Affiliations: College of Chemical Engineering, South China
University of Technology, Guangzhou 510641, China | Swalm School of Chemical Engineering, Mississippi
State University, MS 39762, Starkville,USA
Abstract: Destruction of organic contaminants in water by ozonation is a
gas-liquid process which involves ozone mass transfer and fast irreversible
chemical reactions. Ozonation reactor design and process optimizing require the
modeling of the gas-liquid interactions within the reactor. In this paper a
theoretical model combining the fluid dynamic and reaction kineticparameters is
proposed for predicting the destruction rates of organic pollutants in a
semi-batch stirred-tank reactor by ozonation. A simple expression for the
enhancement factor as ourprevious work (Cheng, 2000) has been applied to
evaluate the chemical mass transfer coefficient in ozone
absorption.2,4-dichlorophenol (2,4-DCP) and 2,6-DCP or their mixture are chosen
as the model compounds for simulating, and the predicted DCP oundation item:
The National Natural Science Foundation of China (No. 20006006) ncentrations
are compared with some measured data.