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Effect of thermodynamic parameters on prediction of phase behavior and process design of extractive distillation 被引量:3

Effect of thermodynamic parameters on prediction of phase behavior and process design of extractive distillation
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摘要 Extractive distillation was investigated for separation of the minimum azeotrope of n-propanol/water, via the Aspen Plus simulation platform. Experimental data of n-propanol/water, which could pass the thermodynamic consistency test, were regressed to get suitable binary interaction parameters(BIPs) by the UNIQUAC thermodynamic model. The azeotrope system was heterogeneous in the simulation with built-in BIPs, which was contrary to the experimental data. The study focused on the effect of thermodynamic parameters on the prediction of phase behavior, and process design of extractive distillation. N-methyl-2-pyrrolidone(NMP) and ethylene glycol were used as solvents to implement the separation. Processes with built-in and regressed BIPs were explored,based on the minimum total annual cost(TAC). There were significant differences in the phase behavior simulation using different thermodynamic parameters, which showed the importance of BIPs in the design and optimization of extractive distillation. Extractive distillation was investigated for separation of the minimum azeotrope of n-propanol/water, via the Aspen Plus simulation platform. Experimental data of n-propanol/water, which could pass the thermodynamic consistency test, were regressed to get suitable binary interaction parameters (BIPs) by the UNIQUAC thermody- namic model. The azeotrope system was heterogeneous in the simulation with built-in BIPs, which was contrary to the experimental data. The study focused on the effect of thermodynamic parameters on the prediction of phase behavior, and process design of extractive distillation. N-methyl-2-pyrrolidone (NMP) and ethylene glycol were used as solvents to implement the separation. Processes with built-in and regressed BIPs were explored, based on the minimum total annual cost (TAC). There were significant differences in the phase behavior simulation using different thermodynamic parameters, which showed the importance of BIPs in the design and optimization of extractive distillation.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2018年第5期993-1002,共10页 中国化学工程学报(英文版)
基金 Supported by the National Natural Science Foundation of China(21676152) the Key Research Project of Shandong Province(2016GSF116004)
关键词 Extractive distillation Thermodynamic parameters Phase behavior UNIQUAC TAC 行为模拟 热力学 蒸馏 设计 进程 预言 UNIQUAC 共沸混合物
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