Full Paper
Electrocatalytic Reduction of Acetone in a Proton-Exchange-Membrane Reactor: A Model Reaction for the Electrocatalytic Reduction of Biomass
Article first published online: 7 SEP 2012
DOI: 10.1002/cssc.201200416
Copyright © 2012 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim
Additional Information
How to Cite
Green, S. K., Tompsett, G. A., Kim, H. J., Kim, W. B. and Huber, G. W. (2012), Electrocatalytic Reduction of Acetone in a Proton-Exchange-Membrane Reactor: A Model Reaction for the Electrocatalytic Reduction of Biomass. ChemSusChem, 5: 2410–2420. doi: 10.1002/cssc.201200416
Publication History
- Issue published online: 3 DEC 2012
- Article first published online: 7 SEP 2012
- Manuscript Received: 18 JUN 2012
Funded by
- University of Massachusetts CVIP Technology Development Fund
- Abstract
- Article
- References
- Cited By
Keywords:
- biofuels;
- electrochemistry;
- energy conversion;
- fuel cells;
- heterogeneous catalysis
Abstract
Acetone was electrocatalytically reduced to isopropanol in a proton-exchange-membrane (PEM) reactor on an unsupported platinum cathode. Protons needed for the reduction were produced on the unsupported Pt
Ru anode from either hydrogen gas or electrolysis of water. The current efficiency (the ratio of current contributing to the desired chemical reaction to the overall current) and reaction rate for acetone conversion increased with increasing temperature or applied voltage for the electrocatalytic acetone/water system. The reaction rate and current efficiency went through a maximum with respect to acetone concentration. The reaction rate for acetone conversion increased with increasing temperature for the electrocatalytic acetone/hydrogen system. Increasing the applied voltage for the electrocatalytic acetone/hydrogen system decreased the current efficiency due to production of hydrogen gas. Results from this study demonstrate the commercial feasibility of using PEM reactors to electrocatalytically reduce biomass-derived oxygenates into renewable fuels and chemicals.

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