Production process of alkoxy silane

A technology of alkoxysilane and production process, which is applied in the production process field of preparing alkoxysilane by alcoholysis, and achieves the effect of reducing the existence of organic chlorine

Active Publication Date: 2017-05-31
LUZHOU NORTH CHEM IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented technology allows for precise control over certain areas within reactor systems during chemical vapor deposition (CVD). By adjustting how much or what type of compound reacts with each component being deposited on substrates, this results in fewer unwanted impurities such as organohydroxylic acid) that are introduced into the system without affecting its quality level negatively impacted. Additionally, it provides an efficient way to produce high-purity alkoxy silanes while minimizing any harmful side products like halogenated alkenes from excessive use of nitrogen gas.

Problems solved by technology

Technological Problem addressed in this patented technical solution describes how to efficiently manufacturers find ways to enhance their ability to create highly pure organoxymolidsilanes while minimizing wastage and environmental impact associated with producing large quantities of chemical waste. Current techniques involve expensive and cumbersome procedures involving multiple distillations and treatments. Therefore, new technologies aim to simplify the overall production process and reduce energy consumption.

Method used

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  • Production process of alkoxy silane

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Embodiment 1

[0034] The device used is a reaction analysis tower with a length of 4.8m and an inner diameter of 0.3m, which is filled with PTFE ring packing and regular corrugated packing. The height of the packing is about 2.3m. The gas phase outlet at the top of the tower is equipped with an outlet material condenser. After being adsorbed by molecular sieves, the water content in ethanol is 900ppm. The ethanol after water removal is added from the tower kettle, and the temperature of the kettle is controlled at 110-130°C. When a stable ethanol reflux appears at the top of the tower, methyltrichlorosilane is added from the top of the reaction analysis tower. After the ethanol began to reflux, the ethanol addition rate was reduced to 250kg / h. Adjust the adding rate of methyltrichlorosilane to about 250kg / h, so that the temperature at about 0.3m below the adding point of silane is 80-85°C, and make the temperature below the adding point of methyltrichlorosilane higher than the boiling poin...

Embodiment 2

[0036] The device used is a reaction analysis tower with a length of 4.8m and an inner diameter of 0.3m, which is filled with PTFE ring packing and regular corrugated packing. The height of the packing is about 2.3m. The gas phase outlet at the top of the tower is equipped with an outlet material condenser. After being adsorbed by molecular sieves, the water content in methanol is 730ppm. The methanol after water removal is added from the tower kettle, and the temperature of the kettle is controlled at 95-115°C. When a stable methanol reflux appears at the top of the tower, methyltrichlorosilane is added from the top of the reaction analysis tower. After methanol began to reflux, the ethanol addition rate was reduced to 200kg / h. Adjust the addition rate of methyltrichlorosilane to about 300kg / h, so that the temperature at about 0.3m below the addition point of silane is 65-70°C, and make the temperature below the addition point of methyltrichlorosilane higher than the boiling...

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Abstract

The invention belongs to the field of chemical engineering, and relates to a production process of alkoxy silane for improving the purity of products. The production process comprises the following steps: A, dewatering alcohol, and conveying the alcohol into reaction equipment to generate an esterification reaction with organic chlorosilane; B, conveying the material into evaporation equipment after the esterification reaction, and evaporating a small part of alcohol in the material; C, neutralizing the distillation product to obtain the alkoxy silane, wherein in a starting phase of the production process, excessive alcohol is added in step A to generate backflow of the alcohol in the reaction equipment; and in the case of backflow of the alcohol, organochlorosilane is added, and the adding dosage of the alcohol is reduced to the dosage consumed in the reaction. The alkoxy silane, and particularly methyl triethoxysilane, is produced by a simple preparation process. Compared with other processes, a rectifying column is eliminated and is replaced by a cyclic evaporator, and a dehydration system and a fixed bed neutralization system are added. By means of control of temperature, pressure and feeding dosage in the reaction process, the HCl content of the alkoxy silane is lower than or equal to 10ppm, and the purity is higher than or equal to 99.0wt%.

Description

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Claims

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Application Information

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Owner LUZHOU NORTH CHEM IND
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