Abstract
Abstract A computer model based on the establishment of mass balance equations and on the model of fluids flow “stirred tank in series” was developed in order to calculate the ozone transfer coefficient kLa and kinetic constant kc of ozone consumption by water. On the basis of experimental data, the correlation for gas holdup eg and bubble diameter dvs, were proposed and used to calculate the specific interfacial area a. The liquid-phase mass transfer coefficient kL for ozone was evaluated from a and the kLa data.
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