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Original article
13 (
1
); 3372-3382
doi:
10.1016/j.arabjc.2018.11.011

Synthesis of a magnetic-based yolk-shell nano-reactor: A new class of monofunctional catalyst by Cu0-nanoparticles and its application as a highly effective and green catalyst for A3 coupling reaction

Department of Chemistry, Semnan University, Semnan, Iran

⁎Corresponding author. fnemati@semnan.ac.ir (Firouzeh Nemati)

Disclaimer:
This article was originally published by Elsevier and was migrated to Scientific Scholar after the change of Publisher.

Peer review under responsibility of King Saud University.

Abstract

Abstract

A novel and yolk/shell nanoreactor catalyst (H-Fe3O4@h-Cu0@m-SiO2) was designed and synthesized with a hollow magnetite core encapsulated in a mesoporous silica shell which Cu0-nanoparticles were decorated in the interior cavity shell in order to enhance the catalytic activity. The morphology, structure and physicochemical properties of the yolk/shell nanoreactor were then fully characterized by using high resolution transmission electron microscopy (HRTEM), field-emission scanning electron microscopy (FE-SEM), energy-dispersive X-ray spectroscopy (EDX), X-ray diffraction patterns (XRD), Fourier transform infrared spectroscopy (FT-IR). The N2 absorption-desorption isotherms indicate a Brunauer–Emmett–Teller (BET) specific surface area of 287.36 m2/g and a pore width of 2–50 nm. Applied as a catalyst for three-component A3 coupling reaction of alkynes, aldehydes and amines under the optimized condition. Interestingly, the characterization results indicate that (H-Fe3O4@h-Cu0@m-SiO2) has great catalytic performance, which could be related to unique hollow morphology with an active core contains Cu0-nanoparticles, protective mesoporous shell and hollow void. This aspect of morphology leads to favoring the transfer of the reactants and products. Reusability up to 10 times without any obvious decline in catalytic activity and short reaction time are other advantageous of this green nano-reactor.

Keywords

Hallow sphere nanoparticles
Porous shell
Yolk/shell nanoreactor
Coupling reaction
1

1 Introduction

Hollow nanoparticles with functionalized interior space, specially core@void@shell structures that frequently called yolk-shell nanoreactors (YSN), have been known as an ideal candidate for catalyst applications due to their unique properties, including low density, large surface area, free void space between the core and porous shell and excellent loading capacity in the void space.

The yolk-shell nanostructures (YSNs), which consists catalyst species inside the cavity supplemented with a porous nano shell are a promising skeleton for the nanoreactor, which can tackle the issues of conventional nanoparticle-based catalyst. Among them nanoparticle-based nanoreactors have attracted considerable attention due to both scientific and application perspectives. Avoiding the aggregation, greater selectivity, easy recovery from the effluent, high stability, and eventually avoiding to significant decreases in surface area and catalytic activity are reasons of this interesting researches (Lee et al., 2014; Priebe and Fromm, 2015; Yang et al., 2012; Zhou et al., 2017).

Accessible pore channels of the mesoporous materials within high surface area and hollow void is another important factor to effect the catalytic performances of a yolk/shell nanoreactor catalyst which are beneficial for the diffusion and direction of transportation the starting materials and products. Functionalization of mesoporous silica nanomaterials has been proved because of good chemo and thermal stability as a shielding factor to protect the active sites from the harsh reaction conditions, and facilitating efficient transportations of starting materials and products for promoting various organic transformations under the green condition (Long et al., 2017; Yue et al., 2017; Zhou et al., 2017).

The most important feature in many catalyst systems is recovery and recycle after reaction completion without a meaningful reduction of the catalytic ability. So, the magnetic separation could be a good preference, which also is facilitated the elimination of the long time separation procedures such as filtration or centrifugation. Recently, excellent properties of hollow magnetic microspheres (H-F3O4) have attracted great interest because of their magnetic condensation, low density, high specific surface, large surface permeability, thermal stability and so. Accordingly, among different yolk-shell nanoparticles, YSNs that contains a magnetic core encapsulated in hollow mesoporous shell, due to high stability, biocompatibility, and significant magnetic strength of iron oxides, are in demand catalyst supports (Do et al., 2017; Hussain and Das, 2017; Liu, 2018; Nabid et al., 2014, 2015).

