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Probing biomass mimic guaiacol confinement and interactions in ZSM-5 zeolite

Kyle A. Watsona, Ming-Feng Hsiehb, Stephen Dayc, Luke Tuxworthb and Frédéric Blanc*ade
aDepartment of Chemistry, University of Liverpool, Liverpool L69 7ZD, UK. E-mail: frederic.blanc@liverpool.ac.uk
bJohnson Matthey, Billingham TS23 1LB, UK
cJohnson Matthey Technology Centre, Sonning Common RG4 9NH, UK
dStephenson Institute for Renewable Energy, University of Liverpool, Liverpool L69 7ZF, UK
eLeverhulme Research Centre for Functional Materials Design, University of Liverpool, Liverpool L7 3NY, UK

Received 4th March 2026 , Accepted 20th May 2026

First published on 21st May 2026


Abstract

The catalytic upgrading of biomass-derived compounds in zeolites such as ZSM-5 remains poorly understood at a molecular level, particularly with respect to adsorption and confinement of trapped species. Guaiacol, a key product of catalytic fast pyrolysis of lignocellulosic biomass, exhibits complex behaviour in ZSM-5, yet direct experimental evidence of zeolite-guaiacol host–guest interactions has been lacking. Here, we directly identify distinct in-pore and ex-pore guaiacol species in adsorbed ZSM-5 and trapped unreacted species following catalytic upgrading. These species are distinguished using 1H and 13C magic angle spinning (MAS) nuclear magnetic resonance (NMR) spectroscopy differentiating through characteristic differences in chemical shifts, linewidths and relaxation data observables, and are complemented by thermogravimetric analysis coupled with mass spectrometry (TGA-MS) to reveal differences in their desorption profiles. Furthermore, 17O isotopic enrichment of the ZSM-5 framework enables two-dimensional 1H–17O dipolar heteronuclear multiple-quantum coherence (D-HMQC) NMR experiments, providing molecular-level insight into the through-space interactions between guaiacol and framework oxygen atoms. Together, these results suggest the location, confinement and reactivity of guaiacol within ZSM-5 pores, offering atomic-scale observations for the rational design of future zeolite catalysts for sustainable fuel production.


Introduction

The conversion of biomass into upgraded bio-oils has become of increasing importance for the production of sustainable aviation fuel and other biofuels, offering a more sustainable pathway less reliant on fossil resources.1,2 Bio-oils are typically produced by fast pyrolysis at high temperatures (250–600 °C), however they are not immediately suitable for direct fuel applications due to factors such as high oxygen content and low pH.3,4 Further catalytic upgrading is therefore required with microporous aluminosilicate zeolites such as ZSM-5 emerging as leading catalysts.5 Biomass is primarily composed of three biopolymers: cellulose, hemicellulose and lignin, whose pyrolysis-derived bio-oils contain a wide range of compounds (e.g., anhydrosugars, furans, phenols and light oxygenates).6,7 Although reaction mechanisms have been proposed for individual components, an overarching mechanism for the conversion and catalytic upgrading process remains incomplete, particularly for how adsorbates interact within the zeolite catalyst frameworks.8,9

ZSM-5 has been chosen as the zeolite due to its well-established shape selectivity and affinity for the formation of light aromatics.10–13 A SiO2-to-Al2O3 ratio of 34 has been selected to reflect catalytic conditions for maximising the yield of desirable small aromatic products such as benzene, toluene, ethylbenzene and xylenes (BTEX).14 ZSM-5 is a medium pore zeolite, with a framework comprising a three-dimensional structure of straight channels (5.6 Å by 5.4 Å) intersected by sinusoidal channels (5.5 Å by 5.1 Å).15 Despite these nominal pore dimensions, it has been observed that molecules with kinetic diameters larger than the channel openings such as guaiacol (6.68 Å) have been shown to diffuse in and out of the ZSM-5 framework.16,17 This apparent contradiction has been long attributed to the structural adaptability of ZSM-5 with the reversible adsorption of guest species triggering a symmetry change from the standard monoclinic to the orthorhombic phase.18–20 More recently, in situ imaging has directly visualised channel deformation upon benzene adsorption, revealing a transition from almost completely circular to elliptical pore cross-sections.21 These observations suggest that, while being macroscopically rigid, ZSM-5 exhibits inherent microscopic flexibility allowing for the diffusion and confinement of molecules larger than anticipated from static pore dimensions alone.

In the industrial catalytic process, a chemical reactor does not contain exclusively ‘fresh’ pristine zeolite catalyst but consists of a mix that routinely has fractions removed and replaced by a fresh catalyst.22 This achieves a steady state, equilibrium catalyst which is composed of a distribution of aged zeolite populations, with a range of catalytic activities and densities of Brønsted acid sites (BAS). This is caused in part by the gradual dealumination of ZSM-5, whereby aluminium is removed from the framework structure to form extra-framework sites. Dealumination is a substantial obstacle in the industrial use of ZSM-5, which predominantly occurs due to the process requiring harsh temperatures in combination with the high-water content of biomass and bio-oils.23 Dealuminated zeolites have been prepared in the literature for comparison to industrial equilibrium catalysts, most commonly using steaming or acid treatments.24 In this work, ZSM-5 samples are exposed to high temperatures during 17O isotopic enrichment, causing notable dealumination and loss of BAS, mirroring that observed in the aged component of industrial equilibrium catalysts.

