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

Methanol adsorption isotherms of fresh f-ZSM-5 and steamed s-ZSM-5 (Si/Al E 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.

Publication Details

Journal
UCL Discovery (University College London)
Published
2025-02-07
Primary Topic
Diverse Scientific and Economic Studies
Type
article
Field-Weighted Citation Impact
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article

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

UCL Discovery (University College London)
Diverse Scientific and Economic Studies
article

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

article en

Abstract

Methanol adsorption isotherms of fresh f-ZSM-5 and steamed s-ZSM-5 (Si/Al E 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.

UCL Discovery (University College London)
University College London, Cardiff University, UK Catalysis Hub, Engineering and Physical Sciences Research Council
Openalex Percentile: Top 37%
Diverse Scientific and Economic Studies
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A complementary experimental and computational study on methanol adsorption isotherms of H-ZSM-5 · UCL Discovery (University College London) (2025) | TGRS Research Map | TGRS