Kinetic resolution of secondary alcohols with Burkholderia cepacia lipase immobilized on a biodegradable ternary blend polymer matrix as a highly efficient and heterogeneous recyclable biocatalyst

Ganesh V. More, Kirtikumar C. Badgujar and Bhalchandra M. Bhanage*
Institute of Chemical Technology, Department of Chemistry, Matunga, Mumbai-400019, India. E-mail: bm.bhanage@gmail.com; Fax: +91-22-3361-1020; Tel: +91-22-3361-2601

Received 13th November 2014 , Accepted 5th December 2014

First published on 9th December 2014


Abstract

The present work reports a highly efficient and biocatalytic heterogeneous protocol for kinetic resolution (KR) of racemic secondary alcohols with vinyl acetate as an acyl donor, using the biocatalyst Burkholderia cepacia lipase (BCL) immobilized on a biodegradable ternary blend support through polylactic acid (PLA)/polyvinyl alcohol (PVA)/chitosan (CHI); (PLA/PVA/CHI–BCL). The KR reaction with various substituted aromatic, heterocyclic racemic secondary alcohols gave enantiomerically pure alcohol and its enantioenriched acetate derivatives with high conversion (45–50%) and excellent enantiomeric excess (up to 99% ee) at optimized reaction conditions. The reaction works under mild conditions using simple and inexpensive starting materials such as racemic alcohols, vinyl acetate, and immobilized biocatalyst. The given protocol provides excellent recyclability with good yield and enantiomeric excess values up to the studied range of five cycles. The resultant products were characterized with the help of different analytical techniques such as 1H and 13C-NMR, chiral HPLC column, polarimeter, IR and GC-MS.


Introduction

The development of novel greener methodologies are of great interest for synthesis of enantiomerically pure compounds as chiral moieties with a single enantiomer are widely found in several applications such as agrochemicals, pharmaceuticals, flavours, fragrances, fine chemicals and materials for electronics, biosensors and optics.1 Enantiomerically pure secondary alcohols are an important class of chiral building blocks and these are utilized for the synthesis of bio-active compounds and chiral auxiliaries for pharmaceutical intermediates.2 After KR, these enantiopure alcohols can be converted into biologically significant compounds, such as Ezetimibe,3a Prozac,3b Emend3c & Sotalol3d (Fig. 1).
image file: c4ra14478c-f1.tif
Fig. 1 Enantiopure alcohol motifs in bioactive compounds.

From last decades, several strategies were invented for the preparation of enantiopure alcohols such as: (a-i) an asymmetric transfer hydrogenation of ketones using mixture of formic acid–triethylamine, HCO2Na or IPA as a hydrogen source, (a-ii) an organocatalytic reduction of ketones, (a-iii) reduction of ketone using silane as a hydrogen source with metal, (a-iv) and reduction of ketones by using molecular hydrogen,4b oxidative kinetic resolution (OKR) of alcohol,5c selective hydrolysis of epoxides.6 These methodologies gave good yield and enantiomeric excess of compounds, but suffers from several drawbacks such as use of molecular hydrogen that requires high pressure autoclave, low enantiomeric excess, longer reaction time, use of expensive metal precursor, phosphine based ligands, additives, multistep synthesized chiral ligands and no catalyst recovery, which limits their practical catalytic applications. Thus, the synthesis of enantiomerically pure alcohol and its acetate derivative is a challenging task, which can be achieved simply via greener biocatalytic pathway. In biocatalysis enzymes are used as catalysts which possessing advantages such as excellent stereo-, regio- and chemo-selectivities, milder reaction condition, no by-products formation and no need of cofactors.7

In recent years, lipases have been widely used as an eco-friendly biocatalyst for the synthesis of pharmaceutical active intermediates and fine chemicals because of their stability, broad range of substrate scope and easy availability from bacteria and fungi.8 Kinetic resolution of various racemates using lipases is considered to be a greener method for the separation of enantiomers as it works at mild reaction conditions without any harm.9 Kinetic resolution of inexpensive racemic alcohols using lipases is an attractive process for synthesis of expensive optically active alcohol intermediates as compared to hydrogenation of ketones, OKR and hydrolysis of epoxide.10 However, direct use of free enzymes as a biocatalyst for the synthesis of enantiopure molecules suffers from several drawbacks such as lower activity, low selectivity, low yield, no recyclability, lesser stability in organic solvents and denaturation at higher temperature.11 Also enzymes are expensive, and discarding them after one use is not economical, which restricts use of free enzymes for further industrial applications. To overcome theses drawbacks, various immobilization protocols are applied which give benefits such as improved stability, activity, reusability and less reaction time to obtain high yield and enantiopure compounds.12 In literature various reports are present for KR of secondary alcohols but still there is lot of scope to find out new lipases and new immobilization techniques for the synthesis of chiral drug intermediate via KR.10 In 2007, Sheldon et al.13 proposed that immobilized enzyme on biodegradable polymer can serve great application in membrane and bioreactor coating; considering these aspects, use of the polymer matrix for enzyme immobilization is of great interest.

