Melting Curves, Densities, Viscosities and Thermodynamic Excess Properties of 1,2,4‐Trichlorobenzene + n‐Decane and + n‐Tetradecane

Atrops, H.; Kalali, H.; Köhler, Friedrich

doi:10.1002/bbpc.19820860106

Cited by 26 publications

(2 citation statements)

References 16 publications

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“…Stephen and Lucas (1979) review the viscosity values of butane, pentane, hexane, and octane and give recommended values of these pure substances. Experimental measurements of decane have been published by Mumford and Phillips (1950), Lee and Ellington (1965b), Carmichael et al (1969), Moore and Wellek (1974), Dymond and Young (1981), Atrops et al (1982), Ducoulombier et al (1986), Knapstad et al (1989), and Assael et al (1992). They report an accuracy of approximately 0.5%.…”

Section: Introductionmentioning

confidence: 99%

Experimental Liquid Viscosities of Decane and Octane + Decane from 298.15 K to 373.15 K and Up to 25 MPa

et al. 1998

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Section: Introductionmentioning

confidence: 99%

Experimental Liquid Viscosities of Decane and Octane + Decane from 298.15 K to 373.15 K and Up to 25 MPa

et al. 1998

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“…Using the global parameters n g, k according to Table of the residual entropy scaling model as described in Section , the fluid-specific scaling factors ξ have been refitted in this work for all linear alkanes and isomers of alkanes for which multiparameter equations of state are available. The experimental viscosity data has been taken from the ThermoData Engine (refs − …”

Section: Resultsmentioning

confidence: 99%

Residual Entropy Scaling for Long-Chain Linear Alkanes and Isomers of Alkanes

Jäger

Steinberg

Mickoleit

et al. 2023

Ind. Eng. Chem. Res.

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Using residual entropy scaling approaches, transport properties, such as viscosity and thermal conductivity, can be linked to a thermodynamic property, i.e., residual entropy. It has been demonstrated in the literature that these approaches can be successfully used to correlate transport properties in the gas phase as well as the liquid phase over large temperature and density ranges. Recently, Yang et al. [J. Chem. Eng. Data 2021, 66(3), 1385−1398 proposed a residual entropy scaling approach for the viscosity of 39 refrigerants and their mixtures, and they extended this approach in a subsequent work to 124 fluids [Int. J. Thermophys. 2022, 43(12), 183]. The method of Yang et al. requires a fluid-specific scaling factor for each fluid. Yang et al. proposed a method for estimating this parameter as being proportional to the residual entropy at the critical point. In this work, it is demonstrated that for hydrocarbons, the fluid-specific scaling factor can be better approximated as a linear function of the longest carbon chain. All linear and branched alkanes for which accurate multiparameter equations of state are available have been considered in this work. Furthermore, the performance of other predictive equations of state, i.e., the Peng− Robinson and Lee−Kesler−Plocker equations of state, is evaluated.

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