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Device and method for preparing high-purity silane through disproportionation reactive distillation of trichlorosilane

A technology of disproportionation reaction and trichlorosilane, which is applied in the field of reactive distillation technology, can solve the problems of high operating pressure of silane purification tower, high cost of condensing refrigerant at the top of the tower, and difficulty in process realization, so as to increase the minimum operating temperature and reduce the The process achieves the effect of difficulty and high purity

Active Publication Date: 2013-06-26
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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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 atmospheric pressure is extremely low, about -112°C, silane The operating pressure of the purification tower is relatively high, generally higher than 1.5Mpa, and the temperature at the top of the tower is relatively low, generally lower than -35°C. , but 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 preparing high-purity silane through disproportionation reactive distillation of trichlorosilane

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example 1

[0045] Accounting and explanation are made based on the production of 10t / y high-purity silane on a pilot scale.

[0046] The 23.4kg / hTCS 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. To the effect of reactive distillation, the upper part is filled with 2m high-efficiency structured packing as a rectification section to recover unreacted chlorosilanes, and the lower part is filled with 3m high-efficiency structured packing as a stripping section to separate TCS and STC. The disproportionation reaction distillation tower is a variable-diameter tower, the diameter of the upper part of the tower is 60mm, and the diameter of the middle and lower part of the tower is 150mm. The top of the tower is condensed with frozen brine, and the temperature at the top of the tower is controlled at 0-5°C. The tower is condensed with circulating water, and the...

example 2

[0051] Accounting explanation is made based on the industrial production scale of 10,000t / y high-purity silane output.

[0052] The 23.4t / hTCS raw material is pumped into the disproportionation reaction rectification tower, and the middle part of the tower is filled with three-stage catalyst with a total structure of 15m. To the effect of reactive distillation, the upper part is filled with 3m high-efficiency structured packing as a rectification section to recover unreacted chlorosilanes, and the lower part is filled with 5m high-efficiency structured packing as a stripping section to separate TCS and STC. The disproportionation reaction rectification tower is a variable-diameter tower, the diameter of the upper part of the tower is 800mm, and the diameter of the middle and lower part of the tower is 2000mm. The top of the tower is condensed with cryogenic ethylene glycol, and the temperature at the top of the tower is controlled at 0-5°C. The tower is condensed with circulat...

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Abstract

The invention relates to a device and a method for preparing high-purity silane through disproportionation reactive distillation of trichlorosilane. The method comprises a disproportionation reactive distillation process (A), a silicon tetrachloride absorption process (B), a fixed bed absorption process (C) and a product filling process (D). The method comprises the steps that: two-step disproportionation reaction is adopted, and the distillation separation action of a reactive distillation column is utilized to finally obtain a mixed gas of silane and dichlorosilane on a column top to be used as non-condensable gas of a condenser to be extracted, and a silicon tetrachloride product is obtained at a column bottom after reaction formation; a gaseous product which is recovered through a disproportionation reactive distillation column enters into a silicon tetrachloride absorption column, wherein the main ingredient of an absorbed gas is silane, an absorption liquid is filled into a silicon tetrachloride desorption column, the desorbed dichlorosilane is recovered on the column top, and the desorption liquid of the column reflows back to the silicon tetrachloride absorption tower; the absorbed gas is filled into a fixed bed to absorb so as to obtain a high-purity silane product; and the silane product is filled into a buffer tank under the pressurization condition. Technological equipment is simple, and the obtained silane product has high purity.

Description

technical field [0001] The present invention relates to a device and method for preparing high-purity silane through disproportionation reaction distillation of trichlorosilane, in particular to a device and method for preparing high-purity silane through disproportionation reaction distillation using trichlorosilane as raw material and using reactive distillation technology devices 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 tetrafluoride as raw materials to react and synthesi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B33/04
CPCY02P20/10
Inventor 黄国强王国峰王红星陈锦溢
Owner TIANJIN UNIV
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