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Production ofh-galactosidase by Bifidobacteria as influenced by
various culture conditions
C.A. Hsu, R.C. Yu, C.C. Chou*
Graduate Institute of Food Science and Technology, National Taiwan University, Taipei, Taiwan, ROC
Received 25 February 2004; received in revised form 16 August 2004; accepted 12 February 2005
Abstract
h-Galactosidase production by Bifidobacterium longum CCRC 15708, Bifidobacterium longum B6 and Bifidobacterium
infantis CCRC 14633 was first examined with B. longum CCRC 15708 showing the highest production ofh-galactosidase and
the highest specific activity. Further study with B. longum CCRC 15708 revealed that the highest level ofh-galactosidase was
produced with lactose and yeast extract as carbon and nitrogen sources, respectively. Optimal enzyme production occurred at an
initial pH of 6.5 and at 37 8C. Under these optimum culture conditions, a maximumh-galactosidase activity of 18.6 U/ml could
be obtained after 16 h of fermentation in a medium contain 4% lactose, 3.5% yeast extract, 0.3% K2HPO4, 0.1% KH2PO4,
0.05% MgSO4d
7H2O and 0.03%l
-cysteine. The highest transgalactosylation activity was also detected in this culture after 1416 h of fermentation.
D 2005 Elsevier B.V. All rights reserved.
Keywords: Bifidobacteria; h-Galactosidase; Nitrogen and carbon sources; Culture conditions
1. Introduction
The enzyme, h-galactosidase (EC 3.2.2.23) is a
commercially important enzyme. It catalyzes the hy-
drolysis of h-d-galactopyranosides such as lactose.By hydrolyzing lactose with h-galactosidase, the pro-
blems associated with whey disposal, lactose crystal-
lization in frozen concentrated deserts and milk
consumption by lactose-intolerant individuals can be
alleviated (Kim and Rajagopal, 2000).
In addition to catalyzing the conversion of lactose
to glucose and galactose, h-galactosidase also cata-lyzes transgalactosylation reaction; lactose serves as
galactosyl donor and an acceptor to form di-, tri-, or
higher galactooligosaccharides (GOS) (Wallenfels and
Weil, 1972; Prenosil et al., 1987). GOS are now
considered as a probiotic food ingredient and have
been demonstrated to promote the growth and the
establishment of bifidobacteria in the intestine
(Tanaka et al., 1983; Mitsuoka, 1990) and thus exert
0168-1605/$ - see front matterD 2005 Elsevier B.V. All rights reserved.
doi:10.1016/j.ijfoodmicro.2005.02.010
* Corresponding author. Postal address: Graduate Institute of
Food Science and Technology, National Taiwan University 59,
lane 144, Keelung Rd., Sec. 4, Taipei, Taiwan, ROC. Tel.: +886 2
2363 0231x2717; fax: +886 2 2362 0849.
E-mail address: [email protected] (C.C. Chou).
International Journal of Food Microbiology 104 (2005) 197206
www.elsevier.com/locate/ijfoodmicro
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a beneficial effect on the human host (Ishibashi and
Shimamura, 1993).
So far, various studies concerning the production
of GOS have been reported (Iwasaki et al., 1996;Onishi and Kira, 1996; Mozaffar et al., 1987; Shin
et al., 1998; Yang and Bedmarcik, 2001). It was
indicated that depending on the source of h-galacto-
sidase, the resulting GOS production from lactose is
quite different in the final products and yields (Yang
and Bednarcik, 2001). Furthermore, most of the h-
galactosidase used in these studies are not approved
for food use, are expensive and many are not available
or not availa ble in sufficient quantities for industrial
application (Kim and Rajagopal, 2000; Albayrak and
Yang, 2002). Therefore, selection of microorganismswhich are safe for human use and are capable of
producing high levels ofh-galactosidase becomes an
urgent and attractive task.
