Modeling pVT Properties and Vapor-Liquid Equilibrium of Ionic Liquids Using Cubic-plus-association Equation of State
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Modeling pVT Properties and Vapor-Liquid Equilibrium of Ionic Liquids Using Cubic-plus-association Equation of State
Modeling pVT Properties and Vapor-Liquid Equilibrium of Ionic Liquids Using Cubic-plus-association Equation of State
中国化学工程学报(英文版)2011年19卷第6期 页码:1009-1016
Affiliations:
State Key Laboratory of Chemical Engineering and Department of Chemistry, East China University of Science and Technology,Shanghai,China,200237
Author bio:
Funds:
Supported by the National Natural Science Foundation of China (20876041, 20736002);the National Basic Research Program of China (2009CB219902);the Program for Changjiang Scholars and Innovative Research Team in University of China(Grant IRT0721);the Programme of Introducing Talents of Discipline to Universities (Grant B08021) of China
马俊, 李进龙, 范冬福, 等. Modeling pVT Properties and Vapor-Liquid Equilibrium of Ionic Liquids Using Cubic-plus-association Equation of State[J]. 中国化学工程学报(英文版), 2011,19(6):1009-1016. DOI: 10.1016/S1004-9541(11)60084-0.
Properties and Vapor-Liquid Equilibrium of Ionic Liquids Using Cubic-plus-association Equation of State[J]. , 2011, 19(6): 1009-1016.
马俊, 李进龙, 范冬福, 等. Modeling pVT Properties and Vapor-Liquid Equilibrium of Ionic Liquids Using Cubic-plus-association Equation of State[J]. 中国化学工程学报(英文版), 2011,19(6):1009-1016. DOI: 10.1016/S1004-9541(11)60084-0.DOI:
Properties and Vapor-Liquid Equilibrium of Ionic Liquids Using Cubic-plus-association Equation of State[J]. , 2011, 19(6): 1009-1016.DOI: 10.1016/S1004-9541(11)60084-0.
Modeling pVT Properties and Vapor-Liquid Equilibrium of Ionic Liquids Using Cubic-plus-association Equation of State
Combining Peng-Robinson (PR) equation of state (EoS) with an association model derived from shield-sticky method (SSM) by Liu
et al
.
a new cubic-plus-association (CPA) EoS is proposed to describe the thermodynamic properties of pure ionic liquids (ILs) and their mixtures. The new molecular parameters for 25 ILs are obtained by fitting the experimental density data over a wide temperature and pressure range
and the overall average deviation is 0.22%. The model parameter
b
for homologous ILs shows a good linear relationship with their molecular mass
so the number of model parameters is reduced effectively. Using one temperature-independent binary adjustable parameter
k
ij
satisfactory correlations of vapor-liquid equilibria (VLE) for binary mixtures of ILs + non-associating solvents and + associating solvents are obtained with the overall average deviation of vapor pressure 2.91% and 7.01%
respectively. In addition
VLE results for ILs + non-associating mixtures from CPA
lattice-fluid (LF) and square-well chain fluids with variable range (SWCF-VR) EoSs are compared.
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references
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