Method for drying hydrogen chloride gas

A technology of hydrogen chloride gas and drying method, which is applied in the direction of chlorine/hydrogen chloride, chlorine/hydrogen chloride purification, chemical instruments and methods, etc., can solve the problems of large energy consumption, narrow application range, large investment, etc., and reduce the probability of equipment blockage, The effect of reducing production costs and reducing environmental pollution

Inactive Publication Date: 2012-07-18
SHANDONG XINLONG TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] Trichlorosilane is a colorless liquid, volatile and deliquescent
The best external condition for the production of trichlorosilane is to rely on the chlor-alkali plant, which has both direct delivery of chlorine and cheap hydrogen, but the synthesized HCL gas contains a lot of water, once the water enters the system, it will be with the Trichlorosilane reacts to form silicon dioxide, which blocks the equipment in the next production process, and ultimately reduces the conversion rate of silicon powder and increases production costs. Therefore, controlling the water content in the raw material hydrogen chloride is the key to increasing the conversion rate and reducing production costs. The essential
[0003] Silicon tetrachloride is a by-product in the production process of trichlorosilane. At present, the scope of use is very narrow, and it is difficult to handle. It has the property of decomposing when it encounters water. It reacts with water to form hydrogen chloride and silicon dioxide. There are no other impurities.
[0004] The traditional process is to reduce the moisture content of hydrogen chloride gas by freezing and cooling. The process is to cool the HCL gas to -17°C with -35°C frozen brine, which can cool most of the water in the HCL gas, thereby To achieve the purpose of drying HCL gas, but this process needs to consume a lot of energy, and the equipment used needs to be made of graphite, which requires a large investment. The water content of hydrogen chloride gas after treatment is about 1000ppm, and the water content is still high, which cannot fundamentally Solve the problem

Method used

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  • Method for drying hydrogen chloride gas
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Experimental program
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Effect test

Embodiment 1

[0024] Embodiment 1, a kind of drying method of hydrogen chloride gas, the hydrogen chloride gas containing moisture comes out from the production workshop and enters the bottom of the drying spray tower 2 through the pipeline 1, and the intake flow rate of the hydrogen chloride gas is 900Nm 3 / h, the temperature is 35°C, the pressure is 130kPaG, the water content is 8000-10000ppm, from the bottom along the inner cavity of the drying spray tower 2, the silicon tetrachloride is stored in the circulation tank 3, and the silicon tetrachloride passes through the filter 5 After filtering, it is extracted from the circulation tank 3 by the circulation pump 4, and is pumped into the drying spray tower 2, from the spray head 6 arranged at the bottom of the dry spray tower 2, the spray head 7 of the middle part and the spray head of the upper part 8. The hydrogen chloride gas is sprayed sequentially. The hydrogen chloride gas produced after the hydrolysis of silicon tetrachloride meets ...

Embodiment 2

[0025] Embodiment 2, a kind of drying method of hydrogen chloride gas, the hydrogen chloride gas containing moisture comes out from the production workshop and enters the bottom of the drying spray tower 2 through the pipeline 1, and the intake flow rate of the hydrogen chloride gas is 950Nm 3 / h, the temperature is 40°C, the pressure is 140kPaG, the water content is 8000-10000ppm, from the bottom along the inner cavity of the drying spray tower 2, the silicon tetrachloride is stored in the circulation tank 3, and the silicon tetrachloride passes through the filter 5 After filtering, it is extracted from the circulation tank 3 by the circulation pump 4, and is pumped into the drying spray tower 2, from the spray head 6 arranged at the bottom of the dry spray tower 2, the spray head 7 of the middle part and the spray head of the upper part 8. The hydrogen chloride gas is sprayed sequentially, and the hydrogen chloride gas produced after the hydrolysis of silicon tetrachloride me...

Embodiment 3

[0026] Embodiment 3, a kind of drying method of hydrogen chloride gas, the hydrogen chloride gas containing moisture comes out from the production workshop and enters the bottom of the drying spray tower 2 through the pipeline 1, and the intake flow rate of the hydrogen chloride gas is 1000Nm 3 / h, the temperature is 45°C, the pressure is 150kPaG, the water content is 8000-10000ppm, from the bottom along the inner cavity of the drying spray tower 2, the silicon tetrachloride is stored in the circulation tank 3, and the silicon tetrachloride passes through the filter 5 After filtering, it is extracted from the circulation tank 3 by the circulation pump 4, and is pumped into the drying spray tower 2, from the spray head 6 arranged at the bottom of the dry spray tower 2, the spray head 7 of the middle part and the spray head of the upper part 8. The hydrogen chloride gas is sprayed sequentially, and the hydrogen chloride gas produced after the hydrolysis of silicon tetrachloride m...

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Abstract

The invention relates to a method for drying a hydrogen chloride gas, which comprises: allowing the hydrogen chloride gas containing water to rise from the bottom part of a drying spray tower along the inner cavity of the drying spray tower; spraying silicon tetrachloride in the inner cavity of the drying spray tower; performing the spray treatment of the hydrogen chloride gas; allowing the sprayed hydrogen chloride gas and the silicon tetrachloride mixed with the hydrogen chloride gas to enter a condenser from the top part of the drying spray tower to perform condensation treatment; and discharging the dried hydrogen chloride gas from the condenser. The silicon tetrachloride decomposes upon the contact with water to form the hydrogen chloride gas and silicon dioxide. The drying of the HCl by using the silicon tetrachloride has the advantages that: the generated HCl can be reused; the water content of the hydrogen chloride gas is reduced to below 50ppm; the conversion rate of silicon powder is improved; the production cost is reduced; the maximum temperature requirement by equipment for operation is 0 DEG C; the cold energy consumption is low; the equipment investment is small; the energy consumption is reduced; and the environmental pollution is relieved.

Description

technical field [0001] The invention relates to a production raw material in the production of trichlorosilane, in particular to a method for drying hydrogen chloride gas in the production of trichlorosilane, and belongs to the technical field of chemical industry. Background technique [0002] Trichlorosilane is a colorless liquid, volatile and deliquescent. The main raw materials for the production of trichlorosilane are industrial silicon and HCl, which are produced in a fluidized bed reactor using silicon powder and hydrogen chloride gas, and decompose and react with water to produce hydrogen chloride gas. It is a first-class flammable material when wet, flammable and explosive, it reacts strongly with oxidants, and burns or explodes when exposed to open flames or high heat. The best external condition for the production of trichlorosilane is to rely on the chlor-alkali plant, which has both direct delivery of chlorine and cheap hydrogen, but the synthesized HCL gas con...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B7/07B01D53/26
Inventor 李法曾杨秀玲苗乃芬李法山王建民常丙杰桑来亮杨海棠
Owner SHANDONG XINLONG TECH
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