A method of high performance dry reforming of methane into syngas at temperatures below 650 °C on membrane catalytic systems was proposed. The membrane catalytic systems consist of porous inorganic membrane supports, prepared by self propagating high tempera ture synthesis and modified by nanosized metallocomplex components, which are uniformly distributed inside membrane pores. The influence of the composition of the supported active components, temperature, and flow rate on the activity and selectivity of СН 4 and СО 2 trans formations into syngas, as well as the dynamics of СН 4 and СО 2 conversion on the membrane catalytic systems were studied.