Liebermann‐fried model parameters for calculating vapour‐liquid equlibria of oxygenate and hydrocarbon mixtures
Author:
Publisher
Informa UK Limited
Subject
General Engineering
Link
http://www.tandfonline.com/doi/pdf/10.1080/02533839.2005.9671086
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1. Isothermal (vapor+liquid) equilibria and excess enthalpy data of {1-hexene+methyl butyl ether (MBE)} and {1-hexene+methyl tert-butyl ether (MTBE)} binary systems at several temperatures;The Journal of Chemical Thermodynamics;2012-11
2. Excess molar enthalpies of ternary mixtures (dibutyl ether or dipropyl ether+2,2-dimethylbutane+2,3-dimethylbutane) at the temperature 298.15K;The Journal of Chemical Thermodynamics;2011-09
3. Excess molar enthalpies of ternary mixtures (1-hexene + tetrahydrofuran + 2,2-dimethylbutane or 2,3-dimethylbutane) at the temperature 298.15 K;The Journal of Chemical Thermodynamics;2011-03
4. Excess Molar Enthalpies of Dipropyl Ether + Dibutyl Ether + (1-Hexene or Tetrahydrofuran) at 298.15 K;Journal of Chemical & Engineering Data;2010-11-02
5. Excess molar enthalpies of the ternary mixtures: Methyltert-butyl ether (or di-isopropyl ether) + n-octane + 2-methylpentane at 293.15 K;The Canadian Journal of Chemical Engineering;2009-08
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