Open Access Article
Maryam
Fereydooni
a,
Ramin
Ghorbani-Vaghei
*ab and
Sedigheh
Alavinia
a
aDepartment of Organic Chemistry, Faculty of Chemistry and Petroleum Sciences, Bu-Ali Sina University, 6517838683, Hamadan, Iran. E-mail: rgvaghei@yahoo.com; ghorbani@basu.ac.ir
bDepartment of Organic Chemistry, Faculty of Chemistry, University of Guilan, Rasht, Iran
First published on 18th December 2024
Here, a straightforward design is employed to synthesize a nanocatalyst based on a carbon-activated modified metal–organic framework using the solvothermal method. This work presents a simple and practical approach for producing the activated carbon derived from the Thymus plant (ACT) modified with amine-functionalized isoreticular metal–organic framework-3 (IRMOF-3) to create an ACT@IRMOF-3 core–shell structure. Successful functionalization was confirmed through N2 adsorption isotherms, FT-IR, FE-SEM, TEM, EDS, elemental mapping, TGA, and XRD analysis. The ACT@IRMOF-3 nanocomposite demonstrated exceptional performance in the synthesis of novel benzodiazepine derivatives, facilitating high product yields using various 1,2-phenylenediamine and aromatic aldehydes under mild conditions. The obtained results demonstrated that the presence of IRMOF-3 on the surface of ACT remarkably increases the catalytic reaction yield. The present methodology offers several merits such as high catalytic activity, excellent yields, short reaction times, cleaner reactions, simple operations, and compatibility of a wide range of substrates. Furthermore, the catalyst can be easily isolated from the reaction mixture via filtration and retains remarkable reusability and catalytic activity even after six consecutive reaction cycles.
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| Fig. 1 Chemical structure of benzodiazepines with biological activity.1–4 | ||
Recently, researchers have focused on synthesizing these derivatives with enhanced biological activities through strategic substitutions and innovative synthesis methods. Continuous flow synthesis has been described for six benzodiazepines from aminobenzophenones, including diazepam and clonazepam.5 One-step synthesis of pyrido-benzodiazepine backbones and analogs was achieved by ring-opening hydrolysis and C–H bond activation.6 In addition, the synthesis of 1,4-benzodiazepines using a palladium catalyst was discussed, highlighting various reactions and catalytic processes for their efficient preparation.7 Multicomponent reactions, especially Ugi and Mannich-type reactions, provide efficient and sustainable methods for the synthesis of benzodiazepines with diverse biological activities, providing novel therapeutic candidates through one-pot protocols.8 Considering the broad medicinal and biological applications of benzodiazepine derivatives, synthetic chemists face a significant challenge in providing newer and more efficient catalytic systems compatible with green chemistry principles for synthesizing these compounds.
Metal–organic frameworks (MOFs) exhibit significant potential in catalysis due to their diverse structures and properties.3 MOFs can act as Lewis acid–base catalysts, with frustrated Lewis acid–base pairs (FLPs) or bifunctional solid catalysts capable of activating molecular hydrogen.9 These structures offer well-defined porosity, controllable morphology, and the ability to support nanomaterials, enhancing their catalytic applications.10 To improve catalytic efficiency, MOFs can be functionalized or integrated with other materials to create composites or hybrids, expanding their active sites and stability.10–12 Additionally, modifications to MOFs can enhance catalytic activity without changing their chemical nature, making them versatile catalysts for various reactions.12 Though, these materials are time-consuming and costly, which limits their utilization in practice.
