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Catalyst for isobutane dehydrogenation to isobutene

A catalyst, isobutane technology, applied in the direction of catalyst, molecular sieve catalyst, carbon compound catalyst, etc., can solve the problem of low catalyst conversion rate

Active Publication Date: 2019-04-12
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 conversion rate of catalysts in the prior art, and a new catalyst for preparing isobutene from isobutane dehydrogenation is provided

Method used

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  • Catalyst for isobutane dehydrogenation to isobutene
  • Catalyst for isobutane dehydrogenation to isobutene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] 1. Catalyst preparation

[0037] Dissolve chromium nitrate equivalent to 5 grams of Cr2O3, gallium nitrate equivalent to 1.0 grams of Ga2O3, and magnesium nitrate equivalent to 2.5 grams of MgO in 100 ml of deionized water, mix with 91.5 grams of SBA-15 carrier, and stand at room temperature for 6 hours, then dried at 110°C for 30 hours, and finally roasted in a muffle furnace at 620°C for 5 hours to obtain the required catalyst. For the convenience of comparison, the composition of the catalyst is listed in Table 1.

[0038] 2. Catalyst evaluation

[0039] The catalyst prepared by the above-mentioned method carries out activity evaluation in the fixed-bed reactor, and the process is as follows:

[0040] The reactor is a stainless steel tube with an internal diameter of 8 mm and a length of 400 mm. The molar ratio of carbon dioxide and isobutane is 4.5, the reaction temperature is 595° C., the mass space velocity of isobutane is 1.2 hours −1 , and the reaction pressur...

Embodiment 2

[0057] 1. Catalyst preparation

[0058] Dissolve chromium nitrate equivalent to 5 grams of Cr2O3, gallium nitrate equivalent to 1.0 grams of Ga2O3, and calcium nitrate equivalent to 2.5 grams of CaO in 100 ml of deionized water, mix with 91.5 grams of SBA-15 carrier, and stand at room temperature for 6 hour, then dried at 110°C for 30 hours, and finally roasted in a muffle furnace at 620°C for 5 hours to obtain the required catalyst. For the convenience of comparison, the composition of the catalyst is listed in Table 1.

[0059] 2. Catalyst evaluation

[0060] The catalyst prepared by the above-mentioned method carries out activity evaluation in the fixed-bed reactor, and the process is as follows:

[0061] The reactor is a stainless steel tube with an internal diameter of 8 mm and a length of 400 mm. The molar ratio of carbon dioxide and isobutane is 4.5, the reaction temperature is 595° C., the mass space velocity of isobutane is 1.2 hours −1 , and the reaction pressure i...

Embodiment 3

[0064] 1. Catalyst preparation

[0065] Dissolve chromium nitrate equivalent to 5 g of Cr2O3, gallium nitrate equivalent to 1.0 g of Ga2O3, magnesium nitrate equivalent to 1.0 g of MgO, and calcium nitrate equivalent to 1.5 g of CaO in 100 ml of deionized water and mixed with 91.5 g of SBA-15 Carriers were mixed and allowed to stand at room temperature for 6 hours, then dried at 110°C for 30 hours, and finally calcined in a muffle furnace at 620°C for 5 hours to obtain the desired catalyst. For comparison, the composition of the catalyst is listed in Table 1.

[0066] 2. Catalyst evaluation

[0067] The catalyst prepared by the above-mentioned method carries out activity evaluation in the fixed-bed reactor, and the process is as follows:

[0068] The reactor is a stainless steel tube with an internal diameter of 8 mm and a length of 400 mm. The molar ratio of carbon dioxide and isobutane is 4.5, the reaction temperature is 595° C., the mass space velocity of isobutane is 1.2...

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Abstract

The invention relates to a catalyst for production of isobutene by dehydrogenation of isobutane and a preparation method and application thereof, and mainly solves the problem that the catalyst conversion rate is low in the prior art. The catalyst for production of isobutene by dehydrogenation of isobutane includes a carrier, an active component and an additive, the carrier of the catalyst is at least one of SBA-15, MCM-41 and HMS, chrome is used as the active component, one or a plurality of gallium and alkaline earth metals is / are used as the additive, and the catalyst better solves the problem that the catalyst conversion rate is low in the prior art. The catalyst can be used in industrial production of isobutene by dehydrogenation of isobutane in a carbon dioxide atmosphere.

Description

technical field [0001] The invention relates to a catalyst for preparing isobutene by dehydrogenating isobutane, a preparation method and 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. Br...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/03B01J29/04C07C5/333C07C11/09
CPCB01J29/0341B01J29/045C07C5/3335C07C2523/02C07C2523/08C07C2523/26C07C2529/03C07C2529/04C07C11/09
Inventor 危春玲缪长喜华伟明乐英红高滋
Owner CHINA PETROLEUM & CHEM CORP