A platform for research: civil engineering, architecture and urbanism
Oil refinery wastewater treatment using physicochemical, Fenton and Photo-Fenton oxidation processes
The objective of this study was to investigate the application of advanced oxidation processes (AOPs) to the treatment of wastewaters contaminated with hydrocarbon oil. Three different oil-contaminated wastewaters were examined and compared: (i) a ‘real’ hydrocarbon wastewater collected from an oil refinery (Conoco-Phillips Whitegate refinery, County Cork, Ireland); (ii) a ‘real’ hydrocarbon wastewater collected from a car-wash facility located at a petroleum filling station; and (iii) a ‘synthetic’ hydrocarbon wastewater generated by emulsifying diesel oil and water. The AOPs investigated were Fe2+/H2O2 (Fenton's reagent), Fe2+/H2O2/UV (Photo-Fenton's reagent) which may be used as an alternative to, or in conjunction with, conventional treatment techniques. Laboratory-scale batch and continuous-flow experiments were undertaken. The photo-Fenton parametric concentrations to maximize COD removal were optimized: pH = 3, H2O2 = 400 mg/L, and Fe2+ = 40 mg/L. In the case of the oil-refinery wastewater, photo-Fenton treatment achieved approximately 50% COD removal and, when preceded by physicochemical treatment, the percentage removal increased to approximately 75%.
Oil refinery wastewater treatment using physicochemical, Fenton and Photo-Fenton oxidation processes
The objective of this study was to investigate the application of advanced oxidation processes (AOPs) to the treatment of wastewaters contaminated with hydrocarbon oil. Three different oil-contaminated wastewaters were examined and compared: (i) a ‘real’ hydrocarbon wastewater collected from an oil refinery (Conoco-Phillips Whitegate refinery, County Cork, Ireland); (ii) a ‘real’ hydrocarbon wastewater collected from a car-wash facility located at a petroleum filling station; and (iii) a ‘synthetic’ hydrocarbon wastewater generated by emulsifying diesel oil and water. The AOPs investigated were Fe2+/H2O2 (Fenton's reagent), Fe2+/H2O2/UV (Photo-Fenton's reagent) which may be used as an alternative to, or in conjunction with, conventional treatment techniques. Laboratory-scale batch and continuous-flow experiments were undertaken. The photo-Fenton parametric concentrations to maximize COD removal were optimized: pH = 3, H2O2 = 400 mg/L, and Fe2+ = 40 mg/L. In the case of the oil-refinery wastewater, photo-Fenton treatment achieved approximately 50% COD removal and, when preceded by physicochemical treatment, the percentage removal increased to approximately 75%.
Oil refinery wastewater treatment using physicochemical, Fenton and Photo-Fenton oxidation processes
Tony, Maha A. (author) / Purcell, Patrick J. (author) / Zhao, Yaqian (author)
Journal of Environmental Science and Health, Part A ; 47 ; 435-440
2012-02-01
6 pages
Article (Journal)
Electronic Resource
Unknown
Oil refinery wastewater treatment using physicochemical, Fenton and Photo-Fenton oxidation processes
Online Contents | 2012
|Cosmetic wastewater treatment using the Fenton, Photo-Fenton and H2O2/UV processes
Taylor & Francis Verlag | 2014
|Cosmetic wastewater treatment using the Fenton, Photo-Fenton and H2O2/UV processes
Online Contents | 2014
|DOAJ | 2024
|