Asadollah Hassankhani*a,
Seyed Mohsen Sadeghzadehb and
Rahele Zhianib
aDepartment of New Materials, Institute of Science and High Technology and Environmental Sciences, Graduate University of Advanced Technology, PO Box 76315-117, Kerman, Iran. E-mail: ahassankhani@gmail.com
bYoung Researchers and Elite Club, Neyshabur Branch, Islamic Azad University, Neyshabur, Iran
First published on 26th February 2018
This study investigates the potential application of an efficient, easily recoverable and reusable magnetically separable Fe3O4/KCC-1/APTPOSS nanoparticle-supported salen/Pd(II) catalyst for C–C and C–H cross-couplings. The Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs were thoroughly characterized by using TEM, FE-SEM, TGA, XRD, VSM, FT-IR, ICP-MS, and BET. This observation was exploited in the direct and selective chemical reaction of 2-acetyl-benzaldehyde with cyclopentadiene for the synthesis of pentafulvene. The recycled catalyst has been analyzed by ICP-MS showing only minor changes in the morphology after the reaction, thus confirming the robustness of the catalyst.
Morphology-controlled nanomaterials such as silica play a decisive role in the development of technologies for addressing challenges in the fields of wellness, environment, and energy. Mesoporous silica materials discovery such as MCM-41 and SBA-15, a notable increase in the design. It was synthesis of nanosilica with different sizes, shapes, morphologies, and tissue properties has been observed in lately years. KCC-1 is dendritic fibrous nanosilica as one notable invention that have a unique fibrous morphology, unlike the tubular porous structure of various customary silica materials. It has a high surface area with improved accessibility to the internal surface, tunable pore size and pore volume, controllable particle size, and, importantly, improved stability.11–20
In recent years, magnetic nanoparticles of iron oxide (Fe3O4) have been widely used as a heterogeneous catalyst in organic reactions because they are cheap, available, low toxicity, recyclable and easy to separate from the reaction solution using a magnet.21,22 Lately, organometallic ionic complexes (OICs) have emerged as very marvelous catalysts because they can be created from readily available and highly tailorable metal and ligand forerunners for multifunctional integration.23,24 Many researchers have showned OICs that contain a Lewis acidic metal center and a nucleophilic halogen anion (X−) portion as highly impressive bifunctional catalysts for the coupling reaction between carbon dioxide and other organic compound under co-catalyst free circumstances owing to the cooperative effects of the catalytic functional groups.25–27 Having this point in mind, we envisioned a way in which the preface of Lewis acid (metal center) active sites to a halogen anion (X−) based ionic polymer could provide highly active, recyclable catalysts for the synthesis of heterocyclic compounds. In continued our research, we've replaced the organic groups with silica groups. Our study illustrated that the APTPOSS was a powerful and highly efficient support for the strength of the catalyst structure. Our goal was to enhance the strength of the catalyst structure by this replacement. This catalyst support via obstruction of Fe3O4/KCC-1 by APTPOSS (Fe3O4/KCC-1/APTPOSS). In fact, Fe3O4/KCC-1/APTPOSS is a nano labyrinth to hold the structure. We believe that this unique property will be very useful for the design of silica-supported catalysts, for which the accessibility of active sites can be increased significantly. Herein, we report the design and synthesis of a novel bifunctional complex composed of the cross-linked Fe3O4/KCC-1/APTPOSS as a substrate with the N,N′-bis({4-dimethylamino}salicylidene)ethylenediamino palladium(II) (salen-Pd(II)) Schiff base outer shell to serve as a catalyst for the synthesis pentafulvene (Scheme 1). It is noteworthy that this is the first report on the synthesis of magnetic nanoparticles that can be reused up to ten times without significant loss of catalytic activity.
