z-logo
Premium
Mass transfer characteristics of horizontal agitated contactors
Author(s) -
Joshi J. B.,
Sharma M. M.
Publication year - 1976
Publication title -
the canadian journal of chemical engineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.404
H-Index - 67
eISSN - 1939-019X
pISSN - 0008-4034
DOI - 10.1002/cjce.5450540535
Subject(s) - impeller , sparging , contactor , nozzle , mass transfer , propeller , mass transfer coefficient , aeration , mechanics , materials science , agitator , chemistry , analytical chemistry (journal) , thermodynamics , chromatography , physics , engineering , marine engineering , power (physics) , organic chemistry
The values of effective interfacial area, a , and liquid side mass transfer coefficient, k L a , were obtained in 0.385, 0.57 and 1.0 m i.d. horizontal agitated contactors by using chemical methods. Propeller type of impellers were employed for agitation. Two modes of operation were studied: (i) surface aeration and (ii) sparging of gas. The impeller speed was varied from 50 to 700 rev/min , and the nozzle gas velocity was varied from 40 to 160 m/s. The effects of impeller spacing, liquid submergence and nozzle gas velocity on the values of a and k L a were investigated. A scale‐up criterion is discussed.

This content is not available in your region!

Continue researching here.

Having issues? You can contact us here
Accelerating Research

Address

John Eccles House
Robert Robinson Avenue,
Oxford Science Park, Oxford
OX4 4GP, United Kingdom