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- W2375234915 abstract "The equilibrium(EQ) stage model has been used to simulate the alkylation of benzene with ethylene or propylene by reactive distillation.The calculated temperatures and liquid compositions agreed well with the available experimental data and non-equilibrium(NEQ) stage simulation,indicating that the EQ stage method is accurate and effective as a description of heterogeneous reactive distillation.The effects of varying the feed molar ratio of benzene to alkene,weight space velocity of benzene,reflux ratio and top pressure of the column on the alkene conversion,heat duty and total annual cost(TAC) were evaluated when ethylene and propylene were fed simultaneously.The conversion of both alkenes reached 100% when the molar ratios of benzene to ethylene and propylene were 3.5 and 2.0 respectively,the weight space velocity of benzene was 2 h-1,the reflux ratio was 10.0,the top pressure was 0.71 MPa and the catalyst packing was 18%.Furthermore,the TAC of the mixed feed was less than with ethylene or propylene as a single feed.Using conventional distillation,the separated yields of benzene,ethylbenzene and cumene were all over 95%." @default.
- W2375234915 created "2016-06-24" @default.
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- W2375234915 date "2011-01-01" @default.
- W2375234915 modified "2023-09-26" @default.
- W2375234915 title "Steady-state simulation of the alkylation of benzene with ethylene and propylene by reactive distillation" @default.
- W2375234915 hasPublicationYear "2011" @default.
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