A Model for the Oxidation of Sulfur Dioxide in a Trickle-Bed Reactor
Authors:
- 1 December 1997
- journal article
- research article
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 36 (12) , 5125-5132
Abstract
No abstract availableKeywords
This publication has 12 references indexed in Scilit:
- Investigation of so2 oxidation rates in trickle‐bed reactors operating at low liquid flow ratesThe Canadian Journal of Chemical Engineering, 1992
- Effectiveness enhancement and reactant depletion in a partially wetted catalystAIChE Journal, 1987
- Trickle‐bed reactors: Liquid diffusional effects in a gas‐limited reactionAIChE Journal, 1987
- Effect of liquid wetting on catalyst effectiveness in trickle‐bed reactorsThe Canadian Journal of Chemical Engineering, 1982
- Effectiveness factors and mass transfer in trickle‐bed reactorsAIChE Journal, 1979
- Effect of Holdup Incomplete Catalyst Wetting and Backmixing during Hydroprocessing in Trickle Bed ReactorsIndustrial & Engineering Chemistry Process Design and Development, 1975
- Sulfur dioxide oxidation in slurries of activated carbon. Part II. Mass transfer studiesAIChE Journal, 1975
- Scale Up of Pilot Plant Data for Catalytic HydroprocessingIndustrial & Engineering Chemistry Process Design and Development, 1973
- Oxidation of SO2 in a trickle-bed reactor packed with carbonChemical Engineering Science, 1972
- Investigation of hydrogenation in liquid phase. XVII. Theoretical model of hydrogenation in a liquid film on a vertical column of spheresCollection of Czechoslovak Chemical Communications, 1971