Water-involved methane-selective catalytic oxidation by dioxygen over copper zeolites

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چکیده

•Water-involved methane-selective oxidation by dioxygen over Cu–CHA zeolite catalyst•Methanol space-time yield of 543 mmol/molCu/h achieved at methanol selectivity 91%•Both monomeric and dimeric Cu species can catalyze the methane-to-methanol conversion•Various undergo interconversion under employed reaction conditions Methane is an abundant fossil resource widely distributed throughout earth, direct functionalization methane a challenging topic in chemistry catalysis. Inspired natural monooxygenase that dioxygen, first-row transition-metal cations stabilized matrix have been developed for dream transformation. However, suffers from extremely low efficiency its mechanism hotly debated. Here, we report water-involved catalytic copper zeolites. A state-of-the-art 91%. The fast redox cycle Cu2+–Cu+–Cu2+ during identified related to high activity Cu–CHA. Both conversion with CuOOH as key intermediate. selective functionalization, which remains challenge catalysis hot controversy. Herein, At 573 K, 91% catalyst. Temperature-programmed surface reactions isotope labeling suggest water apparent oxygen hydrogen source hydroxyl methanol. Spectroscopic analyses reveal Cu2+-Cu+-Cu2+ oxidation, closely Density functional theory calculations both CuOH monomer dimer Cu–OOH intermediate, meanwhile, various sites may conditions. Methane, main component gas, earth.1McFarland E. Chemistry. Unconventional unconventional gas.Science. 2012; 338: 340-342Crossref PubMed Scopus (160) Google Scholar In energy-intensive industrial processes, first converted syngas via reforming or partial oxidation2Sun L. Wang Y. Guan N. Li activation utilization: current status future challenges.Energy Technol. 2020; 8: 1900628Crossref (21) then transformed fuel chemicals. By contrast, appears be more intriguing; however, it greatly challenged large C–H bond dissociation energy 435 kJ/mol. Several strategies, example, oxidative nonoxidative coupling3Keller G.E. Bhasin M.M. Synthesis ethylene coupling I. Determination active catalysts.J. Catal. 1982; 73: 9-19Crossref (1103) Scholar, 4Ito T. Lunsford J.H. ethane lithium-doped magnesium oxide.Nature. 1985; 314: 721-722Crossref (538) 5Guo X. Fang G. Ma H. Fan Yu C. Wu Deng D. Wei M. et al.Direct, ethylene, aromatics, hydrogen.Science. 2014; 344: 616-619Crossref (753) dehydroaromatization,6Spivey J.J. Hutchings Catalytic aromatization methane.Chem. Soc. Rev. 43: 792-803Crossref Scholar,7Gao J. Zheng Jehng J.M. Tang Wachs I.E. Podkolzin S.G. Catalysis. Identification molybdenum oxide nanostructures on zeolites gas conversion.Science. 2015; 348: 686-690Crossref (213) transformation chemicals.8Horn R. Schlögl heterogeneous catalysis.Catal. Lett. 145: 23-39Crossref triggers persistent interests because this type thermodynamically favorable relatively mild (MTM) has accomplished molecular Periana catalyst9Periana R.A. Taube D.J. Gamble S. Satoh Fujii Platinum catalysts high-yield derivative.Science. 1998; 280: 560-564Crossref (1039) solid analog10Palkovits Antonietti Kuhn P. Thomas A. Schüth F. Solid low-temperature methanol.Angew. Chem. Int. Ed. Engl. 2009; 48: 6909-6912Crossref (415) strong acidic media multistep oxyfunctionalization, unfortunately economic environmental concerns. (MMO) ambient conditions,11Sirajuddin Rosenzweig A.C. Enzymatic methane.Biochemistry. 54: 2283-2294Crossref (179) matrix, iron zeolites12Parfenov M.V. Starokon E.V. Pirutko L.V. Panov G.I. Quasicatalytic nitrous FeZSM-5 zeolite.J. 318: 14-21Crossref (89) Scholar,13Snyder B.E.R. Vanelderen Bols M.L. Hallaert S.D. Böttger L.H. Ungur Pierloot K. Schoonheydt Sels B.F. Solomon E.I. site hydroxylation iron-containing zeolites.Nature. 2016; 536: 317-321Crossref (191) zeolites,14Groothaert M.H. Smeets P.J. Jacobs P.A. Selective bis(?