Device and method for preparing high-purity gamma-chloropropyl trichlorosilane
A technology of chloropropyltrichlorosilane and propyltrichlorosilane, which is applied in the field of equipment for preparing high-purity γ-chloropropyltrichlorosilane, and can solve the problems of high energy consumption, high operation precision, and excessive distillation still residue and other problems, to achieve the effect of reducing the difficulty of operation, high operation accuracy, and reducing the residual liquid in the kettle
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Embodiment 1
[0059] In this embodiment, the mass composition after the reaction of chloropropene and trichlorosilane is: 4.31% of chloropropene, 4.31% of trichlorosilane, 15.05% of silicon tetrachloride, 6.33% of propyl trichlorosilane, γ-chlorine Propyltrichlorosilane 69.5%, high boiler 0.5%.
[0060] Further, the reflux ratio of pre-separation rectification tower 1 is R=3, the operating pressure is 900kPa, and the number of theoretical plates is 30.
[0061] Further, the silicon tetrachloride removal tower 2 has a reflux ratio of R=7, an operating pressure of 260kPa, and a theoretical plate number of 30.
[0062] Further, the reflux ratio of the propyltrichlorosilane removal tower 3 is R=13, the operating pressure is 40kPa, and the number of theoretical plates is 30.
[0063] Further, the reflux ratio of the secondary rectification column 4 is R=125, the operating pressure is 40kPa, and the number of theoretical plates is 20.
[0064] Further, the γ-chloropropyltrichlorosilane removal ...
Embodiment 2
[0068] In this embodiment, the mass composition after the reaction of chloropropene and trichlorosilane is the same as that in Embodiment 1.
[0069] Further, the reflux ratio of pre-separation rectification tower 1 is R=3, the operating pressure is 900kPa, and the number of theoretical plates is 30.
[0070] Further, the silicon tetrachloride removal tower 2 has a reflux ratio of R=7, an operating pressure of 260kPa, and a theoretical plate number of 30.
[0071] Further, the reflux ratio of the propyltrichlorosilane removal tower 3 is R=13, the operating pressure is 40kPa, and the number of theoretical plates is 30.
[0072] Further, the reflux ratio of the secondary rectification column 4 is R=125, the operating pressure is 40kPa, and the number of theoretical plates is 20.
[0073] Further, the γ-chloropropyltrichlorosilane removal tower 5 has a reflux ratio of R=1, an operating pressure of 80 kPa, and a theoretical plate number of 30.
[0074] Further, the reflux ratio ...
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