The Experts below are selected from a list of 195 Experts worldwide ranked by ideXlab platform
Sonia Loras - One of the best experts on this subject based on the ideXlab platform.
-
Isobaric vapor–liquid equilibrium for ternary mixtures of ethanol and methylcyclohexane with 3-Methylpentane and tert-butyl alcohol at 101.3 kPa
Fluid Phase Equilibria, 2007Co-Authors: † María Del Carmen Sánchez-russinyol, Antonio Aucejo, Sonia LorasAbstract:Abstract Consistent vapor–liquid equilibrium (VLE) data for the ternary systems 3-Methylpentane + ethanol + methylcyclohexane and ethanol + tert-butyl alcohol (TBA) + methylcyclohexane are reported at 101.3 kPa. The VLE data have been correlated by Wilson, UNIQUAC and NRTL equations. The ternary systems do not present azeotrope and are well predicted from binary interaction parameters.
-
phase equilibria in the systems 3 methylpentane methylcyclohexane diisopropyl ether methylcyclohexane and 3 methylpentane diisopropyl ether methylcyclohexane at 101 3 kpa
Fluid Phase Equilibria, 2002Co-Authors: Sonia Loras, Antonio Aucejo, Rosa MunozAbstract:Abstract Consistent vapor–liquid equilibria (VLE) at 101.3 kPa has been determined for the ternary system 3-Methylpentane+diisopropyl ether (DIPE)+methylcyclohexane and the binary subsystems 3-Methylpentane+methylcyclohexane and DIPE+methylcyclohexane in the temperature range from 336 to 374 K. According to the experimental results, the systems exhibit slight positive deviation from ideal behavior and no azeotrope is present. The VLE data have been correlated with the composition using the Wilson, UNIQUAC and NRTL relations. These models allow good prediction of the VLE properties of the ternary system from those of the pertinent binary subsystems.
-
Phase equilibria in the systems 3-Methylpentane + methylcyclohexane, diisopropyl ether + methylcyclohexane and 3-Methylpentane + diisopropyl ether + methylcyclohexane at 101.3 kPa
Fluid Phase Equilibria, 2001Co-Authors: Sonia Loras, Antonio Aucejo, Rosa MunozAbstract:Abstract Consistent vapor–liquid equilibria (VLE) at 101.3 kPa has been determined for the ternary system 3-Methylpentane+diisopropyl ether (DIPE)+methylcyclohexane and the binary subsystems 3-Methylpentane+methylcyclohexane and DIPE+methylcyclohexane in the temperature range from 336 to 374 K. According to the experimental results, the systems exhibit slight positive deviation from ideal behavior and no azeotrope is present. The VLE data have been correlated with the composition using the Wilson, UNIQUAC and NRTL relations. These models allow good prediction of the VLE properties of the ternary system from those of the pertinent binary subsystems.
-
isobaric vapor liquid equilibrium in the systems 3 methylpentane ethyl 1 1 dimethylethyl ether diisopropyl ether and tetrahydrofuran
Journal of Chemical & Engineering Data, 1999Co-Authors: Sonia Loras, Antonio Aucejo, And Rosa Muñoz, Jaime WisniakAbstract:New consistent vapor−liquid equilibrium data for the binary systems 3-Methylpentane + ethyl 1,1-dimethylethyl ether, + diisopropyl ether, and + tetrahydrofuran are reported at 101.3 kPa. The measured systems, which deviate from ideal behavior, can be described as symmetric solutions, and only the system 3-Methylpentane + tetrahydrofuran presents an azeotrope. The activity coefficients and boiling points of the solutions were correlated with composition by Wilson, UNIQUAC, NRTL, and Wisniak−Tamir equations.
