Preparation method for three-dimensional network structure membrane electrode for direct methanol fuel cell

A methanol fuel cell and network structure technology, applied in battery electrodes, structural parts, circuits, etc., can solve the problems of peeling off from the proton exchange membrane, reducing the catalyst usage rate, MEA dehydration, etc., to increase the active surface area, reduce Internal resistance, the effect of improving stability

Inactive Publication Date: 2011-06-08
UNIV OF SCI & TECH BEIJING
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are patents, such as CN 101626084A and CN 101276919A, etc., the above method will cause the catalyst to remain on the transfer medium in the hot pressing process, reducing the utilization rate of the catalyst. Therefore, they disclose that the catalyst slurry is directly sprayed onto the proton in a heated state. On the exchange membrane, the purpose of heating is to make the proton exchange membrane such as Nafion better stretch and flatten under negative pressure
The method of directly heating and spraying on the proton exchange membrane will cause the catalytic layer to peel off from the proton exchange membrane due to the different shrinkage rates of the catalytic layer and the proton exchange membrane when the temperature drops, and the heating and spraying process will cause MEA to lose water. When the battery is installed and operated, due to the different expansion coefficients of the catalytic layer and the proton exchange membrane, it is bound to cause peeling as the water content increases.

Method used

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  • Preparation method for three-dimensional network structure membrane electrode for direct methanol fuel cell
  • Preparation method for three-dimensional network structure membrane electrode for direct methanol fuel cell
  • Preparation method for three-dimensional network structure membrane electrode for direct methanol fuel cell

Examples

Experimental program
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Effect test

Embodiment 1

[0033] 1. Membrane preparation and pretreatment. Nafion 115 membrane at 5% H by volume 2 o 2 Treat in aqueous solution at 80°C for 1 hour, then treat in double-distilled water at 80°C for 1 hour, and then use 0.5 mol L at 80°C -1 h 2 SO 4 Aqueous solution treatment, and finally placed in double distilled water at 80°C for 1 hour, then put the Nafion membrane in double distilled water for later use.

[0034] 2. Preparation of catalyst slurry and preparation of catalytic layer. Choose 4mg / cm for cathode and anode respectively 2 Pt black and 4mg / cm 2 The PtRu black catalyst, respectively using 0.008mL / cm 2 and 0.013 mL / cm 2 5 wt % Nafion solution as binder, using 0.222mL / cm 2 and 0.235 mL / cm 2 propanol as a dispersant. The glove box was evacuated and filled with Ar gas. The catalyst was weighed in the glove box, the slurry was prepared, and the catalyst slurry was prepared by ultrasonic dispersion using an ultrasonic cell disruptor.

[0035] The flat heater with PTF...

Embodiment 2

[0042] 1. Membrane preparation and pretreatment. Nafion 115 membrane at 5% H by volume 2 o 2 Treat in aqueous solution at 80°C for 1 hour, then treat in double-distilled water at 80°C for 1 hour, and then use 0.5 mol L at 80°C -1 h 2 SO 4 Aqueous solution treatment, and finally placed in double distilled water at 80°C for 1 hour, then put the Nafion membrane in double distilled water for later use.

[0043] 2. Preparation of catalyst slurry and preparation of catalytic layer. Choose 2mg / cm for cathode and anode respectively 2 Pt black and 4mg / cm 2 The PtRu black catalyst, respectively using 0.004mL / cm 2 and 0.013 mL / cm 2 The 5 wt % Nafion solution was used as the binder, respectively using 0.111mL / cm 2 and 0.235 mL / cm 2 propanol as a dispersant. The glove box was evacuated and filled with N 2 gas. The catalyst was weighed in the glove box, the slurry was prepared, and the catalyst slurry was prepared by ultrasonic dispersion using an ultrasonic cell disruptor.

...

Embodiment 3

[0050] 1. Membrane preparation and pretreatment. Nafion 115 membrane at 5% H by volume 2 o 2 Treat in aqueous solution at 80°C for 1 hour, then treat in double-distilled water at 80°C for 1 hour, and then use 0.5 mol L at 80°C -1 h 2 SO 4 Aqueous solution treatment, and finally placed in double distilled water at 80°C for 1 hour, then put the Nafion membrane in double distilled water for later use.

[0051] 2. Preparation of catalyst slurry and preparation of catalytic layer. Choose 3mg / cm for cathode and anode respectively 2 Pt black and 4mg / cm 2 The PtRu black catalyst, respectively using 0.006mL / cm 2 and 0.013 mL / cm 2 5 wt % Nafion solution as binder, using 0.167mL / cm 2 and 0.235 mL / cm 2 propanol as a dispersant. The glove box was evacuated and filled with N 2 gas. The catalyst was weighed in the glove box, the slurry was prepared, and the catalyst slurry was prepared by ultrasonic dispersion using an ultrasonic cell disruptor.

[0052] The flat heater with P...

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PUM

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Abstract

The invention discloses a preparation method for a three-dimensional network structure membrane electrode for a direct methanol fuel cell, belonging to the technical field of the structure and the manufacture of the efficient membrane electrode assembly of the direct methanol fuel cell. A catalysis layer in the membrane electrode prepared by the temperature controlling ultrasound spraying processis adopted to realize the three-dimensional network structure of the catalysis layer; the amount of active sites exposed on a three-phase interface, of the catalyst, is added to provide a path for gas and liquid transmission; a carbon cloth subjected to hydrophobicity processing serves as a diffusion layer; an Nafion membrane serves as a proton exchange membrane; Pt black and PtRu black serve as catalysts, and propyl alcohol serves as a diffusion agent; a Nafion solution serves as a binder in the catalysis layer, and a PTFE (polytetrafluoroethylene) membrane or tinfoil serves as a transferring medium; the catalysis layer is transferred and pressed on two sides of the proton exchange membrane from the transferring medium; and finally, the diffusion layer is arranged on the catalysis layer by hot pressing. The formed laminar combination is the membrane electrode. The membrane electrode prepared with the method has the three-dimensional network structure and has the advantages of evenly distributed pores and centralized pore diameter, the active area of the catalysis layer is obviously enlarged, and the output power density of the cell is obviously improved.

Description

technical field [0001] The invention relates to a preparation method of a direct methanol fuel cell material, and belongs to the technical field of high-efficiency membrane electrode assembly structure and manufacture of a direct methanol fuel cell. Background technique [0002] Direct methanol fuel cell (DMFC) is a power generation device that directly converts chemical energy stored in fuel (methanol) and oxidant (oxygen or air) into electrical energy. The density is high, the fuel is directly fed when the battery is working, no reforming treatment is required, the structure is simple, the response time is short, the operation is convenient, easy to carry and store, and it is an ideal power source for portable electronic devices, mobile phones, cameras and electric vehicles. Applications considered most likely to be commercialized. [0003] Membrane electrode (MEA) is the only place for electrochemical reaction in the fuel cell, and it is the core component to ensure the ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): H01M4/88
CPCY02E60/50
Inventor 王新东刘桂成王一拓王萌苗睿瑛吴珺李建玲赵婷婷
Owner UNIV OF SCI & TECH BEIJING
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