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
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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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