Zahra Arabloo Narei,
Behnaz Shafiee and
Ahmad R. Khosropour*
Department of Chemistry, University of Isfahan, 81746-73441, Isfahan, Iran. E-mail: khosropour@chem.ui.ac.ir; Fax: +98 3116689732; Tel: +98 3117932700
First published on 9th February 2015
The expansion of practical processes for superferromagnetic nanocatalysts is a very attractive subject. In this work, we successfully developed a new and efficient procedure with combination of continuous flow technology with immobilizing of only 0.35 mol% of Nafion-H on silica-encapsulated supperparamagnetic iron oxide nanoparticles (SPIONs) to maximize catalyst efficiency for the synthesis of β-acetamido ketones. The turnover frequency value varies in the range of 1336 to 1577 h−1 compared to 256–515 h−1 in the conventional stirred reactor. Moreover, the catalyst could be quickly recovered by external magnetic field and could be reused for several reaction cycles without any change in its catalytic activity.
Therefore, extension of this investigation and presentation of a new derivative of this generation which could increase the efficiency of the catalyst is highly demanded.
Currently, a growing interest in various nanocatalysts employing the property of magnetic separation has been developed in a number of organic reactions.7 These magnetic nanoparticles (MNPs) that in some cases used as a support show excellent catalytic activity where magnetic separation behavior provides a very practical approach for removing of them from the reaction mixture.8 This can be considered as an environmentally benign that filtration steps were omitted in the reaction.9 Upon on this tremendously specification, various Lewis acids have been immobilized on them and their catalytic activity of these nanocatalysts studied in organic transformation so far.10
β-Acetamido ketones are vital intermediates in that their skeletons exist in a number of biologically or pharmacologically important compounds.11 The Dakin–West reaction as the best known route for the synthesis of these compounds is carried out through the condensation of an aryl aldehyde, acetophenone and acetyl chloride in acetonitrile in the presence of different Lewis or Brønsted acids such as CoCl2,12 montmorillonite K-10 clay,13 silica sulphuric acid,14 heteropoly acids,15 Zr(HSO4)2,16 [Et3N–SO3H]Cl,17 Fe3O4 nanoparticles18 and [(PS)2pi][OTf]2.19 Although, these methods are valuable, however some of them suffer from some disadvantages such as long reaction times (in some cases more than 7 h) or utilizing non-reusable catalysts. Therefore, the introduction of new and efficient methods for this multi-component reaction is still necessary. In this event, we felt that flow technology could considerably enhance rates due to improved heat and mass transfer.
Recently, micro-process technology allow a directed reactant flux through an immobilized catalyst, making them precise attractive process intensification tools by enhancing mass- and heat-transfer characteristics via low hold-up volumes and an excellent thermal transport capability and the ability to efficiently optimize reaction conditions by controlling of residence time.20 Moreover, the results illustrated that at a very short residence time in the microreactor even in scaling up the obtained yields were much higher than operating in the conventional stirring.21
Undoubtedly, one of the significant parameter in the flow reaction design is the kind of the catalyst which it is not only efficient but also could not block the channels of the chambers during of the reaction.22 Therefore, it seems that combination of nanocatalysts especially nano-superferromagnetic nanocatalysts with continuous flow systems could prepare a new and practical manner for overcoming of the aforementioned problems.
These features encouraged us to explore an innovative method for the sustainable synthesis of β-acetamido ketones by immobilization of Nafion-H on SPIONs (Nafion-H@SPIONs) in a continuous flow system.
Fig. 1 illustrates the FT-IR spectrums of SPIONs (a), and nanocatalyst Nafion-H@SPIONs (b) respectively.
The FT-IR spectrum of Nafion-H@SPIONs (Fig. 1b) showed absorption bands at 3400–3220 cm−1 (O–H stretching vibration), 1223 cm−1 (C–F) and 635–587 cm−1 (Fe–O) SPIONs.
The thermal stability of Nafion-H@SPIONs was also evaluated by TGA-DTG. According to this curve, two weight loss steps were observed. In the first step (around 100 °C), the water molecules (4.59%) in the structure were omitted, while only 11.28% of the organic part were lost between 40–425 °C (Fig. 2).
For the studying of morphology characteristics of Nafion-H@SPIONs, HR-TEM image was also investigated (Fig. 3). HR-TEM images of Nafion-H@SPIONs revealed that it appears to have almost a spherical structure with the average size about 9–11 nm (Fig. 3b).
