2006
DOI: 10.1016/j.molliq.2006.02.007
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Excess molar volumes, deviations in viscosity and refractive index of the binary mixtures of mesitylene with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at 298.15, 303.15, and 308.15 K

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Cited by 53 publications
(10 citation statements)
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“… a Lin et al b Urréjola et al c Orge et al d Mutalik et al e Papanastaslou and Ziogas f Papanastaslou et al Standard uncertainties u are u ( T ) = 0.03 K, u ( p ) = 0.01 MPa, u ( n D ) = 2 × 10 –5 . …”
Section: Methodsmentioning
confidence: 99%
“… a Lin et al b Urréjola et al c Orge et al d Mutalik et al e Papanastaslou and Ziogas f Papanastaslou et al Standard uncertainties u are u ( T ) = 0.03 K, u ( p ) = 0.01 MPa, u ( n D ) = 2 × 10 –5 . …”
Section: Methodsmentioning
confidence: 99%
“…The two-parameter McAllister three-body (MAC3) and three-parameter McAllister four-body (MAC4) equations, on the other hand, were correlated with the kinematic viscosities, ν ; the latter being related to η and densities, ρ, as ν = η/ρ. All the experimental data of η and ν in use were collected from previous publications by different authors. Moreover, the results of ρ and η correlations were also compared with the equations of simple polynomials and the Jouyban-Acree model of different degrees. The correlating abilities of each of the above models were tested by calculating the standard percentage deviation, σ%, between experimental and calculated values as Here, Y exp and Y cal refer to experimental and calculated ρ, η, or ν; n represents the number of data points and p is the number of coefficients taken.…”
Section: Resultsmentioning
confidence: 99%
“…In the present investigation of viscosity models, experimental data of different authors are utilized. Also, attempts have been made to estimate some new group interaction parameters of the UNIFAC-VISCO model for the amines (primary and secondary), acetonitrile, nitromethane, nitrobenzene, 4-methylpyridine, pyridine, dimethyl sulfoxide, and sulfolane.…”
Section: Introductionmentioning
confidence: 99%
“…M 1 and M 2 molecular weight of solvent and molecular weight of solute ρ is density of solution respectively. The data of molar volume of solution is reported in Table 3 Knowledge of the excess molar volume is of important property in design and storage and handling facilities of mixtures .The excess molar volume (V E ) for these solutions are obtained by the given expression [10,11], ( )…”
Section: Resultsmentioning
confidence: 99%