화학공학소재연구정보센터
Chemical Engineering Research & Design, Vol.73, No.6, 745-749, 1995
A Modified Axial-Dispersion Model Applied to 3-Phase Fluidized-Bed Reactors with a Transition Zone
Measurements demonstrated that liquid backmixing from freeboard to bed affects gas-liquid mass transfer in fluidized beds, especially when there is a gradual transition between bed and freeboard. New models account for continuous variations with height of the volumetric mass-transfer and axial dispersion coefficients.