Carbon dioxide; Methanol to hydrocarbons; Paraffinic hydrocarbons; Proximity; Tandem catalyst; Zeolite; Bed configuration; Beta zeolite; Dual beds; Methanol-to-hydrocarbons; Silanols; Tandem system; ]+ catalyst; Environmental Chemistry; Chemistry (all); Chemical Engineering (all); Industrial and Manufacturing Engineering
Abstract :
[en] The tandem system for CO2 conversion to C4+ fuels through methanol as an intermediate, in one step, is studied in this work using ZnZrOx and beta zeolites. We show that the bed configuration is of major importance for such systems and highly dependent on the catalytic materials chosen. A dual bed configuration benefits the system showing the highest space time yield for C4+ paraffins when beta Si/Al = 15 is used (1.75 molC.kgcat−1.h−1) and an impressive selectivity of 40 % to isobutane. More beta zeolites with different Si/Al are tested in both mixed and dual bed configuration and correlations between the catalytic behavior and the acidic properties of the zeolites are made. A hypothesis on a correlation between the position of the hydroxy species, especially the silanols, and the difference in activity due to different proximities is proposed, as zeolites with more external silanols seem to benefit more from a dual bed configuration. Higher temperatures and GHSVs increase the production of paraffins but simultaneously increase CO selectivity. Moreover, the tandem system is found stable for more than 30 h. These results are essential for the further development of tandem catalytic systems converting CO2 to light alkanes.
Disciplines :
Chemical engineering
Author, co-author :
Lappa, Foteini ; Université de Liège - ULiège > Chemical engineering ; Center for Sustainable Catalysis and Engineering (CSCE), KU Leuven, Leuven, Belgium
Khalil, Ibrahim; Center for Sustainable Catalysis and Engineering (CSCE), KU Leuven, Leuven, Belgium ; Université Claude Bernard Lyon 1, CNRS, IRCELYON, Villeurbanne, France
Léonard, Grégoire ; Université de Liège - ULiège > Department of Chemical Engineering > PEPs - Products, Environment, and Processes
Dusselier, Michiel; Center for Sustainable Catalysis and Engineering (CSCE), KU Leuven, Leuven, Belgium
Language :
English
Title :
Bed configuration effects of tandem ZnZrOx-Beta zeolite catalysis in the one step methanol-mediated CO2 conversion to C4+ hydrocarbons
FWO - Fonds Wetenschappelijk Onderzoek Vlaanderen FPS Economy - Federal Public Service Economy KU Leuven - Catholic University of Leuven
Funding text :
F.L., G.L. and M. D. acknowledge the main funding for this work: BE-HyFE project funded by the federal Energy Transition Fund by FPS Economy. I.K. acknowledges the Research Foundation Flanders (FWO Vlaanderen) for the Senior postdoctoral research grant ( 12A3M24N ). M.D. acknowledges funding from KU Leuven grant C14/20/086 .
Lappa, F., Khalil, I., Morales, A., Leonard, G., Dusselier, M., One Step Methanol-Mediated CO 2 Conversion to Gasoline: Comprehensive Review and Critical Outlook. Energy and Fuels 38 (2024), 18265–18291, 10.1021/acs.energyfuels.4c03013.
Prévot, M.S., et al. An anthropocene-framed transdisciplinary dialog at the chemistry-energy nexus. Chem. Sci. 15:24 (2024), 9054–9086, 10.1039/d4sc00099d.
Intergovernmental Panel on Climate Change, Technology-specific cost and performance parameters. Clim. Chang. Mitig., 2015, 1329–1356, 10.1017/cbo9781107415416.025.
Garg, S., Xie, Z., Chen, J.G., Tandem reactors and reactions for CO2 conversion., 1(February), 2024, 139–148, 10.1038/s44286-023-00020-2.
Li, W., Wang, K., Zhan, G., Huang, J., Li, Q., Hydrogenation of CO2to dimethyl ether over tandem catalysts based on biotemplated hierarchical ZSM-5 and Pd/ZnO. ACS Sustain. Chem. Eng. 8:37 (2020), 14058–14070, 10.1021/acssuschemeng.0c04399.
