Cu/Al 2 O 3 catalysts with metal loading from 0.64 to 8.8 wt. % have been prepared and characterised by different techniques: N 2 adsorption at -196ºC (BET surface area), ICP (Cu loading), XRD, selective copper surface oxidation with N 2 O (Cu dispersion), TPR-H 2 (redox properties), and XPS (copper surface species). The catalytic activity for soot oxidation has been tested both in air and NOx/O 2 . The activity in air depends on the amount of easily-reduced Cu(II) species, which are reduced around 275ºC under TPR-H 2 conditions. The amount of the most active Cu(II) species increases with the copper loading from Cu_1% to Cu_5% and remains almost constant for higher copper loading.In the presence of NOx, the first step of the mechanism is NO oxidation to NO 2 , and the catalytic activity for this reaction depends on the copper loading. For catalysts with copper loading between Cu_1% and Cu_5%, the catalytic activity for soot oxidation in the presence of NOx depends on NO 2 formation. For catalysts with higher copper loading this trend is not followed because of the low reactivity of model soot at the temperature of maximum NO 2 production. Regardless the copper loading, all the catalysts improve the selectivity towards CO 2 formation as soot oxidation product both under air and NOx/O 2 .