Composite catalyst for preparing trichlorosilane through catalytic hydrogenation of silicon tetrachloride

A technology for catalytic hydrogenation of silicon tetrachloride and composite catalysts, applied in the direction of metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve raw material and energy waste, product and environmental pollution , easy sintering deactivation and other problems, to achieve the effects of energy saving, catalytic efficiency improvement and high selectivity

Active Publication Date: 2013-04-03
SICHUAN UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the metals or chlorides of the main group II also have a catalytic effect on side reactions, and the selectivity is relatively low, and by-products such as dichlorodihydrosilane are generated, resulting in waste of raw materials and energy.
However, silicon carbide nanotube arrays infiltrated with precious metals and special materials such as palladium, platinum, tungsten, and silicon, although this type of catalyst has a high selectivity to the product trichlorosilane, is expensive, has a short life, and is prone to sintering loss. The atomic dust produced by consumption at high temperature will also pollute the product and the environment

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] 32-40 mesh, silicon-aluminum ratio of 60, specific surface area of ​​250-500m 2 / g of Na-ZSM-5 shaped carrier particles impregnated in barium chloride (containing 0.01% cobalt chloride), barium chloride (containing 0.01% copper chloride), barium chloride (containing 0.01% nickel chloride) solution , equal-volume impregnation for 6 hours, during which 100MHz ultrasonic vibration is applied from time to time, after full impregnation, it is taken out and dried at 150°C for 2 hours, and gradiently calcined at 300-600°C for 6 hours to obtain granular Na-ZSM-5 supported catalyst.

Embodiment 2

[0041] The surface of 10-20 mesh is 8-40 m 2 / g of porous silicon carbide / barium titanate high-temperature-resistant ceramic shaped carrier particles were respectively impregnated in strontium chloride (containing 0.1% by weight of ferrous chloride), strontium chloride (containing 0.1% by weight of manganese chloride), strontium chloride ( Containing 0.1% by weight of zinc chloride) solution, immerse in equal volume for 6 hours, during which 100MHz ultrasonic vibration is added from time to time, after full impregnation, take out and dry at 150°C for 2 hours, and gradient calcined at 600-800°C for 6 hours to obtain particles supported catalysts.

Embodiment 3

[0043] Weigh dry HZSM-5 powder (silicon-aluminum ratio 38, specific surface 300-320m 2 / g) Put 20g into a beaker, the specific pore volume of HZSM-5 is 1.0mL / g, and the volume of the solution impregnated with equal volume is 20mL. Add 20mL of a solution containing 3% of barium chloride, 5% of calcium chloride, 0.5% of cadmium chloride, 0.5% of chromium chloride and 0.01% of lanthanum chloride in the beaker, and let it stand for 2 hours after fully stirring. , stirring once every 20 minutes. Weigh Na after standing 2 SiO 3 8.57g (the mass fraction of the binder in the catalyst is 30%, fully dissolved with 10mL of distilled water, added to the catalyst and stirred thoroughly, then put into a drying oven to dry at 100°C for 12 hours, then roasted at 450°C for 2 hours, after cooling Grinding to obtain granular HZSM-5 supported catalyst.

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PUM

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Abstract

The invention discloses composite catalyst for preparing trichlorosilane through catalytic hydrogenation of silicon tetrachloride. The active constituents of the catalyst comprise at least one second main group metallic element and at least one transitional metal element, or a compound of the second main group metallic element and that of the transitional metal element, and can be loaded on a carrier for use. The catalyst can be used for catalytic hydrogenation dehalogenation reaction of silicon tetrachloride in the atmosphere of 700 to 1000 DEG C and 1 to 30 bar hydrogen, has higher catalytic activity and favorable selectivity, and is low in cost, simple to prepare and stable in performance.

Description

technical field [0001] The invention relates to a catalytic reaction technology for heterogeneous gas-solid dehalogenation hydrogenation reaction in the field of chemical industry, in particular to a composite catalytic technology for catalytically hydrogenating silicon tetrachloride to convert silicon tetrachloride into trichlorosilane and hydrogen chloride. Background technique [0002] At present, the polysilicon industry at home and abroad is developing rapidly, and the process of producing high-purity polysilicon with trichlorosilane accounts for a large share of the production capacity that has been put into production. The by-product silicon tetrachloride produced by this series of processes is severely overcapacitated, and 14-20kg of silicon tetrachloride is produced for every 1kg of polysilicon produced, and has low utilization value, high waste disposal cost, high toxicity and high pollution. However, the technology of directly producing electronic-grade or photovo...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/46B01J29/48B01J27/224B01J27/138B01J27/24B01J23/887C01B33/107
Inventor 梁斌周齐领黄韬刘颖颖龙雨谦尹渠军蒋炜
Owner SICHUAN UNIV
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