共沸蒸馏
共沸物
再沸器
化学
非随机双液模型
乙腈
热力学
色谱法
共沸混合物
蒸馏
分馏塔
萃取蒸馏
相对波动率
过程(计算)
分析化学(期刊)
有机化学
制冷剂
活度系数
气体压缩机
物理
水溶液
计算机科学
操作系统
作者
Kyung Won Kim,Jae Sun Shin,Sa Hoon Kim,Sung Kyu Hong,Jung Ho Cho,Soo‐Jin Park
摘要
In this study, a computational study has been performed to separate over 99.9 mol% of acetonitrile from binary azeotropic mixture of acetonitrile and water using a Pressure Swing Distillation process (PSD). The PSD process is used to separate azeotropic mixtures using the difference between the relative volatilities and azeotropic compositions by changing the system pressure. Non-Random Two Liquid (NRTL) model for liquid phase and the Peng–Robinson equation for vapor phase are used. An optimization study for the reflux ratio and feed stage locations which minimize the total reboiler heat duties are studied. Since the PSD process consists of two columns, i.e. high pressure (HP) and low pressure (LP), the effect of column sequences on the optimum process conditions is also reported.
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