Sriparna
Dutta
ab,
Prashant
Kumar
c,
Shivani
Sharma
ad,
Sneha
Yadav
a,
Priyanka
a,
Ranjana
Dixit
ad,
Anju
Srivastava
ab and
Rakesh Kumar
Sharma
*a
aGreen Chemistry Network Centre, Department of Chemistry, University of Delhi, Delhi-110007, India. E-mail: rksharamgreenchem@hotmail.com
bDepartment of Chemistry, Hindu College, University of Delhi, Delhi-110007, India
cDepartment of Chemistry, SRM University Delhi-NCR, Sonepat, Haryana-131029, India
dDepartment of Chemistry, Ramjas College, University of Delhi, Delhi-110007, India
First published on 3rd May 2023
A core–shell hetero-nanostructure comprising a new in situ generated naphthoquinone cobalt complex covalently immobilized on a silica coated magnetite nanosupport has been described for catalyzing the enamination of β-carbonyl compounds. The newly developed catalyst works as a nanoreactor for boosting this reaction and provides unprecedented chemoselective access to the targeted β-enaminoesters as well as β-enaminones. The synergistic covalent incorporation of an organic entity (a flexible spacer) onto an inorganic solid (surface modified support material) imparts a considerable structural rigidity to the catalyst thereby preventing leaching of the active catalytic species as well evidenced by the hot filtration experiment. Elemental survey and core level XPS spectra confirm the presence of the +II oxidation state of cobalt which is the active catalytic species. This work throws light on how catalytic activity can be tuned and “activity, selectivity and recyclability” the three desired features of a green catalyst can be accomplished on a single platform through careful manipulation of interaction between the support material and active metal complex.
Sustainability spotlightIn 2015, the entire world came to a common consensus when seventeen sustainable development goals were outlined by the various member countries of the UN that carried a vision of rendering the planet safer for all. With a very few years left to accomplish these goals, tremendous efforts will be required to transform the commitments into action. Catalysis the key principle of green chemistry provides one of the most promising and logistic routes for achieving most of the SDGs such as zero hunger, good health & well being, clean water & sanitation, affordable & clean energy, industries, innovation & infrastructure, responsible consumption & production and climate action. The present work discloses the design of a novel core–shell hetero nanostructure based catalyst comprising a new in situ generated naphthoquinone cobalt complex covalently immobilized on a silica coated magnetite nanosupport that has unveiled promising outcomes in catalyzing the enamination of β-carbonyl compounds (that synergistically integrate the nucleophilicity of the enamine and electrophilicity of the enone functionalities, thereby serving as valuable synthons for the construction of essential pharmaceutical drugs). Although literature reports document the development of several synthetic approaches involving homogeneous metal complexes that provide access to these compounds, yet appealing generality and the scope of industrial utility of these catalytic protocols are vitiated by the fact that most of them rely on homogeneous metal salts as catalysts that are not only difficult to recover from the reaction mixture but also major contributors to metal contamination. The present work is a sustainable attempt to overcome the serious limitations of previous protocols via the establishment of a catalyst that offers “activity, selectivity and recyclability” the three desired features of a green catalyst in a single platform through careful manipulation of interaction between the support material and active metal complex. |
β-Enaminones and β-enaminoesters represent well documented scaffolds that have fuelled the research interest of several organic chemists worldwide as they synergistically integrate the nucleophilicity of the enamine and electrophilicity of the enone functionalities, thereby serving as valuable synthons for the construction of essential pharmaceutical drugs.21–24 Besides, they constitute prevalent structural motifs of biologically significant natural products that are endowed with a broad spectrum of interesting pharmacological properties such as antibacterial, anticonvulsant, anti-inflammatory, antitumour etc.25–31 Thus, over the past few decades a number of captivating strategies have been reported for obtaining these heterocyclic moieties which include reactions of β-enaminoesters with organolithium reagents,32 addition of amide enolates or metallic esters to imidoyl halides,33–36 nitriles,37–39 and tosylimines40,41 and addition of enamines or ketamines to activated carboxylic acid derivatives.42–44 However, despite the existence/prevalence of a large number of intriguing protocols in the literature, the classical approach involving the direct condensation of amines with 1,3-dicarbonyls still continues to be one of the most widely pursued pathways for the synthesis of β-enamino ketones and esters because of its operational simplicity and higher atom economy.45 Consequently, a wide array of catalysts such as Sc(OTf)3,46 Zn(OAc)2·6H2O,47 ZrOCl2·8H2O,48 Ca(CF3COO)2,49 CoCl2,50 InBr3,51 I2,52 silica gel,53 CeCl3·7H2O54 and NaAuCl455 have been employed proficiently to afford this transformation. Unfortunately, the appealing generality and the scope of industrial utility of these catalytic protocols are vitiated by the fact that most of them rely on homogeneous metal salts as catalysts that are not only difficult to recover from the reaction mixture but also major contributors to metal contamination. Thus, in consideration of growing economic and industrial concerns, it is extremely imperative to develop other alternative environmentally benign, heterogeneous recyclable catalytic systems that can efficiently conquer the challenges of β-enaminone and β-enaminoester synthesis.
