Non-noble metal fuel cell oxygen reduction electrocatalyst

A fuel cell and electrocatalyst technology, applied in battery electrodes, circuits, electrical components, etc., can solve the problems of catalyst catalytic activity and stability gap, high preparation cost, expensive and other problems, which is conducive to large-scale production and reduces preparation Cost and manpower saving effect

Inactive Publication Date: 2010-10-13
CHONGQING UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

For example, patent CN101069857A discloses a halogen-substituted dinuclear phthalocyanine iron oxide reduction catalyst; patent CN101417242A discloses a composite non-noble metal oxygen reduction catalyst, etc. The disadvantage of this method is that the preparation process is complicated, the reaction conditions are harsh, and the yield is low Macrocyclic compounds such as porphyrin and phthalocyanine are also relatively expensive materials, and the preparation cost is high; the catalyst prepared by this method also has a gap with platinum-based catalysts in terms of catalytic activity and stability (Rajesh Bashyam, Piotr Zelenay.A class of non-precious metal composite catalysts for fuel cells. Nature, 443 (2006) 63-66)

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0018] This embodiment uses cobalt chloride (CoCl 2 ·6H 2 O), melamine, acetylene black prepare fuel cell oxygen reduction electrocatalyst of the present invention, and this catalyst is represented by CoMe / C, and wherein Me represents that nitrogen source is melamine, and C represents acetylene black.

[0019] (1) Acetylene black pretreatment: Acetylene black is treated with 1.5M HNO before use 3 Stir for 10 hours, then wash and dry for later use.

[0020] (2) Cobalt chloride (CoCl 2 ·6H 2 O), melamine, and acetylene black were ground in an agate mortar for 30 minutes to make the precursors uniformly mixed.

[0021] (3) Divide the precursor mixture into three equal parts, put them into three ceramic boats, and then transfer the ceramic boats to the middle of the tubular resistance furnace.

[0022] (4) The tubular resistance furnace is fed into N 2 protective gas.

[0023] (5) Heat treatment at 600°C for 2 hours: use step-by-step heating, keep at 100°C, 200°C, 300°C, 40...

Embodiment 2

[0028] According to the method step of embodiment 1, the Vulcan XC-72R carbon black of U.S. Cabot Company is used to replace acetylene black to prepare catalyst, all the other conditions are unchanged, the gained catalyst is marked as CoMe / V, and " V " represents VulcanXC-72R carbon black.

[0029] Figure 4 It is the fuel cell oxygen reduction catalyst CoMe / V that embodiment 2 obtains at 0.5M H 2 SO 4Electrocatalytic activity in solution. The scanning speed is 5mV / s, and the test temperature is 30°C. It can be seen that the oxygen reduction catalysts obtained with two different carbon blacks have similar catalytic activities. Therefore, it is of practical value to use acetylene black as a raw material for preparing catalysts.

Embodiment 3

[0031] According to the method steps of Example 1, an equivalent amount of hexamethylenetetramine was used instead of melamine to prepare the catalyst, and the other conditions were unchanged. The obtained catalyst was marked as CoHMTA / C, and "HMTA" means hexamethylenetetramine.

[0032] Figure 5 It is the fuel cell oxygen reduction catalyst CoHMTA / C that embodiment 3 obtains at 0.5M H 2 SO 4 Electrocatalytic activity in solution. The scanning speed is 5mV / s, and the test temperature is 30°C. It can be seen that CoHMTA / C also has good catalytic activity for oxygen reduction.

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Abstract

The invention relates to a non-noble metal fuel cell oxygen reduction electrocatalyst which is a product obtained by a method comprising the steps of: (1) pretreatment of acetylene black; (2) mechanical grinding: mixing cobalt chloride (CoC12. 6H2O), nitrogen source (melamine or hexamethylene tetramine) and carbon black (acetylene black or Vulcan XC-72R) which have the mass ratio of 1: 2: 10 into a mortar for mechanical grinding for 30min until even dispersion; and (3) heat treatment: adopting a way of sectional type temperature rise under the nitrogen protection, namely, maintaining for 10min when raising 100 DEG C at every time, then raising the temperature again, and so on; finally, maintaining for 1-5h at the required temperature (500-900 DEG C), and stopping heating; and naturally cooling to the room temperature, and then closing nitrogen. The non-noble metal fuel cell oxygen reduction electrocatalyst is low in the price of raw materials, and greatly reduces the preparation cost of oxygen reduction catalyst. The method is simple, convenient and easy, and is suitable for large-scale production and preparation of the catalyst.

Description

technical field [0001] The invention belongs to the field of fuel cell catalysts, and more specifically relates to a non-noble metal fuel cell oxygen reduction electrocatalyst. Background technique [0002] The oxygen reduction reaction of current fuel cells requires the use of expensive platinum-based catalysts with poor methanol resistance, which hinders its large-scale application. Therefore, the research on cathode oxygen reduction catalysts with low price, good stability, good catalytic activity and methanol tolerance is of key significance for the large-scale commercial application of proton exchange membrane fuel cells. [0003] In the past few decades, a variety of non-precious metal or non-platinum catalysts have been developed, among which N 4 - Metal complex catalysts for macrocyclic compounds and derivatives (referred to as TM-N 4 type) is a very important class (Cicero W.B.Bezerra, Lei Zhang, Kunchan Lee, etc. A review of Fe-N / C and Co-N / C catalysts for the ox...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): H01M4/90H01M4/88
CPCY02E60/50
Inventor 司玉军陈昌国尹伟蔡慧
Owner CHONGQING UNIV
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