Correlating Pure Component Properties with MOSCED Solubility Parameters: Enthalpy of Vaporization and Vapor Pressure

Tools to predict vapor–liquid phase equilibria are indispensable for the conceptualization and design of separation processes. Modified separation of cohesive energy density (MOSCED) is a solubility-parameter-based method parameterized to make accurate predictions of the limiting activity coefficient. As a solubility-parameter-based method, MOSCED can not only make quantitative predictions, but can shed light on the underlying intermolecular interactions. In the present study, we demonstrated the ability of MOSCED to correlate the enthalpy of vaporization and vapor pressure at a specific temperature using multiple linear regression. With this addition, MOSCED is able to predict vapor–liquid phase equilibria in the absence of reference data. This was demonstrated for the prediction of the Henry’s constant and solvation free energy of organic solutes in water, which was found to be superior to mod-UNIFAC. In addition to being able to make phase equilibrium predictions, the ability to correlate the enthalpy of vaporization and vapor pressure offers the opportunity to include additional properties in the regression of the MOSCED parameters. Given this success, we additionally attempted to correlate a wide range of physical properties using a similar expression. While, in some cases, the results were reasonable, they were inferior to the correlations of the enthalpy of vaporization and vapor pressure. Future efforts will be needed to improve the correlations.

[1]  Andrew S. Paluch,et al.  Expanding the Solubility Parameter Method MOSCED to Pyridinium-, Quinolinium-, Pyrrolidinium-, Piperidinium-, Bicyclic-, Morpholinium-, Ammonium-, Phosphonium-, and Sulfonium-Based Ionic Liquids , 2020, ACS omega.

[2]  Andrew S. Paluch,et al.  MOSCED parameters for 1-n-alkyl-3-methylimidazolium-based ionic liquids: Application to limiting activity coefficients and intuitive entrainer selection for extractive distillation processes , 2019, Journal of Molecular Liquids.

[3]  M. Abraham,et al.  Development of Abraham model expressions for predicting the standard molar enthalpies of vaporization of organic compounds at 298.15 K , 2019, Thermochimica Acta.

[4]  G. With,et al.  Generalization of Guggenheim's combinatorial activity coefficient equation , 2018, Journal of Molecular Liquids.

[5]  J. Elliott,et al.  Estimation of MOSCED parameters from the COSMO-SAC database , 2018 .

[6]  G. de With,et al.  On the calculation of nearest neighbors in activity coefficient models , 2018, Fluid Phase Equilibria.

[7]  Andrew S. Paluch,et al.  Predicting Limiting Activity Coefficients and Phase Behavior from Molecular Structure: Expanding MOSCED to Alkanediols Using Group Contribution Methods and Electronic Structure Calculations , 2018 .

[8]  Andrew S. Paluch,et al.  Application of MOSCED To Predict Limiting Activity Coefficients, Hydration Free Energies, Henry’s Constants, Octanol/Water Partition Coefficients, and Isobaric Azeotropic Vapor–Liquid Equilibrium , 2018 .

[9]  Andrew S. Paluch,et al.  GC-MOSCED: A group contribution method for predicting MOSCED parameters with application to limiting activity coefficients in water and octanol/water partition coefficients , 2017, Fluid Phase Equilibria.

[10]  G. Rothenberg,et al.  Revisiting Hansen Solubility Parameters by Including Thermodynamics , 2017, Chemphyschem : a European journal of chemical physics and physical chemistry.

[11]  Samantha M. Bozada,et al.  Predicting the equilibrium solubility of solid polycyclic aromatic hydrocarbons and dibenzothiophene using a combination of MOSCED plus molecular simulation or electronic structure calculations , 2017 .

[12]  Jeremy R. Phifer,et al.  Computing MOSCED parameters of nonelectrolyte solids with electronic structure methods in SMD and SM8 continuum solvents , 2017 .

[13]  Hannes H. Loeffler,et al.  Approaches for calculating solvation free energies and enthalpies demonstrated with an update of the FreeSolv database , 2017, bioRxiv.

[14]  Jürgen Gmehling,et al.  Further Development of Modified UNIFAC (Dortmund): Revision and Extension 6 , 2016 .

[15]  Andrew S. Paluch,et al.  Developing a Predictive Form of MOSCED for Nonelectrolyte Solids Using Molecular Simulation: Application to Acetanilide, Acetaminophen, and Phenacetin , 2016 .

[16]  David L. Mobley,et al.  FreeSolv: a database of experimental and calculated hydration free energies, with input files , 2014, Journal of Computer-Aided Molecular Design.

