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Preparation method of platinum-ruthenium alloy catalyst for fuel cell anode

A platinum-ruthenium alloy and fuel cell technology, applied in battery electrodes, circuits, electrical components, etc., can solve problems such as uneven agglomeration and inhomogeneity, and achieve excellent performance, reduced oxidation overpotential, and good resistance to carbon monoxide poisoning. Effect

Pending Publication Date: 2022-01-04
SINOSTEEL ANHUI TIANYUAN TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] The object of the present invention is to provide a method for preparing a platinum-ruthenium alloy catalyst reduced by bubbling with a mixed gas, which can solve the problem of inhomogeneous mixing of two precious metals to form phase separation during the preparation of a PtRu alloy catalyst by dry or wet reduction structure, or severe agglomeration and inhomogeneity, and without the need for high-temperature roasting and alloying steps, the quality of PtRu / C catalyst products is significantly improved and the cost is reduced

Method used

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  • Preparation method of platinum-ruthenium alloy catalyst for fuel cell anode
  • Preparation method of platinum-ruthenium alloy catalyst for fuel cell anode
  • Preparation method of platinum-ruthenium alloy catalyst for fuel cell anode

Examples

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Effect test

Embodiment 1

[0025] Take 5.18g of chloroplatinic acid and 2.07g of ruthenium trichloride, and dissolve them in 200mL of deionized water. Fully homogenize into a slurry, pump the reaction liquid into the bubbling reactor, and blow in the mixed gas of hydrogen and carbon monoxide (H 2 / CO=1:0.5), no inert gas was used as diluent gas, and the bubbling flow rate was 3 L / min. During this process, the reaction solution was heated to 60° C., and the reaction time was 10 h. After the reaction was completed, the reaction liquid was discharged from the reaction kettle, filtered and washed, and the filter cake was dried in a vacuum oven at 60°C to obtain the catalyst product, which was recorded as #1-1.

Embodiment 2

[0029] Take 3.93g of platinum acetylacetonate and 1.75g ​​of ammonium chlororuthenate, and dissolve them in 100mL of deionized water. After the substance is a slurry, the reaction solution is pumped into the bubbling reactor, and a mixture of hydrogen and carbon monoxide (H 2 / CO=1:0.5), using 40% volume of argon as the diluent gas, and the bubbling flow rate was 1.5 L / min. During this process, the reaction solution was heated to 75°C, and the reaction time was 5h. After the reaction was completed, the reaction solution was discharged from the kettle, filtered and washed, and the filter cake was placed in a vacuum drying oven at 70°C and dried overnight to obtain the catalyst product, which was designated as #2-1.

Embodiment 3

[0031] Potassium chloroplatinate (K 2 PtCl 6) 4.86g, potassium chlororuthenate 0.392g, dissolved in 25mL deionized water, fully dissolved and uniform, added 2.5g of XC-72R carbon carrier and 0.125g of PVP K-30 as a dispersant, using high-speed homogenizer After the machine is fully homogenized into a slurry, the reaction solution is pumped into the bubbling reaction kettle, and a mixed gas of hydrogen and carbon monoxide (H 2 / CO=1:0.1), nitrogen was used as the diluent gas, and the volume ratio of hydrogen to nitrogen was 1:0.2. The bubbling flow rate was 0.5 L / min. During this process, the reaction solution was heated to 90° C., and the reaction time was 2 h. After the reaction was completed, the reaction solution was discharged from the kettle, filtered and washed, and the filter cake was placed in a vacuum drying oven at 80°C and dried overnight to obtain the catalyst product, which was designated as #3-1.

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Abstract

The invention discloses a preparation method of a platinum-ruthenium alloy catalyst for a fuel cell anode. The preparation method comprises the following steps: preparing a metal salt solution from a platinum salt solution and a ruthenium salt solution; adding a carbon carrier and an additive into the obtained metal salt solution, stirring, homogenizing and dispersing to obtain a reaction solution; putting the obtained reaction liquid into a bubbling reaction kettle, introducing reaction gas containing hydrogen and carbon monoxide, and carrying out bubbling reduction reaction; and after the bubbling reduction reaction is completed, discharging the obtained reaction liquid from the reaction kettle, filtering, and drying a filter cake to obtain the platinum-ruthenium alloy catalyst. According to the method, the two major problems that in the process of preparing the PtRu alloy catalyst through dry or wet reduction, the two precious metals are not uniformly mixed to form a split-phase structure, or serious agglomeration is not uniform can be solved, the step of high-temperature roasting alloying is not needed, the quality of the PtRu / C catalyst product is remarkably improved, and the cost is reduced.

Description

technical field [0001] The invention relates to the technical field of catalyst preparation, in particular to a method for preparing a platinum-ruthenium alloy catalyst for fuel cell anodes. Background technique [0002] In the anode of the proton exchange membrane fuel cell, pure hydrogen is needed as the fuel gas, and the electrochemical reaction occurs under the action of the catalyst to generate protons, and the chemical energy can be directly converted into electrical energy without fuel. However, at present, hydrogen produced on an industrial scale is usually obtained from liquid hydrocarbon fuels such as methanol, ethanol, gasoline, or natural gas through steam reforming or partial oxidation. These hydrogen production processes will generate about 1-2% hydrogen in the product Carbon monoxide (CO) impurities. Although in the subsequent hydrogen purification process, the concentration of CO can be reduced to less than 100ppm within an acceptable cost range after two pu...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): H01M4/88H01M4/92
CPCH01M4/8825H01M4/921H01M2004/8684Y02E60/50
Inventor 邓翔裴晓东骆艳华
Owner SINOSTEEL ANHUI TIANYUAN TECH