Open Access Article
      
        
          
            Lynda J. 
            Brown
          
        
      *, 
      
        
          
            Richard C. D. 
            Brown
          
        
       and 
      
        
          
            Robert 
            Raja
          
        
      
      
School of Chemistry, University of Southampton, Highfield, Southampton, SO17 1BJ, UK. E-mail: ljb2@soton.ac.uk;  Fax: +44-(0)23-8059-5919;   Tel: +44-(0)23-8059-6757
    
First published on 29th November 2012
The synthesis of the first mesoporous silica (150 Å) anchored carbohydrate-derived chiral ketone is described. This new heterogeneous catalyst has been shown to be effective in the asymmetric epoxidation of olefins by oxone. The heterogeneous ketone catalyst has comparable activity to that of its homogeneous counterpart and returned enantioselectivities up to 90% e.e.
Asymmetric alkene epoxidation is one of the most useful synthetic transformations in the preparation of chiral building blocks for the synthesis of biologically active molecules.6 Non racemic chiral ketones, which generate chiral dioxiranes in situ in the presence of an oxidising agent such as oxone, have been well documented to effectively promote asymmetric epoxidations.7 Early reports from the Shi group described fructose-derived ketone 1a as a successful epoxidation catalyst for trans 1,2-disubstituted and trisubstituted olefins (Fig. 1).8 Subsequent studies from the same group showed that oxazolidinone-bearing ketone (catalyst 1b) catalysed the epoxidation of a wide range of olefins with high enantioselectivities9 and the lactam ketone 1c could be utilised to epoxidise a variety of 1,1-disubstituted terminal olefins using oxone as the oxidant, giving up to 88% e.e.10 However, it is known that these chiral ketones can undergo undesired Baeyer–Villiger side reactions leading to their inactivation, necessitating relatively high catalyst loadings (typically 20–30 mol%).11
It was envisaged that heterogenisation of optically pure chiral ketones 1b within the interior of mesoporous silicas would afford asymmetric epoxidation catalysts with the potential benefits of ease of product separation, and catalyst recovery. Additionally, the environment within the pore structure could influence the reactivity and selectivity of the heterogeneous catalyst (Fig. 2). Indeed, Armstrong et al. showed that immobilisation of an α-fluorotropinone on silica gave a material with comparable catalytic efficiency and selectivity to the homogeneous system.12
Herein we describe the first successful application of a novel heterogeneous system based on an oxazolidinone catalyst to the asymmetric oxidation of a range of conjugated olefins to their corresponding epoxides in high yields and selectivities.
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| Fig. 2 Representation of heterogeneous epoxidation | ||
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| Scheme 1 Synthesis of chiral ketone catalyst-linker conjugate 5. | ||
In order to prepare the supported catalyst, dry calcined (T = 550 °C) mesoporous silica was first reacted with dichlorodiphenylsilane with the objective to preferentially cap the more accessible Si–OH functionality following a method previously described for capping external sites (Scheme 2).16,17 This left the surface of the inner walls of the mesoporous silicas free for catalyst attachment, thus confining the ketone predominately within its interior pores. With the intent of securing the catalyst to the internal siloxyl functionality of the support, the silica was then reacted with 3-mercaptopropyl trimethoxysilane to provide thiol functionalisation ready for radical mediated addition to the olefin moiety of the ketone 5.
Refluxing the thiol modified silica 9 in a CHCl3 solution of catalyst 5 and AIBN in the dark completed the heterogenisation of the ketone catalyst.12 Elemental analysis of both silicas 9a and 10a showed clear incorporation of the thiol, and from nitrogen analysis of 10a the loading of the catalyst was estimated to be 0.20 mmol g−1 (entries 3 and 4, Table 1). IR spectroscopy confirmed the presence of the ketone (vCO 1770 cm−1).
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| Scheme 2 Derivatisation of mesoporous silica. | ||
| Elemental analysis by combustion (%) | ||||||||
|---|---|---|---|---|---|---|---|---|
| Entry | Catalyst sample | S BET/m2 g−1 | Pore volumea/mL g−1 | C | H | N | S | Loadingb/mmol g−1 | 
