Catalyst for hydrolysis of carbonyl sulfide as well as preparation method and application thereof
A catalyst, carbonyl sulfide technology, applied in the field of carbonyl sulfide hydrolysis catalyst and its preparation, can solve the problem of low removal rate, achieve the effect of low applicable temperature, excellent hydrolysis ability, and high resistance to sulfation
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[0032] In the second aspect, the embodiment of the present invention provides a method for preparing the above-mentioned catalyst, comprising: preparing an aqueous solution with a concentration of 7-15% of the active component, and then impregnating the carrier in the active component at 20-25°C In the divided aqueous solution for 2-4 hours, the active component is loaded on the carrier, then dried at 120-150°C for 3-5 hours, and finally roasted at 450-500°C to obtain the desired catalyst;
[0033] Wherein, in the prepared catalyst, the weight of the active component is 5-10% of the weight of the catalyst.
[0034] It can be understood that in this preparation method, the carrier used is selected from the group with a particle size of 4-6mm, a pore volume of 0.35-0.45ml / g, and a specific surface area of 300-350m 2 / g of activated alumina and / or activated titanium oxide. The active components used are selected from at least one of the oxides of alkali metals, alkaline earth ...
Embodiment 1
[0049] This embodiment provides a catalyst for the hydrolysis of carbonyl sulfide in natural gas, the catalyst comprising 93% (weight percent) activated alumina and 7% (weight percent) yttrium oxide supported on the activated alumina. Among them, the particle size of activated alumina is 5mm, the pore volume is 0.4ml / g, and the specific surface area is 300m 2 / g.
[0050] The preparation method of this catalyst is as follows:
[0051] Prepare an aqueous solution of yttrium oxide with a concentration of 10%, and then immerse activated alumina in the aqueous solution of yttrium oxide at 25°C for 3 hours to load yttrium oxide on the activated alumina, and then dry it at 135°C It was treated for 3.5 hours, and finally calcined at 450° C. to obtain the desired catalyst.
Embodiment 2
[0053] This embodiment provides a catalyst for the hydrolysis of carbonyl sulfide in natural gas, the catalyst includes 92% (weight percent) active titanium oxide and 8% (weight percent) rubidium oxide supported on the active titanium oxide. Among them, the particle size of activated titanium oxide is 4mm, the pore volume is 0.35ml / g, and the specific surface area is 250m 2 / g.
[0054] The preparation method of this catalyst is as follows:
[0055] Prepare an aqueous solution of rubidium oxide with a concentration of 12%, and then immerse the active titanium oxide in the aqueous solution of rubidium oxide at 22°C for 3 hours to load the rubidium oxide on the active titanium oxide, and then dry it at 130°C It was treated for 4 hours, and finally calcined at 500° C. to obtain the desired catalyst.
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