M. Nasr-Esfahani*a,
D. Elhamifar*a,
T. Amadeha and
B. Karimib
aDepartment of Chemistry, Yasouj University, Yasouj, 75918-74831, Iran. E-mail: manas@yu.ac.ir; d.elhamifar@yu.ac.ir
bDepartment of Chemistry, Institute for Advanced Studies in Basic Sciences (IASBS), 45137-6731, Gava Zang, Zanjan, Iran
First published on 16th January 2015
An efficient approach for the green and rapid synthesis of biologically active substituted polyhydroquinoline derivatives via unsymmetric Hantzsch reaction using an ionic liquid based periodic mesoporous organosilica supported manganese (Mn@PMO-IL) catalyst under solvent-free conditions is described. This catalyst showed high reactivity and selectivity for the preparation of a set of different derivatives of polyhydroquinolines under moderate reaction conditions and short times. Moreover, the catalyst was also recovered and reused several times without important decrease in reactivity and yields. The nitrogen adsorption–desorption and transmission electron microscopy of the recovered catalyst significantly proved the high stability and durability of the catalyst under applied reaction conditions. Furthermore, compared to the classical methodologies, this method consistently illustrated the advantages of short reaction times, low catalyst loading, high yields, easy separation and purification of the products, and high recoverability and reusability of the catalyst.
9 via cyclocondensation reaction between alkyl acetoacetate, aldehyde and ammonia in acetic acid or by refluxing in alcohol. In recent years, numerous catalysts have been successfully reported for the preparation of these compounds under homogeneous reaction conditions. Some of these developing catalysts include TMS-iodide,10 Bu4N+HSO4−,11 K7[PW11CoO40],12 ionic liquids,13 metal triflates,14 CAN,15 iodine,16 PTSA-SDS,17 tris(pentafluorophenyl)borane,18 boronic acids,19,20 HClO4/SiO2
21 and BINOL-phosphoric acids.22 Nevertheless, the problems of environmentally harmful, expensive and non-reusable catalysts and product separation limit the use of these homogeneous catalytic systems. To overcome these drawbacks, recently several attempts have been successfully developed for the synthesis of polyhydroquinoline derivatives using efficient and reusable heterogeneous catalysts under appropriate conditions. Some of applied catalysts are silica-supported acids,23,24 ZnO NPs,25 polymers26,27 and Ni nanoparticles.28 However, some of the later catalytic methods have disadvantages of high reaction temperature, the use of ecologically suspected organic solvents and longer reaction times. Therefore, the developing reaction conditions in the synthesis of polyhydroquinoline derivatives using efficient and reusable catalysts under green conditions is still the need of the day.
On the other hand, organic functionalized ordered mesoporous silicas with tailored porosity on several length scales are of interest for a variety applications in areas of adsorption, chromatography, catalysis, sensor technology, and gas storage due to their large specific surface area and uniform pore size with high coverage of introduced functional groups.29,30 Among different types of organic containing mesoporous silicas, periodic mesoporous organosilicas (PMOs), which are synthesized by the simultaneous use of a soft template and a hydrolysable bis-silane condensing around the template,31 have mostly progressed the field of material science research. The unique properties of PMOs such as tuneable chemophysical properties, high loading of uniform distribution of organic functional groups in their framework and superior thermal stability make them attractive candidate for a wide range of applications in catalysis, electronic, support and adsorption chemistry.32 In the last decades, ionic liquids (ILs) have attracted rising interest with a various range of applications in different areas of chemistry because of their significant properties such as extremely low volatility, low melting point, high chemical and thermal stability and high ionic conductivity.33 However, in spite of the remarkable utility of these compounds, their widespread applications in process chemistry is still restricted because many of them are very expensive.34 Moreover, due to high viscosity of ionic liquids only a small amount of them (called diffusion layer) participates in the chemical process.35 To overcome these limitations, the concept of supported ionic liquids has been recently developed. Especially, silica supported ionic liquids has been successfully developed and applied in several chemical transformations as an effective support for transition metal catalysts. Along this regard, more recently we have prepared a novel periodic mesoporous organosilica with alkyl imidazolium ionic liquid framework (PMO-IL) and studied its application as effective support for the immobilization and stabilization of a set of different transition metals (M@PMO-IL). The prepared metal containing PMO-IL nanomaterials were then successfully applied as powerful and highly reusable catalysts in a number of organic reactions such as aerobic oxidation of alcohols and carbon–carbon bond coupling processes.36,37 In continuation of our study on applications of metal supported PMO-IL, herein the catalytic application of a manganese containing ionic liquid-based periodic mesoporous organosilica (MnPMO-IL) material is investigated in the synthesis of polyhydroquinoline derivatives. This was achieved by the one-pot condensation of aldehydes (aromatic, aliphatic, unsaturated and heterocyclic), 5,5-dimethyl-1,3-cyclohexanedione (dimedone) or 1,3-cyclohexanedione, β-dicarbonyl and ammonium acetate in the presence of Mn@PMO-IL nanocatalyst under solvent free conditions (Scheme 1). Moreover the reactivity, reusability and stability of the catalyst during reaction process have also been studied in detail.