Recently, employing metal nanoparticles (NPs) as a benign and competitive alternative to common catalysis, due to high surface-to-volume ratio, has significantly increased (Baran, 2018b, 2018a; Baran et al., 2018; Nasrollahzadeh et al., 2015b, 2015b). However, the main difficulty in the use of metal NPs such as Co, Fe and Cu comes from their susceptibility toward leach, sinter, and oxidation during catalyst reaction, which are resulted the catalytic activity was lost. Therefore, to fully exploit the interior space of the hollow nanoreactor, the selectivity functionalized interior cavity by encapsulating catalytic active species (metal NPs) by a porous shell, is the most vital component which allows chemical transformations to happen inside the area of the protected cavity in environmentally acceptable conditions. Recently, different yolk/shell nano-catalysts based on Cu0-nanoparticles in interior cavity of nanoreactor were reported, which have the potential to be used in a wide range of application because more desirable compared to the precious metals, owing to important advantages such as high natural abundance and low cost of copper NPs (Borah et al., 2014; Do et al., 2017; Hao et al., 2016; Nabid et al., 2014; Zhang et al., 2016).

Three-component reaction of terminal alkynes, amines and aldehydes is one of the most powerful and useful synthetic tools for the synthesis of propargylamine derivatives. The propargylamines have played a remarkable role as starting materials for the manufacture various of chemicals such as agricultural chemicals, polymers, natural products such as β-lactams, herbicides, fungicides, and pharmaceutical products for the cure of some diseases such as Parkinson’s and Alzheimer’s disease (Hussain and Das, 2017; Mirhosseyni et al., 2016). In view of the importance of the propargylamines and in continuous of our pursuits for designing new composites (Elhampour et al., 2018; Elhampour and Nemati, 2017; Rangraz et al., 2018a, 2018b; Sabaqian et al., 2017, 2018; Shahamat et al.,) here in, we reported a magnetic yolk/shell nano-reactor, which consists significant impact of Cu0-nanoparticles were used as activity center for synthesize of propargylamines with excellent yields, reducing reaction times and also minimize the undesired products with very excellent reusability under solvent-less condition.

2

2 Experimental section

2.1

2.1 Materials

Iron (III) chloride hexahydrate (FeCl3 6H2O), Sodium acetate (NaOAc·3H2O), Ethylene glycol (EG), Polyvinylpyrrolidine (PVP), Tetraethyl orthosilicate (TEOS), (3-aminopropyl) triethoxysilane (APTES), Copper(II) acetate (Cu(CH3COO)2), Sodium borohydride (NaBH4), Cetyl trimethylammonium bromide (CTAB), Sodium carbonate (Na2CO3), Acetic acid (CH3COOH) and Ammonia (NH3) with analytical grade reagents, bought from Sigma-Aldrich. No additional purification was done.

2.2

2.2 Synthesis of hollow-Fe3O4 (H- Fe3O4)

Hollow-Fe3O4 particles were synthesized according to our earlier report. Typically, ethylene glycol (EG, 40 mL), PVP (1.0 g), ferric chloride hexahydrate (FeCl3·6H2O, 5 mmol) and then 30 mmol of sodium acetate (NaOAc) were added and stirred for 15 min. Thereafter, the obtained solution was transferred into a Teflon-lined stainless steel autoclave (100 cm3). The autoclave was heated to 200 °C and remained at this temperature for 12 h. After cooling the autoclave to the room temperature, the hollow-Fe3O4 spheres obtained as black solid. Ethanol and deionized water were used for washing the hollow-Fe3O4 particles and then were dried at 80 °C in an oven vacuum overnight (Mirhosseyni et al., 2016).

2.3

2.3 Synthesis of H-Fe3O4@SiO2

1 g of H-Fe3O4 particles were dispersed in a mixture of ethanol (60 mL, 99%), water (20 mL) and concentrated ammonium hydroxide (1.5 mL, 28%). The ultrasonic vibration in a water bath was used for homogenizing of the suspension. Then, a solution of tetra ethyl orthosilicate (TEOS) (0.5 mL) in ethanol (10 mL) was added to the mixture drop by drop under continuous stirring for 12 h. Finally, the resulting silica-coated H-Fe3O4 were collected by magnetic separation and washed several times with ethanol to remove black silica nano-particles. Finally, the obtained H-Fe3O4@SiO2 was dried in an oven overnight (Nemati et al., 2012).

