Catalytic wet oxidation (CWO) of
phenolic wastewater containing
phenol, o-cresol, and 2,5-dimethylphenol was carried
out in a batch reactor (phenolics = 10 g/L, chemical oxygen demand
(COD) = 26 000 mg/L, and total organic carbon (TOC) = 7900
mg/L). Using the Box–Behnken experimental design (BBD) approach,
the following optimum CWO conditions (catalyst: 5% Cu/AC) for phenolics
degradation were found: C
cat = 3.4 g/L, T = 148 °C, P
O2
= 0.61 MPa, and pH = 7.4. Under these conditions, TOC and COD removals
of 88 and 90%, respectively, were obtained after 4 h of reaction. p-Benzoquinone and hydroquinone were identified as major
intermediates, whereas a mixture of carboxylic acids was detected
in treated wastewater. At higher oxygen pressures (stoichiometric
and above), mineralization of phenolics was improved although the
overall degradation was lower probably due to overoxidation. Reaction
kinetics, reusability of the catalysts, and detailed characterization
of spent catalysts are also discussed in this paper.