A complementary experimental and computational study on methanol adsorption isotherms of H-ZSM-5

Santhosh K Matam; Lotfi Boudjema; Matthew G Quesne; James D Taylor; C Richard A Catlow

doi:10.1039/d4cp03761h

A complementary experimental and computational study on methanol adsorption isotherms of H-ZSM-5

Phys Chem Chem Phys. 2025 Jan 14. doi: 10.1039/d4cp03761h. Online ahead of print.

Authors

Santhosh K Matam^{1

2}, Lotfi Boudjema^{1

3

4}, Matthew G Quesne^{1

2

5}, James D Taylor⁶, C Richard A Catlow^{1

2

3}

Affiliations

¹ UK Catalysis Hub, Research Complex at Harwell, Science and Technology Facilities Council, Rutherford Appleton Laboratory, OX11 0FA, UK. [email protected].
² Cardiff Catalysis Institute, School of Chemistry, Cardiff University, Cardiff, CF10 3AT, UK.
³ Department of Chemistry, University College London, 20 Gordon St., London WC1E 6BT, UK.
⁴ ICGM, Univ. Montpellier, CNRS, ENSCM, Montpellier, France.
⁵ School of Chemistry, University of Leeds, Leeds LS2 9JT, UK.
⁶ ISIS Pulsed Neutron and Muon Facility, Science and Technology Facilities Council, Rutherford Appleton Laboratory, OX11 0QX, UK.

PMID: 39807066
DOI: 10.1039/d4cp03761h

Abstract

Methanol adsorption isotherms of fresh f-ZSM-5 and steamed s-ZSM-5 (Si/Al ≈ 40) are investigated experimentally at room temperature under equilibrium and by grand canonical Monte Carlo (GCMC) simulations with the aim of understanding the adsorption capacity, geometry and sites as a function of steam treatment (at 573 K for 24 h). Methanol adsorption energies calculated by GCMC are complemented by density functional theory (DFT) employing both periodic and quantum mechanics/molecular mechanics (QM/MM) techniques. Physical and textural properties of f-ZSM-5 and s-ZSM-5 are characterised by diffuse reflectance infrared Fourier transformed spectroscopy (DRIFTS) and N₂-physisorption, which form a basis to construct models for f-ZSM-5 and s-ZSM-5 to simulate methanol adsorption isotherms by GCMC. Both Brønsted and silanol hydroxyls are observed in f-ZSM-5 and s-ZSM-5 by DRIFTS; however, these species, especially Brønsted species, decreased considerably upon steam treatment in s-ZSM-5 due to dealumination. Although the total pore volume and mesoporosity increased in s-ZSM-5 as compared in f-ZSM-5, the total surface area (375 m² g^-1) of the steamed zeolite is lower than the fresh zeolite (416 m² g^-1) due to pore plugging caused by partial dislodgement of framework Al on steam treatment. Implications of the steam treatment on the methanol adsorption capacity of the zeolites are reflected in the experimental methanol adsorption isotherms, collected (in the pressure range between 0 and 12 kPa) at room temperature under equilibrium, which find that the overall methanol uptake is lower for s-ZSM-5 than for f-ZSM-5. The GCMC simulations show that the nature, location and distribution of acidic hydroxyls determine the methanol adsorption capacity, geometry and hence the isotherm profiles of f-ZSM-5 and s-ZSM-5. The GCMC simulations provide insight into the different adsorption sites and their reactivity towards methanol which paves the way not only to describe the isotherms of f-ZSM-5 and s-ZSM-5 but also offers a means to understand better the deactivation of ZSM-5 by steam (leading to dealumination) and subtle differences in surface adsorbed species on ZSM-5 procured from different sources.