| a Total pore volume was measured at P/Po = 0.410. b Loading based on N%. | ||||||||
| 1 | SG-150 Å silica | 263 | 0.156 | — | — | — | — | — | 
| 2 | 8a | 266 | 0.158 | — | — | — | — | — | 
| 3 | 9a | 262 | 0.152 | 1.97 | 1.19 | <0.10 | 2.78 | — | 
| 4 | 10a | 210 | 0.122 | 8.39 | 1.53 | 0.29 | 2.05 | 0.20 | 
Confirmation of the immobilisation of the ketone catalyst within the pores of the supports, not just on the more accessible outer surface sites, came from nitrogen adsorption isotherms. Firstly, there was a clear drop in BET surface area from 263 m2 g−1 for the underivatised mesoporous silica (entry 1, Table 1) to 210 m2 g−1 after heterogenisation of the catalyst (entry 4, Table 1). The total pore volume showed no decrease after capping, when the linker was attached there was a small decrease in volume, however when the catalyst was attached there was a large decrease from 0.152 mL g−1 to 0.122 mL g−1. These data provide strong evidence for the anchoring of the ketone catalyst within the pores of the support.
Evidence to support covalent functionalisation of the mesoporous framework was provided by solid-state NMR spectroscopy; 29Si CP-MAS (cross-polarized magic angle spinning) NMR spectra of the silica 8a showed three signals: Q2 signals (−92 ppm) derived from a low level of silandiol groups (Si(OH)2), Q4 signals (−102 ppm) from the siloxanes (Si(OSi)4) and stronger Q3 signals (−111 pm) from the silanol groups (Si–OH) (Fig. 3). The presence of Si environments due to the capping was below the detection levels of the experiment. The 29Si NMR spectrum of silica 9a containing the mercaptopropyl linker showed a decreased relative intensity of the Q3 signal compared to silica 8a and Q2 almost disappeared, providing a clear indication that the 3-mercaptopropyl trimethoxysilane reacted with the available Si–OH groups. The presence of three new resonances in the 29Si NMR spectrum of 9a (−47 ppm T1, (RSi(OSi)–(OH)2), −57 ppm T2, (RSi(OSi)2–(OH)), −67 ppm, T3, (RSi(OSi)3)) further confirmed the incorporation of organic silanes on the silica surface.
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| Fig. 3 29Si CP-MAS NMR of (a) silica 8a (b) silica 9a. | ||
Fig. 4 shows the 13C CP-MAS NMR spectrum of 9a, with three resonances (27.9, 22.8, 10.6 ppm) corresponding to the CH2SH, CH2 and CH2Si methylene carbons of the propyl linker respectively. Oxidation of surface thiol groups to disulfides may occur in air under ambient conditions, however, the chemical shift data are consistent with the presence of thiol functionality rather than disulfides or higher sulfur oxidation states. The 29Si CP-MAS NMR spectra for the heterogeneous catalyst 10a did not display any new signals as anticipated, whereas the 13C NMR showed characteristic signals for the immobilised catalyst consistent with the presence of aromatic, C–O and aliphatic carbon signals. The ketone carbon signal was too weak to be observed due to its high anisotropic environment and splitting between a centre band and spinning sidebands under experimental conditions. However, the presence of the chiral ketone was strongly supported by IR spectroscopy and the ability of the modified silica to mediate the asymmetric epoxidation of olefins.
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| Fig. 4 13C CP-MAS NMR of (a) silica 9a (b) catalyst 10a. | ||
To enable us to probe the influence of pore size and application of the capping protocol upon the reactivity and selectivity of the heterogeneous chiral ketone catalysts, two uncapped silica supported catalysts 11a,b were also prepared from KG-60 Å and KG-150 Å (Scheme 2).‡ The epoxidation of the chromene 12 was selected as a test reaction and the four heterogeneous catalysts, 10a, 10b, 11a and 11b were evaluated under these conditions. Our preliminary results (Table 2, entries 1–4) were obtained with low catalyst loadings (typically 2.5 mol%). Interestingly, a substantial drop in e.e. was observed for the epoxidations conducted in the presence of the heterogenised catalysts prepared without capping (entries 2 and 4, Table 2) relative to the capped catalysts (entries 1 and 3, Table 2). These results indicate that capping the more accessible Si–OH functionalities is a significant factor in gaining high enantioselectivities in this system, which could be due to confinement of the catalyst within the pores of the silica. It was possible that without capping there was a separate, unselective background epoxidation reaction occuring.17