Bifidobacterium, a probiotic organism, and its h-
galactosidase preparations are generally recognized as
safe (GRAS) for use in foods and food systems. In the
present study, various bifidobacteria were first
screened for the production of h-galactosidase. Cul-
ture conditions that affect enzyme production by the
selected strain were further investigated.
2. Materials and methods
2.1. Microorganisms
Microorganisms tested in the present study in-
cluded Bifidobacterium infantis CCRC 14633, Bifi-
dobacterium longum CCRC 15708 (obtained from
the Food Industry Research & Development Insti-
tute, Hsinchu, Taiwan) and Bifidobacterium longum
B6 (obtained from Prof. H. Y. Lin, Dept. of Food
Science, National Chung-Hsing University, Tai-chung, Taiwan).
2.2. Culture condition
Before the experiment, the test organisms were
activated by two successive transfers in Lactobacilli
MRS agar (Difco, Detroit, MI, USA) supplemented
with 0.05% cysteine (Sigma, St. Louis, MO, USA)
(MRSC agar) at 37 8C for 12 h. The activated
culture was again inoculated into MRS broth
(Difco) supplemented with 0.05% cysteine (MRSC
broth) at 37 8C for 12 h. Cells in the culture were
harvested by centrifugation (10,000g for 10 min at
4 8C, washed twice with saline solution, diluted to a population of ca 109 CFU/ml and used as the
inoculum.
Fermentation for the production ofh-galactosidase
was carried out by transferring an aliquot (1.0 ml) of
the inoculum to a 250-ml Erlenmeyer flask containing
100 ml culture medium which consisted of 10 g
glucose, 20 g lactose, 10 g peptone, 10 g yeast extract,
5.0 g (NH4)2SO4, 3.0 g K2HPO4, 1.0 g KH2PO4, 0.5 g
MgSO4d7H2O and 0.3 g l-cysteine per liter (Onishi
and Tanaka, 1997). After 12-h incubation at 37 8C, the
population of test organisms and h-galactosidase ac-tivity were determined.
To examine the effect of various carbon sources
on h-galactosidase production, lactose, galactose or
glucose (all are products of Sigma) was used as the
carbon source in the medium. To investigate the
effect of nitrogen sources on the h-galactosidase
production, peptone, yeast extract and (NH4)2SO4in the above mentioned medium formula were
replaced with various amount nitrogen sources, so
the medium contained 0.3% N. The nitrogen sources
tested included casein, peptone, tryptone, gelatin,
beef extract and yeast extract (all were Difco pro-
ducts) and (NH4)2SO4 (Baker J. T., Phillipsburg, NJ,
USA). Nitrogen contents of these nitrogen sources
listed in Difco Manual (Anonymous, 1998) were
used to calculate the amount of nitrogen source
required. To examine the effect of pH, the initial
pH of the medium was adjusted to various values
(5.07.5) with sterile 1.0 N NaOH or 1.0 N HCl
solution to investigate the effect of culture tempera-
ture. The culture was maintained at temperatures
from 22 to 47 8C and all fermentation experiments
were carried out for 12 h. Detailed culture conditionsare specified in Results and discussion.
2.3. Determination of b-galactosidase activity
For the determination of h-galactosidase activity,
cells of bifidobacteria in the culture were first har-
vested by centrifugation (10,000g for 10 min at 4
8C). After washing twice with 0.03 M sodium phos-
phate buffer (pH 6.8), they were suspended in phos-
phate buffer. The suspension, maintained in an ice
C.A. Hsu et al. / International Journal of Food Microbiology 104 (2005) 197206198
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bath, was treated by sonication with a sonicator
(Model 3000, Misonix, Farmingdale, NY, USA) and
was centrifuged (15,000g, 10 min). The supernatant
served as the enzyme source.Activity of h-galactosidase was then assayed es-
sentially according to the method described by Nagy
et al. (2001b). The reaction mixture was composed of
0.5 ml of enzyme source and 0.5 ml of 15 mM o-
nitrophenyl h-d-galactopyranoside (OPNG) in 0.03
M sodium phosphate buffer (pH 6.8). After 10 min
at 37 8C, 2.0 ml of 0.1 M sodium carbonate was added
to the reaction mixture to stop reaction. Absorbance
was measured at 420 nm with a spectrophotometer
(Model Helios a, Unicam Co., Cambridge, UK). A
unit ofh-galactosidase was defined as the amount ofenzyme catalyzing the formation of 1 Amol of o-
nitrophenyl per min under the assay condition.