2.4

2.4 Preparation of H-Fe3O4@SiO2 functionalized (3-aminopropyl) triethoxy silane (H-Fe3O4@SiO2-NH2)

0.2 g of prepared H-Fe3O4@SiO2 magnetic nanoparticles was dispersed in 40 mL of anhydrous ethanol under ultrasonic. After 15 min, 5 mL of (3-aminopropyl) triethoxy silane (APTES) was added. The mixture was heated at 80 °C for 24 h under N2 atmosphere. Then, the functionalized MNPs were separated and washed several times with ethanol eventually and dried at 60 °C. This product was be referred as H-Fe3O4@SiO2-NH2 (Zhu et al., 2014b).

2.5

2.5 Synthesis of H-Fe3O4@SiO2-Cu0

In 15 mL water, copper acetate Cu(OAc)2 (0.0254 mmol) was dissolved and added to 0.5 g of H-Fe3O4@SiO2-NH2 magnetic nanoparticles (MNPs) under vigorous stirring for 6 h, drop by drop. In next step, the solvent was evaporated by a rotary evaporator, which 0.3 g of composite was obtained. Then, it was dispersed in 50 mL of water. The aqueous solution of NaBH4 (134 mg, 3.54 mmol) was slowly added to the suspension of the above composite. The suspension was stirred for 15 min under nitrogen gas atmosphere. During this stage, Cu (II) was converted into Cu (0) nanoparticles (Cu0 NPs). After magnetic separation, the obtained H-Fe3O4@SiO2-NH2-Cu0 particles were washed with deionized water several times to remove impurities and then rested in an oven for 12 h (Borah et al., 2014).

2.6

2.6 Synthesis of H-Fe3O4@SiO2-Cu0@SiO2

0.1 g H-Fe3O4@SiO2-Cu0 particles that obtained from the previous step were dispersed in 20 mL water and was applied to ultrasonic vibration for 15 min (part A). 150 mg of cetyltrimethyl ammonium bromide (CTAB) and NH3·H2O (28%, 0.55 mL) were poured into the mixture of 30 mL ethanol and 30 mL H2O and then stirred at 30 °C in water bath (part B). After that, the part A and part B were mixed together and sonicated for 2 h. Next, TEOS (0.25 mL) was quickly added into the mixture, and was stirred further for 6 h. Finally, H-Fe3O4@SiO2-Cu0@SiO2 particles were separated from the suspension magnetically and dried in an oven at 70 °C overnight (Deng et al., 2008).

2.7

2.7 Synthesis of H-Fe3O4@hollow-Cu0@SiO2 and H-Fe3O4@h-Cu0@m-SiO2 yolk-shell nano-reactor

The H-Fe3O4@SiO2-Cu0@SiO2 core/shell particles were dispersed in 10 mL of deionized water. Then, 100 mg Na2CO3 was added into the above suspension during vigorous stirring. After that, it was stirred at 50 °C for 10 h, to remove the inner SiO2 layer. Finally, the as prepared H-Fe3O4@h-Cu0@SiO2 yolk/shell catalyst were collected by using a permanent magnet, washed with ethanol and water, and dried in an oven at 70 °C overnight. In order to synthesis of mesoporous and porous silica shell, the purified H-Fe3O4@h-Cu0@SiO2 microspheres were re-dispersed in 100 mL ethanol until the formation of a black solution. Removing the template (CTAB) was done using addition of 1 mL glacial acetic acid and refluxing the mixture at 80 °C for 12 h. The removal procedure was repeated for two times. The H-Fe3O4@hollow-Cu0@mesoporous-SiO2 (named H-Fe3O4@h-Cu0@m-SiO2) yolk-shell nano-reactor was collected magnetically and washed with deionized water (Zhang et al., 2016; Zhu et al., 2014a).

2.8

2.8 Typical procedure for the synthesis of propargylamine derivatives

In a flask, the mixture of arylaldehyde (1 mmol), amine (1.2 mmol), alkyne (1.5 mmol) and nano-reactor (0.006 g) as a catalyst were added and stirred at 110 °C for a suitable time. Monitoring of the progress of reaction was done by TLC (n-hexane: ethyl acetate, 2:8). When the reaction was ended, the mixture was cooled and diluted with hot ethanol and stirred for some minutes. Afterwards, the catalyst was separated using a permanent magnet, washed with ethanol, and dried in the oven. Then, it re-used for a sequential run under the same reaction condition. The resulting remainder was purified by a short column chromatography on silica gel to acquire the desired product in high purity. All the products are known compounds and the spectral data and melting points were identical to those reported in the literature.

