The estimation of the thermodynamic properties of ternary alloys from binary data using the shortest distance composition path

Jacob, Κ. T.; Fitzner, K.

doi:10.1016/0040-6031(77)80019-1

Cited by 214 publications

(116 citation statements)

References 6 publications

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“…[13] along with the errors as indicated by the solid vertical lines are displayed in Fig. 2 for all the binary mixtures.…”

Section: IXmentioning

confidence: 99%

“…[13] and [14] for binary mixtures have been fitted to eq. [2] to estimate the coefficients that are included in Table 4.…”

Section: IXmentioning

confidence: 99%

“…A search of the literature on ternary mixtures suggests the availability of several empirical relations used to calculate the excess volume (9)(10)(11)(12)(13)(14)(15)(16)(17)(18)(19). In this paper, we report the experimental densities and viscosities of ten binarv and four ternarv mixtures comprising bromofom, mesitylene, chlorobenzene, bromobenzene, dimethylformamide (DMF), and toluene.…”

Section: Introduction Experimentalmentioning

confidence: 99%

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Densities and viscosities of binary and ternary liquid mixtures at 25 °C

Aminabhavi¹,

Joshi²,

Balundgi³

et al. 1991

Can. J. Chem.

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TEJRAJ M. AMINABHAVI, SHRIKANT S. JOSHI, RAMACHANDRA H. BALUNDGI, and SHYAM S. SHUKLA. Can. J. Chem. 69, 1028 (1991).Densities and viscosities of ten binary and four ternary mixtures containing bromoform, bromobenzene, chlorobenzene, toluene, mesitylene, and dimethylformamide at 25°C have been measured over the whole range of mixture compositions. Excess molar volumes, apparent values of excess molar viscosities, and Gibbs energy of activation of flow have been calculated for these mixtures. The calculated results have been fitted to a linear regression equation to estimate the parameters and the standard deviation between the calculated and the experimental data.

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“…[13] along with the errors as indicated by the solid vertical lines are displayed in Fig. 2 for all the binary mixtures.…”

Section: IXmentioning

confidence: 99%

“…[13] and [14] for binary mixtures have been fitted to eq. [2] to estimate the coefficients that are included in Table 4.…”

Section: IXmentioning

confidence: 99%

Section: Introduction Experimentalmentioning

confidence: 99%

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Densities and viscosities of binary and ternary liquid mixtures at 25 °C

Aminabhavi¹,

Joshi²,

Balundgi³

et al. 1991

Can. J. Chem.

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“…Hence, it was assumed that the excess molar volumes can be described with a rather good accuracy by the relations: (15) where: , ) and eq. 15, the excess of the limiting binary alloys of the A-B-C mixture can be written as follows:…”

Section: Modeling Of Density Of Ternary Mixturesmentioning

confidence: 99%

“…In the case of non-ideal mixture, molar volume can be expressed by the relation: (13) where: The excess of molar volume mixture can be described in a way analogous to the excess molar free energy of ternary solution with use of models [10][11][12][13][14][15][16]. If ternary and all three binary solutions, which can be formed with ternary mixture components were regular, Toop's model [10] would describe its thermodynamic properties rigorously.…”

Section: Modeling Of Density Of Ternary Mixturesmentioning

confidence: 99%

Density Of The Copper-Rich Cu-Pb-Fe Alloys

Sak¹,

Kucharski²

2015

Archives of Metallurgy and Materials

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Density of the copper-rich corner of the ternary Cu-Pb-Fe alloys was determined with the dilatometric method. Investigated alloys had constant copper content equal to 0.9, 0.8 and 0.7 mole fraction, and varied iron concentration up to 0.1 mole fraction. A model predicting the density of ternary solution from knowledge of density of pure component and the excess of molar volume for limiting binaries is proposed.

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Viscosity of the binary systems containing trifluoroethanol, water and tetraethylene glycol dimethyl ether. Prediction of the ternary viscosity from binary data

et al. 1996

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Kinematic viscosities were measured over the entire range of composition and at atmospheric pressure for the binary systems trifluoroethanol (TFE)-H,O, TFE-tetraethylene glycol dimethyl ether (TEGDME), and TEGDME-H20 from 293.15 to 333.15 K. The data were fitted by the Stephan and Heckenbergber (1989) correlation, which accounts for the dependence on temperature and mixture composition.Methods for predicting ternary excess viscosities from excess viscosity data for the three binary mixtures involved are examined and tested for the system TFE-H,O-TEGDME at 303.15 K by comparing predicted and experimental data. The empirical correlation of Colinet (1967) is shown to be the best for this system. On a mesurk les viscositks cinkmatiques h la pression atmosphCrique dam une vaste gamme de composition pour les systkmes binaires trifluordthanol (TFE)-H,O, TFE-tktraCthylbne glycol dimkthyle &her (TEGDME) et TEGDME-H,O, entre 293,15 et 333,15 K. Les donnks ont kt6 calks par la corrClation de Stephan et Heckenberger (1989), qui tient compte de la dkpendance en temphature et par rapport h la composition des mClanges. Les mkthodes de prckliction des viscositks d'exds temaires h partir des domks de viscositk d'exds des trois mklanges binaires sont examinks et testks pour le systbme TFE-H,O-TEGDME h 303,15 K par comparaison des donnks praites et exphimentales. On montre que la corrklation empirique de Colinet (1967) est la meilleure pour ce syst&me.

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The estimation of the thermodynamic properties of ternary alloys from binary data using the shortest distance composition path

Cited by 214 publications

References 6 publications

Densities and viscosities of binary and ternary liquid mixtures at 25 °C

Densities and viscosities of binary and ternary liquid mixtures at 25 °C

Density Of The Copper-Rich Cu-Pb-Fe Alloys

Viscosity of the binary systems containing trifluoroethanol, water and tetraethylene glycol dimethyl ether. Prediction of the ternary viscosity from binary data

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