Navneet
Kaur
a,
Simranpreet
Kaur
a,
Gurpreet
Kaur
a,
Aman
Bhalla
a,
Sesha
Srinivasan
b and
Ganga Ram
Chaudhary
*a
aDepartment of Chemistry, Centre for Advanced Studies in Chemistry, Panjab University, Chandigarh-160014, India. E-mail: grc22@pu.ac.in; Fax: +91-172-2545074; Tel: +91-172-2534406
bFlorida Polytechnic University, Lakeland-33805, Florida, USA
First published on 15th June 2019
Metallovesicles are an emerging class of soft nanomaterials where spherical bilayer membranes, resulting from self-aggregation of amphiphilic metal complexes, amalgamate the advantages of metal specific catalytic properties and small hydrophobic cavities serving as nanoreactors. The confinement of substrates in these vesicle bilayers, on account of hydrophobic interactions in aqueous media, encourage their application in catalysis, particularly, where preclusion of organic solvents is of prime concern without compromising desired reaction rates and product yields. In the present work, novel amphiphilic metallosurfactant complex [Cu(C12H25NH2)2]Cl2 has been self-assembled to achieve spherical bilayer structures known as copper metallovesicles (CuMVs). DLS, TEM and FESEM analyses revealed the formation of spherical multivesicular vesicles in the size range 160–200 nm. The multivesicular structure of CuMVs was further supported by small angle X-ray scattering (SAXS) results. The as-synthesized CuMVs were further assessed for their potential as aqueous catalytic system for the synthesis of important therapeutic agents, benzimidazoles. The co-existence of hydrophobic reactants inside the metal-adorned vesicle bilayers, affords high product yield in short times. Facile synthesis of metallosurfactants, self-assembly to metallovesicles, aqueous reaction media, low metal concentration, low E-factor values, stability and recyclability of metallovesicles are the features that establish metallovesicular catalysis as a promising multifaceted approach for greener catalysis of benzimidazole synthesis and many other significant synthetic reactions.
Nanoreactors, comprising the non-covalent self-assemblies of amphiphilic molecules, have emerged as excellent alternatives to combine the features of homogeneous and heterogeneous catalysis in one-pot.7 The amphiphilic nature of these self assemblies resolve the solubility issues of substrates in water, which are held together in hydrophobic pockets of these self-assembled nanoreactors. The compartmentalization of substrates results in their increased proximity and concentration around active catalytic sites.8 In literature, a vast variety of amphiphilic aggregates like micelles, vesicles, microemulsions, liposomes, polymerosomes etc. of suitable morphology are known to enhance the reaction rates of many organic reactions.9–13 Vesicles, for instance, have better catalytic performance in comparison to micelles and other aggregates14–16 because of the following four factors17 (i) they possess chemical aspects of biological membranes and show tremendous selectivity (ii) they increase the proximity between the reagents by decreasing the effective volume where the reaction takes place (iii) their structural complexity provides necessary stearic-hindrance to avoid side reactions (iv) they provide reaction centers with different polarity in comparison to the bulk solvent. Depending upon reaction requirements, the fourth factor can be altered by incorporation of a metal ion into the vesicular structure. The metallovesicles, formed as a result of functionalization of traditional vesicles with suitable metal ions, are adorned with notable catalytic properties.18,19 Though there are numerous applications of vesicular systems in drug delivery, model protocells, vaccination and reaction promoters,20–24 the metallovesicular systems are very less explored for their potential as efficient catalytic systems.
