A kind of preparation method of highly selective benzene alkylation strip catalyst

A benzene alkylation, high selectivity technology, applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve problems that have not been solved well, affect the purity of styrene downstream products, limit the scope of application, etc. problems, achieve the effects of improving mechanical strength, slowing down the deactivation rate of coking, and prolonging the operation cycle

Active Publication Date: 2020-08-14
DALIAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because the small amount of xylene impurities generated by this side reaction will affect the purity of downstream products of styrene, limiting its application range
[0003] The preparation method of the benzene alkylation catalyst disclosed by the existing patent does not solve the above problems well

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Benzene and ethanol alkylation catalysts were prepared by using MFI zeolite molecular sieve with high silicon to aluminum ratio as the precursor. The silicon-alumina ratio of MFI zeolite molecular sieve is 800, and the grain size is between 200-300 nanometers. The hydrothermal synthesis of the above-mentioned molecular sieve is carried out according to the method disclosed in patent ZL201110364516.0 (a synthesis method of ZSM-5 zeolite). The extrusion molding of the above-mentioned zeolite molecular sieve adopts acidified silicon ester hydrolyzate as a binder. The conditions for the hydrolysis of silicone grease are: the ratio of silicone grease / water is 1.0, the pH value of hydrolysis is less than 1.0, the hydrolysis temperature is room temperature, and the hydrolysis time is 0.5h. The solid content in the gel of the hydrolyzed product after removing alcohol under negative pressure is 30 wt.%. The dry basis weight percent of molecular sieve in the extruded particulat...

Embodiment 2

[0037] Example 1 was repeated, but the above catalyst was used for the gas-phase alkylation of benzene and methanol at a reaction temperature of 400 °C, a reaction pressure of 1.0 MPa, a benzene / methanol molar ratio of 2, and a total feed space velocity of 2 h. -1 Under the same conditions, the methanol conversion rates were all greater than 99%. Taking the product of the reaction for 48 hours for analysis and calculation, the result shows that in the C8 aromatic hydrocarbon product, the percentage of ethylbenzene impurities in the main product of xylene is 8.3%.

Embodiment 3

[0039] Example 1 was repeated, but the high silicon-to-aluminum ratio MFI zeolite molecular sieve used had a silicon-to-aluminum ratio of 600 and a grain size of 200-300 nanometers. The hydrothermal synthesis of the above-mentioned molecular sieve is carried out according to the method disclosed in patent ZL201110364516.0 (a synthesis method of ZSM-5 zeolite). The resulting catalyst had an average particle strength of about 5 N / mm. The above catalysts were used in the gas phase alkylation of benzene and ethanol. At a reaction temperature of 400 °C, a reaction pressure of 1.0 MPa, a benzene / ethanol molar ratio of 4, and an ethanol feed space velocity of 0.7 h -1 Under the conditions, the ethanol conversion rate is greater than 99%. Taking the product of the reaction for 24 hours for analysis and calculation, the result shows that in the C8 aromatic product, the proportion of xylene impurities in the main product of ethylbenzene is 420ppm.

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Abstract

Disclosed is a preparation method of a high-selectivity benzene alkylation strip-shaped catalyst. The preparation method comprises the steps that an MFI zeolite molecular sieve with a high silica-alumina ratio is selected as a catalyst precursor; hydrolysate of acidified silicone grease and the MFI zeolite molecular sieve with the high silica-alumina ratio are subjected to strip-extrusion formation, then separation mother liquor obtained when the MFI zeolite molecular sieve with the high silica-alumina ratio is subjected to hydrothermal crystallization is used for treating a formed catalyst, and boride is added into the separation mother liquor; an ion exchange method is adopted for converting the strip-extrusion formed object, treated with the mother liquor, of the MFI zeolite molecular sieve with the high silica-alumina ratio into the hydrogenated alkylation catalyst. According to the method, the mother liquor generated during the hydrothermal synthesis of the MFI zeolite molecular sieve with the high silica-alumina ratio is used for treating the formed strip-shaped catalyst, the useful components in the mother liquor are recovered, the pore passages of the catalyst are cleared,and the environmental pollution in the full production chain of the alkylation catalyst is reduced. When the formed catalyst is treated with the mother liquor, by adding an appropriate amount of boride into the mother liquor, the mechanical strength of catalyst particles is improved, and the service life of the catalyst is conveniently prolonged.

Description

technical field [0001] The invention belongs to the technical field of petrochemical catalysts, and relates to a preparation method of a benzene alkylation catalyst. Background technique [0002] The gas-phase alkylation of benzene, methanol and ethanol can be used to synthesize xylene and ethylbenzene, respectively. The former can be used to produce p-xylene and then terephthalic acid; the latter can be used to dehydrogenate styrene to produce polyphenylene. Ethylene etc. Because of the generation of water, the alkylation of benzene and methanol, benzene and ethanol can only be carried out under the reaction conditions of high temperature and gas phase, so it faces the following common problem: how to reduce the mutual isomerization side between xylene and ethylbenzene reaction. That is, in the alkylation of benzene and methanol, the further isomerization reaction of the target product xylene to the by-product ethylbenzene should be minimized. The ethylbenzene by-product...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/40B01J35/02C07C2/86C07C15/08C07C15/073
CPCB01J29/40B01J35/02B01J2229/14C07C2/864C07C15/08C07C15/073Y02P20/52
Inventor 郭洪臣刘家旭钱吉祝全仁刘春燕易颜辉郭益铜
Owner DALIAN UNIV OF TECH
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