Ramen
Jamatia
,
Ajay
Gupta
and
Amarta Kumar
Pal
*
Department of Chemistry, North Eastern Hill University, Mawlai Campus, Shillong 793022, India. E-mail: amartya_pal22@yahoo.com; Fax: +91 364 2550076; Tel: +91 364 2307930 ext. 2636
First published on 10th February 2016
A glutathione grafted nano-organocatalyst (nano-FGT) was used as an efficient catalyst for the synthesis of spirooxindole derivatives. An aqueous medium, easy separation by an external magnet, efficient catalyst reusability, low catalyst loading, and column chromatography free separation of the product makes the present procedure green, sustainable and economically viable. The TON and TOF of the nanocatalyst reached 850000 and 56
667 min−1 respectively.
Spirooxindole derivatives are privileged indole containing heterocycles of relevant biological and medicinal importance like antitumoral, antifungal and antibacterial activity, inhibitor of muscarinic serotonin receptors and microtubular activity (Fig. 1).10,11 Because of the tremendous biological and medicinal activities, a growing research towards a much efficient, environmentally benign and cost efficient synthetic methods is still appreciated. Some synthetic methods involve the use of catalyst such as InCl3,12 SnCl4,13 NEt3,14 NH4Cl,15 Sodium stearate,16 MgO,17 L-proline,18 silica-supported organocatalyst19 and lipase20 etc. are reported. All this reported methods have their own advantages but at the same time they suffer some drawbacks like use of large amount of catalyst,21 high temperature,22 long reaction time14,23 and unreusable catalyst.24 If the catalyst is reusable but separation is difficult.25 So there is enough room for innovation of new synthetic method. Herein, we report nano-FGT as a viable greener catalyst for the synthesis of spirooxidoles under reflux condition in water within a short period of time, offering high yield with high purity of the product without column chromatographic separation. Easy separation and reusability of the catalyst up to eight consecutive runs makes this procedure sustainable.
Entry | Catalyst | Temperature (°C) | Time (min) | Product | Yield (%) |
---|---|---|---|---|---|
a Reaction condition: isatin (1a, 1 mmol), malononitrile (2a, 1 mmol), dimedone (3a, 1 mmol) and catalyst in water (3 mL). r.t = room temperature. | |||||
1 | Glutathione (10 mol%) | 80 | 15 | 4aaa | 96 |
2 | Cysteine (10 mol%) | 80 | 15 | 4aaa | 88 |
3 | L-Proline (10 mol%) | 80 | 15 | 4aaa | 91 |
4 | Without catalyst | r.t | 15 | 4aaa | 14 |
5 | Without catalyst | 80 | 15 | 4aaa | 21 |
6 | Fe3O4 NPs (8 mg) | 80 | 15 | 4aaa | 66 |
7 | Nano-FGT (8 mg) | r.t | 15 | 4aaa | 57 |
8 | Nano-FGT (8 mg) | 40 | 15 | 4aaa | 69 |
9 | Nano-FGT (8 mg) | 60 | 15 | 4aaa | 85 |
10 | Nano-FGT (8 mg) | 80 | 15 | 4aaa | 94 |
11 | Nano-FGT (8 mg) | 100 | 15 | 4aaa | 94 |
Transmission electron microscope (TEM) was used to analyze the particle size of the prepared nano-FGT. The TEM image is indicative of the fact that the prepared nano-FGT were in the nanometer range. Further, the TEM image shows the uniform distribution of the synthesized nano-FGT with an average size of 10–20 nm (Fig. 2) and also the uniform coating of glutathione over the ferrite NPs (Fig. 2c). Scanning electron microscope (SEM) was also used to examine the surface morphology of the prepared catalyst. From SEM image it is evident that the nano-FGT are spherical in shape (Fig. 3a). Energy Dispersive X-ray (EDX) analysis also indicates the formation of the nano-FGT. The EDX spectra clearly show the presence of Fe, O, C, S and N which is evident for the anchoring of the glutathione to the ferromagnetic Fe3O4 NPs (Fig. 4). Infra-red spectroscopy also provides useful information about the anchoring of glutathione to the ferromagnetic Fe3O4NPs. The strong absorption peak at 599 cm−1 corresponds to the Fe–O stretching of the Fe3O4 NPs. The stretching peaks at 1643 and 1634 cm−1 is characteristic of the acid and amide carbonyls of glutathione respectively. Further, absorption peaks at 3349 and 3166 cm−1 correspond to the –OH and –NH2 groups. The absence of a strong absorption peak at 2525 cm−1 which is characteristic peak of –SH group manifest for the anchoring of glutathione through the thiol group to the Fe3O4 NPs (see ESI, Fig. S1†). The stability of the nano-FGT was also examined by Thermo Gravimetric Analysis (TGA). The degradation at 53 °C in the TGA thermogram corresponds to the solvent molecules trapped. The weight loss at 185 °C is due to the glutathione of nano-FGT. Therefore, the catalyst shows relative stability below 180 °C and can safely be used for organic transformation reactions within this temperature range (Fig. 5).
