The velocity distribution in Rayleigh convection caused by acetone volatilization in acetone-ethyl acetate binary system was observed in a vertical cross section of an initially quiescent liquid layer by utilizing particle image velocimetry. Obvious turbulent vortexes that were induced by Rayleigh convection appeared in the bulk liquid
and its statistic features indicated that Rayleigh convection became more intensewith the increase of Ra number and ReG number. Mass transfer coefficient was measured and the computed enhancement factor indicated that Rayleigh convection could promote the surface renewal of the liquid phase and intensify the interfacial mass transfer significantly. A method was proposed for the prediction of mass transfer coefficient based on the measured velocity vector
and the predicted mass transfer coefficients are in reasonable agreement with the experimental results.
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Characterization of Rayleigh Convection in Interfacial Mass Transfer by Lattice Boltzmann Simulation and Experimental Verification
Dynamic behavior of a single bubble in cavity flow driven by a turbulent channel
Mass transfer enhancement and hydrodynamic performance with wire mesh coupling solid particles in bubble column reactor
Effect of surfactant frequently used in soil flushing on oxygen mass transfer in micro-nano-bubble aeration system
Mixing of miscible shear-thinning fluids in a lid-driven cavity
Related Author
付博
袁希钢
刘伯潭
陈淑勇
张会书
曾爱武
余国琮
Bao Yuyun
Related Institution
State Key Laboratory of Chemical Engineering, School of Chemical Engineering and Technology, Tianjin University
School of Engineering, University of Aberdeen
State Key Laboratory of Chemical Resource Engineering, School of Chemical Engineering, Beijing University of Chemical Technology
College of Electromechanical Engineering, Qingdao University of Science and Technology
Key Laboratory of Multiphase Flow Reaction and Separation Engineering of Shandong Province, College of Chemical Engineering, Qingdao University of Science and Technology