| Entry | Catalyst | Pore size | Capping | conv (%) | e.e. (%) | TON | 
|---|---|---|---|---|---|---|
| a Catalyst (2.5 mol%), oxone (2.7 equiv.), K2CO3 (10.5 equiv.), 0 °C to rt, 24 h. b Catalyst (20 mol%), oxone (2.7 equiv.), K2CO3 (10.5 equiv.), 0 °C to rt, 6 h. c Catalyst (25 mol%), oxone (2.7 equiv.), K2CO3 (10.5 equiv.), 0 °C to rt, 24 h. | ||||||
| 1 | 10a | 150 | ✓ | 23a | 65 | 9.2 | 
| 2 | 11a | 150 | x | 20a | 32 | 8 | 
| 3 | 10b | 60 | ✓ | 16a | 69 | 6.4 | 
| 4 | 11b | 60 | x | 8a | 32 | 3.2 | 
| 5 | 10a | 150 | ✓ | 96b | 88 | 4.8 | 
| 6 | 5 | — | — | 80c | 93 | 3.2 | 
Our results indicated that the KG-150 Å (10a) gave better conversions which may be due to enhanced site isolation of the catalyst molecules within this larger polymeric framework. Subsequent optimisation showed that using the KG-150 Å mesoporous silica with the more accessible sites capped (catalyst 10a) with loadings of 20 mol% (Table 2 entry 5) gave excellent conversions in reasonable timescales and therefore all ensuing reactions were performed under these conditions. Comparing the heterogeneous catalyst 10a to its homogeneous counterpart 5 (Table 2, entries 5 and 6) showed that the heterogeneous ketone gave improved conversion, with only a modest drop in e.e. This conversion required 20 mol% of the heterogeneous catalyst and was almost complete within 6 h, whereas but the homogeneous catalyst used 25 mol% and had not reached completion after 24 h. This was reflected in the improved turnover number (TON = moles of product/moles of catalyst). The conversion of trans-stilbene by heterogeneous epoxidation was also comparable to that attained by the homogeneous equivalent, again with a small drop in enantioselectivity (homogeneous 74%, 93% e.e.; heterogeneous 70%, 86% e.e.).
The heterogeneous catalyst 10a was employed in the epoxidation of a range of olefins and the conversions and e.e. were measured (Table 3). In all cases the epoxidation reactions were very efficient giving high conversions and good isolated yields. A major advantage of the heterogeneous catalyst was the ease of purification. Unlike its homogeneous equivalent which required separation from the product by chromatography, the supported catalyst was removed by simple filtration. The TON in all reactions ranged from 3.5 to 5.0 indicating that the heterogeneous catalyst was as effective as its homogeneous equivalent. The addition of the oxone was performed as described by Shi involving the simultaneous and separate addition of aqueous oxone and aqueous K2CO3 at 0 °C to buffer the effect of KHSO4 and ensure that a mildly basic pH was maintained through the reaction.18 With slower addition times, the e.e. values were typically higher whilst retaining good conversions. trans-Stilbene gave a slightly lower conversion than expected, which was attributed to its insolubility in the mixed aqueous/organic solvent medium.
| Entry | Substrate | Add. time (h)c | Conv.(%)d | Yielde [Sel]f(%) | e.e.g (%) | Configj | 
|---|---|---|---|---|---|---|
                  a Typical procedure: olefin (0.2 mmol), silica supported ketone catalyst 10a (200 mg, 0.04 mmol, 20 mol%, based on a calculated loading of 0.20 mmol g−1), K2CO3 (0.84 M in aq. Na2EDTA (4 × 10−4 M), 2.52 mL, 2.11 mmol, 10.5 equiv.), oxone (0.212 M in aq. Na2EDTA (4 x 10−4 M), 2.52 mL, (0.53 mmol, 2.7 equiv.), Bu4NHSO4 (0.0015 mmol) in DME : DMM (3 : 1, v/v, 3.0 mL) and K2CO3–AcOH buffer (0.1 M, pH 9.3, 2.0 mL) at 0 °C.
                  b Olefin (0.1 mmol), silica supported ketone catalyst 10a (100 mg, 0.02 mmol, 20 mol%, based on a calculated loading of 0.20 mmol g−1), NaHCO3 (3.1 mmol, 30 equiv.), oxone (1.0 mmol, 10 equiv.), in DME : DMM (3 : 1, v/v, 1.5 mL) and Na2EDTA buffer (4 × 10−4 M, 1.0 mL) at 0 °C.
                  c Time allowed for complete simultaneous addition of the K2CO3 and oxone.
                  d The conversions were determined by 1H NMR.
                  e Yields of isolated products.
                  f (Yield/conv.) × 100.
                  g Enantioselectivites were determined by chiral HPLC using a Chiralcel ODH or a Chiralcel OBH column.
                  h Total reaction time 24 h.
                  i Product isolated as a mixture of epoxide (54%) and diol (46%).
                  j The absolute configurations were determined by comparing HPLC retention times and orders of elution with reported values.
                  k The absolute configuration was not determined.
                 | 
              ||||||
| 1a | 
                   