In a quest to design a supreme catalytic route for obtaining these industrially and biologically significant β-enamine based moieties and engaged in the development of organic–inorganic hybrid catalysts for various organic transformations, we herein report the fabrication, characterization and application of a promising core–shell magnetic silica based cobalt nanocatalyst (Co-NQ@Am-SiO2@Fe3O4). The newly developed catalytic system enables the generation of a diverse range of β-enaminones and β-enaminoesters with excellent turnover numbers and high product selectivity under neat reaction conditions at room temperature. Apart from this, the ease of catalytic retrievability via magnetic attraction and outstanding recycling efficiency (observable up to eight consecutive runs) render the present protocol a practical alternative to all previously established methodologies for the synthesis of β-enamine ketones and esters. To the best of our knowledge, this is the first report wherein a magnetically retrievable nanocatalyst has been designed and subsequently utilized for the enamination of β-ketoesters and β-ketones.
In order to gain an insight into the crystallinity and phase composition of the synthesized nanomaterials, wide angle powder X-ray diffraction (PXRD) measurements were performed and the typical XRD profiles of Fe3O4 and SiO2@Fe3O4 are presented in Fig. 2. Interestingly, both these diffractograms display six distinguishable Bragg's peaks at 2θ = 30.1°, 35.4°, 43.1°, 53.4°, 57° and 62.6° that may be correctly assigned to the (220), (311), (400), (422), (511) and (440) crystallographic faces of the cubic inverse spinel structured magnetite. The peak positions as well as the relative intensities are in good agreement with the standard Fe3O4 XRD data as evidenced by the Joint Committee on Powder Diffraction Standards (JCPDS card: 19-629). However, the XRD pattern of silica encapsulated magnetite nanoparticles differs slightly from that of the native magnetite nanoparticles. Besides, exhibiting these well resolved diffraction peaks, the XRD spectrum of SiO2@Fe3O4 shows the appearance of a broad diffused hump centered at around 2θ = 23° which is attributed to the presence of amorphous SiO2.57 One aspect that needs to be highlighted here is that although the silica coating strategy efficiently leads to the generation of a protective layer of silica around the magnetic core, it does not affect the phase and purity of these crystalline nanoparticles, as evident from the diffractogram which clearly shows the retention of the six characteristic Bragg's peaks in this core–shelled nanomaterial. Furthermore, the mean crystallite size of the Fe3O4 nanoparticles has been evaluated using the Debye Scherrer relationship (Dhkl = kλl/βcos
θ) where k is a constant with a typical value of 0.89 for spherical particles, D is the average diameter in A°, β is the broadening of the diffraction line measured at half of its maximum intensity in radians, λ is the wavelength of the X-rays and θ is the Bragg diffraction angle. Choosing (311) as the reference peak, this value has been estimated to be 11.9 nm which matches well with the TEM results. Furthermore, the XRD spectra of the catalyst and the recovered catalyst, exhibiting consistency with the native ferrite peaks have been provided (Fig. S3†).
