Kinetics of catalytic supercritical water oxidation of phenol over TiO2

We oxidized phenol, a model pollutant, in supercritical water at 380-440 de grees C and 219-300 atm using bulk TiO2 as a catalyst in a tubular flow rea ctor. The phenol conversion and CO2 molar yield from this catalytic supercr itical water oxidation (SCWO) are much higher than those from conventional noncatalytic SCWO of phenol under otherwise identical processing conditions . The selectivities to undesired phenol dimers decrease in the presence of TiO2, and the catalyst is stable and maintains its activity during phenol o xidation. All of these features are desirable for a catalytic SCWO waste tr eatment process. The rate of phenol disappearance over TiO2 was consistent with a power-law rate equation that is 0.69 order in phenol and 0.22 order in O-2. The rate of disappearance of total organic carbon (TOC) exhibited r eaction orders of 0.51 for the TOC concentration and 0 for the oxygen conce ntration. Both rates are independent of the water concentration. The cataly tic kinetics for phenol disappearance were also consistent with the Mars-va n Krevelen mechanism and with a Langmuir-Hinshelwood dual-site mechanism co mprising reversible adsorption of phenol on one type of catalytic site, rev ersible dissociative adsorption of oxygen on a different type of site, and irreversible, rate-determining surface reaction between adsorbed phenol and adsorbed oxygen. Our results show that the reactor volume for catalytic SC WO using TiO2 would be about one-fourth that of the volume required for con ventional, noncatalytic SCWO.