Chemical Engineering Journal 168 (2011) 134–139 Contents lists available at ScienceDirect Chemical Engineering Journal journal homepage: www.elsevier.com/locate/cej Degradation of methyl orange by UV/H 2 O 2 advanced oxidation process Shaker Haji , Baghdad Benstaali, Nader Al-Bastaki Department of Chemical Engineering, College of Engineering, University of Bahrain, P.O. 32038, Isa Town, Bahrain article info Article history: Received 12 August 2010 Received in revised form 14 December 2010 Accepted 15 December 2010 Keywords: Methyl orange dye UV/H2O2 process Photochemical degradation Initial reaction rate Kinetics abstract The degradation of the methyl orange (MO) dye was investigated using advanced oxidation process (AOP) by exposing MO aqueous solution to UV irradiation after the addition of hydrogen peroxide (H 2 O 2 ). The presence of H 2 O 2 in MO solutions accelerated the dye degradation process. For instance, a complete degra- dation was achieved in 3 min when 0.1 mL of H 2 O 2 aqueous solution was added to 20 mL of 0.078 mM MO solution compared to only 26% degradation achieved in 4 h in the absence of H 2 O 2 . The degradation of MO molecules was accompanied by the decolorization of the solution. A thorough investigation of the AOP process was carried out by studying the influence of the dye concentration, H 2 O 2 dosage, UV irradi- ation power, and the area of the solution exposed to the UV source. It was found that, at the investigated ranges, the initial dye degradation rate increased with the increase in the initial dye concentration, UV irradiation power, and the surface area of the solution exposed to UV irradiation. An optimum concentra- tion of H 2 O 2 was found to exist for the MO degradation reaction. AOP by UV/H 2 O 2 treatment was found to be a technically feasible approach for the decolorization of MO aqueous solutions. © 2010 Elsevier B.V. All rights reserved. 1. Introduction An increasing interest is noticed in improving the technical means of treatment of industrial wastes owing to their toxic and hazardous organic compounds contents. The combination of one treatment technique (adsorption, oxidation, reduction, electro- chemical, and biological processes) with the addition of reaction stimulators, such as catalysts, electromagnetic radiations, and membranes, is found to lead to more efficient and reliable meth- ods of treatment. In addition, advanced oxidation processes (AOPs) became very common for the treatment of industrial wastes con- taining organic dyes. AOP is based on the generation of highly reactive radicals, which are very strong oxidizing agents (e.g. OH, E 0 = 2.8 V/NHE) at conditions near ambient temperature and pres- sure. Many researchers reported on the effectiveness of AOPs with or without its combination with other techniques. Marto et al. reported on the photocatalytic degradation of the organic dye Orange II in aqueous solutions combined with ZnO active layers deposited on screen-printed ceramic tiles where a decolorization rate over 0.015 min -1 was achieved [1]. Al-Bastaki et al. reported on the advantage of using membranes in treat- ing dyed industrial wastewater [2,3]. Photo-degradation of MO by Advanced Fenton Process using zero valent metallic iron was inves- tigated and the efficiency of the process was examined with the combination of hydrogen peroxide (H 2 O 2 ), ammonium persulfate Corresponding author. Tel.: +973 17876104; fax: +973 17680935. E-mail address: haji@eng.uob.bh (S. Haji). ((NH 4 ) 2 S 2 O 8 ), and ultraviolet (UV) irradiation [4]. Synergistic effect was reported when ultrasound and ozone were collectively used for the decolorization of MO solutions [5]. Razaee et al. reported on the decolorization of reactive blue 19 in less than 30 min using a process where a UV-C lamp (15 W) was combined with potassium persulfate (K 2 S 2 O 8 ) compared to the chemical oxidation process which took 5 h to achieve similar results [6]. Amin et al. reported on the influence of few experimental parameters such as UV inten- sity, pH of the solution, and H 2 O 2 dosage on the degradation of Blue Sulfur dye present in synthetic aqueous solutions [7]. Ale- boyeh et al. [8] investigated the degradation of Acid Orange 8 (AO8), Acid Blue 74 (AB74), and MO through the UV/H 2 O 2 pro- cess using a continuous photochemical reactor with a 15 W low pressure mercury lamp and reported that the decolorization fol- lowed an apparent first order kinetics with respect to the dye concentration. It was also reported that hydrogen peroxide plays an important role in the enhancement of the decolorization rate of azo dyes. However, when its concentration exceeds a specific value, the excess H 2 O 2 works as a hydroxyl radical self-consumer rather than a producer and, therefore, reduces the system oxidizing power [8,9]. In this study MO – which is a water soluble azo dye that is widely used in textile, printing, paper, pharmaceutical, and food industries [10] – was used as a model dye for studying the effective- ness of UV/H 2 O 2 process on the decolorization of dyed industrial wastewater. We emphasized, in this work, on the influence of the concentration of MO, the H 2 O 2 dosage, the UV intensity, and the dye solution area exposed to UV radiation on the dye degradation rate. This study shall help in better understanding the UV/H 2 O 2 process 1385-8947/$ – see front matter © 2010 Elsevier B.V. All rights reserved. doi:10.1016/j.cej.2010.12.050