Reactive distillation purifying method and device for removing carbon-containing impurities in chlorosilane
A technology of reactive distillation and reactive distillation tower, which is applied in the field of reactive distillation purification and equipment for removing carbon-containing impurities in chlorosilane, can solve the problems that methyldichlorosilane cannot be removed, and has not been raised, so as to achieve thorough removal, Less equipment investment, high purity effect
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example 1
[0035] The chlorosilane raw material enters the reactive distillation column from the top to the middle of the second and third fillers in the rectification section, and dichloromethane enters the reactive distillation column from the middle of the rectification section and the reaction section, and the rectification section is filled with three Sectional wire mesh corrugated packing, 5m per section; 6m of wire mesh corrugated packing is filled in the stripping section; 1m of wire mesh corrugated packing and 1m of structural catalyst are alternately filled in the reaction section of the tower from bottom to top, a total of 4 sections of 8m, and the catalyst is 1 % nickel-supported alumina catalyst, the temperature at the top of the tower is controlled between 30°C and 35°C, and the cooling medium of the condenser is 10°C circulating water. The operating pressure of the reactive distillation tower is controlled at 70Kpa, the temperature of the tower tank is about 80°C, the tempe...
example 2
[0037] The chlorosilane raw material enters the reactive distillation column from the top to the bottom of the middle of the second and third fillers in the rectification section, and chloroform enters the reactive distillation column from the middle of the rectification section and the reaction section, and the rectification section is filled with three Sectional orifice corrugated packing, 5m per section; 6m of orifice corrugated packing is filled in the stripping section, 1m of wire mesh corrugated packing and 1m of structural catalyst are alternately filled in the reaction section of the tower from bottom to top, a total of 5 sections of 10m, and the catalyst is 1 % iron-loaded molecular sieve catalyst, the temperature at the top of the tower is controlled between 30°C and 35°C, and the cooling medium of the condenser is 10°C circulating water. The operating pressure of the reactive distillation tower is controlled at 150Kpa, the temperature of the tower bottom is about 90°...
example 3
[0039] The chlorosilane raw material enters the reactive distillation tower from the middle of the second and third fillers from top to bottom in the rectification section, and silicon tetrachloride enters the reactive distillation tower from the middle of the rectification section and the reaction section, and the filling in the rectification section Three sections of grid packing, 4m in each section; 6m of wire mesh corrugated packing in the stripping section; 1m of wire mesh corrugated packing and 1m of structural catalyst alternately filled in the reaction section of the tower from bottom to top, a total of 4 sections of 8m, the catalyst is 1 % copper-loaded artificial zeolite catalyst, the temperature at the top of the tower is controlled between 45°C and 50°C, and the cooling medium of the condenser is circulating water at 10°C. The operating pressure of the reactive distillation tower is controlled at 200Kpa, the temperature of the tower bottom is about 100°C, the temper...
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