5
8
T. SUGISAWA and T. HOSHINO
was done with an aeration rate of 15 L min and an
temperature, agitation speed, and aeration speed,
respectively. During the fermentation, pH was con-
W
agitation speed of 500 rpm at 30
The broth was centrifuged at 400
to remove calcium carbonate, and then at 10,000
9
C for 21.5 hours.
×
g
for 10 minutes
trolled at 7.0 with Na
was converted to -sorbose within 18.5 hours cultiva-
tion and 89.3 g l of -sorbose from the initial
sorbitol concentration of 98.9 g l were produced.
2
CO
3
. As a result,
D
-sorbitol
×
g
L
for pelleting the cells. The cell cake was washed once
with physiological saline solution. The cells (200 g
wet weight from 20 liters of the culture) were frozen
L
D
-
W
W
The average productivity of
L
-sorbose was
at „20
9
C until use.
4.83 g l h.
WW
Preparation of membrane fraction. The cells
Solubilization
(
100 g wet weight) were suspended in 200 ml of
We tried to solubilize the membrane-bound
D
-
5
0 m
M
phosphate buŠer (pH 7.0) and passed through
sorbitol dehydrogenase of G. suboxydans IFO 3255.
a French pressure cell press at 20,000 psi. After cen-
At ˆrst, we tried to apply the method reported by
5)
trifugation to remove intact cells, the supernatant
Shinagawa et al., in which the membrane-bound -
D
(
cell free extract) was centrifuged at 80,000
×
g
for
sorbitol dehydrogenase of G. suboxydans var
. a IFO
one hour. We designated this precipitate as the mem-
brane fraction, which was resuspended into the
above buŠer (100 ml), and the protein concentration
3254 was solubilized. However, the -sorbitol de-
D
hydrogenase activity of G. suboxydans IFO 3255 was
lost in the supernatant and residual membrane
fractions after the solubilization of the membrane in
was 22.8 mg ml.
W
0
.01
Triton X-100, 0.1
10 mg ml of the membrane protein for 2 h at 59
M
sodium acetate buŠer (pH 5.0) containing 1
KCl, 0.1 M D-sorbitol and about
C. It
-sorbitol
dehydrogenase of G. suboxydans IFO 3255 has
diŠerent properties from that of G. suboxydans var
IFO 3254.
Therefore, we modiˆed this method for enzyme
z
Enzyme assay. The basal reaction mixture for
M
assaying
of 50 m
D
-sorbitol dehydrogenase activity consisted
potassium phosphate buŠer (pH 6.0),
W
M
was suggested that the membrane-bound
D
0
.25 m
M
DCIP, and 0.325 m
M
phenazine methosul-
fate (PMS), which was prepared just before the as-
say. A cuvette had a 1-cm light path and contained
.
a
0
D
.4 ml of the basal reaction mixture, 0.1 ml of 0.4
-sorbitol and the enzyme solution, and water with a
M
solubilization. The eŠects of pH and the concentra-
tions of buŠers, detergents, and KCl on the solubili-
zation were studied. When the membrane fraction
total volume of 0.51 ml. The reference cuvette con-
tained all components without the substrate. The
reaction was started at 25
9
C with
D
-sorbitol, and the
was mixed in 0.05
M
potassium phosphate buŠer (pH
Triton X-100 and 0.04
C, 74 of -sorbitol de-
enzyme activity was measured at the initial reduction
rate of DCIP at 600 nm. One enzyme unit is deˆned
as the amount of the enzyme that catalyzes the reduc-
7.0) containing 1
z
M
D
-
sorbitol for 2 h at 5
9
z
D
hydrogenase activity was recovered into the solubi-
lized supernatant from the membrane fraction as
shown in Table 1. The enzyme was not solubilized
tion of 1
mmol of DCIP per min. The extinction
coe‹cient of DCIP at pH 5.5, 6.0, 6.5, and 7.0 to
„
1
1
0.0 was 9.45, 10.8, 13.0, and 15.0 m
ly.
M
, respective-
with
n
-octyl-
b
-
D
-glucopyranoside and the activity
KCl. -Sorbitol had
was lost by the addition of 0.1
M
D
a stabilizing eŠect on the enzyme solubilization.
Measurement of protein concentration. BCA pro-
tein assay reagent (Pierce, Rockford, IL) was used
for the measurement of protein concentrations with
bovine serum albumin as the standard.
Puriˆcation
All steps were done between 4 and 8
9
C with the
buŠer 0.01
stated.
M
potassium phosphate unless otherwise
Results
Step 1. Solubilization. The membrane fraction
was suspended in the buŠer (pH 7.0) to give about
Conversion of
xydans IFO 3255
D
-sorbitol to
L
-sorbose by G. subo-
10 mg ml of protein, and then 1z Triton X-100 and
W
0.1
shaken at 180 rpm for 2 h and centrifuged at
80,000 for 60 min for the removal of the
precipitate. The
M
D
-sorbitol were added. The suspension was
G. suboxydans IFO 3255 was cultivated in glass jar
fermentor, type MB-C2000 (Iwashiya, Tokyo,
Japan) which had a total volume of 3 l with a top
drive system and temperature, pH, D.O., and
exhaust gas monitors, containing the medium
×
g
D
-sorbitol dehydrogenase activity
was recovered in the supernatant (200 ml).
Step 2. DEAE-Cellulose column chromato-
graphy. The supernatant (200 ml) was put on a
column of DEAE-cellulose
equilibrated with the buŠer (pH 7.0) containing
0.05 M D-sorbitol and 0.1
Triton X-100. After it
was washed with the same buŠer, elution of the en-
(
2
0
weight volume; 10
z
D
-sorbitol, 0.5
corn steep liquor, 0.0086
urea, 0.086 KH PO , and 0.15
z yeast extract,
W
.5
z
z
MgSO
4
・
7H
2
O,
an-
(q2.5 by 30 cm)
.086
z
z
2
4
z
tifoam). Its working volume was 2 liters and the fer-
mentation was done at 30 C, 700 rpm, 0.5 vvm for
z
9