Maryam Ansari,
Amir Hossein Ghasemi
and
Hossein Naeimi
*
Department of Organic Chemistry, Faculty of Chemistry, University of Kashan, Kashan, 87317-51167, I. R. Iran. E-mail: Naeimi@kashanu.ac.ir; Fax: +983155912397; Tel: +98-31-55912388
First published on 3rd June 2025
This study reports the fabrication and characterization of a novel magnetic Co–Ni/Fe3O4@mesoporous silica hollow sphere (Co–Ni/Fe3O4@MMSHS) nanocomposite. Then, it was used as an effective nanocatalyst to efficiently synthesize tetrazoles from various aromatic nitriles and sodium azide through a [2 + 3] cycloaddition reaction. This nanocatalyst was provided through a multi-step process involving the preparation of carbon spheres, their magnetization with Fe3O4, loading with cobalt and nickel nanoparticles, and subsequent silica coating and calcining to form a mesoporous hollow structure. The nanocatalyst was characterized using various techniques, including FT-IR, XRD, FE-SEM, EDS, elemental mapping, BET, and VSM, confirming its successful synthesis and desired properties. The catalytic performance of the Co–Ni/Fe3O4@MMSHS was evaluated for the synthesis of a range of tetrazole derivatives. The results demonstrated high catalytic activity, achieving excellent product yields (up to 98%) within short reaction times (8–44 minutes) under mild conditions. The catalyst demonstrated excellent recyclability and reusability, making it an environmentally friendly and economically viable choice for tetrazole synthesis. This study emphasizes the potential of using rationally designed nanocatalysts for efficient and sustainable organic transformations.
They play an essential role in many industrial processes, including the production of chemicals,9–11 fuels,12,13 and pharmaceuticals.14,15 Also, the catalysts are crucial in reducing emissions within the automotive industry and other sectors.16–19
Recent advancements in nanotechnology have spurred the development of innovative catalytic materials, particularly porous20–22 and hollow23–26 nanostructures. These novel catalysts offer substantial advantages over their conventional counterparts.
These nanocatalysts exhibit exceptional catalytic activity due to their remarkably high surface-to-volume ratios, facilitating enhanced interaction with reactants and accelerating reaction kinetics. Moreover, the unique architectures of porous and hollow nanostructures provide precise control over reaction environments and offer a significantly increased density of active catalytic sites.27 These distinctive properties render nanocatalysts highly promising for a wide range of applications, including energy conversion, environmental remediation, and the sustainable production of chemicals and pharmaceuticals.28
Hollow nanostructures are one of the new fields of research in nanosciences. These nanostructures are one of the most used organic reaction catalysts due to their unique capabilities such as; large surface area, large and adjustable internal volume, etc.29 The shell of these nanostructures provides the possibility of optimizing the contact surface of the catalyst with the reactant, which, due to this unique feature, increases the efficiency of the catalyst.30 Changing their compounds can improve catalytic activity, stability, and resistance to catalyst poisoning. One of the outstanding advantages of these structures is the ability to magnetize them. This feature allows the nanocatalyst to be easily separated from the reaction medium and recycled. In green chemistry, these nanostructures reduce the consumption of dangerous chemicals for the environment. In addition to catalysis applications, the hollow nanostructures have many applications in other fields, such as energy storage,31 sensors,32 and drug delivery.33 This versatility is due to the ability to adjust their structural properties, allowing researchers to find innovative applications for these nanostructures.
A diverse array of nanocatalysts exists, encompassing metallic, metal oxide, and metal–polymer hybrid materials.34–36 Each class exhibits unique physicochemical properties, rendering them suitable for specific applications. Furthermore, incorporating multiple metals within a single catalytic system has emerged as a prominent strategy in modern catalysis. This approach, often called bimetallic or multimetallic catalysis, has significantly enhanced the efficiency of numerous organic transformations. The synergistic interactions between the different metals within these systems usually lead to dramatic improvements in catalytic activity, enabling rapid and highly efficient conversion of reactants to desired products.
