Aparna M. Kulkarnia, 
Uday V. Desai*a, 
Kapil S. Pandita, 
Makarand A. Kulkarnia and 
Prakash P. Wadgaonkarb
aDepartment of Chemistry, Shivaji University, Kolhapur-416004, India. E-mail: uvdchem2011@gmail.com;  Fax: +91-0231-2609333
bPolymer Science and Engineering Division, CSIR, National Chemical Laboratory, Pune-411008, India
First published on 23rd July 2014
Nickel ferrite nanoparticles–hydrogen peroxide has been demonstrated for the first time as a green and efficient catalyst-oxidant combination in the chemoselective oxidation of thiols to disulfides and sulfides to sulfoxides. This magnetically separable catalyst was found to be reusable for five consecutive runs without appreciable change in the activity, as well as composition of the catalyst. The mechanism for the oxidation of thiols and sulfides has also been proposed.
In recent years, magnetic nanoparticles (MNPs), owing to their easy separation by application of an external magnetic field, have emerged as a useful class of heterogeneous catalysts.24,25 In particular, iron oxide-based nanoparticles such as magnetite (Fe3O4) and maghemite (γ-Fe2O3) have been previously explored as catalysts, as well as catalyst support in a few organic transformations.26,27 Among other oxides, spinel ferrites (MFe2O4; M = Ni, Zn, Mn or Co) have received a great deal of attention due to their applications as catalyst support, in magnetic drug delivery, magnetic high-density storage, etc.28–31 Among spinel ferrites, nickel ferrite (NiFe2O4) with an inverse spinel structure is an important soft magnetic material with remarkable thermal stability, large magnetic anisotropy and moderate saturation magnetization. A literature survey revealed that very little attention has been paid toward its catalytic potential in organic transformations. With these observations in mind and our continued interest in the development of eco-benign synthetic methodologies,32 we planned to explore the catalytic potential of nickel ferrite-nanoparticles in a few oxidative transformations, beginning with the studies on the oxidation of thiols, as well as sulfides using hydrogen peroxide as a green and commercially available oxidant (Scheme 1).
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| Scheme 1 Nickel ferrite catalyzed oxidation of (a) thiols to disulfides and (b) sulfides to sulfoxides. | ||
Our plan on the use of spinel ferrites in the oxidation of thiols as well as sulfides is based upon the concept that the catalytic properties of AB2O4-type spinel ferrites strongly depend on the nature of A and B ions, their charge, as well as their distribution among the octahedral Oh and tetrahedral Td sites.33 Reithwisch and Dumesic, during their studies on a number of spinel structures have shown that in inverse and mixed spinel structures, there exists a rapid electron exchange between M2+ and M3+ ions.34 Simultaneously, it is also well known that Fe2+ ions during oxidation with H2O2 to Fe3+ ions, generate HO radical and OH− ion.35,36 Based on these facts, we summarised that the nickel ferrite nanoparticles–hydrogen peroxide combination would serve as a useful catalyst-oxidant combination in the oxidation of thiols, as well as sulfides. It was postulated that nickel ferrite on reaction with hydrogen peroxide would generate OH radical, which would subsequently react with thiol to furnish thiol radicals, and dimerization of thiol radicals would furnish disulfide (Scheme 2A). In addition, if this concept proves true, the planned protocol can be safely extended towards oxidation of sulfides to sulfoxides (Scheme 2B).
