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Applied and Environmental Microbiology, February 2002, p. 784-790, Vol. 68, No. 2
0099-2240/02/$04.00+0 DOI: 10.1128/AEM.68.2.784-790.2002
Copyright © 2002, American Society for Microbiology. All Rights Reserved.
Enhanced Exopolysaccharide Production by Metabolic Engineering of Streptococcus thermophilus
Fredrik Levander, Malin Svensson, and Peter Rådström*
Applied Microbiology, Center for Chemistry and Chemical Engineering, Lund Institute of Technology, Lund University, SE-221 00 Lund, Sweden
Received 6 August 2001/
Accepted 8 November 2001

ABSTRACT
It is possible that the low levels of production of exopolysaccharides
(EPSs) by lactic acid bacteria could be improved by altering
the levels of enzymes in the central metabolism that influence
the production of precursor nucleotide sugars. To test this
hypothesis, we identified and cloned the
galU gene, which codes
for UDP glucose pyrophosphorylase (GalU) in
Streptococcus thermophilus LY03. Homologous overexpression of the gene led to a 10-fold
increase in GalU activity but did not have any effect on the
EPS yield when lactose was the carbon source. However, when
galU was overexpressed in combination with
pgmA, which encodes
phosphoglucomutase (PGM), the EPS yield increased from 0.17
to 0.31 g/mol of carbon from lactose. A galactose-fermenting
LY03 mutant (Gal
+) with increased activities of the Leloir enzymes
was also found to have a higher EPS yield (0.24 g/mol of carbon)
than the parent strain. The EPS yield was further improved to
0.27 g/mol of carbon by overexpressing
galU in this strain.
However, the highest EPS yield, 0.36 g/mol of carbon, was obtained
when
pgmA was knocked out in the Gal
+ strain. Measurements of
the levels of intracellular metabolites in the cultures revealed
that the Gal
+ strains had considerably higher glucose 1-phosphate
levels than the other strains, and the strain lacking PGM activity
had threefold-higher levels of glucose 1-phosphate than the
other Gal
+ strains. These results show that it is possible to
increase EPS production by altering the levels of enzymes in
the central carbohydrate metabolism.

INTRODUCTION
Exopolysaccharides (EPSs) produced by lactic acid bacteria are
important for the texture of many fermented milk products. There
is great diversity in the composition and structure of these
EPSs, which results in different properties (for a review, see
reference
12). A variety of EPSs with different repeating units
and chain lengths have been found in
Streptococcus thermophilus,
and diversity is also found in the increasing number of
eps operons that are being sequenced (
1,
7,
32). The operons consist
of a more conserved region with genes that are thought to be
involved in regulation, chain length determination, and export,
which is followed by a variable region with genes coding for
glycosyltransferases and enzymes involved in polymerization
and export of the EPSs. The information being accumulated could
form the basis for the construction of new tailor-made polysaccharides
by genetic engineering (
35). However, before the variety of
EPSs from lactic acid bacteria can be fully exploited, ways
of enhancing the low levels of production must be found. For
example, the amount of EPS produced by
S. thermophilus normally
is less than 1% of the amount of the carbohydrate source (
12).
EPSs are synthesized from activated nucleotide sugars, and a
potential bottleneck in EPS production could be the low levels
of these precursors. In
S. thermophilus, which possesses the
Leloir pathway, UDP glucose (UDPglc) and UDP galactose (UDPgal)
can be formed from either the glucose or the galactose moiety
of lactose (Fig.
1). The enzyme that links the Leloir pathway
with glycolysis is phosphoglucomutase (PGM), which catalyzes
interconversion of glucose 6-phosphate (G6P) and glucose 1-phosphate
(G1P). We have recently found that
S. thermophilus mutants lacking
PGM activity produce the same amount of EPS as the parent strain
when they are grown on lactose (
20), which indicates that the
Leloir pathway is important for supplying EPS precursors. LacS,
the lactose transporter of
S. thermophilus, can transport lactose
either by lactose-galactose antiport or by proton symport (
29),
and in most dairy strains almost all galactose formed by ß-galactosidase
is secreted (
33). The Leloir enzymes, galactokinase (GalK),
galactose 1-phosphate uridyltransferase (GalT), and UDP glucose
4-epimerase (GalE), are present at low levels in these strains,
but they can be upregulated by mutations in the promoter region
since they are transcribed as a single unit (
37). However, to
produce a surplus of UDPglc and UDPgal from G1P or galactose
1-phosphate, UDP glucose pyrophosphorylase (GalU; EC 2.7.7.9)
is also required.
In this paper we describe cloning and characterization of
galU,
which encodes GalU, and its role in EPS production in
S. thermophilus LY03. We show how altered expression of combinations of GalU,
PGM, and the Leloir pathway affect metabolite levels and EPS
production. Our results revealed two different successful metabolic
engineering strategies for EPS overproduction in
S. thermophilus.

