Effects of surfactants on hydrodynamics and mass transfer in a split-cylinder airlift reactor

被引:33
作者
Moraveji, Mostafa Keshavarz [1 ]
Pasand, Mohamad Morovati [1 ]
Davarnejad, Reza [1 ]
Chisti, Yusuf [2 ]
机构
[1] Arak Univ, Fac Engn, Dept Chem Engn, Arak 3815688349, Iran
[2] Massey Univ, Sch Engn, Palmerston North, New Zealand
关键词
airlift reactor; surfactants; gas-liquid mass transfer; gas hold-up; liquid circulation; TRANSFER COEFFICIENTS; TRANSFER PERFORMANCE; BUBBLE-COLUMN; BIOREACTOR; DESIGN; RISE;
D O I
10.1002/cjce.20516
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Effects of various concentrations (05?ppm) of anionic (sodium dodecyl sulfate, SDS) and non-ionic (Tween-80 and Triton X-405) surfactants on gas hold-up and gasliquid mass transfer in a split-cylinder airlift reactor are reported for airwater. 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 gasliquid interfacial area for mass transfer. Nevertheless, the overall gasliquid 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.
引用
收藏
页码:93 / 99
页数:7
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