3

3 Result and discussion

3.1

3.1 Preparation of nano-reactor

Scheme 1 illustrates the five stages of the preparation of novel nano-reactor as catalyst. Briefly, H-Fe3O4 particles were assembled according to our recently reported procedure (Mirhosseyni et al., 2016) and the surface of hollow magnetic particles were covered with SiO2 layer by a sol-gel method (Nemati et al., 2012). Boosting the interaction with Cu nano-particles through the coordination ligand with amino groups was achieved by modification of H-Fe3O4@SiO2 micro-spheres with APTES (Zhu et al., 2014b). The Cu0 nanoparticles were immobilized on the exterior of H-Fe3O4@SiO2-NH2 and was covered by SiO2 layers by means of the Zhang’s procedure using CTAB as template (Borah et al., 2014; Deng et al., 2008). Chemical etching of inner SiO2 layer with Na2CO3 solution followed by extraction of template (Zhang et al., 2016; Zhu et al., 2014a), resulted H-Fe3O4@h-Cu0@m-SiO2 yolk-shell nano-reactor as described in experimental section.

Schematic representation for preparation of H-Fe3O4@h-Cu0@mSiO2 yolk-shell nano-reactor.
Scheme 1 Schematic representation for preparation of H-Fe3O4@h-Cu0@mSiO2 yolk-shell nano-reactor.

3.2

3.2 Characterization of magnetic H-Fe3O4@h-Cu0@mSiO2 yolk-shell nanoreactor

3.2.1

3.2.1 FT-IR spectra

The Fourier transform infrared spectroscopy spectra has been accomplished to check out the structure of the stages of synthesized H-Fe3O4@h-Cu0@mSiO2 nano-reactor. As shown in the Fig. S1a the broad peak over the range of 3470 cm−1 correspond to the OH stretching vibration that are available on the exterior of magnetic H-Fe3O4 particles. The absorption band observed at 850 cm−1 is related to the stretching vibration of Fe-O-Fe in the spinel octahedral structure of H-Fe3O4, which shows decrease in intensity after encapsulation of silica on the magnetic particles (Liu, 2018; Mirhosseyni et al., 2016; Xiong et al., 2012). For all the silica-based materials, the strong and weak absorption bands at 1088 and 1009 cm−1 were appeared, which arise from Si-O-Si asymmetrical stretching vibration and Si-O symmetrical stretching vibration, respectively (Fig. S1b–e) (Do et al., 2017; Zhou et al., 2017). Meantime, functionalization of particles with APTES was confirmed with the absorbance bands at 2976, 2939, 1568 and 1465 cm1, which indicated the stretching modes of the -CH2 and –NH2 groups of APTES (Fig. S1c) (Khatiri et al., 2012; Zhou et al., 2017). The bands at 2976 and 1100 cm−1 are correspond to aliphatic C-H and C-N bonds stretching vibrations in structure of CTAB, respectively (Fig. S1d), which were almost disappeared upon extraction (Fig. S1e). It proved nearly all the CTAB was extracted from the silica shell.

3.2.2

3.2.2 XRD patterns

The phase and combination of as-synthesized sample were thoroughly investigated by applying the XRD patterns. The crystalline cubic spinel structure of H-Fe3O4 particles was confirmed by reflections peaks at (2 2 0), (4 0 0), (4 2 2), (5 1 1), (4 4 0), and (5 3 3) (Fig. 1a) (Liu, 2018; Mirhosseyni et al., 2016). The wide reflection peak at  = 20–30° was confirmed that the silica layer was successfully covered on the surface of magnetic particle (Fig. 1a) (Nemati and Saeedirad, 2013). The additional peak at  = 50.3° which is assigned to the (2 0 0) indices of the metallic Cu. The metal Cu nanoparticles peaks at 43.3° and 73.99° overlap with the 43.2° and 74.3° peaks of H-Fe3O4. These results confirm the formation of copper nanocrystals only in zero oxidation state on the exterior of H- Fe3O4@SiO2-NH2-Cu0 NPs (Fig. 1b) (Borah et al., 2014; Do et al., 2017; Tang et al., 2014). As well as, the XRD pattern of H-Fe3O4@h-Cu0@mSiO2 yolk-shell nano-reactor shows the same peaks, which coincides with H- Fe3O4@SiO2-NH2-Cu0 NPs and obviously not changed after coating with mesoporous silica. These results verify that the peak positions and the crystalline structures of H-Fe3O4 nanoparticles during the procedure of nano-reactor synthesis were kept unchanged. By applying the Scherrer's equation (D = kλ/βcosθ) the average crystalline size of the H-Fe3O4 particles is estimated to be 33 nm.

