Method for preparing low-mercury catalyst by employing high/middle-porosity active carbon
A technology for the preparation of activated carbon and low-mercury catalysts, applied in the field of fine chemistry, can solve the problems of high reaction temperature, high loss rate of mercuric chloride, poor thermal stability, etc., and achieve improved catalytic efficiency, shortened activation time, and lowered reaction temperature Effect
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Embodiment 1
[0027] Embodiment 1 A method for preparing low-mercury catalyst by adopting activated carbon with high and medium porosity
[0028] Step 1 Preparation of Activated Carbon
[0029] (1) Selection of raw coal
[0030] The raw coal is anthracite, with a moisture content of 6%, an ash content of 8.5%, a volatile matter content of 34.5%, and a fixed carbon content of 51%.
[0031] (2) Deashing of raw coal
[0032] Grind the anthracite, pass through a 100-mesh sieve, put the coal powder into a 30ppm polyaluminum chloride solution, stir vigorously at a speed of 5000r / min, after 2 minutes, reduce the speed to 500r / min, stir for 10 minutes, and filter , washed with distilled water until the filtrate is neutral; add polyacrylamide solution, the concentration of polyacrylamide is 0.5ppm, the rotation speed is 400r / min, after stirring for 10 minutes, filter, wash with distilled water until the filtrate is neutral, the ash content after deliming 1.5%.
[0033] (3) Carbonization
[...
Embodiment 2
[0056] Embodiment 2 above-mentioned catalyst is used for synthetic reaction of vinyl chloride
[0057] In the reaction that the catalyst of the present invention is used to prepare vinyl chloride by acetylene hydrochlorination, the molar ratio of the reaction feed gas is C 2 h 2 / HCl=1 / 1.1, the space velocity of acetylene is 67h -1 , the reaction temperature is 110°C, and the hydrogen chloride activation time is 20 minutes.
[0058] The reaction tail gas was analyzed by chromatography, and the conversion rate of acetylene was 99.94%, the yield of vinyl chloride was 95.6%, and the catalytic efficiency was improved by 4m 3 / h; the reaction temperature is reduced to 110°C, the reaction temperature of the prior art is above 130°C, and the hydrogen chloride activation time is shortened by 20%.
[0059] Unless otherwise specified, the percentages used in the present invention are all weight percentages, and the ratios described in the present invention are all mass ratios.
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