In continuation of our ongoing research on development of new superficial protocol for the KR of secondary alcohols;10b hence we prepared a ternary blend of PLA, PVA and CHI using the Grande et al.14 method and used it for further immobilization of Burkholderia cepacia lipase (PLA/PVA/CHI–BCL, as a composition 1[thin space (1/6-em)]:[thin space (1/6-em)]6[thin space (1/6-em)]:[thin space (1/6-em)]1[thin space (1/6-em)]:[thin space (1/6-em)]2) by our procedure reported earlier.15,16 The prepared immobilized biocatalyst was fully characterized by different techniques such as scanning electron microscopy (SEM) FT-IR and thermo-gravimetric (TGA). In the present study, we report a green and convenient strategy for KR of secondary alcohols catalyzed by PLA/PVA/CHI–BCL as a catalyst and reaction is carried out at 40 °C for 30 h, which afforded optically enriched alcohols (up to 99% ee) and its acetate derivatives (up to 99% ee) with high conversion (Scheme 1).


image file: c4ra14478c-s1.tif
Scheme 1 Kinetic resolution of secondary alcohol.

Result and discussion

Characterization of immobilized PLA/PVA/CHI–BCL

The surface analysis of ternary blend (PLA/PVA/CHI) and immobilized lipase (PLA/PVA/CHI–BCL) was performed by Scanning Electron Microscopy analysis (Fig. 2). The ternary blend PLA/PVA/CHI (1[thin space (1/6-em)]:[thin space (1/6-em)]6[thin space (1/6-em)]:[thin space (1/6-em)]1) showed a plane surface (Fig. 2A), whereas the immobilized lipase PLA/PVA/CHI–BCL (1[thin space (1/6-em)]:[thin space (1/6-em)]6[thin space (1/6-em)]:[thin space (1/6-em)]1[thin space (1/6-em)]:[thin space (1/6-em)]2) showed well dispersed globules on the surface (Fig. 2B). This change in surface morphology indicated that, Burkholderia cepacia lipase was successfully immobilized into the ternary blend, which is responsible for the catalytic activity. Similar type of surface morphology was observed in previous report for the HPMC–PVA film immobilized Rhizopus oryzae lipase.17 The FT-IR spectroscopy is the one of the best technique to study the parent amide functionality present in enzyme due to proteneous nature of enzyme (Fig. 3).
image file: c4ra14478c-f2.tif
Fig. 2 (A) Ternary blend PLA/PVA/CHI (1[thin space (1/6-em)]:[thin space (1/6-em)]6[thin space (1/6-em)]:[thin space (1/6-em)]1), (B) immobilized BCL lipase into ternary blend polymer support PLA/PVA/CHI–BCL (1[thin space (1/6-em)]:[thin space (1/6-em)]6[thin space (1/6-em)]:[thin space (1/6-em)]1[thin space (1/6-em)]:[thin space (1/6-em)]2).

image file: c4ra14478c-f3.tif
Fig. 3 (A) Ternary blend PLA/PVA/CHI (1[thin space (1/6-em)]:[thin space (1/6-em)]6[thin space (1/6-em)]:[thin space (1/6-em)]1), (B) PLA/PVA/CHI–BCL (1[thin space (1/6-em)]:[thin space (1/6-em)]6[thin space (1/6-em)]:[thin space (1/6-em)]1[thin space (1/6-em)]:[thin space (1/6-em)]2) immobilized lipase on ternary blend (C) free Burkholderia cepacia lipase.

