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Solid−Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents

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Programa de Investigación y Desarrollo Tecnológico de Procesos y Reactores, Instituto Mexicano del Petróleo, Eje Lázaro Cárdenas 152, C.P. 07730, México, D.F., Departamento de Ingeniería de Procesos e Hidráulica, División de Ciencias Básicas e Ingeniería, Universidad Autónoma Metropolitana-Iztapalapa, Av. Michoacan y La Purísima, Col. Vicentina, 09340 México, D.F., México, and Departamento de Química del Centro de Investigación y de Estudios Avanzados del I.P.N., Av. Instituto Politécnico Nacional 2508, Col. San Pedro Zacatenco, México D.F., C.P. 07360
Cite this: J. Chem. Eng. Data 2007, 52, 6, 2212–2219
Publication Date (Web):October 24, 2007
https://doi.org/10.1021/je700234e
Copyright © 2007 American Chemical Society

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    Abstract

    This work reports the solid−liquid equilibria of several binary systems formed by solvent (1) + dibenzothiophene (2) and solvent (1) + dibenzothiophene sulfone (2). At least six experimental points were obtained to trace the solid−liquid equilibrium curve, using the visual technique to determine the change of phase. The experimental data were obtained at atmospheric pressure and from a (280 to 353) K temperature range. The experimental uncertainties were ± 0.0005 in mole fraction and ± 0.5 K in temperature, respectively. A classical equilibrium solid−liquid equation was used to derive the activity coefficient from the solubility experimental data. The following solution models were employed to correlate the activity coefficient:  UNIQUAC, Wilson, Tsuboka−Katayama−Wilson, van Laar, and Margules. A good agreement can be obtained between derived and correlated activity coefficients for selected systems. Additionaly, the following thermophysical properties were obtained experimentally for the pure dibenzothiophene sulfone:  enthalpy of fusion, melting temperature, and heat capacity for both solid and liquid phases. These values have not been previously reported in the open literature, and the corresponding entropy of fusion was derived from the experimental information. The systems studied in this work are of industrial importance in the production of ultralow sulfur fuels.

    *

     Corresponding author. E-mail:  [email protected].

     Universidad Autónoma Metropolitana-Iztapalapa.

     Instituto Mexicano del Petróleo.

    §

     Centro de Investigación y de Estudios Avanzados.

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    11. Qi Zhang, Yang Yang, Cuicui Cao, Limin Cheng, Ying Shi, Wenge Yang, Yonghong Hu. Thermodynamic models for determination of the solubility of dibenzothiophene in (methanol+acetonitrile) binary solvent mixtures. The Journal of Chemical Thermodynamics 2015, 80 , 7-12. https://doi.org/10.1016/j.jct.2014.08.012
    12. William E. Acree. IUPAC-NIST Solubility Data Series. 98. Solubility of Polycyclic Aromatic Hydrocarbons in Pure and Organic Solvent Mixtures—Revised and Updated. Part 3. Neat Organic Solvents. Journal of Physical and Chemical Reference Data 2013, 42 (1) https://doi.org/10.1063/1.4775402
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