original ) (raw )Vapor-liquid equilibria for binary mixtures of butyl ether with 2-furaldehyde and with 2-, 3-, and 4-heptanone
Stanley Sandler
J Chem Eng Data, 1988
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Vapour–liquid equilibrium measurements and correlation for the pentafluoroethane (R125) + n-butane (R600) system
Laura Fedele
Fluid Phase Equilibria, 2005
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Simulation of 1-alkene and n-alkane binary vapour–liquid equilibrium using different united-atom transferable force fields
Maciej Starzak , Peter Ahlstrom
Fluid Phase Equilibria, 2005
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Vapor-liquid equilibriums. Systems p-xylene-furfural and ethylbenzene-furfural
Pushpinder Puri
Journal of Chemical & Engineering Data, 1970
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Vapour–liquid equilibrium measurements and correlation of the difluoromethane (R32) + propane (R290) + 1,1,1,2,3,3,3-heptafluoropropane (R227ea) ternary mixture at temperatures from 269.85 to 328.35K
Dominique Richon
Fluid Phase Equilibria, 2004
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Liquid−Liquid Equilibria for Mixtures of (Furfural + an Aromatic Hydrocarbon + an Alkane) at T = 298.15 K
Sandile Zondi
Journal of Chemical & Engineering Data, 2003
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Vapor-liquid equilibria of hydrogen chloride, phosgene, benzene, chlorobenzene, ortho-dichlorobenzene, and toluene by molecular simulation
Jadran Vrabec
AIChE Journal, 2011
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Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T=308.15 K
Bal Raj Deshwal
Journal of Chemical Thermodynamics, 2004
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Measurement and theoretical prediction of the vapor–liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
Marcela P Cartes
Fuel and Energy Abstracts, 2011
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Vapour–liquid equilibrium data for the difluoromethane+1,1,1,2,3,3,3-heptafluoropropane system at temperatures from 283.20 to 343.38 K and pressures up to 4.5 MPa
Dominique Richon
International Journal of Refrigeration, 2003
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Vapor−Liquid Equilibrium for the Difluoromethane (R32) + n -Butane (R600) System
Laura Fedele
Journal of Chemical & Engineering Data, 2005
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Vapour-liquid equilibrium of the OPLS, optimized potentials for liquid simulations, model for binary systems of alkanes and alkanes + alcohols
Ivona Radović , Mirjana Kijevcanin
Journal of the Serbian Chemical Society, 2005
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Vapor–liquid equilibria for the binary system 2,2−dimethylbutane + 1,1−dimethylpropyl methyl ether (TAME) at 298.15, 318.15, and 338.15K
Juan Renuncio
Fluid Phase Equilibria, 2004
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Study of Thermodynamic Modeling of Isothermal and Isobaric Binary Mixtures in Vapor-Liquid Equilibrium (VLE) of Tetrahydrofuran with Benzene (303.15 K) Cyclohexane (333.15 K), Methanol (103 kPa), and Ethanol (100 kPa)
Erik Yanza
Thermo, 2021
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Vapor−Liquid Equilibria of the Binary n Butane (HC600) + Difluoromethane (HFC32), + Pentafluoroethane (HFC125), + 1,1,1,2-Tetrafluoroethane (HFC134a) Systems
Myungyoun Kim
Journal of Chemical and Engineering Data, 2005
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Vapour–liquid and vapour–liquid–liquid equilibrium modeling for binary, ternary, and quaternary systems of solvents
Sohrab Rohani
Fluid Phase Equilibria, 2012
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The vapour - liquid equilibrium of n -alkanes
S. Calero , Carlos Vega
Journal of Physics: Condensed Matter, 1996
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Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor–Liquid Equilibrium and Mixing Properties
juan ortega
Journal of Chemical & Engineering Data, 2013
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Vapor-liquid equilibria for model mixtures of coal-derived liquids. 1. Binary systems with 2-methylfuran
David Krevor
J Chem Eng Data, 1986
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Vapor–liquid equilibrium data for the propane+1,1,1,2,3,3,3-heptafluoropropane (R227ea) system at temperatures from 293.16 to 353.18 K and pressures up to 3.4 MPa
Dominique Richon
Fluid Phase Equilibria, 2002
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Vapor–liquid equilibria of the (hexafluoroethane+1,1,1-trifluoroethane) binary system from 258 to 343K up to 3.89MPa
Dominique Richon
International Journal of Refrigeration, 2009
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Isobaric Vapour–Liquid Equilibrium Data Measurement for a Binary System of Green Solvent 2-Methyltetrahydrofuran and Acetic acid at 101.3 kPa
Vyomesh Parsana
Arabian journal for science and engineering, 2018
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Vapor−Liquid Equilibria for Difluoromethane (R32) + and Pentafluoroethane (R125) + 1,1,1,3,3,3-Hexafluoropropane (R236fa) at 303.2 and 323.3 K
Sergio Bobbo
Journal of Chemical & Engineering Data, 1999
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Isothermal Vapor–Liquid Equilibrium Data for Binary Mixtures of Hexafluoroethane (R116) + n-Pentane or n-Hexane at Two Temperatures, 288 and 296 K
Dominique Richon
Journal of Chemical & Engineering Data, 2018
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Vapor–liquid equilibria of ethylene (C2H4)+decafluorobutane (C4F10) at 268–298K from experiment, molecular simulation and the Peng–Robinson equation of state
Prabir Nandi
Fluid Phase Equilibria, 2012
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