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Cyclohexyl benzene catalyst and preparation method therefor

A cyclohexylbenzene and catalyst technology, applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of high content of dicyclohexylbenzene, increased energy consumption, material consumption of process units, etc.

Active Publication Date: 2016-01-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] One of the technical problems to be solved by the present invention is that the catalyst in the prior art causes the high content of the by-product dicyclohexylbenzene in the reaction, which causes the material consumption and energy consumption of the process unit of subsequent dealkylation of dicyclohexylbenzene to generate cyclohexylbenzene to increase. technical problem

Method used

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  • Cyclohexyl benzene catalyst and preparation method therefor

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] 1. Catalyst preparation

[0038] Weigh out 1.87gPdCl 2 Be dissolved in 1mol / L hydrochloric acid aqueous solution and be made into 80g solution I; Take by weighing 100g diameter and be the non-binding spherical hydrogen type BEA zeolite molecular sieve of 1mm (the mol ratio of silicon dioxide / alumina is 45); Solution I is loaded on On the hydrogen-type BEA zeolite molecular sieve, impregnate at room temperature for 12 hours, dry at 100°C for 12 hours, and roast at 450°C for 4 hours to prepare the desired catalyst.

[0039] 2. Catalyst evaluation

[0040] Get 10ml catalyst packing in the fixed-bed reactor, carry out activity evaluation after reduction activation, condition is as follows: the temperature of reaction is 140 ℃, and the molar ratio of benzene and hydrogen in the reaction raw material is 1, and the pressure of reaction is 2.0MPa (gauge pressure) , the weight space velocity of the raw material benzene for the reaction is 1.0h -1 .

[0041] For the convenien...

Embodiment 2

[0055] 1. Catalyst preparation

[0056] Weigh 0.83gPdCl 2 Dissolve in 1mol / L hydrochloric acid aqueous solution and be made into 40g solution I; Take 2.89gFe(NO 3 ) 3 ·6H 2 O was dissolved in water to make 40g solution II; then solution I and solution II were mixed evenly; weighed 100g of binder-free spherical hydrogen-type BEA zeolite molecular sieve with a diameter of 2mm (the molar ratio of silica / alumina was 45) , load the mixed solution on the hydrogen-type BEA zeolite molecular sieve, impregnate at room temperature for 12 hours, dry at 100°C for 12 hours, and calcinate at 450°C for 4 hours to prepare the desired catalyst.

[0057] 2. Catalyst evaluation

[0058] Catalyst evaluation method see embodiment 1.

[0059] For the convenience of comparison, the composition of the catalyst is listed in Table 1, and the evaluation results are listed in Table 2.

Embodiment 3

[0061] 1. Catalyst preparation

[0062] Weigh 0.83gPdCl 2 Dissolve in 1mol / L hydrochloric acid aqueous solution and be made into 40g solution I; Take 1.98g Co(NO 3 ) 3 ·6H 2 O was dissolved in water to make 40g solution II; then solution I and solution II were mixed evenly; weighed 100g of binder-free spherical hydrogen-type BEA zeolite molecular sieve with a diameter of 2mm (the molar ratio of silica / alumina was 45) ; The mixed solution is loaded on the hydrogen-type BEA zeolite molecular sieve, impregnated at room temperature for 12 hours, dried at 100°C for 12 hours, and calcined at 450°C for 4 hours to prepare the desired catalyst.

[0063] 2. Catalyst evaluation

[0064] Catalyst evaluation method see embodiment 1.

[0065] For the convenience of comparison, the composition of the catalyst is listed in Table 1, and the evaluation results are listed in Table 2.

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Abstract

The present invention relates to a cyclohexyl benzene catalyst and a preparation method therefor as well as a method for synthesizing cyclohexyl benzene by a benzene hydrogenation alkylation one-step process; and the technical problem that content of a byproduct dicyclohexyl benzene in a reaction is high due to a catalyst in the prior art is solved. The cyclohexyl benzene catalyst comprises a carrier and the following components in percentage by weight: (1) 0.05-2.0% of Pd; (2) 0-4.0% of at least one of iron series elements ; wherein the carrier acquires good effect for the technical scheme of a hydrogen-zeolite molecular sieve, and can be used for synthesizing cyclohexyl benzene by the benzene hydrogenation alkylation one-step process.

Description

technical field [0001] The invention relates to a catalyst for preparing cyclohexylbenzene, a preparation method thereof and a method for synthesizing cyclohexylbenzene by one-step hydroalkylation of benzene. Background technique [0002] Cyclohexylbenzene (CHB) is an important intermediate widely used in liquid crystals, plastics, coatings, adhesives and other fields. Cyclohexylbenzene liquid crystal has the characteristics of extremely high chemical stability, photochemical stability, low viscosity and excellent physical properties, and is one of the ideal materials for display devices. Cyclohexylbenzene is used as an additive for lithium-ion battery electrolyte, has anti-overcharge performance, and can improve the safety performance of the battery. In addition, phenol and cyclohexanone can be prepared through the peroxidation and decomposition reaction process of cyclohexylbenzene, which are used to produce bulk chemical raw materials such as phenolic resin, caprolactam ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/76B01J29/74C07C2/66C07C13/28
CPCY02P20/52
Inventor 黄琴琴王德举刘仲能唐之勤王辉
Owner CHINA PETROLEUM & CHEM CORP