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Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K

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School of Chemical Engineering and Environment, Beijing Institute of Technology, Beijing 100081, People's Republic of China
Cite this: J. Chem. Eng. Data 2007, 52, 5, 1866–1871
Publication Date (Web):August 1, 2007
https://doi.org/10.1021/je700202h
Copyright © 2007 American Chemical Society

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    Abstract

    Densities and viscosities of four ternary mixtures made from heptane, octane, nonane, and hexyl benzene were measured. The temperature ranged from 293.15 K to 313.15 K. The experimental viscosities of the four pure hydrocarbons and their ternary mixtures vs temperature were fitted to the Andrade equation with an average absolute deviation of 0.13 %. On the basis of these data, the excess molar volumes and viscosity deviations were calculated. The prediction results based on the Przezdiecki−Sridhar method and the Sastri−Rao method for low-temperature liquid viscosity estimation, the Dymond−Assael hard sphere model, and an equation of state based viscosity model proposed by Fan and Wang were compared with the experimental data.

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     Corresponding author. Fax:  +86-10-68911040. E-mail:  lishengwang@ bit.edu.cn.

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