The morphology and structure of the Fe3O4/KCC-1/APTPOSS and Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs are further characterized by TEM and FE-SEM. As shown in Fig. 1a, the Fe3O4/KCC-1/APTPOSS possesses a core of Fe3O4 particle, nonporous silica layer and silica fibres. The as-prepared magnetic core–shell fibrous silica material Fe3O4/KCC-1 with fibrous structure was uniform and monodispersed. Also, TEM and FE-SEM images of highly textured Fe3O4/KCC-1 samples, where the samples have spheres of uniform size with diameters of ∼300 nm and a wrinkled radial structure (Fig. 1a and e). A close inspection of these images shows that wrinkled fibers (with thicknesses of ∼8.5 nm) grow out from the center of the spheres and are arranged radially in three dimensions. Also, the overlapping of the wrinkled radial structure forms cone-shaped open pores. The TEM and FE-SEM images shows that the entire sphere is solid and composed of fibers. Furthermore, this open hierarchical channel structure and fibers are more easily for the mass transfer of reactants and increase the accessibility of active sites. The FE-SEM and TEM images of Fe3O4/KCC-1/salen/Pd(II) MNPs showed that after modification the morphology of Fe3O4/KCC-1 is not change (Fig. 1b and f). To assess the exact impact of the presence of APTPOSS in the catalyst, the Fe3O4/KCC-1/APTPOSS/salen/Pd(II) compared with Fe3O4/KCC-1/salen/Pd(II) MNPs. To further understand this issue, compared FE-SEM and TEM images of used catalyst with those of the fresh catalyst. Comparison of FE-SEM and TEM images of used catalyst with those of the fresh catalyst showed that the morphology and structure of Fe3O4/KCC-1/APTPOSS/salen/Pd(II) and Fe3O4/KCC-1/salen/Pd(II) MNPs remained intact after ten recoveries. Fig. 1d and h shows degradation of structure of Fe3O4/KCC-1/salen/Pd(II) MNPs in the reuse process. Its fiber structure has been destroyed. But, the functionalization of the Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs does not result in the change of the morphology (Fig. 1c and g). These study proves, this stable on structure of Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs were due to the presence of APTPOSS in the catalyst structure. APTPOSS can be a strong scaffold in KCC-1 structure.
The powder X-ray diffraction patterns of Fe3O4, Fe3O4/KCC-1, and Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs are shown in Fig. 2. As can be observed, all samples possess the typical diffraction peaks at (220), (311), (400), (422), (511) and (440), which are in good agreement with the data for standard Fe3O4 sample, as reported in the JCPDS card (no. 19-0629) (Fig. 2a). Besides the peak of iron oxide, the XRD pattern of Fe3O4/KCC-1/APTPOSS core–shell nanoparticles presented a broad featureless XRD peak at low diffraction angle, which corresponded to the amorphous silica (Fig. 2b). Fig. 2c shows a typical XRD pattern of the Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs. There was no change in it.
To confirm the thermal stability of the Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs, the thermogravimetric analysis of this material was performed at temperatures ranging from room temperature to 700 °C (Fig. 3). The weight loss below 250 °C was ascribed to the elimination of the physisorbed and chemisorbed solvent on the surface of the silica material. About 11.6% of the weight loss, in the temperature range 250–450 °C, was due to the organic group derivatives.
The N2 adsorption–desorption isotherms of Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs showed characteristic type IV curve (Fig. 4), which is consistent with literature reports on standard fibrous silica spheres. As for Fe3O4/KCC-1, the BET surface area, total pore volume, and BJH pore diameter are obtained as 427 m2 g−1, 1.23 cm3 g−1, and 14.51 nm respectively, whereas the corresponding parameters of Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs have decreased to 311 m2 g−1, 0.98 cm3 g−1, and 11.16 nm. The nitrogen sorption analysis of Fe3O4/KCC-1/salen/Pd(II) MNPs also confirms a regular and uniform mesostructure with a decrease in surface area, pore diameter and pore volume parameters in comparison with that of pristine Fe3O4/KCC-1. With the functionalization by salen/Pd–Si, the corresponding pore volumes are drastically reduced. This could be ascribed to increased loading with the sensing probe, which occupies a large volume inside the silica spheres (Fig. 4 and Table 1).
