1979
DOI: 10.1016/0021-9614(79)90136-8
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Evaluation of excess isentropic compressibilities and isochoric heat capacities

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Cited by 591 publications
(196 citation statements)
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“…Considering the relationship between the isothermal and adiabatic compressibility coefficients, it has been shown (20)(21)(22)(23)(24) that the adiabatic compressibility coefficient of an ideal mixture can be expessed as where pi, Vi, a,, and C,,, are the adiabatic compressibility coefficient, molar volume, coefficient of thermal expansion, and heat capacity at constant pressure, respectively, of the pure i components and T is the absolute temperature. The excess adiabatic compressibility coefficients are defined as 151 ~p = preal -pideal which represents the excess of the given property of a real mixture over the value for an ideal mixture at the same temperature, pressure, and composition.…”
Section: °Cmentioning
confidence: 99%
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“…Considering the relationship between the isothermal and adiabatic compressibility coefficients, it has been shown (20)(21)(22)(23)(24) that the adiabatic compressibility coefficient of an ideal mixture can be expessed as where pi, Vi, a,, and C,,, are the adiabatic compressibility coefficient, molar volume, coefficient of thermal expansion, and heat capacity at constant pressure, respectively, of the pure i components and T is the absolute temperature. The excess adiabatic compressibility coefficients are defined as 151 ~p = preal -pideal which represents the excess of the given property of a real mixture over the value for an ideal mixture at the same temperature, pressure, and composition.…”
Section: °Cmentioning
confidence: 99%
“…However, closer examination of the physical nature of compressibilities suggests that, 'while many thermodynamic and physical properties of ideal solutions are represented by the mole fraction weighted averages of component properties, it is more appropriate to use volume fraction weighted averages of compressibility coefficients of pure solution components to estimate ideal behavior of this property (20)(21)(22)(23)(24). Large differences occur between the values of excess compressibility coefficients estimated by these two methods, especially when the molar volumes of the individual component differ considerably.…”
Section: Introductionmentioning
confidence: 99%
“…The method used for calculating κ s E (Benson -Kiyohara approach) was outlined previously [34]. V E , κ s E and ∆ values were fitted to a Redlich -Kister [35] polynomial equation,…”
Section: Resultsmentioning
confidence: 99%
“…In this paper we report measurements of densities, speeds of sound and viscosities for three binary systems, 2-methylaniline + o-chlorotoluene, 2-methylaniline + m-chlorotoluene and 2-methylaniline + p-chlorotoluene at T = (303. 15 over whole composition range;V°m,1 andV°m,2;K°s,m,1 andK°s,m,2;V°Em,1 andV°Em,2 andK°Es,m,1 andK°Es,m,2 of the components in the mixture at infinite dilution, have been calculated. The variations of these properties with composition of the binary mixtures are discussed in terms of molecular interactions between components and structural effects.…”
Section: Study Of Intermolecular Interactions In Binary Mixtures Of 2mentioning
confidence: 99%