In FT-IR analysis the wave number values of ternary blend (PLA/PVA/CHI) are in good agreement with the literature values (Fig. 3A).14 The FT-IR analysis of parent lipase molecules showed three characteristics amide I, II, III bands in between spectral region of 1750–1300 cm−1.15,18,19 In our FT-IR study of free lipase BCL (Fig. 3C), the amide I band was observed at 1600–1750 cm−1 which is a characteristic band of the C–O stretching vibrations. The amide II band was observed at 1500–1600 cm−1 because of N–H bending and C–N stretching vibrations.15,18,19 The amide III band is attributed at 1300–1450 cm−1 owing to, C–C, C–N stretching and N–H bending vibrations. Similar types of bands were existed in the immobilized lipase PLA/PVA/CHI–BCL also (Fig. 3B). Thus, the amide I, II, III bands for the free BCL and ternary blend immobilized PLA/PVA/CHI–BCL (1[thin space (1/6-em)]:[thin space (1/6-em)]6[thin space (1/6-em)]:[thin space (1/6-em)]1[thin space (1/6-em)]:[thin space (1/6-em)]2) lipases were observed in same region, which indicating the existance of the parent amide functionality of enzyme in immobilized biocatalyst (Fig. 3B and C).

Turner and Vulfson20 proposed that temperature around 90–130 °C is required to eliminate the physically adsorbed water molecules while temperature between 200–240 °C is required to eliminate tightly bound water which is present in close vicinity of the enzyme (Fig. 4). Similar type of results has been observed in the present study. Physically adsorbed water molecules seem to be eliminated around 100–110 °C of temperatures, while closely associated water molecules are eliminated at around 240 °C as evident from the TGA curve. Moreover it can be clearly seen that stability of the immobilized lipase (Fig. 4; blue colour line) is considerably improved as compared to free lipase (Fig. 4; black colour line). Similar type of improved stability was observed by Dhake et al.17 for the HPMC–PVA film immobilized Rhizopus oryzae lipase.


image file: c4ra14478c-f4.tif
Fig. 4 Pink colour: ternary blend PLA/PVA/CHI (1[thin space (1/6-em)]:[thin space (1/6-em)]6[thin space (1/6-em)]:[thin space (1/6-em)]1); blue colour PLA/PVA/CHI–BCL (1[thin space (1/6-em)]:[thin space (1/6-em)]6[thin space (1/6-em)]:[thin space (1/6-em)]1[thin space (1/6-em)]:[thin space (1/6-em)]2) immobilized lipase on ternary blend and black colour: free Burkholderia cepacia lipase.

In the present study, a series of experiments were performed to optimize the various reaction parameters such as catalyst screening, effect of solvent, biocatalyst loading, effect of acyl donors, effect of agitation speed, molar ratio, reaction temperature and time; which are summarized in Tables 1 and 2. For screening purpose, we used two enzymes i.e. free BCL and CCL (Candida cylindracea lipase), and their ternary blend immobilized form denoted as PLA/PVA/CHI–BCL and PLA/PVA/CHI–CCL (Table 1, entries 1–4). It was observed that among above four biocatalysts; PLA/PVA/CHI–BCL gave 50% conversion with excellent enantioselectivity towards the (S)-1-phenylethanol (ees) 95% ee and (R)-phenylethyl acetate (eep) 93% ee, in n-hexane as a solvent at 45 °C temperature and hence it was used for further studies (Table 1, entry 1). Subsequently, we studied the effect of the catalyst loading on the conversion and enantioselectivity of the desired products. We screened the catalyst loading ranging from 10 mg to 50 mg (see Table 1, entries 5–9). It was observed that with increase in catalyst concentration from 10 mg to 20 mg increases the enantioselectivity and yield of desired product (Table 1, entry 6). Further increase in the amount of catalyst concentration did not show significant effect on the yield and enantioselectivity of the desired product (Table 1, entries 7–9). A control experiment in the absence of PLA/PVA/CHI–BCL did not show any conversion, thus elucidating that PLA/PVA/CHI–BCL was solely responsible to catalyze the KR of racemic alcohols (Table 1, entry 10).

