Seyed Mohsen Sadeghzadeh*,
Rahele Zhiani and
Shokufe Emrani
Department of Chemistry, Faculty of Sciences, Islamic Azad University Neyshabur Branch, Neyshabur, Iran. E-mail: seyedmohsen.sadeghzadeh@gmail.com; Fax: +98 561 2502065; Tel: +98 561 2502065
First published on 10th May 2017
In this study, fibrous nanosilica (KCC-1) was functionalized with octakis[3-(3-aminopropyltriethoxysilane)propyl]octasilsesquioxane (APTPOSS) groups acting as the strong performers so that the palladium nanoparticles (Pd NPs) were well-dispersed on the fibers of the KCC-1 microspheres. The synthesized Pd/APTPOSS@KCC-1 nanocatalyst exhibited excellent catalytic activity for one-pot new C–H activation.
Heterogenization of the corresponding catalysts has become a significant tool to overcome various drawbacks, including catalyst recovery, product separation, environmental pollution and high reaction temperatures.5–8 Along this line, the use of nanometals as catalysts has spread rapidly.9–13 It has resulted in the development of several active and efficient nanocatalysts for various protocols that have several advantages over traditional catalysts such as superior activity and stability. The metal nanocatalysts can be immobilized on the support through two approaches. The first one is to deposit the presynthesized metal nanoparticles onto the support by chemical adsorption, which allows fine control over the size and shape of the metal nanoparticles. However, with this approach, the adsorbed nanocatalysts are easily leached from the support during the catalytic reaction. The other is approach is to directly grow metal nanoparticles on the support using the pregrafted organic functional molecules or polymers as a stabilizer. This method is much better for holding the metal nanoparticles. Periodic mesoporous organosilicas (PMOs) are from this class of functionalized ordered nanoporous materials. PMOs are synthesized by the simultaneous hydrolysis and condensation of alkoxysilane precursors bridged to organic groups in the presence of structure directing agents. PMOs can be easily recovered and reused in a typical chemical process.14–27 Along this line, we prepared and developed metal containing organic-based periodic mesoporous organosilica materials and studied their catalytic applications for synthesis of benzo[c]pyrazolo[1,2-a]cinnolin-1-ones. Continuing our research, we have replaced the organic groups with silica groups. Our study illustrated that APTPOSS was a powerful and highly efficient support for the successful immobilization and stabilization of the metal catalysts. Our goal was to enhance the strength of the catalyst structure by this replacement. This catalyst support functions via obstruction of KCC-1 by APTPOSS (APTPOSS@KCC-1). In fact, APTPOSS@KCC-1 is a nano labyrinth to hold the nanoparticle. 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. This study aimed to develop novel catalysts and noble metal nanoparticles for the synthesis benzo[c]pyrazolo[1,2-a]-cinnolin-1-ones by an eco-friendly method (Scheme 1). In this study, APTPOSS@KCC-1 was used as a new supporting material to stabilize Pd nanoparticles (Pd NPs) to obtain Pd/APTPOSS@KCC-1 nanocatalysts with enhanced accessibility for active sites and high surface area. We compared the three structures of APTPOSS@KCC-1, hyperbranched polyglycerol@KCC-1 (HPG@KCC-1), and ionic liquid@KCC-1 (IL@KCC-1) for the synthesis benzo[c]pyrazolo[1,2-a]cinnolin-1-one. APTPOSS@KCC-1 displayed not only suitable catalytic reaction rate but also excellent reusability in the catalytic reaction. The strong activity of this catalyst is attributed to its high accessibility and low probability of the aggregation and leaching of the nanoparticles on the APTPOSS@KCC-1 support system.
Scheme 1 Synthesis of benzo[c]pyrazolo[1,2-a]cinnolin-1-ones in the presence of Pd/X@KCC-1 (X = APTPOSS, HPG, and IL) NPs. |
FT-IR spectroscopy was employed to determine the surface modification of the synthesized catalyst (Fig. 1). The SiO–Si symmetric and asymmetric stretching vibrations at 802 cm−1 and 1103 cm−1, respectively, and the O–H stretching vibration at 3444 cm−1 were observed for the KCC-1 (Fig. 1a). The bands observed at 3121 and 2929 cm−1 are assigned to the C–H stretching of aromatic and aliphatic moieties, respectively. Moreover, the signals cleared at 1563 and 1635 cm−1 are, respectively, attributed to CC and CN stretching vibrations of the imidazolium ring (Fig. 1b). These results indicated that the imidazolium IL had been successfully introduced onto the surface of KCC-1. The successful functionalization of the APTPOSS based organic–inorganic hybrid on the KCC-1 surface is evidenced by two broad peaks at about 1000–1150 cm−1, assigned to Si–O stretching vibrations, as well as the presence of C–H stretching at 2950 cm−1 and C–H bending vibration at approximately 1450 cm−1 observed in Fig. 1c.
