The Experts below are selected from a list of 309 Experts worldwide ranked by ideXlab platform
Scott W. Campbell - One of the best experts on this subject based on the ideXlab platform.
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Total pressure measurements for benzene with 1-propanol, 2-propanol, 1-pentanol, 3-pentanol, and 2-methyl-2-butanol at 313.15 K
Fluid Phase Equilibria, 2001Co-Authors: Jonathon M. Rhodes, Venkat R. Bhethanabotla, Tyson A Griffin, Michael J Lazzaroni, Scott W. CampbellAbstract:Abstract Total pressure measurements at 313.15 K are reported for binary systems of benzene and 1-propanol, 2-propanol, 1-pentanol, 3-pentanol, and 2-methyl-2-butanol. The results are interpreted by an extended form of the Kretschmer–Wiebe association model, in which it is assumed that linear alcohol chains may solvate with a single benzene molecule.
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Total pressure measurements for 1-propanol + 1-pentanol, 1-propanol + 2-Pentanol, 2-propanol + 1-pentanol, and 2-propanol + 2-Pentanol at 313.15 K
Fluid Phase Equilibria, 1997Co-Authors: Kevin Mara, Venkat R. Bhethanabotla, Scott W. CampbellAbstract:Abstract Total pressure measurements at 313.15 K are reported for 1-propanol + 1-pentanol, 1-propanol + 2-Pentanol, 2-propanol + 1-pentanol, and 2-propanol + 2-Pentanol. The results were obtained using a Van Ness apparatus and were fitted to the three-suffix Margules equation using Barker's method. The Margules equation represents the data to within an average of 0.01 kPa.
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Total vapor pressure measurements for heptane + 1-pentanol, + 2-Pentanol, + 3-pentanol, + 2-methyl-1-butanol, + 2-methyl-2-butanol, + 3-methyl-1-butanol, and + 3-methyl-2-butanol at 313.15 K
Journal of Chemical & Engineering Data, 1997Co-Authors: Jonathon M. Rhodes, Venkat R. Bhethanabotla, Scott W. CampbellAbstract:Total vapor pressure measurements at 313.15 K are reported for binary systems of heptane with each of seven pentanol isomers: 1-pentanol, 2-Pentanol, 3-pentanol, 2-methyl-1-butanol, 2-methyl-2-but...
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Binary total pressure measurements for methanol with 1-pentanol, 2-Pentanol, 3-pentanol, 2-methyl-1-butanol, 2-methyl-2-butanol, 3-methyl-1-butanol, and 3-methyl-2-butanol at 313.15 K
Journal of Chemical & Engineering Data, 1996Co-Authors: Demensio P. Barton, Venkat R. Bhethanabotla, Scott W. CampbellAbstract:Total pressure measurements at 313.15 K are reported for binary systems of methanol with each of seven pentanol isomers: 1-pentanol, 2-Pentanol, 3-pentanol, 2-methyl-1-butanol, 2-methyl-2-butanol, 3-methyl-1-butanol, and 3-methyl-2-butanol. The results were obtained using a Van Ness apparatus and were fitted to the four-suffix Margules equation using Barker`s method. The four-suffix Margules equation represents the data to within an average of approximately 0.02 kPa.
Yoko Tateishi - One of the best experts on this subject based on the ideXlab platform.
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henry s law constants and infinite dilution activity coefficients of cis 2 butene dimethylether chloroethane and 1 1 difluoroethane in methanol 1 propanol 2 propanol 1 butanol 2 butanol isobutanol tert butanol 1 pentanol 2 pentanol 3 pentanol 2 methy
The Journal of Chemical Thermodynamics, 2006Co-Authors: Yoshimori Miyano, Takahiro Kobashi, Hiroshi Shinjo, Shinya Kumada, Yusuke Watanabe, Wataru Niya, Yoko TateishiAbstract:Abstract Henry’s law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-Pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol in the temperature range of 250 K to 330 K were measured by a gas stripping method and partial molar excess enthalpies were calculated from the activity coefficients. A rigorous formula for evaluating the Henry’s law constants from the gas stripping measurements was used for the data reduction of these highly volatile mixtures. The uncertainty is about 2% for the Henry’s law constants and 3% for the estimated infinite dilution activity coefficients. In the evaluation of the infinite dilution activity coefficients, the nonideality of the solute such as the fugacity coefficient and Poynting correction factor cannot be neglected, especially at higher temperatures. The estimated uncertainty of the infinite dilution activity coefficients includes 1% for nonideality.
