K. Miyamoto et al.
would lead to an intramolecular rearrangement to form
the a,b-unsaturated isomers. Nevertheless, conversion of
10a and 11a exclusively afforded the a,a-dideuterated
products. Compound 10a is stable in the presence of
active site. As a final point, the high chemoselectivity in the
conversion of b,g-unsaturated carboxylic acids indicates a
concerted mechanism of AMDase G74C.
diisopropylACHTUNGTRENNUNGamine at pD 12. Upon treatment with 30%
NaOD in D2O, it undergoes complete rearrangement
into crotonic acid in 1 h. This is the preferred species due
to its conjugated double-bond system. In contrast, no re-
arrangement to crotonic acid was observed with NMR
spectroscopy during the G74C/V43A-catalysed conver-
sion of 10a with up to 80% conversion in 48 h. The high
chemoselectivity of the racemase indicates that the re-
deuteration of the Ca atom by the second cysteine pro-
ceeds much faster than a possible deuteration at the C4
atom. This is the case in a concerted mechanism, in
which the subtraction of the proton proceeds simultane-
ously with the deuteration (Scheme 1, path b2). Unsatu-
rated alkanoic acids have recently attracted attention
due to their possible application for the production of bi-
ofuels.[22] Moreover, novel processes for the generation
of biofuels involve b,g-unsaturated carboxylic acids as in-
termediates.[23] Herein, we report a method for the
highly selective generation of their a,a-dideuterated de-
rivatives, which might be useful for mechanistic studies.
The synthetic value of the enzymatic deuteration was
shown when the G74C/V43A-catalysed deuteration af-
forded 2,2-d-11a with excellent d purity (47 mg, 93%
yield, 98% content of d isomer).
Experimental Section
Molecular modelling: Molecular dynamic studies were performed in a
periodic waterbox by using the YASARA software (version 7.4.22) and
an AMBER99 force-field with long-range electrostatics with a cut-off at
7.86 J (Particle Mesh Ewald). The force-field of the substrate was ob-
tained by using AutoSMILES force-field parameter assignment. After ad-
dition of the solvent, cell neutralization and prediction of pKa values,
simulations of 500 ps were performed at 358C, pH 7 and a solvent density
of 0.997 gLÀ1. Each simulation step contained a 1.25 fs step for inter- and
intramolecular forces. The structure in PDB entry 3IXL was in silico
back-mutated to G74C by manual removal of mutation C188S and the
structure was minimised.[15] This structure represents a closed conforma-
tion containing phenylacetic acid (1a) in the active site. It was preferred
to the structure in PDB entry 3IXM[15] because residue Cys188 is moved
3.8 ꢁ away from the active centre in the latter structure. The other sub-
strates were generated manually and minimised prior to molecular dy-
namics simulations. Docking studies were done by using Accelrys Discov-
ery Studio 2.1 software (Accelrys Inc, San Diego, USA). Images were
generated by using Pymol software (DeLano Scientific, San Carlos,
USA).
Expression and purification of AMDase mutants: Escherichia coli
TOP10 cells were used as hosts for the transformation of the pBAD plas-
mid bearing the codon-optimised gene of AMDase as a fusion protein
with a C-terminal His tag.[24] The strains were grown in Luria–Bertani
(LB) liquid media or on LB agar plates supplemented with 100 mgmLÀ1
ampicillin at 378C until an optical density of 0.5 was achieved. AMDase
production was then induced by addition of arabinose (final concentra-
tion 0.025% v/v). After 14 h of further incubation at 308C, cells were har-
vested by centrifugation (15 min, 48C, 8000 g) and washed twice with
tris(hydroxymethyl)aminomethane (Tris) buffer (50 mL, 50 mm, pH 8.0).
Cells were resuspended in Tris buffer (20 mL) containing 10 mm imida-
zole and DNAse and were disrupted by sonification with cooling over
ice. Cell debris was removed by centrifugation (15 min, 48C, 8000 g).
AMDase variants were purified by His-tag purification by using an Ni se-
pharose high-performance column (50 mL, GE Healthcare, Uppsala,
Sweden) according to the instructions of the manufacturer. Protein elu-
tion was performed by using Tris buffer (50 mm, pH 8.0) with an imida-
zole gradient from 10 to 250 mm imidazole. AMDase variants eluted at
imidazole concentrations of around 90 mm. Proteins were also analysed
with a 12% separating sodium dodecylsulfate polyacrylamide gel. After
electrophoresis, the gel was stained with Coomassie brilliant blue. The
protein concentration was determined by using the Biorad assay accord-
ing to the instructions in the manual. Fractions containing AMDase were
pooled and concentrated by using centricons. Deuterated enzyme solu-
tion was prepared by washing the protein in centricons with deuterated
HEPES buffer (10 mm, pH 8.0).
In conclusion, protein engineering, molecular dynamics
simulations and the comparison of different substrates indi-
cate that steric and polar effects of the substrate structure
play a more dominant role on catalysis than mere kinetic a-
proton acidity. This is particularly illustrated in the examples
of analogue substrates 2–4a and 7–9a and profens 1b and
13–15b. It can be argued that a very stable accommodation
of the carboxylic group and an optimal configuration of the
Cys dyad towards the substrate are needed to decrease the
energy barrier of the transition state sufficiently for cataly-
sis. This is more important than the difficulty of abstracting
the a proton.
Conclusion
Protein engineering gave rise to a racemase variant with up
to 30-fold improved activity in the racemisation of bulky
profens. The 20-fold shift of the activity of the variant to-
wards promiscuous racemisation underlines the role of the
hydrophobic pocket as a determinant of the decarboxylating
and racemising activity in AMDase.
We have shown for the first time that a range of 2-aryl,
heteroaryl and vinylacetic acid derivatives are well-accepted
substrates for G74C racemase and its variants. Interestingly,
the racemase accepts nitro compounds as substrates. The a-
proton acidity of a substrate is less important for catalysis
than efficient accommodation of the transition state in the
Site-directed mutagenesis: Complementary primers bearing the nucleo-
tides to be changed and the vector pBAD-AMDase encoding for the
codon-optimised gene of AMDase were used for the polymerase chain
reaction (PCR) with Pyrococcus furiosus (Pfu) DNA polymerase and the
following reaction conditions: 1) 958C, 30 s; 2) 18 cycles: 958C, 50 s, then
54–608C, 60 s, then 728C, 360 s. The PCR mixture was treated afterwards
with DpnI restriction endonuclease to digest non-methylated template
DNA. The mutated plasmids were transformed into competent E. coli
Top10 cells. Mutant G74C/V43A/M159L was generated by using muta-
genic primers bearing the mutation V43A on a plasmid bearing the muta-
tion M159L. For the mutagenic primers, please refer to the Supporting
Information. Mutant G74C/V13D/G190H was generated by using a meg-
aprimer[25] generated from a forward primer bearing mutant V13D and a
reverse primer bearing mutant G190H.
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ꢀ 2011 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
Chem. Eur. J. 2011, 17, 557 – 563