| Abstract |
In keeping with the circular economy approach, reclaiming greywater (GW) is considered a sustainable approach to local reuse of wastewater and a viable option to reduce household demand for freshwater. This study investigated the mineralization of total organic carbon (TOC) in GW using TiO2-based advanced oxidation processes (AOPs) in a custom-built stirred tank reactor. The combinations of H2O2, O-3, and immobilized TiO2 under either dark or UVA irradiation conditions were systematically evaluated-namely TiO2/dark, O-3/dark (ozonation), H2O2/dark (peroxidation), TiO2/UVA (photocatalysis), O-3/UVA (Ozone photolysis), H2O2/UVA (photo-peroxidation), O-3/TiO2/dark (catalytic ozonation), O-3/TiO2/UVA (photocatalytic ozonation), H2O2/TiO2/dark, H2O2/TiO2/UVA, H2O2/O-3/dark (peroxonation), H2O2/O-3/UVA (photo-peroxonation), H2O2/O-3/TiO2/dark (catalytic peroxonation), and H2O2/O-3/TiO2/UVA (photocatalytic peroxonation). It was found that combining different treatment methods with UVA irradiation dramatically enhanced the organic mineralization efficiency. The optimum TiO2 loading in this study was observed to be 0.96 mg/cm(2) with the highest TOC removal (54%) achieved using photocatalytic peroxonation under optimal conditions (0.96 mg TiO2/cm(2), 25 mg O-3/min, and 0.7 H2O2/O-3 molar ratio). In peroxonation and photo-peroxonation, the optimal H2O2/O-3 molar ratio was identified to be a critical efficiency parameter maximizing the production of reactive radical species. Increasing ozone flow rate or H2O2 dosage was observed to cause an efficiency inhibition effect. This lab-based study demonstrates the potential for combined TiO2-AOP treatments to significantly reduce the organic fraction of real GW, offering potential for the development of low-cost systems permitting safe GW reuse. |