Simulataneous heat and mass transfer with and without reactant exhaustion in catalyst particles for reaction with volume change
- 1 July 1973
- journal article
- research article
- Published by Wiley in AIChE Journal
- Vol. 19 (4) , 832-839
- https://doi.org/10.1002/aic.690190423
Abstract
Asymptotic analytic expressions for the concentration and temperature profiles as well as effectiveness factor inside porous, thin‐disk shaped catalyst particles have been developed for zeroth‐order exothermic reaction with reactant‐to‐product volume change. The individual and combinative effects of volume‐change, Thiele and thermal Thiele moduli, and of the dimensionless activation energy are discussed. As expected, the expressions revert to those for the corresponding isothermal and constant‐volume cases. Errors arising from the approximation were calculated and found to be quite acceptable.Keywords
This publication has 5 references indexed in Scilit:
- Transient heat and mass transfer in a porous catalyst III. *1Reaction with finite values of Sherwood and Nusselt number. Effect of volume contractionJournal of Catalysis, 1971
- Concentration distribution, effectiveness factor, and reactant exhaustion for catalytic reaction with volume changeAIChE Journal, 1971
- Modelling of chemical reactors. VII. Heat- and mass transfer in a particle of porous catalyst; Zeroth-order reaction - Numerical resultsCollection of Czechoslovak Chemical Communications, 1968
- Combined effect of volume change and internal heat and mass transfer on gas-phase reactions in porous catalystsJournal of Catalysis, 1966
- Criticality Criteria for Various Configurations of a Self-Heating Chemical as Functions of Activation Energy and Temperature of AssemblyThe Journal of Chemical Physics, 1961