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Catalyst for preparing trichlorosilane by hydrogenation of silicon tetrachloride and preparation method thereof

A technology of silicon tetrachloride and trichlorosilane, which is applied in catalyst activation/preparation, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc. Catalyst activity, catalyst loss of activity and other issues, to achieve the effect of increasing added value, improving catalyst activity, and improving activity

Active Publication Date: 2020-07-21
辽宁金易化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Silicon tetrachloride is a poisonous and harmful gas. If it is discharged arbitrarily without treatment, silicon tetrachloride will combine with water vapor in the atmosphere to produce hydrogen chloride gas, which will cause serious pollution to the environment. In addition, it will also cause extreme resource consumption. Big waste, increasing the production cost of the enterprise
However, the catalyst prepared by this method is powdery, and it is easy to "run away" when used in a fluidized bed, resulting in catalyst loss and reduced activity. At the same time, the specific surface area of ​​the catalyst is not disclosed in the above-mentioned patent, indicating that silicon is simply used as a carrier for co-precipitation The specific surface area of ​​the prepared catalyst should be very small. A catalyst with a small specific surface area cannot provide more reaction sites for the reactants, which will affect the activity of the catalyst.

Method used

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  • Catalyst for preparing trichlorosilane by hydrogenation of silicon tetrachloride and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Add 13.3g of water glass with 30% silicon oxide content to the preparation tank, start the stirring device, and slowly add a 62% nitric acid solution to make the pH of the acidified water glass solution 2.5, and mix it evenly into the preparation tank Add 12.5g of nickel nitrate hexahydrate, stir to dissolve and then add to the above solution the pore volume 1.109mL / g, the specific surface area is 363m 2 / g, the dry basis is 70% pseudo-boehmite 10g and 86g fine silicon powder, stir well, then add the curing agent urea, after the urea is all dissolved, add deionized water to make the silica, The concentration of the sum of alumina, fine silicon powder and nickel oxide is 33%, and it is maintained as a slurry with certain fluidity.

[0035] The above-mentioned slurry with certain fluidity is spray-dried in a spray-drying tower. The nozzle diameter is set to 0.6mm, the gas in the spray-drying tower is inert gas nitrogen, and the drying temperature is 100°C. The spray droplets ...

Embodiment 2

[0038] The preparation process is as in Example 1, except that the curing agent is changed to hexamethylenetetraammonium to prepare the catalyst B of the present invention. The properties are shown in Table 1, and the catalyst evaluation results are shown in Table 2.

Embodiment 3

[0040] The preparation process is the same as in Example 1, except that the nozzle diameter is changed to 1.0 mm, and the internal drying temperature of the spray drying tower is 150° C. The catalyst C of the present invention is prepared. The properties are shown in Table 1, and the catalyst evaluation results are shown in Table 2.

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Abstract

The invention provides a catalyst for hydrogenating silicon tetrachloride to prepare trichlorosilane and a preparation method thereof. A silicon source acidic solution containing silicon oxide is acidified, soluble salts of active components and additives are added, and then pseudo-thin The waste fine powder produced during the catalytic hydrogenation of diaspore and fluidized bed silicon tetrachloride is then added with a curing agent to form a slurry; the slurry is solidified and formed by spray drying, and then washed, dried, and roasted to form a catalyst. The trichlorosilane catalyst prepared by the present invention has round particle size, concentrated particle size distribution, large specific surface area and high active metal dispersion; the method of the present invention makes the fluidized bed silicon tetrachloride catalytic hydrogenation process The waste fine powder produced by the friction between silicon powder and the reactor, the friction between silicon powder and the silicon powder, and the friction between the silicon powder and the catalyst are made into the catalyst carrier, so that the waste fine powder can be reused, while increasing the added value of the waste fine powder, Reduce secondary pollution.

Description

Technical field [0001] The invention relates to a catalyst for preparing trichlorosilane by hydrogenating silicon tetrachloride and a preparation method thereof. Background technique [0002] With the gradual depletion of fossil energy and the increasing environmental pollution problems, the search for a pollution-free renewable energy has become a top priority. As the most abundant renewable energy, solar energy has the advantages of cleanliness, safety, versatility, resource adequacy and potential economy compared with other energy sources. Making full use of solar energy has important economic and strategic significance for achieving sustainable development in a low-carbon model. [0003] In recent years, the output of polycrystalline silicon in my country has increased sharply. The main production processes of polycrystalline silicon include modified Siemens method, silane method and fluidized bed method. Among them, the modified Siemens method is the mainstream technology for...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J35/02B01J35/08B01J35/10B01J37/00C01B33/107B01J35/00
CPCC01B33/1071B01J23/755B01J37/0018B01J37/0045B01J35/40B01J35/51B01J35/613
Inventor 丛玉凤黄玮张晶姚丽珠张晓丽
Owner 辽宁金易化工有限公司
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