• Title of article

    Vapor–liquid equilibria of iso-propanol iso-butanol and iso-propanol iso-butanol calcium chloride at 93.6 kPa

  • Author/Authors

    N.A. Darwish ، نويسنده , , Z.A. Al-Anber، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 1998
  • Pages
    6
  • From page
    295
  • To page
    300
  • Abstract
    Vapor–liquid equilibrium (VLE) data of iso-propanol iso-butanol and iso-propanol iso-butanol CaCl2 (at saturation) were measured at a pressure of 93.6 kPa, using a modified Malanowski equilibrium still. The VLE behavior of the salt-free system is nearly ideal with a maximum normalized excess Gibbs energy (GE:RT) of 0.01. The salt investigated in this work, i.e. CaCl2, shows no effect on the phase behavior of iso-propanol iso-butanol. The experimental results of the salt-free binary were compared with those predicted by the ASOG and UNIFAC models, which predicted the bubble-point temperatures with an RMSD (root mean square deviation) of 1.01 and 1.26 K, respectively. The former model, however, predicted the vapor-phase composition within 0.012 mole fraction while the latter predicted them within 0.016 mole fraction in terms of RMSD. Moreover, two isobaric data sets (at 760 mm Hg) from the literature were analyzed using the above two models
  • Keywords
    Vapor–liquid equilibria , Group contribution methods , Experimental methods , Liquid-phase models , Salt effects
  • Journal title
    Chemical Engineering and Processing: Process Intensification
  • Serial Year
    1998
  • Journal title
    Chemical Engineering and Processing: Process Intensification
  • Record number

    417583