Numerical modeling of mass transfer processes coupling with reaction for the design of the ozone oxidation treatment of wastewater

A computational model for an ozone oxidation column reactor used in dyeing wastewater treatment is proposed to represent, simulate, and predict the ozone bubble process. Considering the hydrodynamics, mass transfer, and ozone oxidation reaction, coupling modeling can more realistically calculate the ozone oxidation bubble process than the splitting methods proposed in previous research. The modeling is validated and shows great consistency with experimental data. The verified model is used to analyze the effect of operating conditions, such as the initial gas velocity and the ozone concentration, and structural conditions, such as multiple gas inlets. The ozone consumption is influenced by the gas velocity and the initial ozone concentration. The ozone's utilization decreases with the increasing gas velocity while nearly the same at different initial ozone concentrations. Simulation results can be used in guiding the practical operation of dyeing wastewater treatment and in other ozonation systems with known rate constants in wastewater treatment.

Automated summary

A computational model is proposed to simulate and predict the ozone bubble process in an ozone oxidation column reactor used in dyeing wastewater treatment. The validated model shows great consistency with experimental data and can be used to analyze the effects of operating and structural conditions on ozone consumption. The results indicate that ozone utilization decreases with increasing gas velocity, while remaining nearly constant at different initial ozone concentrations.