XRD patterns of H-Fe3O4 (a), H- Fe3O4@SiO2-NH2-Cu0 (b), H-Fe3O4@h-Cu0@mSiO2 (c).
Fig. 1 XRD patterns of H-Fe3O4 (a), H- Fe3O4@SiO2-NH2-Cu0 (b), H-Fe3O4@h-Cu0@mSiO2 (c).

3.2.3

3.2.3 Thermo gravimetric analysis

The thermogravimetric analysis (TGA), DTA and DTG analysis of H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor catalyst were evaluated and depicted in Fig. 2 and Fig. S2, respectively. TGA analysis was carried out at temperatures ranging from 30 to 800 °C under air flow. Three stages of mass loss were observed in the thermogram of nano-reactor. The initial lose in the range of 38–125 °C is related to the adsorbed water or organic solvents in the surface of nano-reactor. The second mass loss was occurred between 310 and 530 °C, which could be correspond to the remaining CTAB in the structure of composite. The third stage (530–740 °C) is due to dihydroxylation of silanol groups, which be done in the temperatures higher than 500 °C.

TGA and DTA diagrams of H-Fe3O4@h-Cu0@mSiO2.
Fig. 2 TGA and DTA diagrams of H-Fe3O4@h-Cu0@mSiO2.

Inaddition, the synthesized nano-reactor exhibits a considerable thermal stability at high temperature.

3.2.4

3.2.4 FE-SEM-EDX and TEM analysis

Fig. 3 shows the typical images of FE-SEM of H- Fe3O4@SiO2-NH2-Cu0 NPs and H-Fe3O4@h-Cu0@mSiO2 Yolk-Shell nano-reactor. The FE-SEM images show that the materials have a clean spherical shape, well dispersed and uniform in morphology. Furthermore, the FE-SEM of H-Fe3O4@h-Cu0@mSiO2 yolk-shell nano-reactor declared its mono disperse nanostructures. The energy dispersive X-ray spectroscopy (EDX) analysis of the H-Fe3O4@h-Cu0@mSiO2 yolk-shell nano-reactor has been proved the presence of expected elements Fe, Si, Cu and O in synthesized nano-reactor (Fig. S3). The amount of Cu in the inner cavity shell of final catalyst was measured using ICP-AAS and it was 0.035%.

FE-SEM images of (a) H- Fe3O4@SiO2-NH2-Cu0 NPs, (b) H-Fe3O4@h-Cu0@mSiO2 yolk-shell nanoreactor.
Fig. 3 FE-SEM images of (a) H- Fe3O4@SiO2-NH2-Cu0 NPs, (b) H-Fe3O4@h-Cu0@mSiO2 yolk-shell nanoreactor.

The high resolution transmission electron microscopy (HR-TEM) obviously appears three distinct sections. The black cores of microspheres of H-Fe3O4, the small black spheres of Cu NPs and the gray mesoporous channels of SiO2 which are aligned perpendicular to the microspheres surface of H-Fe3O4 as shell. The HR-TEM also displays the Cu nanoparticles dispersed in the inner surface of mesoporous silica shell (Fig. 4).

HR-TEM images of H-Fe3O4@h-Cu0@mSiO2 yolk-shell nano-reactor.
Fig. 4 HR-TEM images of H-Fe3O4@h-Cu0@mSiO2 yolk-shell nano-reactor.

3.2.5

3.2.5 BET and BJH analysis

Fig. 5 exhibits the N2 adsorption–desorption isotherm and the corresponding BJH pore-size distribution curve of the H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor. As can be seen in Fig. 5, a typical type IV isotherm with high relative pressures (P/P0 < 0.1) was present for as-prepared nanoreactor, which is characteristic of mesoporous material with uniform and desirable pores.

Nitrogen adsorption-desorption isotherm of yolk/shell H-Fe3O4@h-Cu0@mSiO2 (A) and the corresponding pore-size distribution curves isotherm (B).
Fig. 5 Nitrogen adsorption-desorption isotherm of yolk/shell H-Fe3O4@h-Cu0@mSiO2 (A) and the corresponding pore-size distribution curves isotherm (B).

