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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

Active Publication Date: 2019-01-15
JINGZHOU JIANGHAN FINE CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The first method is the esterification method: that is to use methylhydrogendichlorosilane and methanol as raw materials, and carry out esterification reaction under the action of solvent and hydrochloric acid absorbent to synthesize methyldimethoxyhydrogensilane products. Both are in the stage of small laboratory tests, but because the selected hydrochloric acid adsorbent forms a complex with chlorosilane, the absorbent forms a precipitate with HCl on the one hand, and complexes with methyldichlorohydrogensilane on the other hand. Chlorosilane cannot be released from the complex well, and due to the generation of precipitation, the reaction complex product is wrapped, making the reaction uneven. Therefore, the product yield decreases after the absorbent is used, resulting in methyl di The synthesis process of methoxyhydrosilane has not been industrialized
[0005] The second method is the group exchange method: that is to use methyltrimethoxysilane and methyldichlorohydrosilane to carry out group exchange reaction to synthesize methyldimethoxyhydrogensilane products, such as the patent introduction of CN 1410431A , the group exchange process has advantages in principle and process over the above-mentioned esterification process. After reading the patent literature carefully, it can be learned that the methyl dimethoxyhydrosilane product synthesized according to the method provided by the patent must contain methyl A methoxyhydrochlorosilane component, so the synthesized product is acidic, which affects the use of downstream products

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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PUM

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Abstract

The invention relates to the technical field of fine chemical engineering, and in particular relates to a preparation method of methyldimethoxysilane. The preparation method disclosed by the invention is characterized in that methyldichlorosilane and methanol sufficiently react in a packed tower by adopting a one-step esterification process, and Si-Cl bonds of methylhydrochlorosilane are completely converted into Si-O bonds, and the reaction efficiency is high; after the reaction is ended, a crude product is neutralized by hexamethylenetetramine, and then is filtered and distilled and the like to obtain a methyldimethoxysilane product with the mole yield of 99.5 percent or above. The mole yield of a product prepared by the preparation method disclosed by the invention reaches 95.0 percent or above, and the product is neutral, so the use of downstream customers is not affected; in addition, a used neutralizer does not react with the methylhydrochlorosilane or the methyldimethoxysilane product; by-produced hexamethylene tetramine hydrochloride does not cake, is proper in particle size and easy to filter, and is suitable for industrial production.

Description

technical field [0001] The invention relates to the technical field of fine chemicals, in particular to a preparation method of methyldimethoxyhydrogensilane. Background technique [0002] Methyldimethoxyhydrogensilane contains both hydrolyzed alkoxy linkages (Si-OCH 3 ), which also contains active silicon-hydrogen bonds (Si-H), where Si-OCH 3 The bonds are converted into siloxanes through hydrolysis and condensation; reacting with Grignard reagents can generate organoalkoxysilanes; Si-H bonds can undergo hydrosilylation with a series of unsaturated compounds such as alkenes and alkynes under platinum catalysts Synthetic reaction to obtain various silicone coupling agents, silicone-terminated and cured polyethers, polyacrylate sealants and adhesives, etc., and is suitable for the preparation of many high-purity silicone compounds, such as modified silanes Sealants, anti-fogging agents, water repellents, silane coupling agents such as vinyl, epoxy and methacryloxy derivativ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07F7/18
CPCC07F7/1804C07F7/188
Inventor 刘明锋吴兵兵陈圣云杨龙安甘俊甘书官
Owner JINGZHOU JIANGHAN FINE CHEM
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