Article ID Journal Published Year Pages File Type
9623754 Chemical Engineering Journal 2005 13 Pages PDF
Abstract
An experimental study has been carried out to investigate the effect of internals and sparger design on mixing time (θmix) and fractional gas hold-up (ɛG) in a batch mode sectionalized bubble column. Air and water were used as the gas-liquid phases, respectively. In the present work, sparger with the percent free area (% FA) of 0.136 and 0.6% has been used and the superficial gas velocity (VG), liquid height to column diameter (Hc/D), percent free area of the sectionalizing plate was varied from 0.06 to 0.295 m s−1, 3 to 4 and 4 to 23%, respectively. It was found that there is no significant effect of the sparger design on the mixing time but it does strongly depend on VG, Hc/D and % FA of the sectionalizing plate. The one-dimensional dispersion model successfully predicts the tracer concentration profile and the longitudinal dispersion coefficient. Also, the effect of the presence of the electrolyte too has been studied by adding a known volume of the tracer solution (NaCl). Correlations have been developed for the estimation of the fractional gas hold-up, mixing time, longitudinal dispersion coefficient (DL) and the intercell exchange velocity (uB).
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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