Guaiacol (2-methoxyphenol) is used in this work as a prototypical guest molecule as it has previously been shown to be a key component of lignin derived bio-oil.6 Additionally, guaiacol provides a realistic representation of the diverse oxygen functionalities present in biomass-derived aromatics, incorporating both alcohol and ether groups. Guaiacol is also readily available and exhibits comparatively low toxicity relative to alternative model compounds such as phenol. Previous works, which have explored this compound as a model in conjunction with ZSM-5, used gas chromatography–mass spectrometry (GC–MS) to set out expected product distributions and suggested reaction mechanisms over a range of experimental variables including temperature, Si/Al ratio and Ni/La modification of ZSM-5.25–28 Other work has employed TGA, scanning electron microscopy (SEM) and gas adsorption experiments to investigate the conversion and coking behaviour of guaiacol in ZSM-5.29 Imaging PhotoElectron PhotoIon Coincidence (iPEPICO) spectroscopy has identified fulvenone ketene as a key reactive intermediate in the H-USY zeolite-catalysed pyrolysis of guaiacol, allowing for a comprehensive deoxygenation mechanism to be constructed.30

Solid-state NMR spectroscopy is a powerful technique used for determining structures and spatial arrangements across a wide range of materials and has played a critical role in heterogeneous catalysis by elucidating reaction pathways and process mechanisms.31–33 In particular, for porous solids such as zeolites, solid-state NMR spectroscopy provides unique information detailing interactions between the guest molecules and the host framework. To date, extensive use has been made of the 1H,34 27Al,35,36 and 29Si20,37 nuclei for framework characterisation and structural elucidation, while 13C,38,39 15N,40,41 and 31P42,43 introduced via adsorbed probe molecules have been exploited to quantify acid site density and strength, determine guest–host interactions and identify reaction intermediates.44

Solid-state NMR spectroscopy has been used to great effect to gain insight into the methanol-to-hydrocarbons (MTH) and methanol-to-olefins (MTO) reaction mechanisms. Key findings include the detection and direct observation of catalytically critical surface methoxy species (SMS) using 13C MAS NMR45,46 and 13C–27Al NMR correlation experiments.47,48 This identification enabled the elucidation of a previously subject to debate mechanism for the initial C–C bond formation, with further experiments demonstrating the first interaction occurs between SMS and surface adsorbed reactants.49,50 Additionally, elusive cyclopentenyl and cyclohexenyl cations have been identified as important intermediates in the hydrocarbon pool process and have been observed by 13C MAS NMR spectroscopy in ZSM-5,51,52 SAPO-34,53–55 and β zeolites.56

Although oxygen is the most prevalent atom in zeolite frameworks, 17O is the only NMR active isotope, with 17O NMR experiments presenting challenges due to its extremely low natural abundance (0.037%) and quadrupolar nature (I = 5/2). To render 17O MAS NMR experiments feasible, dynamic nuclear polarization (DNP) is typically required to boost NMR sensitivity or isotopic enrichment to increase the 17O spin concentration. At natural abundance, DNP enhanced 17O NMR experiments have been successfully employed to probe surface sites in metal hydroxides,57,58 silica,59 and silica–alumina materials60 and to assign the 17O resonances in materials such as electrodes,61 and metal–organic frameworks (MOFs).62 Alternatively, other works have relied on 17O isotopic enrichment, for example, enriched Na-ZSM-5 and H-ZSM-5 have been prepared by high-temperature treatment in H217O63 or 17O2.64 However, these protocols can induce various degrees of framework dealumination. More recently, it has been demonstrated that zeolites, including ZSM-5, can be enriched under significantly milder conditions through slurry-based treatments with H217O.65–67 In the present work, 17O isotopic enrichment of ZSM-5 are prepared by heating in 17O2 at different temperatures, deliberately exploiting temperature-dependent framework dealumination to enable isolation of the Si–O–Si site.

To the best of our knowledge, guaiacol activated ZSM-5 has received limited attention for elucidating guaiacol–zeolite interactions with MAS NMR spectroscopy, with existing work investigating the deoxygenation during the catalytic vapor phase upgrading of guaiacol and hydroxyacetaldehyde.68 In this previous paper, both bio-oil constituents were reacted over ZSM-5 individually and as a mixed feed across a range of reaction temperatures, with 13C MAS NMR spectroscopy employed to identify reaction products and elucidate coking pathways.

Despite extensive solid-state NMR investigations of zeolite structure, acidity and reaction intermediates, experimental insight into the role of framework oxygen atoms in host–guest interactions remains limited. For oxygenated lignin-derived bio-oil constituents such as guaiacol, previous NMR work has largely been restricted to identifying reaction products and interactions with co-adsorbed biomass-derived species, without addressing how these species interact with the zeolite framework at the atomic level. In this work, we address this gap by providing molecular-level insights through the 17O isotopic enrichment of ZSM-5 combined with a range of multinuclear MAS NMR experiments, enabling the observation of in-pore confined guaiacol and its interactions with distinct framework oxygen environments.

Experimental section

Experimental details can be found in full in the SI.

