The use of mathematical modelling to investigate the effect of chemisorption on the dynamic behavior of catalytic reactors. Partial oxidation of o-xylene in fluidized beds
- 1 January 1990
- journal article
- Published by Elsevier in Mathematical and Computer Modelling
- Vol. 13 (5) , 11-21
- https://doi.org/10.1016/0895-7177(90)90039-p
Abstract
No abstract availableThis publication has 27 references indexed in Scilit:
- Hydrogenation of benzene, mono‐, di‐, and trimethylbenzenes over nickel catalysts supported on porous glassThe Canadian Journal of Chemical Engineering, 1986
- The effect of bubble size variation on the performance of fluidized bed reactorsChemical Engineering Science, 1985
- Investigation of a fixed‐bed pilot plant reactor by dynamic experimentation. Part 2. Simulation of reactor behaviourThe Canadian Journal of Chemical Engineering, 1985
- Adsorption and reaction at a catalytic surface: The quasi-steady conditionChemical Engineering Science, 1984
- Multiplicity of steady states in fluidized bed reactors—V: The effect of catalyst decayChemical Engineering Science, 1980
- Prediction of packed-bed catalytic reactor performance for a complex reaction (oxidation of o-xylene to phthalic anhydride)Chemical Engineering Science, 1979
- Kinetics and Yields in the Catalytic Oxidation of o-Xylene to Phthalic Anhydride with V2O5 CatalystsPublished by American Chemical Society (ACS) ,1974
- On the dynamic modelling of porous catalyst particlesThe Canadian Journal of Chemical Engineering, 1973
- Stability of catalytic wiresChemical Engineering Science, 1969
- Competitive Catalytic Hydrogenation of Benzene, Toluene and the Polymethylbenzenes on PlatinumJournal of the American Chemical Society, 1962