Open Access Article
Rong-Hui Wuab,
Jing Wua,
Ming-Xin Yua and
Long-Guan Zhu
*a
aDepartment of Chemistry, Zhejiang University, Hangzhou 310027, People's Republic of China. E-mail: chezlg@zju.edu.cn
bKey Laboratory of Chemical Utilization of Forestry Biomass of Zhejiang Province, Zhejiang A & F University, Lin'an, Zhejiang Province 311300, China
First published on 14th September 2017
A newly developed and structurally characterized titanium complex [Ti(Phen)(OC2H5)2Cl2] (Phen = 1,10-phenanthroline) is reported as a homogeneous pre-catalyst for the selective oxidation of organic sulfides to sulfoxides with a stoichiometric amount of 30% aq. H2O2 in CH3OH at room temperature. This catalytic system showed high yield (95–100%) and good selectivity (92–100%) during the catalytic reaction in a short period of time.
For the oxidation of sulfides to sulfones, a very wide variety of oxidizing reagents and catalysts have been investigated. Oxidants such as organic peracids, inorganic oxides, oxygen and hydrogen peroxide have been used for the oxidation of sulfides to sulfoxides.4 Among these oxidants, hydrogen peroxide has been widely used since it is readily available, non-toxic and cheap, and forms water as the sole by-product.5 But in the absence of catalyst, the oxidation of sulfides to sulfoxides employing aqueous hydrogen peroxide is very slow, especially at room temperature. Accordingly, aqueous hydrogen peroxide as the terminal oxidant and a Lewis acid as an activator have been developed to promote this transformation.
Over the past few decades, some transition-metal catalysts such as vanadium,6 iron,7 manganese8 and titanium have been diffusely used to catalyze the selective oxidation of sulfides to sulfoxides in the presence of hydrogen peroxide. Among these catalytic systems, titanium complexes have proved themselves as very successful catalysts to activate hydrogen peroxide in sulfoxide syntheses, due to their cheapness and low toxicity, inertness to redox processes, as well as high activity and selectivity even using equimolecular amounts of H2O2.9 Thus, titanium complexes with different ligands have been used as catalysts to promote oxidation reaction of organic sulphides. Kagan10 and Modena11 have initially reported highly enantioselective sulfoxidation by using titanium–tartrate complexes modified with H2O and tartrate as the catalyst. Then, various titanium complexes with different types of ligands such as diol,12 binol,13 salen14 have been used for this type of oxidation. It is noticeable that many of the reported examples of titanium mediated sulfoxidation reactions were performed under “Ligand Assisted Catalysis (LAC)” conditions in situ generation of the catalyst in the reaction mixture. Consequently, a few of structurally characterized titanium complexes15 have been developed for the sulfoxidation reaction in recent years.
Herein, we present a mononuclear titanium(IV) complex Ti(Phen)(OC2H5)2Cl2 (1), and describe its synthesis, characterization, and as an effective homogeneous pre-catalyst for the selective oxidation of sulfides at ambient temperature in a short period of time.
. The ORTEP diagram of the pre-catalyst shows distorted octahedral geometry (Fig. 1) with two chlorine groups occupying the apical positions and the 1,10-phenanthroline N atoms and two ethoxy group O atoms in the equatorial sites.