Catalysts | SBET (m2 g−1) | Va (cm3 g−1) | DBJH (nm) |
---|---|---|---|
Fe3O4/KCC-1 | 427 | 1.23 | 14.51 |
Fe3O4/KCC-1/APTPOSS/salen/Pd(II) | 311 | 0.98 | 11.16 |
The magnetic properties of the nanoparticles were characterized using a vibrating sample magnetometer (VSM). The magnetization curves of the obtained nanocomposite registered at 300 K show nearly no residual magnetism is detected (Fig. 5), which means that the nanocomposite exhibited the paramagnetic characteristics. Magnetic measurement shows that pure Fe3O4, and Fe3O4/KCC-1/APTPOSS/salen/Pd(II) have saturation magnetization values of 55.1, and 22.4 emu g−1 respectively. These nanocomposites with paramagnetic characteristics and high magnetization values can quickly respond to the external magnetic field and quickly redisperse once the external magnetic field is removed. The result reveals that the nanocomposite exhibit good magnetic responsible, which suggests a potential application for targeting and separation.
In addition, as seen in Fig. 6, by putting a magnet nearby the reaction mixture balloons can be seen the magnetic separation ability of catalyst. The magnet will attract the magnetic nanoparticles towards itself, and when the external magnet is removed, the catalyst will scatter in the solution with little shake.
FT-IR spectroscopy was employed to determine the surface modification of the synthesized catalyst (Fig. 7). The Si–O–Si symmetric and asymmetric stretching vibrations at 793 cm−1 and 1091 cm−1 and the O–H stretching vibration at 3430 cm−1 were observed for the Fe3O4/KCC-1 (Fig. 7a). The bands observed at 3121 and 2929 cm−1 are assigned to C–H stretching of aromatic and aliphatic moieties. Moreover, the signals cleared at 1462 and 1632 cm−1 are, respectively, attributed to CC and CN. (Fig. 7b). These results indicated that the salen had been successfully introduced onto the surface of Fe3O4/KCC-1.
To optimize reaction conditions for the Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs catalyst system, the effects of various reaction parameters were investigated. We examined the effect of solvent on the synthesis of pentafulvene using the Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs (Table 2). Solvent does affect on catalysts performance. n-Hexane, benzene, CCl4, or cyclohexane, an non-polar solvent, gave pentafulvene a lower yield (Table 2, entry 16–19). Also, i-PrOH, MeOH, EtOH, and H2O, protic polar solvents, gave also pentafulvene in low yields (Table 2, entry 20–23). The reaction was do better in aprotic polar solvent. CH3CN, THF, CH2Cl2, THF, toluene, dioxane, CHCl3, EtOAc, and DMSO gave pentafulvene in good yields (Table 2, entries 4–12). In this study, it was found that DMF is a more efficient (Table 2, entry 7) over other solvents. A solvent that stabilizes one of two competing transition states that control the selectivity should enhance the selectivity of the product obtained via the stabilized transition state. We also investigated the crucial role of temperature in the synthesis of pentafulvene in the presence of Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs as a catalyst. Results clearly indicated that the catalytic activity is sensitive to reaction temperature. The yield decreased when the temperature reached 130 °C. The best temperature for this reaction was at room temperature (Table 2, entry 1–7).