The elemental and compositional analyses of the bare and modified nanoparticles were performed using energy-dispersive X-ray spectroscopy (EDX), energy dispersive X-ray fluorescence spectroscopy (ED-XRF) and atomic absorption spectroscopy (AAS). Fig. S4† provides the EDX mapping images of the isolated particles of Fe3O4 and SiO2@Fe3O4. The well resolved peaks of iron (Fe) and oxygen (O) atoms in the EDX spectrum of Fe3O4 affirm the presence of an iron oxide core. Besides the elemental distribution of Fe and O, the occurrence of Si in the EDX spectrum of SiO2@Fe3O4 authenticates the successful encapsulation of the core material by silica.
Apart from this, the SEM elemental coloured mapping image of the Co-NQ@Am-SiO2@Fe3O4 nanocatalyst (Fig. 3) has been provided which shows the presence of distinct elements – “Fe, Si, O, C, N, and Co,” thus confirming the successful functionalization, ligand grafting and metallation of the silica coated magnetite nanoparticles. In addition to the elemental mapping, the ED-XRF spectrum of Co-NQ@Am-SiO2@Fe3O4 also provides a concrete proof for the existence of the metal in the catalyst by markedly showing the presence of a sharp and distinct peak of cobalt (Fig. 4). Next, the quantitative estimation of cobalt in the prepared catalyst was performed by digesting Co-NQ@Am-SiO2@Fe3O4 in a microwave oven at 400 W for 15 minutes with aqua regia and then subjecting the sample to AAS analysis. The corresponding metal content was evaluated to be 0.14 mmol g−1.
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Fig. 3 SEM elemental mapping images of the Co-NQ@Am-SiO2@Fe3O4 nanocatalyst showing the presence of Fe, Si, O, C, N, and Co elements. |
With the aim of clearly identifying the chemical composition and acquiring information about the oxidation state of cobalt, the surface structure of the final nanocatalyst was further characterized by X-ray photoelectron spectroscopy (XPS). Fig. 5 presents the XPS elemental survey scans and core level spectra of Fe 2p and Co 2p of the magnetic silica based organic–inorganic hybrid cobalt catalyst. The presence of elements C, O, Si, N, Fe and Co is confirmed from the survey spectrum of Co-NQ@Am-SiO2@Fe3O4. Next, the core level spectrum of Fe 2p was analyzed and it was found that two distinct bands appeared at around 710 and 725 eV along with a satellite peak at 717.8 eV (Fig. S5†). As these bands were broad, deconvolution of the same was attempted and successfully achieved. In the deconvoluted spectrum of Fe 2p, first the presence of combined peaks at binding energy values of 710.8 eV (Fe 2p3/2) and 725 eV (Fe 2p1/2) provided strong evidence of the presence of iron in the +II oxidation state in the catalyst. Furthermore, the occurrence of a satellite peak could be routinely ascribed to iron in the +II oxidation state. Apart from this, the prominent peaks appearing at binding energy values of 712 eV (Fe 2p3/2) and 725 eV (Fe 2p1/2) characterized the simultaneous existence of iron in the +III oxidation state in our sample. But since we are primarily interested in evaluating the oxidation state of cobalt which is the active catalytic species in our final catalyst, the XPS spectrum of Co 2p was plotted and investigated thoroughly. The deconvoluted spectrum revealed the existence of cobalt in the +II oxidation state. In this case, the binding energies for the two possible spin states 781.2 eV and 797.5 eV are responsible for 2p3/2 and 2p1/2 transitions, respectively and in addition, two satellite peaks were observed which primarily arose from each of the 2p transition.
For the structural confirmation of the various nanocomposites through functional group detection, Fourier transform infrared (FT-IR) spectroscopic analysis was carried out at room temperature. Fig. 6 depicts the FT-IR spectra of Fe3O4, SiO2@Fe3O4, Am-SiO2@Fe3O4, NQ@Am-SiO2@Fe3O4 and Co-NQ@Am-SiO2@Fe3O4.