2.4. Determination of transgalactosylation
Transgalactosylation activity was assayed accord-
ing to the method described by Dumortier et al.
(1994). The reaction mixture was composed of 100
Al of enzyme, 300 Al of 0.05 M sodium phosphate
buffer (pH 4.3), and 100 Al of 0.5 M lactose. After 4
h a t 4 5 8C, the enzyme reaction was stopped by
heating for 2 min on a boiling-water bath, then the
incubation mixture was centrifuged for 30 min at
15,000g. The supernatant was diluted with water
before injection (20 Al) onto an HPLC column. An
HPLC system consisting of a degassing system
(Model DG-2410, Sanwa Tsusho Co., Tokyo,
Japan), a pump (880-LC, Jasco Co., Tokyo, Japan),
a carbohydrate analysis column (Rezex RNM carbo-
hydrate column, 7.8300 mm, Phenomenex Co.,
CA, USA), a guard column (Rezex RNM carbohy-
drate column, 7.850 mm, Phenomenex Co., CA,
USA), a column heater (800-LC, Jasco Co., Tokyo,Japan), a refractive index detector (830-RI, Jasco
Co., Tokyo, Japan), and a chromatography data sys-
tem (SISC Co., CA, USA). The eluent was pre-
degassed distilled water at a flow rate of 0.4 ml/
min. The column temperature was maintained at 85
8C and the detector temperature was set at 45 8C. A
unit of transgalactosylation activity was defined as
the amount of enzyme catalyzing the formation of 1
Amol of trisaccharide per min at 45 8C and at pH
4.3.
2.5. Determination of protein
Protein was assayed according to the method de-
scribed by Smith et al. (1985) using the bicinchoninicacid protein assay kit (Sigma). Bovine serum albumin
(Sigma) was used as the standard for calibration.
2.6. Enumeration of bifidobacteria
To enumerate bifidobacteria, samples were serially
diluted with saline solution and pour plated on MRSC
agar. Colonies were counted after incubation at 37 8C
for 48 h.
2.7. Statistical analysis
The mean values and the standard deviation were
calculated from the data obtained with triplicate trials.
These data were then compared by the Duncans
multiple range method (SAS, 2001).
3. Results and discussion
3.1. b-galactosidase production by Bifidobacteria
In a preliminary study, no h-galactosidase activity
was detected in the cultures of Bifidobacterium
longum CCRC 14634, Bifidobacterium breve CCRC
11846, Bifidobacterium bifidum CCRC 14615 and
Bifidobacterium adolescentis CCRC 14608. Howev-
er, B. infantis CCRC 14633, B. longum CCRC 15708
and B6 were found to be capable of producing h-
galactosidase with transgalactosylation activity. h-Ga-
lactosidase production by these bifidobacteria after 12
h of cultivation at 37 8C is shown in Table 1. The h-
galactosidase activities detected in the cultures of B.
lognum B6 and CCRC 15708 were not significantlydifferent (p N0.05), but were significantly higher than
that of only 0.56 U/ml found in the otherh-galacto-
sidase-producing culture of B. infantis CCRC 14633.
On the other hand, h-galactosidase detected in the
culture of B. longum CCRC 15708 showed a specific
activity of 7.15 U/mg protein which was significantly
higher than that (6.48 U/mg protein) detected in the
culture of B. longum B6.