Entry | Solvent | Temp. (°C) | Yieldb (%) |
---|---|---|---|
a Reaction conditions: 2-acetyl-benzaldehyde (10 mmol), cyclopentadiene (70 mmol), and nano Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs (6 mg), and solvent (10 mL), 3 h.b GC yields [%]. | |||
1 | DMF | Reflux | 80 |
2 | DMF | 130 | 85 |
3 | DMF | 110 | 92 |
4 | DMF | 90 | 92 |
5 | DMF | 70 | 92 |
6 | DMF | 50 | 92 |
7 | DMF | r.t. | 92 |
8 | DMSO | r.t. | 74 |
9 | Dioxane | r.t. | 82 |
10 | CH3CN | r.t. | 69 |
11 | CH2Cl2 | r.t. | 77 |
12 | EtOAc | r.t. | 82 |
13 | THF | r.t. | 74 |
14 | Toluene | r.t. | 69 |
15 | CHCl3 | r.t. | 77 |
16 | n-Hexane | r.t. | 21 |
17 | Benzene | r.t. | 17 |
18 | CCl4 | r.t. | 15 |
19 | Cyclohexane | r.t. | 10 |
20 | H2O | r.t. | 29 |
21 | EtOH | r.t. | 21 |
22 | i-PrOH | r.t. | 32 |
23 | MeOH | r.t. | 18 |
24 | Solvent-free | r.t. | — |
The influence of time on this reaction is exhibited in Fig. 8. It is obvious that the pentafulvene yield increased up to 92% for 180 min. Whereas further increase in the time don't resulted in a slight decrease in the product yield. Therefore, the optimal time for synthesis of pentafulvene is 180 min.
The amount of catalyst is another important factor in current reaction for the synthesis of pentafulvene (Fig. 9). As shown in Fig. 9, in the absence of the catalyst no product was obtained. When 1–5 mg of catalyst was elaborated on sample reaction, moderate yields of product was obtained. The best result was achieved when the model reaction was carried out in the presence of 6 mg of catalyst. A rise in the catalyst amount showed no upgrading in the model reaction.
Fig. 9 Effect of increasing amount of Fe3O4/KCC-1/APTPOSS/salen/Pd(II) NPs on yield of pentafulvene. |
For further investigation the efficiency of the catalyst, different control experiments were performed and the obtained information is shown in Table 3. Initially, a standard reaction was carried out using Fe3O4/KCC-1/APTPOSS showed that any amount of the desired product was not formed after 60 min of reaction time (Table 3, entries 1). Also, when Fe3O4/KCC-1/APTPOSS/salen was used as the catalyst, a reaction was not observed (Table 3, entries 2). The salen could not give the satisfactory catalytic activity under mild reactions. Based on these disappointing results, we continued the studies to improve the yield of the product by added the Pd(II). Notably, there was difference in the reaction yields when reaction was carried out using Fe3O4/KCC-1/APTPOSS/salen/Pd(II) NPs and salen/Pd(II) catalyst (Table 3, entries 3 and 7). These results showed catalytic properties of N+Cl− in this structure. These results indicate that both of Pd(II) and ionic structure (N+Cl−) in this catalyst will maximize the catalyst performance. Also, salen/Pd(II) is not recoverable and reusable for the next runs. These observations show that the reaction cycle is mainly catalyzed by Pd(II) species complexed on the Fe3O4/KCC-1/APTPOSS/salen nanostructure. The nano-sized particles increase the exposed surface area of the active site of the catalyst, thereby enhancing the contact between reactants and catalyst dramatically and mimicking the homogeneous catalysts. As a result, Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs was used in the subsequent investigations because of its high reactivity, high selectivity and easy separation. Also, the activity and selectivity of nano-catalyst can be manipulated by tailoring chemical and physical properties like size, shape, composition and morphology. To assess the exact impact of the presence of KCC-1 in the catalyst, the Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs compared with MCM-41/salen/Pd(II), SBA-15/salen/Pd(II), and nano-SiO2/salen/Pd(II). When nano-SiO2/salen/Pd(II), MCM-41/salen/Pd(II) or SBA-15/salen/Pd(II) was used as the catalyst, the yield of the desired product was average to good, but the yield for Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs was excellent. Non-negligible activity of the silica was attributed to its shape, composition and morphology. Besides, the large space between fibers can significantly increase the accessibility of the active sites of the KCC-1. That is why, the KCC-1 was more effective than nano-SiO2, MCM-41, and SBA-15 (Table 3, entries 3–6). As a result, KCC-1 NPs were used in the subsequent investigations because of its high reactivity, high selectivity and easy separation (Table 3).