Tetrazoles are aromatic heterocyclic compounds consisting of a five-membered ring containing four nitrogen atoms and one carbon atom. Due to their stability and similarity to the carboxylate group, they are used as pharmaceutical precursors to design advanced drugs. The presence of multiple nitrogens in the structure of these compounds enables them to create strong hydrogen bonds, which makes them useful in certain chemicals. In addition, tetrazoles are the precursors of many effective and valuable catalysts in the synthesis of complex materials.37 Also, scientists have found antibacterial and anti-cancer properties in certain tetrazoles through their research.
One of the most common methods for synthesizing tetrazoles is using various nitriles in the presence of sodium azide. A common approach is [2 + 3] cycloaddition reactions using nitriles and sodium azide as raw materials. This method is popular due to its simplicity and high efficiency. Sinha et al. developed 5-substituted 1H-tetrazoles by creating a cobalt(II) complex with the tetradentate ligand N,N-bis(pyridin-2-ylmethyl)quinoline-8-amine, utilizing nitrile derivatives alongside sodium azide. They employed cobalt complexes in a [2 + 3] cycloaddition reaction to synthesize 1H-tetrazoles for the first time.38 Safari and colleagues synthesized tetrazole derivatives from N-aryl cyanamides and sodium azide utilizing CuO–NiO–ZnO through both ultrasonic and thermal methods.39 Acid, base, or metallic catalysts have advanced these reactions. The use of an acid catalyst, which must be a strong acid, reduces reaction time and high selectivity in product type, but one of the major problems of using strong acid is the corrosion of equipment, especially on an industrial scale. On the other hand, using strong bases as catalysts in synthetic tetrazoles is a common and compatible method with sensitive functional groups. These reactions are carried out in polar solvents, and their advantages include reducing the production of unwanted products, but one of the significant disadvantages of this method is the possibility of unwanted formation of tetrazolium salts.
Synthesizing tetrazoles with nanocatalysts presents safety, stability, efficiency, and design challenges. Addressing these challenges requires innovative strategies to create safe and appropriate nanocatalysts for industrial use. Nanocatalysts have attracted significant attention due to advantages such as a high surface-to-volume ratio, easy recovery, and reusability. However, several challenges remain in the catalyzed synthesis of tetrazole derivatives via [2 + 3] cycloaddition reaction. The handling and reuse of nanocatalysts can be unstable under reaction conditions, reducing reusability and complicating the separation process. Numerous nanocatalysts, particularly those using metal catalysts on inorganic supports, can experience desorption throughout the reaction or work-up stages. This desorption may decrease catalyst efficiency and lead to product contamination. In addition, the formation of stable metal–tetrazole complexes may complicate the separation process and impact overall efficiency. Without a suitable catalyst, the [2 + 3] cycloaddition reaction is slow and yields low amounts. Although nanocatalysts can somewhat overcome this problem, not all are equally efficient.
This research investigated the effects of a novel heterogeneous catalyst based on magnetic silica hollow spheres containing cobalt and nickel metals on the synthesis of tetrazoles from various nitrile derivatives and sodium azide. This catalyst with a unique structure has the potential to significantly improve the efficiency and speed of the reaction compared to traditional methods. The traditional synthetic methods of tetrazoles are often associated with problems such as; using harmful organic solvents, the need for harsh reaction conditions, and the production of side products. In this method, we seek to present a greener and more efficient process for synthesizing tetrazoles.
To prepare magnetic Fe3O4 nanoparticles, ultrasonic waves dissolved 9.6 g of FeCl3·6H2O and 4 g of FeCl2·4H2O well in 90 mL of deionized water. The resulting solution was transferred to a 250 mL flask equipped with an N2 system and stirred for 30 min by a mechanical stirrer. Then, the solution temperature was raised to 90 °C, stirred for another 30 min, and then, 24 mL of 30% ammonia was added drop by drop to the solution with a syringe. After the reaction mixture was stirred for another 2 h at 90 °C, it was brought to ambient temperature, and magnetic nanoparticles were separated with the help of an external magnet and washed several times with deionized water. The obtained magnetic nanoparticles were dried for 8 h at 60 °C and stored in a sealed container for use in the following steps.
