artículo académico

• Barotropic phenomena in binary mixtures.  FLUID PHASE EQUILIBRIA.  394:175-185. 2015
• Thermophysical properties of 1-Butyl-1-Methyl-Pyrrolidinium dicyanamide + H2O mixtures.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  60(12):3766-3775. 2015
• Comprehensive Characterization of Interfacial Behavior for the Mixture CO2 + H2O + CH4: Comparison between Atomistic and Coarse Grained Molecular Simulation Models and Density Gradient Theory.  JOURNAL OF PHYSICAL CHEMISTRY C.  118:24504-24519. 2014
• Experimental determination and theoretical prediction of the vapor-liquid equilibrium and interfacial tensions of the system methyl-tert-butyl ether+2,5-dimethylfuran.  FUEL.  116:183-190. 2014
• High-pressure densities and interfacial tensions of binary systems containing carbon dioxide plus n-alkanes: (n-Dodecane, n-tridecane, n-tettadecane).  FLUID PHASE EQUILIBRIA.  380:82-92. 2014
• High-pressure interfacial tensions for nitrogen plus ethanol, or hexane or 2-methoxy-2-methylbutane: A comparison between experimental tensiometry and Monte Carlo simulations.  JOURNAL OF SUPERCRITICAL FLUIDS.  89:78-88. 2014
• On the phase and interface behavior along the three-phase line of ternary Lennard-Jones mixtures: A collaborative approach based on square gradient theory and molecular dynamics simulations.  JOURNAL OF CHEMICAL PHYSICS.  141:1-12. 2014
• Phase equilibria and interfacial tensions in the systems ethanol+2-methoxy-2-methylbutane plus hexane.  FUEL.  117:996-1003. 2014
• Use of Equation of State and coarse Grained Simulations to Complement Experiments: Describing the Interfacial Properties of Carbon Dioxide + Eicosane Mixtures.  JOURNAL CHEMICAL & ENGINEERING DATA.  59:2928-2971. 2014
• Vapor-liquid equilibrium and interfacial tensions of the system ethanol plus hexane plus tetrahydro-2H-pyran.  FLUID PHASE EQUILIBRIA.  361:229-236. 2014
• Coarse-grained molecular dynamic simulations of selected thermophysical properties for 1-Butyl-3-methylimidazolium hexafluorophosphate.  JOURNAL OF MOLECULAR LIQUIDS.  186:106-115. 2013
• Dynamic modeling and simulation of an alembic pear wine distillation.  FOOD AND BIOPRODUCTS PROCESSING.  91(c4):447-456. 2013
• Experimental determination and theoretical modeling of the vapor-liquid equilibrium and densities of the binary system butan-2-ol + tetrahydro-2H-pyran.  FLUID PHASE EQUILIBRIA.  342:52-59. 2013
• Experimental determination and theoretical prediction of the vapor-liquid equilibrium and interfacial tensions of the system methyl-tert-butyl ether+2,5-dimethylfuran.  FUEL.  116:183-190. 2013
• Isobaric Vapor-Liquid Equilibrium and Isothermal Interfacial Tensions for the System Ethanol+2,5-Dimethylfuran.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  58(11):3226-3232. 2013
• Isobaric vapor-liquid equilibrium and isothermal surface tensions of 2,2 '-oxybis[propane]+2,5-Dimethylfuran.  FLUID PHASE EQUILIBRIA.  345:60-67. 2013
• Surface Tension of 1-Ethyl-3-methylimidazolium Ethyl Sulfate or 1-Butyl-3-methylimidazolium Hexafluorophosphate with Argon and Carbon Dioxide.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  58:1203-1211. 2013
• Experimental determination and theoretical modeling of the vapor-liquid equilibrium and surface tensions of hexane + tetrahydro-2H-pyran.  FLUID PHASE EQUILIBRIA.  316:55-65. 2012
• Vapor-Liquid Equilibrium, Densities , and Interfacial Tensions of the System Ethanol + Tetrahydro-2H-pyran.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  57:561-567. 2012
• Vapor-Liquid Equilibrium, Densities, and Interfacial Tensions of the System Hexane + 2,5-Dimethylfuran.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  57:2681-2688. 2012
• Interfacial Tensions of Binary Mixtures of Ethanol with Octane, Decane, Dodecane, and Tetradecane.  JOURNAL OF CHEMICAL THERMODYNAMICS.  43:1395-1400. 2011
• Measurement and Theoretical Prediction of the Vapor-Liquid Equilibrium, Densities and Interfacial Tensions of the System Hexane + 2-methoxy-2-methylbutane.  FLUID PHASE EQUILIBRIA.  308:15-24. 2011
• Solid-Liquid equilibrium using the SAFT-VR Equation of State: Solubility of Naphthalene and Acetic Acid in Binary Mixtures and Calculation of Phase Diagrams.  FLUID PHASE EQUILIBRIA.  54:137-147. 2011
• Vapor-Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-Methylbutane.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  56:3142-3148. 2011