The aim of the present work is two-fold; one, to fabricate metallovesicles (CuMVs) from amphiphilic metallosurfacatnt complex, bisdodecylaminecopper(II) chloride and assess their structural details. And two, to efficiently use the as-fabricated CuMVs, as catalyst, in synthesis of benzimidazole derivatives in milder reaction conditions with water as solvent. Benzimidazole and its derivatives are important building blocks of pharmaceutical industries owing to their various biological activities such as antiarrhythmic,25 antiulcer,26 ionotropic,27 antihelmintic,28 anticancer29 and antimicrobial activities.30 Furthermore, these compounds have significant industrial applications in UVB filters, optical devices, paints, and fuel cell membranes.31–34 Many reports are available in literature to synthesize benzimidazoles by the condensation of arylaldehydes with ortho-phenylenediamines using variety of homogeneous and heterogeneous catalysts, for e.g. acetic acid,35 trimethylsilyl chloride,36 oxone,37 sulphamic acid,38 PhI(OAc)2,39 KHSO4,40 K3PO4,41 Amberlite,42L-proline,43 CoCl2,44 PTSA,45 metal triflates,46 heteropoly acids,47 solid support catalysts48 and ionic liquids49etc. Unfortunately, many of these methods suffer from drawbacks such as environmentally hazardous solvents/reagents, drastic reaction conditions, low yields, tedious workup procedures, low atom economy and various side products. Nanoparticles have also been utilized as heterogeneous catalysts in this synthesis but most of the high-performing nanoparticles catalysts include expensive transition metals, hazardous oxidants generating toxic by-products.50–56 As a consequence, the introduction of an efficient and mild method is still needed to overcome these limitations. The present catalytic system, comprising of CuMVs, offers a room temperature synthesis of 2-aryl-1H-benzimidazole derivatives at low metal concentration in aqueous media which is economic, environmentally benign, recyclable and energy efficient. The intriguing results obtained with CuMVs in the present synthetic reaction with low E-factor values, expand their scope as catalysts in other reactions as well as gives direction in designing similar catalytic structures with different functionalities.
The CuMVs were prepared by employing conventional chloroform film method.58 Equimolar amounts of [Cu(C12H25NH2)2]Cl2 (5 mmol) and cholesterol (5 mmol) were dissolved in CHCl3 (20 ml). The solution was stirred at 333 K in a round bottom flask for 30 minutes followed by slow evaporation of CHCl3 under reduced pressure. The resulting thin film on the surface of round bottom flask was dried in vacuum desiccator at room temperature for 24 h and further hydrated with deionized water (100 ml). The obtained solution was repeatedly sonicated, subjected to vortex shaker for about 4 h and obtruded through polycarbonate microfilters (0.25 micron pore size) for at least 10 times which resulted in uniform particle size distribution as monitored by Dynamic Light Scattering (DLS). Different volumes of this solution were further used for catalytic synthesis of benzimidazole derivatives.
| Entry | Diamine | Aromatic aldehyde | Product | Time (min) | Yieldb (%) | E-factor |
|---|---|---|---|---|---|---|
| a Reaction conditions: o-phenylenediamine (1 mmol), aromatic aldehyde (1 mmol), CuMVs (2 ppm, 20 ml), 303 K. b Isolated yield. | ||||||
| 1a |
|
|
|
70 | 94 | 0.175 |
| 1b |
|
|
|
85 | 90 | 0.212 |
| 1c |
|
|
|
80 | 93 | 0.173 |
| 1d |
|
|
|
45 | 95 | 0.142 |
| 1e |
|
|
|
50 | 93 | 0.166 |
| 1f |
|
|
|
60 | 95 | 0.148 |
| 1g |
|
|
|
75 | 95 | 0.130 |
| 1h |
|
|
|
60 | 96 | 0.138 |
| 1i |
|
|
|
80 | 91 | 0.206 |
An amphiphilic metallosurfactant complex of copper equipped with two long hydrocarbon chains viz [Cu(C12H25NH2)2]Cl2 was synthesized and further used for the preparation of CuMVs using film hydration method. The thin film as described in Section 2.2.1 consists of sediments of multiple bilayers which were sonicated and mechanically vortexed with deionised water at a temperature above the phase transition temperature (333 K) of metallosurfactant complex (illustrated by DSC, Fig. S1, ESI†). This resulted in swelling and folding of these lamellar bilayer structures into spherical CuMVs. The addition of equimolar amounts of cholesterol to metallosurfactant complex was done to meliorate rigidity and stability of CuMVs.59 The notably polydisperse CuMVs were repeatedly extruded (at least 10 times) through polycarbonte microfilters resulting in monodisperse CuMVs as monitored by DLS.60 DLS analyses of CuMVs before and after extrusion are given in (Fig. S2, ESI†) respectively. The polydispersity index of CuMVs was reduced from 0.367 to 0.132 after extrusion. The average size of extruded CuMVs was found to be 220 nm. It is to be noted that amount of water used for hydration process has no effect on CuMVs' morphology. However, it results in the variation of concentration of resulting CuMVs in solution.