The powder XRD pattern for nickel ferrite is shown in Fig. 1a. The peaks in the XRD pattern were indexed in light of the natural spinel structure of MgAl2O4. According to the spinel structure, the planes that diffract X-rays are (220), (311), (400), (422), (511) and (440). All of the detectable peaks are indexed as NiFe2O4 with an inverse spinel structure and are in good agreement with the standard data (44-1485 IC DD; JCPDS).37a The absence of extra lines in the present pattern confirms the single-phase formation of nickel ferrite. To corroborate the formation of NiFe2O4 as single phase, using the structural data reported by Kremenovic et al. for the cubic phase,37d theoretical XRD patterns of NiFe2O4 were simulated (Fig. 1c) and were compared with the experimentally observed XRD pattern of the NiFe2O4 nanoparticles prepared in this study. It reveals that the simulated XRD pattern of the NiFe2O4 is in good agreement with the powder XRD patterns of the NiFe2O4 collected before and after the catalytic applications (Fig. 1a and b). The lattice parameter calculated using the XRD data was found to be 8.325 Å and was in good agreement with the value reported for the uncoated ferrite.37b,c The crystallite size of the sample was calculated from the corrected FWHM value of (311) reflection using Scherrer's equation and was found to be ∼20 nm. The SEM image of the catalyst (Fig. 2) indicates the presence of nickel ferrite nanoparticles in aggregated form. Thus, no assertion could be made about the exact morphology of the particles. Hence, the catalyst was further analysed using TEM analysis. The TEM image (Fig. 3) shows cubic morphology of the nanoparticles of size ranging between 14 and 20 nm. The particle size estimated from the TEM image is in good agreement with that predicted using XRD data. Fig. 4 shows the hysteresis loop of the sample. A very narrow hysteresis cycle with a saturation magnetization value of 41.10 emu g−1 indicates the ferrimagnetic behavior of the catalyst, which allows easy separation of the catalyst using an external magnet for possible reuse.
After adequate characterization of the catalyst, we initially planned to explore the catalytic potential of nickel ferrite in the oxidation of thiols. To begin with, 4-bromothiophenol 1a was selected as a model substrate, nickel ferrite nanoparticles as a catalyst and H2O2 as an oxidant (Scheme 1a). A set of reactions were carried out employing different catalysts, as well as an oxidant concentration in different solvents. The results summarized in Table 1 reveal that complete oxidation of 1a to corresponding disulfide 2a takes place in extremely short time with the use of 15 mol% of the catalyst, 2.5 equivalent of 30% H2O2 and acetonitrile as the solvent (entry 8, Table 1). On the other hand, in absence of the catalyst or oxidant, the reaction does not proceed to completion (entry 15 &16 Table 1). Under the established reaction conditions, the oxidation of 1a was also carried out using simple ferrite (Fe3O4), as well as copper ferrite as catalysts (entries 13 and 14, Table 1). Both these catalysts were found to be effective; however, the oxidation was quite slow and considerably less amount of disulfide 2a was obtained.
| No. | Catalyst (mol%) | H2O2 (equiv.) | Solvent | Time (min) | Yielda (%) | 
|---|---|---|---|---|---|
| a Reaction conditions: 4-bromothiophenol (1 equiv.), catalyst (NiFe2O4), solvent, H2O2, RT.b Using Fe3O4 as catalyst.c Using CuFe2O4 as catalyst. | |||||
| 1 | 25 | 5 | CH3CN | 5 | 98 | 
| 2 | 20 | 5 | CH3CN | 5 | 98 | 
| 3 | 15 | 5 | CH3CN | 5 | 96 | 
| 4 | 10 | 5 | CH3CN | 5, 15 | 90, 92 | 
| 5 | 5 | 5 | CH3CN | 20 | 80 | 
| 6 | 15 | 4 | CH3CN | 5 | 96 | 
| 7 | 15 | 3 | CH3CN | 5 | 96 | 
| 8 | 15 | 2.5 | CH3CN | 5 | 96 | 
| 9 | 15 | 2 | CH3CN | 15 | 85 | 
| 10 | 15 | 1.5 | CH3CN | 30 | 60 | 
| 11 | 15 | 2.5 | THF | 30 | 50 | 
| 12 | 15 | 2.5 | CH2Cl2 | 5 | 90 | 
| 13 | 20b | 2.5 | CH3CN | 40 | 80 | 
| 14 | 20c | 2.5 | CH3CN | 40 | 85 | 
| 15 | — | 2.5 | CH3CN | 120 | 20 | 
| 16 | 15 | — | CH3CN | 120 | 30 | 
Based upon this experimental data, nickel ferrite nanoparticles were selected as the catalyst to examine the generality of the reaction conditions, as well as scope of the protocol. Accordingly, a few representative aromatic, as well as aliphatic thiols were subjected to oxidation under the optimized reaction conditions. In each case, corresponding disulfide, 2b–j, were obtained in excellent yield, with high purity in a very short time (Table 2).
