Methyl Isobutyl Ketone

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Isabel Vidal - One of the best experts on this subject based on the ideXlab platform.

Alberto Arce - One of the best experts on this subject based on the ideXlab platform.

Chufen Yang - One of the best experts on this subject based on the ideXlab platform.

  • liquid liquid equilibria for the ternary system Methyl Isobutyl Ketone 1 2 benzenediol water
    Journal of Chemical & Engineering Data, 2014
    Co-Authors: Chufen Yang, Yu Qian, Jianwei Guo, Jingrui Chen
    Abstract:

    Liquid–liquid equilibria data for the ternary system Methyl Isobutyl Ketone +1,2-benzenediol + water were measured at temperatures of (298.15, 308.15, and 318.15) K and atmospheric pressure. The reliability of the experimental tie-line data was verified by the Hand and Bachman equations. The experimental data were correlated with the nonrandom two liquid and universal quasichemical models. The binary interaction parameters of these two models were reported. Both models correlated the experimental data successfully.

  • Liquid–Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + 1,2-Benzenediol + Water
    Journal of Chemical & Engineering Data, 2014
    Co-Authors: Chufen Yang, Yu Qian, Jianwei Guo, Jingrui Chen
    Abstract:

    Liquid–liquid equilibria data for the ternary system Methyl Isobutyl Ketone +1,2-benzenediol + water were measured at temperatures of (298.15, 308.15, and 318.15) K and atmospheric pressure. The reliability of the experimental tie-line data was verified by the Hand and Bachman equations. The experimental data were correlated with the nonrandom two liquid and universal quasichemical models. The binary interaction parameters of these two models were reported. Both models correlated the experimental data successfully.

  • liquid liquid equilibria for the quaternary system Methyl Isobutyl Ketone water phenol hydroquinone
    Fluid Phase Equilibria, 2007
    Co-Authors: Chufen Yang, Yanbin Jiang, Yu Qian, Lijuan Zhang
    Abstract:

    Abstract Liquid–liquid equilibria data of the quaternary system Methyl Isobutyl Ketone (MIBK)–water–phenol–hydroquinone were measured at 25 °C under atmosphere pressure. The experimental data were correlated with the UNIQUAC and NRTL activity coefficient models on the base of the fixed binary interaction parameters that were obtained from two sub-ternary systems MIBK–water–phenol and MIBK–water–hydroquinone. The root mean square deviations (RMSD) show that the regressed results for the quaternary system were in good agreement with the experimental data for both UNIQUAC and NRTL models. The comparison between experimental and calculated distribution coefficient values of phenol and hydroquinone shows that a relative deviation of less than 5% is obtained.

  • Liquid–liquid equilibria for the quaternary system Methyl Isobutyl Ketone–water–phenol–hydroquinone
    Fluid Phase Equilibria, 2007
    Co-Authors: Chufen Yang, Yanbin Jiang, Yu Qian, Lijuan Zhang
    Abstract:

    Abstract Liquid–liquid equilibria data of the quaternary system Methyl Isobutyl Ketone (MIBK)–water–phenol–hydroquinone were measured at 25 °C under atmosphere pressure. The experimental data were correlated with the UNIQUAC and NRTL activity coefficient models on the base of the fixed binary interaction parameters that were obtained from two sub-ternary systems MIBK–water–phenol and MIBK–water–hydroquinone. The root mean square deviations (RMSD) show that the regressed results for the quaternary system were in good agreement with the experimental data for both UNIQUAC and NRTL models. The comparison between experimental and calculated distribution coefficient values of phenol and hydroquinone shows that a relative deviation of less than 5% is obtained.

  • liquid liquid equilibria for the ternary system Methyl Isobutyl Ketone water hydroquinone
    Journal of Chemical & Engineering Data, 2006
    Co-Authors: Chufen Yang, Yanbin Jiang, Lijuan Zhang, Yu Qian
    Abstract:

    Experimental liquid−liquid equilibria data of dilute hydroquinone concentration were determined for the ternary system Methyl Isobutyl Ketone + water + hydroquinone at (25, 40, and 50) °C under atmospheric pressure. The experimental data were satisfactorily correlated with the UNIQUAC equation and the NRTL equation. The relative root-mean-square deviations and absolute mean deviations between the calculated and the experimental value are less than 1.2 %.

