A series of supported Rh/γ-Al 2 O 3 catalysts with an overall metal loading of 0.005 wt % was synthesized by impregnation of γ-Al 2 O 3 with a toluene solution containing colloidally prepared well-defined (1.1, 2.5, 2.9, 3.7, and 5.5 nm) Rh nanoparticles (NP). The size of NP was not found to change after their deposition on γ-Al 2 O 3 and even after performing partial oxidation of methane (POM) to synthesis gas at 1073 K for 160 h on stream. Apparent CO formation turnover rates and CO selectivity strongly decrease with an increase in this size. Contrarily, the overall scheme of POM is size-independent, i.e. CO and H 2 are mainly formed through reforming reactions of CH 4 with CO 2 and H 2 O at least under conditions of complete oxygen conversion. The size effect on the activity and selectivity was related to the kinetics of interaction of CH 4 , O 2 , and CO 2 with Rh/γ-Al 2 O 3 as concluded from our microkinetic analysis of corresponding transient experiments in the temporal analysis of products reactor. The rate constants of CH 4 , O 2 , and CO 2 activation decrease with an increase in the size of supported Rh NP thus influencing both primary (methane combustion) and secondary (reforming of methane) pathways within the course of POM.