Continuous production method of propyl trialkoxysilane
A technology of propyltrialkoxysilane and propyltrichlorosilane, which is applied in the field of chemical synthesis, can solve the problems of many production by-products, poor product quality, and low product yield, and achieve low labor intensity, thorough reaction, The effect of high purity
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Embodiment 1
[0013] According to the usual raw material batching requirements, the reaction raw materials are propyltrichlorosilane and methanol with a total molar ratio of 1:4. Put propyltrichlorosilane and methanol into a pre-reactor (pre-esterification tank) through the insertion tube according to the molar ratio of 1:2.4. At normal temperature, a preliminary reaction is carried out in the pre-esterification tank. The flow enters the tower reactor (esterification tower), and the remaining amount of methanol is vaporized and heated to a temperature of 150°C through two vaporization tanks in sequence. The gaseous alcohol vapor enters from the lower part of the esterification tower. After contacting the pre-esterification solution entering the reactor, the reaction is continued until complete, and the hydrogen chloride generated by the reaction is removed, and the vacuum degree of the reaction system is maintained at 0.02MPa.
[0014] The hydrogen chloride produced by the reaction is absor...
Embodiment 2
[0016] Ratio of reaction raw materials: the total molar ratio of propyltrichlorosilane and methanol is 1:4;
[0017] The add-on of methyl alcohol is 65% in the preliminary reaction;
[0018] The remaining amount of methanol is vaporized and heated to a temperature of 145°C;
[0019] The vacuum degree of the reaction system was kept at 0.015MPa.
[0020] Others are with embodiment 1.
Embodiment 3
[0022] Ratio of reaction raw materials: the total molar ratio of propyltrichlorosilane and methanol is 1: 3.5;
[0023] The add-on of methyl alcohol is 60% in the preliminary reaction;
[0024] The remaining amount of methanol is vaporized and heated to a temperature of 155°C;
[0025] The vacuum degree of the reaction system was kept at 0.02MPa.
[0026] Others are with embodiment 1.
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