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Selective methane oxidation by molecular iron catalysts in aqueous medium

Abstract

Using natural gas as chemical feedstock requires efficient oxidation of the constituent alkanes—and primarily methane1,2. The current industrial process uses steam reforming at high temperatures and pressures3,4 to generate a gas mixture that is then further converted into products such as methanol. Molecular Pt catalysts5,6,7 have also been used to convert methane to methanol8, but their selectivity is generally low owing to overoxidation—the initial oxidation products tend to be easier to oxidize than methane itself. Here we show that N-heterocyclic carbene-ligated FeII complexes with a hydrophobic cavity capture hydrophobic methane substrate from an aqueous solution and, after oxidation by the Fe centre, release a hydrophilic methanol product back into the solution. We find that increasing the size of the hydrophobic cavities enhances this effect, giving a turnover number of 5.0 × 102 and a methanol selectivity of 83% during a 3-h methane oxidation reaction. If the transport limitations arising from the processing of methane in an aqueous medium can be overcome, this catch-and-release strategy provides an efficient and selective approach to using naturally abundant alkane resources.

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Fig. 1: Structures of the Fe–NHC complexes used in this study.
Fig. 2: Comparison of TONs and alcohol selectivity among the three catalysts.
Fig. 3: Proposed mechanism for the catch-and-release oxidation of CH4 by 3-AN and S2O82–.

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Data availability

X-ray data are available free of charge from the Cambridge Crystallographic Data Centre under reference numbers CCDC-2106612 and 2106613. All other experimental, spectroscopic, crystallographic and computational data are available from the corresponding author upon request. Source data are provided with this paper.

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Acknowledgements

This work was supported by JST CREST (grant nos. JPMJCR16P1 and JPMJCR15P5) and by Grants-in-Aid (grant nos. 17H03027, 18K19089 and 21H01947) from the Japan Society for the Promotion of Science (JSPS). K.Y. and Y.S. acknowledge the MEXT projects of Cooperative Research Program of Network Joint Research Centre for Materials and Devices, Integrated Research Consortium on Chemical Sciences and the Elements Strategy Initiative to Form Core Research Centre. H.F. also acknowledges funding from JST SPRING (grant no. JPMJSP2124) and Research Fellowship for Young Scientists provided by JSPS (grant no. 22J10804). We thank Edanz (https://jp.edanz.com/ac) for editing a draft of this manuscript.

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Contributions

T.K. conceived and directed the project. H.F. performed the experimental work and analysed the data. T.I. performed X-ray crystallographic analyses of the complexes. K.Y. and Y.S. performed the computational studies. H.K. contributed to kinetic studies. All of the authors discussed the results and H.F., T.I., Y.S. and T.K. prepared the manuscript.

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Correspondence to Takahiko Kojima.

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Extended data figures and tables

Extended Data Fig. 1 Kinetic studies for the CH4 oxidation.

a, A GC-MS total-ion chromatogram for the reaction mixture of the CH4 (0.75 MPa) oxidation by 3-OH2, obtained by gas chromatography equipped with electron-ionization (EI) mass detector (GC-MS). b, EI-MS spectrum of the fraction eluted at the retention time of 3.09 min in a. c, Dependence of the initial rates, v0, for the catalytic oxidation of CH4 using 3-OH2, on the initial CH4 concentration, [CH4]. [CH4] were calculated on the basis of the values reported for aqueous solutions (0.25 MPa: 2.5 mM, 0.50 MPa: 5.0 mM, 0.75 MPa: 7.5 mM, and 0.98 MPa: 9.8 mM)36. The slope of the line, in which the v0 value at 0.98 MPa (9.8 mM) was omitted, since the initial rate showed saturation behaviour against the [CH4], is calculated to obtain the rate constant, kAntH, as (2.8 ± 0.1) × 10–6 s–1. d, A GC-MS total-ion chromatogram for the reaction mixture of CD4 (0.75 MPa) oxidation by 3-OH2. e, EI-MS spectrum of the fraction eluted at the retention time of 3.00 min in d. f, Dependence of the initial rates, v0, for the catalytic oxidation of CD4 using 3-OH2, on the initial CD4 concentration, [CD4]. The slope of the line is calculated to obtain the rate constant, kAntD, as (7.6 ± 0.8) × 10–8 s–1. Reaction conditions: [3-OH2] = 0.010 mM, [Na2S2O8] = 50 mM, solvent = H2O/CH3CN (95:5, v/v; pD was not adjusted), T = 323 K, reaction time: 3 h.

