141-57-1Relevant articles and documents
The hydrosilylation of propylene
Chernyshev,Belyakova,Yagodina,Nikitinskii,Bykovchenko
, p. 1992 - 1995 (1998)
The reactions of separate and competitive hydrosilylation of propylene with HSiCl3, MeSiHCl2, Me2SiHCl, and MePh2SiH in the presence of the Speier catalyst (SC) with different additives and a catalyst obtained from SC and propylene were studied. A mutual influence of the hydrosilanes in the competitive reactions was found. The influence of various additives to SC on the process was considered.
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Booth,Halbedel
, p. 2652 (1946)
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Method for preparing propyl trichlorosilane by using tail gas propylene in chloropropyl chlorosilane production process
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Paragraph 0021-0031, (2021/07/10)
The invention relates to a method for preparing propyl trichlorosilane by using tail gas propylene in a chloropropyl chlorosilane production process, and belongs to the technical field of fine chemical engineering. According to the method, by-product tail gas propylene generated in the production process of chloropropyl chlorosilane is used as a raw material and is subjected to an addition reaction with trichlorosilane under stirring, and distillation is performed to obtain a propyltrichlorosilane product. As a silane intermediate, propyl trichlorosilane can be used as a cross-linking agent, a coupling agent, a building waterproofing agent, a powder treating agent and many other material industries of RTV silicone rubber after hydrolysis, alcoholysis and acylation. The method has the advantages of simple equipment process and byproduct raw materials, not only creates huge economic benefits, but also solves the problems of safety, environmental protection and occupational health of tail gas propylene in the production process of chloropropyl chlorosilane, and is suitable for industrial production.
PREPARATION OF ORGANOHALOSILANES
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Page/Page column 17, (2011/12/14)
A process for preparing organohalosilanes comprising combining hydrogen, a halosilane having the formula HaSiX4-a (I), and an organohalide having the formula RX (II), wherein R is C1-C10 alkyl or C4-C10 cycloalkyl, each X is independently halo, and the subscript a is 0, 1, or 2, in the presence of a sufficient amount of a catalyst effective in enabling the replacement of one or more of the halo groups of the halosilane with the R group from the organohalide, at a temperature from 200 to 800 °C, to form an organohalosilane and a hydrogen halide, wherein the volumetric ratio of hydrogen to halosilane is from 1 :3 to 1 :0.001 and the volumetric ratio of hydrogen to organohalide is from 1 : 1 to 1 :0.001, and wherein the catalyst is optionally treated with the hydrogen or the halosilane prior to the combining.