1977
DOI: 10.1002/bbpc.19770811007
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Thermodynamik flüssiger Mischungen von Kohlenwasserstoffen mit verwandten Substanzen

Abstract: Einige allgemeine Gesichtspunkte zur Thermodynamik flüssiger Mischungen von Nichtelektrolyten werden diskutiert, wobei die Gruppen‐beitragstheorie besondere Beachtung findet. Die Theorie assoziierter Mischungen wird kritisch untersucht. — Experimentelle Ergebnisse werden für einige ausgewählte Systeme gezeigt. Deren relative Bedeutung mit Hinblick auf ein systematisches Forschungsprogramm zur Thermodynamik organischer Mischungen wird ausführlich behandelt.

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Cited by 93 publications
(12 citation statements)
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“…Note that the Redlich-Kister equation, Eq. 280, may also be transformed into an alternative, equivalent polynomial known as the 4-suffix Margules equation [1,17] In 1964 Wilson suggested a novel equation for G E by introducing the local mole fraction of component i in a mixture {i + j} [198], a concept which has been developed impressively since then [137,[199][200][201][202][203][204][205][206][207][208][209]. For a binary mixture, the molar excess Gibbs energy is given by and the activity coefficients are Thus, at infinite dilution we obtain An iterative procedure is required to evaluate the adjustable parameters Λ 12 and Λ 21 .…”
Section: Excess Molar Gibbs Energy and Lewis-randall Activity Coefficients (In Particular At Infinite Dilution)mentioning
confidence: 99%
See 1 more Smart Citation
“…Note that the Redlich-Kister equation, Eq. 280, may also be transformed into an alternative, equivalent polynomial known as the 4-suffix Margules equation [1,17] In 1964 Wilson suggested a novel equation for G E by introducing the local mole fraction of component i in a mixture {i + j} [198], a concept which has been developed impressively since then [137,[199][200][201][202][203][204][205][206][207][208][209]. For a binary mixture, the molar excess Gibbs energy is given by and the activity coefficients are Thus, at infinite dilution we obtain An iterative procedure is required to evaluate the adjustable parameters Λ 12 and Λ 21 .…”
Section: Excess Molar Gibbs Energy and Lewis-randall Activity Coefficients (In Particular At Infinite Dilution)mentioning
confidence: 99%
“…Enormous research efforts have been invested in developing the local composition concept, for instance in developing the NRTL equation, the UNIQUAC and UNIFAC formalism, and the DISQUAC model [137,[199][200][201][202][203][204][205][206][207][208][209]. This topic definitely deserves a review of its own.…”
Section: Excess Molar Gibbs Energy and Lewis-randall Activity Coefficients (In Particular At Infinite Dilution)mentioning
confidence: 99%
“…This deviation is understandable from the fact that the induced dipole interaction between the alkyl parts of the alkane and the alkanol has not been taken into account in the calculations. It is expected that the inclusion of a dispersion term, as has been done in the DISQUAC [8,36], will improve the prediction of the excess enthalpy. Fig.…”
Section: Cosmospacementioning
confidence: 99%
“…Both theoretical models contain, besides the mole and volume fraction, the surface fraction and require as additional parameter the number of nearest neighbors for each compounds. Abrams and Prausnitz [6] and Magnussen et al [7] derived from the Staverman-Guggenheim (SG) entropy expressions for the activity coefficient, which have been applied in the combinatorial term of the UNIQUAC [6], DISQUAC [8], UNIFAC [9,10], COSMOSAC [11], COSMOSPACE [12] and MOQUAC [13] models. In this paper we show that from the Guggenheim entropy of mixing an alternative expression for the combinatorial activity coefficient equation can be obtained, and thereby a new formula for the number of nearest neighbors.…”
Section: Introductionmentioning
confidence: 99%
“…Значения поверхностей ( qs ) и объемов (r s ) групп, выраженные в единицах стандартного сегмента (Л ст =3,13Х 10 8 z, V CT =2,366 ( z-1) [ п ]), определены для z=lo (табл. 1).…”
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