The advanced chemical oxidation of raw and biologically pretreated textile wastewater by (1) ozonation, (2) H 2 O 2 /UV À C oxidation and (3) sequential application of ozonation followed by H 2 O 2 / UV À C oxidation was investigated at the natural pH values (8 and 11) of the textile ef¯uents for 1 h. Analysis of the reduction in the pollution load was followed by total environmental parameters such as TOC, COD, UV±VIS absorption kinetics and the biodegradability factor, f B . The successive treatment combination, where a preliminary ozonation step was carried out prior to H 2 O 2 /UV À C oxidation without changing the total treatment time, enhanced the COD and TOC removal ef®ciency of the H 2 O 2 /UV À C oxidation by a factor of 13 and 4, respectively, for the raw wastewater. In the case of biotreated textile ef¯uent, a preliminary ozonation step increased COD removal of the H 2 O 2 /UV À C treatment system from 15% to 62%, and TOC removal from 0% to 34%. However, the sequential process did not appear to be more effective than applying a single ozonation step in terms of TOC abatement rates. Enhancement of the biodegradability factor (f B ) was more pronounced for the biologically pretreated wastewater with an almost two-fold increase for the optimized Advanced Oxidation Technologies (AOTs). For H 2 O 2 /UV À C oxidation of raw textile wastewater, apparent zero order COD removal rate constants (k app ), and the second order OH . formation rates (r i ) have been calculated.
NOTATION
AOXAdsorbable organic halogens BOD 5, o 5-day Biochemical Oxygen Demand at time t = 0 (mg dm À3 ) BOD 5, t 5-day Biochemical Oxygen Demand at treatment time t (mg dm À3 ) COD o Chemical Oxygen Demand at time t =0 (mg dm À3 ) COD t Chemical Oxygen Demand at treatment time t (mg dm À3 ) C OH Concentration of OH . (mol dm À3 ) d Effective path length of UV-C light in the reactor (cm) f B Biodegradability factor (dimensionless) F H Fraction of incident radiation at 254 nm absorbed by H 2 O 2 (dimensionless) I o Incident light¯ux of the UV-C lamp (Einstein dm À3 s À1 ) k app Apparent zero order rate constant for COD abatement (mg dm À3 min À1 ) k OH Rate constant for reaction of pollutants with OH . (dm 3 mol s À1 ) r i Second order rate of initiation of OH . formation (mol dm À3 s À1 ) UV-C Light emission in the spectral wavelength region 180 nm`l`290 nm UV H 2 O 2 Absorbance of H 2 O 2 at 254 nm wavelength (m À1 ) UV T Total absorbance at 254 nm wavelength (m À1 ) UV 254 Absorbance of the wastewater at 254 nm wavelength (m À1 ) f Quantum yield for H 2 O 2 photolysis (dimensionless)