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作 者:Lianjie Wu Kun Lu Qirui Li Lianghua Xu Yiqing Luo Xigang Yuan
机构地区:[1]Tianjin Key Laboratory of Organic Solar Cells and Photochemical Conversion,College of Chemical and Chemical Engineering,Tianjin University of Technology,Tianjin 300384,China [2]State Key Laboratory of Chemical Engineering,Tianjin University,Tianjin 300072,China
出 处:《Chinese Journal of Chemical Engineering》2024年第4期1-7,共7页中国化学工程学报(英文版)
基 金:supported by the National Natural Science Foundation of China(21406170);the State Key Laboratory of Chemical Engineering(SKL-ChE-22B02).
摘 要:A huge amount of energy is always consumed to separate the ternary azeotropic mixtures by distillations.The heterogeneous azeotropic distillation and the pressure-swing distillation are two kinds of effective technologies to separate heterogeneous azeotropes without entrainer addition.To give better play to the synergistic energy-saving effect of these two processes,a novel pressure-swing-assisted ternary heterogeneous azeotropic distillation(THAD)process is proposed firstly.In this process,the ternary heterogeneous azeotrope is decanted into two liquid phases before being refluxed into the azeotropic distillation column to avoid the aqueous phase remixing,and three columns'pressures are modified to decrease the flowrates of the recycle streams.Then the dividing wall column and heat integration technologies are introduced to further reduce its energy consumption,and the pressureswing-assisted ternary heterogeneous azeotropic dividing-wall column and its heat integration structure are achieved.A genetic algorithm procedure is used to optimize the proposed processes.The design results show that the proposed processes have higher energy efficiencies and lower CO_(2)emissions than the published THAD process.
关 键 词:DISTILLATION SEPARATION Process control Process systems
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