Ozone Mass Transfer in Stirred Vessel

摘要

A method is proposed and a model is developed which are capable of providing a correlation of the mass transfer coefficient kLa, with stirrer speed and gas superficial velocity. The method can be adopted for deriving a correlation which can be profitably used for ozone gas#x2013;liquid reaction both for assessing the absorption regime and for the simulation of oxidation processes which evolve according to slow reaction regime.