Boretti, A., Carbon dioxide hydrogenation for sustainable energy storage. Int. J. Hydrogen Energy 58:February (2024), 1386–1395, 10.1016/j.ijhydene.2024.01.199.
Mahnaz, F., et al. Selective valorization of CO2 towards valuable hydrocarbons through methanol-mediated tandem catalysis. ChemCatChem, 15(17), 2023, 10.1002/cctc.202300402.
Sajid, A., Devos, J., Robijns, S., Donckels, T., Khalil, I., Dusselier, M., Role of coupling and zeolite acidity in the methanol-mediated CO2 conversion to olefins over ZnZrOx-AEI zeolite tandem catalysis. J. Catal., 442(December), 2025, 115927, 10.1016/j.jcat.2024.115927.
Zhao, T., et al. Compound catalyst of ReMoSx@HSSZ-39 and SAPO-34 zeolites for high performance conversion of CO2 to C2-4 hydrocarbons. Chem. Eng. J., 497(July), 2024, 10.1016/j.cej.2024.154448.
Bakhtyari, A., Parhoudeh, M., Reza, M., Optimal conditions in converting methanol to dimethyl ether, methyl formate, and hydrogen utilizing a double membrane heat exchanger reactor. J. Nat. Gas Sci. Eng. 28 (2016), 31–45, 10.1016/j.jngse.2015.11.028.
Brunetti, A., Migliori, M., Cozza, D., Catizzone, E., Giordano, G., Barbieri, G., Methanol Conversion to Dimethyl Ether in Catalytic Zeolite Membrane Reactors. 2020, 10.1021/acssuschemeng.0c02557.
Bahruji, H., Armstrong, R.D., Ruiz Esquius, J., Jones, W., Bowker, M., Hutchings, G.J., Hydrogenation of CO2 to dimethyl ether over brønsted acidic PdZn catalysts. Ind. Eng. Chem. Res. 57:20 (2018), 6821–6829, 10.1021/acs.iecr.8b00230.
Niu, J., Liu, H., Jin, Y., Fan, B., Qi, W., Ran, J., Comprehensive review of Cu-based CO2 hydrogenation to CH3OH: insights from experimental work and theoretical analysis. Int. J. Hydrogen Energy 47:15 (2022), 9183–9200, 10.1016/j.ijhydene.2022.01.021.
Wang, J., et al. A highly selective and stable ZnO-ZrO2 solid solution catalyst for CO2 hydrogenation to methanol. Sci. Adv. 3:10 (2017), 1–11, 10.1126/sciadv.1701290.
Zhang, X., et al. Highly dispersed ZnO sites in a ZnO/ZrO2 catalyst promote the CO2-to-methanol reaction., 202416899, 2025, 10.1002/ange.202416899.
Chang, H., et al. Unlocking methanol synthesis from CO2 and H2 on ZnO/ZrO2 catalysts: surface hydroxyl-mediated activation. ACS Catal., 2025, 6005–6017, 10.1021/acscatal.5c01585.
Kianfar, E., Hajimirzaee, S., mousavian, S., Mehr, A.S., Zeolite-based catalysts for methanol to gasoline process: a review. Microchem. J., 156(September 2019), 2020, 104822, 10.1016/j.microc.2020.104822.
Biswas, S., Pal, T., Supported Metal and Metal Oxide Particles with Proximity Effect for Catalysis. 2020, 35449–35472, 10.1039/d0ra06168a.
Zecevic, J., Vanbutsele, G., De Jong, K.P., Martens, J.A., Nanoscale intimacy in bifunctional catalysts for selective conversion of hydrocarbons. Nature 528:7581 (2015), 245–254, 10.1038/nature16173.
Martín, N., et al. MOF-derived/zeolite hybrid catalyst for the production of light olefins from CO2. ChemCatChem 12:22 (2020), 5750–5758, 10.1002/cctc.202001109.
Jiang, H., Hou, Z., Luo, Y., A Kinetic View on Proximity-Dependent Selectivity of Carbon Dioxide Reduction on Bifunctional Catalysts. 2020, 10.1021/acscatal.0c03414.