Recently, activated carbon/MOF nanocomposites represent a versatile platform for catalytic reactions, showing great potential in advancing organic chemistry and environmental remediation.13–16 Carbon-based nanocomposites, including graphene, carbon nanotubes, and activated carbon, are extensively utilized in various applications17 The application of activated carbon and its composites is a crucial aspect in various industries due to the unique properties it possesses.18 Activated carbon is known for its exceptional adsorption capabilities, high surface area, porous structure, and high chemical/thermal stability making it an excellent choice for designing carbon-based nanocatalyst.19 In recent years, activated carbon derived from natural sources and biomass such as coconut shells and wood has gained popularity for its environmental and sustainable nature.19–26 Activated carbon, which is derived from natural materials, plays a crucial role in various organic reactions.27–31 Consequently, the development and surface modification of activated carbon-based nanocatalysts from natural materials is a straightforward, cost-effective, and green approach for the synthesis of N-containing heterocyclic compounds.15–18,25
Enthused by the aforementioned findings, in this work, activated carbon derived from the Thymus plant (ACT) has been successfully modified with IRMOF-3 (ACT@IRMOF-3) for the synthesis of benzodiazepine. Given that activated carbon has a smaller surface area compared to IRMOF-3 nanoparticles, incorporating a small number of IRMOF-3 nanoparticles can significantly increase the surface area created in ACT@IRMOF-3 core–shell structure. Furthermore, the synthesized ACT@IRMOF-3 nanocomposite is a cost-effective nanocatalyst as it mainly consists of carbon derived from waste materials. The combination of IRMOF-3 with Thymus-activated carbon enhances catalytic efficiency and selectivity, offering a platform for the development of carbon-based multifunctional catalysts. By integrating the benefits of activated carbon surface modification capabilities with the high surface area and multifunctionality of IRMOF-3, this catalyst provides a unique approach to benzodiazepine synthesis. Each nanocomposite component contributes to a synergistic effect, acting as a Lewis acid and enhancing catalytic efficiency.
The sample was immersed in 10 mL of hot EtOH and 10 mL of DMF for 24 hours to remove any residual trapped acids inside the pores. Subsequently, it was filtered and dried at 100 °C overnight to obtain the ACT@IRMOF-3 nanocomposite (Fig. 2).
:
ethyl acetate, 2
:
1). After the reaction completion, the mixture was cooled and then centrifuged to separate the catalyst. After drying, the sediment was washed with EtOH (5 mL) to gain the product (Scheme 1).
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| Scheme 1 The procedure for the one-pot synthesis of benzodiazepine derivatives using ACT@IRMOF-3 nanocomposite. | ||
C elongation pulsations specific to the aromatic structure. Additionally, the strip at 1099 cm−1 can be tuned to the O–H curvature or the C–O elongation pulse of phenol, while the strip at 1448 cm−1 is tuned to the O–C
O groups (Fig. 3a). FT-IR analysis of the ACT@IRMOF-3 catalyst shows mobile mutations due to the addition of IRMOF-3. An increase in the integration strip to 3396 cm−1 highlights the presence of carboxylic acid groups of IRMOF-3 adsorbed during modification. A new integration band observed at 595 cm−1 is granted to the Zn–O bond of the IRMOF-3 group. An asymmetric strip at 1023 cm−1 and a symmetric strip at 1259 cm−1 are tuned to the C–O and C–N bond. The bands at about 1448, 1615, and 2915 cm−1 are related to O–C
O, C
C, and C–H bonds of ACT@IRMOF-3 (Fig. 3b).
The crystallinity of ACT and ACT@IRMOF-3 nanocomposite were evaluated using X-ray diffraction (Fig. 4). XRD is a noninvasive analytical method that gives thorough evidence regarding the crystalline structure and chemical composition of the material. The XRD pattern for the ACT and ACT@IRMOF-3 nanocomposite demonstrated two main diffraction peaks shown at 24.29° and 43.54° are observed in the 2θ range from 10 to 90° corresponding to hkl plane of (100) and (002), respectively, which are the characteristic peaks of activated carbon, characteristic of the accumulation composition of the aromatic carbon layers. Additionally, the existence of unidentified particles in the carbon structure shows the existence of various minerals (Fig. 4). The synthesized materials have a semi-crystalline nature. XRD spectrum of ACT@IRMOF-3 confirms the successful integration and modification of ACT with IRMOF-3 particles. From XRD analysis, it is clear that there is no specific change in the morphology of the material after modification of activated carbon (ACT). The spectrum of the ACT@IRMOF-3 catalyst indicates a basic structure analogous to that of ACT but with significant variations in pick intensities. It can therefore be concluded that the XRD analysis explained the adsorption and synthesis of IR-MOF-3 on the surface of ACT (Fig. 4).
