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Catalyst with modified alumina as carrier, and preparation method and application thereof

A technology of alumina carrier and catalyst, which is applied in physical/chemical process catalysts, chemical instruments and methods, and hydrocarbon production from halogen-containing organic compounds. problem, to achieve the effect of simple preparation method, mild reaction conditions and easy industrialization

Active Publication Date: 2016-11-23
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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  • Catalyst with modified alumina as carrier, and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Weigh commercially available alumina (pore volume is 0.96ml / g, specific surface area is 286.81m 2 / g, the saturated water absorption is 145ml / g, provided by Fushun Branch of Sinopec Catalyst Co., Ltd., the following examples and comparative examples all use this alumina), the mass concentration is 5% pyridine aqueous solution saturated spray impregnated alumina Immediately after finishing, dry at 95°C for 1 h, the adsorption amount of the dried pyridine aqueous solution is 60% of the saturated absorption solution of the alumina carrier, aging at 60°C for 7 h, drying at 100°C for 24 hours, and then calcining at 300°C for 5 The modified alumina carrier was prepared in hours. Weigh an appropriate amount of manganese nitrate and dissolve it in deionized water, add ammonium thiocyanate so that the mass fraction of ammonium thiocyanate in the solution is 2%, and the manganese salt solution is loaded on the above-mentioned alumina carrier by equal volume impregnation method, a...

Embodiment 2

[0031] Weigh commercially available alumina, saturate spray and impregnate the alumina with a mass concentration of 20% diethanolamine aqueous solution, and immediately dry at 110°C for 0.5h after drying until the adsorption amount of the diethanolamine aqueous solution is the amount of the saturated absorption solution of the alumina carrier. 40%, aged at 80°C for 4 hours, dried at 120°C for 8 hours, and then calcined at 400°C for 3 hours to obtain a modified alumina carrier. Weigh an appropriate amount of manganese nitrate and dissolve it in deionized water, add ammonium thiocyanate so that the mass fraction of ammonium thiocyanate in the solution is 15%, and the manganese salt solution is loaded on the above-mentioned alumina carrier by equal volume impregnation method, and dried at 100 °C 6h, and calcined at 400°C for 8h to prepare the catalyst precursor. The catalyst precursor is placed in a continuous flow fixed-bed reactor, and the catalyst precursor is treated with a m...

Embodiment 3

[0035] Weigh commercially available alumina, saturate spray and impregnate the alumina with a mass concentration of 20% diethanolamine aqueous solution, and immediately dry at 110°C for 0.5h after drying until the adsorption amount of the diethanolamine aqueous solution is the amount of the saturated absorption solution of the alumina carrier. 40%, aged at 80°C for 4 hours, dried at 120°C for 8 hours, and then calcined at 400°C for 3 hours to obtain a modified alumina carrier. Weigh an appropriate amount of manganese nitrate and dissolve it in deionized water, add ammonium thiocyanate so that the mass fraction of ammonium thiocyanate in the solution is 10%, and the manganese salt solution is loaded on the above-mentioned alumina carrier by equal volume impregnation method, and dried at 120 °C 4h, calcination at 500°C for 4h to prepare the catalyst precursor. The catalyst precursor is placed in a continuous flow fixed-bed reactor, and the catalyst precursor is treated with a mi...

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Abstract

The invention discloses a catalyst with modified alumina as a carrier, and a preparation method and an application thereof. The catalyst is prepared by the following steps: (1) carrying out saturated impregnation of an alumina carrier with a nitrogen-containing organic compound aqueous solution with equal volume, after impregnation, immediately drying for 0.5-1 h at the temperature of 95-110 DEG C, drying until the adsorption amount of the nitrogen-containing organic compound aqueous solution is 30-60% of the saturated absorption solution amount of the alumina carrier, and then aging, drying and roasting to obtain a modified alumina carrier; (2) carrying out saturated impregnation of the modified alumina carrier prepared in the step (1) with a manganese salt solution, and then drying and roasting, wherein the manganese salt solution contains 2-15% by mass of ammonium thiocyanate; and (3) carrying out bromination treatment of the material roasted in the step (2), making the weight content of manganese oxide in the catalyst be 0.5%-5%, preferably 1%-3%, and making the weight content of manganese bromide be 5%-40%, preferably 10%-30%. The catalyst can significantly improve the selectivity of isobutene.

Description

technical field [0001] The invention relates to a catalyst with modified alumina as a carrier and its preparation method and application, in particular to a catalyst with modified alumina as a carrier for highly selective production of isobutene using methyl bromide as a raw material and its preparation method and apply. 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 cont...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/138C07C11/09C07C1/26
Inventor 李杰张信伟张舒冬孙晓丹倪向前尹泽群刘全杰张喜文
Owner CHINA PETROLEUM & CHEM CORP