Hydrodynamics and ozone mass transfer in a tall bubble column
Authors:
- A.K. BińABA.K. Biń
- P. MachniewskiPMP. Machniewski
- 1 November 2001
- journal article
- Published by Elsevier in Chemical Engineering Science
- Vol. 56 (21-22) , 6233-6240
Abstract
No abstract availableKeywords
This publication has 9 references indexed in Scilit:
- A comparative study of gas hold-up, bubble size, interfacial area and mass transfer coefficients in stirred gas–liquid reactors and bubble columnsChemical Engineering and Processing - Process Intensification, 2001
- Effect of pressure profile on evaluation of volumetric mass transfer coefficient in ka bioreactorsBiochemical Engineering Journal, 2000
- Hydrodynamics and computer simulation of an ozone oxidation reactor for treating drinking waterChemical Engineering Science, 1999
- Survey of measurement techniques for gas–liquid mass transfer coefficient in bioreactorsBiochemical Engineering Journal, 1999
- Mass transfer in gas–liquid contactorsChemical Engineering and Processing - Process Intensification, 1999
- Gas holdup and mass transfer in bubble column reactors operated at elevated pressureChemical Engineering Science, 1999
- Modeling Hydrodynamics and Ozone Residual Distribution in a Pilot‐Scale Ozone Bubble‐Diffuser ContactorJournal AWWA, 1993
- DISPERSION OF GAS AND LIQUID IN BUBBLE COLUMNS OF HOMOGENEOUS BUBBLE FLOW REGIMEChemical Engineering Communications, 1989
- The use of transfer functions in evaluating residence time distribution curvesChemical Engineering Science, 1969