Carmen
Fernández-Conde
a,
Yongkun
Zheng
b,
Marta
Mon
b,
Antonio
Ribera
c,
Antonio
Leyva-Pérez
*b and
Carlos
Martí-Gastaldo
*a
aInstituto de Ciencia Molecular, Universitat de València, c/Catedrático José Beltrán, 2, 46980, Paterna, Spain. E-mail: carlos.martiuv.es
bInstituto de Tecnología Química UPV-CSIC, Universitat Politècnica de València-Consejo Superior de Investigaciones Científicas, Avenida de los Naranjos s/n, 46022, Valencia, Spain. E-mail: anleyva@itq.upv.es
cDepartament de Química Inorgànica, Universitat de València, c/Dr. Moliner, 50, 46100, Burjassot, Spain
First published on 14th December 2023
Among the multiple applications of metal–organic frameworks (MOFs), their use as a porous platform for the support of metallic nanoparticles stands out for the possibility of integrating a good anchorage, that improves the stability of the catalyst, with the presence of a porous network that allows the diffusion of substrates and products. Here we introduce an alternative way to control the injection of Au nanoparticles at variable stages of nucleation of a titanium(IV) MOF crystal (MUV-10). This allows the analysis of the different modes of nanoparticle integration into the porous matrix as a function of the crystal formation stage and their correlation with the catalytic performance of the resulting composite. Our results reveal a direct effect of the stage at which the Au nanoparticles are integrated into MUV-10 crystals not only on their catalytic activity for the cyclotrimerization of propargyl esters and the hydrochlorination of alkynes, but also on the selectivity and recyclability of the final solid catalyst, which are far superior than those reported for the same reactions with TiO2 supports.
Regarding metal nanoparticles (MNPs), their integration into porous platforms as zeolites, mesoporous silica or activated carbons is often used to prevent their aggregation and catalytic inactivation.6 In the case of molecular frameworks, this route can also benefit from better control of the confinement effects and tailorable interaction with the surface chemistry of the host, both useful in modifying MNP activity for superior catalytic performance.7 Compared to the “ship in a bottle” approach, which involves direct impregnation, the “bottle around ship” or template synthesis method enables the limitations imposed by the porosity metrics of the host on the size of the nanoparticle to be overcome (Fig. 1a). This route relies on the nucleation and growth of MOF crystals by reaction of their molecular components in the presence of surfactant stabilized MNPs, provided that the synthetic conditions used do not prevent the assembly of the framework. This strategy has been used to gain exquisite control over the spatial distribution of the encapsulated nanoparticles and their chemical environment in nanocrystals of MOFs such as ZIF-8,8–10 IRMOF,11,12 HKUST13 or UiO-66,14,15 between 100 and 500 nm in size.
Fig. 1 Comparison of (a) static and (b) time-resolved (this work) methods for encapsulating nanoparticles in MOF crystals. |
These precedents inspired us to explore alternative routes to control the integration of pre-synthesised MNPs in MOF crystals of micrometric size. To this end, we have adapted the solvothermal synthesis of titanium MOFs under static conditions as an alternative method that enables continuous injection of molecular precursors at a fixed concentration and comparatively shorter reaction times for more homogeneous crystal size distributions. This new method is well suited to gain dynamic control over the injection of MNPs at variable nucleation and crystal growth stages for varying degrees of integration in the resulting MNP@MOF hybrid crystal composites (Fig. 1b). Since one of the main applications of MNPs is catalysis,16,17 we next use the time-resolved encapsulation method to analyse the effect of the injection time on the performance of the resulting catalyst associated with changes in reactant accessibility and/or the chemical nature of the MNP surface.18 Our results reveal changes in conversion, selectivity and catalyst recyclability for the Au-catalyzed cyclotrimerization of propargyl esters19 and the hydrochlorination of alkynes,20 confirming the potential of controlling the injection of nanoparticles at adjustable times for composites with superior catalytic performance.
