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dc.contributor.authorWilliams, Kindle
dc.contributor.authorCorbin, Nathan
dc.contributor.authorZeng, Joy
dc.contributor.authorLazouski, Nikifar
dc.contributor.authorYang, Deng-Tao
dc.contributor.authorManthiram, Karthish
dc.date.accessioned2020-03-31T19:43:23Z
dc.date.available2020-03-31T19:43:23Z
dc.date.issued2019-03
dc.date.submitted2019-01
dc.identifier.issn2398-4902
dc.identifier.urihttps://hdl.handle.net/1721.1/124465
dc.description.abstractElectrochemical CO₂ reduction is a promising path toward mitigating carbon emissions while also monetizing waste gas through chemicals production and storage of surplus renewable energy. However, deploying such a technology for use on industrial CO₂ sources requires an understanding of the effects that gas feed impurities have upon CO₂ reduction reaction (CO₂RR). In this work, we elucidate the impact of molecular oxygen on the network of reactions occurring in a CO₂ reduction system. Our findings indicate that for a planar, polycrystalline Au electrode in an aqueous environment, oxygen reduction current is limited by the transport characteristics specific to the cell geometry and solvent; as a result, mass transport confers a protective effect by mitigating the otherwise thermodynamically and kinetically favorable reduction of oxygen. The presence of oxygen does not appear to have a significant impact on either CO₂RR or hydrogen evolution partial currents, indicating that the mechanisms of reduction reactions involving oxygen are independent of CO₂RR and hydrogen evolution. Further, an electrokinetic mechanistic analysis indicates many feasible candidates for the rate-determining step of CO₂RR; there is no indication that the CO₂RR mechanism at P[subscript CO₂] = 0.5 atm is altered by the presence of oxygen, as the Tafel slopes (59 mV dec⁻¹) and reaction orders with respect to bicarbonate (0), CO₂ (∼1.5), and protons (0 from lack of KIE) are consistent between systems with P[subscript O₂] = 0 atm and those with P[subscript O₂] = 0.5 atm. While this is promising for the robustness of CO₂RR to oxygen impurities in gas feeds, the ultimate design tradeoff when utilizing CO₂ sources containing oxygen is between the cost of separation processes and the corresponding cost of power inefficiency as a result of electrons lost to oxygen reduction. This represents a first step in understanding kinetic and transport considerations in the design of gas-impurity-tolerant CO₂ reduction systems.en_US
dc.publisherRoyal Society of Chemistry (RSC)en_US
dc.relation.isversionofhttp://dx.doi.org/10.1039/c9se00024ken_US
dc.rightsCreative Commons Attribution 3.0 unported licenseen_US
dc.rights.urihttps://creativecommons.org/licenses/by/3.0/en_US
dc.sourceRoyal Society of Chemistry (RSC)en_US
dc.titleProtecting effect of mass transport during electrochemical reduction of oxygenated carbon dioxide feedstocksen_US
dc.typeArticleen_US
dc.identifier.citationWilliams, Kindle et al. "Protecting effect of mass transport during electrochemical reduction of oxygenated carbon dioxide feedstocks." Sustainable Energy & Fuels 3, 5 (March 2019): 1225-1232 © 2019 Royal Society of Chemistryen_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Chemical Engineeringen_US
dc.relation.journalSustainable Energy & Fuelsen_US
dc.eprint.versionFinal published versionen_US
dc.type.urihttp://purl.org/eprint/type/JournalArticleen_US
eprint.statushttp://purl.org/eprint/status/PeerRevieweden_US
dspace.date.submission2019-04-24T14:15:44Z
mit.journal.volume3en_US
mit.journal.issue5en_US
mit.licensePUBLISHER_CC
mit.metadata.statusComplete


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