In this investigation, the co-production of barium (Ba) and syngas via a solar-assisted methanothermal reduction of BaO was thermodynamically scrutinized. The equilibrium, as well as efficiency analysis, was conducted by considering two process flow configurations: (a) Ba-Syn open process and (b) Ba-Syn semi-open process. The production of Ba and syngas via complete conversion of BaO and CH 4 (no traces of carbon) was thermodynamically feasible at 2250 K. It was also recorded that the rise in the CH 4 /BaO ratio improved that production of Ba and syngas. The solar energy required to drive the cycles and the energy released during quenching were increased by 973.3 kW and 224.4 kW, respectively, when the CH 4 /BaO ratio was amplified from 0.1 to 1. The solar-to-fuel energy conversion efficiency was also augmented by 18.9% as the syngas production was enhanced. The efficiency analysis further indicates that, after applying heat recuperation of 50%, the Ba-Syn open process and Ba-Syn semi-open process can attain the maximum possible solar-to-fuel energy conversion efficiency equal to 42.8% and 49.7%, respectively.