To magnetize the carbon spheres synthesized in the previous step (Fe3O4 to carbon spheres ratio of 1:
1.67), place 1.2 g of Fe3O4 nanoparticles in 160 mL of hydrochloric acid solution (pH = 2.3). In a separate container, add 2 g of carbon spheres to 120 mL of hydrochloric acid solution (pH = 2.3). Both mixtures were exposed to ultrasound waves for 20 minutes to ensure proper dispersion. The two solutions prepared in the previous step were slowly added to each other and stirred for 6 h. Then, the magnetic carbon nanospheres were separated with an external magnet and washed well with deionized water to neutralize them. Finally, the magnetic carbon nanospheres (Fe3O4@carbon nanospheres) were dried at 50 °C for 12 h.
To load cobalt and nickel nanoparticles on the surface of magnetic carbon nanospheres (Co–Ni/Fe3O4@carbon nanospheres), 10 mg of each CoCl2·6H2O and NiCl2·6H2O salts were first dissolved in 60 mL of deionized water. The prepared solution was gradually added to 300 mg of magnetic carbon spheres suspended in 50 mL of deionized water. The resulting mixture was stirred for 10 h by a mechanical stirrer. The carbon nanospheres functionalized with nickel and cobalt were separated from the reaction medium using an external magnet, washed several times with deionized water and ethanol, and maintained at 50 °C for 12 h.
In the last step, the Co–Ni/Fe3O4@carbon nanospheres prepared in the previous step were dispersed in 80 mL of deionized water for 20 min with the help of ultrasonic waves. Then, 60 mL of ethanol, 2 mL of 30% ammonia, and 0.3 g of CTAB were added to the prepared solution and stirred vigorously. After 10 min, 400 μL of TEOS were added to the reaction mixture. Finally, after 8 h, the nanoparticles were separated with an external magnet and washed with water and ethanol. The nanoparticles were dried at 50 °C for 12 h. Then, the dried nanoparticles were calcined at 400 °C with a ramping rate of 2 °C per minute for 7 h in an air atmosphere to obtain the Co–Ni/Fe3O4@MMSHS.
The FT-IR spectra of the various stages of Co–Ni/Fe3O4@MMSHS nanocatalyst preparation is presented in Fig. 2. Fig. 2a displays the spectrum of the carbon spheres formed during the glucose polymerization process. The peak observed at 3441 cm−1 corresponds to the stretching vibration of the O–H bond, attributed to alcoholic groups in the carbon sphere structure. The absorption peaks observed in regions 2923 and 2871 cm−1 are related to the asymmetric stretching and symmetric stretching vibrations of C–H sp3 bonds, respectively. The absorption peak observed at 1712 cm−1 is associated with the stretching vibration of the ketone carbonyl group within the polymerized structure of glucose. The absorption peaks observed at 1627 and 1383 cm−1 are related to the aromatic rings formed during polymerization. The peak observed at approximately 1300 cm−1 is associated with the C–O stretching vibrations. Fig. 2b displays the spectrum of magnetic carbon spheres. It reveals absorption peaks at 534 and 451 cm−1, which are associated with the stretching vibrations of the Fe–O bond. This evidence confirms the binding of Fe3O4 nanoparticles to the surface of the carbon spheres.
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Fig. 2 The FT-IR spectra of carbon spheres (a), Fe3O4@carbon nanospheres (b), Co–Ni/Fe3O4@carbon nanospheres (c), SiO2@Co–Ni/Fe3O4@carbon nanosphere (d), Co–Ni/Fe3O4@MMSHS (e). |
The absorption spectrum shown in Fig. 2c corresponds to the magnetic carbon sphere covered by cobalt and nickel. The absorption peaks observed at 593 and 470 cm−1 are related to Co–O and Ni–O, respectively. The increase in the intensity of the peaks associated with stretching vibrations of C–H sp3 in the region of 2918 and 2852 cm−1 is due to the presence of the carbon chain of CTAB as a surfactant in the structure of the nanocatalyst (Fig. 2d). Absorption peaks at 1071 and 964 cm−1 correspond to the Si–O–Si and Si–OH, respectively. These peaks indicated that the SiO2 is present on the surface of the nanocatalyst.
Finally, Fig. 2e displays the spectrum of the nanocatalyst following the calcination process. In this spectrum, all peaks associated with the organic substances from the previous stage have vanished, indicating their decomposition and the successful synthesis of a hollow structure.
