A conceptually similar approach to dry reforming of CH 4 (DRM) called Catalytic Decomposition of Biogas (CDB) is proposed. CDB is based on the direct decomposition of CH 4 and CO 2 , which are the most abundant components in biogas (typically with CH 4 :CO 2 molar ratios higher than 1). The main difference between DRM and CDB lies in the desired products obtained in each process. While in DRM carbon formation is not desired and thus avoided, in CDB carbon accumulation in form of filamentous structures is promoted. In this work, the effect of CH 4 and CO 2 partial pressures on the initial reaction rates of CDB was studied using a Ni/Al 2 O 3 catalyst. Furthermore, a deactivation study was carried out in order to determine the experimental conditions (CH 4 and CO 2 partial pressures and temperature) at which carbon formation did not deactivate the catalyst. It was proved that after a certain time on stream, CDB can reach the steady state even though the CH 4 :CO 2 molar ratio is higher than one (typical biogas conditions). In addition, temperature increased reaction rates since CDB is an endothermic process, but it had no effect on catalyst deactivation.