Morphological details of CuMVs were obtained by different microscopic techniques. Preliminary structural examination of CuMVs was done with conventional light microscope that showed spherical structures (Fig. S3(a), ESI†). Further detailed examination of size, morphology and topography of the CuMVs was carried out using TEM, CLSM, FESEM and AFM techniques. TEM, CLSM and FESEM analysis gave a fairer insight into the size, morphology and lamellarity whereas AFM studies showed topographical analysis of the prepared CuMVs. TEM image (Fig. 1(a)) shows the formation of multivesicular metallovesicles (large number of small vesicles inside a giant vesicle) in the size range 160–200 nm. Inset of Fig. 1(a) shows high resolution TEM image of a multivesicular vesicle (180 nm). The spherical shape of CuMVs is further confirmed through CLSM images (Fig. 1(b)). Also, the FESEM results affirm with those of TEM showing spherical shaped structures (Fig. S3(b)†).58 AFM images show height and phase topographies of CuMVs (Fig. S3(c)58 and (d),† respectively). Color contrast in height images reveals the average particle size of CuMVs in the range of 180–200 nm however vesicles are found to be vertically compressed due to high local force applied by the tip of the cantilever. Colour contrast in phase image shows distinct phase boundaries as we move from one metallovesicle to other, showing segregated distribution of CuMVs. Careful analysis of the phase images shows colour contrast within the same vesicle illustrating the presence of different phases in accordance with multivesicular topography.
![]() | ||
| Fig. 1 Structural investigation of CuMVs showing (a) TEM micrograph, inset: single multivesicular vesicle (b) CLSM image. | ||
Further structural investigation of CuMVs was done using SAXS. Fig. 2(a) shows experimental SAXS scattering profile of CuMVs in which scattering intensities I(q) are plotted as a function of scattering vector q, which is defined as 4π
sin
θ/λ; where θ is half the scattering angle and λ is wavelength of X-rays. The absence of distinct diffraction maxima in SAXS profile suggested the lack of periodicity in the structures.61 This was indicative of multivesicular structure of CuMvs consisting of non-concentric bilayers. Also, the power law (q−1) of scattering curve in line collimation mode suggested vesicular structures.61–63 The interpretation of scattering curve in real space was done using General Inverse Fourier Transformation (GIFT) which generated Pair Distance Distribution Function (PDDF), P(r). Fig. 2(b) and (c) show the approximated SAXS scattering data fit with experimental data after carrying out indirect fourier transformation and the corresponding PDDF, respectively. It can be seen that the data fits well with experimental data and the PDDF curve i.e. P(r) vs. r shows asymmetry with alternate signs of distribution function. Since P(r) is calculated by weighting two electron density values connected by distance r, the asymmetry in signs of P(r) points towards inhomogenous interior of CuMVs.
![]() | ||
| Fig. 2 (a) SAXS scattering profile of CuMVs (b) approximated scattering curve (red) after carrying out Indirect Fourier Transformation and (c) the corresponding PDDF. | ||
Initially, a blank experiment was run where the model reaction was performed in the absence of CuMVs. The reaction did not show any progress even after 4 h suggesting the need of catalyst for successful conversion of reactants to product.
In order to optimize the catalyst dose for the reaction, the CuMVs solution was initially assessed for concentration of catalytically active sites (Cu2+) using ICP-MS analysis that suggested it to be 2 ppm. The model reaction was then carried out with different volumes of CuMVs solution. Fig. 3(a) summarizes the time for reaction completion and isolated product yield in each case. An increase in the volume of CuMVs solution led to faster completion of reaction with increased product yield.