Sample nomenclature

This work uses sample names which have been abbreviated to identify treatment and oxygen enrichment conditions. Am, De and AdsX respectively denote ambient moisture, dehydrated and guaiacol adsorbed with X% of the theoretical pore volume filled. Act indicates guaiacol activated ZSM-5 with a standard heated collection period of 30 s, with Act300 used to distinguish an extended heated collection period of 300 s. NatA denotes samples with natural 17O isotopic abundance and 17O(T) used for samples which have been enriched at the given temperature T (°C). A full list of samples and abbreviations can be found in the SI (Table S1).

Results and discussion

The products of the guaiacol pyrolysis reaction were separated by GC and identified by GC–MS (Table 1). More than 100 individual compounds were detected and categorized based on three criteria: oxygenated versus non-oxygenated species, the number of aromatic rings, and key structural motifs. These were further grouped into BTEX, phenols, naphthalenes, unreacted guaiacol and others such as furans, fluorenes, xanthene and other minor components. Literature products distributions for experiments which used similar low Si/Al ratio (≤30) zeolites and fixed bed reactors consistently report product distributions dominated by phenol and phenolic derivatives, followed by BTEX and products formed by secondary reactions such as naphthalene and other polyaromatic, bulkier compounds.25,26,28
Table 1 Products of guaiacol pyrolysis reaction catalysed by ZSM-5 categorised by oxygen content, number of aromatic rings and structural groups expressed as a percentage of peak area of identified peaks. Values are averaged over three reproducible pyrolysis experiments and used to determine the errors
Oxygen content (peak area% of identified peaks).
Oxygenated products/% Non-oxygenated products/%
57.1 ± 1.9 42.9 ± 1.9

Number of aromatic rings (peak area% of identified peaks).
1 ring/% 2 rings/% 3 rings/% 4 rings/%
57.2 ± 1.3 36.0 ± 0.8 6.7 ± 0.5 0.1 ± 0.0

Structural composition (peak area% of identified peaks).
BTEX/% Phenols/% Naphthalenes/% Guaiacol/% Others/%
10.8 ± 1.1 38.0 ± 1.8 20.6 ± 1.7 2.6 ± 2.3 28.0 ± 1.0


1H MAS NMR spectra (Fig. 1), together with measured longitudinal T1 and transverse T2 relaxation times (Table S2), were used to gain insight into the nature of the adsorbate species present in guaiacol adsorbed with 94% of the ZSM-5 theoretical pore volume filled (Ads94-NatA-ZSM-5, see Experimental section in the SI for full samples nomenclature) and guaiacol activated ZSM-5 by fast catalytic pyrolysis (Act-NatA-ZSM-5). This analysis builds on established observations that in-pore adsorbates can be distinguished by differences in isotopic chemical shift (δCS) values, line width and relaxation parameters.69–71 The 1H MAS NMR spectrum of Ads94-NatA-ZSM-5 shows two broad resonances at δCS of 6.9 and 3.9 ppm (Fig. 1f), together with additional narrower peaks at 6.6, 6.4, 6.3 and 3.1 ppm. Those narrow resonances occur at chemical shifts indistinguishable (within ± 0.1 ppm) from those observed for neat guaiacol (Fig. 1b) and are assigned to aromatic protons (6.3–6.6 ppm) and methoxy protons (3.1 ppm). The broad resonances at 6.9 and 3.9 ppm exhibit full width at half maximum (FWHM) values of approximately 350 and 170 Hz, respectively, whereas the narrower peaks between 6.6–6.3 ppm and at 3.1 ppm display FWHM values in the range of 18–47 Hz.


image file: d6qm00172f-f1.tif
Fig. 1 (a), (c)–(g) 1H MAS NMR spectra acquired at B0 = 18.8 T and with a spinning frequency of νr = 60 kHz for (a) Am-NatA-ZSM-5, (c)–(f) guaiacol adsorbed ZSM-5 with 9, 23, 47 and 94% of the theoretical pore volume filled, respectively, and (g) Act-NatA-ZSM-5. (b) 1H NMR spectrum of neat guaiacol acquired at B0 = 9.4 T and νr = 220 Hz. Orange and blue boxes highlight in-pore and ex-pore guaiacol environments respectively. Asterisks (*) denote spinning sidebands.

Relaxation measurements reveal markedly faster relaxation for the broad resonances (T1 and T2 values in the range of 60–100 ms and 0.8 ms, respectively, Table S2), compared to substantially longer relaxation times for the narrower resonances (T1 and T2 in the range of 1–1.5 s and 8.5–18.7 ms, respectively). Shorter T1 and T2 relaxation times are indicative of restricted molecular mobility72,73 suggesting that the broad signals arise from less mobile guaiacol species, while the narrow signals correspond to more mobile molecules and longer coherence lifetimes. A 2D 1H–1H Exchange SpectroscopY (EXSY) NMR spectrum of Ads94-NatA-ZSM-5 (Fig. S1) is consistent with this observation, with the data clearly showing cross-peaks only within each set of broad and narrow resonances, with no exchange observed between them. This confirms that the two sets of signals arise from spatially distinct guaiacol populations with no detectable exchange. These observations support assignment of the broad resonances to in-pore adsorbate guaiacol molecules confined by the zeolite framework, and the narrow resonances to ex-pore guaiacol with a significantly greater degree of freedom.