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Fig. 6 FTIR spectra of (a) Fe3O4; (b) SiO2@Fe3O4; (c) Am-SiO2@Fe3O4; (d) NQ@Am-SiO2@Fe3O4 and (e) Co-NQ@Am-SiO2@Fe3O4. |
The FT-IR spectrum of Fe3O4 exhibits a sharp and intense absorption band at 595 cm−1 indicative of typical Fe–O stretching vibrations and a relatively less intense broad band centered at 3149 cm−1 corresponding to the vibrations of OH groups present on the surface of the magnetite nanoparticles.59 These characteristic absorption bands collectively provide strong evidence for the formation of the Fe3O4 nanocore. Next, the existence of the silane shell around this core is affirmed from the spectrum of SiO2@Fe3O4 which distinctly shows the presence of Si–O–Si symmetric, Si–O–Si asymmetric and Si–O symmetric stretching modes appearing at 806, 954 and 1102 cm−1 respectively.60 Furthermore, the proof for the successful integration of the functionalizing agent “APTES” into the coated nanoparticles is provided by the appearance of two new bands at 2930 cm−1 and 1625 cm−1 that can be assigned to the CH2 and NH2 groups of the aminopropyl moiety. On moving towards NQ@Am-SiO2@Fe3O4, a distinctive band of CN stretch is observed at 1646 cm−1 besides the expected absorption bands which suggests that the ligand has been successfully immobilized over the surface of the amine functionalized silica coated ferrite nanoparticles. Astonishingly, as a result of complexation between the nitrogen atom and the metal, the value of the C
N stretch is shifted to a lower wavenumber (1630 cm−1 from 1646 cm−1) in the case of the final nanocatalyst.
In order to examine the magnetic properties of the synthesized nanocomposites, a vibrating sample magnetometer (VSM) was employed and the resultant magnetization curves of Fe3O4, SiO2@Fe3O4 and Co-NQ@Am-SiO2@Fe3O4 recorded within the field range of −20000 to 20
000 Oe at 300 K are displayed in Fig. 7. The hysteresis loops of these powdered nanomaterials reveal the absence of any remanence or co-ercivity phenomena which confirms their superparamagnetic properties at room temperature. Besides, the inset also supports this observation as the obtained plots clearly show that both the magnetization and demagnetization curves pass through the origin. Furthermore, the value of saturation magnetization (Ms) of the prepared Fe3O4 nanoparticles as estimated from the graph has been found to be 60 emu g−1 which is much lower than that of the bulk Fe3O4 nanoparticles. The significant reduction in the Ms value can be predominantly attributed to the presence of disordered spins on the surface of the nanoparticles that prevent the core spins from aligning along the field direction, thereby causing a net decrease in the saturation magnetization of the small sized nanoparticles. Additionally, the VSM plots show a gradual decrement in the Ms values on moving from the bare Fe3O4 to the surface modified Fe3O4 (i.e. Fe3O4 > SiO2@Fe3O4 > Co-NQ@Am-SiO2@Fe3O4) which may be ascribed to the existence of non-magnetic materials on the surface of the core–shelled nanoparticles.61 However, it is worth mentioning here that regardless of the lowering of the saturation magnetizations, the redispersibility and magnetic properties of the final nanocatalyst remain unaffected and the Co-NQ@Am-SiO2@Fe3O4 nanoparticles are easily retrieved from the reaction mixture with the help of a bar magnet within a very short span of time.
