首页> 外文期刊>The Journal of Supercritical Fluids >Modeling of phase equilibrium of binary mixtures composed by polystyrene and chlorofluorocarbons,hydrochlorofluorocarbons,hydrofluorocarbons and supercritical fluids using cubic and non-cubic equations of state
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Modeling of phase equilibrium of binary mixtures composed by polystyrene and chlorofluorocarbons,hydrochlorofluorocarbons,hydrofluorocarbons and supercritical fluids using cubic and non-cubic equations of state

机译:使用立方和非立方状态方程建模由聚苯乙烯和氯氟烃,氢氯氟烃,氢氟烃和超临界流体组成的二元混合物的相平衡

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摘要

The understanding of the polymer + solvent interactions is of fundamental importance in the development of new products and processes in several important industrial sectors,such as special paints,cosmetics,packing,manufacture of polymeric membranes,etc.Although the nature of these physical interactions is well known,the thermodynamic modeling of polymer + solvent systems in industrial applications presents difficulties,mainly due to the necessity to characterize not only the polymeric phase,in terms of properties that are easily measurable,but also the interaction of the polymer with the other components of low molar mass,through conveniently chosen parameters.In this work,the perturbed chain-statistical associating fluid theory (PC-SAFT) and Sanchez-Lacombe (SL) equations of state (EoS) are used in order to model the gas solubilities of binary systems composed by polystyrene and chlorofluorocarbons,hydrochlorofluorocarbons hydrofluorocarbons and supercritical fluids,which experimental data were obtained from the literature.The results were compared with those obtained by the traditional Peng-Robinson (PR) EoS.In each thermodynamic model,a one fluid-type van der Waals (vDW) mixing rule with conventional combination rules and a temperature-dependent binary interaction parameter were used.Solubilities correlated by the PC-SAFT EoS are in good agreement with the experimental data when compared with those obtained with the SL and PR EoS.
机译:对聚合物+溶剂相互作用的理解对于几个重要工业领域的新产品和工艺的开发至关重要,例如特种涂料,化妆品,包装,聚合物膜的制造等。尽管这些物理相互作用的本质是众所周知,在工业应用中对聚合物+溶剂体系的热力学建模存在困难,这主要是由于不仅需要根据易于测量的性质表征聚合物相,而且还需要表征聚合物与其他组分的相互作用。在这项工作中,使用扰动链统计缔合流体理论(PC-SAFT)和Sanchez-Lacombe(SL)状态方程(EoS)来模拟气体的溶解度。实验由聚苯乙烯和氯氟烃,氢氯氟烃,氢氟烃和超临界流体组成的二元体系从文献中获得数据,并将结果与​​传统的Peng-Robinson(PR)EoS获得的结果进行比较。在每个热力学模型中,一个流体类型的范德华(vDW)混合规则与常规组合规则和一个与SL和PR EoS相比,PC-SAFT EoS关联的溶解度与实验数据吻合良好。

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