The synthesis of the heterogeneous UiO-66/Sal-ZnCl2 nanocatalyst was successfully accomplished through a three-step process. Initially, UiO-66-NH2 was synthesized by combining ZrCl4 and 2-aminoterephthalic acid. Subsequently, the -NH2 groups were chemically reacted with salicylaldehyde in a post-modification step, resulting in the formation of UiO-66/Sal. Finally, the coordination of ZnCl2 salt with UiO-66/Sal led to the creation of UiO-66/Sal-ZnCl2, as illustrated in Fig. 1. Comprehensive characterization of the UiO-66/Sal-ZnCl2 structure was performed using various techniques, including ICP, FT-IR, TGA, BET, TEM, SEM, EDX, and XRD, as detailed in this section.
The quantification of zinc ions on the UiO-66/Sal-ZnCl2 nanocatalyst was conducted through ICP-OES analysis. The zinc concentration was determined to be 0.5 wt.% of the catalyst.
The chemical structure and functional groups of UiO-66-NH2, UiO-66/Sal, and UiO-66/Sal-ZnCl2 were examined via FT-IR analysis, as depicted in Fig. 2. For UiO-66-NH2 (Fig. 2a), peaks at 3458 and 3348 cm-1 were assigned to asymmetric and symmetric vibrations, while the 1658 cm-1 peak indicated the bending vibration of NH2 groups. The symmetric and asymmetric stretching vibrations of carboxyl groups associated with Zr4+ were observed at 1580 and 1386 cm-1, respectively. A peak at 1509 cm-1 corresponded to the stretching vibration of C = C units in benzene rings, while the shear vibration of N-H groups appeared at 1436 cm-1. Additionally, a unique C-N stretching absorption of aromatic amines was evident at 1262 cm-1. Peaks at 768 and 662 cm-1 were attributed to the stretching vibration of µ3-O in Zr-(OC) [43, 44]. After salicylaldehyde modification of UiO-66-NH2, the characteristic amine group peaks disappeared (Fig. 2b), and the peaks at 1580 and 1262 cm-1 sharpened due to the formation of C = N bonds of salicylidene imine [45, 46], indicating successful post-modification. Notably, the FT-IR spectrum of UiO-66/Sal-ZnCl2 (Fig. 2c) did not exhibit characteristic peaks of ZnCl2, possibly due to the weak bands associated with immobilized zinc ions on the nanocatalyst's surface [47].
The crystalline structure of UiO-66-NH2 and UiO-66/Sal-ZnCl2 was investigated using XRD analysis within the 2θ range of 6–80° (Fig. 3). The XRD pattern of UiO-66-NH2 (Fig. 3a) displayed characteristic diffraction peaks at 2θ values of 7.5°, 8.7°, 14.6°, 17.5°, 22.3°, 25.6°, 30.5°, 31.2°, 35.9°, 37.8°, 40.2°, 43.5°, 50.6°, and 56.9°, corresponding to the crystal lattice with Fm3m symmetry of zirconium benzene carboxylate units [48]. These diffraction peaks were also observed in the XRD pattern of UiO-66/Sal-ZnCl2 (Fig. 3b), indicating that the catalyst's crystalline structure remained unchanged after modification and coordination of zinc units on the surface. The characteristic peaks of ZnCl2 should be at 2θ of 16.2°, 17.2°, 26.0°, 29.9°, 35.5°, 38.9°, 49.3°, 49.8°, 51.9°, 52.9°, and 56.8° (JCPDS card no. 96-810-3830) [49] (Trivedi et al., 2017), however the intensity of these expected peaks was quite low, likely due to the results from the ICP analysis and the relatively low metal loading.
As depicted in Fig. 4, the elemental composition of UiO-66-NH2 and UiO-66/Sal-ZnCl2 was determined through EDX analysis. In the EDX spectrum of UiO-66-NH2 (Fig. 4a), signals corresponding to Zirconium (Zr), Oxygen (O), and Nitrogen (N) were observed, representing the primary elements of the intended MOF structure [50]. In the case of UiO-66/Sal-ZnCl2 EDX analysis (Fig. 4b), these expected elements (Zr, O, and N) were again observed, alongside the presence of elemental zinc and chlorine [50].
