Hydrogen peroxide (H
2O
2) is a crucial chemical with a wide range of applications in civil and industrial fields. It is currently produced from the industrial energy- and waste-intensive anthraquinone process. Its centralized feature also makes it rely heavily on the storage and transportation of H
2O
2, which is unstable and hazardous. Electrocatalytic oxygen reduction reaction (ORR) to H
2O
2 provides an alternative to realize green and delocalized production, with the only inputs from renewable electricity, water and air. However, this route still faces two challenges: 1) lack of catalysts which selectively drive the 2e
- ORR towards H
2O
2 (instead of H
2O); 2) generated H
2O
2 are typically in mix with solutes in traditional electrolyzers, which necessitates complicated separation processes to recover pure H
2O
2 solutions for applications.
To make the electrochemical route more reliable in the future scaling-up, we reported a direct and continuous production of pure H2O2 solutions for the first time, through rational design of both catalyst and reactor. Here, we report a direct electrosynthesis strategy that delivers separate water (H2O) and oxygen (O2) streams to an anode and cathode separated by a porous solid electrolyte, wherein the electrochemically generated H+ and HO2â recombine to form pure aqueous H2O2 solutions with different concentrations. By optimizing a functionalized carbon black catalyst, we achieved over 90% selectivity for pure H2O2 at current densities up to 200 mA cm-2, which represents a H2O2 productivity of 3.4 millimoles per square centimeter per hour.
To further improve the activity and lower the overpotential at high current densities for industrial-level applications, we introduced boron-doped carbon catalyst which can achieve better activity under industrial-relevant current densities (saving over 200 mV overpotential at up to 300 mA cm-2) compared to the state-of-the-art oxidize carbon catalyst while maintaining a high selectivity (up to 90%). By incorporating the boron-doped carbon catalyst into our solid electrolyte cell setup, we achieved high partial H2O2 current densities (400 mA cm-2) with high selectivities (up to 95%), which represents a H2O2 productivity of 7.36 millimoles per square centimeter per hour. The setup can also undergo 200-hour stability test without degradation, making it a good candidate to be further improved in the aspect of potential scaling-up for electrochemical H2O2 production in industrial level with long-lasting performance.