Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Exhaust recycling technology in production process of polycrystalline silicon

A production process and tail gas recovery technology, applied in the direction of halosilane, halide silicon compound, hydrogen separation, etc., can solve the problems of complex equipment process and high energy consumption, and achieve the effect of simple process, simplified process flow and convenient operation

Active Publication Date: 2016-05-11
XINTE ENERGY
View PDF9 Cites 6 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, in the above-mentioned tail gas treatment process, the hydrogen chloride in the tail gas is absorbed and analyzed through the absorption tower and the desorption tower, which is not only complicated in equipment and process, but also high in energy consumption.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] This embodiment provides a tail gas recovery process in the polysilicon production process, including the following steps:

[0025] (1) Under the catalysis of the first catalyst, the tail gas in the polysilicon production process reacts with hydrogen chloride and dichlorodihydrosilane in the tail gas to obtain the first mixture; the first mixture is cooled to -5 ~55°C, the first liquid mixture and the first gas mixture were obtained respectively.

[0026] The components of the tail gas in the polysilicon production process include: hydrogen, hydrogen chloride, trichlorosilane, dichlorodihydrosilane, and silicon tetrachloride. Among them, the molar proportion of hydrogen chloride in the tail gas is 0.4% to 6%. The molar ratio of dichlorodihydrosilane is 0.4%-7%. After the above reaction, the mole percentage of hydrogen chloride in the tail gas drops below 0.2%. In step (1), the reaction of hydrogen chloride in the tail gas and dichlorodihydrosilane to generate trichlor...

Embodiment 2

[0032] This embodiment provides a tail gas recovery process in the polysilicon production process, including the following steps:

[0033] (1) Under the catalysis of the first catalyst dimethylformamide, the tail gas in the polysilicon production process reacts with hydrogen chloride and dichlorodihydrosilane in the tail gas, and the reaction temperature is 60-120°C, The pressure is 0.1-2.0MpaG to obtain the first mixture; the first mixture is cooled to -5-55°C to obtain the first liquid mixture and the first gas mixture respectively.

[0034] The components of the tail gas in the polysilicon production process include: hydrogen, hydrogen chloride, trichlorosilane, dichlorodihydrosilane, and silicon tetrachloride. Among them, the molar proportion of hydrogen chloride in the tail gas is 0.4% to 6%. The molar ratio of dichlorodihydrosilane is 0.4%-7%. After the above reaction, the mole percentage of hydrogen chloride in the tail gas drops below 0.2%. In step (1), the reaction ...

Embodiment 3

[0040] This embodiment provides a tail gas recovery process in the polysilicon production process, including the following steps:

[0041] (1) Under the catalysis of the first catalyst dimethylformamide and the macroporous tertiary amine anion exchange resin, the tail gas in the polysilicon production process reacts with hydrogen chloride and dichlorodihydrosilane in the tail gas, and the reaction The temperature is 60-120°C and the pressure is 0.1-2.0MpaG to obtain the first mixture; the first mixture is cooled to -5-55°C to obtain the first liquid mixture and the first gas mixture respectively.

[0042] The components of the tail gas in the polysilicon production process include: hydrogen, hydrogen chloride, trichlorosilane, dichlorodihydrosilane, and silicon tetrachloride. Among them, the molar proportion of hydrogen chloride in the tail gas is 0.4% to 6%. The molar ratio of dichlorodihydrosilane is 0.4%-7%. After the above reaction, the mole percentage of hydrogen chlorid...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses an exhaust recycling technology in the production process of polycrystalline silicon. The exhaust recycling technology comprises the following steps that under the catalytic action of a first catalyst, exhaust is subjected to a reaction generated by hydrogen chloride and dichlorosilane in the exhaust, and a first mixture is obtained; the first mixture is cooled to minus 5-55 DEG C, and a first liquid mixture and a first gas mixture are obtained; under the catalytic action of a second catalyst, the first gas mixture is subjected to a reaction generated by dichlorosilane and silicon tetrachloride in the exhaust, and a second mixture is obtained; the second mixture is cooled to be minus 40-minus 10 DEG C, and a second liquid mixture and a second gas-liquid mixture are obtained; the second gas-liquid mixture is subjected to gas-liquid separation, and a third gas mixture and a third liquid mixture are obtained, wherein the main component of the third gas mixture is hydrogen. The phenomena that in the recycling technology in the prior art, hydrogen chloride in the exhaust is absorbed and resolved, and dichlorosilane in the exhaust enters subsequent chlorosilane rectification purification are avoided.

Description

technical field [0001] The invention belongs to the technical field of polysilicon production, and in particular relates to a tail gas recovery process in the polysilicon production process. Background technique [0002] The main components of the tail gas of the reduction furnace or hydrogenation furnace used in the polysilicon production process include: hydrogen, hydrogen chloride, trichlorosilane, dichlorodihydrogen silicon, and silicon tetrachloride. This part of the tail gas must be fully recycled. [0003] The polysilicon tail gas recovery process currently used is mainly: the tail gas of the reduction furnace or hydrogenation furnace used in the production process of polysilicon is passed through the tail gas water cooler, the gas-gas heat exchanger of the tail gas, the frozen brine heat exchanger of -20 ℃ and the tail gas. The subcooler lowers the temperature step by step, using the different boiling points of the components in the tail gas to remove about 30% of th...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): C01B33/107C01B3/50
Inventor 张伟银波张吉武陈朝霞黄彬
Owner XINTE ENERGY
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products