We are exploring the use of MFCs for the production of hydrogen peroxide (H2O2). H2O2 is a powerful oxidant and disinfectant that can be used onsite at a treatment plant. Its production in MFCs is possible by allowing the 2-e- oxygen reduction reaction (ORR) to occur at the cathode. We have studied several aspects of the selection of cathode catalyst, design of the MFCs, and their operation, to optimize the rates and concentrations of H2O2 that can be achieved in a continuous-flow catholyte scheme.
First, we determined the thickness of the Vulcan carbon catalyst necessary for the cathode to promote the 2-e- vs. the 4-e- ORR, as higher thicknesses tend to lead to the consumption of H2O2 within the catalyst layer. Next, we studied various anion exchange membranes (AEMs) for their compatibility with H2O2. Although high-conductivity AEMs are desirable to decrease Ohmic overpotentials, we had to select an AEM that has a relatively low conductivity, because of its higher compatibility with H2O2 that would allow long-term operation. We also optimized the catholyte composition and hydraulic retention time (HRT) within the MFCs to allow for H2O2 production at a high cathodic Coulombic efficiency, by avoiding its disintegration within the cathode chamber.
Through these advances, we have been able to show consistent H2O2 production in MFCs fed with acetate as the electron donor on the anode to concentrations of >0.3%. These concentrations are significantly higher than those needed for many of the possible onsite applications of H2O2, for e.g. disinfection. Our results should pave the way for further development and scale-up of MFCs for the production of H2O2.