Entry | Catalyst | Yieldb (%) |
---|---|---|
a Reaction conditions: 2-acetyl-benzaldehyde (10 mmol), cyclopentadiene (70 mmol), and catalyst (6 mg), at room temperature for 3 h.b Isolated yield. | ||
1 | KCC-1 | — |
2 | Fe3O4/KCC-1/APTPOSS | — |
3 | Fe3O4/KCC-1/APTPOSS/salen/Pd(II) | 92 |
4 | Nano-SiO2/salen/Pd(II) | 53 |
5 | MCM-41/salen/Pd(II) | 74 |
6 | SBA-15/salen/Pd(II) | 80 |
7 | Salen/Pd(II) | 83 |
To examine the scope of the catalytic properties of the catalyst for synthesis of pentafulvene, various types of 2-acetyl-benzaldehydes was reacted with cyclopentadiene in the presence of a catalytic amount of Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs. Furthermore, electron rich and electron poor 2-acetyl-benzaldehydes react smoothly with cyclopentadiene in similar reaction conditions. The electron rich allylarene show good reactivity (90–94% yield) for the formation of the corresponding products in the C–C and C–H coupling reaction under similar reaction conditions. The relative reactivity of 2-acetyl-benzaldehydes towards the Pd(II) centre decreases in the order: MeO > Me (Table 4, entry 3 and 4). As shown in Table 4, C–C and C–H coupling reaction of cyclopentadiene with fluoro-2-acetyl-benzaldehyde proceeds smoothly under mild reaction conditions giving the reaction condition in excellent yields (Table 4, entries 2).
For further investigation the possibility of the heterogeneous nature of Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs, a kinetic study was performed. For this purpose, copper leaching was study for synthesis of pentafulvene under the optimized reaction condition. To determine the Pd(II) concentration in solution, five samples of the reaction mixture were taken during the reaction. The samples were analyzed by ICP-MS as well as the yield of the reaction was monitored by GC. The results were described in Fig. 10. No obvious leaching was observed, according to the ICP-MS data. According to the obtained results, the conclusion could be derived that the heterogenous palladium species aren't the catalyst promoter in this reaction.
It is important to note that the heterogeneous property of Fe3O4/KCC-1/APTPOSS/salen/Pd(II) MNPs facilitates its efficient recovery from the reaction mixture during work-up procedure. The activity of the recycled catalyst was also examined under the optimized conditions. After the completion of reaction, the catalyst was separated by filtration, washed with methanol and dried at the pump. The recovered catalyst was reused for ten consecutive cycles without any significant loss in catalytic activity (Fig. 11). This lack of reduction in catalyst performance can be attributed to the simple and stability of the catalyst structure. Comparison of FT-IR spectra of used catalyst with those of the fresh catalyst showed that the structure of salen remained intact after ten recoveries (Fig. 12). Also, the loading amount of salen in the fresh Fe3O4/KCC-1/APTPOSS/salen/Pd(II) and Fe3O4/KCC-1/APTPOSS/salen/Pd(II) after ten reuses as determined by TGA. The amount of salen in Fe3O4/KCC-1/APTPOSS/salen/Pd(II) after ten reuses was almost equal to the fresh Fe3O4/KCC-1/APTPOSS/salen/Pd(II) (Fig. 13). Also, the contents of Pd(II) in catalyst before and after reaction were 1.7% and 1.6% respectively, determined by ICP-MS. These indicate that most of Pd(II) species leaching into solution are recaptured onto the fibers of KCC-1 after completion of the reaction (Table 5).
Entry | Catalyst | wt% |
---|---|---|
1 | Fe3O4/KCC-1/APTPOSS/salen/Pd(II) | 1.7 |
2 | Fe3O4/KCC-1/APTPOSS/salen/Pd(II) after ten reuses | 1.6 |
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