Abstract
In Part I of this series we developed a new model for nanoporous materials and inorganic membranes, with a pore space that consists of interconnected pores of irregular shapes, sizes, and connectivity. To test the validity of the model, we utilized it to model adsorption in three distinct silicon-carbide (SiC) membranes, and demonstrated that, using at most one adjustable parameter, the simulated isotherms and the experimental data are in very good agreement. In this paper we use the model of the SiC membrane developed in Part I, and non-equilibrium molecular dynamics simulations, in order to study transport and separation in the membrane of two binary gaseous mixtures, namely, H2/CO2 and H2/CH4, and test the accuracy of the results by comparing them with the experimental data. The model is demonstrated to provide reasonably accurate predictions for various properties of interest, and in particular for the separation factors of the mixtures, without utilizing any new adjustable parameter. The effect of the temperature, the membrane's porosity, and the pressure drop applied externally to the membrane is described, and possible approaches for improving the model further are discussed.
| Original language | English (US) |
|---|---|
| Pages (from-to) | 323-330 |
| Number of pages | 8 |
| Journal | Journal of Membrane Science |
| Volume | 345 |
| Issue number | 1-2 |
| DOIs | |
| State | Published - Dec 1 2009 |
| Externally published | Yes |
Bibliographical note
Funding Information:Parallel computations for the work described in this paper were supported by the University of Southern California Center for High-Performance Computing. This work was supported in part by the National Science Foundation and the Department of Energy. We thank Dr. Bahman Elyassi for useful discussions. We would also like to thank an anonymous referee for useful comments on the manuscript.
Keywords
- Dual control volume method
- Hydrogen
- Non-equilibrium molecular dynamics simulation
- Separation of gaseous mixtures
- Silicon-carbide membranes