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Henry’s law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-Pentanol, 3-pent
The Journal of Chemical Thermodynamics, 2006Co-Authors: Yoshimori Miyano, Takahiro Kobashi, Hiroshi Shinjo, Shinya Kumada, Yusuke Watanabe, Wataru Niya, Yoko TateishiAbstract:Abstract Henry’s law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-Pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol in the temperature range of 250 K to 330 K were measured by a gas stripping method and partial molar excess enthalpies were calculated from the activity coefficients. A rigorous formula for evaluating the Henry’s law constants from the gas stripping measurements was used for the data reduction of these highly volatile mixtures. The uncertainty is about 2% for the Henry’s law constants and 3% for the estimated infinite dilution activity coefficients. In the evaluation of the infinite dilution activity coefficients, the nonideality of the solute such as the fugacity coefficient and Poynting correction factor cannot be neglected, especially at higher temperatures. The estimated uncertainty of the infinite dilution activity coefficients includes 1% for nonideality.
Yoshimori Miyano - One of the best experts on this subject based on the ideXlab platform.
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henry s law constants and infinite dilution activity coefficients of cis 2 butene dimethylether chloroethane and 1 1 difluoroethane in methanol 1 propanol 2 propanol 1 butanol 2 butanol isobutanol tert butanol 1 pentanol 2 pentanol 3 pentanol 2 methy
The Journal of Chemical Thermodynamics, 2006Co-Authors: Yoshimori Miyano, Takahiro Kobashi, Hiroshi Shinjo, Shinya Kumada, Yusuke Watanabe, Wataru Niya, Yoko TateishiAbstract:Abstract Henry’s law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-Pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol in the temperature range of 250 K to 330 K were measured by a gas stripping method and partial molar excess enthalpies were calculated from the activity coefficients. A rigorous formula for evaluating the Henry’s law constants from the gas stripping measurements was used for the data reduction of these highly volatile mixtures. The uncertainty is about 2% for the Henry’s law constants and 3% for the estimated infinite dilution activity coefficients. In the evaluation of the infinite dilution activity coefficients, the nonideality of the solute such as the fugacity coefficient and Poynting correction factor cannot be neglected, especially at higher temperatures. The estimated uncertainty of the infinite dilution activity coefficients includes 1% for nonideality.
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Henry’s law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-Pentanol, 3-pent
The Journal of Chemical Thermodynamics, 2006Co-Authors: Yoshimori Miyano, Takahiro Kobashi, Hiroshi Shinjo, Shinya Kumada, Yusuke Watanabe, Wataru Niya, Yoko TateishiAbstract:Abstract Henry’s law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-Pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol in the temperature range of 250 K to 330 K were measured by a gas stripping method and partial molar excess enthalpies were calculated from the activity coefficients. A rigorous formula for evaluating the Henry’s law constants from the gas stripping measurements was used for the data reduction of these highly volatile mixtures. The uncertainty is about 2% for the Henry’s law constants and 3% for the estimated infinite dilution activity coefficients. In the evaluation of the infinite dilution activity coefficients, the nonideality of the solute such as the fugacity coefficient and Poynting correction factor cannot be neglected, especially at higher temperatures. The estimated uncertainty of the infinite dilution activity coefficients includes 1% for nonideality.
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Henry’s law constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-Pentanol, and 3-pentanol
The Journal of Chemical Thermodynamics, 2005Co-Authors: Yoshimori MiyanoAbstract:Abstract Henry’s law constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-Pentanol in the temperature range of (250 to 330) K and 3-pentanol in the temperature range of (260 to 330) K were measured by a gas stripping method. A rigorous formula for evaluating the Henry’s law constants from the gas stripping measurements was used for the data reduction of these highly volatile mixtures. The uncertainty is about 2% for the Henry’s law constants and 3% for the estimated infinite dilution activity coefficients. In the evaluation of the infinite dilution activity coefficients, the nonideality of the solute such as the fugacity coefficient and Pointing correction factor cannot be neglected, especially at higher temperatures. The estimated uncertainty of the infinite dilution activity coefficients includes 1% for nonideality.
Venkat R. Bhethanabotla - One of the best experts on this subject based on the ideXlab platform.
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Total pressure measurements for benzene with 1-propanol, 2-propanol, 1-pentanol, 3-pentanol, and 2-methyl-2-butanol at 313.15 K
Fluid Phase Equilibria, 2001Co-Authors: Jonathon M. Rhodes, Venkat R. Bhethanabotla, Tyson A Griffin, Michael J Lazzaroni, Scott W. CampbellAbstract:Abstract Total pressure measurements at 313.15 K are reported for binary systems of benzene and 1-propanol, 2-propanol, 1-pentanol, 3-pentanol, and 2-methyl-2-butanol. The results are interpreted by an extended form of the Kretschmer–Wiebe association model, in which it is assumed that linear alcohol chains may solvate with a single benzene molecule.
