title: Changes of turbidity during the phenol oxidation by photo-Fenton treatment.
abstract: Turbidity presented by phenol solutions oxidized with Fenton reagent shows the tendency of a first order intermediate kinetics. Thus, turbidity can be considered a representative parameter of the presence of intermediate oxidation species, which are generated along the decomposition of toxic and reluctant contaminants, such as phenol. Moreover, that parameter presents a linear dependence with the catalyst dosage, but is also determined by the initial contaminant load. When analyzing the oxidation mechanism of phenol, it is found that the maximum turbidity occurs when the treatment is carried out at oxidant to phenol molar ratios R = 4.0. These oxidation conditions correspond to the presence of a reaction mixture mainly composed of dihydroxylated rings, precursors of the muconic acid formation. The oxidation via "para" comprises the formation reactions of charge transfer complexes (quinhydrone), between the para-dihydroxylated intermediates (hydroquinone) and the para-substituted quinones (p-benzoquinone), which are quite unstable and reactive species, quickly decomposed into hydroxyhydroquinones. Working with oxidant ratios up to R = 6.0, the maximum observed value of turbidity in the oxidized solutions is kept almost constant. It is found that, in these conditions, the pyrogallol formation is maximal, what is generated through the degradation of ortho-species (catechol and ortho-benzoquinone) and meta-substituted (resorcinol). Operating with ratios over R = 6.0, these intermediates are decomposed into biodegradable acids, generating lower turbidity in the solution. Then, the residual turbidity is a function of the molar ratio of the ferrous ions vs. moles of oxidant utilized in the essays, that lets to estimate the stoichiometric dosage of catalyst as 20 mg/L at pH = 3.0, whereas operating in stoichiometric conditions, R = 14.0, the residual turbidity of water results almost null.
authors.affiliation: Department of Chemical and Environmental Engineering, EUI Vitoria-Gasteiz, University of the Basque Country UPV/EHU, Nieves Cano, 12, 01006, Vitoria-Gasteiz, Spain, natalia.villota@yahoo.es.
authors.forename: Natalia
authors.initials: N
authors.lastname: Villota
authors.forename: Luis M
authors.initials: LM
authors.lastname: Camarero
authors.forename: Jose M
authors.initials: JM
authors.lastname: Lomas
authors.forename: Jonatan
authors.initials: J
authors.lastname: Perez
mesh_terms: D002384:Catalysis; D002851:Chromatography, High Pressure Liquid; D006861:Hydrogen Peroxide / Q000737:chemistry*; D006863:Hydrogen-Ion Concentration; D007501:Iron / Q000737:chemistry*; D007700:Kinetics; D009391:Nephelometry and Turbidimetry / Q000379:methods; D016877:Oxidants / Q000737:chemistry; D010084:Oxidation-Reduction; D019800:Phenol / Q000737:chemistry*; D011809:Quinones / Q000737:chemistry; D013056:Spectrophotometry, Ultraviolet; D013696:Temperature; D014865:Waste Disposal, Fluid / Q000379:methods*; D014874:Water Pollutants, Chemical / Q000737:chemistry*; D018508:Water Purification / Q000379:methods*
chemical_list: C045076:Fenton's reagent; D016877:Oxidants; D011809:Quinones; D014874:Water Pollutants, Chemical; D019800:Phenol; D006861:Hydrogen Peroxide; D007501:Iron