                 | 
                6h | 100 | 79 [79]i | 90 | (1S,2R)20 | 
| 2b | 
                   
                 | 
                3.5h | 70 | 63 [90] | 86 | (R,R)21 | 
| 3a | 
                   
                 | 
                6 | 96 | 93 [97] | 88 | (3R,4R)22 | 
| 4a | 
                   
                 | 
                6 | 93 | 82 [88] | 80 | (3R,4R)22 | 
| 5a | 
                   
                 | 
                6 | 75 | 65 [86] | 79 | (3R,4R)23 | 
| 6a | 
                   
                 | 
                6 | 93 | 80 [86] | 83 | (3R,4R)22 | 
| 7a | 
                   
                 | 
                6 | 90 | 77 [86] | 81 | (3R,4R)20 | 
| 8a | 
                   
                 | 
                4 | 100 | 75 [75] | 68 | (1R,2S)24 | 
| 9a | 
                   
                 | 
                6 | 100 | 83 [83] | 18 | —k | 
The choice of epoxidation conditions has been noted to be substrate dependant11 and a modified procedure where oxone and NaHCO3 were added as solids proved advantageous raising the conversion to 70%.
The Shi catalysts are well documented to undergo an undesirable Baeyer–Villiger side reaction resulting in their deactivation, thereby impeding a high number of catalytic cycles. Therefore the recyclability of the heterogeneous catalyst 10a was investigated by the epoxidation of the chromene substrate 12. It was observed that after two cycles there was only a minor reduction in catalytic ability and enantioselectivity. However, by the third cycle a significant drop in conversion was noted and a small drop in enantioselectivity due to the increased significance of the background reaction (racemic epoxidation by oxone alone) which becomes more apparent at lower conversions.19
:
hexane mixtures monitored by UV detection at 220 or 254 nm. Elemental analyses were performed at Medac Ltd, Chobham Business Centre, Surrey, UK. BET-Nitrogen asorption isotherms were obtained with a Gemini 2375 volumetric gas adsorption apparatus (micromeritics) at 77 K.
        
