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Trichlorosilane production technique and system

A technology of trichlorosilane and production system, which is applied to silicon compounds, halogenated silanes, halogenated silicon compounds, etc., can solve the problems of low conversion rate, high production cost of trichlorosilane, and high cost of polysilicon, so as to reduce operating costs. , The effect of improving the utilization rate of raw materials and reducing power consumption

Inactive Publication Date: 2017-08-18
INNER MONGOLIA DUNAN PHOTOVOLTAIC TECH
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Problems solved by technology

[0003] However, the above two traditional trichlorosilane production processes have low conversion rates and high energy consumption, resulting in relatively high production costs for trichlorosilane, which is also one of the reasons for the high cost of polysilicon

Method used

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  • Trichlorosilane production technique and system

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Embodiment Construction

[0020] The trichlorosilane production process and system of the present invention will be described in detail below in conjunction with the diagrams.

[0021] See figure 1 , The trichlorosilane production system of the present invention comprises an evaporator 1, a hot hydrogenation furnace 2, a cold hydrogenation reactor 3, a filter 4, a condenser 5, a hydrogen storage tank 6, a compressor 7, a condensate storage tank 8, Purification separation tower 9, silicon tetrachloride storage tank 10, trichlorosilane product storage tank 11.

[0022] In this embodiment, the evaporator 1 is a three-layer heat exchanger for heat exchange between materials. That is, the silicon tetrachloride and hydrogen are exchanged for steam or exhaust gas with heat, and the silicon tetrachloride and hydrogen are heated. The evaporator 1 is simultaneously connected with the filter 4, the silicon tetrachloride storage tank 10, the compressor 7, and the condenser 5, and also has a steam inlet and a ste...

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Abstract

The invention provides a trichlorosilane production system which comprises an evaporator, a hot hydrogenation furnace, a cold hydrogenation reactor, a filter, a condenser and a purifying and separating column, wherein the hot hydrogenation furnace is connected with the cold hydrogenation reactor, and used for introducing tail gas obtained by hot hydrogenation into the cold hydrogenation reactor to perform reaction; the filter is connected with the cold hydrogenation reactor to filter the tail gas of the cold hydrogenation reactor; the evaporator is connected with the hot hydrogenation furnace, the filter and the condenser, and used for performing heat exchange on silicon tetrachloride and hydrogen used as raw materials and the filtered tail gas, and the tail gas is introduced into the condenser; the condenser is used for condensing the tail gas to obtain chlorosilane; and the purifying and separating column is used for separating and purifying the liquid chlorosilane. The invention also provides a trichlorosilane production technique. The trichlorosilane production system and technique provided by the invention can effectively utilize the waste heat of the hot hydrogenation tail gas and use the byproduct chlorine hydride generated by hot hydrogenation as the raw material to participate in the cold hydrogenation reaction, thereby lowering the power consumption, enhancing the raw material utilization ratio and lowering the overall operating cost.

Description

technical field [0001] The invention relates to a production process and system of trichlorosilane. Background technique [0002] Trichlorosilane is used as a raw material for polysilicon production, and its preparation methods are generally divided into thermal hydrogenation and cold hydrogenation. Thermal hydrogenation mainly uses silicon tetrachloride and hydrogen as raw materials, and is carried out at a high temperature exceeding 1,000 degrees to generate trichlorosilane. With hydrogen chloride gas, this reaction is an endothermic reaction. The cold hydrogenation is to use silicon powder, silicon tetrachloride and hydrogen as raw materials, and react in a cold hydrogenation reactor to synthesize trichlorosilane. The temperature required for cold hydrogenation is relatively low (about 550 degrees). [0003] However, the above two traditional trichlorosilane production processes have relatively low conversion rates and high energy consumption, resulting in relatively hig...

Claims

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Application Information

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IPC IPC(8): C01B33/107
CPCY02P20/129C01B33/10763
Inventor 齐林喜赵亮陈建宇
Owner INNER MONGOLIA DUNAN PHOTOVOLTAIC TECH