Method for preparing trichlorosilane

A technology for the manufacture of trichlorosilane, applied in the direction of halosilane, halide silicon compounds, etc., can solve the problems of difficult production operation, high production cost, high raw material purity requirements, high reaction temperature, etc., and achieve improved single-pass conversion rate, The production operation is less difficult and the effect of lowering the reaction temperature

Active Publication Date: 2012-03-07
JIANGSU ZHONGNENG POLYSILICON TECH DEV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Silicon tetrachloride easily reacts with water to form silicon dioxide and hydrogen chloride, and direct discharge will seriously affect the ecological environment
This technology must be supplemented with a gas separation device to separate the reaction product and process hydrogen chloride, so it requires a large investment and occupies a large area
In addition, thermal hydrogenation technology also has the following disadvantages: high reaction temperature, complicated process, and difficult device operation; the heater uses carbon-carbon composite materials, which can only be imported, and the cost is high; the requirement for raw material purity is high, which cannot be solved By-product dichlorosilane in the polysilicon manufacturing process; low conversion rate and high energy consumption, with an average power consumption of 3200-3500kwh per 1t of trichlorosilane produced
[0013] 1. The catalyst used in the manufacture of trichlorosilane contains noble metal components, so the cost of the catalyst is relatively high, resulting in a relatively high manufacturing cost of trichlorosilane;
[0014] 2. When producing trichlorosilane according to the thermal hydrogenation method, due to the high reaction temperature, the production operation difficulty and production cost are relatively high;
[0016] 4. Regardless of whether trichlorosilane is produced by thermal hydrogenation or cold hydrogenation, the single-pass conversion rate from silicon tetrachloride to trichlorosilane is low, generally only 17-25%, and there is still a large Room for improvement

Method used

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  • Method for preparing trichlorosilane
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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0106] The gas mixture consists of hydrogen and silicon tetrachloride in a molar ratio of 2.0:1.

[0107] CuCl is used as the main catalyst and NaCl is used as the co-catalyst, and relative to 100 parts by weight of silicon powder, the amount of CuCl is 1.5 parts by weight, and the amount of NaCl is 0.2 parts by weight.

[0108] The reaction pressure is 2.0MPa, the reaction temperature is 500°C, and the residence time is 26s.

[0109] After the reaction was carried out for 10 hours, the gas product was analyzed, and it was found that the molar content of trichlorosilane in the gas product was 24.7%, and the molar content of silicon tetrachloride was 74.6%. It can be known by calculation that the single pass conversion rate of silicon tetrachloride was 19.89%.

Embodiment 2

[0116] The gas mixture consists of hydrogen and silicon tetrachloride in a molar ratio of 2.0:1.

[0117] CuCl is used as the main catalyst and NaCl is used as the co-catalyst, and relative to 100 parts by weight of silicon powder, the amount of CuCl used is 1.5 parts by weight, and the amount of NaCl used is 0.75 parts by weight.

[0118] The reaction pressure is 2.2MPa, the reaction temperature is 510°C, and the residence time is 24s.

[0119] After the reaction was carried out for 10 hours, the gas product was analyzed, and it was found that the molar content of trichlorosilane in the gas product was 30.6%, and the molar content of silicon tetrachloride was 68.5%. It can be known by calculation that the single pass conversion rate of silicon tetrachloride is 25.10%.

Embodiment 3

[0121] The gas mixture consists of hydrogen, silicon tetrachloride and hydrogen chloride in a molar ratio of 14:7:1.

[0122] NiCl 2 As the main catalyst, KCl is used as the cocatalyst, and relative to 100 parts by weight of silicon powder, the NiCl 2 The consumption of KCl is 1.8 parts by weight, and the consumption of KCl is 0.5 parts by weight.

[0123] The reaction pressure is 2.0MPa, the reaction temperature is 500°C, and the residence time is 26s.

[0124] After the reaction was carried out for 10 hours, the gas product was analyzed, and it was found that the molar content of trichlorosilane in the gas product was 34.7%, and the molar content of silicon tetrachloride was 64.2%. It can be known by calculation that the single pass conversion rate of silicon tetrachloride was 28.84%.

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Abstract

The invention relates to a method for preparing trichlorosilane. The method comprises the step that silicon tetrachloride and hydrogen react with optional hydrogen chloride and silicon powder by adopting at least one main catalyst selected from copper halide and nickel halide and at least one auxiliary catalyst selected from alkali metal compounds. Compared with the prior art, the method for preparing the trichlorosilane has the advantages of low preparing cost, simple and easy technique and high per-pass conversion rate of the silicon tetrachloride.

Description

technical field [0001] The invention relates to a method for producing trichlorosilane, in particular to a method for producing trichlorosilane through catalytic hydrogenation of silicon tetrachloride. Background technique [0002] Polysilicon is the raw material of solar photovoltaic modules. With the introduction of favorable policies for the photovoltaic industry, the photovoltaic industry will surely set off an upsurge, and the market demand for polysilicon will inevitably increase accordingly. [0003] At present, more than 70% of polysilicon manufacturing technologies in the world use the improved Siemens method. The modified Siemens method to manufacture polysilicon is mainly obtained by depositing trichlorosilane and hydrogen on the surface of the silicon core at high temperature in a reduction furnace. While polysilicon is produced, a large amount of silicon tetrachloride is by-produced. On average, 15-20 tons of trichlorosilane will be consumed for every 1 ton of ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B33/107
Inventor 陈其国陈文龙
Owner JIANGSU ZHONGNENG POLYSILICON TECH DEV
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