To further study the purity and repeatability of the crystals, PXRD experiments were carried out for complex 1. The PXRD experimental and computer simulated patterns of the corresponding complex are shown in ESI data (Fig. S1 and S2, ESI†). They showed that the synthesized bulk materials and the measured single crystals are same. The thermal gravimetric analyses (TGA) of complex 1 were carried out at the rate of 10 °C min−1 under an inert (N2) atmosphere (Fig. 2). The TGA curve of complex 1 shows a gradual weight-loss step of 22.96% in the temperature range of 25–155 °C, corresponding to the escape of two oxyethyl groups from the framework (calcd 23.14%). By further increasing the temperature, a successive decomposition step occurs and the framework of complex 1 was destroyed. Other characterization data and spectra can be found in ESI data.†
Our interest in oxidation inspired us to use this complex as a catalyst for sulfide oxidation. In order to achieve optimum conditions, we performed a set of preliminary experiments on methyl phenyl sulfide (MPS) as a model substrate using 30% aqueous hydrogen peroxide in the presence of a catalytic amount of complex 1 at room temperature. The reaction was initially carried out in several solvents (Table 1, entries 1–7) using 0.0025 mmol of pre-catalyst. Interestingly, both methanol and ethanol are found to be highly effective as the solvents, affording high selectivity and conversion in the presence of the pre-catalyst (Table 1, entries 2–3). We also performed the oxidation of several other sulfides in methanol and ethanol maintaining the same conditions (Table S1, ESI†). The results showed methanol was better than ethanol in the oxidation of the other sulfides and therefore, methanol was chosen as solvent in the following experiments. The attention was then turned on to the stoichiometric ratios for the oxidizing agent. 1 eq. of H2O2 was found most useful for maximum conversion of the substrates. A higher amount of an oxidizing agent led to sulfone formation (Fig. S3, ESI†). Furthermore, we carried out the oxidation with different amount of the pre-catalyst under the same conditions (Table 1, entries 2 and 8–11). As the pre-catalyst amount increased from 1 × 10−4 mmol to 2.5 × 10−3 mmol, the conversion and selectivity of the probe reaction increased from 6% to 99% and 54% to 98%, respectively. A further increase in the pre-catalyst amount led to an insignificant effect on the yield of the desired product. Moreover, in a control experiment conducted in the absence of the pre-catalyst, very little conversion of methyl phenyl sulfide to sulfoxide or sulfone was observed under analogous conditions (Table 1, entry 12). Further screening with 0.0025 mmol of Ti(OPi)4 was also carried out, but none of them provided the product in a yield as high as that obtained in the presence of complex 1 (Table 1, entries 13–14). Lastly, the stability and reuse of the pre-catalyst was investigated by adding to the reaction mixture new charges of substrate and oxidant in a ratio of 1
:
1. Interestingly, the pre-catalyst was reused for up to 8 cycles without significant loss in its activity and selectivity (Fig. S4, ESI†). Thus, complex 1 plays a crucial role in facilitating the partial oxidation reactions.
| Entry | Solvent | Catalyst (amount of catalyst) | Conv.b (%) | Sele.c (%) | |
|---|---|---|---|---|---|
| Sulfoxide | Sulfone | ||||
| a Reaction conditions: 1.00 mmol of methyl phenyl sulfide, 1.00 mmol of 30% H2O2, 1 × 10−2 to 1 × 10−4 mmol Ti catalyst, in the special solvent (5 mL) at 25 °C (20 min). Products were quantified by GC analysis and characterized by the standard substance.b The GC yields (%) are measured relative to the starting sulphide.c Selectivity to sulfoxide = (sulfoxide/(sulfoxide + sulfone)) × 100. | |||||
