Abstract
Abstract Photocatalytic oxidation of toluene in the gas phase over UV-illuminated thin layer of titanium dioxide was studied. The reaction was performed in the annular photocatalytic reactor at the room temperature and at various space times. The inlet reacting mixture consisted of air containing toluene and water vapors. Dependence of the reaction rate on various operating variables (water content, inlet toluene concentration and gas flow rate) was examined. The catalytic activity for toluene removal was evaluated by measuring the inlet and outlet toluene concentrations with GC/FID at the steady-state conditions. The additional XRD and FTIR measurements were carried out to get better understanding of the catalytic properties. Modelling analysis was carried out to investigate effect of the key parameters on the reactor performance. To understand complex interaction between the chemical reaction and mass transfer phenomena, experimental data were analysed and compared with three different mathematical models (one-dimensional (1D) model and two-dimensional (2D) models based on ideal flow and laminar flow conditions). The proposed models were verified by comparing the computer simulation data with the experimental laboratory results. It was found out that behaviour of the annular photocatalytic reactor was mainly limited by the interphase mass transfer. Finally, the 2D heterogeneous model, based on the assumed laminar flow through the reactor, appeared to be the most suitable model for a detailed description of the annular photocatalytic reactor used for air pollution remediation.
Published Version
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