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M. Takeuchi et al. / Journal of Molecular Catalysis B: Enzymatic 117 (2015) 7–12
13-hydroxy-cis-9-octadecenoic acid were prepared as previously
described [6,11,13,14]. Oxo fatty acids (KetoA, 10-oxooctadecanoic
acid, 10-oxo-trans-11-octadecenoic acid, 10-oxo-cis-12,cis-15-
octadecadienoic acid, 10-oxo-cis-6,cis-12-octadecadienoic acid,
12-oxo-cis-9-octadecenoic acid, and 13-oxo-cis-9-octadecenoic
acid) were prepared from hydroxy fatty acids (HYA, 10-
acid, (S)-10-hydroxy-cis-12,cis-15-octadecadienoic acid, (S)-10-
hydroxy-cis-6,cis-12-octadecadienoic acid, ricinoleic acid, and
13-hydroxy-cis-9-octadecenoic acid) by Jones oxidation, which
is oxidation of the hydroxy group with CrO3 [15]. (R)-HYA was
purified from racemic HYA using HPLC equipped with a chiral
column in the same method as “Enantiomeric purity analysis of
hydroxy fatty acids” shown in below. Fatty acid-free (<0.02%)
bovine serum albumin (BSA) was purchased from Sigma (St.
Louis, USA). All other chemicals were of analytical grade and were
commercially obtained.
CLA-DH. One unit was defined as the amount of enzyme that cat-
alyzes the conversion of 1 mol of HYA per minute. The reactions
were performed under anaerobic conditions in a sealed chamber
with an O2-absorbent (Anaeropack “Kenki,” Mitsubishi Gas Chem-
ical Co., Ltd., Tokyo, Japan) and gently shaken (120 strokes/min)
at 37 ◦C for 15 min. All experiments were performed in triplicate.
Reactions were performed under the standard reaction conditions
with some modifications, as described below. The optimal reaction
temperature was determined by incubating 1 mL of the reac-
tion mixture (20 mM sodium succinate buffer, pH 4.5) at various
temperatures for 15 min under anaerobic conditions. The opti-
mal reaction pH was determined at 37 ◦C using 1 mL of 20 mM
sodium citrate buffer (pH 3.0–4.0) or 20 mM sodium succinate
buffer (pH 4.0–5.5). Thermal stability was determined by measur-
ing the enzyme activity after incubating 1 mL of reaction mixture
containing 20 mM sodium succinate buffer (pH 4.5) at various tem-
peratures for 15 min under anaerobic conditions. The pH stability
was determined by measuring enzyme activity after incubating at
37 ◦C for 10 min in the following buffers under anaerobic condi-
tions: sodium citrate buffer (50 mM; pH 3.0–4.0), sodium succinate
buffer (50 mM; pH 4.0–6.0), KPB (50 mM; pH 5.5–8.0), and Tris–HCl
buffer (50 mM; pH 7.0–9.0).
2.2. Preparation of CLA-DH
Escherichia coli Rosetta2/pCLA-DH [12] cells were cul-
tured in 1.5 L of Luria-Bertani (LB) medium at 37 ◦C for 2 h
with simultaneous shaking at 100 rpm, and then isopropyl--
thiogalactopyranoside (IPTG) was added to a final concentration of
1.0 mM. After adding IPTG, the transformed cells were cultivated
at 20 ◦C for 8 h with simultaneous shaking at 100 rpm. After culti-
vation, the transformed cells (8 g) were harvested, suspended in a
standard buffer (16 mL), and treated with an ultrasonic oscillator
(5 min, 4 times, Insinator 201 M; Kubota, Japan). The standard
buffer contained 1 mM DTT and 10% (v/v) ethylene glycol in 20 mM
potassium phosphate buffer (KPB) (pH 6.5). The cell debris was
removed by centrifuging at 1700 × g for 10 min. The resulting
supernatant solutions were used as cell-free extracts. The cell-free
extracts were fractioned ultracentrifugation at 100,000 × g for
60 min and the supernatant was obtained. CLA-DH was purified
from this supernatant using a fast protein liquid chromatography
(FPLC) system (GE Healthcare) equilibrated with the standard
buffer. The supernatant was applied to a HiLoad 26/60 Superdex
200 prep-grade column (GE Healthcare) that had already been
equilibrated with standard buffer and eluted. CLA-DH was further
purified using a Mono Q 10/100 GL column (GE Healthcare), a
Superdex 200 10/300 GL column (GE Healthcare), and a Phenyl
Superose HR 10/10 (Pharmacia). The purified CLA-DH was dialyzed
with the standard buffer including 50% (v/v) glycerol and stored at
−20 ◦C until further use.
