Improvements of COSMO-SAC for vapor–liquid and liquid–liquid equilibrium predictions
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Stanley I. Sandler | Chieh-Ming Hsieh | S. Sandler | Chieh-Ming Hsieh | Shiang-Tai Lin | Shiang‐Tai Lin
[1] L. Manna,et al. QSPR prediction of N-boiling point and critical properties of organic compounds and comparison with a group-contribution method , 2008 .
[2] W. Arlt,et al. Liquid-liquid equilibrium data collection , 1979 .
[3] Jiding Li,et al. A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties , 1993 .
[4] S. S. Rath,et al. Multicomponent Liquid−Liquid Equilibria Prediction for Aromatic Extraction Systems Using COSMO-RS , 2007 .
[5] J. S. Rowlinson,et al. Molecular Thermodynamics of Fluid-Phase Equilibria , 1969 .
[6] J. Gmehling,et al. Prediction of liquid heat capacities by the group contribution equation of state VTPR , 2006 .
[7] J. Gmehling. Vapor-Liquid Equilibrium Data Collection , 1977 .
[8] S. Sandler,et al. Henry's law constant of organic compounds in water from a group contribution model with multipole corrections , 2002 .
[9] J. Gmehling,et al. PSRK: A Group Contribution Equation of State Based on UNIFAC , 1991 .
[10] Aage Fredenslund,et al. UNIFAC parameter table for prediction of liquid-liquid equilibriums , 1981 .
[11] Andreas Klamt,et al. COSMO-RS: From Quantum Chemistry to Fluid Phase Thermodynamics , 2005 .
[12] Y. A. Liu,et al. Sigma Profile Database for Predicting Solid Solubility in Pure and Mixed Solvent Mixtures for Organic Pharmacological Compounds with COSMO-Based Thermodynamic Methods , 2008 .
[13] R. Gani,et al. New group contribution method for estimating properties of pure compounds , 1994 .
[14] J. Gmehling,et al. A modified UNIFAC model. 1. Prediction of VLE, hE, and .gamma..infin. , 1987 .
[15] S. Sandler,et al. Infinite dilution activity coefficients from ab initio solvation calculations , 1999 .
[16] Aage Fredenslund,et al. Computerized Design of Multicomponent Distillation Columns Using the UNIFAC Group Contribution Method for Calculation of Activity Coefficients , 1977 .
[17] R. L. Robinson,et al. SVRC–QSPR model for predicting saturated vapor pressures of pure fluids , 2006 .
[18] Y. A. Liu,et al. Sigma-Profile Database for Using COSMO-Based Thermodynamic Methods , 2006 .
[19] J. Gmehling,et al. Performance of COSMO-RS with Sigma Profiles from Different Model Chemistries , 2007 .
[20] Tiancheng Mu,et al. Group contribution prediction of surface charge density profiles for COSMO‐RS(Ol) , 2007 .
[21] S. Sandler. Chemical and engineering thermodynamics , 1977 .
[22] Chieh-Ming Hsieh,et al. Prediction of liquid–liquid equilibrium from the Peng–Robinson+COSMOSAC equation of state , 2010 .
[23] Ashish Dwivedi,et al. Potential applications of artificial neural networks to thermodynamics: vapor–liquid equilibrium predictions , 1999 .
[24] Jorge A. Marrero,et al. Group-contribution based estimation of pure component properties , 2001 .
[25] Roger Hayward,et al. The Hydrogen Bond , 1960 .
[26] Stanley I. Sandler,et al. Refinement of COSMO−SAC and the Applications , 2007 .
[27] A. Klamt,et al. Refinement and Parametrization of COSMO-RS , 1998 .
[28] A. Klamt,et al. COSMO : a new approach to dielectric screening in solvents with explicit expressions for the screening energy and its gradient , 1993 .
[29] Design of a Combined Mixing Rule for the Prediction of Vapor−Liquid Equilibria Using Neural Networks , 1999 .
[30] S. Sandler,et al. Prediction of Octanol−Water Partition Coefficients Using a Group Contribution Solvation Model , 1999 .
[31] W. Goddard,et al. Application of the COSMO−SAC−BP Solvation Model to Predictions of Normal Boiling Temperatures for Environmentally Significant Substances , 2006 .
[32] John M. Stubbs,et al. Effects of conformational distributions on sigma profiles in COSMO theories. , 2005, The journal of physical chemistry. A.
[33] R. Danner,et al. Prediction of liquid-liquid equilibria with UNIFAC: a critical evaluation , 1987 .
[34] Aage Fredenslund,et al. Vapor−Liquid Equilibria by UNIFAC Group Contribution. 6. Revision and Extension , 1979 .
[35] William A. Goddard,et al. Prediction of Vapor Pressures and Enthalpies of Vaporization Using a COSMO Solvation Model , 2004 .
[36] Rafiqul Gani,et al. Estimation of the acentric factor and the liquid molar volume at 298 K using a new group contribution method , 1995 .
[37] R. Reid,et al. The Properties of Gases and Liquids , 1977 .
[38] Study of EOS‐Gex mixing rules for liquid–liquid equilibria , 1998 .
[39] Márcia M. C. Ferreira,et al. QSPR models of boiling point, octanol–water partition coefficient and retention time index of polycyclic aromatic hydrocarbons , 2003 .
[40] Svetoslav H. Slavov,et al. Rapid QSPR model development technique for prediction of vapor pressure of organic compounds , 2007, Comput. Chem. Eng..
[41] Stanley I. Sandler,et al. A Priori Phase Equilibrium Prediction from a Segment Contribution Solvation Model , 2002 .
[42] Jürgen Gmehling,et al. A Modified UNIFAC (Dortmund) Model. 3. Revision and Extension , 1998 .
[43] R. L. Robinson,et al. QSPR generalization of activity coefficient models for predicting vapor–liquid equilibrium behavior , 2007 .
[44] Jürgen Gmehling,et al. Performance of a Conductor-Like Screening Model for Real Solvents Model in Comparison to Classical Group Contribution Methods , 2005 .
[45] S. Sandler,et al. Multipole Corrections To Account for Structure and Proximity Effects in Group Contribution Methods: Octanol−Water Partition Coefficients , 2000 .
[46] Cheng-Ching Yu,et al. Plant-wide design and control of DMC synthesis process via reactive distillation and thermally coupled extractive distillation , 2010, Comput. Chem. Eng..
[47] A. Klamt. Conductor-like Screening Model for Real Solvents: A New Approach to the Quantitative Calculation of Solvation Phenomena , 1995 .
[48] Suojiang Zhang,et al. Prediction of infinite dilution activity coefficients in aqueous solutions by group contribution models. A critical evaluation , 1998 .