Transitioning from Methanol to Olefins (MTO) toward a Tandem CO2 Hydrogenation Process: On the Role and Fate of Heteroatoms (Mg, Si) in MAPO-18 Zeotypes

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Title: Transitioning from Methanol to Olefins (MTO) toward a Tandem CO2 Hydrogenation Process: On the Role and Fate of Heteroatoms (Mg, Si) in MAPO-18 Zeotypes
Authors: Cordero-Lanzac, Tomás | Capel Berdiell, Izar | Airi, Alessia | Chung, Sang-Ho | Mancuso, Jenna L. | Redekop, Evgeniy A. | Fabris, Claudia | Figueroa-Quintero, Leidy | Navarro de Miguel, Juan C. | Narciso, Javier | Ramos-Fernández, Enrique V. | Svelle, Stian | Speybroeck, Veronique Van | Ruiz Martínez, Javier | Bordiga, Silvia | Olsbye, Unni
Research Group/s: Materiales Avanzados
Center, Department or Service: Universidad de Alicante. Departamento de Química Inorgánica | Universidad de Alicante. Instituto Universitario de Materiales
Keywords: CO2 valorization | MTH | MTO | MgAPO-18 | AEI | Deactivation
Issue Date: 13-Feb-2024
Publisher: American Chemical Society
Citation: JACS Au. 2024, 4(2): 744-759. https://doi.org/10.1021/jacsau.3c00768
Abstract: The tandem CO2 hydrogenation to hydrocarbons over mixed metal oxide/zeolite catalysts (OXZEO) is an efficient way of producing value-added hydrocarbons (platform chemicals and fuels) directly from CO2 via methanol intermediate in a single reactor. In this contribution, two MAPO-18 zeotypes (M = Mg, Si) were tested and their performance was compared under methanol-to-olefins (MTO) conditions (350 °C, PCH3OH = 0.04 bar, 6.5 gCH3OH h–1 g–1), methanol/CO/H2 cofeed conditions (350 °C, PCH3OH/PCO/PH2 = 1:7.3:21.7 bar, 2.5 gCH3OH h–1 g–1), and tandem CO2 hydrogenation-to-olefin conditions (350 °C, PCO2/PH2 = 7.5:22.5 bar, 1.4–12.0 gMAPO-18 h molCO2–1). In the latter case, the zeotypes were mixed with a fixed amount of ZnO:ZrO2 catalyst, well-known for the conversion of CO2/H2 to methanol. Focus was set on the methanol conversion activity, product selectivity, and performance stability with time-on-stream. In situ and ex situ Fourier transform infrared spectroscopy (FT-IR), X-ray diffraction (XRD), solid-state nuclear magnetic resonance (NMR), sorption experiments, and ab initio molecular dynamics (AIMD) calculations were performed to correlate material performance with material characteristics. The catalytic tests demonstrated the better performance of MgAPO-18 versus SAPO-18 at MTO conditions, the much superior performance of MgAPO-18 under methanol/CO/H2 cofeeds, and yet the increasingly similar performance of the two materials under tandem conditions upon increasing the zeotype-to-oxide ratio in the tandem catalyst bed. In situ FT-IR measurements coupled with AIMD calculations revealed differences in the MTO initiation mechanism between the two materials. SAPO-18 promoted initial CO2 formation, indicative of a formaldehyde-based decarboxylation mechanism, while CO and ketene were the main constituents of the initiation pool in MgAPO-18, suggesting a decarbonylation mechanism. Under tandem CO2 hydrogenation conditions, the presence of high water concentrations and low methanol partial pressure in the reaction medium led to lower, and increasingly similar, methanol turnover frequencies for the zeotypes. Despite both MAPO-18 zeotypes showing signs of activity loss upon storage due to the interaction of the sites with ambient humidity, they presented a remarkable stability after reaching steady state under tandem reaction conditions and after steaming and regeneration cycles at high temperatures. Water adsorption experiments at room temperature confirmed this observation. The faster activity loss observed in the Mg version is assigned to its harder Mg2+-ion character and the higher concentration of CHA defects in the AEI structure, identified by solid-state NMR and XRD. The low stability of a MgAPO-34 zeotype (CHA structure) upon storage corroborated the relationship between CHA defects and instability.
Sponsor: This work was carried out thanks to the financial support of the European Union’s Horizon 2020 Research and Innovation Programme under grant agreement no. 837733. I.C.B and S.S. thank the iCSI (industrial Catalysis Science and Innovation) Centre for Research-based Innovation, which receives financial support from the Research Council of Norway under contract no. 237922. S.B. and A.A. acknowledge support from the Project CH4.0 under the MUR program “Dipartimenti di Eccellenza 2023-2027″ (CUP: D13C22003520001). S.-H.C, J.C.N., and J.R.-M. are grateful for the Competitive Research Grant (URF/1/4406-01-01) from the King Abdullah University of Science and Technology. J.L.M acknowledges the Fund for Scientific Research – Flanders (FWO) for the financial support through a postdoctoral fellowship (Grant 1262523N). The computational resources used in this work were provided by VSC (Flemish Supercomputer Center) funded by FWO, Ghent University, and the Department of Economy, Science & Innovation in the Flemish Government. V.V.S. acknowledges funding from the Research Fund of Ghent University (BOF). L.F.-Q., J.N., and E.V.R.-F. acknowledge financial support by the Spanish Ministerio de Ciencia e Innovación (PID2020-116998RB-I00).
URI: http://hdl.handle.net/10045/140737
ISSN: 2691-3704
DOI: 10.1021/jacsau.3c00768
Language: eng
Type: info:eu-repo/semantics/article
Rights: © 2024 The Authors. Published by American Chemical Society. This publication is licensed under CC-BY 4.0.
Peer Review: si
Publisher version: https://doi.org/10.1021/jacsau.3c00768
Appears in Collections:Research funded by the EU
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