The prediction of gas hold-up in bubble column reactors: Newtonian and non-newtonian fluids
- 31 October 1992
- journal article
- Published by Elsevier BV in The Chemical Engineering Journal
- Vol. 50 (1), 1-7
- https://doi.org/10.1016/0300-9467(92)80001-q
Abstract
A new model has been developed for the gas hold-up in bubble column reactors. The model is based on two different expressions for the energy dissipation rate used to derive the correlations for the heat transfer rate in bubble column reactors. The present model is applicable to non-newtonian fluids characterized by a power-law model as well as to newtonian fluids.Keywords
This publication has 26 references indexed in Scilit:
- Heat transfer in bubble column and airlift bioreactors: Newtonian and non-Newtonian fermentation brothsJournal of Chemical Technology & Biotechnology, 2007
- Mathematical models for design of bioreactors: Applications ofThe Chemical Engineering Journal, 1990
- Gas-phase mixing in bubble columns.JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1989
- Gas-liquid mass transfer in a bubble column with suspended solidsAIChE Journal, 1987
- PROFILE OF LIQUID FLOW IN BUBBLE COLUMNSChemical Engineering Communications, 1986
- Gas holdup and mass-transfer characteristics in a three-phase bubble columnIndustrial & Engineering Chemistry Process Design and Development, 1986
- INFLUENCE OF NON-NEWTONIAN FLOW BEHAVIOUR ON MASS TRANSFER INBUBBLE COLUMNS WITH AND WITHOUT DRAFT TUBES†Chemical Engineering Communications, 1986
- Stochastic approach to the hydrodynamics of gas-liquid dispersionsIndustrial & Engineering Chemistry Fundamentals, 1981
- Note on mass transfer at gas sparged electrodesElectrochimica Acta, 1979
- Liquid-phase mixing in bubble columns: Effect of liquid propertiesThe Chemical Engineering Journal, 1974