화학공학소재연구정보센터
Canadian Journal of Chemical Engineering, Vol.79, No.1, 107-111, 2001
Suspension of solid particles in multi-impeller three-phase stirred tank reactors
Solids suspension characteristics in gas-liquid-solid three-phase stirred tanks with multi-impellers were experimentally examined. Minimum impeller speeds for ultimately homogeneous solid suspension have been measured stirred tank reactors. Three impellers were installed: two four-pitched blade downflow disk turbines and one Pfaudler type impeller chosen to provide good gas dispersion and to accomplish off-bottom suspension of solid particles, respectively. Cas dispersion causes an increase in particle sedimentation associated with a decrease in power consumption and as a result, minimum impeller speeds for ultimately homogeneous solid suspension increase with increasing gas flow rates. A correlation was developed to predict minimum impeller speeds for ultimately homogeneous solid suspension. The proposed correlation, which agrees satisfactorily with the experimental results, is expected to be useful in design and scale-up.