To further confirm those assignments, a series of guaiacol adsorbed ZSM-5 samples were also prepared using guaiacol loadings corresponding to 9, 23 and 47% of the theoretical pore volume (0.24 cm3 g−1, see Table S3). The 1H MAS spectra of the AdsX-NatA-ZSM-5 samples (Fig. 1c–f) all exhibit two broad resonances at 6.9 and 3.9 ppm (Fig. 1, orange boxes). At 9% pore filling, and to a lesser extent at 23%, an additional very broad signal centred at 5.5 ppm is also observed which is consistent with the proton exchange processes involving adsorbed water and BAS (Fig. 1a).34

At higher guaiacol loadings (23, 47 and 94% pore filling), additional peaks (Fig. 1, blue boxes) emerge and gradually shift towards the chemical shifts characteristic of ex-pore guaiacol as the guaiacol volume increases. This behaviour further supports the assignment of the broad resonances at 6.9 and 3.9 ppm to confined in-pore guaiacol species. Such a trend is expected as guaiacol is anticipated to preferentially occupy the zeolite pores before ex-pore species become detectable once the pores are completely saturated or rendered inaccessible. Notably, the spectra indicate that even at 23% of the theoretical pore volume, guaiacol does not fully diffuse into the ZSM-5 framework at room temperature, suggesting partial pore blockage or diffusion limitations at relatively low loadings.

The 1H MAS spectrum of Act-NatA-ZSM-5 (Fig. 1g) shows four broad resonances at 6.9, 3.9, 2.3 and 1.3 ppm. Notably, the signals at 6.9 and 3.9 ppm coincide with the δCS values assigned to in-pore guaiacol in the spectrum of Ads94-NatA-ZSM-5 (Fig. 1f), indicating the presence of confined guaiacol species following pyrolysis. Ex-pore guaiacol is not expected to remain in the activated ZSM-5 as the elevated temperatures and continuous gas flow employed during the reaction would remove any weakly bound or non-adsorbed molecules passing them out of the reactor. The resonance at δCS = 2.3 ppm is assigned to aliphatic moieties associated with coke precursors, supported by its correlation with a 13C signal at 15–20 ppm (see 13C assignment in Fig. 2b and the 1H–13C heteronuclear correlation spectrum in Fig. S2). The smaller resonance at 1.2 ppm, which is also observed in Am-NatA-ZSM-5 (Fig. 1a), is attributed to silanol lattice defects.74


image file: d6qm00172f-f2.tif
Fig. 2 (a) 13C NMR spectrum of neat guaiacol (not in solvent) at B0 = 9.4 T under static conditions, shown with a numbered structure for resonance assignments. (b) and (c) 13C CP MAS spectra acquired with a 2 ms contact time at B0 = 9.4 T and νr = 10 kHz for (b) Act-NatA-ZSM-5 and (c) Act300-NatA-ZSM-5.

13C CP MAS NMR spectroscopy was also employed to further assess the species confined within the pores of guaiacol activated ZSM-5 (Fig. 2). The 13C CP MAS spectrum of Act-NatA-ZSM-5 (Fig. 2b) displays a broad resonance at 110–160 ppm and several sharper peaks that match with the 13C chemical shifts δCS of the 13C MAS NMR spectrum of neat guaiacol (Fig. 2a and Table 2). Notably, the resonances in the neat guaiacol are significantly narrower (FWHM values of 30–35 Hz) than those observed in the 13C CP MAS spectrum of Act-NatA-ZSM-5 (FWHM 200–500 Hz). This pronounced linewidth broadening is attributed to the reduced mobility of adsorbed guaiacol confined within the zeolite pores compared to their non-adsorbed counterparts. This broadening has similarly been observed in the 13C CP MAS spectra of zeolite occluded organic structure-directing agents when the line widths are compared to the liquid state NMR spectra of their in-solution counterparts.75

Table 2 Comparison of 13C δCS and FWHM between guaiacol in CDCl3 (Fig. S3), neat guaiacol (Fig. 2a) and Act-NatA-ZSM-5 (Fig. 2b)
Carbon number Guaiacol in CDCl3 Neat guaiacol (No solvent) Act-NatA-ZSM-5
δCS/ppm (±0.1 ppm) FWHM/Hz (±0.1 Hz) δCS/ppm (±1.0 ppm) FWHM/Hz (±1.0 Hz) δCS/ppm (±1.0 ppm) FWHM/Hz (±50 Hz)
a,bSignals not resolved.
2 146.7 1.5 148 29 143–150a 600a
7 145.7 1.3 147 28 143–150a 600a
5 121.5 1.3 122 27 118–125b 450b
4 120.2 1.3 121 30 118–125b 450b
6 114.7 1.6 115 28 114–118 340
3 110.9 1.7 112 27 110–114 250
1 55.9 1.2 56 26 53–57 250


Additional resonances at 13C δCS of 130 ppm and in the range 150–160 ppm are observed and are consistent with the formation of coke species on the zeolite catalysts.76,77 Specifically, the signal at 130 ppm is assigned to non-substituted aromatic coke, while the 150–160 ppm resonances are attributed to hydroxy- or methoxy-substituted aromatic coke species. This assignment is further confirmed by comparing this 13C CP MAS spectrum (Fig. 2b) with the one for Act300-NatA-ZSM-5 (Fig. 2c), in which only a broad resonance between 110 and 130 ppm remains. Under these more severe conditions, signals corresponding to the reactant guaiacol are significantly reduced or removed due to the longer exposure to high temperature, leaving predominantly coke-derived species. In addition, the 13C signals in the 15–20 ppm region (Fig. 2b), which are absent in neat guaiacol, are indicative of aliphatic carbon moieties associated with from coke precursor end groups.68

