Preparation method of methyldimethoxysilane
A technology of methyldimethoxyhydrogensilane and methylhydrogendichlorosilane, which is applied in the field of preparation of methyldimethoxyhydrogensilane, can solve the problem of uneven reaction, non-release of chlorosilane, and influence on the use of downstream products, etc. problem, to achieve the effect of improving product quality
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Embodiment 1
[0031] Add 250g methanol to the constant pressure dropping funnel A on the upper part of the esterification packed tower, add 292g methanol to the constant pressure dropping funnel B in the three-necked flask, and add 1000g methylhydrogendichlorosilane to the constant pressure dropping funnel C in the middle of the packed tower After the material preparation is completed, turn on the magnetic stirrer, and turn on the oil margin heating device outside the three-necked flask. After the oil margin temperature reaches 70°C, start to drop methanol from the upper part of the packed tower into the packed tower at a rate of 25.0g / h. Hydrogen dichlorosilane is dripped into the middle part of the packed tower at a speed of 90g / h, and the methanol in the lower part of the packed tower is dripped into a three-necked flask at a speed of 29.2g / h to carry out the esterification reaction, and the hydrogen chloride by-product is absorbed into hydrochloric acid by tap water. To avoid overflow of...
Embodiment 2
[0033] Add 280g methanol to the constant pressure dropping funnel A on the upper part of the esterification packed tower, add 250g methanol to the constant pressure dropping funnel B in the three-necked flask, and add 1000g methylhydrogendichlorosilane to the constant pressure dropping funnel C in the middle of the packed tower After the material preparation is completed, turn on the magnetic stirrer, and turn on the oil margin heating device outside the three-necked flask. After the oil margin temperature reaches 75°C, start to drop methanol from the upper part of the packed tower into the packed tower at a rate of 28.0g / h. Hydrogen dichlorosilane is dripped into the middle part of the packed tower at a speed of 100g / h, and the methanol in the lower part of the packed tower is dripped into a three-necked flask at a speed of 25.0g / h to carry out esterification reaction, and the by-product hydrogen chloride is absorbed into hydrochloric acid by tap water. To avoid the overflow o...
Embodiment 3
[0035] Add 265g of methanol to the constant pressure dropping funnel A on the upper part of the esterification packed tower, add 270g of methanol to the constant pressure dropping funnel B of the three-necked flask, and add 1000g of methylhydrogendichlorosilane to the constant pressure dropping funnel C in the middle of the packed tower , after the material preparation is completed, turn on the magnetic stirrer, and turn on the oil margin heating device outside the three-necked flask. After the oil margin temperature reaches 80°C, start to drop methanol from the upper part of the packed tower into the packed tower at a rate of 26.5g / h. Hydrogen dichlorosilane is dripped into the middle part of the packed tower at a speed of 110g / h, and the methanol in the lower part of the packed tower is dripped into the three-necked flask at a speed of 27.0g / h to carry out the esterification reaction, and the by-product hydrogen chloride is absorbed into hydrochloric acid by tap water. To avo...
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