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Anti-reverse nitrogen-carbon carrier catalyst for proton exchange membrane fuel cell and preparation method of anti-reverse nitrogen-carbon carrier catalyst

A proton exchange membrane and fuel cell technology, applied in battery electrodes, circuits, electrical components, etc., can solve the problems of electrolytic water oxidation reaction activity decline, instability, unreliable vehicle operation, etc., to achieve stability, easy cleaning, and inhibition Effects of Migration and Reunion

Pending Publication Date: 2022-07-29
国家电投集团氢能科技发展有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, during the test, the traditional "anti-reversal" catalysts will quickly aggregate the metal active sites, resulting in a sharp drop in the activity of the electrolytic water oxidation reaction, which leads to the inability of the traditional "anti-reverse" catalysts to be long-term and efficient. Inhibit the progress of carbon carrier oxidation reaction, resulting in unreliable and unstable vehicle operation

Method used

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  • Anti-reverse nitrogen-carbon carrier catalyst for proton exchange membrane fuel cell and preparation method of anti-reverse nitrogen-carbon carrier catalyst
  • Anti-reverse nitrogen-carbon carrier catalyst for proton exchange membrane fuel cell and preparation method of anti-reverse nitrogen-carbon carrier catalyst
  • Anti-reverse nitrogen-carbon carrier catalyst for proton exchange membrane fuel cell and preparation method of anti-reverse nitrogen-carbon carrier catalyst

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preparation example Construction

[0036] like figure 1 As shown, the preparation method of the anti-reverse polar nitrogen-carbon supported catalyst for the proton exchange membrane fuel cell according to the embodiment of the present invention includes the following steps:

[0037] a. Dissolving the transition metal salt, the nitrogen source and the carbon source in the first dispersant to obtain a nitrogen-doped metal organic framework;

[0038] b. Dissolving the nitrogen-doped metal-organic framework and the composite pore-forming agent in a second dispersant, mixing and stirring, drying and then placing it in a first sintering atmosphere for sintering treatment to obtain a carrier porous metal nitrogen-carbon material, wherein the The composite pore-forming agent includes a first pore-forming agent and a second pore-forming agent, and the first pore-forming agent includes at least one of ammonium chloride, ammonium carbonate, ammonium sulfate, and ammonium bicarbonate; the second pore-forming agent Includ...

Embodiment 1

[0058] (1) dissolving zinc nitrate and cobalt nitrate in methanol, adding them to methanol containing 2-methylimidazole, stirring and mixing, washing and drying to obtain nitrogen-doped metal organic framework;

[0059] (2) Dissolve the composite pore-forming agent composed of nitrogen-doped metal-organic framework, ammonium chloride and sodium chloride in water, wherein the mass ratio of metal-organic framework and composite pore-forming agent is 1:5, ammonium chloride and chlorine The mass ratio of sodium chloride is 1:6, fully stirring and mixing at 90 °C, rotary evaporation, drying and grinding, and then sintering at 900 °C for 3 hours in a nitrogen atmosphere to obtain a carrier porous metal carbonitride material, wherein the nitrogen content is 12.8%, zinc content is 0% (Zn atom evaporates at high temperature), cobalt content is 2%, the porous metal nitrogen carbon material is first washed with ultrapure water, and then placed in a nitric acid aqueous solution of 60°C and...

Embodiment 2

[0063] (1) Ferric chloride and zinc chloride are dissolved in ethanol, and added to the ethanol containing dicyandiamide and trimesic acid (the mass ratio of the two is 8:2), stirred and mixed, and rotary evaporated and dried to obtain a mixed solution. Nitrogen metal organic framework;

[0064] (2) Dissolve the composite pore-forming agent composed of nitrogen-doped metal-organic framework, ammonium carbonate and sodium chloride in water, wherein the mass ratio of metal-organic framework and composite pore-forming agent is 1:3, and the mass ratio of ammonium carbonate and sodium chloride is 1:3. The ratio is 1:3, fully stirring and mixing at 60 ° C, rotary evaporation, drying and grinding, and sintering at 1100 ° C in an argon atmosphere for 2 hours to obtain a carrier porous metal nitrogen carbon material, wherein the nitrogen content is 11.5% , the iron content is 3%, the zinc content is 0%, the porous metal nitrogen carbon material is first washed with ultrapure water, and...

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Abstract

The preparation method comprises the following steps: a, dissolving transition metal salt, a nitrogen source and a carbon source in a first dispersing agent to obtain a nitrogen-doped metal organic framework; b, dissolving the nitrogen-doped metal organic framework and a composite pore-forming agent in a second dispersing agent, mixing and stirring, drying, and sintering in a first sintering atmosphere to obtain a carrier porous metal nitrogen carbon material; and c, adding the porous metal nitrogen-carbon material and the noble metal precursor into a third dispersing agent, heating, drying, and sintering in a second sintering atmosphere to obtain the anti-reverse-pole catalyst. According to the preparation method, migration and agglomeration of the iridium-based compound can be effectively inhibited, the stability of the catalyst is improved, and the catalyst has excellent performance of high activity and high stability.

Description

technical field [0001] The invention belongs to the technical field of fuel cells, in particular to an anti-reverse polar nitrogen carbon carrier catalyst for a proton exchange membrane fuel cell, and further relates to a preparation method of the anti-reverse polar nitrogen carbon carrier catalyst for the proton exchange membrane fuel cell. Background technique [0002] Proton exchange membrane fuel cell is a kind of fuel (such as H 2 ) and oxidizing agents (such as O 2 ) directly converts the chemical energy into electrical energy, and the energy conversion process of the system is not limited by the thermodynamic Carnot cycle. Its working principle is fuel (such as H 2 ) in the anode oxidation reaction to generate H + and e - , H + It is transmitted to the cathode through the proton exchange membrane, and e- flows to the cathode through the external circuit, so that the oxidant of the cathode (such as O 2 ) and H + and e - Combined with a reduction reaction to gen...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): H01M4/86H01M4/88H01M4/92
CPCH01M4/926H01M4/861H01M4/8636H01M4/88
Inventor 陈立刚赵维刘敏张纪廷王晓冉柴茂荣
Owner 国家电投集团氢能科技发展有限公司
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