• Title of article

    Liquid–liquid equilibrium for the ternary systems water + 2-methyl-1-propanol + butyl acetate and water + 2-methyl-2-propanol + butyl acetate at (298.15 and 323.15) K

  • Author/Authors

    Xu، نويسنده , , Dongmei and Wu، نويسنده , , Chunxia and Zhang، نويسنده , , Qing and Zhang، نويسنده , , Huan and Wang، نويسنده , , Yinglong and Gao، نويسنده , , Jun، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2014
  • Pages
    7
  • From page
    60
  • To page
    66
  • Abstract
    Liquid–liquid equilibrium (LLE) data for the ternary system water + 2-methyl-1-propanol + butyl acetate and water + 2-methyl-2-propanol + butyl acetate were measured at the temperature T = (298.15 and 323.15) K and under atmospheric pressure, respectively. Both the Othmer–Tobias and Bachman equations were used to test the reliability of the experimental data. Moreover, the NRTL and UNIQUAC activity coefficient models were applied to correlate the determined data, and the result showed that the UNIQUAC and the NRTL models both could correlate the two systems studied well at the same conditions. In addition, distribution ratios and separation factors in the two ternary systems were calculated using the equations from the experimental liquid liquid equilibrium data and discussed in detail.
  • Keywords
    LLE , butyl acetate , 2-methyl-1-propanol , 2-Methyl-2-propanol
  • Journal title
    Fluid Phase Equilibria
  • Serial Year
    2014
  • Journal title
    Fluid Phase Equilibria
  • Record number

    1990193