2018
DOI: 10.1021/acs.jced.8b00662
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Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K

Abstract: Measurements on density and viscosity at atmospheric pressure for the ternary system 1,2,3,4-tetrahydronaphthalene (1) + isopropylcyclohexane (2) + cyclopropanemethanol (3) and three corresponding binary systems from (293.15 to 343.15) K have been carried out over the whole composition range. The excess molar volumes (V m E) and viscosity deviations (Δη) of the ternary system have been derived from the experimental data and then fitted to the Cibulka, Singh, Redlich–Kister, and Nagata–Tamura equations, respect… Show more

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Cited by 5 publications
(15 citation statements)
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References 36 publications
(41 reference statements)
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“…In eqs 4 and 5, n is the number of compounds in the mixture; i represents a pure compound; x i and M i represent the mole fraction and mole mass of pure compound i in the mixture, respectively; ρ and η represent the density and viscosity of the mixture, respectively; and ρ i and η i represent the density and viscosity of pure compound i, respectively. 29 The excess molar volumes and viscosity deviations of binary systems at the investigated temperatures are fitted to the Redlich−Kister equation 38…”
Section: ■ Results and Discussionmentioning
confidence: 99%
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“…In eqs 4 and 5, n is the number of compounds in the mixture; i represents a pure compound; x i and M i represent the mole fraction and mole mass of pure compound i in the mixture, respectively; ρ and η represent the density and viscosity of the mixture, respectively; and ρ i and η i represent the density and viscosity of pure compound i, respectively. 29 The excess molar volumes and viscosity deviations of binary systems at the investigated temperatures are fitted to the Redlich−Kister equation 38…”
Section: ■ Results and Discussionmentioning
confidence: 99%
“… a Standard uncertainties u ( T ) = 0.01 K, u ( P ) = 0.50 kPa, u r (ρ) = 0.00034, and u r (η) = 0.01. b Reference . c Reference . d Reference . e Reference . f Reference . g Reference . h Reference . i Reference . j Reference . k Reference . m Reference . n Reference . o Reference . p Reference . q Reference . r Reference . s Reference . w Reference . t Reference . z Reference . …”
Section: Resultsmentioning
confidence: 99%
“…21−28 Han et al, 24 Singh et al, 25 and Ma et al 26 and co-workers investigated four semiempirical equations (i.e., Cibulka, Singh, Redlich−Kister, and Nagata−Tamura equations) to represent V E and Δη of several nonaqueous ternary systems. 27 Zhao et al 28 used a modified Jouyban−Acree model including the effects of temperature to represent the property data of the ternary systems.…”
Section: Introductionmentioning
confidence: 99%
“…In addition, the correlations and prediction of volumetric properties and viscosities of ternary mixtures using empirical models is an active area of research in development. There are several semiempirical equations that have been applied to correlate the experimental ternary results in the literature. Han et al, Singh et al, and Ma et al correlated the excess molar volume ( V E ) and viscosity deviation (Δη) of different ternary systems with Redlich–Kister and Cibulka equations. Guo and co-workers investigated four semiempirical equations (i.e., Cibulka, Singh, Redlich–Kister, and Nagata–Tamura equations) to represent V E and Δη of several nonaqueous ternary systems .…”
Section: Introductionmentioning
confidence: 99%
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