2002
DOI: 10.1007/3-540-45791-7_19
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Thermodiffusion in Porous Media and Its Consequences

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Cited by 27 publications
(24 citation statements)
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“…The non-equilibrium part in the model is accounted by incorporating the energy of viscous flow. The expression obtained for the thermal diffusion factor in a binary mixture has the form of: 30) where U i and V i are partial molar volume and partial molar internal energy, τ i is the ratio of the energy of vaporization and the energy of viscous flow for component i. This model together with two previously developed models of Kempers [71] and Rutherford [138] were tested for three groups of mixtures: hydrocarbon systems CH 4 Semenov model Semenov and Schimpf [151], derived expressions for the thermal diffusion coefficient for a liquid mixture by hydrodynamic approach.…”
Section: Shukla and Firoozabadi Modelmentioning
confidence: 99%
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“…The non-equilibrium part in the model is accounted by incorporating the energy of viscous flow. The expression obtained for the thermal diffusion factor in a binary mixture has the form of: 30) where U i and V i are partial molar volume and partial molar internal energy, τ i is the ratio of the energy of vaporization and the energy of viscous flow for component i. This model together with two previously developed models of Kempers [71] and Rutherford [138] were tested for three groups of mixtures: hydrocarbon systems CH 4 Semenov model Semenov and Schimpf [151], derived expressions for the thermal diffusion coefficient for a liquid mixture by hydrodynamic approach.…”
Section: Shukla and Firoozabadi Modelmentioning
confidence: 99%
“…In some cases, even qualitative predictions, which are of practical importance, are impossible. The main practical applications are separation processes [145,29] such as thermal field flow fractionation of polymers and colloids or isotope separation, characterization of geochemical processes [66,30] and combustion [128].…”
Section: Introductionmentioning
confidence: 99%
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