-oxo)dicopper core ZSM-5 mordenite zeolites.J. Am. 2005; 127: 1394-1395Crossref (446) 15Alayon E.M. Nachtegaal Ranocchiari van Bokhoven J.A. Cu-mordenite.Chem. Commun. 404-406Crossref 16Wulfers M.J. Teketel Ipek B. Lobo R.F. Conversion copper-containing small-pore zeotypes.Chem. 51: 4447-4450Crossref 17Grundner Markovits M.A. Tromp Pidko E.A. Hensen E.J. Jentys Sanchez-Sanchez Lercher Single-site trinuclear clusters methanol.Nat. 6: 7546Crossref (399) 18Sushkevich V.L. Palagin anaerobic enables synthesis methanol.Science. 2017; 356: 523-527Crossref (354) 19Sushkevich effect active-site structure aerobic into 2018; 57: 8906-8910Crossref (82) 20Pappas D.K. Borfecchia Dyballa Pankin I.A. Lomachenko K.A. Martini Signorile Arstad Berlier al.Methane methanol: structure-activity relationships Cu-CHA.J. 139: 14961-14975Crossref (173) 21Pappas Kvande Baran Glatzel al.The nuclearity Cu-mordenite: quantitative assessment.J. 140: 15270-15278Crossref (105) 22Ipek Cu-SSZ-13 using N2O oxidant.Chem. 52: 13401-13404Crossref 23Narsimhan Iyoki Dinh Román-Leshkov copper-exchanged temperature.ACS Cent. Sci. 2: 424-429Crossref (227) 24Dinh K.T. Sullivan Narsimhan Serna Meyer R.J. Dinc? Continuous catalyzed diffusion-paired dimers 2019; 141: 11641-11650Crossref (69) metal-organic frameworks25Ikuno Vjunov Ortuño Pahls D.R. Fulton J.L. Camaioni D.M. Z. Ray Cu-oxo NU-1000 metal–organic framework.J. 10294-10301Crossref (186) Scholar,26Baek Rungtaweevoranit Pei Park Fakra S.C. Liu Y.S. Matheu Alshmimri S.A. Alshehri Trickett C.A. al.Bioinspired framework methanol.J. 18208-18216Crossref (129) candidate materials MTM stepwise strategy consisting (1) sample temperature, (2) introduction (3) product extraction steam, commonly employed, tactfully blocks co-existence accordingly hinders over-oxidation methanol.16Wulfers chemical-looping process maximum productivity self-limited one complete (typically dozen hours). To establish promising transformation, continuous desired27Dinh Viewpoint Cu- Fe-exchanged zeolites.ACS 8306-8313Crossref (75) several requirements should satisfied, namely: use inexpensive oxidants like methanol, sustainable rate, (4) good catalyst stability operation. production presence dioxygen. With elaborate optimization conditions, (STY) simultaneously achieved, makes important step forward methane. clear picture depicted combination spectroscopic theoretical calculations, clarifies misunderstandings will stimulate further development reaction. Copper were prepared wet ion exchange (see Supplemental experimental procedures, Figures S1–S6; Table S1) applied different temperature was raised 473 523–723 K promote while concentration regulated (from impurities extra dioxygen) minimize byproduct carbon dioxide production. (Si/Al = 11.4; Cu/Al 0.23), significant contrast other zeolites, such Cu-MOR Cu-MFI, exhibited remarkable (Figures S7–S21). performance controlled multiple factors, including but not limited concentration, space velocity. Experimentally, STY 542 (195 ?mol/gcat/h) 91 % 2% 400 ppm (Figure 1A). This value order magnitude higher than those mentioned previous reports similar processes (Table S2). crucial trigger (vide infra) dioxygen/methane ratio (<1/2,000) maintaining toward desired time-on-stream behaviors investigated, amazingly stable 500-h operation 1B). Besides, very reproducibility errors <5% repeated tests. These data clearly demonstrate potential one-step oxidation. Since reaction, aqueous solution mass fraction 1.2% could obtained S22) valuable utilization. For insight pathway MTM, temperature-programmed (TPSR) performed. TPSR mode, started ?523 generating S23; detected dominating Cu-MFI; S24 S25). Dihydrogen also outlet amount lower lagged slightly behind absence water, dominant trace above 673 when produced total S26), indicating role MTM. 13CH4 isotopically labeled reagent, definitively