Experimental study on gas-liquid dispersion and mass transfer in shear-thinning system with coaxial mixer
Fluid Dynamics and Transport Phenomena|Updated:2026-01-06
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Experimental study on gas-liquid dispersion and mass transfer in shear-thinning system with coaxial mixer
Chinese Journal of Chemical EngineeringVol. 26, Issue 9, Pages: 1785-1791(2018)
Affiliations:
Institute of Process Equipment, College of Energy Engineering, Zhejiang University,Hangzhou,China,310027
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Published:2018
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Baoqing Liu, Yijun Zheng, Ruijia Cheng, Zilong Xu, Manman Wang, Zhijiang Jin. Experimental study on gas-liquid dispersion and mass transfer in shear-thinning system with coaxial mixer[J]. Chin.J.Chem.Eng., 2018, 26(9): 1785-1791.
DOI:
Baoqing Liu, Yijun Zheng, Ruijia Cheng, Zilong Xu, Manman Wang, Zhijiang Jin. Experimental study on gas-liquid dispersion and mass transfer in shear-thinning system with coaxial mixer[J]. Chin.J.Chem.Eng., 2018, 26(9): 1785-1791.DOI:
Experimental study on gas-liquid dispersion and mass transfer in shear-thinning system with coaxial mixer
and liquid concentration on the gas-liquid mixing in a shear-thinning system with a coaxial mixer were investigated by experiment
and the overall gas holdup
relative power demand
and volumetric mass transfer coefficient under different conditions were compared. The results show that
the increasing stirring power or gas flow rate is beneficial in promoting the overall gas holdup and volumetric mass transfer coefficient
while the increasing system viscosity weakens the mass transfer in a shearing-thinning system. Among the three turbines
the six curved-blade disc turbine (BDT-6) exhibits the best gas pumping capacity; the six 45° pitched-blade disc turbine (PBDT-6) has the highest volumetric mass transfer coefficient at the same unit volume power.
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