5
6
L. Chaput et al. / Journal of Molecular Catalysis B: Enzymatic 84 (2012) 55–61
Resolution of three different secondary alcohols with three dif-
ferent acyl donors by lipase-catalyzed transesterification with
C. antarctica and Pseudomonas cepacia lipases were performed.
Results demonstrated that the enantioselectivity of lipases was
maximized by using acyl donor and alcohol substrates which
matched well. The hypothesis of the “enzyme memory” induced by
the acyl donors active site moulding in the first step of the reaction
was proposed. This work differs from previous studies in that the
buffer (pH 7.5, 10 mM), and dry Chromosorb P AW DMCS (1 g)
was added to the solution. The amount of immobilized enzyme
was determined by measuring absorbance at 280 nm, by taking a
molar extinction coefficient equal to 40,690 M cm . After vigor-
ous shaking, the preparation was left for 1 week under vacuum and
−
1
−1
over P O5 at room temperature.
2
2.3. Enzymatic reactions
“
imprinting” molecule is consistently in contact with the enzyme
◦
during the reaction, because it is the first substrate of the reaction.
Here we used this “imprinting” method and experimentally
highlight the significant influence of the alkoxy part of the ester acyl
donor on the enantiomeric ratio, for the resolution of pentan-2-ol
by CALB. We then established the full kinetic model for a Ping Pong
Bi Bi mechanism with two competing chiral alcohol substrates, in
order to verify that the differences in enantiomeric ratio, obtained
with different acyl donors, did not simply arise from differences
in reaction rates occurring during the acylation step, with the dif-
ferent esters. Our data from both experimental and kinetic studies
support the hypothesis of molecular imprinting. We then looked
for structural changes using molecular modeling methods.
Molecular modeling is a useful tool to provide a rational expla-
nation of experimental data. In 2010, Lousa et al. provided a
structural explanation for the imprinting effect [6] observed with
pre-treated subtilisin by co-lyophilization with an inhibitor in the
active site, using a molecular modeling approach. Results showed
that in the presence of the inhibitor, the active site was maintained
in an open conformation which was stable in hexane solvent, in
contrast to simulation with “untreated” enzyme. Here, 20 ns molec-
ular dynamics simulations were carried out to study how the first
step of the reaction, through the first tetrahedral intermediate,
affects the enzyme conformation, depending on the enantiopure
ester substrate used.
Initial rate of reaction measurements were performed at 70 C
in a solid-gas reactor as previously described [10]. Thermody-
namic activities for ester and alcohol substrates were respectively
aester = 0.1 and aalcohol = 0.05. Reactions were carried out in anhy-
drous conditions. The amount of enzyme comprised between 20
and 200 mg, depending on the acyl donor used. The total flow was
−
1
equal to 900 mol mol
.
2.4. GC analysis
Quantitative analysis of reaction products were conducted using
a 7890 GC system from Agilent for the analysis of ester products
◦
◦
−1
(R)-1- and (S)-1-methylbutyl propanoate (55 C 15 min, 3 C min ,
◦
−1
85 C 5 min), at a flow rate of 1.5 ml min with a Chirasil-Dex CB
(25 m, 0.25 mm i.d., 0.25 m ˇ-cyclodextrin, Chrompack, France)
column. Products were detected by FID and quantified using HP
Chemstation software.
2.5. Enantioselectivity measurements
Enantiomeric ratio values for the different kinetics reported in
Section 4, were obtained in our laboratory, by measuring the ratio
of initial reaction rates for ester products synthesis [11], in a contin-
uous solid-gas reactor with different acyl donors, and immobilized
CALB, as previously described [9,12].
2
. Experimental
3. Computational methods
2.1. Chemicals
3.1. Setup of the system
Substrates and other chemicals were purchased from
The starting CALB enzyme was the R = 1.55 A˚ crystallographic
Sigma–Aldrich–Fluka Chemical Co. They were of the highest
purity available (98% minimum) and checked by gas chromatog-
raphy before use. Substrates were dried by distillation under
argon prior to use and stored under argon atmosphere and over
molecular sieves. Solvents were purchased from Carlo Erba.
Racemic 1-methylpentyl propanoate was synthesized from the
corresponding alcohol and propanoic anhydride in pyridine at
room temperature [7].
structure solved by Uppenberg et al. [13] (PDB entry 1TCA). To
evaluate the effect of the ester substrate on the enzyme struc-
ture during the first step of the reaction path, the two tetrahedral
intermediates, obtained in the reaction with R or S 1-methylpentyl
propanoate were modelized. The choice of studying the intermedi-
ates, instead of free substrates, in the active site was done in order
to prevent the substrates from getting out of active site, observed
several times in the case of subtilisin by Lousa et al. [6]. Further-
more, the formation of the tetrahedral intermediate may have
more impact on the structure conformation, because its formation
requires the crossing of the energy barrier. Thus, three systems
were modelized: free enzyme, enzyme with R and S tetrahedral
intermediates.
A transition state analog crystal structure, obtained with phos-
phonate irreversible inhibitor (PDB entry 1LBS) was used to build
the tetrahedral part of the reaction intermediate, to allow for the
correct location of the central part of the tetrahedral intermediate.
The acyl part is a propanoyl group. The negatively charged oxy-
gen was oriented toward the oxyanion hole to establish hydrogen
bonds with Thr40 and Gln106.
(
R)-1-methylpentyl propanoate was obtained by enzymatic
resolution from vinyl propionate and hexan-2-ol using CALB
®
◦
Novozym 435 in heptane solvent at 35 C, eep enantiomeric
excess of ester product was 99.3%. Enriched hexan-2-ol in S
form taken from the previous reaction was used after purifica-
tion by chromatography on silica gel (eluent EP/AcOEt: 95/5), then
esterification with anhydride propionic was done to obtain 1-(S)-
methylpentyl propanoate.
2
.2. Enzyme used for kinetic studies
CALB was produced in the methylotropic yeast Pichia pastoris
and was expressed extracellularly and purified from the medium
by hydrophobic interaction chromatography, followed by gel fil-
tration [8,9]. Enzyme adsorption was performed onto 60/80 mesh
Chromosorb P AW DMCS (acid washed dimethylchlorosilanized)
NAMD 2.7 program and the CHARMM22 all-atom force field
were used. Calculations were done in an explicit water box (model
TIP3P) with boundary conditions (15 A˚ between the enzyme and the
edge of the box). A waterbox was used for the calculations because
it is in accordance with the CHARMM force field parameters def-
inition. It is supposed to increase the flexibility of the enzyme,
(
Varian, France). In a typical adsorption procedure for solid/gas
catalysis, enzyme (0.106 mg) was dissolved in sodium phosphate