Extended Data Fig. 2 Entrapment of CH4 with 3-OD2 monitored by 1H NMR spectroscopy.

a, 1H NMR spectra of CH4, whose concentration was estimated to be 0.05 mM, in D2O/CD3CN (1:1, v/v) in the absence (top) and presence (bottom) of 3-OD2 (0.1 mM) at 298 K. b, 1H NMR spectra in D2O/CD3CN (1:1, v/v) of 3-OD2 (0.1 mM) at 298 K before (top) and after (bottom) bubbling CH4, whose concentration was estimated to be 0.05 mM.

Extended Data Fig. 3 Analysis of the chemical shift change for the 1H NMR signal of CH4 upon addition of the FeII-NHC complexes.

Plots of the chemical shift change for the 1H NMR signal of CH4 against the concentration of 3-OD2 at 298 K (a), 278 K (b), 308 K (c), and 323 K (d) in D2O/CD3CN (1:1, v/v). e, van’t Hoff plot for the association of CH4 with 3-OD2. Plots of the chemical shift change for the 1H NMR signal of CH4 against the concentration of 1-OD2 (f) and 2-OD2 (g) at 298 K. The fitting curves (solid lines) in ad, f & g are calculated using equation (1) in the Methods as described previously29. The error bars in the plots represent the digital resolution for the 1H NMR spectroscopy under the conditions.

Extended Data Fig. 4 Spectroscopic data for 3-O.

CSI-TOF-MS spectra of 3-16O (top) and 3-18O (bottom), obtained from oxidation of 3-OH2 with 5 equiv of CAN in a mixed solvent of CH3CN:H216O (3:1) and CH3CN:H218O (3:1), diluted with CH3CN and measured at 278 K and their simulations (a) and the full-range spectra (m/z = 200 – 2000) (b). c, Microscopic Raman spectra of 3-O, formed from 3-OH2 with 5 equiv of CAN in CH3CN:H216O (3:1, v/v) (red) or CH3CN:H218O (3:1, v/v) (blue), at 298 K and the differential spectrum (black). d, UV-vis spectra of 3-OH2 (red); [FeIII(AntPY4Cl2BIm)(OH2)]2+ (blue), generated in-situ from 3-OH2 by addition of 1.2 equiv of CAN; 3-O (green), generated in-situ from 3-OH2 by addition of 5 equiv of CAN, in CH3CN:H2O (3:1). e, (top) ESR spectrum of the reaction mixture, quickly frozen during the catalytic oxidation of CH4 (3.5 mM) by 3-OH2 (0.1 mM) in the presence of Na2S2O8 (50 mM) in H2O:CH3CN (95:5) at 323 K; (bottom) ESR spectra of 3-OH2 (red), [FeIII(AntPY4Cl2-BIm)(OH2)]2+ (blue) and 3-O (green), obtained from oxidation of 3-OH2 with 1.2 equiv and 5 equiv of CAN, respectively, in CH3CN:H2O (3:1) (bottom).

Extended Data Fig. 5 DFT-calculated energy profile for the rate-determining HAT step in the CH4 oxygenation process.

Relative free energy values are given in kcal mol–1 with respect to a reactant complex consisting of the FeIV-oxo complex (3-O) and one trapped methane molecule. Here, “TS” and “Int” refer to a transition state generated during methane oxygenation and an intermediate consisting of the FeIII-OH complex and the methyl radical, respectively.

Extended Data Table 1 Summary of the product concentrations obtained from the oxidation reactions of gaseous alkanes in the absence and presence of iron salts or 3-OD2 in a mixed solvent of D2O/CD3CN (95/5)
Extended Data Table 2 Summary of the product concentrations obtained from the oxidation of alcohol derivatives in a mixed solvent of D2O/CD3CN (95:5, v/v) using 1-OD2, 2-OD2, and 3-OD2 as catalysts

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This Supplementary Information PDF contains the following sections: general, synthesis and X-ray crystallography; also included are Supplementary Figs. 1–41, Supplementary Tables 1–4 and Supplementary References.

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Fujisaki, H., Ishizuka, T., Kotani, H. et al. Selective methane oxidation by molecular iron catalysts in aqueous medium. Nature 616, 476–481 (2023). https://doi.org/10.1038/s41586-023-05821-2

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