## Abstract The influences of aliphatic alcohols (C~n~H~2n+1~OH, __n__ = 1–4) and their concentrations (0–1 vol.‐%) on gas holdup, liquid circulation velocity, mixing time, and overall volumetric gas‐liquid oxygen mass transfer coefficient were considered in a split‐cylinder airlift reactor sparged
Effects of surfactants on hydrodynamics and mass transfer in a split-cylinder airlift reactor
✍ Scribed by Mostafa Keshavarz Moraveji; Mohamad Morovati Pasand; Reza Davarnejad; Yusuf Chisti
- Publisher
- John Wiley and Sons
- Year
- 2011
- Tongue
- English
- Weight
- 219 KB
- Volume
- 90
- Category
- Article
- ISSN
- 0008-4034
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✦ Synopsis
Abstract
Effects of various concentrations (0–5 ppm) of anionic (sodium dodecyl sulfate, SDS) and non‐ionic (Tween‐80 and Triton X‐405) surfactants on gas hold‐up and gas–liquid mass transfer in a split‐cylinder airlift reactor are reported for air–water. Surfactants were found to strongly enhance gas hold‐up. Non‐ionic surfactants were more effective in enhancing gas hold‐up compared to the anionic surfactant SDS. An enhanced gas hold‐up and a visually reduced bubble size in the presence of surfactants implied an enhanced gas–liquid interfacial area for mass transfer. Nevertheless, the overall gas–liquid volumetric mass transfer coefficient was reduced in the presence of surfactants, suggesting that surfactants greatly reduced the true liquid film mass transfer coefficient and this reduction outweighed the interfacial area enhancing effect. Presence of surfactants did not substantially affect the induced liquid circulation rate in the airlift vessel.
📜 SIMILAR VOLUMES
The hydrodynamics and mass transfer, specifically the effects of gas velocity and the presence and type of solids on the gas hold-up and volumetric mass transfer coefficient, were studied on a lab-scale airlift reactor with internal draft tube. Basalt particles and biofilmcoated particles were used
## Abstract The aim of this work was to investigate an influence of different alcohols on the behavior of a draft tube airlift reactor. The main hydrodynamic and mass transfer parameters in 1 wt % aqueous solutions of five aliphatic alcohols were examined. The results showed that alcohol addition e
## Abstract Computational Fluid Dynamics (CFD) is used to compare the hydrodynamics and mass transfer of an internal airlift reactor with that of a bubble column reactor, operating with an air/water system in the homogeneous bubble flow regime. The liquid circulation velocities are significantly hi