Encouraged with this initial success on the oxidation of thiols to disulfides, we then turned our attention towards the oxidation of sulfides to sulfoxides (Scheme 2B). Accordingly, thioanisole, 3a, was chosen as the substrate, and it was observed that under the reaction conditions established for the oxidation of thiols, the oxidation of thioanisole proceeds smoothly to furnish corresponding sulfoxide as the only product (TLC), but it requires slightly longer time (2 h). Most interestingly, either upon the use of an excess amount of oxidant or upon stirring the reaction mixture overnight, we did not notice the formation of sulfone as an over-oxidation product (TLC, Table 3, entry a). Hence, without the modification of the reaction conditions, we planned to examine the scope of the developed protocol. Initially, thioethers bearing electron-donating as well as electron-withdrawing groups on aromatic rings were subjected to oxidation under the established reaction conditions. In each case, corresponding sulfoxide was obtained in excellent yield (Table 3, entries 4a–f). Thus, to check the functional group compatibility in this oxidative transformation, thioethers containing alcohol, nitrile, aldehyde, ketone, and ester groups, as well as an unsaturation centre were then subjected to oxidation. In all cases, corresponding sulfoxides were obtained in excellent yield (4g–o, Table 3), and no side products or over-oxidation products were observed.
| Entry | Product | Time (h) | Yieldb (%) | 
|---|---|---|---|
| a Reaction conditions: sulfide (2 mmol), catalyst (15 mol%, 0.07 g), acetonitrile (5 mL), H2O2 (2.5 equiv., 30%, 0.6 mL), RT.b Yields refer to pure isolated products.c In absence of oxidant.d Using 5.0 equiv. (1.2 mL) 30% H2O2. | |||
| a | ![]()  | 
2.0 | 90 | 
| 24 | 90 | ||
| 6.0 | NRc | ||
| 2.0 | 92d | ||
| b | ![]()  | 
2.0 | 87 | 
| c | ![]()  | 
2.5 | 90 | 
| d | ![]()  | 
3.5 | 88 | 
| e | ![]()  | 
1.5 | 90 | 
| f | ![]()  | 
3.5 | 85 | 
| g | ![]()  | 
2.0 | 84 | 
| h | ![]()  | 
2.5 | 85 | 
| i | ![]()  | 
3.0 | 90 | 
| j | ![]()  | 
3.0 | 87 | 
| k | ![]()  | 
2.0 | 85 | 
| l | ![]()  | 
2.5 | 87 | 
| m | ![]()  | 
3.5 | 90 | 
| n | ![]()  | 
2.0 | 92 | 
| o | ![]()  | 
2.5 | 88 | 
Heterogeneously catalyzed reactions generally offer an advantage of the possibility of catalyst reuse. Hence, upon completion of the model reaction, the catalyst was separated by the application of an external magnet (Fig. 5). The recovered catalyst was washed with acetone, dried in oven at 80 °C for 3 hours and reused for the next run. It was observed that the catalyst could be recycled efficiently for five cycles without appreciable loss in its activity (Fig. 6). So as to check the stability of the catalyst during recycling, the SEM and XRD spectra of the catalyst recovered after fifth cycle were recorded (Fig. 1b and 2b). Comparison of the SEM images and XRD pattern reveals that although the morphology of the catalyst does not change appreciably (Fig. 2a and b), as evidenced from the increased peak width in the XRD pattern (Fig. 1a and b), the grain size of the particles obtained after use decreased.38 Lately, the leaching behavior of the catalyst was tested. Thus, upon completion of the model reaction, the catalyst was separated and the resultant organo-aqueous phase was examined for the presence of Fe as well as Ni by performing spot tests, as well as through AAS analysis. In both the cases, the results obtained were negative. Hence, the composition of the catalyst before and after use was then confirmed from the EDAX spectra (Fig. 7). To our delight, we did not observe any appreciable change in the composition of the catalyst.
:
5%, v/v) furnished pure disulfide, 2 (or sulfoxide, 4) in excellent yields.
All the synthesized compounds are known. However, they were characterised by NMR spectroscopy. For original NMR spectra of sulfoxides, please see the ESI.†
Footnote | 
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c4ra04095c | 
| This journal is © The Royal Society of Chemistry 2014 |