The solvothermal synthesis reported originally was adapted to a dual syringe infusion pump for the separate injection of stock solutions of CaCl2 and Ti(OiPr4) dissolved in a mixture of DMF and acetic acid, and the linker (H3BTC = benzene-1,3,5-tricarboxylic acid) dissolved in DMF. Both solutions were continuously injected into a round bottom flask preheated at 120 °C under an inert atmosphere and constant stirring. As shown in Fig. 2b, the initial injection feed rate of 20 mL h−1 (t1) was gradually decreased (t2–t4) down to a minimum of 6 mL h−1 (t5). From this point, the reaction was let to proceed for 24 hours without further injection of reagents (t6). This experimental design ensures a constant linker to metal ratio with negligible changes in reaction volume during the nucleation process. A similar approach has been used previously to synthesize nanoparticles of various MOFs with different chemistries for narrow particle size distributions in all cases.23 As shown in Fig. 2c, the concentration of added reagents and their ratio remain constant despite a progressive reduction of the injected volume throughout the process (t1 to t5). Although both the concentration of acetic acid acting as a modulator and the L:M ratio are the same as those used in the solvothermal synthesis reported, the concentration of the linker and metal precursors used was 1000 times higher. We argued that this supersaturation would result in increased nucleation and faster crystal growth rates at a fixed reaction temperature for better control of crystal size and morphology.24 According to our tests, a continuous injection of reagents at a low feed rate seems to facilitate the formation of crystals with much more homogeneous size than faster injections (ESI Section S2.1†). For additional information, all synthetic details are summarized in ESI S2.†
After the reaction was completed at t6, the mixture was left to cool down to room temperature and the material was recovered by centrifugation and washed thoroughly with DMF and methanol before analysis. Scanning electron microscopy (SEM) images confirm the expected octahedral morphology for the MUV-10 crystals prepared by time-resolved synthesis, which also present a more homogeneous size dispersion centered at 2 μm, compared to the polydispersity obtained with conventional synthesis (Fig. 3a). On a related note, we also analysed separate aliquots over the 24 hours of reaction to account for the effect of time on the crystal sizes to confirm that this reaction time provides the most homogeneous size dispersion of micrometric crystals (Table S4†).
One of the main difficulties in controlling the formation of titanium–organic frameworks is the tendency of titanium(IV) in solution to form amorphous oxides by hydrolysis reactions which are difficult to control.25 This reaction competes with the formation of the MOF and could lead to the formation of amorphous species, rich in titanium but undetectable by X-ray diffraction, which would contaminate the bulk material.26 This risk is even higher in an open synthesis system with continuous injection of reagents despite the inert atmosphere. Single-point energy dispersive X-ray (EDX) and ICP-MS analysis of the time-resolved sample rules out this possibility and confirms a Ti:Ca ratio that matches the stoichiometry of the Ti2Ca2 cluster, and does not present significant deviations with respect to the material prepared under static conditions (Fig. 3b and ESI 2.2, Table S5†). The powder X-ray diffraction (PXRD) pattern of the ground crystals also confirms the formation of a crystallographically pure phase corresponding to the simulated structure of the material, which shows no significant differences with respect to that of the material prepared under static conditions (Fig. 3b). The Le Bail refinements of the PXRD patterns of both samples confirm minimal deviations in the cell parameters (ESI Section S2.2, Fig. S2†). Finally, we tested the adsorption capacity of the material by N2 uptake at 77 K after thermal vacuum activation of the washed solid. Fig. 3c confirms that the synthetic method has no effect on the gravimetric surface area, which remains close to 1000 m2 g−1 in both cases. The pore size distribution (PSD) plot shows a broad contribution centered at around 1.1 nm, corresponding to the overlap of the octahedral and cuboctahedral cavities of a very similar size in the MUV-10 framework (Fig. 2a).
These results confirm time-resolved synthesis by continuous injection of molecular precursors to be a method compatible with the synthesis of MUV-10 crystals which, in addition to reducing reaction times from 48 to 24 hours, also results in better control of particle size possibly as a result of maintaining the supersaturation conditions throughout the synthesis.
Fig. 4 (a) Scheme showing the times for which an aliquot of the material formed during the time-resolved synthesis is extracted according to the procedure described in Fig. 2b. (b) SEM images of the isolated solids at t1, t3 and t5. (c) Variations in the proportions of metals in the solids before (t1, t3, and t5) and after the injection of Au nanoparticles until complete crystal growth (Au@t1, t3, and t5). (d) Diffraction patterns and (e) gas uptake isotherms of all materials confirming the formation of MUV-10 with the expected structure and porosity after Au injection in all cases. (f) Color gradient in the Au@MUV-10 samples compared to that of the material without gold (top) and changes in particle size and morphology as a function of the addition time (bottom). (g) TEM analysis of Au@MUV-10 crystals before (top) and after microtoming them into 0.5 μm thick slices for facilitating the visualization of the nanoparticles (bottom). |
This information suggests the presence of three different stages of MUV-10 formation, which we will refer to as amorphous (t1, A), incipient (t3, I) and fully formed (t5, FF). This differentiation between MOF formation states seemed appropriate to study the effect of injecting NPs and analysing their impact on the formation of the final material and possible variations in the distribution of nanoparticles in the resulting crystals. For this purpose, we synthesized Au nanoparticles of sizes between 15 and 20 nm stabilized with polyvinylpyrrolidone (PVP) by following the Turkevich method (ESI Section S3.1†).27 By introducing an additional pump in the scheme shown in Fig. 2b for a third addition channel, we injected 1 mL of a freshly made solution of Au NPs [0.35 mM] in methanol at the points t1, t3 or t5 with a fixed injection feed rate of 20 mL h−1. All reactions were performed according to the reagent injection rates described in the above procedures, followed by a reaction time of 24 hours to ensure a meaningful comparison between the resulting Au@MUV-10 materials.