2.5. Kinetic analysis
All procedures were performed in an anaerobic chamber. Reac-
tions were performed under standard reaction conditions with
modified substrate and enzyme concentrations. The kinetics of HYA
dehydrogenation were studied using 30–1000 M HYA complexed
with 0.02% (w/v) BSA as the substrate, 7 g/mL CLA-DH, and a reac-
tion time of 15 min. The kinetics of KetoA dehydrogenation were
studied using 1–20 M KetoA complexed with 0.02% (w/v) BSA as
the substrate, 0.35 g/mL CLA-DH, and a reaction time of 5 min.
The kinetic parameters were calculated by using the experimental
data with the Michaelis–Menten equation using KaleidaGraph 4.0
(Synergy Software Inc., PA, USA).
2.6. Lipid analysis
to the reaction mixture as an internal standard. Lipids were
extracted from 1 mL of the reaction mixture using 5 mL of chloro-
form/methanol/1.5% (w/v) KCl in H2O (2:2:1, by volume) according
to the procedure of Bligh–Dyer, and then concentrated by evap-
oration under reduced pressure [16]. The resulting lipids were
dissolved in 5 mL of benzene/methanol (3:2, by volume) and
methylated with 300 L of 1% trimethylsilyldiazomethane (in hex-
ane) at 28 ◦C for 30 min. After methyl esterification, the resulting
fatty acid methyl esters were concentrated by evaporation under
reduced pressure. The resulting fatty acid methyl esters were ana-
lyzed by gas–liquid chromatography (GC) using a Shimadzu (Kyoto,
Japan) GC-1700 gas chromatograph equipped with a flame ion-
ization detector, a split injection system, and a capillary column
(SPB-1, 30 m × 0.25 mm I.D., SUPELCO, PA, USA). The initial col-
umn temperature 180 ◦C (for 30 min) was subsequently increased
to 210 ◦C at a rate of 60 ◦C/min, and then maintained at 210 ◦C for
29.5 min. The injector and detector were operated at 250 ◦C. Helium
was used as a carrier gas at a flow rate of 1.4 mL/min. The fatty acid
peaks were identified by comparing the retention times to those of
known standards.
2.3. Determination of the molecular mass of CLA-DH
In order to determine the native molecular mass of CLA-
DH, the enzyme solution was subjected to high perfor-
mance gel-permeation chromatography on a G-3000SW column
(0.75 × 60 cm, Tosoh, Tokyo, Japan) at room temperature. It was
eluted with 100 mM KPB (pH 6.5) containing 100 mM Na2SO4 at
a flow rate of 0.5 mL/min. The absorbance of the effluent was
monitored at 280 nm. The molecular mass of the enzymes was
determined from their mobility relative to those of standard pro-
teins.
2.4. Reaction conditions
All operations were performed in an anaerobic chamber. The
standard reaction conditions were as described. The reactions were
performed in test tubes (16.5 × 125 mm) that contained 1 mL of
reaction mixture (20 mM sodium succinate buffer, pH 4.5) with
0.1% (w/v) HYA or KetoA complexed with BSA [0.02% (w/v)] as the
substrate, 5 mM NAD+ or NADH and 42 g (=0.04 U/mL) purified
2.7. Enantiomeric purity analysis of hydroxy fatty acids
The enantiomeric purity of HYA, which was produced from
KetoA hydrogenation with CLA-DH, was analyzed using HPLC (Shi-
madzu, Kyoto, Japan) using a Shimadzu LC 20A System (Shimadzu)