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Fig. 7 Magnetization curves obtained by VSM at room temperature for (a) Fe3O4, (b) SiO2@Fe3O4, and (c) Co-NQ@Am-SiO2@Fe3O4 and (d) inset: an enlarged image near the coercive field. |
The quest for establishing optimal reaction conditions began by performing the catalytic screening test. However, at the outset, to truly assess the significance of a catalyst in the enamination reaction, a control experiment was conducted with the test substrates in the absence of a catalyst. A careful evaluation of the outcome divulged that only traces of the expected product could be detected under such experimental conditions (Table 1, entry 1). Next, a wide range of cobalt based catalysts were screened sequentially for the generation of the desired β-enaminoester scaffold with a high conversion percentage. Gratifyingly, as shown in Table 1, amongst all the tested cobalt sources, the developed Co-NQ@Am-SiO2@Fe3O4 and Co-based catalysts formed by the coordination of CoCl2 with 1,2-naphthoquinone (Co-NQ complex) prove to be the most proficient ones, exhibiting the best catalytic activity by causing a 100% conversion of the employed reactants. In comparison to the precursor CoCl2 salt utilized for the reaction which gave 95% conversion and the other salts such as CoSO4 and CoBr2 that showed very low activity (42% and 45%, respectively) the Co-NQ complex gave a higher conversion that could be ascribed to the coordinating effect of 1,2-naphthoquinone with CoCl2, leading to a robust and active complex. Furthermore, although Co-NQ and Co-NQ@Am-SiO2@Fe3O4 showed similar conversions, yet the fabricated catalyst “Co-NQ@Am-SiO2@Fe3O4” emerged as the material of choice owing to the exceptional magnetism conferred by the material which enhanced the catalytic recoverability and reusability properties. Subsequently, in order to analyse the effect of catalyst concentration, the reactions were performed by varying the amount of catalyst from 5 to 20 mg and the results have been demonstrated in Table 1. It was found that an increase in the catalyst loading caused a substantial improvement in the conversion percentage of the product from 39% to 100% which could be attributed to the simultaneous increase in the active catalytic sites. Thus, for the rest of the studies, the amount of the catalyst was fixed at 20 mg.
Entry | Catalyst | Yieldb (%) | Conversionc (%) | TONd | TOFe |
---|---|---|---|---|---|
a Reaction conditions: benzylamine (1 mmol), methylacetoacetate (1 mmol), catalyst (20 mg unless specified), stirring at r.t. (25 °C), no solvent. b Isolated Yield. c Conversion (%) determined by GC-MS. d TON is the number of moles of product per mole of catalyst. e TOF = TON/time (in hours). | |||||
1 | No catalyst | — | Traces | — | — |
2 | SiO2@Fe3O4 | — | Traces | — | — |
3 | CoSO4 | 35 | 42 | 150 | 300 |
4 | Co(OAc)2 | 37 | 48 | 171 | 342 |
5 | CoBr2 | 40 | 45 | 161 | 322 |
6 | CoCl2 | 82 | 95 | 339 | 678 |
7 | Co-NQ complex | 94 | 100 | 357 | 714 |
8 | Co-NQ@Am-SiO2@Fe3O4 (5 mg) | 30 | 39 | 139 | 278 |
9 | Co-NQ@Am-SiO2@Fe3O4 (10 mg) | 55 | 68 | 243 | 486 |
10 | Co-NQ@Am-SiO2@Fe3O4 (15 mg) | 88 | 95 | 339 | 678 |
11 | Co-NQ@Am-SiO2@Fe3O4 (20 mg) | 95 | 100 | 357 | 714 |
After optimization of the amount of catalyst, our next investigation was focussed on addressing the influence of the substrate molar ratio on the reaction conversions. For an accurate assessment, three different sets of reactions were performed with 1:
0.5, 1
:
0.75 and 1
:
1 molar ratios of methylacetoacetate and benzylamine, respectively in the presence of the Co-NQ@Am-SiO2@Fe3O4 nanocatalyst (Fig. S6†). Apparently, the results indicated that the enamination reaction utilizing a reagent molar ratio of 1
:
0.5 could afford a conversion of only 70% even after a prolonged stirring (up to 6 h) period. However, with a further increase in the molar ratio of the substrates to 1
:
1, a complete 100% conversion of the subjected reactants could be accomplished within a shorter time (30 minutes) interval. Hence, a 1
:
1 substrate molar ratio was the optimum requirement for the efficient synthesis of β-enaminones and β-enaminoesters with a good conversion percentage.