X-ray diffraction (XRD) was utilized to investigate the different stages of the nanocatalyst synthetic process, as shown in Fig. 3. The amorphous pattern observed in the X-ray diffraction of the synthesized carbon spheres, as shown in Fig. 3a, indicates the nature of their carbon structure. Fig. 3b shows the X-ray diffraction pattern of carbon spheres after magnetization. The decrease in the pattern's height at 2θ = 25° is attributed to the surface of the carbon spheres covered by Fe3O4 nanoparticles. The observed pattern aligns perfectly with the pattern associated with Fe3O4 (JCPDS no. 01-075-0449). Additionally, the size of the Fe3O4 nanoparticles on the catalyst surface was determined to be 16.70 nm using the Debye–Scherrer equation. By adding cobalt and nickel to the surface of magnetic carbon spheres, the amorphous pattern seen in Fig. 3c has been eliminated due to increased structural crystallinity. According to JCPDS no. 01-086-2267 and 00-022-1086, the presence of cobalt and nickel nanoparticles in the structure has been confirmed. The pattern in Fig. 3d relates to the nanocatalyst's silica coating. The amorphous pattern observed in 2θ = 25° indicates that silica successfully covers the surface and confirms the coating process. The pattern shown in Fig. 3e illustrates the nanocatalyst after calcination. As the carbon structure and the surfactant within the silica wall of the nanocatalyst are eliminated, the crystallinity of the material increases. Consequently, the amorphous pattern observed in the previous step has disappeared. The average size of the Co–Ni/Fe3O4@MMSHS nanocatalyst was calculated using the Debye–Scherrer formula, with an average crystallite size of 12.31 nm.
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Fig. 3 The XRD patterns of carbon spheres (a), Fe3O4@carbon nanospheres (b), Co–Ni/Fe3O4@carbon nanospheres (c), SiO2@Co–Ni/Fe3O4@carbon nanosphere (d), Co–Ni/Fe3O4@MMSHS (e). |
The field emission scanning electron microscopy (FE-SEM) images of the nanocatalyst are shown at two different scales: 200 and 500 nm, illustrated in Fig. 4a and b. These images reveal the catalyst's spherical morphology. Fig. 4b demonstrates the hollowness of the Co–Ni/Fe3O4@MMSHS nanocatalyst. The internal space increases the contact surface between the nanocatalyst and the reactants, thereby enhancing reaction efficiency and reducing reaction time. The thickness of the nanocatalyst's silica wall was measured at 81 nm (Fig. 4b). This thickness enhances the nanocatalyst's physical and chemical resistance, allowing for consecutive reuse.
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Fig. 4 The FE-SEM images of the Co–Ni/Fe3O4@MMSHS nanocatalyst with magnification 500 (a) and 200 (b) nanometers. |
Fig. 5 illustrates the histogram displaying the size distribution of the Co–Ni/Fe3O4@MMSHS nanocatalyst. The mean size of the Co–Ni/Fe3O4@MMSHS was determined to be 388 nm, with a standard deviation of 95.05 nm.
Fig. 6 shows the energy dispersive X-ray analysis of Co–Ni/Fe3O4@MMSHS nanocatalyst. 12.07% of carbon was observed in the sample, which can be attributed to the residual carbon after calcination. The estimated amount of Si in the walls of nanoparticles is 14.52 wt%. Additionally, the weight percentages of Fe, Co, and Ni were measured as 22.32%, 0.39%, and 0.12%, respectively. Approximately 50.58% of the sample's weight consists of oxygen.
EDS elemental mapping analysis is a valuable method for studying the distribution of elements in nanomaterials. Fig. 7 shows the EDS elemental mapping of the Co–Ni/Fe3O4@MMSHS nanocatalyst. The obtained data show the proper dispersion of O, Ni, Si, Co, Fe elements throughout the nanocatalyst. The uniform dispersion of nanoparticles as catalytic active sites enhances nanocatalyst efficiency, ensuring uniform catalytic performance across the entire surface.
The Brunauer–Emmett–Teller (BET) technique estimates the surface area, pore volume, and pore size of the Co–Ni/Fe3O4@MMSHS nanocatalyst (Fig. 8). The BET plot (Fig. 8a) indicates that the nanocatalyst's specific surface area is 204.83 m2 g−1. Additionally, this technique calculates the total pore volume of the Co-nanocatalyst, which is 0.1434 cm3 g−1.
