Modified method for producing alkylbenzene
A production method and technology of alkylbenzene, applied in the direction of chemical instruments and methods, hydrocarbons, hydrocarbons, etc., can solve the problem of accelerating catalyst carbon deposition and deactivation, affecting the selectivity of the target product mono-alkylbenzene, and affecting the alkyl Catalyst life and other issues, to achieve the effect of flexible operation and prolonging the operation cycle
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Embodiment 1
[0061] According to the flow process of accompanying drawing 6, benzene and ethylene react to generate ethylbenzene. Alkylation reactor 5 is an alternative reaction zone reactor. The catalyst used in the alkylation reactor 5, the alkylation reactor 8 and the alkylation reactor 10 is the same alkylation catalyst. The reaction is carried out under the reaction conditions that the circulation weight ratio is 0.6, the ethylene conversion rate is 100%, the ethylbenzene selectivity is 87%, and the ethylation selectivity is greater than or equal to 99%. Benzene and recovered polyethylbenzene are reacted in a transalkylation reactor equipped with a transalkylation catalyst. The reaction conditions are as follows: the reaction temperature is 170-250° C., the reaction pressure is 3.0 MPa, and the molar ratio of the phenyl group to the alkyl group is 12. The single-pass conversion of diethylbenzene in the reactants was 87.3%, and the ethylbenzene selectivity was 100%. The transalkylat...
Embodiment 2
[0064] According to the flow process of accompanying drawing 6, benzene and propylene react to generate cumene. Alkylation reactor 5 is an alternative reaction zone reactor. The catalyst used in the alkylation reactor 5, the alkylation reactor 8 and the alkylation reactor 10 is the same alkylation catalyst. The reaction is carried out under the condition that the weight ratio is 0.4, the conversion rate of propylene is 100%, the selectivity of cumene is 89%, and the selectivity of isopropylation is ≥99%. The benzene and recovered dicumylbenzene are reacted in a transalkylation reactor equipped with a transalkylation catalyst. The reaction conditions are: a reaction temperature of 160-240° C. and a reaction pressure of 2.6 MPa. The single-pass conversion rate of cumene in the reactant is 80%, and the selectivity of cumene is greater than 99%. The transalkylation reaction product and the alkylation product are sent to the rectification system for separation to obtain benzene,...
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