Integrating Electrocatalytic 5-Hydroxymethylfurfural Oxidation and Hydrogen Production via Co–P-Derived Electrocatalysts
Интеграция электрокаталитического окисления 5-гидроксиметилфурфурола и получения водорода с использованием электрокатализаторов на основе Co–P
2016-07-18
SCID: 54.1/yuckdres
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2,5-furandicarboxylic acid5-hydroxymethylfurfural oxidationCo–P electrocatalystsbiomass valorizationhydrogen production
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Abstract (AI)
Electrocatalytic biomass valorization with renewable energy input represents a promising way to produce sustainable and nonfossil-based carbon products. Even more desirable is that the oxidative biomass upgrading can be integrated with H 2 production in a single electrolyzer. Herein, we report that electrodeposited Co–P can act as competent electrocatalysts for 5-hydroxymethylfurfural (HMF) oxidation to 2,5-furandicarboxylic acid (FDCA) at the anode and H 2 production at the cathode simultaneously in alkaline media. When serving as a catalyst precursor on the anode, Co–P was able to achieve a current density of 20 mA/cm 2 for HMF oxidation in 1.0 M KOH with 50 mM HMF at 1.38 V vs RHE, prior to the takeoff of the competing reaction, O 2 evolution. Long-term chronoamperometry demonstrated a nearly 100% conversation of HMF and a ∼90% yield of FDCA. When HMF oxidation and H 2 evolution were integrated in one electrolyzer with a Co–P/Co–P catalyst couple, the potential required to achieve a current density of 20 mA/cm 2 was 1.44 V, 150 mV lower than that of overall water splitting. Nearly unity Faradaic efficiency was obtained for H 2 evolution. Overall, our results indicate that it is feasible to employ earth-abundant electrocatalyts to integrate H 2 production and oxidative biomass upgrading with higher energy conversion efficiency than water splitting as well as to produce valuable products at both cathode and anode in a single electrolyzer.
Key Findings
1
A Co–P/Co–P electrolyzer requires 1.44 V to deliver 20 mA/cm², 150 mV less than overall water splitting, while hydrogen evolution shows nearly 100% Faradaic efficiency.
2
Co–P-driven HMF oxidation reaches 20 mA/cm² at 1.38 V versus RHE in 1.0 M KOH containing 50 mM HMF, before competing oxygen evolution becomes dominant.
3
Electrodeposited Co–P functions as an earth-abundant electrocatalyst for simultaneous anodic HMF oxidation to FDCA and cathodic hydrogen production in alkaline media.
4
Integrating biomass upgrading with hydrogen production can improve energy conversion efficiency relative to water splitting and generate valuable products at both electrodes.
5
Long-term chronoamperometry achieves nearly 100% HMF conversion and approximately 90% FDCA yield.
Research Object
An alkaline electrolyzer using electrodeposited Co–P-derived electrocatalysts for simultaneous HMF oxidation and hydrogen production
Research Subject
Electrocatalytic performance, product conversion and energy efficiency of integrated HMF-to-FDCA oxidation at the anode coupled with H2 evolution at the cathode
Publication Details
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2016-07-18
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