Previously, h-galactosidase biosynthesis by bacte-
ria, yeasts, and moulds has been reported by various
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investigators (Ramana Rao and Dutta, 1977; Park et
al., 1979; Itoh et al., 1982; Dumortier et al., 1994;
Kim and Rajagopal, 2000; Nagy et al., 2001b). h-
Galactosidase activity varied up to a maximum of 2.5
U/ml forLactobacillus crispatus (Kim and Rajagopal,2000). Therefore, h-galactosidase production by B.
longum B6 and CCRC 15708 reported here is mark-
edly higher than previously recorded across a wide
range of microorganisms.
3.2. Effect of carbon source on the growth and b-
galactosidase production
Several investigators have described the carbon
source regulation of h-galactosidase biosynthesis in
various microorganisms (Fantes and Roberts, 1973;
Montero et al., 1989; Fiedurek and Szczodrak, 1994;
Nikolaev and Vinetski, 1998; De Vries et al., 1999;
Nagy et al., 2001a; Fekete et al., 2002). All indicated
that the role of carbon source in the biosynthesis ofh-
galactosidase may vary and depend on the microor-ganisms tested.
To examine the effect of carbon source on the
production of h-galactosidase, B. longum CCRC
15708, which produced a high amount ofh-galacto-
sidase with the highest specific activity (Table 1) was
used as the test organism. Growth and h-galactosidase
detected in cultures containing lactose, glucose or
galactose as the sole carbon source is shown in Fig.
1. It was found that the final viable population of B.
longum CCRC 15708 was higher in cultures contain-
ing either lactose or glucose as the sole carbon source
Carbon source
lactose glucose galactos
Final
population(logCFU/ml)
0
2
4
6
8
10
12
-galac
tosidaseactivity(U/ml)
0
3
6a a
b
A
C
B
e
Fig. 1. Effect of carbon source on the growth and h-galactosidase production by B. longum CCRC 15708. Medium contained 1% yeast extract,
1% peptone, 0.5% (NH4)2SO4, 0.3% K2HPO4, 0.1% KH2PO4, 0.05% MgSO4d 7H2O, 0.03% l-cysteine and 1% of various carbon sources.
Determinations were made after a 12-h cultivation at 37 8C. Bars indicate standard deviations. Different letters, within each type of
determination, indicate significant difference (p b0.05).
Table 1
Final pH, population size and h-galactosidase production by bifidobacteria*
Strain Final pH Final population
(log CFU/ml)
Activity (U/ml) Protein
(mg/ml)
Specific activity
(U/mg)B. longum CCRC 15708 4.0F0.0b** 8.2F0.0ab 4.96F0.42a 0.69F0.06b 7.15F0.16a
B. longum B6 3.9F0.0ab 8.2F0.0ab 4.81F0.66a 0.74F0.04a 6.48F0.70b
B. infantis CCRC 14633 4.2F0.0a 8.4F0.0a 0.56F0.04b 0.35F0.02c 1.63F0.17c
* Fermentation was conducted in a medium containing 2% lactose, 1% glucose, 1% yeast extract, 1% peptone, 0.5% (NH 4)2SO4, 0.3%
K2HPO4, 0.1% KH2PO4, 0.05% MgSO4d 7H2O and 0.03% l-cysteine at 37 8C for 12 h.
** Values in the same column with different letters were significantly different by Duncans multiple range test ( p b0.05).
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with the highesth-galactosidase activity (5.44 U/ml)
detected with lactose followed by galactose and the
lowest activity with glucose as the carbon source.
These results were different from the report of Kimand Rajagopal (2000) which indicated thatL. cripatus
grown in MRS broth containing galactose as the
carbon source showed the highest h-galactosidase
activity followed by moderate levels of enzyme pro-
duction on lactose and insignificant activity with glu-
cose or maltose. However, our results agree with those
observed for Kluyveromyces fragilis and Rhizomucor
sp. by Fiedurek and Szczodrak (1994) and Shaikh et
al. (1997), respectively, who demonstrated that lactose
is the best carbon source which induces the maximum
synthesis ofh-galactosidase by Rhizomucorsp., whileglucose is a poor inducer.
