connecting channel 10 and The cooling liquid and the cooling air passage 13 are respectively located on two opposite sides of the cooling plate. The connecting channel between the feed or discharge main channel on the anode plate and the ectopic through hole on the plate is arranged on the plate adjacent to the anode plate, and the connecting channel is on the other side of the plate flow channel. side.

Embodiment 3

[0042] The structure of this embodiment is basically the same as that of Embodiment 1, and the only difference is that: the connecting channel 14 between the main channel for feeding the oxidant and the dislocation through hole for feeding the oxidant is arranged on the cathode plate, and the connecting channel 14 and the flow channel 16 for the oxidizing agent They are respectively located on two opposite sides of the cathode plate.

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Abstract

The invention relates to a plate for a fuel battery, which belongs to the field of fuel batteries. A feeding main channel and a discharging main channel penetrating an anode plate, a cathode plate and a cooling plate are respectively communicated with flow channels of respective plates through deviation through holes. The deviation through holes penetrate the plates, one end of each of the deviation through holes is communicated with the feeding main channel or the discharging main channel, and the other end is communicated with the flow channels on the plates. The plates can be used for manufacturing fuel batteries with different flow field structures of small power to large power, can prolong the service life of membrane electrodes of fuel batteries, and are suitable for the scale production of fuel batteries.

Description

technical field [0001] The invention relates to a fuel cell polar plate, which belongs to the field of fuel cells. technical background [0002] With the increasing shortage of natural resources and the gradual exhaustion of mineral energy such as oil, people are facing an increasingly severe energy crisis. In addition, the increasingly serious environmental pollution problem also forces people to look for cleaner energy sources. A fuel cell is an electrochemical device that directly converts chemical energy into electrical energy in an efficient and environmentally friendly manner. The theoretical conversion rate can reach more than 80%. It is a green energy source that can simultaneously solve two world problems of energy saving and environmental protection. Countries attach great importance to fuel cells, which promotes the rapid development of fuel cells. Proton exchange membrane fuel cell (PEMFC) has the advantages of light weight, compact structure, easy drainage, hi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): H01M4/86H01M8/02H01M8/0202
CPCY02E60/50Y02P70/50
Inventor 曾蓉李培金曹兵
Owner BEIJING UNIV OF CHEM TECH
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