CO low temperature oxidation catalyst and its preparation process
A technology of oxidation catalyst and carbon monoxide, which is applied in the direction of metal/metal oxide/metal hydroxide catalyst, catalyst activation/preparation, physical/chemical process catalyst, etc. It can solve the problems of large environmental pollution and achieve high catalytic activity and low cost. The effect of low and high stability
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Embodiment 1
[0020] The catalyst was prepared by liquid phase precipitation method, and 17.4632g Co(NO 3 ) 2 ·6H 2 Dissolve O in 30ml of distilled water, add 4.0mol / L ammonium bicarbonate solution drop by drop under strong stirring until pH = 7.5, after the dropwise addition, raise the temperature to 30°C, react for 3 hours, filter and wash repeatedly with distilled water , dried in an oven at 80-120°C, and then placed in a muffle furnace and baked at 300°C for 3 hours in a flowing air atmosphere to obtain Co 3 o 4 Catalyst, the catalyst is a uniform black color. After tableting and sieving, the particles with a particle size of 40-60 mesh are taken.
[0021] The raw gas composition is CO: 0.5%, O 2 : 14.4%, N 2 : 85.1% (volume percentage), gas volume space velocity is 5000h -1 , when the reaction temperature is 25°C, the catalyst can keep catalytic CO completely converted to CO 2 360min.
Embodiment 2
[0023] The catalyst was prepared by liquid phase precipitation method, and 17.4632g Co(NO 3 ) 2 ·6H 2 Dissolve O in 30ml of distilled water, add 7.4mol / L ammonia water drop by drop under strong stirring until pH = 9.0, react at 25°C for 5 hours after the addition, then filter and wash repeatedly with distilled water, place in an oven for 80 Dry at -120°C, then place in a muffle furnace and bake at 300°C for 3 hours in a flowing air atmosphere to obtain Co 3 o 4 catalyst. The catalyst was uniformly black in color. After tableting and sieving, the particles with a particle size of 40-60 mesh are taken.
[0024] When using the raw material gas described in Example 1, the gas volume space velocity and the reaction temperature, the catalyst can keep catalytic CO fully converted into CO 2 120min.
Embodiment 3
[0026] Catalyst was prepared by liquid phase precipitation method, 14.9358g Co(CH3 COO) 2 4H 2 Dissolve O in 30ml of distilled water, add 4.0mol / L ammonium bicarbonate solution drop by drop at room temperature to pH = 6.5, or add dropwise in reverse order, after the dropwise addition, raise the temperature to 50°C, react for 2 hours, and filter And washed repeatedly with distilled water, dried in an oven at 80-120 °C, and then placed in a muffle furnace and roasted at 300 °C for 3 hours in a flowing air atmosphere to obtain Co 3 o 4 catalyst. Uniform black color in catalyst. After tableting and sieving, the particles with a particle size of 40-60 mesh are taken.
[0027] When using the raw material gas described in Example 1, the gas volume space velocity and the reaction temperature, the catalyst can keep catalytic CO fully converted into CO 2 150min.
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