:
CH2Cl2. The combined solids were dried in vacuo to give the title compound as an off white solid (2.58 g, 8.35 mmol, 50%). IR νmax(neat)/cm−1 3345 (s), 1616 (m); 1H NMR (DMSO-d6, 300 MHz): δ 6.89 (d, J = 7.9 Hz, 2H), 6.55 (d, J = 7.9 Hz, 2H), 5.69–5.93 (m, 1H), 5.47 (s, 1H), 5.01 (d, J = 17.2 Hz, 1H), 4.94 (d, J = 9.1 Hz, 2H), 4.24–4.56 (m, 3H), 3.84 (d, J = 12.1 Hz, 1H), 3.71–3.22 (m, 5H), 3.05–2.93 (m, 1H), 2.50 (t, J = 7.1 Hz, 2H), 2.32–2.18 (m, 2H); 13C NMR (DMSO-d6, 75 MHz): δ 147.2, 138.4, 128.6, 128.5, 114.9, 112.3, 98.1, 70.0, 69.2, 68.7, 63.3, 49.6, 35.6, 33.8; LRMS (ESI+) m/z 310.2 ([M+H]+).
        
:
CH2Cl2 to give the title compound as a clear oil (383 mg, 1.10 mmol, 100%). IR νmax(neat)/cm−1 3393 (s), 2985 (m), 2932 (m), 1616 (m); 1H NMR (CDCl3, 300 MHz): δ 7.04 (d, J = 8.4 Hz, 2H), 6.73 (d, J = 8.4 Hz, 2H), 5.86 (ddt, J = 17.0, 10.3, 6.4 Hz, 1H), 5.11–4.92 (m, 2H), 4.33–4.10 (m, 3H), 4.01 (d, J = 13.0 Hz, 2H), 3.55–3.70 (m, 2H), 3.23 (d, J = 13.0 Hz, 1H), 2.56–2.69 (m, 2H), 2.25–2.39 (m, 2H), 1.57 (s, 3H), 1.40 (s, 3H); 13C NMR (CDCl3, 75 MHz): δ 145.9, 138.3, 132.9, 129.2, 114.7, 109.3, 96.3, 77.4, 73.6, 72.1, 59.5, 50.5, 35.8, 34.4, 28.1, 26.1; LRMS (ESI+) m/z 350.2 ([M+H]+), 332.2 ([M–OH]+).
        
:
hexane gave the title oxazolidinone as a pale yellow foam (702 mg, 1.87 mmol, 82%). IR νmax(neat)/cm−1 3395 (w), 2985 (w), 2935 (w), 1754 (s), 1518 (m); 1H NMR (CDCl3, 300 MHz): δ 7.40 (d, J = 8.8 Hz, 2H), 7.17 (d, J = 8.8 Hz, 2H), 5.83 (ddt, J = 17.0, 10.3, 6.4 Hz, 1H), 5.08–4.94 (m, 2H), 4.38–4.24 (m, 4H), 4.18–4.10 (m, 1H), 3.85–3.74 (m, 2H), 3.05 (d, J = 7.7 Hz, 1H), 2.74–2.63 (m, 2H), 2.40–2.29 (m, 2H), 1.57 (s, 3H), 1.39 (s, 3H); 13C NMR (CDCl3, 75 MHz): δ 153.0, 138.1, 137.7, 135.3, 129.0, 118.6, 115.1, 109.8, 100.8, 76.4, 73.1, 71.4, 61.7, 53.0, 35.4, 34.6, 28.0, 26.0; LRMS (ESI+) m/z 396.2 ([M+H]+).
        