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| Fig. 3 (a) HR-TEM image of Nafion-H@SPIONs and (b) Nafion-H@SPIONs particle size distribution histogram. | ||
The dc magnetic characterization of Fe3O4, the neat SPIONs nanoparticles and Nafion-H@SPIONs, were examined at room temperature in an external field range of ±10 kOe. In this investigation, due to the functionalization of SPIONS by Nafion-H, Ms (saturation magnetization) is found to be 20.3 emu g−1, which is considerably lower than that of the bulk magnetite (Fig. 4).
The schematic of the experimental setup is illustrated in Scheme 1. This procedure is very simple and no previous studies were available in the literature upon this protocol for this transformation. The microreactor system used in this study includes a T-shape micromixer and an in-house-made tubing glass reactor which can be implemented in any chemistry laboratory. The microtube reactor was fabricated in a glass column (internal diameter, 0.5 mm; internal volume, 0.6 mL; length, 200 cm), which was placed in a water bath.
Two syringes, fixed on a syringe pump, were used to introduce the reactants into the microreactor. Syringe A, consisted a sonicated mixture of an aldehyde (1 eq.), a nitrile (1.0 eq.) and Nafion-H@SPIONs (20 mg containing of 0.35 mol% Nafion-H) using THF as solvent with a concentration of 2 M and syringe B, involved a 2 M solution of an arylmethyl ketone (1.0 eq.) and acetyl chloride (1.0 eq.) in THF. A temperature controller (TC) was used for balancing and setting up heating. A round-bottom flask was connected to the flow reactor to collect the product. It should be noted that after the reaction was completed, the catalyst could be separated from the mixture by using a permanent magnet.
In an initial study with 3-nitrobenzaldehyde, acetyl chloride, acetonitrile and acetophenone as a template, revealed that the reaction temperature was a key factor for this transformation. It was found that at 40 °C with a residence time of 10 minutes the optimal isolated yield (90%) was obtained exclusively (Table 1, entry 5).
| Entry | Nafion-H loaded (mol%) | T/°C | Residence time/min | Yieldb (%) |
|---|---|---|---|---|
| a Reaction condition: 3-nitobenzadehyde (1.0 eq.), acetophenone (1.0 eq.), acetyl chloride (1.0 eq.), and acetonitrile (1.0 eq.) in the presence of 20 mg Nafion-H@SPIONs.b Isolated yield.c In 30 mg Nafion-H@SPIONs.d Under traditional conditions in a flask after 10 min. | ||||
| 1 | — | 40 | 10 | 5 |
| 2 | 0.087 | 40 | 10 | 32 |
| 3 | 0.174 | 40 | 10 | 45 |
| 4 | 0.261 | 40 | 10 | 62 |
| 5 | 0.35 | 40 | 10 | 90 |
| 6 | 0.35c | 40 | 10 | 83 |
| 7 | 0.35 | 60 | 10 | 87 |
| 8 | 0.35 | 30 | 10 | 58 |
| 9 | 0.35 | 40 | 20 | 90 |
| 10 | 0.35 | 50 | 30 | 91 |
| 11 | 0.35d | 40 | — | 52 |
We found that the catalyst could greatly act on this transformation.
Notably, lower yields were obtained when the same reaction carried out with utilizing of lower amount of the catalyst loading (Table 1, entries 2–4). On the other hand, in the absence of any catalyst the product was obtained very slightly (Table 1, entry 1).
Moreover, temperature is also a key factor in this reaction. The improvement in the conversion (90%) was reached at 40 °C (Table 1, entry 5). Higher temperature made no obvious difference in the yield of the product (Table 1, entry 7) but using lower one (30 °C), sharply decreased the conversion to 58% yield (Table 1, entry 8). Further evaluations showed when the flow rate was decreased to 0.06 mL min−1, the desired product increased to 90% surprisingly (Table 1, entry 5). Further decrease (0.05 mL min−1 to 0.04 mL min−1) makes no obvious difference in the yield of the product (Table 1, entries 9, 10).
In contrast to the traditional manner in a flask, it is interesting to note that the product of the model reaction was produced in a lesser amount, indicating a relatively slow conversion of it under the condition (Table 1, entry 11). Therefore, these achievements firmly approved that both the catalyst and continuous flow method have crucial impact on this transformation.
We assume that one of the beneficial effect of continuous flow on this reaction may be attributed to a better dispersion of the nanocatalyst in an at least volume in comparison with magnetically stirred reaction, which it make the catalyst more effective in this transformation.
