Advanced oxidation processes (AOPs) based on ozone are gaining continuously growing popularity in wastewater treatment. This study explored the treatment of coking wastewater using a combination of ozonation (O-3), ultraviolet (UV), and hydrogen peroxide (H2O2) process expressed by % chemical oxygen demand (COD) removal, % total organic carbon (TOC), % UV254, % fluorescence intensity removal and its electrical energy consumption. The obtained results demonstrated that, the combination of O-3, UV, and H2O2 which is denoted by O-3/UV/H2O2 in this study achieved great success in COD removal (92.08%), TOC removal (78.25%), and reduction of fluorescence intensity (99.82%). Compared with the O-3 and O-3/UV processes, O-3/UV/H2O2 improved the COD removal by approximately 54-69% and 38-51%, respectively. In addition, the energy consumption was reduced by 53-67%. The TOC removal rate in the effluent ranged 71% and 83%, while the UV254 removal rate was up to 90%. The fluorescence spectroscopy showed that the O-3/UV/H2O2 combination process reduced the fluorescence intensity by almost 97% within 10 min. Furthermore, the total polycyclic aromatic hydrocarbons (PAHs) concentration in the effluent was less than 10 mu g/L (removal efficiency > 80%) and the most toxic benzo(a)pyrene (BaP) was less than 0.03 mu g/L (0.018 mu g/L). In addition, the energy consumption of the O-3/UV/H2O2 process was 53-67% lower than those of O-3 and O-3/UV processes. Furthermore, the energy consumption was 80.26 kWh m(-3) after 60 min of reaction time when the COD (69.3 mg/L) met the standard discharge. Finally, the O-3/UV/H2O2 process could be an effective method for improving the mineralisation of refractory organic matter.