title={{Physical and Thermodynamic Properties of Pure Chemicals: Design institute for physical property data, American institute of chemical engineers. vp}},
title={{Physical and Thermodynamic Properties of Pure Chemicals: Design institute for physical property data, American institute of chemical engineers. vp}},
title={The impact of thermal non-equilibrium and large-scale 2D/3D effects on debris bed reflooding and coolability},
title={The impact of thermal non-equilibrium and large-scale 2D/3D effects on debris bed reflooding and coolability},
journal={Nuclear Engineering and Design},
journal={Nuclear Engineering and Design},
...
@@ -2008,3 +2012,19 @@ issn = {0029-5493},
...
@@ -2008,3 +2012,19 @@ issn = {0029-5493},
doi={10.1016/j.nucengdes.2006.03.059},
doi={10.1016/j.nucengdes.2006.03.059},
author={F. Fichot and F. Duval and N. Trégourès and C. Béchaud and M. Quintard},
author={F. Fichot and F. Duval and N. Trégourès and C. Béchaud and M. Quintard},
}
}
@Article{Krishna1997,
author={Krishna, R. and Wesselingh, J. A.},
journal={Chemical Engineering Science},
title={The Maxwell-Stefan approach to mass transfer},
year={1997},
number={6},
pages={861-911},
volume={52},
abstract={The limitations of the Fick's law for describing diffusion are discussed. It is argued that the Maxwell-Stefan formulation provides the most general, and convenient, approach for describing mass transport which takes proper account of thermodynamic non-idealities and influence of external force fields. Furthermore, the Maxwell-Stefan approach can be extended to handle diffusion in macro- and microporous catalysts, adsorbents and membranes.},
affiliation={Department of Chemical Engineering, University of Amsterdam, Nieuwe Achtergracht 1661018 WV AmsterdamThe Netherlands; Department of Chemical Engineering, University of Groningen, Nijenborgh 49747 AG GroningenThe Netherlands},
* With \f$\eta^i\f$ as the chemical potential of the species i. Note, the diffusion coefficients are based on the Onsager symmetry, thus the diffusion coefficients can be expressed as