Multicomponent and contamination effects on mass transfer in a liquid-liquid extraction rotating disc contractor

Chemical Engineering Research and Design

Volumn 79, Issue 3, 2001, Pages 335-346

  Brodkorb, M J ^a   Slater, M J ^a  

^a UNIVERSITY OF BRADFORD   (United Kingdom)

Author keywords

[No Author keywords available]

Indexed keywords

ACETONE; CONTAMINATION; EXTRACTION; HYDRODYNAMICS; PHENOLS; PILOT PLANTS; ROTATING DISKS; SURFACE TENSION; TERNARY SYSTEMS; TOLUENE;

QUARTENARY SYSTEMS;

MASS TRANSFER;

LIQUID-LIQUID EXTRACTION; MASS TRANSFER; PHENOL; PILOT PLANT; POLLUTANT TRANSPORT; ROTATING DISC;

EID: 0035299139     PISSN: 02638762     EISSN: None     Source Type: Journal    
DOI: 10.1205/026387601750281699     Document Type: Article

References (14)

1. Maxwell-Stefan approach in extractor design
2. A possible approach to improving rotating disc contractor design accounting for drop breakage and mass transfer with contamination
3. A combined model of mass transfer coefficients for contaminated drop liquid-liquid systems
4. An improved stage-wise model of counter-current flow liquid-liquid extractors
5. Simulation of the fluid dynamics of solvent extraction columns from single droplet parameters
6. Computational procedures for column simulation and desing
7. The application of a combined mass transfer coefficient model in understanding the extraction section of a new caprolactam production process
8. Determination of phase equilibria and mixture densities for the quaternary system: Toluene-acetone-phenol-water
9. Aspects of multicomponent mass transfer kinetics in liquid-liquid systems