[17]  Gürkan Sin,et al.  Group-contribution+ (GC+) based estimation of properties of pure components: Improved property estimation and uncertainty analysis , 2012 .

[18]  Ali Eslamimanesh,et al.  Determination of Vapor Pressure of Chemical Compounds: A Group Contribution Model for an Extremely Large Database , 2012 .

[19]  C. Panayiotou,et al.  A new expanded solubility parameter approach. , 2012, International journal of pharmaceutics.

[20]  C. Panayiotou Redefining solubility parameters: the partial solvation parameters. , 2012, Physical chemistry chemical physics : PCCP.

[21]  J. Romagnoli,et al.  Use of Predictive Solubility Models for Isothermal Antisolvent Crystallization Modeling and Optimization , 2011 .

[22]  R. Missen On Criteria for Occurrence of Azeotropes in Isothermal and Isobaric Binary Systems , 2008 .

[23]  Timothy C. Frank,et al.  Application of MOSCED and UNIFAC to Screen Hydrophobic Solvents for Extraction of Hydrogen-Bonding Organics from Aqueous Solution , 2007 .

[24]  Laura C. Draucker,et al.  Experimental Determination and Model Prediction of Solid Solubility of Multifunctional Compounds in Pure and Mixed Nonelectrolyte Solvents , 2007 .

[25]  J. Gmehling,et al.  Further Development of Modified UNIFAC (Dortmund): Revision and Extension 5 , 2006 .

[26]  Peter W Carr,et al.  The chemical interpretation and practice of linear solvation energy relationships in chromatography. , 2006, Journal of chromatography. A.

[27]  F. Quina,et al.  A linear solvation energy relationship to predict vapor pressure from molecular structure , 2005 .

[28]  Charles A. Eckert,et al.  Revision of MOSCED Parameters and Extension to Solid Solubility Calculations , 2005 .

[29]  Jürgen Gmehling,et al.  A Modified UNIFAC (Dortmund) Model. 4. Revision and Extension , 2002 .

[30]  Jorge A. Marrero,et al.  Group-contribution based estimation of pure component properties , 2001 .

[31]  S. Verevkin,et al.  Measurement and Prediction of the Monocarboxylic Acids Thermochemical Properties , 2000 .

[32]  C. Eckert,et al.  Comparative Study of Semitheoretical Models for Predicting Infinite Dilution Activity Coefficients of Alkanes in Organic Solvents , 1999 .

[33]  Jürgen Gmehling,et al.  A Modified UNIFAC (Dortmund) Model. 3. Revision and Extension , 1998 .

[34]  C. Eckert,et al.  Developing models for infinite dilution activity coefficients using factor analysis methods , 1993 .

[35]  Kevin M. Stephenson,et al.  An improved MOSCED equation for the prediction and application of infinite dilution activity coefficients , 1989 .

[36]  J. Gmehling,et al.  A modified UNIFAC model. 1. Prediction of VLE, hE, and .gamma..infin. , 1987 .

[37]  Charles A. Eckert,et al.  Prediction of limiting activity coefficients by a modified separation of cohesive energy density model and UNIFAC , 1984 .

[38]  A. Beerbower,et al.  Expanded solubility parameter approach. I: Naphthalene and benzoic acid in individual solvents. , 1984, Journal of pharmaceutical sciences.

[39]  H. Billiet,et al.  Use of the solubility parameter for predicting selectivity and retention in chromatography , 1976 .

[40]  C. A. Smolders,et al.  The determination of solubility parameters of solvents and polymers by means of correlations with other physical quantities , 1975 .

[41]  V. Brandani Use of Infinite-Dilution Activity Coefficients for Predicting Azeotrope Formation at Constant Temperature and Partial Miscibility in Binary Liquid Mixtures , 1974 .

[42]  C. Eckert,et al.  Use of Infinite Dilution Activity Coefficients with Wilson's Equation , 1971 .

[43]  C. Hansen,et al.  The Universality of the Solubility Parameter , 1969 .

[44]  R. F. Blanks,et al.  Thermodynamics of Polymer Solubility in Polar and Nonpolar Systems , 1964 .

[45]  K. M. Watson,et al.  Thermodynamics of the Liquid State , 1943 .

[46]  Jiding Li,et al.  A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties , 1993 .

[47]  C. Eckert,et al.  Space predictor for infinite dilution activity coefficients , 1993 .

[48]  P. Carr,et al.  Predictive ability of the MOSCED and UNIFAC activity coefficient estimation methods , 1987 .

[49]  C. Eckert,et al.  Measurement and application of limiting activity coefficients , 1981 .