Parra, O., Portillo, A., Ereña, J., Aguayo, A.T., Bilbao, J., Ateka, A., Boosting the activity in the direct conversion of CO2/CO mixtures into gasoline using ZnO-ZrO2 catalyst in tandem with HZSM-5 zeolite. Fuel Process. Technol., 245(January), 2023, 10.1016/j.fuproc.2023.107745.
Weber, J.L., Krans, N.A., Hofmann, J.P., Hensen, E.J.M., Zecevic, J., De Jongh, P.E., Effect of proximity and support material on deactivation of bifunctional catalysts for the conversion of synthesis gas to olefins and aromatics. Catal. Today 342:January 2019 (2020), 161–166, 10.1016/j.cattod.2019.02.002.
Ding, Y., et al. Effects of Proximity-Dependent Metal Migration on Bifunctional Composites Catalyzed Syngas to Olefins. 2021, 10.1021/acscatal.1c01649.
Lyu, J., Yu, S., Peng, Z., Zhou, J., Liu, Z., Li, X., Control of the proximity of bifunctional zeolite @Al2O3 catalysts for efficient methanol conversion into hydrocarbons., 406(March), 2022, 82–91, 10.1016/j.cattod.2022.07.017.
Chen, S., Wang, J., Feng, Z., Jiang, Y., Hu, H., Qu, Y., Hydrogenation of CO2 to Light Olefins over ZnZrOx/SSZ-13 Angewandte., 730000, 2024, 10.1002/anie.202316874.
Wang, X., et al. Macroscopic assembly style of catalysts significantly determining their efficiency for converting CO2 to gasoline. Cat. Sci. Technol. 9:19 (2019), 5401–5412, 10.1039/c9cy01470e.
Dokania, A., et al. Designing a multifunctional catalyst for the direct production of gasoline-range isoparaffins from CO2. JACS Au 1:11 (2021), 1961–1974, 10.1021/jacsau.1c00317.
Li, Z., et al. Highly selective conversion of carbon dioxide to aromatics over tandem catalysts. Joule 3:2 (2019), 570–583, 10.1016/j.joule.2018.10.027.
Parra, O., Portillo, A., Ereña, J., Bilbao, J., Ateka, A., Production of isoparaffinic gasoline from CO2/CO over ZnO-ZrO2/nano-sized HZSM-5 tandem catalyst. Catal. Today, 458(December 2024), 2025, 10.1016/j.cattod.2025.115397.
Ghosh, S., Olsson, L., Creaser, D., Methanol mediated direct CO2 hydrogenation to hydrocarbons: experimental and kinetic modeling study. Chem. Eng. J., 435(P3), 2022, 135090, 10.1016/j.cej.2022.135090.
Wang, Y., et al. Visualizing element migration over bifunctional metal-zeolite catalysts and its impact on catalysis. Angew. Chemie 133:32 (2021), 17876–17884, 10.1002/ange.202107264.
Khalil, I., Thomas, K., Jabraoui, H., Bazin, P., Maugé, F., Selective elimination of phenol from hydrocarbons by zeolites and silica-based adsorbents—impact of the textural and acidic properties. J. Hazard. Mater., 384(July 2019), 2020, 121397, 10.1016/j.jhazmat.2019.121397.
Emeis, C.A., Cheminform abstract: determination of integrated molar extinction coefficients for IR absorption bands of pyridine adsorbed on solid acid catalysts. ChemInform, 24(38), 1993, 10.1002/chin.199338056.
Alirio, J., et al. Support effects in vanadium incipient wetness impregnation for oxidative and non-oxidative propane dehydrogenation catalysis. Catal. Today, 430(January), 2024, 114546, 10.1016/j.cattod.2024.114546.
Devos, J., Sajid, A., Aelbers, C., Dusselier, M., Parallel-consecutive CO formation during CO2 hydrogenation to olefins in a tandem ZnZrOx/SSZ-13. ACS Sustain. Chem. Eng., 2025, 10.1021/acssuschemeng.5c01336.
Brandi, F., et al. The role of Beta zeolites in the selective single O-demethylation of alkyl-syringols to alkyl-methoxycatechols, a novel polymer building block class. Green Chem., 2025, 10.1039/d4gc04824e.
Westgård Erichsen, M., Svelle, S., Olsbye, U., The influence of catalyst acid strength on the methanol to hydrocarbons (MTH) reaction. Catal. Today 215 (2013), 216–223, 10.1016/j.cattod.2013.03.017.
