Mojtaba Amini*a,
Mohammad Mahdi Najafpour*bc,
Hadi Naslhajianad,
Emad Aminib and
S. Morteza F. Farniad
aDepartment of Chemistry, Faculty of Science, University of Maragheh, Golshahr, P.O. Box. 55181-83111731, Maragheh, Iran. E-mail: mamini@maragheh.ac.ir; Tel: +98 935 4171381
bDepartment of Chemistry, Institute for Advanced Studies in Basic Sciences (IASBS), Zanjan, 45137-66731, Iran. E-mail: mmnajafpour@iasbs.ac.ir; Tel: +98 241 415 3201
cCenter of Climate Change and Global Warming, Institute forAdvanced Studies in Basic Sciences (IASBS), Zanjan, 45137-66731, Iran
dDepartment of Chemistry, University of Tehran, Tehran, Iran
First published on 6th February 2014
We for the first time report that nanolayered Mn–Ca oxide in the presence of H2O2 is an efficient catalyst toward sulfide oxidation to sulfoxide. We characterized the catalyst by DLS, UV-Vis, diffuse reflectance infrared Fourier transform spectroscopy, SEM, TEM and HRTEM. We also considered different parameters of the sulfide-oxidation reaction.
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33) in 1 h.4 Asymmetric oxidation of sulfides was also examined by using (salen)Mn(III) complexes as catalyst and was found to show high asymmetric induction.5 Mn oxides are cheap and environmentally friendly compounds and used extensively as bulk, supported, nano-sized with large surface area and colloidal forms. Mn oxides are efficient catalysts for oxidation of both organic6 and inorganic compounds such as carbon monoxide,7 nitrogen oxides,8 and water.9 Recently, we used layered Mn oxides as efficient catalysts for oxidation of water,10 alcohols11 and alkenes.12 Here, we report nanolayered Mn oxides as efficient catalysts toward organic sulfide oxidation to sulfoxide.
XRD data for the compound is of very poor resolution and the weak peak in 2θ ∼11 related (00l) in layered Mn oxides, reveals the absence of long-range order of the layer stacking (Fig. S2, ESI†).13
Using extended-range X-ray absorption spectroscopy (XAS) at the K-edges of both Ca and Mn, two different Ca-containing motifs were identified. One of the motifs was the formation of Mn3CaO4 cubes while the other Ca(II) ions probably interconnected oxide-layer fragments (Fig. 1).14
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| Fig. 1 A motif for Mn–Ca cubic in layered Mn oxide (a). Surface area of layered Mn oxide (Ca(II) ions are omitted for clarification) (b). | ||
SEM images from the catalyst show aggregated nanoparticles from <100 nm. In TEM images, layers of Mn oxide are clearly detected and showed that the nano-compounds observed by SEM contain nanosheets (Fig. 2 and S3, ESI†). Only a few short-range orders among layers can be observed in the sample by HRTEM. Such layered Mn oxides without any long-range order among layers are rare. DLS shows that particles are in the range of 100–200 nm (Fig. S4, ESI†). Comparing with SEM (<100 nm), we found aggregation of particles in solution. Peak at ∼400 nm in solid state UV-Vis spectrum of oxide is related to Mn(III)/Mn(IV) ions in the structure (Fig. S5, ESI†).
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| Fig. 2 SEM micrographs (a), TEM (b) and HRTEM (c and d) images of nano-size Mn–Ca oxide prepared at 400 °C. | ||
In order to understand the effect of catalyst on the catalytic reactivity, the first, MPS oxidation reaction was carried out without catalyst. Results indicated that in the absence of catalyst, trace amount of product was generated in presence of H2O2 as an oxidant. Various oxidants including TBHP, H2O2, NaClO and molecular oxygen were tested for the oxidation of MPS over Ca0.16MnO2·2H2O at room temperature. Among these oxidants, molecular oxygen and H2O2 were much more efficient for the oxidation of MPS. The amount of H2O2 could also significantly affect the conversion and selectivity for MPS oxidation to sulfoxide (selectivity: sulfoxide/(sulfoxide + sulfone) × 100) (Table 1). When the amount of H2O2 was increased from 0.5 to 1.5 mmol, the conversion of MPS increased drastically from 47 to 85%. With a further increasing of H2O2 to 2.0 mmol, the selectivity for MPS oxidation to sulfoxide decreases from 92 to 70%. The conversion of MPS monotonously increases with the addition of catalyst from 5 to 10 mg. When the amount of catalyst is increased to 20 mg, the selectivity for MPS oxidation to sulfoxide reduces from 95 to 70%. Hence, the amount of catalyst can enhance the reaction rate for the selectivity for MPS oxidation to sulfoxide. In the next step, a series of reactions was investigated by performing the model reaction in different solvents such as dichloromethane, methanol, acetonitrile, benzene, acetone and n-hexane. Among the solvents examined, acetonitrile was found to be the best for this protocol (Table 1).
