Modeling pVT Properties and Vapor-Liquid Equilibrium of Ionic Liquids Using Cubic-plus-association Equation of State
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Ma Jun
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机构:E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Ma Jun
Li Jinlong
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机构:E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Li Jinlong
Fan Dongfu
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机构:E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Fan Dongfu
Peng Changjun
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E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R ChinaE China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Peng Changjun
[1
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Liu Honglai
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机构:E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Liu Honglai
Hu Ying
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机构:E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Hu Ying
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[1] E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
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.