Preparation technology of methyl triethoxysilane
A technology for methyltriethoxysilane and a preparation process, which is applied in the field of preparation technology of methyltriethoxysilane, can solve the problems of discarding and no recovery method, achieves less side reactions, realizes recycling and reaction low temperature effect
Patent Information
- Authority / Receiving Office
- CN · China
- Current Assignee / Owner
- Publication Date
- 2015-12-02
Smart Images
Figure 1 Figure 2
Abstract
Description
technical field
[0001] The invention relates to a preparation process of organosilane, in particular to a preparation process of methyltriethoxysilane. Background technique
[0002] Methyltriethoxysilane is a common organosilicon material widely used in the rubber and pharmaceutical industries, mainly as a crosslinking agent for room temperature vulcanized silicone rubber, a glass fiber coupling It is used as an end-capping agent for siloxane polymers, and is also one of the important raw materials for the production of silicone resin, benzyl silicone oil, and waterproofing agent.
[0003] At present, the conventional preparation process of methyltrialkoxysilane is to prepare methyltrichlorosilane and ethanol through esterification reaction, and generate hydrogen chloride gas at the same time. However, during the alcoholysis reaction between methyltrichlorosilane and alcohol, the substitution reaction of the third chloro group in methyltrichlorosilane is very difficult, and...
Examples
Embodiment 1
[0032] A. alcoholysis
[0033] 150 parts by weight of methylhydrogendichlorosilane is first vaporized through a vaporizer, and then enters the bottom of the alcoholysis reaction tower through a stripper, and 190 parts by weight of absolute ethanol is added into the alcoholysis reaction tower in liquid form from the top inlet of the alcoholysis reaction tower , the upward gaseous methylhydrogendichlorosilane and the downward liquid anhydrous ethanol are fully contacted, alcoholysis reaction and hydrogen substitution occur, and methyl triethoxysilane and by-product hydrogen chloride are generated; the temperature control of the vaporizer and the stripper All at 55°C; alcoholysis reaction temperature is 45°C;
[0034] Most of the hydrogen chloride escapes through the outlet at the top of the alcoholysis reaction tower, and the remaining hydrogen chloride forms a product mixture with the reaction product;
[0035] B. Neutralization
[0036] Keep the temperature in the stripping ...
Embodiment 2
[0042] Change alcoholysis reaction temperature to be 60 ℃, all the other are the same as embodiment 1.
Embodiment 3
[0044] Change alcoholysis reaction temperature to be 70 ℃, all the other are the same as embodiment 1.