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Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures Shekaari H, Zafarani-Moattar MT, Mohammadi B Fluid Phase Equilibria, 484, 38, 2019 |
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Separation of thiophene, or benzothiophene from model fuel using glycols. Liquid-liquid phase equilibria and oxidative desulfurization study Krolikowski M, Lipinska A Fluid Phase Equilibria, 482, 11, 2019 |
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Measurements and correlation of liquid-liquid equilibrium data for the ternary (3-heptanone plus phenol plus water) system Xu GJ, Yang DL, Ning PG, Wang QJ, Gong FC, Cao HB Journal of Chemical Thermodynamics, 106, 295, 2017 |
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Comments on the correlation of vapor-liquid equilibrium (VLE) data in azeotropic ternary systems Marcilla A, Olaya MM, Reyes-Labarta JA Fluid Phase Equilibria, 426, 110, 2016 |
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Liquid-liquid equilibrium data for water-ethanol-entrainer ternary system with entrainers: Cyclohexane, n-pentane, DEE (diethyl ether), DIPE (di-isopropyl ether), ETBE (ethyl tert-butyl ether) Qasim F, Choi HC, Shin JS, Park SJ Korean Journal of Chemical Engineering, 33(7), 2179, 2016 |
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Solubility and tie line data for the aqueous solutions of butyric acid with 1-octanol and 2-ethyl-1-hexanol at various temperatures Gilani AG, Gilani HG, Saadat SLS Fluid Phase Equilibria, 361, 45, 2014 |
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Phase equilibrium data for the hydrogen sulphide plus methane system at Cross Mark temperatures from 186 to 313 K and pressures up to about 14 MPa Coquelet C, Valtz A, Stringari P, Popovic M, Richon D, Mougin P Fluid Phase Equilibria, 383, 94, 2014 |
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Tie line data for the (water plus butyric acid plus n-butyl alcohol or amyl alcohol) at T = ( 298.2, 308.2, and 318.2) K and ( water plus butyric acid plus isoamyl alcohol) at T=298.2 Gilani AG, Gilani HG, Amouzadeh F Journal of Chemical Thermodynamics, 71, 103, 2014 |
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Ternary liquid-liquid equilibrium data for the (water plus butyric acid plus n-hexane or n-hexanol) systems at T = (298.2, 308.2, and 318.2) K Gilani AG, Gilani HG, Saadat SLS, Janbaz M Journal of Chemical Thermodynamics, 60, 63, 2013 |
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Liquid-liquid equilibria for ternary systems of (ethylene glycol plus toluene plus heptane) at temperatures (303.15, 308.15, and 313.15) K and atmospheric pressure: Experimental results and correlation with UNIQUAC and NRTL models Haghnazarloo H, Lotfollahi MN, Mahmoudi J, Asl AH Journal of Chemical Thermodynamics, 60, 126, 2013 |