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Isobutane oxidative dehydrogenation catalyst, preparation method and application thereof

A technology for oxidative dehydrogenation and isobutane, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., and can solve problems such as low selectivity

Active Publication Date: 2020-08-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] One of the technical problems to be solved by the present invention is the low selectivity of isobutane oxidative dehydrogenation catalysts with chromium as the active component in the prior art, and a new isobutane oxidative dehydrogenation catalyst is provided

Method used

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  • Isobutane oxidative dehydrogenation catalyst, preparation method and application thereof
  • Isobutane oxidative dehydrogenation catalyst, preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Weigh 2.0 g of HMS carrier in the container, transfer 1.0 ml of 0.01003 g / ml chromium nitrate solution with a pipette, then transfer 1.0 ml of 0.01007 g / ml cerium nitrate solution with a pipette, and then add deionized water to 40 After stirring evenly, let it stand at room temperature for 4 hours, then add a magnetic stir bar and put it in a 60°C magnetic stirring constant temperature water bath to evaporate to dryness, then put it in a 100°C oven for 24 hours, and finally put it in a 600°C muffle furnace Medium roasting for 4 hours to obtain the desired catalyst. Adjust the flow of carbon dioxide and isobutane through a mass flow meter, the molar ratio of which is 5.0, enter the distributor for pre-mixing, and then enter the reaction zone. The reactor is heated by electric heating wire to make it reach the predetermined temperature. The inner diameter of the reactor is 8 mm stainless steel pipe, about 400 mm long. After the reaction gas passes through the condensatio...

Embodiment 2

[0034] Weigh 2.0 g of HMS carrier in the container, transfer 12.6 ml of 0.02308 g / ml chromium nitrate solution with a pipette, then transfer 3.1 ml of 0.01603 g / ml cerium nitrate solution with a pipette, and then add deionized water to 40 After stirring evenly, let it stand at room temperature for 24 hours, then add a magnetic stirrer and put it in a 85°C magnetic stirring constant temperature water bath to evaporate to dryness, then put it in a 120°C oven for 28 hours, and finally put it in a 650°C muffle furnace Medium roasting for 4 hours to obtain the desired catalyst. The evaluation conditions are the same as in [Example 1], and the results are as follows: the conversion rate of isobutane in this process is 40.0%, and the selectivity of isobutene is 92.0%.

Embodiment 3

[0036] Weigh 2.0 g of HMS carrier in the container, transfer 34.2 ml of 0.02308 g / ml chromium nitrate solution with a pipette, and then transfer 25.0 ml of 0.01603 g / ml cerium nitrate solution with a pipette, stir well, and Let it stand for 8 hours, then add a magnetic stirrer and put it in a 90°C magnetic stirring constant temperature water bath to evaporate to dryness, then put it in a 150°C oven for 36 hours, and finally roast it in a 800°C muffle furnace for 2 hours to obtain the required catalyst. The evaluation conditions are the same as in [Example 1], and the results are as follows: in this process, the conversion rate of isobutane is 35.3%, and the selectivity of isobutene is 92.2%.

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Abstract

The invention relates to an isobutane oxydehydrogenation catalyst as well as a preparation method and application thereof and mainly aims at solving the problem of relatively low olefin selectivity ofthe catalyst containing chromium serving as an active component in the prior art. The problem is better solved by the technical scheme that a catalyst taking at least one of mesoporous molecular sieves HMS and MSU as a carrier, chromium as the active component and rare earth metal as an adjuvant, wherein the catalyst does not adopt precious metal so as to be low in cost. The catalyst has relatively high isobutene conversion ration and olefin selectivity when being applied to isobutene preparation realized by isobutane carbon dioxide oxydehydrogenation and can be used in industrial productionof isobutene realized by isobutane carbon dioxide oxydehydrogenation.

Description

technical field [0001] The invention relates to an isobutane oxidative dehydrogenation catalyst, a preparation method and an application thereof. Background technique [0002] Isobutylene is a very important chemical raw material. In chemical production, isobutylene is widely used and can be used to synthesize methyl tert-butyl ether (MTBE), ethyl tert-butyl ether (ETBE), butyl rubber, ABS Resin and more. With the expansion of the production scale of isobutene downstream products, the demand for isobutene is also increasing. The amount of isobutene obtained by the traditional method can no longer meet the demand of the market. In addition, my country is very rich in C4 resources, but compared with European and American countries, the utilization rate of C4 resources in my country is less than 40%, which is only about half of that in European and American countries, and it is mainly concentrated in the utilization of olefins, most of which are used as fuels. Bring about a h...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/03C07C5/333C07C11/09
CPCB01J29/0341B01J2229/18C07C5/324C07C5/3335C07C11/09
Inventor 危春玲缪长喜刘剑锋宋磊华伟明
Owner CHINA PETROLEUM & CHEM CORP