Fully thermally coupled distillation column design for liquid petroleum gas recovery

U. Hosanna, A. Goyal, Minchul Ha, Kim Se Jung, K. Hwang
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Abstract

A fully thermally coupled distillation column is conceived and applied to a system of pretreated natural gas stream containing C3 through nC7. The design procedure consists of computation of limiting requirements and rigorous simulation using material and energy balances. The results of the proposed design are compared with those of the conventional two-column system; the comparison shows that the fully thermally coupled distillation column requires 30.8% less energy than conventional system. From the required energy, the thermodynamic efficiency of fully thermally coupled distillation column is higher than that of conventional distillation system in the separation of the ternary mixture considered in this study.
液化石油气回收全热耦合精馏塔设计
设计了一种全热耦合精馏塔,并将其应用于含C3至nC7的天然气预处理系统。设计过程包括极限要求的计算和使用材料和能量平衡的严格模拟。将设计结果与传统的双柱系统进行了比较;结果表明,全热耦合精馏塔比常规系统能耗降低30.8%。从所需要的能量来看,本研究所考虑的三元混合物分离中,全热耦合精馏塔的热力学效率高于常规精馏系统。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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