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Method and apparatus for preparing trichlorosilane through reaction rectification by using proportionate reaction

A technology of trichlorosilane and reactive distillation, which is applied in the field of reactive distillation, can solve the problems of low boiling point of dichlorodihydrosilane, large amount of silicon tetrachloride to be treated, technical blockade, etc., so as to improve the single-pass conversion rate, Improve the utilization rate of raw materials and solve the effect of enrichment

Active Publication Date: 2011-01-26
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For silicon tetrachloride, there are methods such as cold hydrogenation to treat it, so that it can be re-converted into trichlorosilane for reuse, but the domestic technology is immature, and the amount of silicon tetrachloride to be treated is large; Dihydrosilane, although there are relatively mature technologies abroad to prepare polysilicon using it as a raw material, due to technological blockade, this field is still almost blank in China, and the boiling point of dichlorodihydrosilane is relatively low, which is relatively dangerous.

Method used

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  • Method and apparatus for preparing trichlorosilane through reaction rectification by using proportionate reaction
  • Method and apparatus for preparing trichlorosilane through reaction rectification by using proportionate reaction
  • Method and apparatus for preparing trichlorosilane through reaction rectification by using proportionate reaction

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example 1

[0022] It is suitable for separate feeding of raw materials: silicon tetrachloride is fed from the liquid phase at position a at the top of reactive distillation tower 1, dichlorodihydrogen silicon is fed from the gas phase or liquid phase at position b at the middle of reactive distillation tower 1, and the reaction is carried out in the reactive distillation tower 1. Carry out in the middle and upper part of distillation tower 1, the dichlorodihydrosilane of incomplete reaction is obtained at the top of the tower, after condensation, a small amount is refluxed from the tower top, and a large amount is returned to the reactive distillation tower 1 from the middle of the tower, and a small amount of dichlorodihydrosilane, The incompletely reacted silicon tetrachloride and the trichlorosilane generated by the reaction are pumped into the middle part of the light removal tower 2 by the feed pump 4 of the light removal tower. The dichlorodihydrogen silicon obtained from the top of...

example 2

[0030] Suitable for mixed feeding of raw materials: the mixed chlorosilane raw material containing dichlorodihydrosilane, trichlorosilane and silicon tetrachloride is fed from the position c in the middle of light removal tower 2, and dichlorodihydrosilane is obtained from the top of the tower, which enters the reaction The middle part of the rectification tower 1 is used as a reactant, and another reactant, silicon tetrachloride, is withdrawn from the side line of the lower part of the weight removal tower 3 and enters the top of the reactive rectification tower 1 . Incompletely reacted dichlorodihydrosilane is obtained from the top of reactive distillation tower 1. After condensation, a small amount is refluxed from the top of the tower, and a large amount is returned to reactive distillation tower 1 from the middle of the tower. A small amount of dichlorodihydrosilane, incompletely The reacted silicon tetrachloride and the trichlorosilane generated by the reaction are fed in...

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Abstract

The invention relates to a method and an apparatus for preparing trichlorosilane through reaction rectification by using proportionate reaction. The method comprises the following steps of: reacting dichlorosilane with silicon tetrachloride in the upper middle part of a reaction rectification tower, obtaining incompletely reacted dichlorosilane at the top of the reaction rectification tower; reflowing at the top of the tower and in the middle of the tower, obtaining a mixture of dichlorosilane, trichlorosilane and silicon tetrachloride at the bottom of the tower, entering a light-end removal tower to remove a light component, obtaining the dichlorosilane at the top of the light-end removal tower; reflowing to the reaction rectification tower for recycling, obtaining a mixture of trichlorosilane and silicon tetrachloride at the bottom of the tower, entering a heavy-end removal tower to separate the trichlorosilane from the silicon tetrachloride, wherein the trichlorosilane at the top of the heavy-end removal tower is a product; and taking out the silicon tetrachloride at the side line of the lower part of the tower, entering the reaction rectification tower for recycling, and obtaining excessive silicon tetrachloride at the bottom of the tower. In the invention, by utilizing the proportionate reaction, the utilization ratio of the raw materials is enhanced; the problem of dichlorosilane and silicon tetrachloride enrichment is solved; and the final conversion ratio of the dichlorosilane is ensured to reach 100 percent theoretically.

Description

technical field [0001] The invention relates to the technical field of reactive distillation, in particular to a method and equipment for preparing trichlorosilane through reactive distillation using anti-disproportionation reaction in the production process of polysilicon. Background technique [0002] Trichlorosilane is also known as trichlorosilane, silicon chloroform, English name: trichlorosilane or siliconochloroform, molecular formula is SiHCl 3 , used in the synthesis of organosilanes and alkyl, aryl and organofunctional group chlorosilanes, is the most basic monomer in organosilane coupling agents, and is also the raw material for the production of semiconductor silicon, single crystal silicon and polycrystalline silicon. [0003] Reactive distillation technology is the process of separating the product by rectification while the reaction is in progress. The principle is: for a reversible reaction, when the volatility of a certain product is greater or less than tha...

Claims

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Application Information

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IPC IPC(8): C01B33/107
CPCY02P20/10
Inventor 黄国强王国锋王红星华超
Owner TIANJIN UNIV
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