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Catalysts for the production of isobutene

A catalyst and isobutylene technology, applied in molecular sieve catalysts, physical/chemical process catalysts, organic chemistry, etc., can solve problems such as poor catalyst stability, and achieve good stability and good technical effects

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 problem of poor catalyst stability in the prior art, and a new catalyst for isobutane dehydrogenation to isobutene is provided

Method used

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  • Catalysts for the production of isobutene
  • Catalysts for the production of isobutene
  • Catalysts for the production of isobutene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] 1. Catalyst preparation

[0040] Dissolve ammonium metavanadate equivalent to 8 grams of V2O5, cerium nitrate equivalent to 2.5 grams of CeO2, and antimony trichloride equivalent to 3.0 grams of Sb2O5 in 40 ml of 0.25 mol / L tartaric acid aqueous solution, and mix with 86.5 grams of MCF carrier , stood at room temperature for 8 hours, then dried at 120°C for 24 hours, and finally roasted in a muffle furnace at 620°C for 6 hours to obtain the desired catalyst. For comparison, the composition of the catalyst is listed in Table 1.

[0041] 2. Catalyst evaluation

[0042] The catalyst prepared by the above-mentioned method carries out activity evaluation in the fixed-bed reactor, and the process is as follows:

[0043] 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 5.0, the reaction temperature is 575° C., the mass space velocity of isobutane is 0.8 h −1 , and the reaction p...

Embodiment 2

[0060] 1. Catalyst preparation

[0061] Dissolve ammonium metavanadate equivalent to 8 grams of V2O5, neodymium nitrate equivalent to 2.5 grams of Nd2O3, and antimony trichloride equivalent to 3.0 grams of Sb2O5 in 40 ml of 0.25 mol / L tartaric acid aqueous solution, and mix with 86.5 grams of MCF carrier , stood at room temperature for 8 hours, then dried at 120°C for 24 hours, and finally roasted in a muffle furnace at 620°C for 6 hours to obtain the desired catalyst. For comparison, the composition of the catalyst is listed in Table 1.

[0062] 2. Catalyst evaluation

[0063] The catalyst prepared by the above-mentioned method carries out activity evaluation in the fixed-bed reactor, and the process is as follows:

[0064] 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 5.0, the reaction temperature is 575° C., the mass space velocity of isobutane is 0.8 h −1 , and the reacti...

Embodiment 3

[0067] 1. Catalyst preparation

[0068] Dissolve ammonium metavanadate equivalent to 8 grams of V2O5, neodymium nitrate equivalent to 1.0 grams of Nd2O3, cerium nitrate equivalent to 1.5 grams of CeO2, and antimony trichloride equivalent to 3.0 grams of Sb2O5 in 40 ml of 0.25 mol / L tartaric acid In the aqueous solution, mix with 86.5 grams of MCF carrier, let it stand at room temperature for 8 hours, then dry at 120°C for 24 hours, and finally roast in a muffle furnace at 620°C for 6 hours to obtain the required catalyst. For the convenience of comparison, the composition of the catalyst is listed in Table 1.

[0069] 2. Catalyst evaluation

[0070] The catalyst prepared by the above-mentioned method carries out activity evaluation in the fixed-bed reactor, and the process is as follows:

[0071] 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 5.0, the reaction temperature is ...

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Abstract

The invention relates to a catalyst for preparing isobutene, a preparation method for the catalyst and an application of the catalyst. The catalyst is mainly used for solving the problem in the prior art that the catalyst stability is poor. According to the catalyst, through adopting the technical scheme that the catalyst for preparing the isobutene through dehydrogenating isobutane contains a carrier, an active ingredient and auxiliaries, wherein at least one of MCF and SAPO serve as the carrier, vanadium serves as the active ingredient, and one or more of Sb and rare-earth metal serve as the auxiliaries, the technical problem is better solved, so that the catalyst can be applied to the industrial production of preparation of the isobutene through dehydrogenating the isobutane in a carbon dioxide atmosphere.

Description

technical field [0001] The invention relates to a catalyst for preparing isobutene, 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. Bring about a huge waste of res...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/035B01J29/85B01J29/03C07C1/24C07C11/09
Inventor 危春玲缪长喜宋磊张新玉华伟明
Owner CHINA PETROLEUM & CHEM CORP