The objective of this paper is to outline the essential features of a model for a supported liquid phase catalyst (SLPC) system, taking into account evaporation or condensation of the solvent. While the model has been developed and applied to the case of a specific reaction system - the oxidation of carbon monoxide by an aqueous Pd-Cu chloride solution, its general features should be applicable to any SLPC system involving a volatile solvent. Emphasis in this work will be on the formulation of a comprehensive steady-state model for such a system. A preliminary simplified model was developed previously by J. C. Tang (1983). A transient model has also been formulated (J. H. Glick, 1984), but that work will not be considered here.
|Original language||English (US)|
|Journal||Annual Meeting - American Institute of Chemical Engineers|
|State||Published - Dec 1 1985|
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