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dc.contributor.authorGani, Terry Zhi Hao
dc.contributor.authorKulik, Heather Janine
dc.date.accessioned2019-11-12T18:38:26Z
dc.date.available2019-11-12T18:38:26Z
dc.date.issued2017-12-08
dc.date.submitted2017-10-22
dc.identifier.issn2155-5435
dc.identifier.urihttps://hdl.handle.net/1721.1/122918
dc.description.abstractComputational high-throughput screening is an essential tool for catalyst design, limited primarily by the efficiency with which accurate predictions can be made. In bulk heterogeneous catalysis, linear free energy relationships (LFERs) have been extensively developed to relate elementary step activation energies, and thus overall catalytic activity, back to the adsorption energies of key intermediates, dramatically reducing the computational cost of screening. The applicability of these LFERs to single-site catalysts remains unclear, owing to the directional, covalent metal-ligand bonds and the broader chemical space of accessible ligand scaffolds. Through a computational screen of nearly 500 model Fe(II) complexes for CH[subscript 4] hydroxylation, we observe that (1) tuning ligand field strength yields LFERs by comparably shifting energetics of the metal 3d levels that govern the stability of different intermediates and (2) distortion of the metal coordination geometry breaks these LFERs by increasing the splitting between the d[subscript xz]/d[subscript yz] and d[subscript z][superscript 2] metal states that govern reactivity. Thus, in single-site catalysts, low Brønsted-Evans-Polanyi slopes for oxo formation, which would limit peak turnover frequency achievable through ligand field tuning alone, can be overcome through structural distortions achievable in experimentally characterized compounds. Observations from this screen also motivate the placement of strong HB donors in targeted positions as a scaffold-agnostic strategy for further activity improvement. More generally, our findings motivate broader variation of coordination geometries in reactivity studies with single-site catalysts. Keywords: density functional theory; single-site catalysis; high-throughput screening; catalyst design; minimal models; linear scaling relations; methane activation; iron-oxoen_US
dc.description.sponsorshipUnited States. Office of Naval Research (Grant N0001-17-1-2956)en_US
dc.description.sponsorshipNational Science Foundation (U.S.) (Grant CBET-1704266)en_US
dc.description.sponsorshipMIT Energy Initiativeen_US
dc.language.isoen
dc.publisherAmerican Chemical Societyen_US
dc.relation.isversionofhttp://dx.doi.org/10.1021/acscatal.7b03597en_US
dc.rightsArticle is made available in accordance with the publisher's policy and may be subject to US copyright law. Please refer to the publisher's site for terms of use.en_US
dc.sourceOther repositoryen_US
dc.titleUnderstanding and Breaking Scaling Relations in Single-Site Catalysis: Methane to Methanol Conversion by Fe(IV)=Oen_US
dc.title.alternativeUnderstanding and Breaking Scaling Relations in Single-Site Catalysis: Methane to Methanol Conversion by Fe[superscript IV]=Oen_US
dc.typeArticleen_US
dc.identifier.citationGani, Terry Z. H. and Heather J. Kulik. "Understanding and Breaking Scaling Relations in Single-Site Catalysis: Methane to Methanol Conversion by Fe(IV)=O.” ACS Catalysis 8, 2 (2018): 975-986 © 2017 Publisheren_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Chemical Engineeringen_US
dc.relation.journalACS Catalysisen_US
dc.eprint.versionOriginal manuscripten_US
dc.type.urihttp://purl.org/eprint/type/JournalArticleen_US
eprint.statushttp://purl.org/eprint/status/NonPeerRevieweden_US
dc.date.updated2019-08-22T15:47:04Z
dspace.date.submission2019-08-22T15:47:05Z
mit.journal.volume8en_US
mit.journal.issue2en_US


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