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hexane the resultant off white foam was recrystallised from hot Et2O to give the title ketone as a white solid (168 mg, 0.45 mmol, 85%). IR νmax(neat)/cm−1 1755 (s), 1518 (m); 1H NMR (CDCl3, 400 MHz): δ 7.43 (d, J = 8.5 Hz, 2H), 7.21 (d, J = 8.5 Hz, 2H), 5.83 (ddt, J = 16.9, 10.3, 6.5 Hz, 1H), 5.08–4.93 (m, 2H), 4.87 (d, J = 5.5 Hz, 1H), 4.75 (d, J = 10.3 Hz, 1H), 4.57–4.68 (m, 2H), 4.27 (d, J = 13.6 Hz, 1H), 3.76 (d, J = 10.3 Hz, 1H), 2.75–2.63 (m, 2H), 2.36 (q, J = 7.2 Hz, 2H), 1.49 (s, 3H), 1.44 (s, 3H); 13C NMR (CDCl3, 100 MHz): δ 195.0, 151.2, 138.7, 137.7, 134.8, 129.3, 118.7, 115.1, 111.1, 99.1, 77.5, 75.5, 60.9, 49.8, 35.3, 34.6, 27.0, 25.9; LRMS (EI+) m/z 398 ([M+Na]+).
        1-(But-3-en-1-yl)-4-nitrobenzene (14.5 g, ca. 75.6 mol) was dissolved in EtOH (300 mL), SnCl2·2H2O (85.0 g, 0.38 mol, 5.0 equiv.) was added and the reaction allowed to stir for 2 days. The reaction was poured onto water (250 mL) and the pH raised to 9 with 1 M NaOH, the cloudy mixture was extracted with EtOAc (x 3), Rochelle's salt was added to aid separation. Combined organics were washed with brine and dried (MgSO4) and concentrated in vacuo to a brown oil which was purified by silica gel column chromatography eluting with 25 to 30% EtOAc
:
hexane gave a the title para-isomer as a pale oil (6.40 g, 43.5 mmol, 58%) and the undesired ortho-isomer as a pale oil (2.10 g, 14.30 mmol, 19%). Data consistent with reported values27 IR νmax(neat)/cm−1 1640 (m), 1515 (s), 1342 (s); 1H NMR (CDCl3, 400 MHz): δ 7.01 (d, J = 8.0 Hz, 2H), 6.65 (d, J = 8.0 Hz, 2H), 5.88 (ddt, J = 16.9, 10.3, 6.7 Hz, 1H), 5.11–4.93 (m, 2H), 3.50 (br s, 2H), 2.68–2.55 (m, 2H), 2.35 (q, J = 7.2 Hz, 2H); 13C NMR (CDCl3, 101 MHz): δ 144.2, 138.4, 132.0, 129.1, 115.2, 114.6, 35.8, 34.5; LRMS (ESI+) m/z 464.2 ([3M+Na]+).
:
DMM (3
:
1, v/v, 3.0 mL) were stirred at room temperature for 5 min and then cooled to 0 °C. K2CO3–AcOH buffer (0.1 M in aq. Na2EDTA (4 × 10−4 M), pH 9.3, 2.0 mL) was added and the mixture stirred for a further 10 min at 0 °C. K2CO3 (0.84 M in aq. Na2EDTA (4 × 10−4 M), 2.52 mL, 2.11 mmol, 10.5 equiv.) and oxone (0.212 M in aq. Na2EDTA (4 × 10−4 M), 2.52 mL, 0.53 mmol, 2.7 equiv.) were then added simultaneously through separate syringes using a syringe pump. Addition times and final reaction times were as denoted in Table 3. The reaction was then diluted with Et2O (20 mL) and water (20 mL), and extracted further with Et2O (20 mL, ×2). Combined organics were washed with brine, dried (MgSO4) and concentered in vacuo and then purified by silica gel column chromatography using the eluents described below.
        
