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With n-butyl acetate as the organic solvent, product
concentration was increased by 50% when compared
to the reduction in an aqueous reaction system with
the enantiomeric excess reaching >98% (Fig. 2). (S)-
alcohol 2 (4.1mmol) was formed by 1g of biocatalyst
(dry cell weight).
suspension was fed for 20h. Complete conversion of 1
(350mM) was achieved within 24h. The yield of the
reaction and the enantiomeric excess was 91% and
95%, respectively. Compound 1 (5.8mmol) was formed
by 1g of biocatalyst (dry cell weight). This is an
improvement of 41% when compared to the batch reac-
tion. The yield was higher than reported for bioreduc-
tions with recombinant E. coli being 85%, while the
enantiomeric excess did not reach 100%.5
160
140
120
100
80
100
98
96
94
92
90
3. Conclusion
The recombinant yeast P. pastoris is a useful tool for the
stereoselective reduction of b-keto ester 1 to the corre-
sponding (S)-alcohol 2. The decomposition of the sub-
strate and the inhibitory effect on the biocatalyst were
significantly reduced in a two-phase reaction system
containing n-butyl acetate as the organic phase and by
continuously feeding substrate 1 and the biocatalyst.
60
TMBE
hexene
aqueous
ethyl acetate
n-butyl acetate
Figure 2. Effect of the organic solvents on the concentration of 2 and
the enantiomeric excess. The relative concentration of 2 is calculated
relative to the bioreduction in a monophasic aqueous reaction system.
4. Experimental
4.1. Chemicals
Previously published results have demonstrated that
the carbonylreductase is most stable in the presence of
n-butyl acetate when compared to other organic
solvents.10 Furthermore, n-butyl acetate shows good
extraction properties towards 1 and 2.
All chemicals were purchased from VWR/Merck except
yeast nitrogen base (YNB), which was obtained from
Difco.
4.2. Microorganism
The reduction efficiency was further improved by adding
6.5% v/v Triton X100 thus increasing the yield by 60%
compared to the aqueous reaction system. Triton X100
leads to a permeabilization of the cells and therefore
to an increased mass transfer.11 Furthermore, the sur-
factant reduces the equilibrium droplet size of the
n-butyl acetate in water and therefore increases the
interfacial area.
The methylotrophic yeast strain Pichia pastoris GC909
over-expressing the glucose dehydrogenase gene of
Bacillus subtilis and the carbonyl reductase gene of
Candida magnoliae, both under control of the AOX
promoter, was provided by the Consortium fur
¨
Munchen,
¨
Elektrochemische
Germany.
Industrie
GmbH,
Lysis was observed in the presence of n-butyl acetate. In
order to maintain the stability and activity of the biocat-
alyst cell suspension and substrate solved n-butyl acetate
were fed into the reactor.
4.3. Growth conditions
Cells were grown in 1L shaking flasks with 200mL com-
plex media (10g/L yeast extract, 20g/L peptone, 13.4g/L
yeast nitrogen base, 10g/L glycerol, 0.4mg/L biotin,
0.1mol/L potassium phosphate puffer, pH6.0) at 28ꢁC
for three days on a rotary shaker at 250rpm. The expres-
sion of recombinant proteins was induced by adding
methanol (2mL) every 24h for three days. The biomass
was collected by centrifugation.
The feeding rate of the substrate led to an accumulation
of 1 during the first 15h of the process (Fig. 3). The cell
400
300
200
100
0
200
150
100
50
Feed of11
4.4. Bioreductions
For batch reductions, cells were dissolved in 20mL reac-
tion buffer (1M glucose, 0.1M sodium chloride, 0.1M
potassium phosphate buffer, pH7.0 or 0.1mM NADP).
The reaction was started by adding 1 (0.5mL) and
1.5mL of ethyl acetate, n-butyl acetate, tert-butyl
methyl ether (TBME) or hexane, respectively. Flasks
were incubated on a magnetic stirrer at 30ꢁC for 24h.
0
0
6
12
Time [h]
18
24
Figure 3. Concentration of CAAE 1, (R)-CHBE and (S)-CHBE 2 in a
fedbatch reduction. CAAE was fed for 15h and cell suspension for
20h; dotted line: expected course of concentrations.
For fedbatch bioreductions, cells were dissolved in reac-
tion buffer as described above to a final volume of