Sulfuryl fluoride (SO2F2) has been largely used as a postharvest fumigant replacing methyl bromide (widely recognized among ozone-depleting substances). Sulfuryl fluoride, however, is a potent greenhouse gas with a Global Warming Potential (GWP) of ~ 5000 for a 100-year time zone far higher than that of carbon dioxide and methane. Ongoing pilot work showed that SO2F2 fumes vented from fumigation chambers can be captured and hydrolyzed by hydroxide (OH-) and hydrogen peroxide (H2O2) solution at pH ~12 in a scrubber with a complete conversion into SO4 2- and F- as waste salts. The purchase, shipment, storage, and handling of concentrated stocks of H2O2 and NaOH for use in SO2F2 hydrolysis involve cost and safety concerns. Herein, we present an on-site, facile, and cost-effective pathway for the electrochemical production of OH- and H2O2 in large enough concentrations to fully degrade ~ 95% of SO2F2 captured. In that, we employed a commercial carbon catalyst that produced 250 mM H2O2 at pH 12.6 within 4 h with a Faradaic efficiency of 98.8% for O2 reduction to H2O2. We also propose a facile approach via surface oxidation of abundant carbon materials to significantly enhance both activity and selectivity for OH- and H2O2 production under electrochemical oxygen reduction reaction. These findings provide new insights in the on-site production of industrial chemicals by means of clean, facile, and environmentally friendly electrochemical pathway. Moreover, the capability of recycling the hazardous SO2F2 fumes and using the SO4 2- and F- waste products as free sources of electrolyte can’t be overemphasized.