Fig. 5 displays the FESEM images of the raw material (Thymus), ACT, and ACT@IRMOF-3 core–shell. Fig. 5A provides evidence that the Thymus particles possess a surface that is predominantly smooth and uniform in nature. It can be observed from Fig. 5(B and C) that the ACT surface shows the presence of numerous cavities, indicating that the pore structure expands after the activation procedure. The ACT material showed a three-dimensional network structure. The high-magnification SEM photograph of ACT reveals the microporous surface Fig. 5(B and C). The synthesized IRMOF-3 shows well-dispersed and nearly spherical uniform nanostructures (Fig. 5D).27Fig. 5(E and F) reveals an irregular surface, confirming the loading of IRMOF-3 NPs onto the microporous surface of activated carbon of Thymus. The pore size of the sample ACT was mainly concentrated in 10–30 μm Fig. 5(B and C), while the surface of the ACT@IRMOF-3 catalyst clearly shows the catalyst particles are uniformly nanoscale (Fig. 5F).
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| Fig. 5 FESEM images of raw material (Thymus leaves) (A), ACT (B and C), IRMOF-3 (D), ACT@IRMOF-3 (E and F). | ||
More intrinsic and clear images were obtained through TEM analysis which has been displayed in Fig. 6A and B. It shows that the IRMOF-3 particles are mostly cubic-shaped and not aggregated, at all. The particle sizes also are quite in agreement with the FE-SEM data. On close observation, a feeble layer can be observed around the particles, which is anticipated to be the ACT modification with IRMOF-3.
The EDS analysis of ACT (Fig. 7a) and ACT@IRMOF-3 (Fig. 7b) provided crucial insights into the surface composition. The chemical composition of ACT is composed mainly of carbon with a mass percentage of 85.9%, but also of oxygen (14.00%) coming from numerous surface oxygen. The weight percentage results of the EDS analysis of both samples show that the main constituent is carbon. The equivalent quantities of carbon, nitrogen, oxygen, and zinc were 73.1, 0.6, 9.3, and 17.0%, respectively, in the ACT@IRMOF-3 (Fig. 7b). The zinc peak presence confirms the successful modification of ACT with IRMOF-3 and the construction of ACT@IRMOF-3. The analysis showed an increase in the elements nitrogen with a weight percentage reaching 0.6 six times.
Elemental mapping analysis of ACT (Fig. 8a) and ACT@IRMOF-3 (Fig. 8b) nanocomposites shows a high density of carbon elements originating from the ACT nanocomposites. The collaborative evidence from these analytical techniques strengthens the credibility of the findings and provides a comprehensive understanding of IRMOF-3 distribution on the surface of CAT. The ACT@IRMOF-3 analysis reveals consistent distribution patterns of carbon, nitrogen, oxygen, and zinc elements. This indicates that ACT promotes the adsorption of IRMOF-3. By uniformly dispersing zinc as the active component in this heterogeneous catalyst, an increase in the number of active sites is anticipated to provide in a higher production rate of organic products.
To obtain specific surface area, nitrogen uptake and desorption, and total pore volume analysis was performed at 77 K (Fig. 9). The synthesized samples showed a combination of type III and IV isotherms, indicating a mesoporous structure.28 The results show that ACT possesses a total specific surface area of 42.662 m2 g−1, a pore size distribution of 54.52 Å, and a pore volume of 0.019 cm3 g−1 (Fig. 9a, Table 1). The nitrogen adsorption/desorption isotherms of ACT@IRMOF-3 reveal a total specific surface area of 806 m2 g−1, a pore size distribution of 1.22 nm, and a pore volume of 190.23 cm3 g−1 (Fig. 9b, Table 1). The observed increase is related to the modification of ACT with IRMOF-3 NPs and the interaction of IRMOF-3 groups with the surface of ACT. The mesoporous structure is essential in effectively enhancing the catalytic activity in the ACT@IRMOF-3 matrix.