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Fig. 8 The BET plot (a), adsorption/desorption isotherm (b), and BJH plot (c) of the Co–Ni/Fe3O4@MMSHS nanocatalyst. |
Fig. 8b illustrates the N2 adsorption–desorption isotherm for the Co–Ni/Fe3O4@MMSHS nanocatalyst. According to the IUPAC classification, the nanocatalyst exhibited type IV adsorption–desorption isotherms. This type of isotherm indicates the synthesized nanocatalyst is mesoporous. The hysteresis type of the nanocatalyst is H4, commonly found in nanomaterials with inner space, like hollow spheres with mesoporous silica walls. Using the Barrett–Joyner–Halenda (BJH) method, the pore radius was determined to be 1.21 nm, and the pore area was calculated to be 18.68 m2 g−1 (Fig. 8c).
Fig. 9 shows that the magnetic properties of the prepared nanoparticles are measured using the vibrating-sample magnetometry (VSM) analysis at room temperature. The magnetic property of the Fe3O4 nanoparticles 63.60 emu g−1 was measured (Fig. 9a). After layering various materials on the nanocatalyst and calcining it, the magnetic properties of the final nanocatalyst, 24.51 emu g−1 were measured (Fig. 9a). The analysis results indicate that the synthesized nanocatalyst retains its magnetic properties and can be easily separated from the reaction medium using an external magnet.
Table 1 shows the results of the optimum amount of catalyst. According to the obtained results, the optimal amount of catalyst is 8 mg (entry 5), and no change in reaction time or efficiency has been observed in higher amounts of catalyst (entry 6).
Entry | Catalyst amount (g) | Time (min) | Yieldb (%) |
---|---|---|---|
a Reaction conditions: benzonitrile (1 mmol), sodium azide (1.2 mmol), Co–Ni/Fe3O4@MMSHS as a catalyst, and 5 mL of H2O/EtOH (1![]() ![]() |
|||
1 | — | 300 | Trace |
2 | 0.002 | 240 | 37 |
3 | 0.004 | 90 | 66 |
4 | 0.006 | 32 | 79 |
5 | 0.008 | 12 | 98 |
6 | 0.010 | 12 | 98 |
Table 2 indicates that the reaction efficiency at room temperature was very low during the temperature optimization study. By increasing the reaction temperature to 60 °C, we have seen an increase in the reaction efficiency. As a result, the catalyst has reduced the energy required to carry out the reaction. Also, no change in product yield was observed by further increasing the reaction temperature to 100 °C.
Table 3 shows the results of optimizing the solvent in the reaction. The solvents such as; DMSO, DMF, EtOH, H2O, THF, PEG, toluene, CH3CN, and H2O/EtOH were investigated, and according to the obtained results, the 1:
1 mixture of H2O and EtOH showed the highest efficiency and the shortest reaction time (Table 3, entry 9).
Entry | Solvent | Time (min) | Yieldb (%) |
---|---|---|---|
a Reaction conditions: benzonitrile (1 mmol), sodium azide (1.2 mmol), Co–Ni/Fe3O4@MMSHS (8 mg) as a catalyst, and 5 mL of selected solvent at 60 °C.b Isolated yields. | |||
1 | DMSO | 68 | 72 |
2 | DMF | 56 | 64 |
3 | EtOH | 188 | 69 |
4 | H2O | 260 | 55 |
5 | THF | 260 | 28 |
6 | PEG | 240 | 56 |
7 | Toluene | 300 | 42 |
8 | CH3CN | 300 | 17 |
9 | H2O/EtOH (1![]() ![]() |
12 | 98 |
To demonstrate the positive synergistic effect of nanoparticles in the nanocatalyst structure, the model reaction was conducted under optimal conditions using the nanoparticles illustrated in Fig. 10. According to the results obtained from Fig. 10, the mesoporous silica hollow sphere did not show the catalytic effect. The Fe3O4@MMSHS catalyzed the reaction due to the presence of Fe3O4 nanoparticles as a Lewis acid, which showed a product yield of about 17%. When nickel and cobalt nanoparticles are present individually on the surface of the magnetic hollow mesoporous spheres, lower efficiency is observed compared to when both metals are present simultaneously on the surface of the nanocatalyst. This analysis demonstrated a positive synergistic effect between cobalt and nickel nanoparticles in synthesizing tetrazole derivatives.