Amounts of carbon source in the medium may
affect the expression of h-galactosidase by microor-
ganisms (Fiedurek and Szczodrak, 1994; Inchaur-
rondo et al., 1998). As shown in Fig. 2, a final
viable population of the test organism ranging be-
tween 8.1 and 8.4 log CFU/ml was observed in the
culture originally containing 1.010.0% lactose. h-
galactosidase activity increased as the concentration
of lactose in the medium was increased up to 4.0%.
Further increasing the lactose content resulted in the
reduction of h-galactosidase activity. A similar phe-
nomenon was observed by Fiedurek and Szczodrak
(1994) who investigated the biosynthesis ofh-galac-
tosidase by K. fragilis. The decreased h-galactosi-
dase activity in the medium containing 5% or morelactose may be attributed to the increased concentra-
tion of internally released glucose which represses
biosynthesis of h-galactosidase by test organism
(Inchaurrondo et al., 1998). Furthermore, we also
demonstrated that 4% lactose was sufficient to induce
the highest expression of h-galactosidase under the
condition tested.
Kim and Rajagopal (2000) described that galactose
was the best carbon source for the biosynthesis of h-
galactosidase by L. crispatus, while addition of glu-
cose or lactose to the growth medium containinggalactose inhibited the synthesis of h-galactosidase.
We then further examined the effect of glucose and
galactose supplementation (0.55.0%) on the produc-
tion ofh-galactosidase in a medium containing 4.0%
lactose by B. longum CCRC 15708. We noted a
significantly (p b0.05) reduced enzyme activity in
the lactose-containing broth supplemented with
2.0% or more glucose or 0.5% galactose. Further-
more, as the amount of glucose or galactose was
increased in the growth medium, h-galactosidase ac-
tivity was repressed with galactose having a much
greater effect than glucose (data not shown).
Lactose concentration (%)
0.5 2 3 4 51 10
Finalpopulation(logCFU/ml)
0
2
4
6
8
10
12
-galac
tosidaseactivity(U/ml)
0
2
4
6
8
10
a cd D abab b d
C
D
BB
A A
D
Fig. 2. Effect of lactose concentration on the growth and h-galactosidase production by B. longum CCRC 15708. Medium contained 1% yeast
extract, 1% peptone, 0.5% (NH4)2SO4, 0.3% K2HPO4, 0.1% KH2PO4, 0.05% MgSO4d 7H2O, 0.03% l-cysteine and different concentrations of
lactose. Determinations were made after a 12-h cultivation at 37 8C. Bars indicate standard deviations. Different letters, within each type of
determination, indicate significant difference (p b0.05).
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3.3. Effect of nitrogen source on the production of
b-galactosidase
Nitrogen sources may affect microbial biosynthesisof h-galactosidase (Ramana Rao and Dutta, 1977;
Shaikh et al., 1997). Viable populations of B. longum
CCRC 15708 after 12 h of fermentation in the m edia
containing different nitrogen sources are shown in Fig.
3. It was noted that the final viable population of the test
organism ranged from 5.9 to 8.7 log CFU/ml depend-
ing on the nitrogen source. A large variation in the
activity of h-galactosidase, ranging from 0.00 to
11.13 U/ml, was also detected in the cultures with
different nitrogen sources. Yeast extract was found to
support the highest production ofh-galactosidase byB.longum CCRC 15708. This may be attributed to the
growth factors in addition to the nitrogen compounds
present in yeast extract (Bridson and Brecker, 1970).
As shown Table 2, the concentration of yeast ex-
tract in the medium was also found to affecth-galac-
tosidase production by B. longum CCRC 15708. The
activity ofh-galactosidase increased upon increasing
the yeast extract concentration up to 10.0% in the
medium. Further increasing yeast extract content in
the medium resulted in a sharp reduction in the activ-
ity ofh-galactosidase and a reduced final population
of the test organism. As show in Table 2, a consider-
able amount ofh-galactosidase could be obtained in
the medium containing 3.5% yeast extract, and this
level was used in subsequent studies.
