This article presents an experimental investigation of the photocatalytic oxidation of several volatile organic compounds (formaldehyde, benzene, and toluene) under realistic indoor conditions. A novel annular reactor coated with TiO 2 was designed to perform kinetic studies on (1) pollutant removal, (2) mineralization by CO 2 formation, and (3) intermediate formation and removal in the gas phase. The pollutant(s) was/were injected at a constant rate in a 1.95-m 3 environmental chamber ventilated at a constant rate between 3.8 and 4.2 m 3 /h. The annular reactor was installed on an external recirculation loop, and processed air was reintroduced into the chamber. Recirculation rates were set at 25-200 m 3 /h, corresponding to recycle ratios between 6 and 50. Reaction area and residence time were greatly increased when fins were added in the annular reactor, and the removal efficiency and mineralization rate were, therefore, obviously improved. The pressure drop produced by the fins was insignificant and increased as a function of the recirculation rate. Intermediates were identified by using the GC-MS instrument, and GC-FID was used for the CO 2 measurements. Benzaldehyde, benzyl alcohol, benzene, phenol, and acetone (or propionaldehyde) were the main intermediates in the gas phase. Increase in residence time for a reactor operating in a high face velocity regime was an important factor that led to the complete oxidation of primary and secondary pollutants. For mixture oxidation, selectivity toward benzene and toluene blocked the elimination of formaldehyde. A simple model was developed to predict removal efficiency by the recycle ratio. Model predictions showed good agreement with the experimental results.