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A kind of ethylbenzene dehydrogenation catalyst and preparation method thereof

A technology of ethylbenzene dehydrogenation and catalyst, applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of high catalyst cost, difficult heat recovery, chromium catalyst poisoning, etc. Effects of hydrogen efficiency, reduction of carbon deposition, and improvement of catalytic performance

Inactive Publication Date: 2016-05-11
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The main disadvantages of the current technology are: (1) the reaction temperature is high; (2) the large amount of heat released by the liquefaction of water vapor in the gas-liquid separator is difficult to recover, and the energy consumption is huge
Chinese patents CN100413581C and CN100413830C improve CeO by adding precious metals Pt and Pd 2 -Cr 2 o 3 / Al 2 o 3 Catalytic activity and stability, but the cost of the catalyst is high and the chromium catalyst has a great poisonous effect on the human body and the environment
[0004] for CO 2 The main disadvantages of existing catalysts are the low catalyst activity and poor reaction stability, and the life of some catalysts is even only a few hours.

Method used

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  • A kind of ethylbenzene dehydrogenation catalyst and preparation method thereof
  • A kind of ethylbenzene dehydrogenation catalyst and preparation method thereof
  • A kind of ethylbenzene dehydrogenation catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Dissolve 14ml of tetrapropylammonium hydroxide (1mol / L) and 0.26g of aluminum isopropoxide in 65ml of distilled water, then add 20.8g of ethyl orthosilicate, and crystallize at 110°C for 4 hours to obtain a clear solution A; Dissolve 4.5g of cetyltrimethylammonium bromide in 80ml of sodium hydroxide solution (0.5mol / L), stir until completely dissolved, then mix with clear solution A, crystallize at 140°C for 9 hours, wash , filtered, dried, and calcined at 600°C for 4 hours to obtain ZSM-5 / MCM-48 microporous / mesoporous composite molecular sieve; using equal volume co-impregnation method, the required amount of ammonium metavanadate solution and cerium acetate solution were impregnated On 1g ZSM-5 / MCM-48 microporous / mesoporous composite molecular sieve, after standing at room temperature for 15 hours, dry at 110°C for 4 hours, and then bake at 550°C for 5 hours to obtain a weight percent composition of 4.5% CeO 2 -11%V 2 o 5 - 84.5% catalyst of ZSM-5 / MCM-48. The catal...

Embodiment 2~6

[0033] CeO 2 -V 2 o 5 -The preparation of ZSM-5 / MCM-48 catalyst and activity evaluation method are the same as embodiment 1, difference is to change CeO 2 , V2 o 5 And ZSM-5 / MCM-48 component content. Its weight percent composition and catalytic activity are shown in Table 1 and Table 2, respectively.

[0034] The weight percent composition of table 1 catalyst

[0035]

[0036]

[0037] Table 2 Catalysts in CO 2 Catalytic Activity in Dehydrogenation of Ethylbenzene under Atmosphere

[0038]

Conversion rate of ethylbenzene (%)

Styrene selectivity (%)

Styrene yield (%)

Example 1

75.2

98.7

74.2

Comparative example 1

66.4

82.5

54.8

Comparative example 2

61.9

95.2

58.9

Example 2

73.1

98.3

71.9

Example 3

65.8

98.9

65.1

Example 4

71.2

98.4

70.1

Example 5

75.0

98.8

74.1

Example 6

73.9

98.5

72.8

...

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Abstract

The invention discloses an ethylbenzene dehydrogenation catalyst and a preparation method thereof. A carrier of the ethylbenzene dehydrogenation catalyst is a ZSM-5 / MCM-48 micro-porous / meso-porous composite molecular sieve; an active component of the catalyst is V2O5; an auxiliary of the catalyst is CeO2. According to the ethylbenzene dehydrogenation catalyst and the preparation method thereof disclosed by the invention, the ZSM-5 / MCM-48 micro-porous / meso-porous composite molecular sieve is used as the carrier; the carrier is combined with the pore structural characteristics of two molecular sieves including micro-porous ZSM-5 and meso-porous MCM-48, therefore, high dispersion of the active component and the auxiliary is favorably realized; a rapid diffusion and transfer channel can be provided for molecules; generation of deposit carbon is slowed down; the catalytic performance of a vanadium-based catalyst for preparing vinyl benzene through ethylbenzene dehydrogenation in a CO2 atmosphere is improved; in addition, compared with the prior art, the ethylbenzene dehydrogenation catalyst has the advantages that under same reaction conditions, the catalytic performance is far prior to that of a traditional uni-structure molecular sieve loaded vanadium catalyst.

Description

technical field [0001] The invention belongs to the technical field of catalysts, in particular to a 2 Catalyst for the reaction of ethylbenzene dehydrogenation to styrene under atmosphere and its preparation method. Background technique [0002] Styrene is one of the basic products of the petrochemical industry and is widely used in the production of plastics, resins and synthetic rubber. Industrially, 90% of styrene is produced by dehydrogenating ethylbenzene at high temperature (600-650°C) on an iron oxide catalyst modified with potassium and other additives. Since the dehydrogenation of ethylbenzene to styrene is a strong endothermic reaction limited by thermodynamic equilibrium, in order to supply heat to the reaction, promote chemical equilibrium and prevent catalyst coking and deactivation, a large amount of superheated steam must be introduced in industrial production. The main disadvantages of the current technology are: (1) the reaction temperature is high; (2) t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/80C07C5/333C07C15/46
CPCY02P20/52
Inventor 陈树伟崔杏雨潘大海李瑞丰崔健秦张峰张海新
Owner TAIYUAN UNIV OF TECH