The BET surface area, pore diameter and pore volume of H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor were 287.36 m2/g, 4.9817 nm and 0.3579 cm3/g, respectively. These data further prove that the mesoporous structure is dominant in synthesized nanoreactor.

3.3

3.3 Catalytic activity

Having synthesized and characterized of H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor, at first, its catalytic activity was compared with H-Fe3O4@SiO2-NH2-Cu0, H-Fe3O4@SiO2-Cu0@CTAB-SiO2 and H-Fe3O4@h-Cu0@CTAB-SiO2 core/shell nanoparticles. So, they were used as a heterogeneous magnetic catalysts in one-pot, three component reaction of benzaldehyde, morpholine, and phenylacetylene, which was selected as the model reaction for synthesis of propargylamines (Table 1, entries 2–5). As shown in Table 1, the yield of the corresponding product is negligible for the A3 coupling reaction by using H-Fe3O4@SiO2-Cu0@CTAB-SiO2 and H-Fe3O4@h-Cu0@CTAB-SiO2, due of the presence of silica shell and CTAB, which has led to decrease in the activity of zero copper nanoparticles. The H-Fe3O4@SiO2-NH2-Cu0 shows lower yield than the H-Fe3O4@h-Cu0@mSiO2 nanoreactor. This observation can be due to the stronger and more effective interaction between zero copper nanoparticles as a predominant catalytic active site with reactants in the internal cavity of the magnetic H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor.

Table 1 Optimization of the reaction of three-component reaction catalyzed by H-Fe3O4@h-Cu0@mSiO2a
Entry Catalyst (g) Condition Yield (%)b
1 Solvent free/110 °C Trace
2 H-Fe3O4@SiO2-NH2-Cu0(0.006) Solvent free/110 °C 85
3 H-Fe3O4@SiO2-Cu0@CTAB-SiO2(0.006) Solvent free/110 °C Trace
4 H-Fe3O4@h-Cu0@CTAB-SiO2(0.006) Solvent free/110 °C Trace
5 H-Fe3O4@h-Cu0@mSiO2 (0.01) Solvent free/25 °C Trace
6 H-Fe3O4@h-Cu0@mSiO2 (0.01) Solvent free/80 °C 60
7 H-Fe3O4@h-Cu0@mSiO2 (0.01) Solvent free/100 °C 90
8 H-Fe3O4@h-Cu0@mSiO2 (0.01) Solvent free/110 °C 98
9 H-Fe3O4@h-Cu0@mSiO2 (0.01) Solvent free/130 °C 98
10 H-Fe3O4@h-Cu0@mSiO2 (0.006) Solvent free/110 °C 98
11 H-Fe3O4@h-Cu0@mSiO2 (0.003) Solvent free/110 °C 70
12b H-Fe3O4@h-Cu0@mSiO2 (0.006) Toluenec/110 °C 60
13b H-Fe3O4@h-Cu0@mSiO2 (0.006) DMFc/110 °C 70
Reaction conditions: benzaldehyde (1 mmol), morpholine (1.2 mmol), phenylacetylene (1.5 mmol); at ambient atmosphere. Time of the reactions for entries 1–11: 15 min, for entries 12 and 13: 1 h.
Isolated yield.
Solvent (3 mL).

In the next step, after optimization of appropriate catalyst, in order to obtain the best suitable conditions for synthesis of target products by A3 coupling reaction, we have optimized the reaction variables by studying the effect of reaction parameters including solvent, temperature, and the amount of catalyst for the aforementioned reaction as shown in Table 1, entries 5–11. The results established that most favorable reaction condition was achieved by using 6 mg catalyst (0.03 mol %) in the solvent-less condition at 110 °C. The ratio of aldehyde: amine: alkyne as substrates was optimized to 1:1.2:1.5.

Having the optimized reaction condition for examining the scope of our methodology, we have applied the procedure to various substrates for this catalytic system. For this purpose, various type of substituents arylaldehydes (electron-donating and electron-withdrawing), alkynes and secondary amines were employed and the results are out came in Table 2. The results indicate arylaldehydes bearing different functional groups such as -Br, -Cl, -Me, -OMe, and –OH, were able to produce the corresponding A3 coupling products. However, the transformation with electron-donating or electron-withdrawing substitutions on arylaldehyde derivatives has been observed with no difference in reactivity.