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| Scheme 1 Preparation of the Mn@PMO-IL nanocatalyst and its application in synthesis of polyhydroquinolines. | ||
C and C
N stretching vibrations of imidazolium ring.36c,36e These observations successfully confirm victorious incorporation of alkyl imidazolium ionic liquid groups in the material framework.
Thermal gravimetric analysis (TGA) of the Mn@PMO-IL was performed to investigate the thermal stability of the material (Fig. 2). This analysis illustrated a weight loss of 6.64% in the temperature below 120 °C corresponding to removal of water. A very small weight loss (2.28%) between 120 and 280 °C is attributed to elimination of surfactant template remained from extraction process. The third weight loss (18.35%) from 280 to 800 °C is related to removal of ionic liquid functional groups located in the material framework. This data successfully proves the successful incorporation of organic functional moieties in the solid network and confirms high thermal stability of the material.
The PXRD analysis of the material demonstrated a single high intensity peak at 2θ 0.7–1.3 which indexed as the d100 reflection and matches with the 2-dimensional hexagonal materials having long range periodicity (Fig. 3). This significantly proves the presence of uniform mesostructure with high regularity. The transmission electron microscopy (TEM) image of the Mn@PMO-IL was in good agreement with PXRD analysis and successfully confirmed a two dimensional hexagonal structure with high regularity for the material (Fig. 4). Furthermore, this image together with PXRD analysis proved the high stability of the material structure after immobilization of manganese species onto/into the mesopores.
Energy-dispersive X-ray (EDX) spectroscopy showed the presence of C, O, Si, Cl and Mn in the Mn@PMO-IL nanocatalyst (Fig. 5). The elemental distribution mapping of this analysis shows signals of carbon
:
oxygen
:
silicon
:
chlorine
:
manganese in the ratio of 34.2
:
44.9
:
16.7
:
1.3
:
1.9 wt%, respectively. This confirms successful incorporation of expected elements in the material network. It is also important to note that the X-ray photoelectron spectroscopy (XPS) of the catalyst showed peaks at binding energies of 654.2 and 642.6 eV for the Mn 2p1/2 and Mn 2p3/2, respectively, confirming that Mn species are strongly bound to electronegative atoms and may be they are as Mn(III).38
| Entry | Mn@PMO-IL (mol%) | Temp. (°C) | Solvent | Time (min) | Yieldb (%) |
|---|---|---|---|---|---|
| a Reaction conditions: dimedone (1 mmol), benzaldehyde (1 mmol), ethylacetoacetate (1 mmol), ammonium acetate (1 mmol) and catalyst (1 mol%).b Isolated yields. | |||||
| 1 | 1 | Reflux | Ethanol | 30 | 53 |
| 2 | 1 | Reflux | Methanol | 30 | 48 |
| 3 | 1 | Reflux | Water | 30 | 45 |
| 4 | 1 | Reflux | Chloroform | 30 | 38 |
| 5 | 1 | 80 | — | 20 | 95 |
| 6 | 0.7 | 80 | — | 20 | 67 |
| 7 | 0.35 | 80 | — | 20 | 35 |
| 8 | None | 80 | — | 120 | Trace |
| 9 | 1 | 60 | — | 20 | 53 |
| 10 | 1 | 45 | — | 20 | 30 |
| 11 | PMO-IL | 80 | — | 60 | 25 |
| 12 | Mn(OAc)3·2H2O | 80 | — | 20 | 95 |
It is also important to note, in the absence of catalyst at 120 min under the same conditions as before, only a trace amount of product was obtained (Table 1, entry 8). Furthermore, by using PMO-IL instead of Mn@PMO-IL as catalyst, the rate of the model reaction was significantly decreased and a lower yield of product was obtained after 60 min (Table 1, entry 11). On the other hand, applying of Mn(OAc)3·2H2O as catalyst gave excellent yield of the product (Table 1, entry 12), however, this is not recoverable and reusable for the next runs. These observations show that the reaction cycle is mainly catalyzed by manganese species immobilized on the PMO-IL nanostructure. Accordingly, in all further reactions, 1 mol% of the Mn@PMO-IL catalyst was used because of satisfactory yield of the product in reasonably short time.