Following the elemental composition analysis, the distribution of these elements on the catalyst's surface was examined. Figure 5 presents the X-ray elemental mapping of UiO-66/Sal-ZnCl2, demonstrating the even dispersion of elements within the catalyst framework. Zirconium (Zr), being the fundamental building block with a considerably higher density compared to other elements, exhibited a uniform distribution. This observation further underscores the crucial role of uniform zinc (Zn) distribution within the catalyst matrix, which contributes significantly to its exceptional catalytic performance. These observations are in agreement with ICP and EDX analyses and confirm the successful coordination of Zn complexes onto the surface of modified MOF.
In order to ascertain the loading capacity of the organic linker and examine the thermal stability of UiO-66-NH2 and UiO-66/Sal-ZnCl2, thermal gravimetric analysis (TGA) was conducted across a temperature range spanning from 25 to 700°C (Fig. 6). Three weight losses were observed in the thermogravimetric analysis (TGA) curve of UiO-66-NH2, as depicted in Figure (Fig. 6a). The initial weight reduction step, occurring up to 150°C, involved the removal of trapped water, solvent, and CO2 molecules. During the second phase of weight loss, occurring at temperatures exceeding 180°C, the organic linker initiates decomposition. The third stage of weight loss, occurring between 350°C and 500°C, can be attributed to the complete disassembly of the framework. In the case of UiO-66/Sal-ZnCl2, a greater weight loss was observed during this stage compared to UiO-66-NH2, primarily due to the presence of a surface-bound organic linker (Fig. 6b) [51]. From these results, the amount of organic linker was estimated to be about 6% by weight These results are in accordance with other analyses approve the successful synthesis and post-synthetic modification of UiO-66.
The porous structures of UiO-66-NH2 and UiO-66/Sal-ZnCl2 were characterized using N2 adsorption-desorption analysis (Fig. 7). According to Brunauer-Emmett-Teller (BET) calculations, the surface areas of UiO-66-NH2 and UiO-66/Sal-ZnCl2 were determined to be 909.59 and 550.11 m2g− 1, respectively (Fig. 7a, 7b). This reduction in surface area for UiO-66/Sal-ZnCl2 compared to UiO-66-NH2 suggests that the post-modification and coordination steps involving ZnCl2 primarily occurred on the support surface. The adsorption-desorption isotherm of UiO-66-NH2 displayed a type I isotherm, indicative of a microporous structure (Fig. 7a). The Barrett-Joyner-Halenda (BJH) diagram for UiO-66-NH2 revealed the presence of a single type of micropores with a pore diameter of 1.21 nm (Fig. 7c). Similarly, the BJH plot for UiO-66/Sal-ZnCl2 also indicated reduced-intensity micropores, consistent with changes in surface area and pore filling resulting from the coordination of the zinc salt (Fig. 7d) [51].
In the TEM image of UiO-66-NH2 (Fig. 8a), one can observe aggregated octahedral particles measuring less than 50 nm in size. Interestingly, the TEM image of UiO-66/Sal-ZnCl2 (Fig. 8b) displayed an identical morphology, suggesting that the post-modification of the (MOF with salicylaldehyde and the coordination of zinc units did not have any discernible impact on the MOF's morphology. Furthermore, SEM images (Figs. 8d & 8e) supported these findings, confirming the preservation of the MOF's morphology throughout the modification and coordination processes.
Following the successful synthesis and characterization of UiO-66/Sal-ZnCl2, its catalytic activity was evaluated in a one-pot multicomponent reaction involving benzyl halides/alkyl halides, phenylacetylene/propargyl alcohol, and sodium azide for the synthesis of 1,2,3-triazole, as depicted in Fig. 9.