The XRD patterns of KCC-1 NPs, Pd/IL@KCC-1, and Pd/APTPOSS@KCC-1 NP catalyst are shown in Fig. 2. The broad peak between 20° and 30° corresponds to amorphous silica (Fig. 2a). Moreover, new peaks at 2θ = 40.1°, 46.5° and 68° reflection of the Pd (JCPDS 05-0681) (Fig. 2b) crystal were observed for Pd/APTPOSS@KCC-1, confirming the successful growth of Pd particles on the surface of APTPOSS@KCC-1 again. The broad peak between 20° and 30° corresponds to amorphous silica. XRD analysis can easily be indexed to the cubic phase of Pd NPs. Fig. 1c reveals that Pd NPs exhibit sharp peaks of Pd (111), Pd (200), Pd (220) and Pd (311), which also verify the existence of fcc-Pd, confirming the successful growth of metal particles on the surface of IL@KCC-1 again.
The structures of the synthesized Pd/IL@KCC-1 and Pd/APTPOSS@KCC-1 NPs were analyzed by TEM (Fig. 3). The as prepared KCC-1 microspheres with fibrous structure were uniform and monodispersed (Fig. 3). The average diameter of the microspheres was about 200–220 nm. TEM image shown in Fig. 3 further clarifies that the distance between the two fibers was about 10–15 nm. Moreover, after Pd was anchored, the metal nanoparticles are clearly distinguishable with the difference in their contrast. As can be observed, the as-prepared metal nanoparticles are spherical without obvious aggregation (Fig. 3a and b).
The N2 adsorption–desorption isotherms of Pd/X@KCC-1 (X = APTPOSS, IL, and HPG) showed characteristic type IV curve, which is consistent with literature reports on standard fibrous silica spheres (Fig. 4). For Pd/APTPOSS@KCC-1, Pd/IL@KCC-1, and Pd/HPG@KCC-1, the BET surface areas were 231, 238, and 195 m2 g−1; pore diameters were 11.26, 11.52, and 10.97 nm; and pore volumes 1.02, 0.98, and 0.87 cm3 g−1, respectively. The nitrogen sorption analysis of Pd/APTPOSS@KCC-1 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 KCC-1. With the functionalization by X–Si (X = APTPOSS, IL, and HPG), 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 (Table 1).
Fig. 4 Adsorption–desorption isotherms of (a) Pd/APTPOSS@KCC-1, (b) Pd/IL@KCC-1, and (c) Pd/HPG@KCC-1. |
Catalysts | SBET (m2 g−1) | Vt (cm3 g−1) | DBJH (nm) |
---|---|---|---|
KCC-1 | 439 | 1.49 | 14.78 |
Pd/APTPOSS@KCC-1 | 231 | 1.02 | 11.26 |
Pd/IL@KCC-1 | 238 | 0.98 | 11.52 |
Pd/HPG@KCC-1 | 195 | 0.87 | 10.97 |
The catalytic potential of the Pd/APTPOSS@KCC-1, Pd/IL@KCC-1, and Pd/HPG@KCC-1 NPs was evaluated in condensation reactions. At first, the reaction of ethyl acetoacetate (10 mmol), phenylhydrazine hydrate (10 mmol), and aryl iodide (12 mmol) was chosen as a model reaction to optimize the reaction conditions, such as the amount of catalyst, temperature, time, and solvent (Table 2). Applying 12 mg of catalyst in 50 mL TFA is the best conditions for the reaction. Moreover, it was found that conventional heating under reflux for 8 h is more efficient. In all cases, higher catalyst power of Pd/IL@KCC-1 was evident relative to that of Pd/APTPOSS@KCC-1 and Pd/HPG@KCC-1. Reaction was conducted in a shorter time in the presence of the Pd/IL@KCC-1. This ability was due to the presence of ionic liquid on the catalyst structure. The ionic liquid may play the role of a catalyst in the reaction. Among the studied bases, K2CO3 showed the best results for this reaction in terms of reaction time and yield and also K2S2O8 was the best oxidant for this reaction (Table 3).