The selection of an appropriate solvent is a matter of increasing importance in the field of catalytic science and research as solvents play a key role in either facilitating or hindering a reaction through their interaction with the catalyst and the solute molecules. Thus, a scrupulous examination of the solvent effect on the enamination reaction was carried out by stirring the model reactants in the presence of solvents of variable polarities. Additionally, in consideration of the current emphasis on green, waste free synthesis, solvent free conditions were also tested, while keeping the rest of the parameters fixed. Fig. S7† illustrates the influence of solvents on the conversion percentages of the reactants. In comparison to all the non-polar solvents employed, polar solvents such as ethanol, isopropanol, acetonitrile and dimethylformamide (DMF) led to a superior reaction conversion owing to the higher solubility of the substrates in them. Notably, the best results were obtained under solvent less conditions as complete (100%) conversion of the subjected reactants was achieved in this case.
Considering the significance of temperature in altering the outcome of a reaction, we decided to investigate its effect on the one pot synthesis of β-enaminones and β-enaminoesters. As a step towards accomplishing this task, at first, the enamination reaction was performed at 25 °C using 20 mg of the synthesized Co-NQ@Am-SiO2@Fe3O4 nanocatalyst. Thereafter, the temperature of the reaction was increased progressively at intervals of 10 °C and its simultaneous influence on the product conversion and selectivity was studied. The results presented in Table S1† unambiguously revealed that among all the temperatures evaluated, 25 °C was found to be the most ideal one as it afforded the desired product with 100% conversion and selectivity. However, higher reaction temperatures (35 °C, 45 °C, 55 °C, and 65 °C) showed a noticeable decrease in the product selectivity which could be attributed to the formation of the di-substituted product.
Finally, the effect of reaction time on the percentage conversion of the model reactants was monitored by varying the time interval from 5 minutes to 30 minutes at 25 °C. The experimental results are displayed in Fig. S8.†
It is well apparent from the plot that the reaction conversion increases significantly with increasing the reaction time which is due to the fact that a longer time period favours the formation of the reactive intermediate species (substrate + catalyst) that eventually facilitates the formation of the desired product. A close inspection of the results showed that a reaction time of 30 minutes was the optimal period for the complete conversion of the model substrates.
Entry | R1 | R2 | R3 | Conversionb (%) | Yieldc (%) | TONd | TOFe |
---|---|---|---|---|---|---|---|
a Reaction conditions: amine (1 mmol), β-ketoester (1 mmol), Co-NQ@Am-SiO2@Fe3O4 catalyst (20 mg), stirring at r.t. (25 °C). b Conversion percentages determined via GC-MS have been given in parentheses. c Isolated yield. d TON is the number of moles of the product per mole of the catalyst. e TOF = TON/time (in Hours). | |||||||
1 | CH3 | OCH3 | CH2Ph | 100 | 95 | 357 | 714 |
2 | CH3 | OCH3 | Ph | 96 | 87 | 343 | 686 |
3 | CH3 | OCH3 | 4-CH3Ph | 95 | 90 | 339 | 678 |
4 | CH3 | OCH3 | 4-OCH3Ph | 86 | 82 | 307 | 614 |
5 | CH3 | OCH3 | 2-OCH3Ph | 80 | 80 | 286 | 572 |
6 | CH3 | OCH3 | 4-FPh | 47 | 40 | 168 | 336 |
7 | CH3 | OCH2CH3 | CH2Ph | 98 | 91 | 350 | 700 |