In this specific context, a thorough analysis was conducted to investigate the influence of various parameters, including reaction time, solvent, temperature, and catalyst quantity. Initially, the selection of phenylacetylene, benzyl bromide, and NaN3 was made as model substrates to optimize the reaction conditions, as presented in Table 1. It was observed that the model reaction failed to proceed without the presence of a catalyst after 3 h in water at 60°C, confirming the necessity of a catalyst (Table 1, entry 1). In model reactions catalyzed by UiO-66-NH2 and ZnCl2, the product yields were only 30% and 15%, respectively (Table 1, entries 2 and 3). However, upon the addition of 5 mol% UiO-66/Sal-ZnCl2 as a catalyst in the model reaction, the yield of the isolated product reached 98% (Table 1, entry 4). Various polar and nonpolar solvents were examined while using UiO-66/Sal-ZnCl2 as the catalyst (Table 1, entries 5–9). Ultimately, considering the green nature of water and the achieved yield, water was chosen as the reaction solvent for further investigation. Model reactions were monitored at different time intervals, such as 2, 1, and 0.5 h. The results indicated that the reaction was completed after 2 h (Table 1, entries 10–12). Different quantities of catalysts were also tested in the model reaction. It was observed that the product yield decreased from 5 to 3.1 mol% with decreasing catalyst loading (Table 1, entries 13 and 14). Additionally, the reaction temperature was evaluated, revealing a decrease in yield with decreasing temperature. Consequently, the optimal reaction conditions were determined as follows: phenylacetylene (1.0 mmol), benzyl bromide (1.0 mmol), sodium azide (1.0 mmol), and a catalyst (5 mol%) in an aqueous medium at a temperature of 60°C for 2 h.
Table 1
The optimized reaction conditions for the synthesis of triazole via the model reaction.a
Entry | Catalyst | Catalyst amount | Solvent | Temp. (°C) | Time (h) | Yield (%) |
1 | - | - | Water | 60 | 3 | 0 |
2 | UiO-66-NH2 | 0.1 g | Water | 60 | 3 | 30 |
3 | ZnCl2 | 0.1 g | Water | 60 | 3 | 15 |
4 | UiO-66/Sal-ZnCl2 | 5 mol% | Water | 60 | 3 | 98 |
5 | UiO-66/Sal-ZnCl2 | 5 mol% | EtOH | 60 | 3 | 95 |
6 | UiO-66/Sal-ZnCl2 | 5 mol% | DMF | 60 | 3 | 96 |
7 | UiO-66/Sal-ZnCl2 | 5 mol% | Toluene | 60 | 3 | 65 |
8 | UiO-66/Sal-ZnCl2 | 5 mol% | Hexane | 60 | 3 | 50 |
9 | UiO-66/Sal-ZnCl2 | 5 mol% | CH3CN | 60 | 3 | 85 |
10 | UiO-66/Sal-ZnCl2 | 5 mol% | water | 60 | 2 | 98 |
11 | UiO-66/Sal-ZnCl2 | 5 mol% | water | 60 | 1 | 70 |
12 | UiO-66/Sal-ZnCl2 | 5 mol% | water | 60 | 0.5 | 50 |
13 | UiO-66/Sal-ZnCl2 | 3 mol% | water | 60 | 2 | 80 |
14 | UiO-66/Sal-ZnCl2 | 1 mol% | water | 60 | 2 | 70 |
15 | UiO-66/Sal-ZnCl2 | 5 mol% | water | 50 | 2 | 85 |
16 | UiO-66/Sal-ZnCl2 | 5 mol% | water | 40 | 2 | 65 |
a Reaction conditions: phenylacetylene (1.0 mmol), benzyl bromide (1.0 mmol), sodium azide (1.0 mmol), catalyst (x mol%), and solvent (2 ml). |
The versatility of UiO-66/Sal-ZnCl2 was further explored with different substrates under the optimized reaction conditions. Substituted phenylacetylene and propargyl alcohol were successfully converted to terminal alkynes and benzyl /alkyl halides (Table 2). Employing various terminal alkynes, corresponding triazoles were obtained with exceptional performance under these optimal conditions. Additionally, a range of aryl and alkyl halides exhibited favorable reactivity in the presence of UiO-66/Sal-ZnCl2, as demonstrated in Table 2.