Entry | Catalyst | Solvent | Temp. (°C) | Time (h) | Yielda (%) |
---|---|---|---|---|---|
a Isolated yields. | |||||
1 | Pd/APTPOSS@KCC-1 | — | 100 | 8 | — |
Pd/IL@KCC-1 | — | ||||
Pd/HPG@KCC-1 | — | ||||
2 | Pd/APTPOSS@KCC-1 | TFA | Reflux | 8 | 87 |
Pd/IL@KCC-1 | 91 | ||||
Pd/HPG@KCC-1 | 88 | ||||
3 | Pd/APTPOSS@KCC-1 | EtOH | Reflux | 8 | 51 |
Pd/IL@KCC-1 | 39 | ||||
Pd/HPG@KCC-1 | 53 | ||||
4 | Pd/APTPOSS@KCC-1 | H2O | Reflux | 8 | 45 |
Pd/IL@KCC-1 | 31 | ||||
Pd/HPG@KCC-1 | 46 | ||||
5 | Pd/APTPOSS@KCC-1 | CH2Cl2 | Reflux | 8 | 64 |
Pd/IL@KCC-1 | 67 | ||||
Pd/HPG@KCC-1 | 62 | ||||
6 | Pd/APTPOSS@KCC-1 | n-Hexane | Reflux | 8 | — |
Pd/IL@KCC-1 | — | ||||
Pd/HPG@KCC-1 | — | ||||
7 | Pd/APTPOSS@KCC-1 | TFA | 60 | 8 | 74 |
Pd/IL@KCC-1 | 80 | ||||
Pd/HPG@KCC-1 | 75 | ||||
8 | Pd/APTPOSS@KCC-1 | TFA | 40 | 8 | — |
Pd/IL@KCC-1 | — | ||||
Pd/HPG@KCC-1 | — | ||||
9 | Pd/APTPOSS@KCC-1 | TFA | Reflux | 7 | 84 |
Pd/IL@KCC-1 | 90 | ||||
Pd/HPG@KCC-1 | 85 | ||||
10 | Pd/APTPOSS@KCC-1 | TFA | Reflux | 6 | 72 |
Pd/IL@KCC-1 | 90 | ||||
Pd/HPG@KCC-1 | 71 | ||||
11 | Pd/APTPOSS@KCC-1 | TFA | Reflux | 5 | 68 |
Pd/IL@KCC-1 | 86 | ||||
Pd/HPG@KCC-1 | 65 | ||||
12 | Pd/APTPOSS@KCC-1 | TFA | Reflux | 8 | 87 |
Pd/IL@KCC-1 | 91 | ||||
Pd/HPG@KCC-1 | 88 | ||||
13 | Pd/APTPOSS@KCC-1 | TFA | Reflux | 8 | 76 |
Pd/IL@KCC-1 | 91 | ||||
Pd/HPG@KCC-1 | 78 | ||||
14 | Pd/APTPOSS@KCC-1 | TFA | Reflux | 8 | 67 |
Pd/IL@KCC-1 | 85 | ||||
Pd/HPG@KCC-1 | 69 |
Entry | Catalyst | Base | Oxidant | Yielda (%) |
---|---|---|---|---|
a Isolated yields. | ||||
1 | Pd/APTPOSS@KCC-1 | K2CO3 | K2S2O8 | 87 |
Pd/IL@KCC-1 | 91 | |||
Pd/HPG@KCC-1 | 88 | |||
2 | Pd/APTPOSS@KCC-1 | K2CO3 | — | — |
Pd/IL@KCC-1 | — | |||
Pd/HPG@KCC-1 | — | |||
3 | Pd/APTPOSS@KCC-1 | K2CO3 | AgOAc | 60 |
Pd/IL@KCC-1 | 61 | |||
Pd/HPG@KCC-1 | 58 | |||
4 | Pd/APTPOSS@KCC-1 | K2CO3 | Ag2O | 48 |
Pd/IL@KCC-1 | 53 | |||
Pd/HPG@KCC-1 | 46 | |||
5 | Pd/APTPOSS@KCC-1 | K2CO3 | Cu(OAc)2 | 54 |
Pd/IL@KCC-1 | 52 | |||
Pd/HPG@KCC-1 | 53 | |||
6 | Pd/APTPOSS@KCC-1 | K2CO3 | (NH4)2S2O8 | 32 |
Pd/IL@KCC-1 | 35 | |||
Pd/HPG@KCC-1 | 37 | |||
7 | Pd/APTPOSS@KCC-1 | — | K2S2O8 | — |
Pd/IL@KCC-1 | — | |||
Pd/HPG@KCC-1 | — | |||
8 | Pd/APTPOSS@KCC-1 | CsF | K2S2O8 | 38 |
Pd/IL@KCC-1 | 45 | |||
Pd/HPG@KCC-1 | 37 | |||
9 | Pd/APTPOSS@KCC-1 | Na2CO3 | K2S2O8 | 74 |
Pd/IL@KCC-1 | 70 | |||
Pd/HPG@KCC-1 | 72 | |||
10 | Pd/APTPOSS@KCC-1 | Et3N | K2S2O8 | 84 |
Pd/IL@KCC-1 | 90 | |||
Pd/HPG@KCC-1 | 85 | |||
11 | Pd/APTPOSS@KCC-1 | NaOAc | K2S2O8 | 68 |
Pd/IL@KCC-1 | 66 | |||
Pd/HPG@KCC-1 | 65 | |||
12 | Pd/APTPOSS@KCC-1 | KOH | K2S2O8 | 36 |
Pd/IL@KCC-1 | 39 | |||
Pd/HPG@KCC-1 | 37 | |||
13 | Pd/APTPOSS@KCC-1 | K3PO4 | K2S2O8 | 39 |
Pd/IL@KCC-1 | 37 | |||
Pd/HPG@KCC-1 | 40 | |||
14 | Pd/APTPOSS@KCC-1 | Cs2CO3 | K2S2O8 | 52 |