-
Vapor–liquid equilibria in the systems 3-Methylpentane+methyl 1,1-dimethylethyl ether and 3-Methylpentane+methyl 1,1-dimethylpropyl ether at 101.3 kPa
Fluid Phase Equilibria, 1999Co-Authors: Sonia Loras, Antonio Aucejo, Rosa MunozAbstract:Abstract Pure-component vapor pressure of 3-Methylpentane and vapor–liquid equilibrium (VLE) for the binary systems of 3-Methylpentane with methyl 1,1-dimethylethyl ether (MTBE) and with methyl 1,1-dimethylpropyl ether (TAME) at 101.3 kPa have been measured. Both systems exhibit small positive deviations from ideality. They can be described as regular solutions and do not present azeotrope. The activity coefficients and boiling points of the solutions were correlated with its composition by Wilson, UNIQUAC, NRTL, and Wisniak–Tamir equations.
Antonio Aucejo - One of the best experts on this subject based on the ideXlab platform.
-
Isobaric vapor–liquid equilibrium for ternary mixtures of ethanol and methylcyclohexane with 3-Methylpentane and tert-butyl alcohol at 101.3 kPa
Fluid Phase Equilibria, 2007Co-Authors: † María Del Carmen Sánchez-russinyol, Antonio Aucejo, Sonia LorasAbstract:Abstract Consistent vapor–liquid equilibrium (VLE) data for the ternary systems 3-Methylpentane + ethanol + methylcyclohexane and ethanol + tert-butyl alcohol (TBA) + methylcyclohexane are reported at 101.3 kPa. The VLE data have been correlated by Wilson, UNIQUAC and NRTL equations. The ternary systems do not present azeotrope and are well predicted from binary interaction parameters.
-
phase equilibria in the systems 3 methylpentane methylcyclohexane diisopropyl ether methylcyclohexane and 3 methylpentane diisopropyl ether methylcyclohexane at 101 3 kpa
Fluid Phase Equilibria, 2002Co-Authors: Sonia Loras, Antonio Aucejo, Rosa MunozAbstract:Abstract Consistent vapor–liquid equilibria (VLE) at 101.3 kPa has been determined for the ternary system 3-Methylpentane+diisopropyl ether (DIPE)+methylcyclohexane and the binary subsystems 3-Methylpentane+methylcyclohexane and DIPE+methylcyclohexane in the temperature range from 336 to 374 K. According to the experimental results, the systems exhibit slight positive deviation from ideal behavior and no azeotrope is present. The VLE data have been correlated with the composition using the Wilson, UNIQUAC and NRTL relations. These models allow good prediction of the VLE properties of the ternary system from those of the pertinent binary subsystems.
-
Phase equilibria in the systems 3-Methylpentane + methylcyclohexane, diisopropyl ether + methylcyclohexane and 3-Methylpentane + diisopropyl ether + methylcyclohexane at 101.3 kPa
Fluid Phase Equilibria, 2001Co-Authors: Sonia Loras, Antonio Aucejo, Rosa MunozAbstract:Abstract Consistent vapor–liquid equilibria (VLE) at 101.3 kPa has been determined for the ternary system 3-Methylpentane+diisopropyl ether (DIPE)+methylcyclohexane and the binary subsystems 3-Methylpentane+methylcyclohexane and DIPE+methylcyclohexane in the temperature range from 336 to 374 K. According to the experimental results, the systems exhibit slight positive deviation from ideal behavior and no azeotrope is present. The VLE data have been correlated with the composition using the Wilson, UNIQUAC and NRTL relations. These models allow good prediction of the VLE properties of the ternary system from those of the pertinent binary subsystems.
-
isobaric vapor liquid equilibrium in the systems 3 methylpentane ethyl 1 1 dimethylethyl ether diisopropyl ether and tetrahydrofuran
Journal of Chemical & Engineering Data, 1999Co-Authors: Sonia Loras, Antonio Aucejo, And Rosa Muñoz, Jaime WisniakAbstract:New consistent vapor−liquid equilibrium data for the binary systems 3-Methylpentane + ethyl 1,1-dimethylethyl ether, + diisopropyl ether, and + tetrahydrofuran are reported at 101.3 kPa. The measured systems, which deviate from ideal behavior, can be described as symmetric solutions, and only the system 3-Methylpentane + tetrahydrofuran presents an azeotrope. The activity coefficients and boiling points of the solutions were correlated with composition by Wilson, UNIQUAC, NRTL, and Wisniak−Tamir equations.