Our study also showed that the reaction was also effected by the amount of heat and the best result was observed at 80 °C (Table 1, entry 5 vs. entries 9, 10). In another study, the reaction was performed using different quantities of reagents. This showed that the best result is obtained with a 1
:
1:1
:
1 ratio of dimedone, benzaldehyde, ethyl acetoacetate and ammonium acetate, respectively.
To demonstrate the generality of this method, we next investigated the scope of this reaction under the optimized conditions (Mn@PMO-IL 1 mol%, solvent-free, 80 °C). As shown in Table 2, this method was equally effective irrespective of the nature and positions of the substituents attached to the phenyl ring of the aromatic aldehyde. All strongly activating (4c, 4f, 4g, 4k, 4l, 4p, 4s, 4u), weakly activating (4h, 4n, 4x), weakly deactivating (4d, 4m, 4r, 4t), and strongly deactivating (4b, 4j, 4v) substrates gave products with nearly equal ease. As shown, benzaldehyde substrates containing activating substituents such as OH (Table 2, entries 6, 12 and 19), CH3O (Table 2, entry 21) and CH3 (Table 2, entries 8, 14 and 23) furnished high yields of corresponding coupling adducts. Benzaldehyde (Table 2, entries 1, 5, 9 and 23) also gave satisfactory yields of related products. Moreover, other aldehyde substrates containing deactivating substituents such as NO2 (Table 2, entries 2, 10 and 22) and Cl (Table 2, entries 4, 13, 18 and 20) delivered high yields of corresponding coupling products. In addition, the aliphatic aldehydes such as butanal (Table 2, entry 15) afforded a 55% yield in 100 min. Also acid-sensitive substrates such as cinnamaldehyde proceeded well to give the corresponding polyhydroquinoline without any side product (entry 17). Furthermore, the procedure worked well for heterocyclic aldehydes (Table 2, entries 3, 7, 11 and 16). These observations strongly confirm high efficiency and powerful activity of the present catalyst for a broad range of aldehydes to produce different derivatives of polyhydroquinolines which are important and applicable in drug chemistry.
| Entry | R1 | R2 | R3 | Compounds | Time (min) | Yieldb (%) | Mp (°C) | |
|---|---|---|---|---|---|---|---|---|
| Found | Reported | |||||||
| a All products were characterized by 1H NMR, 13C NMR and IR spectroscopies and compared with the reports in the literature.15,26,28,39,40b Isolated yields. | ||||||||
| 1 | C6H5 | H | OEt | 4a | 20 | 90 | 241–242 | 240–241 |
| 2 | 4-NO2C6H4 | H | OEt | 4b | 25 | 90 | 203–205 | 204–205 |
| 3 | 2-Thienyl | H | OEt | 4c | 15 | 92 | 232–233 | 233–234 |
| 4 | 4-ClC6H4 | H | OEt | 4d | 20 | 87 | 234–236 | 234–235 |
| 5 | C6H5 | H | Me | 4e | 45 | 80 | 227–230 | 229–230 |
| 6 | 3-HOC6H4 | H | Me | 4f | 35 | 87 | 244–246 | — |
| 7 | 2-Furyl | H | OMe | 4g | 20 | 95 | 212–216 | — |
| 8 | 4-CH3C6H4 | H | OMe | 4h | 20 | 89 | 218–220 | — |
| 9 | C6H5 | Me | OEt | 4i | 20 | 95 | 202–204 | 203–204 |
| 10 | 4-NO2C6H4 | Me | OEt | 4j | 20 | 88 | 243–245 | 244–246 |
| 11 | 2-Thienyl | Me | OEt | 4k | 20 | 90 | 239–241 | 237–239 |
| 12 | 3-HOC6H4 | Me | OEt | 4l | 20 | 92 | 220–222 | 218–220 |
| 13 | 2-ClC6H4 | Me | OEt | 4m | 20 | 92 | 207–209 | 206–208 |
| 14 | 4-CH3C6H4 | Me | OEt | 4n | 20 | 88 | 260–262 | 261–263 |
| 15 | CH3CH2CH2 | Me | OEt | 4o | 100 | 55 | 147–149 | 147–148 |