Table 1 Effect of various enzymes and catalyst loading on the kinetic resolution of racemic 1-phenylethanola
Entry Catalyst Catalyst loading (mg) Conversion (%) % eesb % eepc E
a Reaction conditions: 1-phenylethanol-0.5 mmol, vinyl acetate-2 mmol, n-hexane-2 mL, speed of agitations-150 rpm, temp-45 °C, time-48 h, NR: no reaction.b Determined by chiral HPLC on chiralcel OD-H column.c Determined by chiral HPLC on chiralcel OD-H column.
Biocatalyst screening
1 PLA/PVA/CHI–BCL 20 50 95 93 103
2 Free BCL 4 10 10 95 43
3 PLA/PVA/CHI–CCL 20 30 25 57 5
4 Free CCL 4 17 8 40 3
[thin space (1/6-em)]
Catalyst loading
5 PLA/PVA/CHI–BCL 10 43 68 90 39
6 PLA/PVA/CHI–BCL 20 50 95 93 103
7 PLA/PVA/CHI–BCL 30 50 91 92 76
8 PLA/PVA/CHI–BCL 40 50 93 92 82
9 PLA/PVA/CHI–BCL 50 50 93 94 110
10 PLA/PVA/CHI–BCL NR


Table 2 Effect of reaction parameters on the kinetic resolution of racemic 1-phenylethanola

image file: c4ra14478c-u1.tif

Entry Solvent Acyl donor Temp. (°C) Time (h) Conversion (%) % eesb % eePc E
a Reaction conditions: 1-phenylethanol-0.5 mmol, acyl donor-2 mmol, PLA/PVA/CHI–BCL-20 mg, solvent-2 mL.b Analysis performed by chiral HPLC on chiralcel OD-H column.c Analysis performed by chiral HPLC on chiralcel OD-H column.d SF: solvent free.e Vinyl acetate 1.5 mmol.f Vinyl acetate 2.5 mmol.g Speed of agitation-165 rpm.h Speed of agitations-125 rpm, NR: no reaction, RT: room temperature.
Effect of solvent
1 n-Hexane Vinyl acetate 45 48 50 95 93 103
2 Toluene Vinyl acetate 45 48 42 69 95 81
3 MTBE Vinyl acetate 45 48 50 96 97 >200
4 DCM Vinyl acetate 45 48 49 93 96 168
5 THF Vinyl acetate 45 48 50 97 95 165
6 ACN Vinyl acetate 45 48 49 94 96 175
7 1,4-Dioxane Vinyl acetate 45 48 20 22 88 19
8 Ethyl acetate Vinyl acetate 45 48 50 94 93 98
9 n-Heptane Vinyl acetate 45 48 50 97 93 116
10 SFd Vinyl acetate 45 48 45 78 95 93
[thin space (1/6-em)]
Effect of acyl donor
11 MTBE Ethyl acetate 45 48 15 6 35 2
12 MTBE Acetic anhydride 45 48 34 34 66 7
13 MTBE Acetic acid 45 48 NR Racemic NR
14e MTBE Vinyl acetate 45 48 49 91 95 124
15f MTBE Vinyl acetate 45 48 49 95 97 >200
[thin space (1/6-em)]
Effect of temperature
16 MTBE Vinyl acetate RT 48 35 54 99 >200
17 MTBE Vinyl acetate 40 48 50 98 99 >200
18 MTBE Vinyl acetate 50 48 49 96 96 >200
19g MTBE Vinyl acetate 40 48 49 97 99 >200
20h MTBE Vinyl acetate 40 48 50 96 99 >200
[thin space (1/6-em)]
Effect of time
21 MTBE Vinyl acetate 40 1 6 6 99 >200
22 MTBE Vinyl acetate 40 3 11 12 99 >200
23 MTBE Vinyl acetate 40 5 15 18 99 >200
24 MTBE Vinyl acetate 40 10 30 42 99 >200
25 MTBE Vinyl acetate 40 15 40 66 99 >200
26 MTBE Vinyl acetate 40 24 48 90 99 >200
27 MTBE Vinyl acetate 40 30 50 98 99 >200
28 MTBE Vinyl acetate 40 48 50 98 99 >200


Next, by using PLA/PVA/CHI–BCL as a catalyst, the influence of the solvent on the KR of racemic 1-phenylethanol reaction was investigated (Table 2, entries 1–10). Nonpolar solvents like n-hexane, n-heptane, toluene, methyl tertiary butyl ether (MTBE), dichloromethane (DCM) and polar solvents like tetrahydrofuran (THF), acetonitrile (ACN), ethyl acetate were screened.

