A kind of diene selective hydrogenation catalyst and its preparation method and application

A hydrogenation catalyst and selective technology, which is applied in the field of diene selective hydrogenation catalyst and its preparation, can solve the problems of low conversion rate of hydrogenation catalyst, low selectivity of hydrogenation catalyst, and unsatisfactory effect, etc. Achieve the effects of good product selective hydrogenation, improve the problem of agglomeration and loss, and improve the problem of selectivity reduction

Active Publication Date: 2016-11-23
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The active components of conventional catalysts are easy to agglomerate and lose during the reaction process, resulting in a low conversion rate of the hydrogenation catalyst. At the same time, diolefins are easily hydrogenated to form alkanes, resulting in low selectivity of the hydrogenation catalyst, resulting in the generation of a large amount of alkanes, causing serious loss of octane
In order to solve these problems, researchers have developed a series of catalysts for the selective hydrogenation of diolefins in order to increase the hydrogenation conversion rate of the catalyst while improving its hydrogenation selectivity, but the effect is not ideal

Method used

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  • A kind of diene selective hydrogenation catalyst and its preparation method and application
  • A kind of diene selective hydrogenation catalyst and its preparation method and application
  • A kind of diene selective hydrogenation catalyst and its preparation method and application

Examples

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Effect test

Embodiment 1

[0033] This example provides a catalyst for the selective hydrogenation of diolefins. Based on the weight of the catalyst carrier, the content of the active component palladium is 0.3 wt%, which is designated as catalyst A.

[0034] The catalyst is prepared by the following steps:

[0035] Dissolve 3.6 g of CTAB and 3.0 g of NaOH in 50 ml of deionized water, stir until completely dissolved, add 1.3 g of 2-methyl-1H-imidazole-4,5-dicarboxylic acid, and add 1.2 g of Zn( NO 3 ) 2 ·6H 2 O, obtain mixed reaction solution;

[0036] Pour the reaction solution into a 100 ml polytetrafluoroethylene reactor, crystallize at 140°C for 24 hours, cool naturally to room temperature after the reaction, separate the solid product by suction filtration, wash with deionized water, extract CTAB with absolute ethanol, and then The product was separated by centrifugation and dried at 100°C for 12 hours to make a catalyst carrier FZIF-8. Its XRD spectrum is as follows: figure 1 shown;

[0037]...

Embodiment 2

[0039] This example provides a catalyst for the selective hydrogenation of diolefins. Based on the weight of the catalyst carrier, the content of the active component palladium is 0.3 wt%, which is designated as catalyst B. The particle size distribution of palladium is shown in Figure 2B shown.

[0040] The preparation method is the same as in Example 1, except that the amount of CTAB is changed to 2.6 grams.

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Abstract

A selective hydrogenation catalyst for alkadiene. A carrier of the catalyst is a carboxyl-functionalized step hole FZIF-8, an active component is palladium, and the content of the active component ranges from 0.1% to 10% on the basis of the total weight of the carrier of the catalyst. A method for preparing the catalyst comprises: mixing and crystallizing raw materials, and conducting extraction and drying to obtain an FZIF-8 carrier, and making palladium immerse the carrier, so as to obtain the catalyst. Uses of the catalyst in a selective hydrogenation reaction for alkadiene are also provided. A step hole structure is formed in the carrier of the catalyst, so that carboxyl groups have accessibility, and the active components and the carboxyl groups can mutually interact; the carboxyl groups are contained in the carrier of the catalyst, and can anchor the active components, so that high dispersion of the active components is achieved, agglomeration and drain of the active components during the reaction are prevented, and the catalyst has high activity.

Description

technical field [0001] The invention relates to a diolefin selective hydrogenation catalyst, a preparation method and application thereof, and belongs to the technical field of catalyst preparation. Background technique [0002] The 21st century is a new era of developed economy and clean environment. The research and development of environmentally friendly clean fuels is one of the most important research topics in green chemistry. [0003] In recent years, the problem of air pollution has become increasingly prominent, and the problem of smog has become more and more serious. China's smog standard was officially implemented on January 1, 2013. However, since 2013, the central and eastern regions of China have been hit by smog. About 7 times the average concentration limit. PM2.5 has increasingly become the focus of public attention. In my country's energy consumption, coal and oil account for about 90%. It is generally believed that coal and oil contribute the most to m...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/22B01J35/10C10G45/40
CPCB01J23/44B01J31/22B01J37/02
Inventor 范煜贾晓千王世华
Owner CHINA UNIV OF PETROLEUM (BEIJING)
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