The potential for reusing the UiO-66/Sal-ZnCl2 catalyst was also explored. In this investigation, the model reaction was performed using a fresh catalyst under the optimized conditions. After confirming the completion of the reaction through thin-layer chromatography (TLC), the catalyst was subjected to filtration, followed by washing with both water and ethyl acetate multiple times. Subsequently, the recovered catalyst was dried in an oven at 70°C. Remarkably, this regenerated catalyst demonstrated activity for five consecutive cycles in model reactions with new substrates. The efficiency of the catalyst slightly decreased from 99% in the first cycle to 86% in the last one, as illustrated in Fig. 10.
A plausible mechanism for a model click reaction catalyzed by UiO-66/Sal-ZnCl2 is shown in Fig. 11. In the first step, coordination between the catalyst and the terminal alkyne transforms the activated acetylene (I) into a more potent dienophile. In the next step, the intermediate alkyl azide formed by the reaction of alkyl halide and sodium azide interacts with complex (I) to form complex (II). Complex (II) gives complex (III) via a 1,3-dipolar cycloaddition reaction. The final step converts the complex (III) to the desired triazole (IV) and regenerates the catalyst.
Hot filtration test
The hot filtration test as a strong test was conducted to evaluate the heterogeneity nature of the catalytic species in the model reaction under the optimal conditions through the possibility of zinc leaching into the reaction mixture (Fig. 12).
Precisely, at the midway of the reaction (60 minutes), the nanocatalyst was separated from the reaction mixture by filtration. In this step, only 53% conversion was achieved. Subsequently, the reaction mixture was allowed to continue without a catalyst for another 60 minutes under similar conditions. The reaction progress before and after the separation was checked by TLC.
Assessment of the rate of the desired product preparation demonstrates that no remarkable increase in conversion was observed even after an expanded time.
Also, to elucidate the stability of the catalyst, after five cycles in the model reaction, any structural changes of the catalyst were studied by FT-IR, TEM techniques. It is evident from the FT-IR spectrum of the 5th reused catalyst that no significant changes in the frequencies, intensities, and shapes of absorption bands were observed (Fig. 1d). Moreover, the TEM image of the 5th reused catalyst confirmed the aggregated octahedral particles measuring less than 50 nm in size which was approximately similar to the TEM image of the fresh catalyst, and there were not any significant differences in size and morphology (Fig. 8c). There is also negligible leaching of Zn species in the reaction medium, justifying its true heterogeneity.
By knowing the effectiveness of the prepared nanocatalyst, a comparison investigated between its catalytic performance and that of zinc-based catalyst systems documented in the existing literature in the reaction of benzyl bromide, sodium azide, and phenylacetylene under various catalytic conditions (Table 3, entries 1–5).
Nearly all the catalysts mentioned below exhibit notable yields of the desired products. However, the limitations including the long reaction time (Table 3, entries 1 & 2), the high reaction temperature (Table 3, entries 1 & 5), and applying hazardous solvent and reaction conditions (Table 3, entries 2 & 4) represent the drawbacks of some of these methods. As is evident, our studied system (Table 3, entry 6) has advantages such as an excellent yield in a shorter reaction time, simple separation, easy preparation of the catalyst, and milder reaction conditions.
Table 3
Comparison of UiO-66/Sal-ZnCl2 catalyst with other catalysts that used for the synthesis of 1-benzyl-4-phenyl-1H-1,2,3-triazole.
Entry | Catalyst | Solvent | Temp.(°C) | Time (h) | Yield (%) | Ref. |
1 | Zn(OAc)2/ ascorbic acid | Water | 75 | 6 | 87 | 52 |
2 | Zn/C | DMF | 50 | 15 | 90 | 53 |
3 | GO-Salen-Zn | Water | 100 | 2 | 92 | 54 |
4 | SMI/ZnCl2 | DMF | - | 0.4 | 94 | 55 |
5 | Zinc(II) L-prolinate | Water | 100 | 2 | 91 | 56 |
6 | UiO-66/Sal-ZnCl2 | Water | 60 | 2 | 98 | This study |