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Collect. Czech. Chem. Commun. 1973, 38, 1295-1301
https://doi.org/10.1135/cccc19731295

Liquid-vapour equilibrium. LVIII. The systems benzene-2-butanol, benzene-isobutanol and benzene-tert-butanol

H. Ruíz Echevarría

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  • Neau Evelyne, Escandell Joan, Raspo Isabelle: A generalized reference state at constant volume for the prediction of phase equilibria from low pressure model parameters: Application to size-asymmetric systems and to the Wong–Sandler mixing rule. Chemical Engineering Science 2011, 66, 4148. <https://doi.org/10.1016/j.ces.2011.05.043>
  • Kurihara Kiyofumi, Egawa Yusuke, Iino Shinya, Ochi Kenji, Kojima Kazuo: Evaluation of thermodynamic consistency of isobaric and isothermal binary vapor–liquid equilibrium data using the PAI test II, alcohol+n-alkane, +aromatic, +cycloalkane systems. Fluid Phase Equilibria 2007, 257, 151. <https://doi.org/10.1016/j.fluid.2007.01.025>
  • Nagata Isamu, Tamura Kazuhiro, Kishi Naoki, Tada Kaoru: Association model of fluids. Simultaneous representation of excess Gibbs energies and excess enthalpies for liquid mixtures with alkanols. Fluid Phase Equilibria 1997, 135, 227. <https://doi.org/10.1016/S0378-3812(97)00080-0>
  • Satyro Marco A., Trebble Mark A.: On the applicability of the Sandler-Wong mixing rules for the calculation of thermodynamic excess properties—VE, HE, SE, CpE. Fluid Phase Equilibria 1996, 115, 135. <https://doi.org/10.1016/0378-3812(95)02826-9>
  • RUIZ ECHEVARRIA H.: ChemInform Abstract: LIQUID‐VAPOUR EQUILIBRIUM PART 58, THE SYSTEMS BENZENE‐BUTANOL‐2, BENZENE‐ISOBUTANOL, AND BENZENE‐TERT.‐BUTANOL. Chemischer Informationsdienst 1973, 4. <https://doi.org/10.1002/chin.197333098>