A system and method for organochlorosilane hydrolysis and hydrochloric acid refining
An organochlorosilane and refining system technology, applied in chemical instruments and methods, inorganic chemistry, chlorine/hydrogen chloride, etc., can solve the problems affecting the synthesis process of methyl chloride, increasing the frequency of shutdown and maintenance, and reducing the yield of siloxane. Achieve the effect of alleviating the problem of equipment blockage, increasing the economic benefits of the enterprise, and prolonging the equipment cycle
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specific Embodiment 1
[0033] Organogen hydrolyzate and hydrochloric acid purified system, such as figure 1 As shown, including the hydrolysis column 1, the primary phase separator 2, the secondary phase separator 3, the first hydrochloric acid purification column 4, a reduced tank 5, the second hydrochloric acid purification tower 6, the first extract tower 7, the second extraction The tower 8, the stripping tower 99 and the wire ring separation column 10, the side portion of the hydrolyzed column 1 is provided with a multi-segment feed port, the upper end of the hydrolyzed column 1 is connected to the feed port of the primary phase separator 2, level 1 The oil phase outlet of the phase separator 2 is connected to the feed port of the secondary phase separator 3, the top air phase outlet of the hydrolysis column 1, the gas phase outlet of the primary phase separator 2, and the air phase outlet of the secondary phase separator 3 are respectively connected. The top air phase outlet of the first hydrogera...
specific Embodiment 2
[0036] An organochlorosilane hydrolyzate and hydrochloric acid purification method, including the following steps:
[0037] (1) When 0-0.5 MpAg of the pressure-free diethylene dichlorosilane passes through the vaporizer 17 or after heating the liquid phase dimethyl dichloronilane, after heating through the heat exchanger 13, the segment is sent to the hydrolyzate tower 1 The hydrolysis reaction is performed, and the reaction temperature in the hydrolyzing tower 1 is controlled to 20-60 ° C, and the pressure is controlled to 0.5 MpAg, and the reaction is obtained to obtain a gas phase to the first condenser 11, and the reaction is obtained to obtain an oil phase to the primary phase separator. 2; the dimethyl dichlorosilane in the hydrolysis column 1 is used in a gas phase multi-segment feed, and the amount of dimethyl dichlorosily dichlorosily dichlorosilane is 40-90%, 40-5% and 20-5%;
[0038] (2) Control the primary phase separator 2 pressure to separate the oil and gas three-ph...
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