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A kind of catalyst with silicon dioxide as carrier and its preparation method and application

A technology of silica and catalysts, applied in physical/chemical process catalysts, chemical instruments and methods, and hydrocarbon production from halogen-containing organic compounds, etc., can solve the problem of low selectivity of a single product and the high selectivity of methyl bromide to synthesize isobutene. and other problems, to achieve the effect of simple preparation method, mild reaction conditions and high product selectivity

Active Publication Date: 2018-10-12
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the technology with higher value-added low-carbon olefins as the target product, the selectivity of a single product is not high, and no relevant reports have been found on the synthesis of isobutene with high selectivity from methyl bromide

Method used

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  • A kind of catalyst with silicon dioxide as carrier and its preparation method and application

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Experimental program
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Effect test

Embodiment 1

[0028] Weigh an appropriate amount of cetyltrimethylammonium bromide, TMB, and tetraethylorthosilicate, add it to an appropriate amount of deionized water, stir evenly, and after obtaining a clear solution, add an appropriate amount of ethyl acetate, and stir at 70°C Generate a sol, stir at 80°C to form a gel, age the obtained gel in air for 15 hours, dry at 80°C for 18 hours, heat up to 500°C at 1°C / min and bake for 6 hours to obtain a silica carrier. Hexaalkyltrimethylammonium bromide: TMB: silicon element: water: ethyl acetate = 1:0.1:1:80:10.

[0029] Weigh an appropriate amount of zinc nitrate and dissolve it in deionized water, load it on the above-mentioned silica carrier by equal volume impregnation method, dry at 100°C for 6h, and calcinate at 500°C for 6h to prepare the catalyst precursor ZnO / SiO 2 . The catalyst precursor is placed in a continuous flow fixed-bed reactor, and the catalyst precursor is treated with a mixed gas of methyl bromide and nitrogen. The volu...

Embodiment 2

[0032] Weigh an appropriate amount of cetyltrimethylammonium bromide, TMB, and tetraethylorthosilicate, add it to an appropriate amount of deionized water, stir evenly, and after obtaining a clear solution, add an appropriate amount of ethyl acetate, and stir at 60°C Generate a sol, stir at 70°C to form a gel, age the obtained gel in air for 20 hours, dry at 60°C for 24 hours, heat up to 700°C at 3°C / min and bake for 8 hours to obtain a silica carrier. Hexaalkyltrimethylammonium bromide: TMB: silicon element: water: ethyl acetate = 5:2:1:200:20.

[0033] Weigh an appropriate amount of zinc nitrate and dissolve it in deionized water, load it on the above-mentioned silica carrier by equal volume impregnation method, dry at 80°C for 8h, and roast at 400°C for 8h to prepare the catalyst precursor ZnO / SiO 2 . The catalyst precursor is placed in a continuous flow fixed-bed reactor, and the catalyst precursor is treated with a mixed gas of methyl bromide and nitrogen. The volume con...

Embodiment 3

[0036] Weigh an appropriate amount of cetyltrimethylammonium bromide, TMB, and tetraethylorthosilicate, add it to an appropriate amount of deionized water, stir evenly, and after obtaining a clear solution, add an appropriate amount of ethyl acetate, and stir at 70°C A sol is formed, and the stirring is continued until a gel is formed. The obtained gel is aged in air for 18 hours, dried at 70°C for 18 hours, and heated at 2°C / min to 600°C for 7 hours to obtain a silica carrier, in which hexadecane Trimethylammonium bromide: TMB: silicon element: water: ethyl acetate = 3: 1.2: 1: 120: 15.

[0037] Weigh an appropriate amount of zinc nitrate and dissolve it in deionized water, load it on the above-mentioned silica carrier by equal volume impregnation method, dry at 120°C for 4h, and calcinate at 600°C for 4h to prepare the catalyst precursor ZnO / SiO 2 . The catalyst precursor is placed in a continuous flow fixed-bed reactor, and the catalyst precursor is treated with a mixed ga...

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Abstract

The invention discloses a catalyst with silica as a carrier, and a preparation method and an application thereof, wherein the preparation method comprises the following processes: (1) preparing the silica carrier; (2) introducing zinc oxide and / or an auxiliary agent oxide into the silica carrier; and (3) carrying out bromination treatment of the silica carrier after introduction of zinc oxide. The catalyst contains zinc oxide, zinc bromide and the silica carrier, according to the weight of the catalyst, the content of zinc oxide is 0.5%-20%, the content of zinc bromide is 10%-50%, and the content of the silica carrier is 40%-90%. The catalyst is used for a reaction of preparing isobutylene from methyl bromide, and can significantly improve the selectivity of isobutene.

Description

technical field [0001] The invention relates to a catalyst with silicon dioxide as a carrier, a preparation method and application thereof. Background technique [0002] Isobutene is an important basic organic chemical raw material. Its derivative products are numerous, the upstream and downstream industrial chains are complicated, and the consumption structure shows a trend of diversification. A variety of high value-added products can be prepared from isobutylene, such as: butyl rubber, polyisobutylene, methyl tert-butyl ether, isoprene and organic glass and other organic chemical raw materials and fine chemical products. As the market scale of isobutene downstream products continues to expand, the contradiction between supply and demand will gradually become prominent, especially in the context of the depletion of oil resources, the output of isobutene has become a key bottleneck restricting the development of downstream industries. Therefore, it is imminent to develop a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/138C07C1/26C07C11/09
Inventor 张舒冬张信伟孙晓丹李杰倪向前张喜文刘继华
Owner CHINA PETROLEUM & CHEM CORP