:
pentane. White solid (yield 43% epoxide; 36% diol, e.e. 90%). Chiral HPLC: Chiralcel OBH column, eluent 1% IPA
:
hexane, UV 254 nm, flowrate: 1.0 mL min−1 (peak 1 15.59 min, 95.16%; peak 2 19.63 min, 4.84%).
        
:
hexane. Pale yellow oil (yield 63%, e.e. 86%). Chiral HPLC: Chiralcel ODH column, eluent 2% IPA
:
hexane, UV 254 nm, flowrate: 1.0 mL min−1 (peak 1 8.05 min, 6.90%; peak 2 8.77 min, 93.10%).
        
:
hexane. White solid (yield 93%, e.e. 88%). Chiral HPLC: Chiralcel ODH column, eluent 10% IPA
:
hexane, UV 220 nm, flowrate: 1.0 mL min−1 (peak 1 10.96 min, 94.01%; peak 2 13.31 min, 5.94%).
        
:
hexane. Off white solid (yield 82%, e.e. 80%). Chiral HPLC: Chiralcel ODH column, eluent 10% IPA
:
hexane, UV 220 nm, flowrate: 1.0 mL min−1 (peak 1 5.62 min, 89.91%; peak 2 6.34 min, 10.09%).
        
:
hexane. White solid (yield 65%, e.e. 79%). Chiral HPLC: Chiralcel ODH column, eluent 10% IPA
:
hexane, UV 220 nm, flowrate: 1.0 mL min−1 (peak 1 5.36 min, 89.25%; peak 2 5.83 min, 10.75%).
        
:
hexane. Pale yellow oil (yield 80%, e.e. 83%). Chiral HPLC: Chiralcel ODH column, eluent 10% IPA
:
hexane, UV 220 nm, flowrate: 1.0 mL min−1 (peak 1 5.41 min, 87.79%; peak 2 6.15 min, 8.29%).
        
:
hexane. Pale yellow oil (yield 77%, e.e. 81%). Chiral HPLC: Chiralcel ODH column, eluent 10% IPA
:
hexane, UV 220 nm, flowrate: 1.0 mL min−1 (peak 1 5.28 min, 90.65%; peak 2 5.95 min, 9.35%).
        
:
hexane. Pale yellow oil (yield 75%, e.e. 68%). Chiral HPLC: Chiralcel OBH column, eluent 0.5% IPA
:
hexane, UV 220 nm, flowrate: 1.0 mL min−1 (peak 1 20.63 min, 16.06%; peak 2 32.18 min, 83.94%).
        
:
pentane. Colourless oil (yield 83%, e.e. 18%). Chiral HPLC: Chiralcel ODH column, eluent 1% IPA
:
hexane, UV 220 nm, flowrate: 1.0 mL min−1 (peak 1 6.45 min, 59.18%; peak 2 6.98 min, 40.82%).
        Footnotes | 
| † Electronic supplementary information (ESI) available: 1H and 13C NMR of compounds 2–7, 1H NMR and HPLC of epoxides and 13C and 29Si CP-MAS NMR of silicas 8a–10a. See DOI: 10.1039/c2ra21837b | 
| ‡ KG-60 Å: particle size 70-230 mesh; 63-200 μm; pore size 0.8 cm3 g−1; pore volume 60 Å; surface area 500 m2 g−1; pH 6.0-7.5 (10% in H2O); bp 2230 °C; mp 1600 °C. KG-150 Å: particle size 100-200 mesh; 75-150 μm; pore size 1.15 cm3 g−1; pore volume 150 Å; surface area 300 m2 g−1; pH 7.0 (5% in slurry); bp 2230 °C; mp 1600 °C. | 
| § The silica was turned slowly in a round bottom flask attached to a rotary evaporator (without vacuum). | 
| This journal is © The Royal Society of Chemistry 2013 |