Electroosmotic flow steers neutral products and enables concentrated ethanol electroproduction from CO2

dc.contributor.authorMiao, Rui Kai
dc.contributor.authorXu, Yi
dc.contributor.authorOzden, Adnan
dc.contributor.authorRobb, Anthony
dc.contributor.authorO’Brien, Colin P.
dc.contributor.authorGabardo, Christine M.
dc.contributor.authorLee, Geonhui
dc.contributor.authorEdwards, Jonathan P.
dc.contributor.authorHuang, Jianan Erick
dc.contributor.authorFan, Mengyang
dc.contributor.authorWang, Xue
dc.contributor.authorLiu, Shijie
dc.contributor.authorYan, Yu
dc.contributor.authorSargent, Edward H.
dc.contributor.authorSinton, David
dc.date.accessioned2021-11-29T18:50:48Z
dc.date.available2021-11-29T18:50:48Z
dc.date.issued2021-10-20
dc.description.abstractElectrochemical reduction of carbon dioxide (CO2RR) converts intermittent renewable energy into high energy density fuels, such as ethanol. Membrane electrode assembly (MEA) electrolyzers are particularly well-suited to CO2-to-ethanol conversion in view of their low ohmic resistance and high stability. However, over 75% of the ethanol produced at the cathode migrates through the membrane where it is diluted by the anolyte and may be oxidized. The ethanol concentration that results is two orders of magnitude below the 10 wt% standard set by the incumbent industrial process, fermentation. Here, we reverse the direction of ion and electroosmotic transport by means of a porous proton exchange layer, and thereby block both the convective and diffusive routes of ethanol loss. With this strategy, we eliminate ethanol crossover to the anode (< 1%), and achieve an ethanol concentration of 13.1 wt% directly from the cathode outlet.en_US
dc.description.sponsorshipThe authors acknowledge support and infrastructure from the Natural Sciences and Engineering Research Council (NSERC), the Government of Ontario through the Ontario Research Fund. This work is supported by Suncor Energy Ltd and the NSERC Alliance grant program. R.K.M. thanks NSERC, Hatch, and the Government of Ontario for their support through graduate scholarships. Y.X. thanks NSERC for support in the form of a graduate scholarship. Infrastructure provided by the Canada Foundation for Innovation (CFI) and the Ontario Research Fund (ORF) is gratefully acknowledged.en_US
dc.identifier.citationMiao, R.K., Xu, Y., Ozden, A., Robb, A., O’Brien, C.P., Gabardo, C.M., Lee, G., Edwards, J.P., Huang, J.E., Fan, M., Wang, X., Liu, S., Yan, Y., Sargent, E.H., Sinton, D. (2021). Electroosmotic flow steers neutral products and enables concentrated ethanol electroproduction from CO2. Joule 5, 2742–2753. https://doi.org/10.1016/j.joule.2021.08.013en_US
dc.identifier.doi10.1016/j.joule.2021.08.013en_US
dc.identifier.issn25424351en_US
dc.identifier.urihttp://hdl.handle.net/1807/108505
dc.language.isoen_caen_US
dc.publication.journalJouleen_US
dc.publisherElsevieren_US
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 International*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.subjectCO2 electroreductionen_US
dc.subjectcarbon utilizationen_US
dc.subjectcatalysisen_US
dc.subjectelectrolyzeren_US
dc.subjectethanolen_US
dc.subjectdownstream separationen_US
dc.subjectliquid crossoveren_US
dc.subjectpolymer electrolyteen_US
dc.subjectmembrane electrode assemblyen_US
dc.titleElectroosmotic flow steers neutral products and enables concentrated ethanol electroproduction from CO2en_US
dc.typeArticle Post-Printen_US

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