Next, upon the optimum conditions, a series of β-acetamido ketones were prepared with excellent turnover frequency (>1300 h−1) (Table 2) with representing a noteworthy acceleration compared to the corresponding batch experiments with lower one (<512 h−1).
| Entry | R1 | R2 | R | Yielda,b (%) | TOFb (h−1) | Yielda,c (%) | TOFc (h−1) |
|---|---|---|---|---|---|---|---|
| a Isolated yield.b [mol product/Nafion-H]/h under the flow reaction.c [mol product/Nafion-H]/h under conventional stirred in a flask at 75 °C.d After 30 min.e After 40 min.f After 35 min.g After 50 min.h After 45 min. | |||||||
| 1 | H | H | CH3 | 92 | 1577 | 87d | 497 |
| 2 | 3-NO2 | H | CH3 | 90 | 1542 | 90e | 256 |
| 3 | 4-NO2 | H | CH3 | 87 | 1490 | 85e | 364 |
| 4 | 4-Cl | H | CH3 | 89 | 1526 | 84f | 410 |
| 5 | 4-CHO | H | CH3 | 80 | 1372 | 78g | 266 |
| 6 | 4-CH3O | H | CH3 | 90 | 1542 | 90d | 515 |
| 7 | 2-HO | H | CH3 | 82 | 1404 | 75h | 284 |
| 8 | H | 4-Br | CH3 | 91 | 1562 | 87d | 497 |
| 9 | 4-Cl | 4-Cl | CH3 | 88 | 1508 | 85f | 418 |
| 10 | 4-Cl | 4-CH3O | CH3 | 78 | 1336 | 75g | 256 |
| 11 | 4-CHO | 4-Cl | CH3 | 89 | 1526 | 82h | 313 |
| 12 | 4-Cl | H | C6H3 | 87 | 1490 | 83d | 475 |
| 13 | 4-Cl | H | 4-ClC6H3 | 90 | 1544 | 90d | 515 |
This protocol also avoids the problems associated with handling, safety and pollution. Nafion-H@SPIONs can act as eco-friendly catalytic system for a variety of organic transformations, since it is non-volatile, non-explosive, easy to handle and thermally robust. The use of Nafion-H@SPIONs as a powerful nano-catalyst in combination with continuous flow system showed rate enhancements, high yields and short reactions times.
The recovered Nafion-H@SPIONs could also be reused straightforward by an applied magnetic field after the end of the reaction without any significant loss of its high catalytic performance (Fig. 5).
The results illustrated the excellent stability of the catalyst under the reaction condition (Fig. 6). The performance of the recovered catalyst during the synthesis of the template reaction was found to be satisfactory and no considerable variation in the yield.
A plausible rationalization upon the literature11c for the Dakin–West reaction is shown in Scheme 2.
In summary, we have introduced the synthesis of a new and robust nanocatalyst which employed in the Dakin–West reaction, providing the corresponding products in very high to excellent yields. Moreover, for the first time, it was developed a simple system that allows combination of a superferromagnetic nanocatalyst and continuous flow technology as an expeditious process for the synthesis of β-acetamido ketones through a multicomponent reaction. The turnover frequency value is varied in the range of 1336 to 1577 h−1 in this investigation, while the value is only ca. 260–520 h−1 in a conventional stirred reactor. The catalyst loading is significantly lower than all cases that previously reported for the synthesis of β-acetamido ketones. Very high recyclability of the catalyst (more than seven runs) is other main characteristic of the process. Further investigations on the aspect of combination of nano-catalyst and micro-flow system are currently ongoing in our laboratory.
Mp: 110–112 °C. IR (KBr) νmax = 3290, 1687, 1652 cm−1; 1H-NMR (400 MHz; CDCl3) δ = 2.07 (s, 3H, CH3), 3.50 (dd, J = 6.0 and 16.0 Hz, 1H, CH2), 3.80 (dd, J = 5.2 and 16.0 Hz, 1H, CH2), 5.70–5.72 (m, 1H), 7.10 (d, J = 8.0 Hz, 1H, NH), 7.45–7.61 (m, 5H, Ar-H), 7.73 (d, J = 8.0 Hz, 1H, Ar-H), 7.91 (d, J = 7.2 Hz, 1H, Ar-H), 8.10 (d, J = 8.0 Hz, 1H, Ar-H) 8.24 (s, 1H, Ar-H); 13C-NMR (100 MHz, CDCl3) δ: 198.08, 169.82, 148.40, 143.44, 136.16, 134.01, 132.96, 129.57, 128.88, 128.10, 126.37, 124.87, 122.41, 121.34, 49.06, 42.74, 23.42.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c4ra15466e |
| This journal is © The Royal Society of Chemistry 2015 |