-
Vapor–liquid equilibria in the systems 3-Methylpentane+methyl 1,1-dimethylethyl ether and 3-Methylpentane+methyl 1,1-dimethylpropyl ether at 101.3 kPa
Fluid Phase Equilibria, 1999Co-Authors: Sonia Loras, Antonio Aucejo, Rosa MunozAbstract:Abstract Pure-component vapor pressure of 3-Methylpentane and vapor–liquid equilibrium (VLE) for the binary systems of 3-Methylpentane with methyl 1,1-dimethylethyl ether (MTBE) and with methyl 1,1-dimethylpropyl ether (TAME) at 101.3 kPa have been measured. Both systems exhibit small positive deviations from ideality. They can be described as regular solutions and do not present azeotrope. The activity coefficients and boiling points of the solutions were correlated with its composition by Wilson, UNIQUAC, NRTL, and Wisniak–Tamir equations.
Jaime Wisniak - One of the best experts on this subject based on the ideXlab platform.
-
isobaric vapor liquid equilibrium in the systems 3 methylpentane ethyl 1 1 dimethylethyl ether diisopropyl ether and tetrahydrofuran
Journal of Chemical & Engineering Data, 1999Co-Authors: Sonia Loras, Antonio Aucejo, And Rosa Muñoz, Jaime WisniakAbstract:New consistent vapor−liquid equilibrium data for the binary systems 3-Methylpentane + ethyl 1,1-dimethylethyl ether, + diisopropyl ether, and + tetrahydrofuran are reported at 101.3 kPa. The measured systems, which deviate from ideal behavior, can be described as symmetric solutions, and only the system 3-Methylpentane + tetrahydrofuran presents an azeotrope. The activity coefficients and boiling points of the solutions were correlated with composition by Wilson, UNIQUAC, NRTL, and Wisniak−Tamir equations.
-
Isobaric Vapor−Liquid Equilibrium in the Systems 3-Methylpentane + Ethyl 1,1-Dimethylethyl Ether, + Diisopropyl Ether, and + Tetrahydrofuran
Journal of Chemical & Engineering Data, 1999Co-Authors: Sonia Loras, Antonio Aucejo, And Rosa Muñoz, Jaime WisniakAbstract:New consistent vapor−liquid equilibrium data for the binary systems 3-Methylpentane + ethyl 1,1-dimethylethyl ether, + diisopropyl ether, and + tetrahydrofuran are reported at 101.3 kPa. The measured systems, which deviate from ideal behavior, can be described as symmetric solutions, and only the system 3-Methylpentane + tetrahydrofuran presents an azeotrope. The activity coefficients and boiling points of the solutions were correlated with composition by Wilson, UNIQUAC, NRTL, and Wisniak−Tamir equations.
Rosa Munoz - One of the best experts on this subject based on the ideXlab platform.
-
phase equilibria in the systems 3 methylpentane methylcyclohexane diisopropyl ether methylcyclohexane and 3 methylpentane diisopropyl ether methylcyclohexane at 101 3 kpa
Fluid Phase Equilibria, 2002Co-Authors: Sonia Loras, Antonio Aucejo, Rosa MunozAbstract:Abstract Consistent vapor–liquid equilibria (VLE) at 101.3 kPa has been determined for the ternary system 3-Methylpentane+diisopropyl ether (DIPE)+methylcyclohexane and the binary subsystems 3-Methylpentane+methylcyclohexane and DIPE+methylcyclohexane in the temperature range from 336 to 374 K. According to the experimental results, the systems exhibit slight positive deviation from ideal behavior and no azeotrope is present. The VLE data have been correlated with the composition using the Wilson, UNIQUAC and NRTL relations. These models allow good prediction of the VLE properties of the ternary system from those of the pertinent binary subsystems.
