The steady state diffusion of gases through capillaries or through the pores of a solid when fusion, bulk flow of the gases is free to the total pressure in the system is constant is considered. I t is shown that the ratio of the molar occur, but in the present situation diffusion rate of the lighte
Dynamic transport of multicomponent mixtures of gases in porous solids
✍ Scribed by Daniel Arnošt; Petr Schneider
- Publisher
- Elsevier Science
- Year
- 1995
- Tongue
- English
- Weight
- 725 KB
- Volume
- 57
- Category
- Article
- ISSN
- 0923-0467
No coin nor oath required. For personal study only.
✦ Synopsis
Dynamics of transport of ternary mixtures of non-adsorbable gases (hydrogen, helium, nitrogen, argon) through porous solids was studied experimentally in the dynamic version of the Wicke-Kallenbach diffusion cell. Four samples of (\alpha)-alumina pellets prepared under different compressing pressures and calcination temperatures with pore structures resembling commercial catalysts/carriers were used. Responses to composition step changes at one face of cylindrical pellets were followed at the other pellet face. The dusty gas model (DGM) and mean pore transport model (MTPM), based on the modified Maxwell-Stefan equation and Darcy law, were used for simulation of experimental responses with transport parameters obtained from dynamic measurements with binary gas mixtures. The predicted and measured responses to step changes of gases agreed very well for both models.
📜 SIMILAR VOLUMES
Toor (5, 6) has recently presented methods of solution of the linearized by was shown by Toor [Equations ( 3 7 ) and ( 49) in reference 61 to be given
The dynamics of the binary transport of non-adsorbable gases (hydrogen. helium, nitrogen, argon) through porous solids were studied by means of the dynamic version of the Wicke-Kallenbach diffusion cell. Six samples of a-alumina pellets were used which were prepared under different compressing press
Exact (numencal) and approxunate semi-analytical solution procedures are developed to mvestlgate the problem of multlcomponent dlffuslon accompamed by multiple reactions m porous catalyst pellets Examples are presented to illustrate the apphcatlon of the proposed procedures and to compare exact and