Pd/IL@KCC-1 | 55 | |||
Pd/HPG@KCC-1 | 48 |
To assess the exact impact of the presence of APTPOSS in the catalyst, Pd/APTPOSS@KCC-1 was compared with Pd/IL@KCC-1 and Pd/HPG@KCC-1. The loading amount of Pd in Pd/APTPOSS@KCC-1, Pd/IL@KCC-1, and Pd/HPG@KCC-1 was determined by inductively coupled plasma (ICP). The amount of Pd in Pd/APTPOSS@KCC-1 was less than the amount of Pd/HPG@KCC-1, but it is almost equal with that of Pd/IL@KCC-1. This amount was reused for ten consecutive cycles of catalysis, and the amount of Pd in Pd/APTPOSS@KCC-1, Pd/IL@KCC-1 and Pd/HPG@KCC-1 was stable. However, this amount was reduced by half in KCC-1. The abilities of the Pd/APTPOSS@KCC-1, Pd/IL@KCC-1, and Pd/HPG@KCC-1 are attributed to APTPOSS, IL, and HPG units that effectively manage the reaction by preventing Pd agglomeration and releasing and recapturing Pd during the reaction process. It is interesting that the amount of Pd in Pd/APTPOSS@KCC-1 was stable after being reused for twenty cycles, wherein a significant reduction in the amount of Pd in Pd/HPG@KCC-1 and Pd/IL@KCC-1 was observed. This remarkable ability of the Pd/APTPOSS@KCC-1 mesostructure may be attributed to stability of coupling APTPOSS and KCC-1 (Table 4). To examine this matter, the loading amount of HPG and IL in the fresh Pd/HPG@KCC-1 and Pd/IL@KCC-1 after twenty reuses was determined by TGA. The amount of HPG and IL in Pd/HPG@KCC-1 and Pd/IL@KCC-1 after twenty reuses was about half that of the fresh Pd/HPG@KCC-1 and Pd/IL@KCC-1, but the amount of APTPOSS in Pd/APTPOSS@KCC-1 was equal to the fresh Pd/APTPOSS@KCC-1 (Fig. 5).
Entry | Catalyst | Reuse wt% | ||
---|---|---|---|---|
1 | 10 | 20 | ||
1 | Pd/KCC-1 | 4.3 | 2.2 | 0.9 |
2 | Pd/HPG@KCC-1 | 6.2 | 5.9 | 1.9 |
3 | Pd/IL@KCC-1 | 5.7 | 5.1 | 2.7 |
4 | Pd/APTPOSS@KCC-1 | 5.9 | 5.8 | 5.5 |
Fig. 5 TGA diagram of (a) Pd/HPG@KCC-1, (b) Pd/IL@KCC-1, and (c) Pd/APTPOSS@KCC-1. (Blue) new catalyst. (Red) recovered catalyst. |
To further understand this issue, we compared TEM images of used catalyst with those of the fresh catalyst. Comparison of TEM images of used catalyst (Fig. 6) with those of the fresh catalyst (Fig. 3) showed that the morphology and structure of Pd/X@KCC-1 (X = APTPOSS, IL, and HPG) NPs remained intact after twenty recoveries. Fig. 6 shows degradation of the structure of Pd/HPG@KCC-1 and Pd/IL@KCC-1 in the reuse process, but the amount of degradation was more in Pd/IL@KCC-1 (Fig. 6a and b). However, the functionalization of the Pd/APTPOSS@KCC-1 NPs does not result in the change of the morphology (Fig. 6c). This study proves that the stabilities of the structures of Pd/APTPOSS@KCC-1 NPs were due to the presence of APTPOSS in the catalyst structure. APTPOSS can be a strong scaffold in the KCC-1 structure.