The first piece of experimental evidence of the incorporation of the nanoparticles is the purple colour of all the materials isolated compared to white MUV-10 (Fig. 4f top). It is worth noting their relative variations in color that seem to indicate either different amounts of Au loaded or changes in its distribution within the solid. To confirm this possibility, the Au@MUV-10 solids were analysed by ICP-MS after digestion in an acid medium. The results confirm the presence of comparable amounts of gold in all samples, with values ranging from 161 to 240 ± 3 ppm. However, the samples show significant differences in particle size and morphology depending on the point at which the nanoparticles were injected. According to the SEM analysis shown in the same figure (Fig. 4f bottom), the most abrupt change is observed for Au@t1, which presents particles much smaller than 1 μm. This suggests a possible effect of the addition of NPs on the early stages of MUV-10 nucleation for the formation of smaller crystals. This effect is much less pronounced in Au@t3 and t5, possibly because the injection has already taken place on crystals with fairly advanced growth, consistent with the characteristics of incipient and fully formed states of formation of the MOF that correspond to these points as described above. We argue that these changes in particle size for comparable Au loadings result in changes in the density of nanoparticles per crystal that translate into the observed colour intensity changes.
To confirm the incorporation of the nanoparticles into the MUV-10 crystals, the samples were also analyzed by transmission electron microscopy (TEM). Compared to similar studies on the encapsulation of NPs between 100 and 500 nm in MOFs,8–15 the high contrast of the crystals and the smaller size of the nanoparticles made the analysis more challenging, especially in the case of Au@t1 for which we did not observe NPs in any of the crystals examined compared to their presence in t3 and t5 (Fig. 4g top). To simplify the analysis and improve the transmittance of the samples, we microtomed them into ≈0.5 μm thick slices which were then deposited on the mesh grid for TEM analysis by following the same protocol reported for the spectroscopic analysis of UiO-68 lamellae at the nanoscale.28 The bottom part of Fig. 4g confirms the presence of NPs in the sections of all crystals, although more clearly in Au@t1 and t3. In the case of t1, where their presence was not evident before the crystal was cut, the high density observed also seems to support the hypothesis that their incorporation takes place in the early stages of MUV-10 formation, relegating the nanoparticles to the inner core of the crystal. This was further confirmed by focused ion beam scanning electron microscope (FIB-SEM) analysis (Fig. S19†). These relative differences between materials are not reflected in their bulk properties. All Au@MUV-10 solids show minimal compositional variations with Ti:Ca ratios close to those expected for MUV-10 (Fig. 4c). Their PXRD patterns are also consistent with the formation of the framework without significant variations in their crystallinity or diffraction lines indicative of the formation of an additional phase (Fig. 4d). The N2 isotherms are also consistent with the behavior expected for MUV-10, with total pore volumes of 0.4 cm3 g−1 and non-hysteretic type I adsorption profiles (Fig. 4e). Au@t1 is the only system that shows a small adsorption tail at P/P0 > 0.9, due to the smaller particle size and corresponding intergrain mesoporosity.
We chose to test their ability to activate electron deficient alkynes during the cyclotrimerization reaction of propargyl esters, using 1,2-dichlorobenzene (o-DCB) as a solvent, to forge three new C–C bonds in one pot (Fig. 5a). The experiments were carried out by reacting ethyl propiolate at 120 °C under mechanical stirring in the presence of 0.2 mol% Au NPs encapsulated as Au@t1, t3 or t5 materials. The results after 20 hours (GC-FID analysis, see also Scheme S1 and Table S12†) show that the three materials have very different catalytic activities: while Au@t1 shows a consistent 60% conversion and 10:1 selectivity towards the 1,2,4- (1a) vs. the 1,3,5-trisubstituted isomer product (1b) during 5 reuses, Au@t3 only achieves a ∼45% conversion and ∼5:1 selectivity (products 1a:1b) under the same reaction conditions, and Au@t5 significantly loses catalytic activity and selectivity throughout the reuses, to give ∼30% yield and ∼1:1 selectivity in the fifth use. The chemical structure of the products 1a:1b was confirmed by combined gas chromatography-mass spectrometry (GC-MS) and 1H- and 13C-nuclear magnetic resonance (NMR) analyses.24 These results, obtained with 0.05 mmol of organic substrate, are consistent with those of experiments at other scales (Fig. S25†). It is noteworthy here that the catalytically active surface Au atoms on a 20 nm NP account for just 5% of the total Au atoms,30 and thus the true catalytic loading of Au in the reaction is 0.01 mol% and the turnover number (TON) of the reaction with Au@t1 after 5 cycles is 30000, two orders of magnitude higher than that of any other metal NP or cluster catalyst reported so far for this reaction, either under heterogeneous or homogeneous conditions, as far as we know (Table S13†).31–33 Considering that previous studies with the Au–TiO2 catalyst suggests that the electron-richest the Au NP is, the highest catalytic activity is found,29,34 it is not surprising that the encapsulated Au NPs in the electron-rich MUV-10 MOF show an enhanced catalytic activity.
