Ceramic open cell foams have recently been proposed as a new catalyst structure to benefit from its characteristic properties like low pressure drop at relatively high specific surface and enhancement of heat and mass transfer. This study focuses on the application of an impregnated ceramic foam inside a gas-particle filter element to create a multifunctional reactor configuration. Selective catalytic NO reduction (SCR) and C3H6 oxidation over a V2O5-WO3-TiO2 catalyst are used as model reactions. Experiments were performed in two different reactor configurations (axial flow in cylindrical foam, radial flow in foam ring) and at typical conditions of filtration in flue gas cleaning (low gas velocity, low concentrations) and compared with data from a particle fixed bed as reference structure. Experiments at various temperatures (150-340 degrees C) and modified residence times (0.02-0.07 g s/cm(3)) in foams show no deviation from particles in the axial configuration. Conversion in the radial flow configuration, however, is significantly lower for both reactions. Given the low gas velocities due to a higher cross-sectional area and a shorter length of the catalyst in flow direction, backmixing is presumed to be the cause. For closer examination, experiments were performed to quantify the foam backmixing behaviour by measuring the residence time distribution (RTD). Combining the results, it was possible to establish mixed flow models in agreement with the data, thus suggesting backmixing to be the cause of decreasing conversion. The results of the kinetic study show no effect on the performance comparing fixed bed configurations of particles and foams. Ceramic foams appear well suited as structured catalyst inserts in gas-particle filters, given their low pressure drop and permeability in all flow directions. (C) 2009 Elsevier B.V. All rights reserved.