TGA-MS was employed to evaluate the nature of the various species confined within the pores in Am-NatA-ZSM-5, Ads94-NatA-ZSM-5 and Act-NatA-ZSM-5. The TGA-MS profile of Am-NatA-ZSM-5 (Fig. 3, brown) reveals a single mass loss at around 70 °C which quasi multiple ion detection (QMID, Fig. S4) attributes to the release of weakly adsorbed water (m/z = 18). In contrast, the TGA-MS data for Act-NatA-ZSM-5 (Fig. 3, red) shows 3 distinct regions of mass loss: the first, occurring near 75 °C, corresponds to the desorption of adsorbed water; the second, observed in the 130–250 °C temperature region, is ascribed to the removal of residual adsorbed guaiacol as evidenced by the detection of the corresponding m/z = 124 in the QMID data (Fig. S5); the final mass loss spans over a broad temperature range from 300 to 650 °C accounting for approximately 6% of the total sample weight is accompanied by a QMID ion current at m/z = 44 (Fig. S6), indicative of CO2 evolution and is consistent with complete combustion of coke formed during the guaiacol pyrolysis reaction over ZSM-5.29


image file: d6qm00172f-f3.tif
Fig. 3 (a) TGA curves and (b) first derivative of the TG curves (DTG) for Am-NatA-ZSM-5 (brown), Ads94-NatA-ZSM-5 (green) and Act-NatA-ZSM-5 (red).

The TGA-MS profile of Ads94-NatA-ZSM-5 (Fig. 3, green) shows 3 regions of mass loss. The first, appearing at around 100 °C, corresponds to the overlapping desorption of water (Fig. S7) and an initial loss of weakly adsorbed ex-pore guaiacol (Fig. S8). A secondary mass loss from 140–240 °C is attributed to more strongly adsorbed in-pore guaiacol molecules and closely matches the loss at 130–250 °C in Act-NatA-ZSM-5. The loss of guaiacol at two distinct temperature ranges and therefore binding strengths supports the 1H NMR data in the assignment of in- and ex-pore guaiacol in Ads94-NatA-ZSM-5. An additional broad mass loss is observed in the TGA profile of Ads94-NatA-ZSM-5 from 300 °C as observed in Act-NatA-ZSM-5 and this is suggested to be due to in situ pyrolysis in the TGA-MS during measurements.

Building on these observations, 17O MAS NMR experiments were performed on ZSM-5 enriched in 17O via a high temperature sintering process at 500 °C under a 17O enriched O2 atmosphere (see Experimental Section in the SI for details) and on guaiacol activated 17O enriched ZSM-5.64,78 GC–MS results of the guaiacol activated sample Act-17O(500)-ZSM-5 (Table S4) revealed product distributions comparable to those obtained for Act-NatA-ZSM-5 (Table 1). These similar results, particularly the high percentage of non-oxygenated products produced by 17O enriched ZSM-5 demonstrate that the zeolite sample remains catalytically functional and industrially relevant despite the extended high temperatures of the enrichment process. This is consistent with literature, where it was found that ZSM-5 samples which had been similarly exposed to high temperatures up to 600 °C showed comparable or even marginally improved catalytic performance for aromatization reactions.79 Importantly, the mass spectra of the activation products on the 17O enriched ZSM-5 showed no evidence of 17O incorporation, as indicated by the absence of (M + 1)+ signals relative to the unenriched samples. This confirms that isotopic exchange does not occur with the reactant or products under these experimental conditions.

The 17O MAS NMR spectra of Am-17O(500)-ZSM-5 acquired at two different external magnetic fields (Fig. 4a) show a significant field-dependent line narrowing and a shift to higher frequency at higher field capturing the inverse dependency of the second-order quadrupolar broadening with increasing field strength. Specifically, the spectral line width decreases from approximately 6.8 kHz (125 ppm) at 9.4 T to around 4.9 kHz (45 ppm) at 18.8 T, as expected. Nevertheless, MAS alone does not completely remove second-order quadrupolar broadening, which remain partially present at 18.8 T in these 17O MAS NMR spectra.


image file: d6qm00172f-f4.tif
Fig. 4 (a) and (b) 17O MAS and (c) and (d) 17O 2D MQMAS spectra recorded at B0 = 9.4 T of (a) and (c) Am-17O(500)-ZSM-5 (purple) and (b) and (d) Act-17O(500)-ZSM-5 (red). The 17O MAS spectra in (a) and (b) were acquired at the magnetic fields indicated; experimental spectra are shown as solid coloured lines, with corresponding simulations overlaid as black dashed lines. Asterisks (*) denote spinning sidebands. The black dashed boxes highlight regions associated the assigned Si–O–Al and Si–O–Si framework oxygen environments.

