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Suspension catalytic distillation of simultaneous alkylation and transalkylation for producing cumene

机译:悬浮催化蒸馏同时烷基化和烷基转移生产异丙基苯

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摘要

This work deals with the improvement of the suspension catalytic distillation (SCD)process.An improved process that alkylation and transalkylation reactions for producting cumene are carried out simulataneously i a scd column,was put forward.The inetic data of alkylation of benzene with proplyene oer a modified beta-zeolite catalyst,YSBH-01,were determined in a fixed-bed laboratory micro-reactor.On this basis,the equilirium stage (EQ)model (MESHR equatins)is established to simulate the SCD column.The performance of The SCD column is discussed.The innovation present in this work for the SCD process is also suitable for the fixed-bed catalytic distillation (FCD)process for producing cumene.
机译:这项工作是对悬浮催化蒸馏(SCD)工艺的改进。提出了一种在scd柱上同时进行异丙基苯烷基化和烷基转移反应的改进工艺。苯与丙烯的烷基化反应动力学数据在固定床实验室微型反应器中测定了改性的β-沸石催化剂YSBH-01。在此基础上,建立了平衡阶段(EQ)模型(MESHR equatins)来模拟SCD色谱柱。 SCD工艺的这项工作中的创新也适用于生产异丙苯的固定床催化蒸馏(FCD)工艺。

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