A kind of preparation method of methyldimethoxyhydrosilane
A technology of methyldimethoxyhydrogensilane and methylhydrogendichlorosilane, which is applied in the field of preparation of methyldimethoxyhydrogensilane, can solve uneven reaction, affect the use of downstream products, and decrease product yield. problem, to achieve the effect of improving product quality
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Embodiment 1
[0034] 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 bath heating device outside the three-necked flask. After the oil bath 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 of the packed tower at a rate of 90g / h, and methanol in the lower part of the packed tower is dripped into a three-necked flask at a rate of 29.2g / h for esterification, and the by-product hydrogen chloride is absorbed by tap water to prepare hydrochloric acid. To avoid overflow of hydrogen chloride and pollute ...
Embodiment 2
[0036]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 bath heating device outside the three-necked flask. After the temperature of the oil bath 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 of the packed tower at a rate of 100g / h, and methanol in the lower part of the packed tower is dripped into a three-necked flask at a rate of 25.0g / h for esterification, and the by-product hydrogen chloride is absorbed by tap water to prepare hydrochloric acid. To avoid the overflow of hydrogen chloride a...
Embodiment 3
[0038] 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 bath heating device outside the three-necked flask. After the temperature of the oil bath reaches 80°C, start to drop the methanol on 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 of the packed tower at a rate of 110g / h, and methanol in the lower part of the packed tower is dripped into a three-necked flask at a rate of 27.0g / h for esterification, and the by-product hydrogen chloride is absorbed by tap water to prepare hydrochloric acid. To avoid the overflow of hydro...
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