A single tower reaction industrial preparation process of alkoxyhydrogensilane
A kind of technology of alkoxyhydrogensilane and preparation process, which is applied in the direction of silicon organic compounds, etc., can solve the problems of insufficient industrial preparation process, and achieve the effect of increasing product content
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Embodiment 1
[0021] Press the methanol and trichlorosilane raw materials into the metering tank and weigh the metering volume respectively. The methanol is divided into two metering tanks. Slowly raise the temperature of the kettle to 45°C, raise the temperature of the gas phase methanol evaporator to 110°C, feed the material after the temperature rise is completed, strictly control the mass ratio during the feeding process, trichlorosilane:gas phase methanol:liquid phase methanol=1:0.3:0.4 Control, the upper tower temperature is controlled at 20°C, the middle tower temperature is controlled at 70°C, and the lower tower is controlled at 56°C.
[0022] After the capacity of the crude product in the reaction kettle reaches saturation, it will be transported to the overflow kettle through pipelines for aging. The aging temperature is controlled at: 65°C and aged for two hours. Pour the aged crude product into the rectification kettle, and the temperature of the rectification kettle is slow. T...
Embodiment 2
[0024] Press the methanol and trichlorosilane raw materials into the metering tank and weigh the metering volume respectively. The methanol is divided into two metering tanks. Slowly raise the temperature of the kettle to 50°C, raise the temperature of the gas phase methanol evaporator to 115°C, feed the material after the temperature rise is completed, strictly control the mass ratio during the feeding process, trichlorosilane:gas phase methanol:liquid phase methanol=1:0.3:0.4 Control, the upper tower temperature is controlled at 25°C, the middle tower temperature is controlled at 75°C, and the lower tower is controlled at 55°C.
[0025] After the capacity of the crude product in the reaction kettle reaches saturation, it will be transported to the overflow kettle through pipelines for aging. The aging temperature is controlled at: 60°C, aged for two hours, and the aged crude product is poured into the rectification kettle, and the temperature of the rectification kettle is sl...
Embodiment 3
[0027] Press the methanol and trichlorosilane raw materials into the metering tank and weigh the metering volume respectively. The methanol is divided into two metering tanks. Slowly raise the temperature of the kettle to 50°C, raise the temperature of the gas phase methanol evaporator to 115°C, feed the material after the temperature rise is completed, strictly control the mass ratio during the feeding process, trichlorosilane:gas phase methanol:liquid phase methanol=1:0.3:0.4 Control, the temperature of the upper tower is controlled at 30°C, the temperature of the middle tower is controlled at 80°C, and the temperature of the lower tower is controlled at 60°C.
[0028] After the capacity of the crude product in the reaction kettle reaches saturation, it will be transported to the overflow kettle through pipelines for aging. The aging temperature is controlled at: 60°C, aged for two hours, and the aged crude product is poured into the rectification kettle, and the temperature ...
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