CO 2 electroreduction to value-added products has promise as a scalable technique for mitigating climate change, but CO 2 purification requirements raise the overall process cost. Direct reduction of flue gas is thus an attractive approach, but the sensitivity of the catalyst activity to flue gas contaminants and increased hydrogen evolution with diluted CO 2 have been major challenges. Herein, flue gas electroreduction in a methyl formate synthesis route has been investigated on a Pb-catalyzed electrode in acidic methanol catholyte with an aqueous anolyte for promotion of a sustainable water oxidation half-reaction. Contaminant concentrations of 50 ppm SO 2 and NO each had a minimal effect on the product faradaic efficiencies, whereas 4% O 2 led to a notable improvement in partial current density for methyl formate attributed to the improved durability of the catalyst surface oxide. Decreased CO 2 concentration showed a corresponding decline in current density attributed to CO 2 mass transfer limitations. • Study of the effects of flue gas contaminants and CO 2 concentration • Pb-catalyzed methyl formate production from CO 2 and methanol • High-performance tolerance to SO 2 and NO impurities • Improved performance with dilute O 2 Increasing atmospheric CO 2 is contributing to anthropogenic climate change. Industrial utilization of CO 2 can add economic value to this waste product and provide a route to decreased greenhouse gas emissions. Direct electroreduction of post-combustion flue gas would bypass expensive and energy-intensive carbon capture technologies and improve the overall economics of the process. However, the contaminants in flue gas and the lower partial pressure of CO 2 can deleteriously affect the electrolyzer performance. Herein, the influence of flue gas components and combined simulated flue gas feedstock on the electrochemical reduction of CO 2 in a methyl formate synthesis route has been investigated on a Pb-catalyzed cathode in acidic methanol in conjunction with water at the anode for a sustainable reaction. The results show promise for a viable route to produce a chemical not reported in aqueous CO 2 electroreduction directly from the output of a fossil fuel utility or similar industrial process. The feasibility of electrochemical reduction of waste carbon dioxide from industrial flue gas was investigated in an uncommon methanol/water dual electrolyte approach targeting a methyl formate product. The work demonstrates a pathway to produce a chemical not formed in aqueous CO 2 reduction that is largely compatible with direct operation from flue gas.