It was observed that the nature of solvent marginally affects the conversion and enantioselectivity of the (R)-phenylethyl acetate (eep) and (S)-1-phenylethanol (ees) except 1,4 dioxane. All developed immobilized biocatalyst are stable in various screened solvents (except 1,4 dioxane). Literature survey showed that generally solvent greatly influences the catalytic activity and stability of the lipase enzymes. Present biocatalyst is highly stable and in literature, we rarely find any report which showed such excellent stability and activity of immobilized biocatalyst in various solvents. The activity along with the enantioselectivity was significantly higher in nonpolar solvents such as MTBE gives ees 96% ee and eep 97% ee with 50% conversion (Table 2, entry 3) hence; MTBE was used it for further studies. Also one experiment was carried out in under neat condition (solvent free – SF) which provides the 45% conversion with ees 78% ee and eep 95% ee (Table 2, entry 10). It is well known fact that acyl donor plays a crucial role in prediction of the conversion and enantioselectivity in KR reaction; hence we screened various acyl donors such as vinyl acetate, ethyl acetate, acetic anhydride, acetic acid (Table 2, entries 11–13). Among these acyl donors vinyl acetate gives 50% conversion with ees 96% ee and eep 97% ee (Table 2, entry 3), while in presence of acetic acid no conversion was observed (NR) (Table 2, entry 13). Thus we used vinyl acetate as an acyl donor for further experiments. However molar ratio study is an important aspect hence we studied effect of the molar ratio on conversion and enantioselectivity, the different molar ratio of alcohol: vinyl acetate was screened ranging from (0.5[thin space (1/6-em)]:[thin space (1/6-em)]1.5) to (0.5[thin space (1/6-em)]:[thin space (1/6-em)]2.5). The molar ratio 0.5[thin space (1/6-em)]:[thin space (1/6-em)]2 (alcohol[thin space (1/6-em)]:[thin space (1/6-em)]vinyl acetate) gave better conversion and enantioselectivity (Table 2, entry 3). The decrease in moles of vinyl acetate from 2 to 1.5 showed decreases in the conversion and enantioselectivity (Table 2, entry 14); whereas increase in moles of vinyl acetate from 2 to 2.5 had no significant effect on the conversion as well as enantioselectivity (Table 2, entry 15).

Influence of temperature is an important aspect which greatly affect on the enantioselectivity in chiral chemistry hence we studied the effect of temperature (30–50 °C) on conversion and enantioselectivity of desired products (Table 2, entries 16–18). It was observed that at room temperature, the conversion and enantioselectivity of alcohol (ees) was low, whereas increase in the temperature to 40 °C increases the conversion up to 50% as well as enantioselectivity of ees 98% ee and eep 99% ee. Further increase in the temperature up to 50 °C had no profound effect on conversion but slightly decreases the enantioselectivity of product; therefore further experiments were carried at 40 °C temperature.

Finally, we examined the effect of the reaction time on the reaction yield and enantioselectivity for a given model reaction (Table 2, entries 21–28). After 30 h, maximum conversion and enantioselectivity of desired product was obtained. Thus, the best optimized reaction parameters to obtain the good yield and enantioselectivity for KR of racemic alcohol are as: 1-phenylethanol (0.5 mmol: 1 eq.), vinyl acetate (2 mmol: 4 eq.), PLA/PVA/CHI–BCL (20 mg), and MTBE (2 mL) at 40 °C for 30 h.

Encouraging with these mild and softer optimized reaction conditions, we studied the various racemic secondary alcohols for broaden the scope and general applicability of the developed methodology (Fig. 5). It was observed that all substrate gave higher conversion and excellent enantioselectivity. The model reaction of rac 1-phenylethanol with vinyl acetate under the optimized reaction conditions provides 50% conversion and enantiomeric excess as 1a: 98% ee, 2a: 99% ee. Among the various electron donating (–Me, –OMe) derivatives furnished good yield of corresponding enantiomerically pure alcohols and its acetate derivatives as 1b: 77% ee; 2b: 99% ee and 1c: 99% ee; 2c: 97% ee. Moreover, derivatives bearing halo-substituents (–F, –Cl, –Br) were also provided good yield of corresponding enantiomerically pure alcohols and its acetate derivatives as for 1d: 99% ee; 2d: 99% ee, 1e: 93% ee; 2e: 98% ee, 1f: 83% ee; 2f: 99% ee. It was found that bulky naphthyl-based carbinols providing corresponding enantio-rich alcohol and its acetate derivatives gives 1g: 74% ee, 2g: 98% ee respectively. Next, we also studied heterocyclic derivative which gave enantio-rich alcohol and its acetate derivatives as 1h: 85% ee, 2h: 96% ee respectively. Subsequently, cyclic aromatic derivatives also provided good enantiomeric excess of desired products 1i: 99% ee; 2i: 91% ee and 1j: 99% ee; 2j: 91% ee.


image file: c4ra14478c-f5.tif
Fig. 5 Kinetic resolution of substituted racemic secondary alcohols. Reaction conditions: racemic alcohol (1 mmol), vinyl acetate (4 mmol), MTBE (4 mL), speed of agitation-150 rpm, temperature-40 °C, analysis performed by chiral HPLC on chiralcel OD-H column and chiralcel OJ-H column.

