Cracking process for byproduct chlorosilane high-boiling residue in polycrystalline silicon production

A high boiler, chlorosilane technology, applied in the direction of silicon compounds, halogenated silanes, halogenated silicon compounds, etc., can solve the problem of high cost of cracking catalysts, and achieve the effects of high compatibility, cost saving and conversion rate improvement.

Active Publication Date: 2020-08-07
CHINA ENFI ENGINEERING CORPORATION +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The main purpose of the present invention is to provide a cracking process of polysilicon production by-product chlorosilane high boilers to solve the problem of high cost of chlorosilane high boiler cracking catalysts in the prior art

Method used

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  • Cracking process for byproduct chlorosilane high-boiling residue in polycrystalline silicon production

Examples

Experimental program
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Effect test

Embodiment 1

[0037] refer to figure 1 Do the following.

[0038] Filter 50,000g of polysilicon production by-product chlorosilane high boilers to remove amorphous silicon and obtain purified high boilers, which are filtered by silicon carbide ceramic membrane filter elements with a filtration accuracy of 1 micron; filled in the cracking reactor Catalyst, the catalyst is an organic amine loaded on a macroporous weakly basic polystyrene anion exchange resin, the particle size of the macroporous weakly basic polystyrene anion exchange resin is 0.5-0.7mm, the pore diameter is 50-150nm, and the specific surface area is 30 ~40m 2 / g, the organic amine is a composition composed of tri-n-butylamine, tri-n-octylamine and N, N-dimethylaniline in a weight ratio of 1:0.4:0.7, and the organic amine is in the macroporous weakly basic polystyrene anion The loading on the exchange resin was 1.0%. Preheat the purified high boilers to 60°C and send them into the cracking reactor, and make the purified hi...

Embodiment 2

[0042] The difference from Example 1 is that the organic amine is a composition composed of tri-n-butylamine, tri-n-octylamine and N,N-dimethylaniline in a weight ratio of 1:0.5:0.5

[0043] The weight ratio of silicon tetrachloride in the feed chlorosilane high boiler: trichlorosilane: high boiler is 45:0:55; in the bottom liquid phase product obtained, silicon tetrachloride: trichlorosilane: high boiling The weight ratio of the material is 66:27:9.

Embodiment 3

[0045] refer to figure 1 Do the following.

[0046] The difference from Example 1 is that the organic amine is a composition composed of tri-n-butylamine, tri-n-octylamine and N,N-dimethylaniline in a weight ratio of 1:0.3:0.8.

[0047] The weight ratio of silicon tetrachloride in the feed chlorosilane high boiler: trichlorosilane: high boiler is 45:0:55; in the bottom liquid phase product obtained, silicon tetrachloride: trichlorosilane: high boiling The weight ratio of the material is 65:28:9.

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Abstract

The invention provides a cracking process for a byproduct chlorosilane high-boiling residue in polycrystalline silicon production. The cracking process comprises the following steps: filtering the byproduct chlorosilane high-boiling residue in polycrystalline silicon production to remove amorphous silicon in the byproduct chlorosilane high-boiling residue so as to obtain a purified high-boiling residue; and cracking hydrogen chloride and the purified high-boiling residue by using a catalyst to obtain a cracking product system, wherein the catalyst comprises macroporous resin and organic amineloaded on the macroporous resin, and the organic amine is selected from and any one or more of tri-n-butylamine, tri-n-octylamine, N,N-dimethylaniline, dioctadecyl secondary amine and perfluorotriethylamine. A framework of macroporous resin serving as a carrier in the catalyst is high in compatibility with the chlorosilane high-boiling residue, more reaction interfaces are provided, and organic amine loaded on the framework is enriched in micropores, so that the reaction of the inner surface and the outer surface of the resin is more thorough, the conversion rate can be increased, and the pyrolysis temperature can be reduced. The catalyst can be recycled. Before entering macroporous resin, amorphous silicon in the polysilicon production byproduct is removed through filtration, and resin pores are prevented from being blocked.

Description

technical field [0001] The invention relates to the technical field of polysilicon production, in particular to a cracking process for polysilicon production by-product chlorosilane high boilers. Background technique [0002] In the process of producing polysilicon by the improved Siemens method, SiHCl 3 and H 2 The gas enters the reduction furnace in a certain proportion, and the temperature of the silicon core carrier in the furnace reaches above 1050°C, and the SiHCl 3 and H 2 The mixed gas of SiHCl undergoes a reduction reaction on the surface of the carrier 3 +H 2 =Si+3HCl and thermal decomposition reaction 4SiHCl 3 =Si+3SiCl 4 +2H2, the generated silicon is deposited on the surface of the silicon core to form polycrystalline silicon rods. During the reduction process, in addition to silicon, SiCl 4 、SiH 2 Cl 2 、H 2 In addition to the formation of HCl, etc., there is also Si 2 Cl 6 、Si 2 HCl 5 、Si 2 h 2 Cl 4 , Cl 6 OSi 2 and Si 3 Cl 8 A series of b...

Claims

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Application Information

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IPC IPC(8): C01B33/107
CPCC01B33/1071Y02P20/584
Inventor 曾晓国万烨张晓伟张伟严大洲路向飞刘允许
Owner CHINA ENFI ENGINEERING CORPORATION
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