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Steady-state simulation of a reactive internally heat integrated distillation column (R-HIDiC) for synthesis of tertiary-amyl methyl ether (TAME)

机译:反应性内部热集成蒸馏塔(R-HIDiC)合成叔戊基甲基醚(TAME)的稳态模拟

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摘要

Tertiary-amyl methyl ether (TAME) is a very important fuel additive, which has attracted the attention of many researchers. In this article, the synthesis of TAME by a reactive internally heat integrated distillation column (R-HIDiC) is investigated. A complex mathematical formulation is developed for simulating the proposed reactive heat integrated distillation column (R-HIDiC), based on material balance, equilibrium, summation of mole fractions and enthalpy balance (MESH) equations. The suggested model is used for simulating an R-HIDiC for industrial production of TAME. The performance of the proposed R-HIDiC is compared to the conventional reactive distillation column which is usually used in TAME production plants. The model verification has been performed using industrial data of the conventional TAME reactive distillation. The simulation results show that the total energy consumption of the proposed R-HIDiC is about 22% less than that of the conventional reactive distillation column.
机译:叔戊基甲基醚(TAME)是非常重要的燃料添加剂,引起了许多研究人员的关注。在本文中,研究了通过反应性内部热集成蒸馏塔(R-HIDiC)合成TAME。基于物料平衡,平衡,摩尔分数总和和焓平衡(MESH)方程,开发了一种复杂的数学公式来模拟拟议的反应热集成蒸馏塔(R-HIDiC)。所建议的模型用于模拟工业用TAME的R-HIDiC。将拟议的R-HIDiC的性能与TAME生产厂通常使用的常规反应蒸馏塔进行了比较。已使用常规TAME反应蒸馏的工业数据进行了模型验证。仿真结果表明,所提出的R-HIDiC的总能耗比常规反应蒸馏塔的总能耗低约22%。

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