A review on thermodynamic modeling of pervaporation for organic compounds removal from dilute aqueous solutions
Publish Year: 1391
نوع سند: مقاله کنفرانسی
زبان: English
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شناسه ملی سند علمی:
ICECS01_006
تاریخ نمایه سازی: 23 خرداد 1392
Abstract:
Benzene, toluene, and xylene (BTX) isomers are major components of gasoline. They are also used extensively as solvents and feedstocks by chemical industries.Compared to other hydrocarbons, BTX have relatively high water solubility; accidental gasoline spills and leaky service station tanks are prime sources of aquifer contamination. Because of their water solubility and their acute toxicities and genotoxicities, BTX compo-nents are classified as priority pollutants by the U.S. Environmental Protection Agency.The thermodynamic models of Flory-Huggins, UNIFAC-FV and UNIFAC-ZM for separating mixtures of substances such as water/benzene, toluene/chloro-form and benzene/cyclohexane have been reviewed. A modified solution-diffusion model was established based on Flory-Huggins thermodynamic theory and Fujita's free volume theory. This model was used for description of mass transfer of benzene removal from dilute aqueous solutions through PDMS membranes. A predictive model was proposed based on solution-diffusion mechanism to predict mass transfer during pervaporation process. The solubility of components in the membrane was described by UNIFAC-FV model, and the diffusion coefficients in polymeric membrane were calculated by free volume and Vrentas-Duda theories. It has shown that the proposed model can be applied to select membrane materials and predict the permeation flux and selectivity of components through the polymeric membrane. A modified solution-diffusion model is proposed to account for the mass transport of penetrants in the polymer membrane. In the model, the group contribution method (UNIFAC-ZM model) is introduced to calculate the activity of penetrants in the polymer membrane. This model has advantage over the UNIFAC-FV model that it does not require the knowledge of the molar volumes of the system components
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Authors
Vida Zargar
Separation Processes Research Group (SPRG), Department of Engineering, University of Kashan, Kashan, Iran
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