| 16 | 2-Furyl | Me | OEt | 4p | 20 | 92 | 247–248 | 246–248 |
| 17 | C6H5–CH CH |
Me | OEt | 4q | 28 | 87 | 204–206 | 205–207 |
| 18 | 2,4-Cl2C6H3 | Me | OEt | 4r | 20 | 85 | 240–243 | 241–244 |
| 19 | 3-CH3O-4-HOC6H4 | Me | OEt | 4s | 20 | 91 | 202–204 | 200–202 |
| 20 | 4-ClC6H4 | Me | OMe | 4t | 20 | 85 | 219–222 | 220–222 |
| 21 | 4-CH3OC6H4 | Me | OMe | 4u | 20 | 87 | 258–260 | 259–261 |
| 22 | 3-NO2C6H4 | Me | OMe | 4v | 20 | 85 | 232–234 | 234–236 |
| 23 | C6H5 | Me | OMe | 4w | 20 | 90 | 209–211 | 212–214 |
| 24 | 4-CH3C6H4 | Me | OMe | 4x | 20 | 86 | 268–271 | 270–274 |
Since the reusability of the catalysts is an important benefit and makes them useful for commercial applications, in the next study the recovery and reusability of Mn@PMO-IL were investigated. For this, the reaction of dimedone, benzaldehyde, ethylacetoacetate and ammonium acetate in the presence of 1 mol% catalyst was selected as a test model. To achieve the reaction efficiency of recovered catalyst, after completion of the reaction, the obtained mixture was filtered and washed completely with ethanol to give the catalyst. The recovered catalyst was dried and then used again in the same reaction that led to the yield of 94%. The more investigations showed that the catalyst could be recovered and reused, under the same conditions of the fresh run, for at least five times without any considerable loss in activity (Fig. 6A). Also, re-activity of the catalyst was investigated (Fig. 6B). To do this, Mn@PMO-IL was added to a mixture of dimedone, benzaldehyde, ethylacetoacetate and ammonium acetate and the reaction mixture was heated in 80 °C. After completion of the reaction, monitored by TLC, the fresh amounts of starting materials were added to the previous reaction mixture in the flask and stirring and heating were carried out to complete the second cycle. These cycles were occurred to ten times without noticeable decrease in yield of the reactions (Fig. 6B). These observations significantly prove high recoverability, reusability, reactivity and stability of the present catalyst under applied reaction conditions.
The recovered catalyst after third reaction cycle was analyzed by transmission electron microscopy and nitrogen adsorption–desorption experiment. The nitrogen adsorption–desorption analysis showed a type IV isotherm with H1 hysteresis loop and high intensity in relative pressure of 0.4–0.6 (Fig. 7). The BET surface area and mean pore volume of this material was found to be 435 m2 g−1 and 8.54 cm3 g−1, respectively. Moreover, the BJH calculations also illustrated a peak with high intensity and mean pore diameter of 6 nm confirming the presence of uniform pores in the meso-range (Fig. 7). The TEM image of this material was in good agreement with nitrogen sorption data and significantly illustrated a uniform and regular mesopores which is characteristics of two dimensional hexagonal structures (Fig. 8). These observations strongly confirm high stability and recoverability of the Mn-nanocatalyst under applied reaction conditions. The high activity, recoverability and stability of the present catalytic system may be attributed to ionic liquid nature of the PMO-IL as well as uniform mesoporous channels of the material, which effectively immobilize the active Mn species and protect them against leaching and deactivation.