The above results suggest a relationship between the way in which the Au NPs are integrated into the porous support and not only the catalytic activity, but also the selectivity and recyclability of the final solid catalyst.35 The latter displays better endurance when Au NPs are concentrated in the innermost areas of the crystal (Au@t1) compared to the significant loss of activity for Au@t5. In order to check this hypothesis, two new materials prepared in the same way as Au@t1 but with 10× and 5× times higher Au loadings were prepared and tested in catalysis (see ESI Sections S3.3 and S4.1†). The results (Table S12†) confirm that when Au NPs are not completely integrated into the MOF structure, the product 1a:1b selectivity decreases to ∼3:1, values similar to those obtained with Au NPs supported on TiO2 (ref. 29) and also the value observed here for unsupported Au NPs (Table S12†). Indeed, this ∼3:1 selectivity value is, in average, the selectivity observed for the less stable Au@t5 catalyst. In other words, one can conclude that the stability conferred by the MUV-10 MOF framework to the encapsulated Au NPs is essential to achieve a very good catalytic activity (60%), selectivity (10:1) and recyclability (5 uses without catalytic activity depletion). Hot filtration tests (Fig. S26†) showed that there is no catalytic active species in the solution during the reaction for any of the Au@t1–5 MOF catalysts, and thus leaching does not occur and cannot explain the catalytic differences observed between the solid materials.
In order to confirm if the encapsulation of the Au NPs at different stages of MUV-10 MOF formation translates in a high catalytic activity for other organic reactions, we decided to test catalysts Au@t1, Au@t3 and Au@t5 for the hydrochlorination reaction of phenylacetylene (0.25 mol% Au, Fig. 5b).36 This reaction has been reported to be catalyzed by 3 nm diameter size Au NPs supported on TiO2 (ref. 20 and 37) but not by any other solid catalyst or metal NP-based catalyst, as far as we know. The lack of solid metal catalysts for the hydrochlorination reaction is not surprising since the highly aggressive HCl reactant favors leaching of the metal, although the industrially relevant hydrochlorination reaction of acetylene to manufacture vinyl chloride can be performed with Au species supported on activated charcoal supports.37 Here, having in mind the larger size of our Au NPs (20 nm) and their strong encapsulation within the MOF, the leaching could be minimized while the catalytic activity could be tuned by the Au NP/MUV-10 MOF composite structure. Indeed, the results show that, as in the previous reaction, the conversion and selectivity for products 2a:2b follows the order Au@t1 (67%) > Au@t3 (42%) > Au@t5 (41%) (Fig. 5b, for results at five times lower scales see Fig. S27†). GC-MS and NMR analyses confirmed the structure of products 2a:2b.20 However, only Au@t3 was reusable with constant conversion and major selectivity to the Markovnikov product (2a:2b 4:1). If we consider again that only 5% of Au atoms are available on the surface of the 20 nm Au NPs, probably much less because of the tight MOF-Au NP interaction, the catalytic activity must be one order of magnitude higher than that of the supported 3 nm Au NPs, where 38% of Au atoms are available on surface. As for the previous reaction, we performed new experiments to confirm the negligible activity of unsupported Au NPs and the lack of significant leaching as assessed by hot filtration tests, to support the heterogeneous nature of the catalytic reaction (Table S14 and Fig. S28†). At this point, the origin of the decrease in catalytic activity found for the Au@t1 and Au@t5 catalysts throughout the reuses is not clear; however, a tentative explanation would be the competitive polymerization of phenylacetylene on the MOF catalyst under acidic reaction conditions, which might block the access of the reactants to the encapsulated Au NPs.
Our preliminary results suggest that the time-resolved synthesis of MUV-10 can be adapted to other titanium(IV) MOFs and additives in solution for the design of composites of very diverse nature and range of applications.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3sc04678h |
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