-
Phase equilibria in the systems 3-Methylpentane + methylcyclohexane, diisopropyl ether + methylcyclohexane and 3-Methylpentane + diisopropyl ether + methylcyclohexane at 101.3 kPa
Fluid Phase Equilibria, 2001Co-Authors: Sonia Loras, Antonio Aucejo, Rosa MunozAbstract:Abstract Consistent vapor–liquid equilibria (VLE) at 101.3 kPa has been determined for the ternary system 3-Methylpentane+diisopropyl ether (DIPE)+methylcyclohexane and the binary subsystems 3-Methylpentane+methylcyclohexane and DIPE+methylcyclohexane in the temperature range from 336 to 374 K. According to the experimental results, the systems exhibit slight positive deviation from ideal behavior and no azeotrope is present. The VLE data have been correlated with the composition using the Wilson, UNIQUAC and NRTL relations. These models allow good prediction of the VLE properties of the ternary system from those of the pertinent binary subsystems.
-
Vapor–liquid equilibria in the systems 3-Methylpentane+methyl 1,1-dimethylethyl ether and 3-Methylpentane+methyl 1,1-dimethylpropyl ether at 101.3 kPa
Fluid Phase Equilibria, 1999Co-Authors: Sonia Loras, Antonio Aucejo, Rosa MunozAbstract:Abstract Pure-component vapor pressure of 3-Methylpentane and vapor–liquid equilibrium (VLE) for the binary systems of 3-Methylpentane with methyl 1,1-dimethylethyl ether (MTBE) and with methyl 1,1-dimethylpropyl ether (TAME) at 101.3 kPa have been measured. Both systems exhibit small positive deviations from ideality. They can be described as regular solutions and do not present azeotrope. The activity coefficients and boiling points of the solutions were correlated with its composition by Wilson, UNIQUAC, NRTL, and Wisniak–Tamir equations.
Carmen Gabaldón - One of the best experts on this subject based on the ideXlab platform.
-
Isobaric Vapor−Liquid Equilibria for the Binary System 3-Methylpentane + Ethanol and for the Ternary System 2-Methyl-2-propanol + Ethanol + 3-Methylpentane at 101.3 kPa
Journal of Chemical & Engineering Data, 2000Co-Authors: Carmen Gabaldón, V. Martínez-soria, Paula Marzal, Juan B. MontónAbstract:Isobaric vapor-liquid equilibria data were measured for the 3-Methylpentane + ethanol binary system and 2-methyl-2-propanol + ethanol + 3-Methylpentane ternary system at 101.3 kPa in a temperature range from 329 to 356 K. The data were found to be thermodynamically consistent according to the Van Ness-Byer-Gibbs method for the binary system and according to the McDermott-Ellis method for the ternary one. The binary system shows a minimum boiling azeotrope that boils at 327.9 K and contains 71.4 mol % 3-Methylpentane. The binary interaction parameters obtained from this work and literature data are used to predict the vapor-liquid equilibrium for the ternary system using the UNIQUAC, NRTL, and Wilson models. The ternary system is well predicted from binary data.
-
Isobaric vapor-liquid equilibria for the binary system 3-Methylpentane + 2-methyl-2-propanol and for the ternary system methyl 1,1-dimethylethyl ether + 3-Methylpentane + 2-methyl-2-propanol at 101.3 kPa
Journal of Chemical & Engineering Data, 1999Co-Authors: Carmen Gabaldón, Paula Marzal, And Juan B. Montón, Josep M. Penya-rojaAbstract:Isobaric vapor−liquid equilibria data were obtained for the 3-Methylpentane + 2-methyl-2-propanol binary system and methyl 1,1-dimethylethyl ether + 3-Methylpentane + 2-methyl-2-propanol ternary system at 101.3 kPa in a temperature range from 329 to 356 K. The data were found to be thermodynamically consistent according to the Van Ness−Byer−Gibbs method for the binary system and according to the McDermott−Ellis method for the ternary one. The binary system shows a minimum boiling azeotrope that boils at 333.4 K and contains 82.6 mol % of 3-Methylpentane. The binary interaction parameters obtained from this work and literature data are used to predict the vapor−liquid equilibrium for the ternary system using the UNIQUAC, NRTL, and Wilson models. The ternary system is well predicted from binary data.