To further resolve overlapping oxygen environments, multiple-quantum magic angle spinning (MQMAS) experiments were exploited, correlating isotropic multiple quantum coherences with the partially averaged MAS signals. The 17O MQMAS spectrum of Am-17O(500)-ZSM-5 (Fig. 4c) is dominated by a single broad resonance. As this material was enriched using the 17O2 gas method, enrichment occurs predominantly on the Si–O–Si framework sites, consistent with significant dealumination of the zeolite as further supported by the 1H and 27Al NMR data (see below). The high temperatures required for oxygen exchange remove Si–O–Al sites leading to their substantial depletion. This lack of enriched Si–O–Al sites is not attributed to a slower exchange of this site compared to Si–O–Si sites, as the H217O enrichment method shows that O exchange typically occurs faster at the more labile Si–O–Al site.66 An isotropic chemical shift δCS value of 40.3 ± 0.7 ppm was determined for the Si–O–Si site by extracting the position of the centre of gravity of the resonances projected along the δ1 and δ2 dimensions of the sheared MQMAS spectrum (see Fig. 4c and Experimental Section details in the SI). Line shape simulations of the 17O MAS NMR spectra of Am-17O(500)-ZSM-5 17O spectra at 9.4 and 18.8 T (Fig. 4a, dashed black lines) were performed to simultaneously reproduce the experimental spectra at both magnetic fields, yielding quadrupolar parameters of quadrupolar coupling CQ = 5.3 ± 0.1 MHz and electric field gradient tensor asymmetry parameter ηQ = 0.15 ± 0.06. At both fields, though most notably on the experimental data at 9.4 T, the lower frequency horn of the second-order quadrupolar pattern is under excited relative to the simulations, an effect attributed to the non-uniform excitation across the powder pattern as encountered in quadrupolar nuclei.80

In addition to the dominant Si–O–Si resonance, the 17O MQMAS spectrum of Am-17O(500)-ZSM-5 (Fig. 4c) exhibits a weak secondary signal corresponding to Si–O–Al framework sites. At this 9.4 T magnetic field strength, Si–O–Al environments are expected to appear at a lower δ1 value than the Si–O–Si sites, typically around 50 ppm.63,67 A δCS value of 34.1 ± 1.5 ppm was extracted for the Si–O–Al site and a corresponding line shape simulation centred at δ1 = 50 ppm (Fig. S9a) yielded CQ = 3.8 ± 0.1 MHz and ηQ = 0.28 ± 0.03. These quadrupolar parameters are in excellent agreement with those in the literature for Na-ZSM-5 (Table 3).63 While the δCS determined here is slightly higher than some previously reported values, it lies well within the expected range expected for a Si–O–Al framework oxygen site.81

Table 3 Quadrupolar parameters of 17O sites determined for Am-17O(500)-ZSM-5 and Act-17O(500)-ZSM-5 in this work, compared with reported values for Na-ZSM-563 and dehydrated ZSM-564 from the literature
Source Site type δCS/ppm CQ/MHz ηQ
Am-17O(500)-ZSM-5 Si–O–Si 40.3 ± 0.7 5.3 ± 0.1 0.15 ± 0.06
Si–O–Al 34.1 ± 1.5 3.8 ± 0.1 0.28 ± 0.03
Act-17O(500)-ZSM-5 Si–O–Si 40.5 ± 0.3 5.3 ± 0.1 0.15 ± 0.06
Na-ZSM-563 Si–O–Si 40 5.3 0.12
Si–O–Al 30 3.5 0.29
Dehydrated ZSM-564 Si–O–Si 40.5 5.45 0.2


The 17O MAS NMR spectra of Act-17O(500)-ZSM-5 (Fig. 4b) exhibit chemical shifts, line shapes and field-dependent line narrowing comparable to those of the unreacted Am-17O(500)-ZSM-5. A δCS value of 40.5 ± 0.3 ppm was extracted for the Si–O–Si framework oxygen site from the sheared 17O MQMAS spectrum of Act-17O(500)-ZSM-5 (Fig. 4d). Line shape simulations fitted to the experimental spectra acquired at both magnetic fields gave CQ = 5.3 ± 0.1 MHz and ηQ = 0.15 ± 0.06. These δCS, CQ and ηQ values are strongly in agreement with those reported for the Si–O–Si sites of hydrated Na-ZSM-563 and dehydrated H-ZSM-564 (Table 3). In contrast, the minor Si–O–Al site observed in Am-17O(500)-ZSM-5 is almost entirely lost upon guaiacol pyrolysis, as shown by the isotropic projection of the MQMAS spectrum at δ1 = 50 ppm (Fig. S9 and S10). This loss of the Si–O–Al framework oxygen site is most likely attributable to the second high temperature heat treatment applied during the activation process.

The 27Al MAS NMR spectra of Am-NatA-ZSM-5 and of the various 17O enriched ZSM-5 samples (Fig. S11) display two main signals at 54 and 0 ppm, assigned tetrahedrally coordinated framework aluminium and octahedrally coordinated extra-framework aluminium, respectively.82,83 As the enrichment temperature is increased from 300 to 500 and 700 °C, the relative intensity of the tetrahedral framework Al signal decreases, accompanied by a corresponding increase in the octahedral extra-framework Al resonance, consistent with thermodynamically driven framework dealumination.79 At the highest temperature, an additional resonance emerges at 30 ppm which is tentatively attributed to 5-coordinate aluminium species.84 With increasing enrichment temperature, all 27Al resonances display continuous line broadening, reflecting an increased distribution of local aluminium environments within the zeolite framework.