The results could be understood in terms of increase in number of catalytically active Cu2+ sites. Increasing the volume of solution ensured more number of CuMVs and hence faster reactions with better yields. The constant results beyond 20 ml of catalyst volume suggest the complete encapsulation of reactants in the CuMVs. Introduction of anymore amount of CuMVs did not affect the reaction rate as there was no further encapsulation of reactants in newly introduced CuMVs. The catalytic reaction was also performed at higher temperatures to understand the effect of temperature on the reaction performance. It was found that increasing the reaction temperature had negligible effect on product yield (Fig. 3(b)). Based on these results, the optimum reaction temperature for the reaction was fixed to be 303 K.
![]() | (1) |
It is to be noted that since the CuMVs were recovered during the process for further usage, mass of CuMVs have been omitted from the E-factor calculations. The values of E-factor have been calculated for synthesis of all the benzimidazole derivatives and are given in Table 1. It can be seen from Table 1 that E-factor values are very small ranging between 0.14 and 0.21 which advocates the green nature of the protocol. This is attributed to minimum waste generation during the process which occurs in water as reaction medium in presence of highly active recyclable CuMVs.
The proposed mechanism for the reaction taking place inside the CuMVs is depicted in Scheme S1 (ESI†). The Cu2+ sites in the CuMVs activate the carbonyl carbon of the aromatic aldehyde for nucleophilic attack by –NH2 group of o-phenylenediamine. The resulting imine is further attacked by second –NH2 to form dihydroimidazole followed by aromatization in presence of air to give 2-aryl-1H-benzimidazoles as product.
![]() | ||
| Fig. 5 (a) FESEM image and (b) optical micrograph of CuMVs recovered after 1st cycle of catalytic reaction. | ||
The recycled CuMVs solution was subjected to further catalytic cycles and the reaction performance was noted in each case. It was found that the CuMVs maintained their catalytic performance for up to 6 reaction cycles (Fig. 6). The performance is attributed to mechanical strength and stability of metallovesicular structures.
The decline in the performance of the catalytic system can be explained on the basis of rupture of metallovesicle structure on repeated use beyond 6th cycle (Fig. S4, ESI†).
| S. no. | Catalyst | Catalyst dose | Time/yield (%) | Solvent/temperature | Ref. |
|---|---|---|---|---|---|
| 1 | VOSO4 | 3 mol% | 1 h/92% | EtOH/rt | 64 |
| 2 | TiCl3OTf | 10 mol% | 50 min/86% | EtOH/rt | 65 |
| 3 | Ce(NO3)3·6H2O | 30 mol% | 1.5–2 h/93% | DMF/80 °C | 66 |
| 4 | PhSiH3 | 4 equivalent | 2 h/95% | DMF/120 °C | 67 |
| 5 | Co(OH)2 | 10 mol% | 4–7 h/82–96% | EtOH/rt | 68 |
| 6 | ClSO3H | 10 mol% | 1.8 h/93% | 2-Propanol/rt | 69 |
| 7 | CuFe2O4 NPs | 20 mol% | 24 h/89% | Toluene/O2 | 51 |
| 8 | Mesoporous TiO2–Fe2O3 | 20 mg | 3 h/97% | H2O/O2 | 52 |
| 9 | Pt/TiO2 | 1 mol% | 1 h/78% | Mesitylene | 53 |
| 10 | Fe3O4–SiO2–(NH4)6Mo7O24 nanocomposite | 220 mg | 0.5 h/90% | EtOH/H2O2 | 54 |
| 11 | α-MoO3 nanobelts | 2 mol% | 0.5 h/93% | t-BuOOH | 55 |
| 12 | CuI Nps | 10 mol% | 1 h/96% | CH3CN/O2 | 56 |
| 13 | CuMVs | 0.03 mol% | 1 h/96% | H2O | Present work |
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c9ta05441c |
| This journal is © The Royal Society of Chemistry 2019 |