| Parameter | ACT | ACT@IRMOF-3 |
|---|---|---|
| a s (m2 g−1) | 42.662 | 806 |
| V m (cm3(STP) g−1) | 0.019 | 190.23 |
| r p | 54.52 Å | 1.22 nm |
| a p (m2 g−1) | 13.86 | 6.5 |
Fig. 10a indicates that ACT lost 12.06% of its weight in a two-step decomposition at 89.16 °C, and 340.04 °C in the order of their appearance (Fig. 10a). In the TGA curve of synthesized nanocatalyst, ACT@IRMOF-3 occurs via three successive steps (at 73.66 °C, 107.84 °C, and 306.25 °C), by which its losses are 25.58% of its weight (Fig. 10b). These results indicate that ACT@IRMOF-3 demonstrates high thermal stability compared to ACT. In addition, these analyses confirm the successful synthesis of ACT and ACT@IRMOF-3 nanocomposites.
| Entry | Cat. (mol%) | T (°C) | Solvent | Time (h) | Yieldb (%) | TOFc | TONd |
|---|---|---|---|---|---|---|---|
| a Reaction conditions: benzaldehyde (1 mmol), dimedone (1 mmol), 1,2-phenylenediamine (1 mmol), and ACT@IRMOF-3 nanocomposite. b Isolated yield. c TON = yield/amount of catalyst (mol). d TOF = TON/reaction time (h). | |||||||
| 1 | — | Reflux | EtOH | 1 | N. R. | — | — |
| 2 | ACT@IRMOF-3 (0.8) | Reflux | EtOH | 1 | 75 | 93.75 | 93.75 |
| 3 | ACT@IRMOF-3 (1.5) | Reflux | EtOH | 1 | 95 | 63.33 | 63.33 |
| 4 | ACT@IRMOF-3 (3) | Reflux | EtOH | 1 | 95 | 31.66 | 31.66 |
| 5 | ACT@IRMOF-3 (1.5) | — | EtOH | 1 | Trace | — | — |
| 6 | ACT@IRMOF-3 (1.5) | 60 °C | EtOH | 1 | 72 | 48 | 48 |
| 7 | ACT@IRMOF-3 (1.5) | Reflux | H2O | 1 | 42 | 28 | 28 |
| 8 | ACT@IRMOF-3 (1.5) | Reflux | MeOH | 1 | 76 | 50.66 | 50.66 |
| 9 | ACT@IRMOF-3 (1.5) | Reflux | DMF | 1 | 57 | 38 | 38 |
| 10 | ACT@IRMOF-3 (1.5) | Reflux | CHCl3 | 1 | 50 | 33.33 | 33.33 |
| 11 | ACT@IRMOF-3 (1.5) | Reflux | PEG | 1 | 53 | 35.33 | 35.33 |
| 12 | ACT@IRMOF-3 (1.5) | Reflux | Toluene | 1 | 35 | 29.16 | 29.16 |
| 13 | ACT@IRMOF-3 (1.5) | Reflux | EtOH | 2 | 95 | 31.66 | 63.33 |
| 14 | ACT@IRMOF-3 (1.5) | Reflux | EtOH | 0.5 | 58 | 77.33 | 38.66 |
In addition, we performed experiments to investigate different solvents for the model reaction (entries 7–12). When the reaction was tested in water, the yield of the corresponding product went down. This is likely because some of the raw materials did not dissolve and there were fewer collisions and interactions between the raw materials, which are needed to turn them into intermediates and the corresponding products. The results showed that both methanol and PEG are good solvents for these organic transformations. On the contrary, there are problems in using these solvents, i.e., the need for more purification steps, making this method less effective and less cost effective. Among these, ethanol proved to be the most effective solvent, resulting in the highest product yields. The excellent catalytic performance of the ACT@IRMOF-3 in the ethanol can be attributed to ACT@IRMOF-3's amphiphilic behavior using hydrophobic monomers (aromatic groups of ACT) and hydrophilic monomers (i.e., Zn, carboxylate, and amine). Further, ACT@IRMOF-3 activates the intermediates via H-bonding with ACT@IRMOF-3's polar functional groups. It is worth noting that the presence of DMF, chloroform, PEG, and toluene solvents had a negative impact on the reaction efficiency. Furthermore, our investigation into different reaction times revealed that a duration of 60 minutes resulted in the highest conversion rate (entries 13 and 14).
