Simulation of Oxygen Mass Transfer in an Internal Loop Airlift Reactor with Axial Dispersion Model

Simulation of Oxygen Mass Transfer in an Internal Loop Airlift Reactor with Axial Dispersion Model

Show other versions (1)

The effect of superficial gas velocity within the range 0.01-0.164 m/s on gas holdup (overall, riser and down comer), volumetric oxygen mass transfer coefficient, liquid circulation velocity was studied in an internal loop concentric tubes airlift reactor (working volume 45 liters). It was shown tha...

Full description

Bibliographic Details
Main Authors: Aseel Abd Al-Jabbar, Ameel Mohammed Rahman, Mohammed Abd Atiya Al-Saraj
Format: Article
Language:English
Published: Al-Khwarizmi College of Engineering – University of Baghdad 2011-01-01
Series:Al-Khawarizmi Engineering Journal
Subjects:
Airlift bioreactor
reactor
dissolved oxygen; modeling
axial dispersion model
hydrodynamics
mixing
internal loop
liquid circulation velocity
gas holdup.
Online Access:http://www.iasj.net/iasj?func=fulltext&aId=2183

Internet

http://www.iasj.net/iasj?func=fulltext&aId=2183

Similar Items