Table 2 Synthesis of propargylamine derivatives using H-Fe3O4@h-Cu0@mSiO2 as nano-reactor.a
Entry Aldehyde Amine Product Time (min) Yield (%)b
1 C6H5-CHO Morpholine 4a 15 98
2 3-HO-C6H4-CHO Morpholine 4b 25 83
3 4-Me-C6H4-CHO Morpholine 4c 35 92
4 4-HO-3-OMe-C6H4-CHO Morpholine 4d 45 90
5 2-HO-C6H4-CHO Morpholine 4e 25 85
6 2-Me-C6H4-CHO Morpholine 4g 35 93
7 4-MeO-C6H4-CHO Morpholine 4g 35 90
8 Thiophene-2-carbaldehyde Morpholine 4 h 30 94
9 4-F-C6H4-CHO Morpholine 4i 30 93
10 2-F-C6H4-CHO Morpholine 4j 30 90
11 4-Br-C6H4-CHO Morpholine 4k 30 93
12 4-Cl-C6H4-CHO Morpholine 4L 30 92
13 4-CHO-C6H4-CHO Pipiridine 4m 30 95
14 2-naphtaldehyde Piperidine 4n 30 94
15 C6H4-CHO Piperidine 4o 20 96
16 3-OHC6H4-CHO Piperidine 4p 25 81
17 4-HO-3-Me-C6H4-CHO Piperidine 4q 40 89
18 4-MeO-C6H4-CHO Piperidine 4r 35 86
19 4-FC6H4-CHO Piperidine 4s 30 91
20 Thiophene-2-carbaldehyde Piperidine 4t 30 93
21 C6H4-CHO Morpholine 4u 20 97
22 C6H4-CHO Piperidine 4v 20 95
23 2-HO-C6H4-CHO Morpholine 4w 25 80
24 C6H5-CHO Diethyl amine 4x 30 81

For entries 1–20 and 24, R = Ph and for entries 21–23, R = -C(CH3)2OH.

Reaction conditions: arylaldehyde (1 mmol), amine (1.2 mmol), alkyne (1.5 mmol), H-Fe3O4@h-Cu0@mSiO2 (0.006 g), under solvent-free condition at 110 °C at ambient atmosphere.
Isolated yield.

A comparative study has been made for the catalyst performance of the H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor with the other reported copper-metal containing catalyst for the synthesis of propargylamine derivatives (Table 3).

Table 3 Comparison of catalytic activity of H-Fe3O4@h-Cu0@mSiO2 with reported copper content catalyst for synthesis of propargylamine 4a.
Entry Catalyst Condition Time (h) Yield (%) Ref
1 Cu@PMO-1La CHCl3/60 °C 24 96 Gholinejad et al. (2015)
3 Cu/Al Toluene/100 °C 22 94 Dulle et al. (2013)
3 CuNPs@TiO2 Solvent free/70 °C 7 91 Albaladejo et al. (2012)
4 Cu NPs Solvent free/80 °C 7 90 Shouli, et al. (2017)
5 Cu@MOF-5-Cb Toluene/110 °C 6 90 Cheng et al. (2017)
6 CuO/GNSc CH3CN/82 °C 5 89 Gopiraman et al. (2015)
7 SiO2@Cu Toluene/110 °C 5 94 Guo et al. (2013)
8 Cu-MPTA-ld CH2Cl2/25 °C 24 93 Salam et al. (2013)
9 Cu-MCM-41 Solvent free/110 °C 2/30 93 Abdollahi-Alibeik and Moaddeli (2014)
10 Cu/G Toluene/110 °C 4 96 Frindy et al. (2016)
11 H-Fe3O4@h-Cu0@mSiO2 Solvent free/110 °C 15 min 98 This work
Copper supported on periodic mesoporous organosilica (PMO) ionic liquid.
Metal-organic-frameworks (MOFs)-Prous carbon materials.
CuO nanoparticles (CuO NPs)/graphene nanosheet (GNS).
Mesoporous poly-triallylamine (MPTA-1).

Incomparable superiorities of our protocol quite clear in terms of reaction time and yield for the synthesis of propargylamines via A3 coupling reaction compared to other reported catalysts. Therewith, by using this yolk/shell nanoreactor as catalyst, the reaction could progress under benign reaction condition, i.e. solvent-free and low amount of catalyst with maximum efficiency and activity of copper-metal.

