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

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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...

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Autores principales: Aseel Abd Al-Jabbar, Ameel Mohammed Rahman, Mohammed Abd Atiya Al-Saraj
Formato: article
Lenguaje:EN
Publicado: Al-Khwarizmi College of Engineering – University of Baghdad 2011
Materias:
Airlift bioreactor
reactor
dissolved oxygen; modeling
axial dispersion model
hydrodynamics
mixing
internal loop
liquid circulation velocity
gas holdup.
Chemical engineering
TP155-156
Engineering (General). Civil engineering (General)
TA1-2040
Acceso en línea:https://doaj.org/article/c4235a41836c4d2ab48329873c330dfe
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