| Entry | Catalyst amount (mg) | Oxidant | Oxidant amount (mmol) | Solvent | Conversiona (%) | Selectivityb (%) |
|---|---|---|---|---|---|---|
| a The GC conversion (%) are measured relative to the starting substrate.b Selectivity to sulfoxide = (sulfoxide/(sulfoxide + sulfone)) × 100. | ||||||
| 1 | — | H2O2 | 0.5 | CH3CN | Trace | — |
| 2 | 20 | H2O2 | 0.5 | CH3CN | 47 | 100 |
| 3 | 20 | TBHP | 0.5 | CH3CN | 45 | 94 |
| 4 | 20 | NaClO | 0.5 | CH3CN | 28 | 100 |
| 5 | 20 | O2 | Bubbled | CH3CN | 97 | 41 |
| 6 | 20 | H2O2 | 1.0 | CH3CN | 63 | 99 |
| 7 | 20 | H2O2 | 1.5 | CH3CN | 85 | 92 |
| 8 | 20 | H2O2 | 2.0 | CH3CN | 88 | 70 |
| 9 | 15 | H2O2 | 1.5 | CH3CN | 83 | 93 |
| 10 | 10 | H2O2 | 1.5 | CH3CN | 83 | 95 |
| 11 | 5 | H2O2 | 1.5 | CH3CN | 62 | 99 |
| 12 | 10 | H2O2 | 1.5 | CH3OH | 75 | 96 |
| 13 | 10 | H2O2 | 1.5 | CH2Cl2 | 21 | 100 |
| 14 | 10 | H2O2 | 1.5 | C6H6 | 29 | 100 |
| 15 | 10 | H2O2 | 1.5 | CH3COCH3 | 33 | 100 |
| 16 | 10 | H2O2 | 1.5 | n-Hexane | 8 | 100 |
A series of various types of structurally diverse sulfides were subjected to the oxidation reaction using Ca0.16MnO2·2H2O as catalyst and H2O2 as oxidant (Table 2). Arylalkyl (Table 2, entries 1 and 2), arylbenzyl (Table 2, entry 3), dibenzyl (Table 2, entry 4), diaryl (Table 2, entry 5) and dialkyl (Table 2, entries 6–8) sulfides underwent clean and the selectivity for MPS oxidation to sulfoxide under air, is high (89–100%). Significantly, the very good conversions of substrates depending on the nature of the sulfide, in the range of 51–100% were obtained for all cases. It was observed that aromatic sulfides undergo oxidation reactions can be oxidized to sulfoxide more easily than aliphatic substrates. These results may indicate that the MnV
O intermediate can efficiently transfer oxygen atom to electron-rich sulfides than electron-poor one. The highest and the lowest conversions were obtained for dibenzyl sulfide (100%) and diethyl sulfide (51%), respectively (Table 2, entries 4 and 6).
| Entry | Substrate | Conversionb (%) | Selectivityc (%) |
|---|---|---|---|
a The molar ratios for substrate : oxidant are 1 : 3. The reactions were performed in CH3CN (1 mL) under air at room temperature within 2 h.b The GC yield (%) are measured relative to the starting sulfide.c Selectivity to sulfoxide = (sulfoxide/(sulfoxide + sulfone)) × 100. |
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| 1 | ![]() |
83 | 95 |
| 2 | ![]() |
85 | 91 |
| 3 | ![]() |
99 | 91 |
| 4 | ![]() |
100 | 89 |
| 5 | ![]() |
68 | 98 |
| 6 | CH3CH2–S–CH2CH3 | 51 | 100 |
| 7 | CH3(CH2)2–S–(CH2)2CH3 | 55 | 100 |
| 8 | CH3(CH2)7–S–(CH2)7CH3 | 52 | 100 |
The recovery and recyclability of Ca0.16MnO2·2H2O have been also examined for the oxidation of MPS at room temperature for 2 h and the results have been shown in Fig. 3. The catalyst was separated after each run by filtration, washed 2–3 times with water and diethyl ether repeatedly, and then dried at 50 °C for half an hour. The catalyst could be recycled five times with no significant loss in activity. During reusability studies fifth run provided ∼79% conversion and 95% selectivity.
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| Fig. 3 Recycling studies of the catalyst Ca0.16MnO2·2H2O in the oxidation of MPS. Condition is similar to Table 2. | ||
In order to investigate catalyst leaching in the oxidation of MPS as a model reaction, the reaction was stopped at half the reaction time (1 h) and the solid catalyst was completely separated from solution. The rest of the reaction mixture (without catalyst) was allowed to stir for another period of half the reaction time. As seen in Fig. 4, no amount of MPS was produced after catalyst separation. After separation of the catalyst, the reaction mixture was analyzed by AAS and no Mn ions were detected. These results show that Ca0.16MnO2·2H2O is truly heterogeneous and catalyst leaching is negligible under these conditions.
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| Fig. 4 Leaching experiment; the blue line shows the reaction without Ca0.16MnO2·2H2O and the red line shows the reaction with Ca0.16MnO2·2H2O. | ||
The probable factors of Mn–Ca oxide for activity toward oxidation reactions are:
• The catalyst has a layered structure with considerable thermodynamic stability.15
• The oxide has high surface area and many of Mn ions are active sites regarding layered structure. In other words, in contrast to other Mn oxides, in layered Mn oxides many Mn ions are on the surface where can act as active sites.
• Both Mn(III)/Mn(IV) ions are stable in the structure that the factor helps to conversion of Mn(III) and Mn(IV) in the catalytic cycle.15
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c4ra00008k |
| This journal is © The Royal Society of Chemistry 2014 |