3.4

3.4 Reaction mechanism

A proposed mechanism route for the three component synthesis of propargylamines, which catalyzed in the internal cavity of the H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor is illustrated in Scheme 2.. In the first stage, the formation of Cu-acetylide intermediate take place from activation of the terminal C—H bond of acetylenic substrate by zero copper nanoparticles in the internal cavity of nanoreactor. In the second step, the iminium ion is produced from the reaction of aldehyde and secondary amine, which permitted the reaction with Cu-acetyline to provide the desired propargylamine and regenerate the active h-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor for further reaction.

Reaction mechanism for the synthesis of propargylamines.
Scheme 2 Reaction mechanism for the synthesis of propargylamines.

3.5

3.5 Reusability of the catalyst

Stability, recovered simply and reusability of a magnetic catalyst are one the most important basic parameter for sustainability of yolk/shell nanoreactor. So, the recyclability of h-Fe3O4@h-Cu0@mSiO2 catalyst was examined for the model reaction and the results show that very acceptable outcomes. Upon completion of the reaction, hot ethanol was added to the reaction mixture and the catalyst was easily separated using an external magnetic and extensively washed (see experimental section). The results determined that, the yield of the corresponding product was saved to 96%, even after 10 runs (Run 1: 98%; Run 2: 98%; Run 3: 98%; Run 4: 97%; Run 5: 97%; Run 6: 97%; Run 7: 96%; Run 8: 96% Run 9: 96%; Run 10: 98%;).

From where, the H-Fe3O4@SiO2-NH2-Cu0 shows moderate catalytic efficiency toward A3 coupling reaction (Table 1, entry 2), we examined the recyclability of it too. However, with the increasing of run to 3 cycle in model reaction, losing of catalytic effect could be observed and the yield of the corresponding product decreased to 51%. This diminishing mainly could be due to leaching of copper nanoparticles. So, the Cu amounts, which loaded in H-Fe3O4@SiO2-NH2-Cu0 was determined before and after three runs by AAS. They were 0.04% and 0.01%, respectively.

On the other hand, h-Fe3O4@h-Cu0@mSiO2 could serve its catalytic performance even after 10 runs. It is quite clear that the porous shell of silica is responsible for fixation and stability of copper nanoparticles. The content of Cu deceased from 0.035% to 0.030% after 10 cycles. So, we make sure the principle reason for the deactivation of catalyst is leaching of active sites, which is copper nanoparticles.

Interestingly, comparing the XRD pattern of fresh and recovered Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor catalyst displayed that the phase composition and crystalline structure of the prepared nano reactor remained unchanged after using ten times in the three-component A3-coupling reaction and by applying the Scherrer's equation (D = kλ/βcosθ) the average crystalline size of the H-Fe3O4 particles is estimated to be 33 nm (Fig. 6).

XRD pattern of Fe3O4@h-Cu0@mSiO2 (a) before use and (b) after reused 10 runs.
Fig 6 XRD pattern of Fe3O4@h-Cu0@mSiO2 (a) before use and (b) after reused 10 runs.

4

4 Conclusion

In summary, a novel and efficient magnetic catalyst, H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor was designed and prepared with Fe3O4 hollow spheres with mesoporous and hollow silica shell that zero copper nanoparticles are concentrated in the shell inner cavity via a facile hydrothermal method. H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor was successfully applied as superior and magnetic catalyst for pushing three-component A3-coupling reaction of alkyne, amine and aldehyde for synthesis of c propargylamines under benign condition. The magnetic H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor catalyst could promote A3 coupling reaction to obtain up to 98% yield of the coupling product under optimized condition, and most importantly, this yolk/shell nanoreactor could be easily separated and reused up and it offers 96% yield of the desired product even after using ten times of the catalyst, and it is worth mention that the loss of copper metal in the inner cavity was negligible. The result revealed that the magnetic H-Fe3O4@h-Cu0@mSiO2 yolk/shell nanoreactor catalyst is premiere over to other previously reported catalyst in terms of yield, reaction times, and recyclability.

Acknowledgements

The authors gratefully acknowledge the Semnan university research council for the financial of this project.

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Appendix A

Supplementary material

Supplementary data to this article can be found online at https://doi.org/10.1016/j.arabjc.2018.11.011.

Appendix A

Supplementary material

The following are the Supplementary data to this article:

Supplementary data 1

Supplementary data 1

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