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Fig. 2 TEM image of nano-FGT at (a) lower magnification (b) before use at 10 nm (c) before use at 5 nm (d) after use at 10 nm and (e) SAED of the catalyst before use. |
We initiated our study by taking isatin (1a, 1 mmol), malononitrile (2a, 1 mmol), dimedone (3a, 1 mmol) and nano-FGT in water (3 mL) as the model system (Scheme 2) and the reaction was carried out at room temperature. Interestingly, in the presence of catalyst, the reaction formed the desired product 4aaa in 57% yield in 15 min. To increase the yield of the reaction, we carried out the reaction at higher temperatures ranging from 40–100 °C. It was observed that the yield was enhanced with increasing temperature and the maximum yield of 94% was obtained at 80 °C. Further increase in the temperature did not have any effect in the yield or time of the reaction. The possibility of Fe3O4 NPs to catalyse the reaction process was also tested. It was observed that Fe3O4 NPs could not efficiently catalyze the reaction, resulting in only moderate yield of the product (66%, Table 1). The structure of the product was then characterized by elemental analysis as well as IR, 1H and 13C NMR and mass spectroscopy.
Several sets of reaction were performed in order to determine the optimum amount of catalyst required for the said reaction. The model reaction of isatin (1a, 1 mmol), malononitrile (2a, 1 mmol) and dimedone (3a, 1 mmol) without any catalyst in aqueous medium (3 mL) at 80 °C was carried out. The reaction resulted only in traces of the product 4aaa leaving behind unreacted starting materials even after 15 min of heating. When the same reaction was carried out with varying amount of the catalyst ranging from 2–12 mg, a much promising results were achieved. The yield of the product increased with increasing amount of the catalyst from 2–8 mg. The reaction with 8 mg of the catalyst produced the maximum yield of the product (94%). However further increase in the amount of the catalyst did not lead to any improvement in the yield of the product. Therefore the optimum amount of the catalyst required for the present reaction is 8 mg (Fig. 6). The turn over number (TON) and the turn over frequency (TOF) of the catalyst reached 850000 and 56
667 min−1 with respect to glutathione.
To search the best solvent system for the model reaction, we examined various solvents such as toluene, CHCl3, CH3CN, EtOH and water. The catalyst shows better activity in acetonitrile (73%) compared with other polar solvents like THF and CHCl3 but most satisfactory result was achieved in case of EtOH (97%) and water (94%). Toluene was also not effective as a solvent for the present catalytic protocol. Because water and ethanol producing almost same amount of yield so we chose water as the solvent due to environmental awareness, cost effectiveness and easy accessibility (Fig. 7).
After optimization of the reaction parameters, the versatility of the catalyst was tested with various C–H activated compounds like dimedone (3a), pyrazolone (3b), barbituric acid (3c), 1,3-dimethyl barbituric acid (3d), 2-thiobarbituric acid (3e) and 4-hydroxy coumarin (3f) and also 1,2-diketo compounds such as isatin derivatives (1a and 1b) and acenaphthenequinone (1c). In all the cases the reaction proceeded smoothly and produced good to excellent yield of the desired product (Table 2). It was observed that the electronic effect had no influence on the product yield of the reaction. The most important advantage of the present method is the chromatography free separation of the desired product. Only recrystallization from methanol afforded the desired product with excellent purity. The above results are indicative of the fact that the nano-FGT catalyst is highly efficient and can be applied for the synthesis of a diverse library of spirooxindole derivatives (Scheme 3). To outline the industrial applicability of the present methodology, a gram scale reaction was also studied (Scheme 4). Gram scale reaction was performed by taking isatin (1a, 7 mmol), malononitrile (2a, 7 mmol), dimedone (3a, 7 mmol) and catalyst nano-FGT (56 mg) in aqueous medium (20 mL). The resulting reaction mixture was heated at 80 °C with stirring for a period of 15 min. The reaction proceeded smoothly to completion and an isolated yield of 91% was achieved.