Gounder, R., Iglesia, E., Catalytic consequences of spatial constraints and acid site location for monomolecular alkane activation on zeolites. J. Am. Chem. Soc. 131:5 (2009), 1958–1971, 10.1021/ja808292c.
Vimont, A., Thibault-Starzyk, F., Daturi, M., Analysing and understanding the active site by IR spectroscopy. Chem. Soc. Rev. 39:12 (2010), 4928–4950, 10.1039/b919543m.
Marques, J.P., et al. Dealumination of HBEA zeolite by steaming and acid leaching: distribution of the various aluminic species and identification of the hydroxyl groups. Comptes Rendus Chim. 8:3–4 (2005), 399–410, 10.1016/j.crci.2005.01.002.
Medeiros-Costa, I.C., Dib, E., Nesterenko, N., Dath, J.P., Gilson, J.P., Mintova, S., Silanol defect engineering and healing in zeolites: opportunities to fine-tune their properties and performances. Chem. Soc. Rev. 50:19 (2021), 11156–11179, 10.1039/d1cs00395j.
Arudra, P., Bhuiyan, T.I., Akhtar, M.N., Aitani, A.M., Al-Khattaf, S.S., Hattori, H., Silicalite-1 as efficient catalyst for production of propene from 1-butene. ACS Catal. 4:11 (2014), 4205–4214, 10.1021/cs5009255.
Gounder, R., Iglesia, E., The catalytic diversity of zeolites: confinement and solvation effects within voids of molecular dimensions. Chem. Commun. 49:34 (2013), 3491–3509, 10.1039/c3cc40731d.
Rungsirisakun, R., Nanok, T., Probst, M., Limtrakul, J., Adsorption and diffusion of benzene in the nanoporous catalysts FAU, ZSM-5 and MCM-22: a molecular dynamics study. J. Mol. Graph. Model. 24:5 (2006), 373–382, 10.1016/j.jmgm.2005.10.003.
Zhang, J., et al. Hydrogen transfer versus olefins methylation: on the formation trend of propene in the methanol-to-hydrocarbons reaction over Beta zeolites. J. Catal. 368 (2018), 248–260, 10.1016/j.jcat.2018.10.015.
Lee, K., Lee, S., Jun, Y., Choi, M., Cooperative effects of zeolite mesoporosity and defect sites on the amount and location of coke formation and its consequence in deactivation. J. Catal. 347 (2017), 222–230, 10.1016/j.jcat.2017.01.018.
Schulz, H., ‘Coking’ of zeolites during methanol conversion: basic reactions of the MTO-, MTP- and MTG processes. Catal. Today 154:3–4 (2010), 183–194, 10.1016/j.cattod.2010.05.012.
Benito, P.L., Gayubo, A.G., Aguayo, T., Deposition and Characteristics of Coke over a H-ZSM5 Zeolite-Based Catalyst in the MTG Process. 1996, 3991–3998.
Arora, S.S., Nieskens, D.L.S., Malek, A., Bhan, A., Lifetime improvement in methanol-to-olefins catalysis over chabazite materials by high-pressure H2 co-feeds. Nat. Catal. 1:9 (2018), 666–672, 10.1038/s41929-018-0125-2.
Sharma, P., Sebastian, J., Ghosh, S., Creaser, D., Olsson, L., Recent advances in hydrogenation of CO2into hydrocarbonsviamethanol intermediate over heterogeneous catalysts. Cat. Sci. Technol. 11:5 (2021), 1665–1697, 10.1039/d0cy01913e.
Mirshafiee, F., Khoshbin, R., Karimzadeh, R., A green approach for template free synthesis of Beta zeolite incorporated in ZSM-5 zeolite to enhance catalytic activity in MTG reaction: effect of seed nature and temperature. J. Clean. Prod., 361(May), 2022, 132159, 10.1016/j.jclepro.2022.132159.
Gayubo, A.G., Aguayo, A.T., Morán, A.L., Olazar, M., Bilbao, J., Role of water in the kinetic modeling of catalyst deactivation in the MTG process. AIChE J. 48:7 (2002), 1561–1571, 10.1002/aic.690480718.