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2-Pentanol

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Scott W. Campbell – One of the best experts on this subject based on the ideXlab platform.

  • 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, 2001
    Co-Authors: Jonathon M. Rhodes, Venkat R. Bhethanabotla, Tyson A Griffin, Michael J Lazzaroni, Scott W. Campbell
    Abstract:

    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.

  • 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, 1997
    Co-Authors: Kevin Mara, Venkat R. Bhethanabotla, Scott W. Campbell
    Abstract:

    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.

  • 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, 1997
    Co-Authors: Jonathon M. Rhodes, Venkat R. Bhethanabotla, Scott W. Campbell
    Abstract:

    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…

Yoko Tateishi – One of the best experts on this subject based on the ideXlab platform.

  • 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, 2006
    Co-Authors: Yoshimori Miyano, Takahiro Kobashi, Hiroshi Shinjo, Shinya Kumada, Yusuke Watanabe, Wataru Niya, Yoko Tateishi
    Abstract:

    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.

  • 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, 2006
    Co-Authors: Yoshimori Miyano, Takahiro Kobashi, Hiroshi Shinjo, Shinya Kumada, Yusuke Watanabe, Wataru Niya, Yoko Tateishi
    Abstract:

    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.

  • 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, 2006
    Co-Authors: Yoshimori Miyano, Takahiro Kobashi, Hiroshi Shinjo, Shinya Kumada, Yusuke Watanabe, Wataru Niya, Yoko Tateishi
    Abstract:

    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.

  • 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, 2006
    Co-Authors: Yoshimori Miyano, Takahiro Kobashi, Hiroshi Shinjo, Shinya Kumada, Yusuke Watanabe, Wataru Niya, Yoko Tateishi
    Abstract:

    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.

  • 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, 2005
    Co-Authors: Yoshimori Miyano
    Abstract:

    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.