TY - JOUR
T1 - On the redox mechanism of methanol carbonylation on a dispersed ReOx/SiO2 catalyst
AU - Tran, Neil D.
AU - Mironenko, Alexander V.
N1 - The authors thank Stephen Garofalini for providing the atomic structure of the vitreous silica. The authors acknowledge the ACS Petroleum Research Fund Doctoral New Investigator Award 65292-DNI5 for the financial support. This work used SDSC Expanse CPU at the University of California San Diego through allocation CHM230055 from the Advanced Cyberinfrastructure Coordination Ecosystem: Services & Support (ACCESS) program, which is supported by National Science Foundation grants #2138259, #2138286, #2138307, #2137603, and #2138296.
PY - 2024/12/18
Y1 - 2024/12/18
N2 - Acetic acid is industrially produced by methanol carbonylation using Ir- or Rh-based homogeneous catalysts and a corrosive HI promoter. Recently, a heterogeneous catalyst with atomically dispersed ReO4 sites on an inert mesoporous SBA-15 support demonstrated high acetic acid yields and stability without the need for a promoter (J. Qi, J. Finzel, H. Robatjazi, M. Xu, A. S. Hoffman, S. R. Bare, X. Pan and P. Christopher, Selective methanol carbonylation to acetic acid on heterogeneous atomically dispersed ReO4/SiO2 catalysts, J. Am. Chem. Soc., 2020, 142(33), 14178-14189, https://doi.org/10.1021/jacs.0c05026). In this study, we investigate the reaction mechanisms of methanol carbonylation on monopodal -ORe( 00000000 00000000 00000000 00000000 11111111 00000000 11111111 00000000 00000000 00000000 O)3 sites using density functional theory calculations, natural bond orbital analysis, and the energetic span model. We find that the reduction of dispersed Re(vii) oxide by CO through an indirect mechanism is essential for catalyst activation. The C-C coupling of methyl and carbonyl ligands is favorable in both Re(v) and Re(iii) complexes, with Re(iii) being superior due to transition state stabilization by a metal-localized lone electron pair. The preceding C-O bond activation is favorable only on Re(v) and leads to a thermodynamic sink, posing challenges in interpreting the high carbonylation activity in terms of monopodal ReOx site catalysis. We hypothesize that multi-nuclear sites or more exotic ligand environments drive the cooperative reaction mechanism of selective carbonylation.
AB - Acetic acid is industrially produced by methanol carbonylation using Ir- or Rh-based homogeneous catalysts and a corrosive HI promoter. Recently, a heterogeneous catalyst with atomically dispersed ReO4 sites on an inert mesoporous SBA-15 support demonstrated high acetic acid yields and stability without the need for a promoter (J. Qi, J. Finzel, H. Robatjazi, M. Xu, A. S. Hoffman, S. R. Bare, X. Pan and P. Christopher, Selective methanol carbonylation to acetic acid on heterogeneous atomically dispersed ReO4/SiO2 catalysts, J. Am. Chem. Soc., 2020, 142(33), 14178-14189, https://doi.org/10.1021/jacs.0c05026). In this study, we investigate the reaction mechanisms of methanol carbonylation on monopodal -ORe( 00000000 00000000 00000000 00000000 11111111 00000000 11111111 00000000 00000000 00000000 O)3 sites using density functional theory calculations, natural bond orbital analysis, and the energetic span model. We find that the reduction of dispersed Re(vii) oxide by CO through an indirect mechanism is essential for catalyst activation. The C-C coupling of methyl and carbonyl ligands is favorable in both Re(v) and Re(iii) complexes, with Re(iii) being superior due to transition state stabilization by a metal-localized lone electron pair. The preceding C-O bond activation is favorable only on Re(v) and leads to a thermodynamic sink, posing challenges in interpreting the high carbonylation activity in terms of monopodal ReOx site catalysis. We hypothesize that multi-nuclear sites or more exotic ligand environments drive the cooperative reaction mechanism of selective carbonylation.
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U2 - 10.1039/d4re00496e
DO - 10.1039/d4re00496e
M3 - Article
AN - SCOPUS:85213046958
SN - 2058-9883
VL - 10
SP - 534
EP - 549
JO - Reaction Chemistry and Engineering
JF - Reaction Chemistry and Engineering
IS - 3
ER -