Palladium-based catalyst carrier for direct formic acid fuel cell and preparation method thereof
A formic acid fuel cell and catalyst carrier technology, applied in fuel cells, battery electrodes, electrochemical generators, etc., can solve the problems of poor interaction between carriers and active metal particles, insufficient stability of Pd catalysts, poor stability of carrier materials, etc. , to achieve the effects of reducing the loading of precious metals, making the preparation method simple and feasible, and improving the corrosion resistance
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specific Embodiment approach 1
[0023] Specific embodiment 1: A palladium-based catalyst carrier for a direct formic acid fuel cell in this embodiment is to add a precursor of tungsten, an intermediate of cerium and a carbon material into a solvent, and then undergo ultrasonic dispersion, drying, calcination and grinding to obtain Carrier WO 3 -CeO 2 @C; the precursor of tungsten is ammonium tungstate, ammonium paratungstate or ammonium metatungstate;
[0024] The intermediate of cerium is specifically prepared according to the following steps: the precursor of cerium is added to water to obtain a saturated solution of the precursor of cerium, and the saturated solution of the precursor of cerium is adjusted by using ammonia water with a mass percentage of 9% to 11%. The pH value of the cerium is 8-12, and then under stirring conditions, the temperature of the precursor saturated solution of cerium with a pH value of 8-12 is heated to 50°C-90°C, and the reaction is carried out at a temperature of 50°C-90°C ...
specific Embodiment approach 2
[0029] Embodiment 2: The difference between this embodiment and Embodiment 1 is that the cerium salt is cerium nitrate or cerium sulfate. Others are the same as in the first embodiment.
specific Embodiment approach 3
[0030] Specific embodiment three: the difference between this embodiment and specific embodiment one or two is that the precursor of cerium is added to water to obtain a saturated solution of the precursor of cerium, and the precursor of cerium is adjusted by using ammonia water with a mass percentage of 10% The pH value of the precursor saturated solution is 10, and then under stirring conditions, the temperature of the precursor saturated solution of cerium with a pH value of 10 is heated to 80 ° C, and the temperature is 80 ° C under the condition of reaction for 3 hours, after aging, filtering, Washing and drying give intermediates of cerium. Others are the same as in the first or second embodiment.
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