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Total pressure measurements for 1-propanol + 1-pentanol, 1-propanol + 2-Pentanol, 2-propanol + 1-pentanol, and 2-propanol + 2-Pentanol at 313.15 K
Fluid Phase Equilibria, 1997Co-Authors: Kevin Mara, Venkat R. Bhethanabotla, Scott W. CampbellAbstract:Abstract Total pressure measurements at 313.15 K are reported for 1-propanol + 1-pentanol, 1-propanol + 2-Pentanol, 2-propanol + 1-pentanol, and 2-propanol + 2-Pentanol. The results were obtained using a Van Ness apparatus and were fitted to the three-suffix Margules equation using Barker's method. The Margules equation represents the data to within an average of 0.01 kPa.
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Total vapor pressure measurements for heptane + 1-pentanol, + 2-Pentanol, + 3-pentanol, + 2-methyl-1-butanol, + 2-methyl-2-butanol, + 3-methyl-1-butanol, and + 3-methyl-2-butanol at 313.15 K
Journal of Chemical & Engineering Data, 1997Co-Authors: Jonathon M. Rhodes, Venkat R. Bhethanabotla, Scott W. CampbellAbstract:Total vapor pressure measurements at 313.15 K are reported for binary systems of heptane with each of seven pentanol isomers: 1-pentanol, 2-Pentanol, 3-pentanol, 2-methyl-1-butanol, 2-methyl-2-but...
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Binary total pressure measurements for methanol with 1-pentanol, 2-Pentanol, 3-pentanol, 2-methyl-1-butanol, 2-methyl-2-butanol, 3-methyl-1-butanol, and 3-methyl-2-butanol at 313.15 K
Journal of Chemical & Engineering Data, 1996Co-Authors: Demensio P. Barton, Venkat R. Bhethanabotla, Scott W. CampbellAbstract:Total pressure measurements at 313.15 K are reported for binary systems of methanol with each of seven pentanol isomers: 1-pentanol, 2-Pentanol, 3-pentanol, 2-methyl-1-butanol, 2-methyl-2-butanol, 3-methyl-1-butanol, and 3-methyl-2-butanol. The results were obtained using a Van Ness apparatus and were fitted to the four-suffix Margules equation using Barker`s method. The four-suffix Margules equation represents the data to within an average of approximately 0.02 kPa.
María Dolores Saquete - One of the best experts on this subject based on the ideXlab platform.
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Liquid–liquid–solid equilibria for ternary systems of water + potassium chloride + pentanols
Fluid Phase Equilibria, 2001Co-Authors: N Boluda, Vicente Gomis, Francisco Ruiz, María Dolores Saquete, N BarnesAbstract:Liquid–liquid–solid equilibria for the ternary systemswater+potassium chloride+1-pentanol,water+potassium chloride+2-Pentanol,water+potassium chloride+3-pentanol,water+potassium chloride+2-methyl-1-butanol and water+potassium chloride+2-methyl-2-butanol have been measured at 25 ºC. The data obtained have been fitted by the Setschenov equation and compared with the equilibria of several systems of water+sodium chloride+pentanols.The authors wish to thank the DGICYT (Spain) for the financial aid for the Project PB96-0338. N. Barnes acknowledges a grant from “Agencia Española de Cooperación Internacional”, Programa de Cooperación Interuniversitaria/AL.E (1999)
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liquid liquid solid equilibria for ternary systems water sodium chloride pentanols
Journal of Chemical & Engineering Data, 1999Co-Authors: Vicente Gomis, Francisco Ruiz, N Boluda, María Dolores SaqueteAbstract:Liquid-liquid-solid equilibria for the ternary systems water + sodium chloride + 1-pentanol, water + sodium chloride + 2-Pentanol, water + sodium chloride + 3-pentanol, water + sodium chloride + 2-methyl-1-butanol, and water + sodium chloride + 2-methyl-2-butanol have been measured at 25 °C. The data obtained have been fitted by the Setschenov equation.
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Liquid-liquid-solid equilibria for ternary systems water + sodium chloride + pentanols
Journal of Chemical & Engineering Data, 1999Co-Authors: Vicente Gomis, Francisco Ruiz, N Boluda, María Dolores SaqueteAbstract:Liquid-liquid-solid equilibria for the ternary systems water + sodium chloride + 1-pentanol, water + sodium chloride + 2-Pentanol, water + sodium chloride + 3-pentanol, water + sodium chloride + 2-methyl-1-butanol, and water + sodium chloride + 2-methyl-2-butanol have been measured at 25 °C. The data obtained have been fitted by the Setschenov equation.