Furthermore, we conducted a comparison of the efficiency between the ACT@IRMOF-3 catalyst and several catalyst precursors, including UiO-66-NH2, MIL-101-NH2 (Fe), IRMOF-3, MIL-101-NH2 (Cr), and ACT. The best result was obtained when ACT@IRMOF-3 was utilized, as shown in Table 3, entries 1–6. This observation emphasizes the distinctive catalytic efficiency of ACT@IRMOF-3 in facilitating this particular organic transformation. By providing a platform for adsorption and reaction sites, activated carbon facilitates the conversion of reactants into desired products with enhanced efficiency. Moreover, IRMOF-3 accelerate the reaction by activating aldehydes and dimedone.
| Entry | Catalyst (mg) | Condition | Solvent | Time (h) | Yield (%) |
|---|---|---|---|---|---|
| 1 | IRMOF-3 (5 mg) | Reflux | EtOH | 1 | 70 |
| 2 | ACT (5 mg) | Reflux | EtOH | 1 | 40 |
| 3 | UiO-66-NH2 (5 mg) | Reflux | EtOH | 1 | 60 |
| 4 | MIL-101-NH2 (Fe) (5 mg) | Reflux | EtOH | 1 | 42 |
| 5 | MIL-101-NH2 (Cr) (5 mg) | Reflux | EtOH | 1 | 35 |
| 6 | ACT@IRMOF-3 (5 mg) | Reflux | EtOH | 0.5 | 95 |
Following the successful attainment of both satisfactory and optimal catalytic performance from ACT@IRMOF-3, an in-depth exploration of its applicability across a diverse range of substrates is detailed in Table 4. The synthesized ACT@IRMOF-3 nanocatalyst exhibited notable strength in catalyzing the reaction involving aryl benzaldehyde as delineated in Table 4. The reactivity of diverse benzaldehydes with substituents (p-Cl, p-Br, p-NO2, 2,4-Cl2, p-N(CH3)2, p-OCH3, p-CH3, p-OH, o-OCH3, H) was initiate to be moderate to good for producing the products. Aromatic diamines such as 1,2-phenylenediamine and 4-methylbenzene-1,2-diamine showed high yields of product. Especially remarkable was the fact that, compared to electron-donating-substituted substrates, electron-withdrawing groups on the aryl ring produced greater yields of the desired product in a short reaction time. Across this expansive spectrum of substrates, the reactions exhibited robust efficiency yielding a diverse array of products 4a–o. Moreover, the reaction of aryl aldehydes with electron-donating groups (Me, OMe, OH, N(Me)2) affects the aryl ring and prolongs the reaction time.
| a Reaction conditions: benzaldehyde (1 mmol), dimedone (1 mmol), 1,2-phenylenediamine (1 mmol), and ACT@IRMOF-3 (1.5 mol%) in EtOH (2 mL) were heated at reflux condition. |
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The yields ranged from 85% to 95%, underscoring the versatility of our methodology across a broad range of electron-rich and electron-deficient aryl benzaldehydes. This comprehensive investigation not only broadens the scope of applicable substrates but also showcases the adaptability of our approach to various chemical environments.
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| Fig. 11 FESEM of recycled ACT@IRMOF-3 nanocatalyst after six times at the scale bare of 10 μm (a and b). | ||
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4na00907j |
| This journal is © The Royal Society of Chemistry 2025 |