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The substrate of choice was rac-3, due to (a) the interest
of the corresponding (R)-diol 3d for the synthesis of var-
ious b3-adrenergic receptor agonists;2 (b) its low E value
(and therefore the moderate biohydrolysis rate differ-
ence between the two enantiomers); and (c) its reasona-
ble enzymatic activity. Obviously, one important
parameter for implementation of such a process is the
determination of the maximum substrate concentration
usable. We have shown previously, that when using
the A. niger EH, in certain cases, a substrate concentra-
tion as high as 500g/L could be used.13 Exploration of
this possibility was therefore conducted by increasing
the concentration of rac-3 upto 200mM (34.5g/L).
Our exploratory results indicated that contrary to our
previous results, a concentration limitation appeared
at a value higher than 75mM of substrate. Due to pre-
vious experiences, we felt that this limitation could be
due to product inhibition. We therefore tested this
hypothesis by conducting several experiments (at 2mM
substrate concentration), adding various concentrations
of the (formed) (R)-3 diol enantiomer at the start of the
biohydrolysis. The results shown in Figure 2 clearly indi-
cate that this concentration limitation was indeed due to
product inhibition. They also indicate that a 75mM
(11.6g/L) substrate concentration (which corresponds
to a concentration of about 13g/L of formed diol) was
a reasonable compromise for further elaboration of an
enzymatic reactor.
sponded to an overall concentration of about 10g/L of
substrate. The mixture was then vigorously stirred (mag-
netic stirrer). In order to further minimise any spontane-
ous hydrolysis of the substrate and favour enzyme
stability, the process was conducted at 20°C (instead
of 28°C as used for the analytic experiments). Due to
low solubility of 3 in water, this was done at the start
of a biphasic system. However, the solution became
homogeneous as the reaction proceeded, since the diol
formed is totally soluble in water at that concentration.
The reaction was followed by HPLC analysis, showing
that total conversion occurred after a 1.5h reaction time
for this first run. The aqueous (homogeneous) solution
was filtered through an ultrafiltration membrane, which
allowed us to recover the enzyme (as a concentrated
solution). This was re-used to perform the next biohy-
drolysis run on another 340mg substrate sample, using
the same reactor and experimental conditions. Nine
runs were thus performed successively, using the same
enzyme, which corresponds to a biohydrolysis of a total
of 3g (19.4mmol) of rac-3. The nine aqueous solutions
containing the product 3d were pooled and extracted
(ethyl acetate). This afforded 3.5g of 3d (100% analytical
yield), which were purified by bulb-to-bulb distillation.
A total amount of 3g of pure 3d (waxy solid) was
thus obtained, which corresponds to an 88% prepara-
tive yield. As expected, the ee of the thus obtained
22
D
(R)-3d was excellent (97%) {½a ¼ À23:4 (c 1.55,
26
EtOH); lit.15 for (S)-3d ½a ¼ þ21:1 (c 1.31, EtOH),
D
ee=91%}.
100.00
90.00
80.00
70.00
60.00
50.00
40.00
30.00
20.00
10.00
0.00
3. Conclusion
Herein we have reported the biohydrolysis of the substi-
tuted styrene oxide derivatives 1–4 catalysed by the S.
tuberosum epoxide hydrolase, overexpressed in an
appropriate E. coli strain. We observed that each one
of the two enantiomers of these substrates were attacked
by this enzyme with a different and complementary regio-
selectivity. Thus, the (S)-enantiomers were preferably
attacked at the benzylic position, whereas the (R)-
enantiomers were mostly attacked at the terminal
carbon atom. As a consequence, this led to a so-called
enantioconvergent process. Based on this very interest-
ing property, we were able to perform the preparative
scale biohydrolysis of 3g (19.4mmol) of rac-3 in a re-
peated batch reactor, which was run over nine cycles
using the same enzyme sample. The corresponding diol
(R)-3d was thus obtained with an excellent yield (100%
analytic, 88% preparative), in nearly enantiopure form
(ee 97%). This illustrates the highly interesting potential
offered by the enantio-dependent regioselectivity of this
enzyme, which allows to efficiently overcome the 50%
yield limitation theoretically linked to any resolution
process. It should be stressed that this biohydrolysis
was performed using plain water instead of a buffer solu-
tion, thus affording a so-called salt-free process. More-
over, it should also be emphasized that, the best of
our knowledge such an enantio- and regio-complemen-
tary behaviour has never been described for a metal-
based catalysed hydrolytic kinetic resolution of an epox-
ide. Work is currently in progress in our laboratory in
0
200 400 600 800 1000 1200 1400
time (min)
Figure 2. Influence of the initial (R)-3 diol concentration on the
biohydrolysis rate. [(R)-3 diol]: j=0mM; m=75mM (13g/L);
d=100mM (17.2g/L); r=200mM (34.5g/L).
2.5. Preparative scale biohydrolysis of rac-3 using a
repeated batch reactor
Owing to the above described results, we decided to run
a preparative scale repeated batch reactor, using the
most appropriate experimental conditions for the biohy-
drolysis of rac-3. Thus, 340mg of rac-3 dissolved in
300lL of DMSO were placed in a 100mL reactor, to-
gether with 22mL of plain water. The StEH was added
(960U)à,14 as an aqueous solution (10mL, containing
10% of glycerol for enzyme stabilisation), which corre-
à This enzymatic activity was measured against styrene oxide, using the
same methodology as the one we have described previously for the A.
niger EH.14