![]() | ||
| Fig. 7 Nitrogen adsorption–desorption (top) and BJH pore size distribution (bottom) isotherms of recovered Mn@PMO-IL after third reaction cycle. | ||
A proposed mechanism for the Mn@PMO-IL nanocatalyst catalyzed synthesis of polyhydroquinolines is presented in Scheme 2. The role of catalyst is shown in steps 1 and 5 where it catalyzes the Knoevenagel type coupling of aldehydes with active methylene compounds and in steps 3 and 6 where it catalyzes the Michael type addition of intermediates 5, 6 or 7, 8 to give product 4. The formation of acridinedione 9 is possible when 5 reacts with 7,41 since this possibility is discarded due to non-formation of intermediates 5 and 6.42 A literature survey also adjusts with absence of acridinediones as a by-product during present reaction.10–28
:
EtOAc
:
n-hexane), hot ethanol (5 mL) was added and the obtained solution was filtered and completely washed with ethanol. The solvent was then evaporated and the crude products were recrystallized in ethanol and gave pure crystals in 80–95% yields based on the starting aldehyde. The products were characterized by IR, 1H NMR, 13C NMR and via comparison of their melting points with the reported ones. Spectroscopic data of new compounds are as following:
:
ethyl acetate = 3
:
1); IR (KBr): 3417, 3255, 3202, 2960, 1665, 1613, 1478, 1222 cm−1; 1H NMR (400 MHz, DMSO-d6) δ (ppm): 1.91–2.15 (m, 2H), 2.18 (s, 3H), 2.25 (t, J = 11.2 Hz, 2H), 2.41 (s, 3H), 2.46 (t, J = 7.9 Hz, 2H), 5.24 (s, 1H), 7.08–7.30 (m, 4H), 9.11 (s, 1H); 13C NMR (100 MHz) δ (ppm): 18.79, 26.24, 29.13, 29.88, 31.95, 35.22, 50.24, 109.86, 113.09, 127.05, 127.58, 129.26, 131.14, 131.46, 142.74,144.55, 149.44, 193.78, 197.91; Anal. calcd for C18H19NO3: C, 72.71; H, 6.44; N, 4.71; O, 16.14; found: C 72.62, H 6.37, N 4.80.
:
ethyl acetate = 3
:
1); IR (KBr): 3285, 3079, 2944, 1698, 1649, 1608, 1483, 1220 cm−1; 1H NMR (400 MHz, DMSO-d6) δ (ppm): 0.91–1.15 (m, 2H), 1.93 (t, J = 6.5 Hz, 2H), 2.26 (s, 3H), 2.51 (t, J = 4.0 Hz, 2H), 3.60 (s, 3H), 5.06 (s, 1H), 5.79–5.83 (m, 1H), 6.19–6.25 (m, 1H), 7.32–7.40 (m, 1H), 9.25 (s, 1H); 13C NMR (100 MHz) δ (ppm):18.16, 20.78, 26.11, 29.35, 36.58, 50.78, 100.24, 104.0, 107.71, 109.43, 141.18, 146.03, 152.26, 158.29, 167.09, 194.42; Anal. calcd for C16H17NO4: C, 66.89; H, 5.96; N, 4.88; O, 22.27; found: C 66.78, H 5.89, N 4.95.
:
ethyl acetate = 3
:
1); IR (KBr): 3286, 2960, 1716, 1671, 1605, 1379, 1225 cm−1; 1H NMR (400 MHz, DMSO-d6) δ (ppm): 1.70–1.92 (m, 2H), 2.18 (t, J = 4.2 Hz, 2H), 2.26 (s, 3H), 2.28 (s, 3H), 2.47 (t, J = 7.7 Hz, 2H), 3.52 (s, 3H), 4.87 (s, 1H), 6.97 (d, J = 7.8 Hz, 2H),7.02 (q, J = 7.93 Hz, 2H), 9.13 (s, 1H); 13C NMR (100 MHz) δ (ppm):18.14, 20.52, 26.08, 31.64, 34.90, 50.60, 103.24, 111.23, 111.26, 112.58, 127.09, 128.45, 134.53, 144.74, 145.03, 151.16, 167.38, 194.61; Anal. calcd for C19H21NO3: C, 73.29; H, 6.80; N, 4.50; O, 15.41; found: C 73.19, H 6.72, N 4.57.
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