Fig. 6 TEM images of (a) Pd/IL@KCC-1 NPs, (b) Pd/HPG@KCC-1 NPs, and (c) Pd/APTPOSS@KCC-1 NPs after ten reuses. |
With the optimized reaction conditions in hand, we next managed to examine the scope and limitation of this palladium cross-coupling reaction with various types of phenylhydrazine hydrates and aryl iodides. The results of this study are collected in Table 5. As can be seen from Table 5, electronic effects and the nature of substituents on the phenylhydrazine hydrates and aryl iodides did not show strong obvious effects in terms of yields under the reaction conditions. Phenylhydrazine hydrates and aryl iodides containing electron-withdrawing groups or electron-donating groups were employed and reacted well to give the desired products in good yields with high purity.
Entry | Phenylhydrazine hydrate | Aryl iodide | Time (h) | Yieldb (%) |
---|---|---|---|---|
a Reaction conditions: ethyl acetoacetate (10 mmol), phenylhydrazine hydrates (10 mmol), aryl iodides (12 mmol), K2CO3 (10 mmol), K2S2O8 (10 mmol) and Pd/HPG@KCC-1 NPs (12 mg) were stirred with heating under reflux in TFA (30 mL) for 8–10 hours.b Isolated yields (%). | ||||
1 | 8 | 87 | ||
2 | 8 | 82 | ||
3 | 10 | 79 | ||
4 | 9 | 81 | ||
5 | 9 | 85 | ||
6 | 8 | 80 | ||
7 | 9 | 80 | ||
8 | 8 | 86 | ||
9 | 10 | 84 | ||
10 | 10 | 77 | ||
11 | 10 | 75 |
The recovery and reuse of a catalyst is highly preferable for a catalytic process. Our goal since the development of silica was the production of a new support with high power in recovery and reuse. After ten reuse cycles from Pd/KCC-1, the catalyst performance decreased by half, and after twenty, this amount was below twenty percent. To solve this problem, functionalization was achieved by post-synthetic modification of the fibers of KCC-1 by reaction with IL and HPG to produce IL@KCC-1 and HPG@KCC-1, which could then act as pseudochelators or ligands to control the metal leaching during the reaction. After twenty consecutive reuses, the IL@KCC-1 and HPG@KCC-1 could not give a satisfactory catalytic activity under mild reactions. After ten reuse cycles from IL@KCC-1 and HPG@KCC-1, the catalyst performance fell between 30% and 40%. Based on these frustrating results, we continued the research to improve the yield of the product by adding the APTPOSS to the catalyst. Pd/APTPOSS@KCC-1 NPs exhibited catalytic activity almost identical to that of the fresh catalyst (Table 6). The reason for this difference in yield was the designed and synthesized APTPOSS functionalized KCC-1. Moreover, the blockage of pore entrances by APTPOSS could also account for the decreased leaching of nanoparticles.
Catalyst | Recycle | |||||||||||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 9 | 10 | 11 | 12 | 13 | 14 | 15 | 16 | 17 | 18 | 19 | 20 | |
Pd/APTPOSS@KCC-1 | 87 | 87 | 87 | 87 | 87 | 87 | 87 | 87 | 86 | 86 | 86 | 86 | 86 | 86 | 86 | 86 | 85 | 85 | 85 | 85 |
Pd/IL@KCC-1 | 91 | 91 | 90 | 90 | 90 | 89 | 87 | 85 | 85 | 85 | 80 | 74 | 69 | 63 | 58 | 52 | 47 | 41 | 36 | 28 |
Pd/HPG@KCC-1 | 88 | 88 | 88 | 86 | 83 | 81 | 78 | 75 | 71 | 67 | 65 | 60 | 58 | 54 | 49 | 47 | 43 | 39 | 36 | 32 |
Pd/KCC-1 | 64 | 59 | 52 | 50 | 47 | 41 | 39 | 35 | 34 | 30 | 29 | 29 | 27 | 24 | 21 | 18 | 17 | 17 | 14 | 12 |
This journal is © The Royal Society of Chemistry 2017 |