dc.contributor.author | Williams, Kindle | |
dc.contributor.author | Corbin, Nathan | |
dc.contributor.author | Zeng, Joy | |
dc.contributor.author | Lazouski, Nikifar | |
dc.contributor.author | Yang, Deng-Tao | |
dc.contributor.author | Manthiram, Karthish | |
dc.date.accessioned | 2020-03-31T19:43:23Z | |
dc.date.available | 2020-03-31T19:43:23Z | |
dc.date.issued | 2019-03 | |
dc.date.submitted | 2019-01 | |
dc.identifier.issn | 2398-4902 | |
dc.identifier.uri | https://hdl.handle.net/1721.1/124465 | |
dc.description.abstract | Electrochemical 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.publisher | Royal Society of Chemistry (RSC) | en_US |
dc.relation.isversionof | http://dx.doi.org/10.1039/c9se00024k | en_US |
dc.rights | Creative Commons Attribution 3.0 unported license | en_US |
dc.rights.uri | https://creativecommons.org/licenses/by/3.0/ | en_US |
dc.source | Royal Society of Chemistry (RSC) | en_US |
dc.title | Protecting effect of mass transport during electrochemical reduction of oxygenated carbon dioxide feedstocks | en_US |
dc.type | Article | en_US |
dc.identifier.citation | Williams, 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 Chemistry | en_US |
dc.contributor.department | Massachusetts Institute of Technology. Department of Chemical Engineering | en_US |
dc.relation.journal | Sustainable Energy & Fuels | en_US |
dc.eprint.version | Final published version | en_US |
dc.type.uri | http://purl.org/eprint/type/JournalArticle | en_US |
eprint.status | http://purl.org/eprint/status/PeerReviewed | en_US |
dspace.date.submission | 2019-04-24T14:15:44Z | |
mit.journal.volume | 3 | en_US |
mit.journal.issue | 5 | en_US |
mit.license | PUBLISHER_CC | |
mit.metadata.status | Complete | |