| 1 | Water | Complex 1 (2.5 × 10−3 mmol) | 100 | 80 | 20 |
| 2 | Methanol | 99 | 98 | 2 | |
| 3 | Ethanol | 99 | 98 | 2 | |
| 4 | Acetonitrile | 23 | 89 | 11 | |
| 5 | Acetone | 14 | 82 | 18 | |
| 6 | Tetrahydrofuran | 28 | 82 | 18 | |
| 7 | Dichloromethane | 11 | 95 | 5 | |
| 8 | Methanol | Complex 1 (1 × 10−4 mmol) | 6 | 54 | 46 |
| 9 | Methanol | Complex 1 (1 × 10−3 mmol) | 53 | 96 | 4 |
| 10 | Methanol | Complex 1 (5 × 10−3 mmol) | 99 | 97 | 3 |
| 11 | Methanol | Complex 1 (1 × 10−2 mmol) | 99 | 96 | 4 |
| 12 | Methanol | — | 8 | 81 | 19 |
| 13 | Methanol | Ti(OPi)4 (2.5 × 10−3 mmol) | 33 | 88 | 12 |
| 14 | Methanol | Ti(OPi)4 (2.5 × 10−3 mmol + 2.5 × 10−3 mmol phen) | 37 | 87 | 13 |
To study the scope of this procedure, a series of structurally diverse sulfides with different electronic and steric effects were then examined under the optimized reaction conditions. The reactions went on well affording high yields (95–99%) and excellent sulfoxide selectivity (92–100%) under the optimum conditions. The results are presented in Table 2. As it can be seen aliphatic sulfides undergo oxidation reactions more easily than aromatic substrates. It is notable that sulfides were chemoselectively oxidized in the presence of some oxidation prone functional groups such as C
C and –OH (Table 2, entries 3 and 5). However, the oxidation of aryl sulfides containing electron-withdrawing groups (Table 2, entries 5–8) was sluggish producing the corresponding sulfoxides, which may be due to the presence of electron-withdrawing groups reduces the electron density on the sulfur atom thereby decreasing its nucleophilicity. Regarding sulfoxidation of benzyl phenyl sulfide, diphenylsulfide and dibenzothiophene, due to their large steric hindrance, a drastic decrease of the catalytic activity is observed with excellent selectivity to the sulfoxides (Table 2, entries 9–11). Quite significantly, catalytic activity of diphenylsulfide is greatly inferior to that of benzyl phenyl sulfide, which is probably due to the influence of conjugation effect.
| Entry | Substrate | Time | Conv.b (%) | Sele.b,c (%) | TOFd | |
|---|---|---|---|---|---|---|
| Sulfoxide | Sulfone | |||||
a Reaction conditions: sulfide : 30% H2O2 : catalyst = 1 : 1 : 0.0025 mmol; methanol: 5 mL, 25 °C.b Conversion and selectivity were determined by GC.c Products were characterized by GC-MS.d TOF (product mol × catalyst mol−1 × h−1). |
||||||
| 1 | ![]() |
15 min | 97 | 99 | 1 | 1544 |
| 2 | ![]() |
15 min | 100 | 99 | 1 | 1598 |
| 3 | ![]() |
15 min | 98 | 98 | 2 | 1574 |
| 4 | ![]() |
20 min | 99 | 98 | 2 | 1182 |
| 5 | ![]() |
50 min | 96 | 99 | 1 | 459 |
| 6 | ![]() |
65 min | 99 | 97 | 3 | 364 |
| 7 | ![]() |
30 min | 98 | 98 | 2 | 787 |
| 8 | ![]() |
145 min | 98 | 95 | 5 | 163 |
| 9 | ![]() |
360 min | 98 | 92 | 8 | 65 |
| 10 | ![]() |
45 min | 98 | 96 | 4 | 524 |
| 11 | ![]() |
24 h | 95 | 100 | 0 | 12 |
In order to obtain more insight on the nature of titanium-based oxidant species, the thianthrene 5-oxide was used as a mechanistic probe for the sulfoxidation reactions (Table 3, entries 1–2). The results show that thianthrene 5-oxide was predominantly oxidized at the sulfide for complex 1/H2O2 catalytic system. Meanwhile, complex 1/H2O2 shows higher activity than Ti(OPi)4/H2O2 under same conditions. We also performed the competitive experiment by putting together p-chlorophenyl methyl sulfide and methyl phenyl sulfoxide one against the other to compete for the titanium complex (Table 3, entries 3–4). A much higher oxidative reactivity of p-ClC6H4SCH3 was observed for complex 1/H2O2 catalytic system, which is in accordance with the competition experiment on thianthrene 5-oxide.