Biocatalyst recyclability

In order to increase feasibility of our biocatalytic protocol, we determined reusability of PLA/PVA/CHI–BCL for KR reaction. It was found that immobilized biocatalyst was used for five consecutive cycles (Fig. 6). There was marginal (1–2% ee) decrease in enantiomeric excess with respect to acetate derivative in all five recycles. Alcohol also showed the good enantiomeric excess in three recycle however; while enantiomeric excess declined up to 75% ee for the fifth cycle. The decrease in enantiomeric excess was believed to be deactivation of lipase due to continuous exposure to alcoholic substrate.17,18
image file: c4ra14478c-f6.tif
Fig. 6 Recyclability study of immobilized lipase.

Conclusions

In this work, we have developed a robust and efficient immobilized PLA/PVA/CHI–BCL catalyst for the synthesis of enantiopure alcohols and its acetate derivative via KR methodology. The protocol showed excellent enantiomeric excess (up to 99% ee) when the reaction was carried out at mild condition such as 40 °C. Obviously, this is a new immobilized biocatalyst which having great competitive advantages such as high thermal stability, low catalyst loading, high enantioselectivity and good conversion of desired products. Catalyst PLA/PVA/CHI–BCL is highly stable in polar and nonpolar solvents with good activity and recyclability (up to 5 cycles). This biodegradable catalyst shows attractive results and has bright future in pharmaceutical science for synthesis of active pharmaceutical ingredients (APIs).

Acknowledgements

G.V.M. is thankful to the Council of Scientific and Industrial Research (CSIR), New Delhi for providing a senior research fellowship. The authors also thank to Department of Science and Technology (DST)-SERB, India (project file no. SR/S1/OC-09-2012) for financial support.

