Ni-Co bimetallic and Ni or Co monometallic catalysts prepared for CO 2 reforming of methane were tested with the stimulated biogas containing steam, CO 2 , CH 4 , H 2 , and CO. A mix of the prepared CO 2 reforming catalyst and a commercial steam reforming catalyst was used in hopes of maximizing the CO 2 conversion. Both CO 2 reforming and steam reforming of CH 4 occurred over the prepared Ni-Co bimetallic and Ni or Co monometallic catalysts when the feed contained steam. However, CO 2 reforming did not occur on the commercial steam reforming catalyst. There was a critical steam content limit above which the catalyst facilitated no more CO 2 conversion but net CO 2 production for steam reforming and water-gas shift became the dominant reactions in the system. The Ni-Co bimetallic catalyst can convert more than 70% of CO 2 in a biogas feed that contains~33 mol% of CH 4 , 21.5 mol% of CO 2 , 12 mol% of H 2 O, 3.5 mol% of H 2 , and 30 mol% of N 2. The H 2 /CO ratio of the produced syngas was in the range of 1.8-2. X-ray absorption spectroscopy of the spent catalysts revealed that the metallic sites of Ni-Co bimetallic, Ni and Co monometallic catalysts after the steam reforming of methane reaction with equimolar feed (CH 4 :H 2 O:N 2 = 1:1:1) experienced severe oxidation, which led to the catalytic deactivation.