A kind of preparation method of high selectivity anti-carbon deposition benzene alkylation catalyst
A high-selectivity, carbophenane technology, applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve problems affecting the purity of styrene, increased benzene circulation, and increased energy consumption of industrial equipment , to achieve the effects of slowing down the deactivation rate of coking, reducing the probability of occurrence, and improving product quality
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Embodiment 1
[0037] The catalyst for the alkylation of benzene and ethanol was prepared by using MFI zeolite molecular sieve with high silicon-aluminum ratio as the matrix. The silicon-aluminum 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 sieves is carried out according to the method disclosed in the patent ZL201110364516.0 (a synthesis method of ZSM-5 zeolite). The extrusion molding of the above-mentioned zeolite molecular sieve adopts the acidified silicon ester hydrolyzate as the binder. The silicone grease hydrolysis conditions are: the silicone grease / water ratio is 1.0, the hydrolysis pH value is -1 Under certain conditions, the conversion rate of ethanol is greater than 99%. The product of reacting for 24 hours was analyzed and calculated, and the result showed that among the C8 aromatic products, the proportion of xylene impurities in the main product of ethylbenzene was 3...
Embodiment 2
[0039] Repeat Example 1, but use the above catalyst 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 certain conditions, the methanol conversion rate is greater than 99%. The product reacted for 48 hours was analyzed and calculated, and the result showed that in the C8 aromatic hydrocarbon product, the percentage of ethylbenzene impurity in the xylene main product was 8.0%. The one-way operation period of the catalyst is more than 3 months.
Embodiment 3
[0041] Repeat Example 1, but the silicon-aluminum ratio of the high-silicon-aluminum ratio MFI zeolite molecular sieve used is 600, and the grain size is between 200-300 nanometers. The hydrothermal synthesis of the above-mentioned molecular sieves is carried out according to the method disclosed in the patent ZL201110364516.0 (a synthesis method of ZSM-5 zeolite). The above catalyst was used in the gas phase alkylation reaction of benzene and ethanol. When the reaction temperature is 400°C, the reaction pressure is 1.0MPa, the benzene / ethanol molar ratio is 4, and the ethanol feed space velocity is 0.7h -1 Under certain conditions, the conversion rate of ethanol is greater than 99%. The product of reaction for 24 hours was analyzed and calculated, and the results showed that among the C8 aromatic products, the proportion of xylene impurities in the main product of ethylbenzene was 415ppm, and the one-way operation period of the catalyst was more than 6 months.
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