Entry | 1,2-Diketone | Malonates | C–H activated compounds | Product | Yield (%) | Melting point (°C) |
---|---|---|---|---|---|---|
a Reaction condition: 1,2-diketone (1a–c, 1 mmol), malonates (2a–c, 1 mmol), enolizable C–H activated compounds (3a–f, 1 mmol) and nano-FGT (8 mg) in aqueous medium (3 mL) at 80 °C for 15 min. | ||||||
1 | 1a | 2a | 3a | 4aaa | 94 | 289–292 |
2 | 1a | 2a | 3b | 4aab | 93 | 236–237 |
3 | 1a | 2a | 3c | 4aac | 97 | 296–298 |
4 | 1a | 2a | 3d | 4aad | 96 | 229–231 |
5 | 1a | 2a | 3e | 4aae | 95 | 240–241 |
6 | 1a | 2a | 3f | 4aaf | 91 | 290–291 |
7 | 1a | 2b | 3a | 4aba | 95 | 275–277 |
8 | 1a | 2b | 3b | 4abb | 96 | 236–239 |
9 | 1a | 2c | 3a | 4aca | 92 | 254–256 |
10 | 1b | 2a | 3a | 4baa | 90 | 251–252 |
11 | 1b | 2a | 3b | 4bab | 92 | 198–199 |
12 | 1b | 2b | 3a | 4bba | 94 | 254–256 |
13 | 1c | 2a | 3a | 4caa | 95 | 267–268 |
14 | 1c | 2a | 3b | 4cab | 93 | 193–195 |
15 | 1c | 2a | 3c | 4cac | 91 | >300 |
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Scheme 4 Synthesis of spirooxindole in gram scale. Reaction condition: isatin (1a, 7 mmol), malononitrile (2a, 7 mmol), dimedone (3a, 7 mmol) and nano-FGT (56 mg) in aqueous medium (20 mL) at 80 °C. |
The plausible catalytic cycle for the synthesis of spirooxindole derivatives is given below (Scheme 5). Initially,26 amine functionality of the catalyst forms iminium intermediate 5 with 1,2-diketones (1a–c). This iminium intermediate inturn facilitates the Knoevenagel condensation with malonates (2a–c) and a new intermediate is formed (7). On the other hand nano-FGT helps to enolize the 1,3-diketo compounds (3a–f). These enolized compounds undergo Michael addition with Knoevenagel product 7 and generates another intermediate 8. Finally intramolecular cyclization followed by hydrogen shift furnish the products 4aaa–4cac.
A hot filtration test was performed to measure the leaching of the catalyst nano-FGT. Initially, the solvent water (3 mL) and the catalyst nano-FGT (8 mg) were heated at 80 °C for a period of 15 min. After the time frame, the catalyst was removed by means of simple external magnet. The reactants isatin (1a, 1 mmol), malononitrile (2a, 1 mmol) and dimedone (3a, 1 mmol) were then added to the reaction pot. The reaction mixture was then allowed to proceed for a further period of 15 min. It was observed that after the removal of the catalyst from the reaction only trace amount (21%) of product formed. This trace amount of product formed due to the uncatalyzed pathway (Table 1; entry 5). Thus it confirmed that, there was no significant amount of leaching of nano-FGT taking place.
Reusability is one of the essential parameter of a good and efficient catalyst which makes the procedure economically cheap, industrially profitable and environmentally sustainable. Therefore the reusability of the catalyst was also studied. After the completion of the reaction, the nano-FGT catalyst was separated by means of simple external magnet, washed with MeOH and dried. The nano-FGT was then used for another set of reaction under the same experimental condition. It was interesting to note that the recycled catalyst drove the reaction to completion with almost equal efficiency as the new catalyst. The nano-FGT catalyst could be recycled and reused for eight consecutive runs without any appreciable change in catalytic activity. The reproducibility of the reaction was also accessed. Five model reactions for each set under the same reaction condition were performed. The reproducibility of the reaction was then calculated using the mean data for each set (93.8, 93.8, 93.6, 92.8, 92.8, 92.8, 91.6 and 89.8) and the error bars are reported by means of standard deviation method (Fig. 8).
After completion of eight cycles, we analyzed TEM, and SEM of the reused catalyst. We found that the morphology and shape remained unaltered. The TEM image of the nano-FGT after use (Fig. 2d) revealed that the coating, shape and size almost remained intact even after eight consecutive runs. The SEM image also shows no change in surface morphology of the nano-FGT after eight runs (Fig. 3b).
The compounds 4aaa, 4aab and 4caa were carefully recrystallized from MeOH. The structures of the aforementioned compounds were further confirmed using X-ray crystallography. Fig. 9 shows the ORTEP diagram of the compounds 4aaa, 4aab and 4caa.
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Fig. 9 ORTEP diagram of compounds (a) 4aaa (CCDC no. 1031108), (b) 4aab (CCDC no. 1031133) and (c) 4caa (CCDC no. 1032132). |
Footnote |
† Electronic supplementary information (ESI) available. CCDC 1031108, 1031133 and 1032132. For ESI and crystallographic data in CIF or other electronic format see DOI: 10.1039/c5ra27552k |
This journal is © The Royal Society of Chemistry 2016 |