confirmed S27). Deuterium experiments (D2O reagent Figure 2A CD4 2B) indicated predominantly came whereas dihydrogen apparently abstracted dissociated water. Subsequently, 18O-labeling performed oxidant H218O 2C), CH318OH observed together CH3OH due non-labeled system. It seems acted conversion. CO2 ruled out C18O2 CO18O come (major route, Equation 1) (minor S28; 2), respectively. Meanwhile, consumption >573 confirming participation 18O2 2D), mainly formation demonstrating reaction.CH3OH+H2O?CO2+3H2(Equation 2CH3OH+3O2?2CO2+4H2O(Equation 2) According results, participate Provided oxidized stoichiometric 1 (Equation 3). far below dependent system 3A), i.e., nH2/nCH3OH increased increasing 50 550 (high >85% all cases). Considering secondary 1), contribution deducted give intrinsic amazing only along formation, (nH2-nCO2?3)/nCH3OH < 0.1, concentrations 50–550 ppm. That is, instead agreement S23). Now, present (shown [O] simplicity), shown 4. From element balance point view, [O], essential initiate becomes methanol.CH4+H2O?CH3OH+H2(Equation 3) CH4+H2O+[O]?CH3OH+H2O(Equation 4) Cu-zeolites debated.14Groothaert Scholar,16Wulfers Scholar,28Woertink J.S. Groothaert Vance [Cu2O]2+ Cu-ZSM-5, methanol.Proc. Natl. Acad. USA. 106: 18908-18913Crossref (429) 29Vanelderen Snyder B.E. Tsai Hadt R.G. Vancauwenbergh Coussens O. definition mordenite: oxidation.J. 137: 6383-6392Crossref (161) 30Kulkarni A.R. Zhao Z.-J. Siahrostami Nørskov J.K. Studt Monocopper Cu-exchanged 8MR 6531-6536Crossref (118) 31Mahyuddin Staykov Shiota Miyanishi Yoshizawa Roles confinement Cu–O–Cu angle [Cu2(?-O)]2+-exchanged AEI, CHA, AFX, MFI 7: 3741-3751Crossref (85) 32Ipek Wulfers Kim Göltl Hermans Smith J.P. Booksh K.S. Brown C.M. Formation [Cu2O2]2+ Cu-SSZ-39.ACS 4291-4303Crossref (127) topology composition hosts show impacts cooper sites, dynamic changes conditions.33Alayon E.M.C. Bodi Reaction affect sites.ACS 4: 16-22Crossref (122) 34Paolucci Parekh A.A. Khurana Di Iorio J.R. Albarracin Caballero J.D. Shih A.J. Anggara Delgass W.N. Miller J.T. al.Catalysis cage: condition-dependent speciation dynamics exchanged SSZ-13 138: 6028-6048Crossref (356) 35Paolucci Albarracin-Caballero Yezerets al.Dynamic multinuclear formed mobilized ions NOx reduction.Science. 357: 898-903Crossref (397) CHA reaction-relevant investigated ultraviolet-visible-near-infrared (UV-vis-NIR) spectroscopy. spectrum (473 He; S29) showed d-d transitions Cu2+ (3d9) ?12,000 cm?1 ligand-to-metal charge transfer (LMCT) isolated (O2?Cu2+?O-Cu+) 50,000–40,000 cm?1.36Korhonen S.T. Fickel D.W. Weckhuysen B.M. Beale A.M. Isolated ions: reduction NO.Chem. 2011; 47: 800-802Crossref 37Giordanino Vennestrøm P.N.R. Lundegaard L.F. Stappen F.N. Mossin Beato Bordiga Lamberti Characterization SSZ-13: comparative FTIR, UV-vis, EPR study Cu-ZSM-5 Cu-? Si/Al ratios.Dalton Trans. 2013; 42: 12741-12761Crossref 38Oord Schmidt J.E. Methane-to-methanol Cu-SSZ-13, comparison NH3.Catal. 1028-1038Crossref treated atmospheres temperatures ranging 773 S30). Treatment resulted slight increase intensity band 12,000 noticeable shifts 40,000–30,000 cm?1, probably reconstruction creation small quantity species. declines intensities bands Cu+ highly overlapped their interpretation might misleading, decline revealed Cu+, since no occur fully occupied d shell.37Giordanino Interestingly, readily back H2O–O2 S31). involved CH4–H2O–O2. We focused constant temperature. coordination geometry influence extinction coefficients change transitions,39Negri Porcaro N.G. Janssens T.V.W. Dynamic CuII/CuI Cu-CHA situ diffuse reflectance UV-vis-NIR spectroscopy.Appl. 578: 1-9Crossref (27) 40Negri Selleri Cutini Structure reactivity oxygen-bridged diamino dicopper(II) complexes Cu-ion-exchanged chabazite NH3-mediated reduction.J. 142: 15884-15896Crossref (31) 41Li Paolucci Wilcox L.N. Ribeiro F.H. Gounder Schneider W.F. Consequences exchange-site heterogeneity UV-visible SSZ-13.Chem. 10: 2373-2384Crossref cautious assessing Cu2+-Cu+ abundance based regions. existed hydrated partially form (as OH-stretching modes NIR region) transition region stable, qualitatively indicate 4). 