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Multiple Analysis in a Reactive Distillation Column for the Synthesis of tert-Amyl Methyl Ether

机译:反应精馏塔中叔戊基甲基醚合成的多重分析

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摘要

tert-Amyl methyl ether (TAME) is produced via reactive distillation. A simulation is set up and controlled on Aspen HYSYS v 8.0 for generating the highest purity of TAME. This simulation includes a plug-flow reactor and a reactive distillation column. Emphasis was put on finding the optimal operating conditions of the reactive distillation column in order to get the maximum purity of TAME. The operational parameters were reflux ratio, number of reactive stages in the distillation column, and condenser pressure. The results indicated the optimal reflux ratio and condenser pressure which could be adapted to industrial scale.
机译:叔戊基甲基醚(TAME)通过反应蒸馏生产。在Aspen HYSYS v 8.0上建立并控制了仿真,以生成最高纯度的TAME。该模拟包括活塞流反应器和反应蒸馏塔。重点放在寻找反应蒸馏塔的最佳操作条件上,以获得最大纯度的TAME。操作参数为回流比,蒸馏塔中反应段数和冷凝器压力。结果表明最佳的回流比和冷凝器压力可以适应工业规模。

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