References

  1. (a) Houben-Weyl: Methods of Organic Chemistry, ed. G. Helmchen, R. W. Hoffmann, J. Mulzer and E. Schaumann, Thieme, Stuttgart, 1995, vol. E21 Search PubMed; (b) M. Nogradi, Stereoselective Synthesis, Wiley-VCH, Weinheim, 1995 Search PubMed; (c) FDA's statement for the development of new stereoisomeric drugs, Chirality, 1992, 4, 338–340 Search PubMed; (d) V. Farina, J. T. Reeves, C. H. Senanayake and J. J. Song, Chem. Rev., 2006, 106, 2734–2793 CrossRef CAS PubMed; (e) D. Muñoz Solano, P. Hoyos, M. J. Hernáiz, A. R. Alcántara and J. M. Sánchez-Montero, Bioresour. Technol., 2012, 115, 196–207 CrossRef PubMed.
  2. (a) Chirality in Industry, ed. A. N. Collins, G. N. Sheldrake and J. Crosby, John Wiley & Sons, Chichester, 1992 Search PubMed; (b) G. Wang, X. Liu and G. Zhao, Tetrahedron: Asymmetry, 2005, 16, 1873–1879 CrossRef CAS PubMed; (c) G. V. More and B. M. Bhanage, Eur. J. Org. Chem., 2013, 30, 6900–6906 CrossRef; (d) D. Zhu, C. Mukherjee and L. Hua, Tetrahedron: Asymmetry, 2005, 16, 3275–3278 CrossRef CAS PubMed; (e) I. C. Lennon and J. A. Ramsden, Org. Process Res. Dev., 2005, 9, 110–112 CrossRef CAS; (f) M. Fuchs, D. Koszelewski, K. Tauber, J. Sattler, W. Banko, A. K. Holzer, M. Pickl, W. Kroutil and K. Faber, Tetrahedron, 2012, 68, 7691–7694 CrossRef CAS PubMed; (g) M. Reilly, D. R. Anthony and C. Gallagher, Tetrahedron Lett., 2003, 44, 2927–2930 CrossRef CAS; (h) K. Han, C. Kim, J. Park and M.-J. Kim, J. Org. Chem., 2010, 75, 3105–3108 CrossRef CAS PubMed; (i) T. Ohkuma, H. Doucet, T. Pham, K. Mikami, T. Korenaga, M. Terada and R. Noyori, J. Am. Chem. Soc., 1998, 120, 1086–1087 CrossRef CAS.
  3. (a) B. Bertrand, S. Durassier, S. Frein and A. Burgos, Tetrahedron Lett., 2007, 48, 2123–2125 CrossRef CAS PubMed; (b) D. M. Perrine, N. R. Sabanayagam and K. J. Reynolds, J. Chem. Educ., 1998, 75, 1266 CrossRef CAS; (c) P. J. Vankawala, R. R. C. Elati, N. K. Kolla, S. R. Chamala, S. Gangula, Pub. No. US 2011/0094321 A1, 2011; (d) P. R. Brodfuehrer, P. Smith, J. L. Dillon and P. Vemishetti, Org. Process Res. Dev., 1997, 1, 176–178 CrossRef CAS.
  4. (a) A. Fujii, S. Hashiguchi, N. Uematsu, T. Ikariya and R. Noyori, J. Am. Chem. Soc., 1996, 118, 2521–2522 CrossRef CAS; (b) M. Watanabe, M. Watanabe, K. Murata, K. Murata, T. Ikariya and T. Ikariya, J. Org. Chem., 2002, 67, 1712–1715 CrossRef CAS PubMed; (c) H. Y. Rhyoo, H.-J. Park and Y. K. Chung, Chem. Commun., 2001, 2064–2065 RSC; (d) H. Y. Rhyoo, Y. A. Yoon, H. J. Park and Y. K. Chung, Tetrahedron Lett., 2001, 42, 5045–5048 CrossRef CAS; (e) T. Langer and G. Helmchen, Tetrahedron Lett., 1996, 37, 1381–1384 CrossRef CAS; (f) D. Cuervo, M. P. Gamasa and J. Gimeno, Chem.–Eur. J., 2004, 10, 425–432 CrossRef CAS PubMed; (g) D. R. Li, A. He and J. R. Falck, Org. Lett., 2010, 12, 1756–1759 CrossRef CAS PubMed; (h) T. Inagaki, A. Ito, J. I. Ito and H. Nishiyama, Angew. Chem., Int. Ed., 2010, 49, 9384–9387 CrossRef CAS PubMed; (i) M. Tokunaga, J. F. Larrow, F. Kakiuchi and E. N. Jacobsen, Science, 1997, 277, 936–938 CrossRef CAS; (j) R. Noyori and T. Ohkuma, Angew. Chem., Int. Ed., 2001, 40, 40–73 CrossRef CAS.
  5. (a) J. T. Bagdanoff, E. M. Ferreira and B. M. Stoltz, Org. Lett., 2003, 5, 835–837 CrossRef CAS PubMed; (b) J. T. Bagdanoff and B. M. Stoltz, Angew. Chem., Int. Ed., 2004, 43, 353–357 CrossRef CAS PubMed; (c) S. K. Mandal, D. R. Jensen, J. S. Pugsley and M. S. Sigman, J. Org. Chem., 2003, 68, 4600–4603 CrossRef CAS PubMed.
