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Device and method for producing silane by disproportionated reaction distillation of trichlorosilane

A technology of trichlorosilane and disproportionation reaction, applied in the direction of silicon hydride, etc., can solve the problems of high operating pressure of silane purification tower, high cost of condensing refrigerant at the top of the tower, and difficult process realization, so as to save high-quality cooling capacity and increase operation The effect of pressure, reducing equipment requirements

Active Publication Date: 2015-10-21
TIANJIN JINGCHUN TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] There are certain defects in the existing foreign chlorosilane disproportionation technology to prepare silane: firstly, the multi-step disproportionation process equipment using fixed bed matching rectification sequence is complex, and because the boiling point of silane at normal pressure is extremely low, about -112°C, silane The operating pressure of the purification tower is high, generally higher than 5Mpa, the temperature at the top of the tower is low, generally lower than -110°C, and the cost of condensing refrigerant at the top of the tower is relatively high; secondly, the simplified disproportionation reaction distillation process, although the process equipment is simplified, However, it also faces the problem of low-temperature condensation, and the process is more difficult to realize

Method used

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  • Device and method for producing silane by disproportionated reaction distillation of trichlorosilane

Examples

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Effect test

example 1

[0040] The TCS raw material is pumped into the disproportionation reaction rectification tower, and the middle part of the tower is filled with two sections of catalyst with a total structure of 8m. The catalyst is A21, which is made of basic anion exchange resin packed in a corrosion-resistant cloth bag, and the wire mesh corrugated packing is spaced into rolls. It plays the role of reactive distillation, and the number of plates in the column rectification section and stripping section is 10. The temperature at the top of the control tower is between -40°C, and circulating water is used to condense in the tower, and the temperature in the control tower is about 0°C. The operating pressure of the disproportionation reaction distillation tower is controlled at 500Kpa, the temperature of the tower bottom is about 110°C, the temperature of the middle reaction section increases gradually from top to bottom, and the temperature of the reaction section is controlled between 50-100°C...

example 2

[0042] The TCS raw material is pumped into the disproportionation reaction rectification tower, and the middle part of the tower is filled with a catalyst with a total structure of 8m in two sections. The catalyst is A100, which is made of basic anion exchange resin packed in a corrosion-resistant cloth bag, and is rolled into a roll with a wire mesh corrugated packing. It plays the role of reactive distillation, and the number of plates in the column rectification section and stripping section is 10. The temperature at the top of the control tower is between -40°C, and circulating water is used to condense in the tower, and the temperature in the control tower is about 0°C. The operating pressure of the disproportionation reaction distillation tower is controlled at 500Kpa, the temperature of the tower bottom is about 110°C, the temperature of the middle reaction section increases gradually from top to bottom, and the temperature of the reaction section is controlled between 5...

example 3

[0044] The TCS raw material is pumped into the disproportionation reaction rectification tower, and the middle part of the tower is filled with two sections of catalyst with a total structure of 8m. The catalyst is A21, which is made of basic anion exchange resin packed in a corrosion-resistant cloth bag, and the wire mesh corrugated packing is spaced into rolls. It plays the role of reactive distillation, and the number of plates in the column rectification section and stripping section is 100. The temperature at the top of the control tower is between -40°C, and circulating water is used to condense in the tower, and the temperature in the control tower is about 0°C. The operating pressure of the disproportionation reaction distillation tower is controlled at 500Kpa, the temperature of the tower bottom is about 110°C, the temperature of the middle reaction section increases gradually from top to bottom, and the temperature of the reaction section is controlled between 50-100°...

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Abstract

The invention relates to a device and method for producing silane by disproportionated reaction distillation of trichlorosilane. The device is a distillation tower; the distillation tower is provided with a distillation section, a reaction section and a stripping section; a tower-top deep freezer is arranged on the distillation section; a tower kettle is provided with a reboiler; the distillation section and the stripping section are internally provided with structured packing; the reaction section is internally provided with a structure catalyst; a tower-top condenser and the distillation section are respectively provided with a vacuum jacket and an insulating layer; the vacuum jackets of the tower-top condenser and the distillation section are respectively provided with a vacuum extraction opening; the reaction section and the stripping section are provided with insulating layers; a silane outlet is arranged at the tower top; the tower-top deep freezer is provided with a tower-top condensate inlet and a tower-top condensate outlet; and a trichlorosilane inlet is arranged under the reaction section. Compared with a multi-step disproportionation process, the process has the advantages that the equipment is simple, the multi-step disproportionation reaction can be realized only by one reaction distillation tower, silicon tetrachloride as a product of the tower kettle returns into a cold hydrogenation system and is converted into the trichlorosilane, so that the closed-loop circulation is realized and simultaneously the purity of the obtained silane is high.

Description

technical field [0001] The present invention relates to a device and method for generating silane through disproportionation reaction rectification of trichlorosilane, in particular to a device and method for producing silane through disproportionation reaction rectification by using trichlorosilane as raw material, adding condensation in the middle section, and utilizing reactive rectification technology. Silane apparatus and methods. Background technique [0002] Silane, English name: silane, molecular formula is SiH 4 . As an important silicon source material, silane is widely used in semiconductor microelectronic IC, photovoltaic solar cell PV, liquid crystal display LCD and other industries. [0003] At present, there are three main production methods of silane: sodium aluminum fluoride method, silicon-magnesium alloy method and chlorosilane disproportionation method. Among them, the sodium aluminum fluoride method uses sodium aluminum hydride and silicon tetrafluori...

Claims

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Application Information

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IPC IPC(8): C01B33/04
Inventor 黄国强黄友光
Owner TIANJIN JINGCHUN TECH CO LTD
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