Liquid−Liquid Extraction with an Interphase Chemical Reaction in an Air-Driven Two-Impinging-Streams Reactor: Effective Interfacial Area and Overall Mass-Transfer Coefficient
- 9 July 2002
- journal article
- research article
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 41 (16) , 4085-4093
- https://doi.org/10.1021/ie010750x
Abstract
No abstract availableKeywords
This publication has 36 references indexed in Scilit:
- Alkaline hydrolysis of isoamylformate: Effect of dissolved electrolytes on kineticsThe Canadian Journal of Chemical Engineering, 2001
- Flow and thermal characteristics of steady two dimensional confined laminar opposing jets: Part II. Unequal jetsInternational Communications in Heat and Mass Transfer, 1997
- Flow and thermal characteristics of steady two dimensional confined laminar opposing jets: Part I. Equal jetsInternational Communications in Heat and Mass Transfer, 1997
- Kinetics of alkaline hydrolysis of 2‐ethylbutylformateThe Canadian Journal of Chemical Engineering, 1996
- COMPARATIVE EVALUATION OF DIFFERENT TURBULENCE MODELS FOR CONFINED IMPINGING AND OPPOSING JET FLOWSNumerical Heat Transfer, Part A: Applications, 1995
- Liquid-Liquid Extraction with Interphase Chemical Reaction in Agitated Columns. 2. Hydrodynamics and Mass Transfer in Rotating Disk and Oldshue Rushton ContactorsIndustrial & Engineering Chemistry Process Design and Development, 1980
- Mass transfer in packed liquid—liquid extraction columnsChemical Engineering Science, 1975
- Effective interfacial area in packed liquid extraction columnsChemical Engineering Science, 1970
- Effective interfacial area in agitated liquid—liquid contactorsChemical Engineering Science, 1967
- Effective interfacial area in liquid—liquid extractionChemical Engineering Science, 1966