Yu Qian - One of the best experts on this subject based on the ideXlab platform.

  • liquid liquid equilibria for the ternary system Methyl Isobutyl Ketone 1 2 benzenediol water
    Journal of Chemical & Engineering Data, 2014
    Co-Authors: Chufen Yang, Yu Qian, Jianwei Guo, Jingrui Chen
    Abstract:

    Liquid–liquid equilibria data for the ternary system Methyl Isobutyl Ketone +1,2-benzenediol + water were measured at temperatures of (298.15, 308.15, and 318.15) K and atmospheric pressure. The reliability of the experimental tie-line data was verified by the Hand and Bachman equations. The experimental data were correlated with the nonrandom two liquid and universal quasichemical models. The binary interaction parameters of these two models were reported. Both models correlated the experimental data successfully.

  • Liquid–Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + 1,2-Benzenediol + Water
    Journal of Chemical & Engineering Data, 2014
    Co-Authors: Chufen Yang, Yu Qian, Jianwei Guo, Jingrui Chen
    Abstract:

    Liquid–liquid equilibria data for the ternary system Methyl Isobutyl Ketone +1,2-benzenediol + water were measured at temperatures of (298.15, 308.15, and 318.15) K and atmospheric pressure. The reliability of the experimental tie-line data was verified by the Hand and Bachman equations. The experimental data were correlated with the nonrandom two liquid and universal quasichemical models. The binary interaction parameters of these two models were reported. Both models correlated the experimental data successfully.

  • liquid liquid equilibria for the quaternary system Methyl Isobutyl Ketone water phenol hydroquinone
    Fluid Phase Equilibria, 2007
    Co-Authors: Chufen Yang, Yanbin Jiang, Yu Qian, Lijuan Zhang
    Abstract:

    Abstract Liquid–liquid equilibria data of the quaternary system Methyl Isobutyl Ketone (MIBK)–water–phenol–hydroquinone were measured at 25 °C under atmosphere pressure. The experimental data were correlated with the UNIQUAC and NRTL activity coefficient models on the base of the fixed binary interaction parameters that were obtained from two sub-ternary systems MIBK–water–phenol and MIBK–water–hydroquinone. The root mean square deviations (RMSD) show that the regressed results for the quaternary system were in good agreement with the experimental data for both UNIQUAC and NRTL models. The comparison between experimental and calculated distribution coefficient values of phenol and hydroquinone shows that a relative deviation of less than 5% is obtained.

  • Liquid–liquid equilibria for the quaternary system Methyl Isobutyl Ketone–water–phenol–hydroquinone
    Fluid Phase Equilibria, 2007
    Co-Authors: Chufen Yang, Yanbin Jiang, Yu Qian, Lijuan Zhang
    Abstract:

    Abstract Liquid–liquid equilibria data of the quaternary system Methyl Isobutyl Ketone (MIBK)–water–phenol–hydroquinone were measured at 25 °C under atmosphere pressure. The experimental data were correlated with the UNIQUAC and NRTL activity coefficient models on the base of the fixed binary interaction parameters that were obtained from two sub-ternary systems MIBK–water–phenol and MIBK–water–hydroquinone. The root mean square deviations (RMSD) show that the regressed results for the quaternary system were in good agreement with the experimental data for both UNIQUAC and NRTL models. The comparison between experimental and calculated distribution coefficient values of phenol and hydroquinone shows that a relative deviation of less than 5% is obtained.

  • liquid liquid equilibria for the ternary system Methyl Isobutyl Ketone water hydroquinone
    Journal of Chemical & Engineering Data, 2006
    Co-Authors: Chufen Yang, Yanbin Jiang, Lijuan Zhang, Yu Qian
    Abstract:

    Experimental liquid−liquid equilibria data of dilute hydroquinone concentration were determined for the ternary system Methyl Isobutyl Ketone + water + hydroquinone at (25, 40, and 50) °C under atmospheric pressure. The experimental data were satisfactorily correlated with the UNIQUAC equation and the NRTL equation. The relative root-mean-square deviations and absolute mean deviations between the calculated and the experimental value are less than 1.2 %.

Pilar Souza - One of the best experts on this subject based on the ideXlab platform.

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