• Vapor-Liquid Equilibrium in the Binary Systems 2-Butanol + tert-Amyl Methyl Ether, 2-Butanol + Heptane, and Heptane + tert-Amyl Methyl Ether.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  56:2256-2265. 2011
• Vapor-Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-Methylpropane.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  55:428-434. 2010
• Comments on "Experimental Isobaric Vapor-Liquid Equilibrium Data for Binary Mixtures of Cyclic Ethers with (1-Methylethyl)benzene" (Gill, B.K.; Rattan, V.K.; Kapoor, S. J. J. Chem. Eng. Data 2008, 53, 2041-2043.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  54:1165-1167. 2009
• Comments on "Joule-Thomson Inversion Curves and third Virial Coefficients for Pure Fluids from Molecular-Based Models" and Predicted Inversion Curve and Third Virial Coefficients of Carbon Dioxide at High temperatures.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  48:6901-6903. 2009
• Limiting conditions for the critical pressure step point behavior in the Global Phase Diagram of binary mixtures composed by spherical molecules of equal sizes.  JOURNAL OF SUPERCRITICAL FLUIDS.  48(2):108-119. 2009
• Some observations regarding the prediction of isochoric heat capacities by engineering EOS models.  FLUID PHASE EQUILIBRIA.  277(2):121-125. 2009
• A New Reference State for the Calculation of Activity Coefficients: Comment on the Paper "A Molecular Theory of the Activity Coefficient and their Reference Fugacities at the Supercritical State.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  47:5758-5760. 2008
• An Accurate Direct Technique for Parameterizing Cubic Equations of State. Part I. Determining the Cohesion Temperature Function in the Low Temperature Range.  FLUID PHASE EQUILIBRIA.  265:63-83. 2008
• An Accurate Direct Technique for Parameterizing Cubic Equations of State. Part II. Specializing Models for Predicting Vapor Pressures and Phase Densities.  FLUID PHASE EQUILIBRIA.  265:155-172. 2008
• An accurate Direct Technique for Parameterizing Cubic Equations of State. Part III. Application of a Crossover Treatment.  FLUID PHASE EQUILIBRIA.  264:201-210. 2008
• Phase Equilibria and Interfacial Tensions in the Systems Methyl tert-butyl Ether + Acetone + Cyclohexane, Methyl tert-butyl Ether + Acetone and Methyl tert-butyl Ether + Cyclohexane.  FLUID PHASE EQUILIBRIA.  273:68-77. 2008
• Vapor-Liquid Equilibria and Interfacial Tensions for the Ternary System Acetone +2-2'oxybis(propane)+ Cyclohexane and its Constituent Binary Systems.  FLUID PHASE EQUILIBRIA.  270:75-86. 2008
• Vapor-Liquid Equilibrium, Densities, and Interfacial Tensions for the System Benzene + Propan-1-ol.  PHYSICS AND CHEMISTRY OF LIQUIDS.  46:185-200. 2008
• Azeotropic Behavior of Dieterici Binary Fluids.  FLUID PHASE EQUILIBRIA.  257:18-26. 2007
• Phase Equilibrium Behavior in Water (1) + n-Alkane (2) Mixtures.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  46:947-954. 2007
• Vapor-Liquid Equilibrium, Densities, and Interfacial Tensions for the System Ethyl 1,1-dimethylethyl Ether (ETBE) + propan-1-ol.  FLUID PHASE EQUILIBRIA.  255:121-130. 2007
• Association and Molecular Chain Length Effects on Interfacial Behaviour.  PHYSICS AND CHEMISTRY OF LIQUIDS.  44:45-59. 2006
• Comments on "Computing all the Azeotropes in Refrigerant Mixtures Through Equations of State" by Naveed Aslam and Aydin K. Sunol (Fluid Phase Equilib. 2004, 224, 97-109).  FLUID PHASE EQUILIBRIA.  235:232-237. 2005
• Correlation and Prediction of Interface Tension for Fluid Mixtures: An Approach Based on Cubic Equations of State With the Wong-Sandler Mixing Rule.  JOURNAL OF PHASE EQUILIBRIA.  26(3):215-224. 2005
• On the Interfacial Behavior About the Schield Region.  INTERNATIONAL JOURNAL OF THERMOPHYSICS.  26(1):13-29. 2005
• Phase and Interface Behaviors in Type-I and Type-V Lennard-Jones Mixtures: Theory and Simulations.  JOURNAL OF CHEMICAL PHYSICS.  123:034505-1-034505-10. 2005
• Simulaneous Prediction of Interfacial Tension and Phase Equilibria in Binary Mixtures. An Approach Based on Cubic Equations of State With Improved Mixing Rules.  FLUID PHASE EQUILIBRIA.  227:225-238. 2005
• Simultaneous prediction of the critical and subcritical phase behavior in mixtures of ethane-n-alkanes.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  44(7):2292-2300. 2005