The 29Si MAS NMR spectra of the same materials (Fig. S12) show broad resonances from −110 to −120 ppm, accompanied with a shoulder at −105 ppm. The dominant resonance between −110 to −120 ppm is assigned to Si(4Si) environments, in which each Si is bonded to four neighbouring Si atoms via O bonds, while the shoulder corresponds to Si(3Si,1Al) environments, where one of the neighbouring Si atoms is replaced by an aluminium. In principle, the Si/Al ratio could be extracted from these 29Si NMR spectra,85 however the substantial overlap between the Si(4Si) and Si(3Si,1Al) resonances arising from chemical shift distributions across the 24 crystallographically non-equivalent silicon sites preclude reliable quantitative deconvolution.86,87

As the 17O enrichment temperature increases, the relative intensity of the −105 ppm 29Si resonance for the Si(3Si,1Al) environment decreases with respect to the main Si(4Si) signal, indicative of progressive removal of aluminium from the zeolite framework.85 This trend is fully consistent with the disappearance of the Si–O–Al signal observed in the 17O MAS NMR data. Together, 27Al and 29Si MAS NMR data results demonstrate that dealumination is minimal at enrichment temperatures up to 300 °C, but becomes significant at 500 °C (and above), although both datasets show that not all of the framework aluminium has been removed. This structural modification of the ZSM-5 zeolite framework results in the loss of BAS without significantly altering catalytic activity, as evidenced by the comparable product distributions from the non-enriched and enriched samples (Table 1 and Table S4). This has been rationalised by the formation of the octahedral extra-framework Al species, which acting as Lewis acid sites have been suggested to compensate for the loss of Brønsted acidity.79,88

The 1H MAS NMR spectrum of Am-NatA-ZSM-5 (Fig. 1a) is dominated by a broad resonance at 5.5 ppm which results from the rapid proton exchange between adsorbed water with any present OH groups and hydroxonium ions.34,89 This signal can obscure the observation of other resonances in the spectrum, therefore 1H MAS NMR spectra were also recorded for dehydrated ZSM-5 samples maintained in an inert atmosphere. Dehydration was performed by gradually heating the samples to 300 °C, a temperature chosen to minimise dealumination as per the observation for the 27Al and 29Si NMR experimental spectra. Upon dehydration (Fig. 5a), additional resonances become apparent at 3.9, 2.4 and 1.6 ppm with the highest resonating signal at 3.9 ppm assigned to BAS consistent with the expected chemical shift range of 3.9–4.2 ppm.90 The resonance at 2.4 ppm is attributed to Al–OH aluminol species while the signal at 1.6 ppm corresponds to Si-OH silanol groups.74,91,92 In contrast, the 1H MAS NMR spectrum of De-17O(700)-ZSM-5 (Fig. 5b) shows a complete absence of resonances in the regions corresponding to the BAS and AlOH sites, with only silanol signals remaining. Additionally, there are broad signals from 9 to 2 ppm and 2 to −3 ppm which are attributed to strongly bound water90,91 and the probe background signal respectively (Fig. S13). Take together with the 27Al and 29Si NMR data, these results indicate that dealumination in the 17O enriched samples is sufficiently extensive that Si–O–Al linkages are present at concentrations below the detection limit to be observed by 17O NMR experiments.


image file: d6qm00172f-f5.tif
Fig. 5 1H MAS NMR spectra acquired at B0 = 20.0 T and with νr = 16 kHz for (a) De-NatA-ZSM-5 and (b) De-17O(700)-ZSM-5. The less intense signals observed between 0 to 1.2 ppm are attributed to residual vacuum grease.93

2D 1H–17O D-HMQC spectra of Act-17O(500)-ZSM-5 (Fig. 6) were recorded with multiple recoupling times ranging from 0.75 to 6.0 ms and the evolution of the correlation intensities as a function of recoupling time was plotted (Fig. 6b, coloured points) to provide a quantitative estimate of the 1H–17O heteronuclear dipolar coupling constant. Maximum signal intensity was observed at an intermediate recoupling time of 2.25 ms (Fig. 6a) which clearly reveals correlations between the 17O resonance centred at around 30 ppm and the 1H signals at 6.9 ppm (guaiacol aromatic protons, Fig. 1g), 3.9 ppm (methoxy protons), and 2.3 ppm (aliphatic coke precursor). As only Si–O–Si bridging oxygen sites are detectable in this sample following activation at 500 °C, these correlations can be unambiguously assigned to the spatial proximities between framework Si–O–Si oxygen atoms and confined (in-pore) guaiacol and derived species.


image file: d6qm00172f-f6.tif
Fig. 6 (a) 2D 1H–17O D-HMQC spectrum of Act-17O(500)-ZSM-5 with a recoupling time of 2.25 ms at B0 = 23.5 T and νr = 16 kHz. The internal projections (red) and the corresponding 1H and 17O MAS NMR spectra (black) are also shown. (b) 1H signal amplitude build-up curves of Act-17O(500)-ZSM-5 in the 2D 1H–17O D-HMQC spectra (at 17O shift = 30 ppm) as a function of recoupling times for signals at 6.9 (red), 3.9 (green) and 2.3 ppm (blue). SIMPSON numerical simulations of the build-up curves for a two-spin 1H–17O system with a dipolar coupling constant of 130 ± 15 Hz and an additional 1H spin with a dipolar coupling constant of 300 Hz are shown in solid black line, with dashed lines corresponding to 1H–17O dipolar coupling constants boundaries of 115 and 145 Hz.

