Catalyst for removing H2S from gas by catalytic oxidation, preparation method and application
A catalytic oxidation and catalyst technology, which is applied in the catalytic conversion of impurities, gas purification, etc., can solve the problem of low sulfur capacity, achieve the effects of improving desulfurization activity and selectivity, realizing recycling, and increasing the penetration of sulfur capacity
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Embodiment 1
[0018] Mn(NO 3 ) 2 Solution, uniformly impregnated an equal volume on 30-60 mesh 5g activated carbon, placed at room temperature for 6h, dried at 60°C for 10h, dried at 100°C for 10h, and then calcined at 400°C for 4h in a nitrogen atmosphere to obtain 1% Mn / AC catalyst. The catalyst is loaded into a fixed bed reactor, the reaction temperature is controlled at 180°C, and the space velocity is 3000h -1 , H in raw gas 2 S content 3000ppm, pass O 2 / H 2 O with an S ratio of 1:1 2 , balance gas N 2 , its breakthrough sulfur capacity is 14.2%, and its desulfurization efficiency is 99.2%.
Embodiment 2
[0020] Fe(NO 3 ) 3 Solution, uniformly impregnated an equal volume on 5g activated carbon of 30-60 mesh, placed at room temperature for 3h, dried at 60°C for 8h, dried at 100°C for 10h, and then calcined at 300°C for 3h in a nitrogen atmosphere to obtain Fe / AC with a mass percentage of 0.1%. catalyst. The catalyst is loaded into a fixed bed reactor, the reaction temperature is controlled at 150°C, and the space velocity is 8000h -1 , H in raw gas 2 S content 2500ppm, pass O 2 / H 2 O with an S ratio of 1:2 2 , CO30%, H 2 40%, CO 2 21%, CH 4 1.7%, balance gas N 2 . Its breakthrough sulfur capacity is 5.82%, and its desulfurization efficiency is 99.2%.
Embodiment 3
[0022] A vanadium concentration of 0.0747g / ml NH 4 VO 3 An equal volume of oxalic acid solution was uniformly impregnated onto 5g activated carbon of 30-60 mesh, placed at room temperature for 3 hours, dried at 50°C for 4 hours, dried at 100°C for 8 hours, and then calcined at 450°C for 3 hours in a nitrogen atmosphere to obtain V / AC catalyst. The catalyst is loaded into a fixed bed reactor, the reaction temperature is controlled at 250°C, and the space velocity is 8000h -1 , H in raw gas 2 S content 2500ppm, pass O 2 / H 2 O with an S ratio of 1:2 2 , CO30%, H 2 40%, CO 2 21%, CH 4 1.7%, balance gas N 2 . Its breakthrough sulfur capacity is 3.82%, and its desulfurization efficiency is 96.5%.
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