Tandem Electro- and Thermo-Catalytic Continuous Reactor for Hydrogen Peroxide-Mediated Cyclohexene Epoxidation

电解 催化作用 电化学 化学 过电位 环己烯 电解水 电解质 选择性 氢 制氢 环氧化物 化学工程 氧化还原 材料科学 过氧化氢 烯烃纤维 化学工业 电子转移 无机化学 石墨烯 级联反应 碳纳米管 电催化剂 组合化学 灵活性(工程) 纳米技术 串联
作者
Mark Kazour,Justin Dong,Justin Notestein,Linsey Christine Seitz
出处
期刊:Meeting abstracts [Institute of Physics]
卷期号:MA2025-02 (25): 1414-1414
标识
DOI:10.1149/ma2025-02251414mtgabs
摘要

Electrocatalysis offers a sustainable and safe alternative to fossil fuel-based chemical production by converting carbon feedstocks into value-added chemicals using renewable electricity. One promising target is the production of epoxides. Epoxides are key chemical intermediates to produce epoxies, pharmaceuticals, and textiles, yet electrochemical approaches to their synthesis remain limited by poor selectivity and low activity. Direct electrooxidation, in which electrons transfer from the electrode directly to the organic substrate, suffers from high overpotential and numerous by-products. As an alternative, indirect electrooxidation via redox mediators such as hydrogen peroxide can enhance selectivity and activity towards the desired epoxide product, while maintaining industrially relevant current densities. In this approach, the electrochemically generated mediator subsequently reacts thermocatalytically to form the epoxide. Integrating electrocatalytic and thermocatalytic processes offers an industrially relevant path to improve performance, while mitigating safety and environmental risks. Herein, we present a hydrogen-peroxide-mediated cyclohexene epoxidation system that integrates a dual-membrane electrode assembly (MEA) solid-electrolyte electrolyzer with a downstream thermocatalytic flow reactor. The indirect electrooxidation strategy first produces hydrogen peroxide, which oxidizes cyclohexene downstream in a biphasic, thermocatalytic reactor. We evaluate the resiliency of the MEA towards continuous recycle operation, evaluating the impact of temperature modification, Na 2 WO 4 catalyst addition, and solid electrolyte variability. This work highlights the operational flexibility of tandem electro- and thermo-catalytic reactor designs, especially for future integration into existing industrial thermochemical processes. Insight from this work supports the development of indirect electrooxidation platforms for scalable and flexible industrial applications. Figure 1

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