The experimental build-up curves were compared with numerical simulations of a simplified 1H–17O spin system. Although guaiacol confined within ZSM-5 represents a structurally and dynamically complex environment to simulate, a satisfactory reproduction of the experimental behaviour for all three experimental resonances was obtained using a three-spin model comprising two 1H nuclei and one 17O nuclei (of the Si–O–Si bridging oxygen sites), using a 1H–17O heteronuclear dipolar coupling constant of 130 Hz and a 1H–1H homonuclear dipolar coupling constant of 300 Hz (Fig. 6b, Fig. S14). In the absence of dynamic averaging, a 1H–17O dipolar coupling constant of 130 Hz corresponds to an internuclear distance of 5.0 Å which is comparable to the diameter of the straight channels in ZSM-5, and is therefore too long to indicate a fixed, short-range contact between guaiacol (or derivatives) and Si–O–Si framework oxygen sites. Instead, it likely suggests that guaiacol remains mobile within the pore, the extracted dipolar coupling constant representing a motionally-averaged coupling under confined conditions. While 1H–17O D-HMQC experiments have previously provided structural insight into zeolite frameworks,67 the data presented here suggest that 17O nuclei can additionally serve as sensitive probes of host–guest interactions, enabling evaluation of molecular confinement within microporous catalysts.

Conclusions

This work demonstrates that 17O isotopic enrichment, combined with solid-state MAS NMR spectroscopy, provides deeper understanding of the interactions between oxygenated biomass-derived molecules and zeolite frameworks. Using guaiacol as a representative lignocellulosic bio-oil mimic in ZSM-5, multinuclear NMR experiments reveal the retention of guaiacol following catalytic activation, clearly distinguishing in-pore and ex-pore molecules, and identifying the formation of aromatic and aliphatic coke precursors. 1H MAS NMR experiments differentiate in-pore guaiacol from ex-pore species through characteristic larger chemical shifts, broader NMR lines and faster relaxation rates. 13C MAS NMR and TGA-MS data confirm the presence of confined adsorbed guaiacol and aromatic coke in guaiacol activated ZSM-5.

Additionally, 1H, 27Al and 29Si MAS NMR spectra highlight the extent of dealumination induced by the high temperature enrichment process. 17O MAS, MQMAS, and 1H–17O D-HMQC experiments probe framework oxygen environments, their interactions with in-pore guaiacol and confinement effects. These results establish 17O solid-state NMR spectroscopy as a powerful approach for investigating host–guest interactions in zeolite catalysts, providing molecular-level insight to support the rational design of improved catalysts for biomass conversion and deoxygenation.

Author contributions

Kyle A. Watson: writing – original draft, visualization, validation, project administration, methodology, investigation, formal analysis, conceptualization. Ming-Feng Hsieh: writing – review & editing, resources, supervision, methodology, investigation. Stephen Day: writing – review & editing, supervision, project administration, methodology, conceptualization. Luke Tuxworth: writing – review & editing, supervision, project administration, methodology, funding acquisition, conceptualization. Frédéric Blanc: writing – review & editing, validation, supervision, project administration, methodology, funding acquisition, conceptualization.

Conflicts of interest

The authors declare no competing financial interest.

Data availability

The research data supporting this publication are accessible from the University of Liverpool Data catalogue: https://doi.org/10.17638/datacat.liverpool.ac.uk/3086.

Supplementary information (SI): free of charge online. Additional information includes experimental details, extended 1H FWHM, T1 and T2 parameters, further 1D and 2D NMR spectra, GC–MS results and TGA-MS QMID traces. See DOI: https://doi.org/10.1039/d6qm00172f.

Acknowledgements

K. A. W. thanks Johnson Matthey and the Engineering and Physical Sciences Research Council (EPSRC) for funding an Industrial CASE PhD studentship under EP/X524955/1. The UK High-Field Solid State NMR Facility at 850 MHz and 1 GHz used in this research was funded by EPSRC and BBSRC (EP/T015063/1) as well as the University of Warwick including via part funding through Birmingham Science City Advanced Materials Projects 1 and 2 supported by Advantage West Midlands (AWM) and the European Regional Development Fund (ERDF), as well as, for the 1 GHz instrument, EP/R029946/1. F. B. also thanks the EPSRC for upgrading the 800 MHz spectrometer at the University of Liverpool (EP/S013393/1) and for funding the purchase of 17O enriched O2 gas used in this work (EP/K031511/1), also supported by a Royal Society of Chemistry Research Fund Grant (R21-2293948533). Collaborative assistance from the Facility Manager Team (Dr Dinu Iuga and Dr Paolo Cerreia Vioglio, University of Warwick) is acknowledged. Glyn Connolly, Richard Roberts and Zidane Mdarhri of the University of Liverpool are thanked for assistance and helpful discussions with TGA-MS and GC–MS experiments, and for technical assistance in obtaining the 1H background spectra at 850 MHz, respectively. Emma Softley and Rob Fletcher of Johnson Matthey, Billingham are thanked for the argon physisorption analysis.

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