3.4. Effect of initial pH and temperature on the
production ofb-galactosidase
In media with an initial pH between 5.0 and 6.5, the
test organism showed a final population of 8.58.7 log
CFU/ml with a smaller yield in media having an initial
pH of 7.0 or 7.5 as shown in Fig. 4. At an initial pH 5.0,
h-galactosidase activity was found to be ca 10.95 U/ml
increasing as the initial pH of the culture medium
increased, reaching a maximum of ca 15.87 U/ml at pH 6.5. Higher initial pH values resulted in a sharp
reduction in the production ofh-galactosidase by the
test organism (Fig. 4).
Although the final population detected in the culture
grown at 2742 8C is similar, h-galactosidase activity
at 37 8C was significantly higher than that detected at
other cultivation temperatures (Fig. 5). The activity of
h-galactosidase was increased as the cultivation tem-
perature was increased from 22 8C, the lowest cultiva-
tion temperature tested in the present study, to 37 8C.
Further increases in the cultivation temperature led to a
Contr
ol
Casei
n
Pepto
ne
(NH4)2S
O4
Trypto
neGelati
n
Beefe
xtract
Yeast
extra
ct
Fina
lpopulation(logCFU/ml)
0
2
4
6
8
10
12
-galactosidaseactivity(U/ml)
0
3
6
9
12
15
ba
eg
d
h
f
c
B
G
E
H
C
F
D
A
Fig. 3. Effect of nitrogen source on the growth and h-galactosidase production by B. longum CCRC 15708. Medium contained 4% lactose,
0.3% K2HPO4, 0.1% KH2PO4, 0.05% MgSO4d 7H2O, 0.03% l-cysteine and various nitrogen sources. Determinations were made after a 12-
h cultivation at 37 8C. Bars indicate standard deviations. Different letters, within each type of determination, indicate significant difference
(p b0.05).
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reduction of enzyme production accompanied by a
reduction in the final viable population. These observa-
tions agree with Fiedurek and Szczodrak (1994) and
Smith et al. (1985) and demonstrated that the highesth-
galactosidase production by B. longum CCRC 15708
was obtained with an initial medium pH of 6.5 at 37 8C.
The time course of h-galactosidase production,
transgalactosylation activity and growth of B. longum
CCRC 15708 for a period of 24 h is shown in Fig. 6.
Viable cells of the test organism increased gradually as
the fermentation started and reached a maximum after
ca 10 h of cultivation. Thereafter, the population of
viable cells showed no marked change. During the
fermentation, the pH of the medium declined rapidly
from 6.5 at the beginning to ca 3.8 after 16 h of fer-
mentation. On the other hand, h-galactosidase activity
increased sharply from the beginning of fermentation,
reached its maximum of ca 18.60 U/ml after 16 h of
fermentation, after which the level ofh-galactosidase
activity decreased. In general, changes of transgalacto-
Initial pH value5 65.5 6.5 7 7.5
Finalp
opulation(logCFU/ml)
0
3
6
9
12
-galactosidaseactivity(U/ml)
0
4
8
12
16
20
c
C
bc Ba
A
ab
A
d
C
e
D
Fig. 4. Effect of initial pH on the growth and h-galactosidase production by B. longum CCRC 15708. Medium with various initial pH contained
4% lactose, 3.5% yeast extract, 0.3% K2HPO4, 0.1% KH2PO4, 0.05% MgSO4d 7H2O, and 0.03% l-cysteine. Determinations were made after a
12-h cultivation at 37 8C. Bars indicate standard deviations. Different letters, within each type of determination, indicate significant difference
(p b0.05).