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Fig. 10 Investigating the synergistic effect of the catalyst for the synthesis of the model reaction. |
After optimizing the reaction conditions, Table 4 shows the results of synthesizing tetrazole derivatives from various aromatic nitriles and sodium azide. This table displays each synthesized derivative's reaction time and yield under optimal reaction conditions.
The radar chart comparing yield and reaction time based on various substitutions is extracted from Table 4 and shown in Fig. 11. The results indicate that the reaction yield ranged from 88% to 98%. It was also observed that the nitrile compounds with electron-donating groups had higher yields, but they did not differ much from nitriles with electron-withdrawing groups. In addition, the results showed that nitriles with the group in position 2 have lower yield and longer time due to the steric hindrance.
Table 5 compares the Co–Ni/Fe3O4@MMSHS nanocatalyst with other reported catalysts for synthesizing 5-phenyl-1H-tetrazole (3m) from benzonitrile and sodium azide. The reactions in entries 1 to 4 were performed at temperatures above 100 °C. The catalysts listed in this table (entries 1 to 5) are organometallic complexes, and their efficiency may decrease after multiple recoveries. Also, the solvents used in entries 1 to 4 are not green and environmentally friendly conditions. As a result, the Co–Ni/Fe3O4@MMSHS nanocatalyst synthesizes tetrazole derivatives with high efficiency in a shorter reaction time (Table 5, entry 6). In addition, water and ethanol solvents, which are green and environmentally friendly solvents, are used. Compared to others, one important feature of this catalyst is its high stability and reusability. All of these features have made the Co–Ni/Fe3O4@MMSHS nanocatalyst significantly better than the catalysts that have been previously reported.
Entry | Catalyst (conditions) | Time (min) | Yielda (%) | Ref. |
---|---|---|---|---|
a Isolated yield. | ||||
1 | Sm-TADDbBP@MCM-41 (50 mg, PEG-400, 120 °C) | 70 | 97 | 48 |
2 | Nd-bis(PYT)@boehmite NPs (50 mg, PEG-400, 120 °C) | 150 | 97 | 49 |
3 | Cobalt(II) complex with (N,N-bis pyridin-2-yl methyl)quinolin-8-amine (1 mol%, DMSO, 110 °C) | 720 | 99 | 38 |
4 | [Cu(L)]·0.5H2O (0.7 mol%, DMSO, 110 °C) | 240 | 96 | 50 |
5 | FeTSPP (0.05 mmol, H2O/EtOH, 60 °C) | 20 | 97 | 51 |
6 | Co–Ni/Fe3O4@MMSHS (8 mg, H2O/EtOH, 60 °C) | 12 | 98 | This work |
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Scheme 2 Proposed reaction mechanism for the synthesis of tetrazole derivatives from sodium azide and aromatic nitriles. |
After recovery, the FE-SEM image (Fig. 13a) and XRD image (Fig. 13b) of the Co–Ni/Fe3O4@MMSHS show no significant changes in the catalyst's structure and morphology. After multiple recovery steps, the catalyst's structural stability demonstrates its excellent durability and retention of catalytic activity under the reaction conditions. Also, by comparing the catalyst's XRD patterns before and after recovery and examining the data obtained from the reaction yield, it can be concluded that the catalyst's active sites have largely maintained their structure and efficiency after several stages of recovery.
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Fig. 13 The FE-SEM image (a) and the XRD spectra (b) of the Co–Ni/Fe3O4@MMSHS nanocatalyst after recovery. |
The designed catalyst was also evaluated through a leaching test. The model reaction was placed under optimal conditions for 6 min, and then the catalyst was separated from the reaction medium by an external magnet. After removing the catalyst from the reaction environment, the progress of the reaction was assessed using the TLC technique. The TLC technique revealed that the reaction did not proceed. Stopping the reaction at this stage indicates the stability of the catalyst and its excellent separation ability.
The prepared catalyst showed greater efficiency than other catalysts used in tetrazole synthesis. Many of the catalysts used in synthesizing tetrazoles could not easily separate from the reaction medium, and their efficiency was significantly reduced after reuse. However, the catalyst developed in this research demonstrates effective separation and high recovery capability without compromising efficiency.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d5ra02982a |
This journal is © The Royal Society of Chemistry 2025 |