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Catalyst layer full-ordered fuel cell electrode and membrane electrode

A fuel cell electrode and membrane electrode technology, applied in fuel cells, battery electrodes, nanotechnology for materials and surface science, etc., to achieve the effect of ensuring stability and high electrochemical reaction efficiency

Active Publication Date: 2018-09-14
广东泰极动力科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The above studies show that single ordered materials still have limitations in improving the performance or stability of PEMFC electrodes and membrane electrodes.

Method used

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  • Catalyst layer full-ordered fuel cell electrode and membrane electrode
  • Catalyst layer full-ordered fuel cell electrode and membrane electrode

Examples

Experimental program
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Effect test

Embodiment 1

[0026] combined with figure 2 The process and process shown to prepare the catalyst layer fully ordered polyelectrolyte membrane fuel cell electrode and membrane electrode, and carry out the discharge test, the main steps are as follows:

[0027] (1) In situ growth of VACNT array on gas diffusion layer 1

[0028] After washing and drying a piece of AAO double-pass porous template with a size of 2.3cm×2.3cm (pore size is 30nm, thickness is 100μm), it is bonded with a piece of carbon paper of the same size as the gas diffusion layer 1, and placed in a tube furnace , pass through acetylene at 600°C for 60 min, make it vapor-deposit in the channels of the AAO template, and finally use 1mol / L NaOH solution to remove the AAO template, and obtain the carbon nanotube 2 array vertically grown on the gas diffusion layer 1 (VACNTs).

[0029] (2) In situ growth of Pt-based NWs

[0030] The gas diffusion layer 1 loaded with the VACNT array prepared above was immersed in 50ml concentratio...

Embodiment 2

[0036] According to the following steps, the catalytic layer fully ordered polyelectrolyte membrane fuel cell electrode and membrane electrode with N-doped VACNT array as the carrier were prepared, and the discharge test was carried out.

[0037] (1) In situ growth of N-doped VACNT arrays on the gas diffusion layer

[0038] After washing and drying a piece of AAO double-pass porous template with a size of 2.3cm×2.3cm (pore size is 30nm, thickness is 100μm), it is bonded with a piece of carbon paper of the same size as the gas diffusion layer 1, and placed in a tube furnace At 600°C, acetylene was passed through for 60 minutes to vapor-deposit it in the pores of the AAO template, and finally the AAO template was removed with 1 mol / L NaOH solution to obtain VACNTs grown vertically on the gas diffusion layer 1. Then, the gas diffusion electrode grown with VACNT was put into the tube furnace again, and NH was fed at a temperature of 500 °C 3 gas, the flow rate is 0.1slpm, and the...

Embodiment 3

[0041] According to the following steps, the catalytic layer fully ordered polyelectrolyte membrane fuel cell electrode and membrane electrode with S-doped VACNT array as the carrier were prepared, and the discharge test was carried out.

[0042] (1) In situ growth of S-doped VACNT arrays on the gas diffusion layer

[0043] Using the same method as in Example 1, VACNTs grown in situ on the gas diffusion layer 1 were firstly prepared. Then, the gas diffusion electrode grown with VACNT was placed in the tube furnace again, and H was introduced at a temperature of 500 °C 2 S gas, the flow rate is 0.1slpm, and the surface S-doped VACNT array is obtained

[0044] Step (2) in-situ growth of Pt-NW and step (3) membrane electrode assembly method are the same as in Example 1. Under the same conditions as in Example 1, the discharge test was carried out, and at a working voltage of 0.6V, the current density can reach 0.48A / cm 2 , the maximum power density reaches 0.82W / cm 2 .

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Abstract

The invention discloses a catalyst layer full-ordered fuel cell electrode and a membrane electrode, and relates to the technical field of fuel cells. An electrode catalyst layer is formed by an ordered carbon nano tube carrier and a platinum-based catalyst nanowire orderly grown on the carrier. Ionic conductors are uniformly distributed in the catalyst layer so as to form an ordered ion transmission channel, and ordered array structures of the carrier and the catalyst nanowire determine the orderliness of a gas-liquid transmission channel. A catalyst layer component and structure full-orderedelectrode and a polymer electrode plasma membrane are laminated to form the membrane electrode based on the catalyst layer component and structure full-orderliness. The full-ordered fuel cell electrode and the membrane electrode are capable of combining the efficient electron conduction and mass transfer features of an ordered carbon nano tube carrier array and the high activity and stability of the ordered platinum-based catalyst nanowire, and greatly improving the discharge performance and stability of the fuel cell electrode and the membrane electrode.

Description

technical field [0001] The invention relates to the technical field of fuel cells, in particular to a fully ordered fuel cell electrode and membrane electrode based on catalytic layer components and structures. Background technique [0002] Electrodes and membrane electrodes are the core components of proton exchange membrane fuel cells (PEMFC). They are the final places for multiphase material transport and electrochemical reactions that cause energy conversion, and determine the performance, life and cost of PEMFC. As early as 2013, the U.S. Department of Energy clearly stated in the "Fuel Cell Technical Roadmap" that the performance target of membrane electrodes in 2020 is to achieve a power density of 1.0W / cm 2 , the accelerated aging life can reach 5000h, and the cost is less than 14$ / kW. With the process of commercialization of PEMFC, people put forward a higher pursuit of its performance and life. [0003] However, in the current preparation of PEMFC electrodes and ...

Claims

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Application Information

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IPC IPC(8): H01M4/86H01M4/88H01M4/92H01M8/1004B82Y30/00
CPCB82Y30/00H01M4/8605H01M4/8657H01M4/8673H01M4/8828H01M4/926H01M8/1004Y02E60/50
Inventor 苏华能姚东梅张玮琦马强徐丽徐谦李华明
Owner 广东泰极动力科技有限公司