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A kind of isobutane dehydrogenation preparation isobutene catalyst, its preparation method and application

A technology for producing isobutene and catalyst, which is applied in the field of isobutane dehydrogenation to produce isobutene, can solve the problems of affecting the service life of the catalyst, deep dehydrogenation and cracking, and weak anti-carbon deposition ability, so as to improve chemical stability and life, Improve the conversion rate and yield, improve the effect of anti-carbon deposition ability

Active Publication Date: 2021-02-05
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] There are literatures that use co-precipitation, slurry mixing method to load Cr, Pt, V and other elements, and use impregnation method to load La, Zr, Sn, Fe and other elements to obtain supported catalysts, and preferably Al 2 o 3 The catalyst prepared as a carrier has high activity and high selectivity, but the preparation cost is high, the anti-coking ability is not strong, and the service life is short
The preparation methods of Pt-based catalysts are also disclosed in the prior art, but there are some deficiencies in that it is easy to cause side reactions such as deep dehydrogenation and cracking of isobutane, which affects the service life of the catalyst.

Method used

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  • A kind of isobutane dehydrogenation preparation isobutene catalyst, its preparation method and application
  • A kind of isobutane dehydrogenation preparation isobutene catalyst, its preparation method and application

Examples

Experimental program
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Effect test

Embodiment 1

[0033] Preparation of modified carrier

[0034] Add 1g of attapulgite to 100g of pure alumina powder, then add 2wt% nitric acid aqueous solution to knead, extrude, dry at 120°C for 10 hours, and roast at 500°C for 4 hours to obtain attapulgite. Modified carrier A in an amount of 1 wt% of the weight of the carrier (alumina).

[0035] Catalyst preparation

[0036]Immerse 100g of modified carrier A into 19ml of 0.032g / ml aqueous solution of chloroplatinic acid for 8 hours, drain the water, wash with deionized water until there is no chloride ion, dry at 120°C for 10 hours, and then Calcined at 600°C for 5 hours, then immersed in 107ml of magnesium nitrate 0.4g / ml aqueous solution, soaked for 8 hours, dried at 120°C for 10 hours, and calcined at 600°C for 5 hours to obtain catalyst A. Wherein the platinum content is 0.26wt% of the catalyst weight, and the magnesium content is 12.14wt% of the catalyst weight.

Embodiment 2

[0038] Preparation of modified carrier

[0039] Add 1.5g of attapulgite to 100g of pure alumina powder, then add 2wt% nitric acid aqueous solution, knead, extrude, dry at 120°C for 10 hours, and roast at 650°C for 5 hours to obtain attapulgite The amount of modified support B is 1.5 wt% of the support weight.

[0040] Catalyst preparation

[0041] Immerse 100g of modified carrier B into 35ml of 0.025g / ml aqueous solution of chloroplatinic acid. After soaking for 9 hours, drain the water and wash with deionized water until there are no chloride ions. Dry at 120°C for 10 hours. Calcined at ℃ for 6 hours, then immersed in 157ml of magnesium nitrate 0.35g / ml aqueous solution, soaked for 9 hours, dried at 120℃ for 10 hours, and calcined at 700℃ for 6 hours to obtain catalyst B. Wherein the platinum content is 0.35wt% of the catalyst weight, and the magnesium content is 15.20wt% of the catalyst weight.

Embodiment 3

[0043] Preparation of modified carrier

[0044] Add 2g of attapulgite to 100g of pure alumina powder, then add 2wt% nitric acid aqueous solution to knead, extrude, dry at 120°C for 11 hours, and roast at 600°C for 6 hours to obtain attapulgite. Modified carrier C in an amount accounting for 2 wt% of the carrier weight.

[0045] Catalyst preparation

[0046] Immerse 100g of modified carrier C into 56ml of 0.015g / ml aqueous solution of chloroplatinic acid. After soaking for 8 hours, drain the water and wash with deionized water until there are no chloride ions. Dry at 120°C for 10 hours. Calcined at a temperature of 1°C for 7 hours, then immersed in 209ml of magnesium nitrate 0.25g / ml aqueous solution, soaked for 8 hours, dried at a temperature of 120°C for 10 hours, and fired at a temperature of 700°C for 7 hours to obtain catalyst C. Wherein the platinum content is 0.34wt% of the catalyst weight, and the magnesium content is 14.48wt% of the catalyst weight.

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Abstract

The application relates to a catalyst for preparing isobutene from isobutane dehydrogenation, comprising an attapulgite-modified carrier and a Pt metal component loaded on the modified carrier. The present application also relates to the preparation method and application of the above-mentioned catalyst. The catalyst according to the invention is used for isobutane dehydrogenation to produce isobutene, and has the advantages of high activity, high carbon deposition resistance, long service life, low cost, high isobutane conversion rate and isobutene yield.

Description

technical field [0001] The invention relates to the field of isobutane dehydrogenation to isobutene, in particular to a catalyst for isobutane dehydrogenation to isobutene. The present invention further relates to the preparation method and application of the above-mentioned catalyst. Background technique [0002] Isobutane is a low-carbon alkane that can be used to prepare isobutene. Isobutylene is a very important organic chemical raw material, mainly used to synthesize methyl tert-butyl ether, butyl rubber and polyisobutylene, in addition, it can also be used to synthesize methacrylate, isoprene, tert-butylphenol, tert-butylamine, Various organic raw materials and fine chemicals such as 1,4-butanediol and ABS resin. With the development and utilization of isobutene downstream products, the demand for isobutene is increasing, so isobutane dehydrogenation technology has received more and more attention. The research on isobutane dehydrogenation technology includes cataly...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/42C07C5/333C07C11/09
CPCB01J23/42B01J23/58C07C5/3337C07C2523/42C07C2523/58C07C11/09
Inventor 季静纪玉国柴忠义熊凯龚凤霞
Owner CHINA PETROLEUM & CHEM CORP