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Controlling the selectivity–stability tradeoff in zeolite catalysis: oligomerization–alkylation, cracking, and methanol-to-hydrocarbons 


    Problem Statement

    Olefins and aromatics are commodity chemicals used in producing plastics (in the petrochemical industry), lubricants, plasticizers, and surfactants, among other products. However, there is an imbalance between their production and demand, which reactions like oligomerization, alkylation, and cracking over zeolites could help address. At the same time, zeolites serve as excellent catalysts for converting methanol to hydrocarbons (MTH), olefins (MTO), or aromatics (MTA). These processes aim to produce light hydrocarbons such as propylene or to convert ethylene into higher-value alpha-olefins, aromatic hydrocarbons (BTX), and jet fuel.


    Our focus in this project is to synthesize, modify, and develop new catalysts with engineered porosity at multiple scales: from hierarchical and hollow zeolites to catalytic particles, bodies, or technical catalysts intended for implementation. Additionally, we incorporate various metals (e.g., Ni, Cr, Zn) to influence the selectivity toward the desired products.

    We utilize various reactors, including forced dynamic, operando, high-throughput packed-bed, and batch reactors.

    OLG-O2H

    Goals

    • Control the catalyst structure to balance selectivity and stability.
    • Metal modulation: Use Ni, Cr, Zn to bias reaction pathways and improve selectivity to target hydrocarbons.
    • Deactivation control: Reduce coke formation and extend catalyst lifetime with regeneration strategies.
    • Reactor optimization: Shape catalysts into bodies/extrudates and validate 100 h continuous stable operation.

    Related People

    Related Publications

    Metal speciation in hierarchical ZSM-5 programs ethylene oligomerization selectivity

    by Mohamed, Velisoju, khairova, Trueba, Zambrano, Hassine, Hedhili, Abou-Hamad, Telalovic, Cavallo, Castaño
    ACS Catal. Year: 2026 DOI: https://doi.org/10.1021/acscatal.6c03322

    Abstract

    Metal cations in zeolites can redirect alkene oligomerization from Brønsted-acid-mediated secondary chemistry toward coordination-insertion pathways; however, controlling whether metal precursors form accessible cationic sites or oxide nanoparticles remains challenging. Here, we prepared hierarchical ZSM-5 by polymeric templating (PT) at a common nominal loading of 3 wt % and compared the protonic parent H/PT with Ni/PT, Cr/PT, and Zr/PT to determine how metal speciation governs ethylene oligomerization. X-ray diffraction, N2 physisorption, microscopy, X-ray photoelectron spectroscopy, in situ X-ray absorption spectroscopy, CO-DRIFTS, pyridine-FTIR, and multinuclear solid-state NMR show that Ni/PT is dominated by accessible, framework-interacting Ni2+ Lewis sites, with a minor NiO-like contribution. Cr/PT contains accessible Cr-associated Lewis sites together with CrOx-like domains that evolve toward Cr2O3 during pretreatment, whereas Zr/PT is dominated by ZrO2 nanoparticles and retains more Brønsted acidity than Ni/PT and Cr/PT. These differences reshape catalytic activity: Ni/PT achieves 92% combined C4–C8 olefin selectivity with a butene-rich, dimerization-dominated slate, whereas Cr/PT gives a C6-rich distribution from a mixed network of Cr-associated Lewis sites and residual acid-mediated chemistry; H/PT and Zr/PT instead favor hydrogen transfer, aromatization, and paraffin formation. Density functional theory on an initiated [Ni(II)–ethyl]+ model places β-hydrogen transfer/chain termination 10 kJ mol–1 below further ethylene insertion, rationalizing the C4-rich response. The coke content increases in the order H/PT < Ni/PT < Cr/PT < Zr/PT, whereas total retained-deposit content follows H/PT < Cr/PT < Ni/PT < Zr/PT. Thus, olefin selectivity and deposit formation do not vary in parallel. Within this matched catalyst series, chain-length selectivity and deactivation reflect the coupled effects of metal speciation, site accessibility, thermal evolution, and residual acidity rather than nominal metal loading, total Lewis acidity, or texture alone.

    Keywords

    OLG HCE