Molecular separation in liquid phase: Development of mechanistic model in membrane separation of organic compounds

被引:27
作者
Ghadiri, Mehdi [1 ]
Mohammadi, Mehrnoush [2 ]
Asadollahzadeh, Mehdi [3 ]
Shirazian, Saeed [4 ,5 ]
机构
[1] Islamic Azad Univ, South Tehran Branch, Young Researchers & Elite Club, Tehran, Iran
[2] Islamic Azad Univ, South Tehran Branch, Dept Chem Engn, Tehran, Iran
[3] Iran Univ Sci & Technol, Dept Chem Engn, Tehran, Iran
[4] Ton Duc Thang Univ, Dept Management Sci & Technol Dev, Ho Chi Minh City, Vietnam
[5] Ton Duc Thang Univ, Fac Appl Sci, Ho Chi Minh City, Vietnam
关键词
Mechanistic modeling; Simulation; Separation; Membranes; Extraction; WASTE-WATER TREATMENT; MASS-TRANSFER SIMULATION; CONTINUOUS WET GRANULATION; BENZOIC-ACID; NUMERICAL-SIMULATION; CFD SIMULATION; COMPUTATIONAL SIMULATION; PERVAPORATION SEPARATION; REACTIVE EXTRACTION; AQUEOUS-SOLUTION;
D O I
10.1016/j.molliq.2018.04.101
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Membrane-based removal of benzoic acid from effluents was investigated in this work. A comprehensive predictive model was developed in order to describe and predict the continuous separation process for wastewater treatment. Separation of benzoic acid from wastewater using a hollow-fiber membrane module was modeled and simulated. Transport phenomena equations as well as extraction reaction of benzoic acid were taken into account upon developing the model of process. The model equations were solved using a numerical scheme based on finite element approach. Computational fluid dynamic tool was used for solution of the model's equations. The model findings were validated through comparing with measured values, and it was revealed that the model is valid for this particular process and can be used for design and optimization of the membrane -based benzoic acid removal. Moreover, the simulation results showed that the flow rate of aqueous phase (feed solution) has significant effect on the removal of benzoic acid from wastewater streams. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:336 / 344
页数:9
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