523 (CH4–H2O–O2) (those parent auto-reduction helium) Cu2+, quite H2O CH4–H2O. 623 between demonstrated. Typically, quickly (partially) reduced simply On hand, re-oxidation Cu2+. these exist CH4–H2O–O2 473–623 573–623 reason much literature reports.23Narsimhan Scholar,24Dinh information FTIR As 5A, IR 3,730, 3,655, 3,605, 3,580 flowing helium, Si-OH, Cu(II)-OH, two types Si-OH-Al species, respectively.34Paolucci Scholar,42Borfecchia Svelle Olsbye U. – model catalysis.Chem. 8097-8133Crossref Si-OH regarded reference 5B). Feeding quick appearance 2,155 carbonyl group Cu+,43Hadjiivanov K.I. Vayssilov G.N. surfaces monoxide probe molecule.Adv. 2002; 307-511Google titrate centers. decreased gradually (CH4–H2O) disappeared (CH4–H2O–O2). Removal O2 stream reappearance results agree well spectroscopy Brønsted acid six-membered rings (3,580 cm?1) upon activation, following possible 5 (Z: Zeolite Si-O-Al site). confirm hypothesis, fed deuterated 2,640 S32). (CH4–H2O), Cu(II)-OH (3,655 synchronously hydrolysis bare 6).Z2?Cu2++CH4?Z?[Cu?CH3]++Z?H+(Equation 5) Z2?Cu2++H2O?Z?[Cu?OH]++Z?H+(Equation 6) steady-state spectra sampled recorded. 5C, treatment isotope-labeled did bring about Cu–CHA, excluding gas-phase oxygen-isotope 3,605 3,595 3,570 respectively) groups 3,655 3,645 ?O-H/?18O-H ?1.003. hydroxyls 18O-exchange led 18O-carboxyl (band 2,105 ?C–O/?C–18O =1.024) accordance 13C-carboxyl 2,107 feeding (?C–O/?13C–O 1.023). Following particulate MMO (pMMO), dicopper proposed process. recently argued pMMO contains mononuclear centers.44Ross M.O. MacMillan Nisthal Lawton T.J. Olafson B.D. Mayo S.L. Hoffman Particulate centers.Science. 364: 566-570Crossref (104) there signs our even if they certain would excess Furthermore, series samples loadings specific compared. S33, site-specific yields similarly level 400–600 0.6–2.3 wt <300 loading 3.5 %. context, rational propose 5), catalytically although excluded. Finally, spin-polarized density (DFT) rationalize observations Data S1, energies spin states S3). 6, set Regarding evolution variation 6A, 6C, S34), (TS-A, 90 kJ/mol) subsequent adsorption CH3Cu[OH2]2 cation cage (M3). Dioxygen molecule demonstrated chemically adsorb center four-coordinated complex (M4). framework-bound methoxide (ZCH3) demethylation (TS-B) accompanied two-coordinated H2OCuO2 (M5). Methanol typical methylation (TS-C) adjacent H2O, leaving H atom H2OCuO2. barriers steps 101 kJ/mol, adsorbed found play facilitating Framework-bound (M7) intermediate CuOH. (TS-D, 99 produce regenerate center. served explicit steps. case CuOH-dimer 6B, 6D, S35), assumed follow aforementioned CuOH-monomer pathway, close proximity another If appropriate distance, binuclear (D2) formed. feasible breaking O–OH (TS-E, 82 immobilized HOCuOCuOH (D3). (TS-F) needed overcome barrier ?59 kJ/mol dimer. comparing kinetics pathways (TS-D versus TS-F), seemed activation. highlight Cu(II), CuOCu, CuOOCu interconverted S34–S39). originating provides alternative producing without 3B) reveals experiments, proved necessary chemisorption 6). origin reflected variations Bader charge, S40. some comes 6), 5C) 2C 2D). Water known prerequisite conversion, plays route hydrolyzing Cu–O bond, (CuOCu, CuOOCu) (CuOH). noted host allows free diffusion (M3) within separate cages aggregation across cages, inactive Cu0. ideal choice Cu-SAPO-34 exhibits S41). ratios S33 S42–S45 Note S1). roles explicated. parameters, kinetic labeling. unique established considering exchange.

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ژورنال

عنوان ژورنال: Chem

سال: 2021

ISSN: ['2451-9308', '2451-9294']

DOI: https://doi.org/10.1016/j.chempr.2021.02.026