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Method used for preparing phenethylene through alkylation on side chains of toluene and methanol

A technology of alkylation and styrene, applied in chemical instruments and methods, catalyst activation/preparation, organic chemistry, etc., can solve the problems of low selectivity of ethyl styrene and low conversion rate of toluene

Active Publication Date: 2014-05-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The technical problem to be solved by the present invention is that the prior art has the problems of low conversion rate of toluene and low selectivity of ethylstyrene and styrene, and provides a new method for producing styrene by side chain alkylation of toluene and methanol

Method used

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  • Method used for preparing phenethylene through alkylation on side chains of toluene and methanol
  • Method used for preparing phenethylene through alkylation on side chains of toluene and methanol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Take 10 grams of silicon-aluminum molar ratio SiO 2 / Al 2 o 3 For X-type zeolite molecular sieve raw powder of 2, use 0.1mol / L potassium acetate as the exchange liquid to exchange the molecular sieve, and exchange 3 times at 50°C according to the solid-liquid ratio of 5, and each exchange time is 2 hours; then wash , suction filtration, and the filter cake was dried at 80° C. for 4 hours. The obtained molecular sieve was exchanged with 0.1mol / L magnesium nitrate as the exchange liquid, and exchanged three times at 50°C according to a solid-to-liquid ratio of 5, and each exchange time was 2 hours; after that, washing and suction filtration, the filter cake was Dry at 80°C for 4 hours. The molecular sieve was calcined at 500°C for 4 hours, and then cooled in a desiccator to obtain a KMgX type molecular sieve. Tablet forming and crushing into 40-60 mesh particles to obtain the finished catalyst.

[0023] 3.0 grams of the above-mentioned finished product catalysts are ...

Embodiment 2

[0026] Take 10 grams of silicon-aluminum molar ratio SiO 2 / Al 2 o 3 The original powder of Y-type zeolite molecular sieve is 4, and the molecular sieve is exchanged with 0.5mol / L potassium chloride as the exchange liquid, and exchanged three times at 90°C according to the solid-liquid ratio of 15, and each exchange time is 2 hours; After washing and suction filtration, the filter cake was dried at 150° C. for 4 hours. The obtained molecular sieve was exchanged with 0.5mol / L calcium chloride as the exchange liquid, and exchanged three times at 90°C according to the solid-to-liquid ratio of 15, and each exchange time was 2 hours; after that, washing, suction filtration, and filter cake Dry at 150°C for 4 hours. The molecular sieve was calcined at 800°C for 4 hours, and then cooled in a desiccator to obtain a KCaY molecular sieve. Tablet forming and crushing into 40-60 mesh particles to obtain the finished catalyst.

[0027] The activity evaluation was carried out according...

Embodiment 3

[0030] Take 10 grams of silicon-aluminum molar ratio SiO 2 / Al 2 o 3 For X-type zeolite molecular sieve raw powder of 2, use 1.0mol / L cesium nitrate as the exchange liquid to exchange the molecular sieve, and exchange 3 times at 80°C according to the solid-to-liquid ratio of 10, each exchange time is 2 hours; then wash , suction filtration, and the filter cake was dried at 110° C. for 4 hours. The obtained molecular sieve was exchanged with 1.0mol / L magnesium nitrate as the exchange liquid, and exchanged three times at 80°C according to the solid-to-liquid ratio of 10, and each exchange time was 2 hours; after that, washing and suction filtration, the filter cake was Dry at 110°C for 4 hours. The molecular sieve was calcined at 600° C. for 4 hours, and then cooled in a desiccator to obtain a CsMgX type molecular sieve. Tablet forming and crushing into 40-60 mesh particles to obtain the finished catalyst.

[0031] The activity evaluation was carried out according to the ev...

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Abstract

The invention relates to a method used for preparing phenethylene through alkylation on side chains of toluene and methanol, and mainly solves the problem in the prior art that the conversion rate of toluene is low and the selectivity of ethylbenzene and phenethylene is low. According to the invention, toluene and methanol are adopted as raw materials; the raw material and a catalyst contact and react to generate ethylbenzene and phenethylene under the condition that the molar ratio of toluene to methanol is (0.8-5):1, the reaction temperature is 350-450 DEG C, the reaction pressure is 0.08-0.15 MPa, and the mass space velocity of the raw materials is 1-5 h<-1>; the catalyst adopts alkali molecular sieves as a carrier; by the technical scheme of the method that one or more alkaline metals and one or more alkaline-earth metals are chosen to perform exchange modification on the molecular sieves, the problems in the prior art are excellently solved. The method can be applied to the industrial production of ethylbenzene and phenethylene through alkylation on the side chains of toluene and methanol.

Description

technical field [0001] The invention relates to a method for preparing ethylbenzene and styrene by side-chain alkylation of toluene and methanol. Background technique [0002] Researchers began to explore the process route of preparing styrene from toluene and methanol 30 years ago. This is mainly because compared with traditional processes, this method has the advantages of wide source of raw materials, low cost, low energy consumption, and less pollution. The use of petroleum and its processed products can also use natural gas. The reaction can be carried out under normal pressure, high temperature and large space velocity. Since Sidorenko et al first used alkali metal ion-exchanged X-type and Y-type zeolites as catalysts in 1967 to successfully synthesize styrene with toluene and methanol, this process route has received extensive attention, and there are more and more related researches. . [0003] According to current reports, the catalysts used in alkylation are mos...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C15/46C07C15/073C07C2/86C07C5/333B01J29/08B01J37/30
CPCY02P20/52
Inventor 高翔蒋见缪长喜
Owner CHINA PETROLEUM & CHEM CORP