The emission of low-concentration coal mine methane (LCM) resulted in serious greenhouse effect. In order to utilize the LCM efficiently, a heat-recirculating porous reactor was built to realize the catalytic partial oxidation of the methane and air mixture. The effects of composite double-perovskite catalysts on the reaction temperature and gas production were investigated at different operating parameters. The results demonstrated that the B-site of Mn obviously enhanced the low-temperature catalytic activity of Co-based double-perovskite, which improved the methane reaction rate and hydrogen yield. The highest H2 yield (YH2 = 50.3 %) was obtained by La2CoMnO6 (D-CoMn). And the A-site partial doping of Ce promoted the production of syngas (ηe−s = 50.2 %). The addition of 25 % CeO2 enhanced the methane reaction rate and syngas production efficiency of D-CoMn. However, excessive CeO2 inhibited the generation of syngas. Meanwhile, the anti-supported catalyst CoMn/25Ce-S, synthesized by the sol-gel impregnation, performed good crystal morphology and the largest concentration of oxygen vacancies ((OIII+OII)/OI = 0.9). This enhanced the partial oxidation of methane and lowered the reaction temperature. The maximum H2 selectivity (SH2 = 44.2 %) and CH4 conversion efficiency (ηCH4 = 92.7 %) were attained at T4=998 K. Moreover, the increased flow velocity and equivalency ratio led to enhanced syngas production.
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