| Entry | Substrate | Catalyst | Conversion (%) | Product distribution (%) | |||
|---|---|---|---|---|---|---|---|
| (i) | (ii) | (1) | (2) | (3) | |||
a Reaction conditions: sulfides or sulfoxides : 30% H2O2 : catalyst = 1 : 1 : 0.0025 mmol; methanol: 5 mL, 25 °C.b Products was determined by HPLC and reaction equation is described as follows. c Products was determined by GC and reaction equation is described as follows. ![]() |
|||||||
| 1b | ![]() |
Ti(OPi)4 | 7 | 90 | 10 | — | |
| 2 | Complex 1 | 11 | 94 | 6 | — | ||
| 3c | ![]() |
Ti(OPi)4 | 47 | 7 | 79 | 7 | 14 |
| 4 | Complex 1 | 92 | 4 | 93 | 3 | 4 | |
The active species in this system is still unknown. However, the generally accepted mechanism for titanium-based oxidation pre-catalysts involves the formation of titanium-based active intermediate species, Ti-hydroperoxo or Ti-peroxo species in the oxygen transfer process.16 It is largely accepted that in the H2O2 activation by titanium complexes, the active species originates from exchange of the alkoxy group by the oxidant.15a,b,17 According to these above results and analysis, a plausible mechanism for the oxidation of sulfides over the pre-catalyst is proposed in Scheme 1.
:
titanium(IV) chloride (110 μL, 1 mmol) was slowly added to a previously prepared ethanol solution (10 mL) containing 1,10-phenanthroline (0.198 g, 1 mmol). Then the resulting solution was allowed to slowly evaporate at room temperature and about two days later colourless block-shaped single crystals were obtained. Yield: 57.0%. Elem. anal. calcd for the synthesized compound 1: C, 42.17%; H, 4.6%; N, 7.20%. Found: C, 42.55%; H, 4.5%; N, 6.98%. UV-Vis [λmax; nm (ε; L cm−1 mol−1) in methanol; Fig. S5, ESI†]: 230 (57
420), 263 (35
100). IR (KBr pellet, cm−1; Fig. S6, ESI†): 3336(s), 2928(m), 1654(w), 1626(w), 1582(w), 1519(m), 1424(s), 1222(w), 1136(w), 1118(w), 1104(s), 1065(s), 921(m), 870(m), 845(s), 735(m), 724(s), 646(m), 602(m), 429(m). 1H NMR [DMSO-d6, 25 °C, 400 MHz; δ (ppm)] (Fig. S7, ESI†): 9.25 (d, J = 6.3 Hz, 2H), 8.89 (d, J = 8.2 Hz, 2H), 8.25 (s, 2H), 8.08 (dd, J = 8.2, 4.7 Hz, 2H), 3.44 (q, J = 7.0 Hz, 4H), 1.05 (t, J = 7.0 Hz, 6H). 13C NMR [DMSO-d6, 25 °C, 126 MHz, δ (ppm)] (Fig. S8, ESI†): 148.25, 140.54, 139.45, 129.32, 127.34, 125.13, 55.96, 18.44.
Thianthrene 5-oxide: a soln of MCPBA (878 mg, 5.08 mmol) in CH2Cl2 (15 mL) was added to a stirred solution of thianthrene (1.0 g, 4.62 mmol) in CH2Cl2 (15 mL) cooled in an ice bath under N2. After 1 h, the mixture was extracted with sat. aq. NaHCO3 (3 × 15 mL). The organic layer was washed with H2O (2 × 25 mL), then dried (MgSO4) and concentrated under vacuum. The sample was then chromatographed on silica gel utilizing petroleum ether/ethyl acetate (6
:
1) as eluent to give thianthrene oxide in a good yield. 1H NMR [CDCl3-d6, 25 °C, 500 MHz; δ (ppm)]: 7.93 (d, J = 7.8 Hz, 2H), 7.63 (d, J = 7.7 Hz, 2H), 7.56 (t, J = 7.6 Hz, 2H), 7.43 (t, J = 7.5 Hz, 2H).
Footnote |
| † Electronic supplementary information (ESI) available: CCDC 1554126. For ESI and crystallographic data in CIF or other electronic format see DOI: 10.1039/c7ra06883b |
| This journal is © The Royal Society of Chemistry 2017 |