• Estimation of Interfacial Behavior Using the Global Phase Diagram Approach: I. Carbon Dioxide-n-Alkanes.  THERMOCHIMICA ACTA.  411:171-176. 2004
• Estimation of Liquid-Liquid-Vapor Equilibria in Binary Mixtures of n-Alkanes.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  43:5957-5964. 2004
• Global Phase Diagram Analysis of the Dieterici Equation of State.  PHYSICAL CHEMISTRY CHEMICAL PHYSICS.  22:5189-5194. 2004
• Interfacial Behavior in Type IV Systems.  INTERNATIONAL JOURNAL OF THERMOPHYSICS.  25(5):1395-1414. 2004
• Rebuttal to the Comments of Paul M. Mathias on "Unnoticed Pitfalls of Soave-Type Alpha Functions in Cubic Equations of State".  JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY.  43:1895-1896. 2004
• Simultaneous prediction of the critical and sub-critical phase behavior in mixtures using equations of state IV. Mixtures of chained n-alkanes.  CHEMICAL ENGINEERING SCIENCE.  59(3):633-643. 2004
• Estimation of Liquid-Liquid-Vapor Equilibria Using Predictive EOS Models. 1. Carbon Dioxide-n-Alkanes.  JOURNAL OF PHYSICAL CHEMISTRY B.  107:1864-1874. 2003
• Estimation of Phase Behavior in Mixtures of CO2 and C20 + n-Alkanes Using Predictive OS Models.  PHYSICS AND CHEMISTRY OF LIQUIDS.  41:623-637. 2003
• Isobaric Vapor-Liquid Equilibria and Densities for the Binary Systems Oxalane + Ethyl 1,1-Dimethylethyl Ether, Oxolane + 2-Propanol and Propan-2-One + Trichloromethane.  PHYSICS AND CHEMISTRY OF LIQUIDS.  41:283-301. 2003
• Isobaric Vapor-Liquid Equilibria for the Ternary System Oxolane + Ethyl 1,1-Dimethylethyl Ether + 2-Propanol at 50 kPa.  PHYSICS AND CHEMISTRY OF LIQUIDS.  41:493-501. 2003
• Simultaneous prediction of the critical and sub-critical phase behavior in mixtures using equations of state II. Carbon dioxide-heavy n-alkanes.  CHEMICAL ENGINEERING SCIENCE.  58(12):2529-2550. 2003
• Simultaneous prediction of the critical and sub-critical phase behavior in mixtures using equations of state III. Methane-n-alkanes.  CHEMICAL ENGINEERING SCIENCE.  58(19):4363-4376. 2003
• Unnoticed Pitfalls of Soave-Type Alpha Functions in Cubic Equations of State.  JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY.  42:5662-5673. 2003
• About the Relation Between the Empirical and Theoretically Based Parts of van der Waals-Like Equations of State.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  41:4414-4421. 2002
• Closed Loops of Liquid-Liquid Immiscibility Predicted by Semi-Empirical Cubic Equations of State and Classical Mixing Rules.  PHYSICAL CHEMISTRY CHEMICAL PHYSICS.  4:879-883. 2002
• Comments on "Development of a Universal Group Contribution Equation of State. 2, Prediction of Vapor-Liquid Equilibria for Asymmetric Systems" by Jens Ahlers and Jürgen Gmehling (Ind. Eng. Chem. Res. 2002, 41, 3489-3498).  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  41:6634-6634. 2002
• Isobaric Vapor-Liquid Equilibria and Densities for the System Ethyl 1,1-Dimethylethyl Ether + 2-Propanol.  PHYSICS AND CHEMISTRY OF LIQUIDS.  40:685-702. 2002
• Isobaric Vapor-Liquid Equilibria and Densities for the System Methyl 1,1-Dimethylethyl Ether + 2-Propanol.  PHYSICS AND CHEMISTRY OF LIQUIDS.  40:277-294. 2002
• Phase Equilibria in the Systems 1,1,1,2,3,4,4,5,5,5-Decafluoropentane + 2-Methylfuran, 2-Methylfuran + Oxolane and 1,1,1,2,3,4,4,5,5,5-Decafluoropentane + 2-Methylfuran + Oxolane at 35 kPa.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  47:1256-1262. 2002
• Phase Equilibria in the Systems 1-Hexene + Heptane and 1-Hexene ´Ethyl 1,1-Dimethylethyl Ether + Heptane at 94.00 kPa.  PHYSICS AND CHEMISTRY OF LIQUIDS.  40:277-281. 2002
• Prediction of High Phase Equilibria Using Cubic EOS. What Can Be Learned?.  CANADIAN JOURNAL OF CHEMICAL ENGINEERING.  80:927-942. 2002
• A Model-Free Approach Data Treatment of Vapor-Liquid Equilibrium Data in Ternary Systems. 1. Theory and Numerical Procedures.  JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY.  40:2134-2148. 2001
• A Model-Free Approach Data Treatment of Vapor-Liquid Equilibrium Data in Ternary Systems. 2. Applications.  JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY.  40:2149-2159. 2001
• Simultaneous prediction of the critical and sub-critical phase behavior in mixtures using equation of state I. Carbon dioxide-alkanols.  CHEMICAL ENGINEERING SCIENCE.  56(2):6485-6510. 2001
• Prediction of Azeotropic Behavior Using Equations of State.  FLUID PHASE EQUILIBRIA.  166:141-162. 1999