Oxidation of NO by ozone in the presence of TiO2 catalyst was studied at varying NO inlet concentrations, gas flow rates and reactor temperatures. Ozone produced by a coaxial DBD reactor was mixed with N-2 diluted NO and directed to a reaction chamber. The experiments were carried out with and without the presence of TiO2 catalyst. The inlet concentration of NO was varied between 200 and 800 ppm and the total flow rate was varied between 0.5 and 2 slm which resulted in the reaction times of 1-4 s. Independent of NO inlet concentration, gas flow rate, reactor temperature and presence of catalyst, NO was totally oxidized to NO2 when the inlet O-3 concentration reached the value of the inlet NO concentration. Further increase of inlet O-3 concentration resulted in the oxidation of NO2 to N2O5. The effect of TiO2 catalyst appeared at higher reactor temperatures, where the presence of TiO2 increased the oxidation efficiency of NO2 to N2O5. The proposed model showed that the gas phase oxidation of NO to NO2 and N2O5 is possible to describe by three main reactions between nitrogen-oxides and ozone. The effect of catalyst can be explained by additional oxidation of NO2 on the catalyst surface by oxygen species created on the surface by catalytic decomposition of ozone. (C) 2016 Elsevier Ltd. All rights reserved.