8 | CH3 | OCH2CH3 | Ph | 98 | 93 | 350 | 700 |
9 | CH3 | OCH2CH3 | 4-CH3Ph | 95 | 86 | 339 | 678 |
10 | CH3 | OCH2CH3 | 4-ClPh | 61 | 55 | 218 | 436 |
11 | CH3 | OCH2CH3 | 4-OCH3Ph | 88 | 81 | 314 | 628 |
12 | CH3 | OCH2CH3 | 2-OCH3Ph | 67 | 59 | 239 | 478 |
13 | Ph | OCH2CH3 | PhCH2 | 89 | 80 | 318 | 636 |
14 | Ph | OCH2CH3 | Ph | 80 | 74 | 286 | 572 |
15 | Ph | OCH2CH3 | 4-CH3Ph | 84 | 77 | 300 | 600 |
16 | Ph | OCH2CH3 | 4-OCH3Ph | 78 | 69 | 279 | 558 |
17 | Ph | OCH2CH3 | 2-OCH3Ph | 72 | 62 | 257 | 514 |
18 | CH3 | OC(CH3)3 | PhCH2 | 91 | 79 | 325 | 650 |
19 | CH3 | OCH2Ph | PhCH2 | 65 | 59 | 232 | 464 |
20 | CH3 | OCH(CH3)2 | PhCH2 | 93 | 88 | 332 | 664 |
21 | ClCH2 | OCH2CH3 | PhCH2 | 85 | 79 | 304 | 608 |
22 | CF3 | OCH2CH3 | PhCH2 | 73 | 62 | 261 | 522 |
23 | CH3 | CH3 | PhCH2 | 100 | 95 | 357 | 714 |
24 | CH3 | CH3 | 4-ClPhCH2 | 72 | 72 | 257 | 514 |
25 | CH3 | CH3 | 4-CH3PhCH2 | 87 | 85 | 311 | 622 |
In order to investigate the chemoselectivity of the process, we carried out a simple test (Scheme 2). First, we reacted a primary amine (n-butylamine) with β-ketoester (methylacetoacetate) under the optimized reaction conditions. We obtained the desired product with 70% reaction conversion. Next, we reacted a secondary amine (morpholine) with the same substrate (i.e. methylacetoacetate) and found that no morpholine derived product was formed even after prolonged stirring of the reaction contents.
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Fig. 8 Recycling experiment for the enamination reaction [reaction conditions: benzylamine (1 mmol), methylacetoacetate (1 mmol), Co-NQ@Am-SiO2@Fe3O4 catalyst (20 mg), stirring at r.t. (25 °C)]. |
Entry | β-Ketoester/β-ketone | Amine | Catalytic system | Reaction conditions | Yield (%) | Ref. |
---|---|---|---|---|---|---|
1 |
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[Cu(Hnbta)(1,3-btp)]·2H2O | Solvent free r.t. | 93 | 62 |
Metal–organic-framework | ||||||
Recyclability: three runs | ||||||
2 |
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SiW/c-Al2O3 | Acetonitrile r.t. | 94 | 63 |
Supported heteropolyacid | ||||||
Recyclability: four runs | ||||||
3 |
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Cu nanoparticles | Methanol 45–50 °C under a N2 atmosphere | 92 | 64 |
Recyclability: not evaluated | ||||||
4 |
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Silica sulfuric acid | Solvent-free 80 °C | 89 | 65 |
Recyclability: three runs | ||||||
5 |
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ZnO nanoparticles | Solvent-free 80 °C | 94 | 66 |
Recyclability: four runs | ||||||
6 |
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NiO | Ultrasound sonication 30 °C | 90 | 67 |
Recyclability: three runs | ||||||
7 |
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Ag nanoparticles in hollow mesoporous spheres | Methanol 60 °C | 84 | 68 |
Recyclability: five runs | ||||||
8 |
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Silver nanoparticles | Methanol 60 °C | 70 | 69 |
Recyclability: three runs | ||||||
9 |
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Naphthoquinone cobalt complex supported on SiO2@Fe3O4 nanoparticles | Solvent free r.t. | 98 | Present work |
Recyclability: eight runs | ||||||
10 |
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Naphthoquinone cobalt complex supported on SiO2@Fe3O4 nanoparticles | Solvent free r.t. | 99 | Present work |
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3su00073g |
This journal is © The Royal Society of Chemistry 2023 |