  6. (a) D. A. Annis and E. N. Jacobsen, J. Am. Chem. Soc., 1999, 121, 4147–4154 CrossRef CAS; (b) E. N. Jacobsen, Acc. Chem. Res., 2000, 33, 421–431 CrossRef CAS PubMed; (c) N. S. E. Schaus, B. D. Brandes, J. F. Larrow, M. Tokunaga, K. B. Hansen, A. E. Gould, M. E. Furrow and E. N. Jacobsen, J. Am. Chem. Soc., 2002, 124, 1307–1315 CrossRef PubMed.
  7. F. Hasan, A. A. Shah and A. Hameed, Enzyme Microb. Technol., 2006, 39, 235–251 CrossRef CAS PubMed.
  8. (a) S. Benjamin and A. Pandey, Yeast, 1998, 14, 1069–1087 CrossRef CAS; (b) K. E. Jaeger and M. T. Reetz, Trends Biotechnol., 1998, 16, 396–403 CrossRef CAS.
  9. (a) J. M. Keith, J. F. Larrow and E. N. Jacobsen, Adv. Synth. Catal., 2001, 343, 5–26 CrossRef CAS; (b) M. Breuer, K. Ditrich, T. Habicher, B. Hauer, M. Keßeler, R. Stürmer and T. Zelinski, Angew. Chem., Int. Ed., 2004, 43, 788–824 CrossRef CAS PubMed; (c) A. Ghanem and H. Y. Aboul-Enein, Chirality, 2005, 17, 1–15 CrossRef CAS PubMed.
  10. (a) R. V. Muralidhar, R. Marchant and P. Nigam, J. Chem. Technol. Biotechnol., 2001, 76, 3–8 CrossRef CAS; (b) N. K. P. Dhake, K. M. Deshmukh, Y. S. Wagh, R. S. Singhal and B. M. Bhanage, J. Mol. Catal. B: Enzym., 2012, 77, 15–23 CrossRef PubMed; (c) G. D. Yadav and S. Devendran, J. Mol. Catal. B: Enzym., 2012, 81, 58–65 CrossRef CAS PubMed; (d) L. Borén, B. Martín-Matute, Y. Xu, A. Córdova and J.-E. Bäckvall, Chem.–Eur. J., 2006, 12, 225–232 CrossRef PubMed; (e) B. S. Chen and U. Hanefeld, J. Mol. Catal. B: Enzym., 2013, 85–86, 239–242 CrossRef CAS PubMed; (f) E. A. Manoel, K. C. Pais, M. C. Flores, L. S. D. M. E Miranda, M. A. Z. Coelho, A. B. C. Simas, D. M. G. Freire and R. O. M. A. De Souza, J. Mol. Catal. B: Enzym., 2013, 87, 139–143 CrossRef CAS PubMed; (g) Micro review: J. H. Lee, K. Han, M. Kim and J. Park, Eur. J. Org. Chem., 2010, 999–1015 CrossRef CAS; (h) L. H. Andradea, L. P. Rebeloa, C. G. C. M. Netto and H. E. Toma, J. Mol. Catal. B: Enzym., 2010, 66, 55–62 CrossRef PubMed.
  11. (a) M. T. Reetz, Curr. Opin. Chem. Biol., 2002, 6, 145–150 CrossRef CAS; (b) C. Mateo, J. M. Palomo, G. Fernandez-Lorente, J. M. Guisan and R. Fernandez-Lafuente, Enzyme Microb. Technol., 2007, 40, 1451–1463 CrossRef CAS PubMed.
  12. (a) X. Liu, Y. Guan, R. Shen and H. Liu, J. Chromatogr. B: Anal. Technol. Biomed. Life Sci., 2005, 822, 91–97 CrossRef CAS PubMed; (b) X. Wenlei and M. Ning, Energy Fuels, 2009, 23, 1347–1353 CrossRef; (c) J. C. Santos, P. D. Mijone, G. F. M. Nunes, V. H. Perez and H. F. de Castro, Colloids Surf., B, 2008, 61, 229–236 CrossRef CAS PubMed; (d) P. Adlercreutz, Chem. Soc. Rev., 2013, 42, 6406–6436 RSC.
  13. R. A. Sheldon, Adv. Synth. Catal., 2007, 349, 1289–1307 CrossRef CAS.
  14. R. Grande and A. J. F. Carvalho, Biomacromolecules, 2011, 12, 907–914 CrossRef CAS PubMed.
  15. K. C. Badgujar, K. P. Dhake and B. M. Bhanage, Process Biochem., 2013, 48, 1335–1347 CrossRef CAS PubMed.
  16. K. C. Badgujar and B. M. Bhanage, Enzyme Microb. Technol., 2014, 57, 16–25 CrossRef CAS PubMed.
  17. K. P. Dhake, P. J. Tambade, Z. S. Qureshi, R. S. Singhal and B. M. Bhanage, ACS Catal., 2011, 1, 316–322 CrossRef CAS.
  18. K. C. Badgujar, K. P. Dhake and B. M. Bhanage, Process Biochem., 2013, 49, 1304–1313 CrossRef PubMed.
  19. K. Ramani, R. Boopathy, C. Vidya, L. John Kennedy, M. Velan and G. Sekaran, Process Biochem., 2010, 45, 986–992 CrossRef CAS PubMed.
  20. N. A. Turner and E. N. Vulfson, Enzyme Microb. Technol., 2000, 27, 108–113 CrossRef CAS.

Footnote

Electronic supplementary information (ESI) available: General experimental procedure, copies of the 1H and 13C NMR spectra and the chiral HPLC chromatograms of the products. See DOI: 10.1039/c4ra14478c

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