Table 2
Effect of yeast extract concentration on the growth and h-galactosidase production by B. longum CCRC 15708*
Yeast extract (%) Final pH Final population
(log CFU/ml)
Activity (U/ml) Protein (mg/ml) Specific activity
(U/mg)0 6.7F0.0ab** 7.3F0.4e 0.00F0.00i 0.00F0.00f 0.00F0.00e
1.5 4.5F0.3d 8.0F0.3d 6.03F0.61e 0.59F0.08d 10.27F0.60b
3.5 4.4F0.2d 8.5F0.1ab 13.40F0.55d 1.26F0.17c 10.73F1.20b
4.5 4.4F0.1d 8.6F0.0a 15.71F0.56c 1.50F0.19b 10.61F1.04b
5.5 4.4F0.4d 8.5F0.1ab 17.32F0.44b 1.62F0.04a 10.70F0.37b
10 5.3F0.1c 8.2F0.1c 18.80F0.78a 1.53F0.12ab 12.32F0.45a
12 6.5F0.1b 7.2F0.1b 2.78F0.18f 0.55F0.01e 10.20F0.97bc
14 6.5F0.1b 7.0F0.1f 2.21F0.02g 0.47F0.01e 9.36F0.39c
16 6.8F0.0a 6.9F0.2f 0.62F0.05h 0.18F0.01f 6.93F0.69d
* Fermentation was conducted in a medium containing 4% lactose, 0.3% K2HPO4, 0.1% KH2PO4, 0.05% MgSO4d 7H2O, 0.03% l-cysteine
and different concentrations of yeast extract at 37 8C for 12 h.
** Values in the same column with different letters were significantly different by Duncans multiple range test ( p b0.05).
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p
H
4
5
6
7
Finalpopulation(logCFU/ml)
6.5
7.0
7.5
8.0
8.5
9.0
Time (h)
0 4 8 12 16 20 24
-galactosidase
activity(U/ml)
0
5
10
15
20
Transgalactosylationactivity(U/ml)
0.00
0.01
0.02
0.03
0.04
Fig. 6. Time course of growth, final pH value, h-galactosidase activity and transgalactosylation activity of B. longum CCRC 15708.
Fermentation was conducted at 37 8C in a medium with an initial pH 6.5 containing 4% lactose, 3.5% yeast extract, 0.3% K2HPO4, 0.1%
KH2PO4, 0.05% MgSO4d 7H2O, an 0.03% l-cysteine. Bars indicate standard deviations.
Temperature (C)
22 27 30 37 42 47
Finalpopulation(logC
FU/ml)
0
3
6
9
12
-galactosidaseactivity
(U/ml)
0
5
10
15
20
b
E
a
C
a
B
a
A
a
D
b
E
Fig. 5. Effect of temperature on the growth and h-galactosidase production by B. longum CCRC 15708. Medium with an initial pH 6.5
contained 4% lactose, 3.5% yeast extract, 0.3% K2HPO4, 0.1% KH2PO4, 0.05% MgSO4d 7H2O, and 0.03% l-cysteine. Determinations were
made after a 12-h cultivation at various incubation temperature. Bars indicate standard deviations. Different letters, within each type of
determination, indicate significant difference (p b0.05).
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sylation activity detected in the culture showed a sim-
ilar trend as that observed withh-galactosidase activity.
The transgalactosylation activity increased as the fer-
mentation started, reached a maximum after ca 1216h of cultivation and declined as the fermentation was
further extended.
4. Conclusion
The results of this study demonstrated that produc-
tion ofh-galactosidase by bifidobacteria varied with
the strains selected. B. longum CCRC 15708 is capa-
ble of producing a high level ofh-galactosidase with
high specific activity. After optimizing the mediacomposition and culture growth conditions for the
production ofh-galactosidase by B. longum CCRC
15708, we achieved a maximum of 18.6 U/ml, which
was about 3.8-fold over the initial values obtained
with the non-optimized medium. Considering the
high yield of h-galactosidase with transgalactosyla-
tion activity and its GRAS nature, B. longum CCRC
15708 may be a potentially useful industrial strain for
the production ofh-galactosidase. Thus characteriza-
tion ofh-galactosidase produced by B. longum CCRC
15708 and application of this enzyme for GOS pro-
duction with lactose are being investigated.
Acknowledgment
This work was supported by the National Science
Council (NSC 91-2313-B-002-305), Taiwan, ROC.
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