MATERIALS AND METHODS
Bacterial strains, media, and culture conditions.
The strains and plasmids used are listed in Table
1.
Escherichia coli strains were cultivated in Luria-Bertani medium or Terrific
broth.
S. thermophilus strains were grown at 42°C in M17
(Oxoid) containing 5 g of lactose or galactose per liter. Spectinomycin
was used at a concentration of 100 µg ml
-1, and erythromycin
was used at a concentration of 0.2 µg ml
-1. Controlled
batch experiments were performed in MST medium (
21) containing
(per liter) 50 g of lactose, 2.5 g of K
2HPO
4, 2.5 g of KH
2PO
4,
0.25 g of MgSO
4 · 6H
2O, 5 g of Casamino Acids (technical;
Difco), 0.06 g of
L-alanine, 0.2 g of
L-serine, 0.03 g of
L-tryptophan,
0.2 g of
L-asparagine, 0.17 g of
L-cysteine, 0.01 g of reduced
glutathione, and 1 ml of Tween 80, as well as the nucleotides,
trace elements, and vitamins that are in SD3 medium (
36). Batch
cultures were grown at least in duplicate in Biostat fermentors
(B. Braun) at 42°C with an initial volume of 1.0 liter.
The pH was maintained at 6.2 by automatic addition of 10 M NaOH,
and anaerobic conditions were established by nitrogen flushing
of the headspace. The first precultures were inoculated into
M17 from stocks that were stored at -80°C, and this was
followed by two more precultures inoculated (1%, vol/vol) into
M17. The final precultures were grown for 9 h in M17 before
inoculation (2%, vol/vol) of the fermentors.
DNA techniques and cloning procedure.
DNA was manipulated by using standard procedures (
3), and DNA
enzymes were purchased from Roche (Roche Diagnostics Scandinavia
AB).
E. coli was transformed by using the protocol of Inoue
et al. (
19), and
S. thermophilus was electroporated as described
previously (
27). Plasmid isolation was performed with Quantum
kits (Bio-Rad Laboratories AB), with some modification of the
protocol for
S. thermophilus (
20). A PCR was performed with
Pwo DNA polymerase, and an inverse PCR was performed with Expand
High Fidelity by using standard conditions, as described by
the manufacturer. Sequencing was performed with an ABI Prism
BigDye terminator cycle sequencing Ready Reaction kit (Perkin-Elmer,
Warrington, Great Britain). Degenerate primers 5"-AA
CTGCAGCNYTNGCNAARGARATGYT-3"
and 5"-CC
CTCGAGMTCNGTNAARYTGNAYYTCRTT-3" (restriction sites
are underlined) were used to amplify an internal fragment of
galU. The fragment was sequenced and used for construction of
primers 5"-GTAATCGCTCCTCAGGGTAAAGG-3" and 5"-GCTTCTTCAACGATAAATTGGATG-3",
which were used for the inverse PCR performed with
HindIII-digested
and religated chromosomal DNA as the template. The whole gene
was finally amplified from chromosomal DNA by PCR and was sequenced
in both directions on two independent PCR amplicons.
Overexpression of galU.
The galU gene was amplified by PCR using primers 5"-TCTAAGGAGTTCTCATGAAAAATCA-3" and 5"-GCTCTAGATTCGATGGATTTTATATTAGCC-3" (restriction site is underlined) and was ligated into SmaI-cut pUC19. The gene was cut out with EcoRI and ScaI from a construct with galU in the reverse orientation and was ligated into pFL42 cut with EcoRI and partially with HincII, yielding pFL52. In this way, galU was expressed from the promoter of pgmA. For overexpression of both pgmA and galU, the PCR product was ligated into ScaI-cleaved pFL42, and the construct with both genes in the same orientation was designated pFL46. The galU gene in this construct was located immediately downstream of pgmA, which was expressed from its own promoter.
Selection and characterization of a galactose-positive (Gal+) strain.
S. thermophilus LY03 was grown continuously under lactose limitation conditions, as described previously (33), with some modifications. The cells were grown in 0.2 liter of M17 containing lactose (7 g liter-1). The pH was adjusted to 6.2 by automatic base addition, and the dilution rate was 0.25 h-1. The cells were harvested after 30 reactor volumes, plated on M17 plates containing galactose (4 g liter-1), and incubated overnight anaerobically at 42°C. One clone was chosen, and this strain was designated TMB 6010. Parts (350 bp) of the gal promoter regions from LY03 and TMB 6010 were amplified by PCR and sequenced in both directions by using primers 5"-CCGATTTCATCAGCGATAGTT-3" and 5"-TCCGTATGCTCACCAATCAA-3". A pgmA knockout derivative of TMB 6010 was constructed by transforming the strain with pFL41 at 30°C. The plasmid was integrated at 42°C, and the correct integration was verified by PCR (20).
Measurement of growth, substrate consumption, and product formation.
Cell growth was monitored by determining the optical density at 620 nm after appropriate dilution of samples. Samples were filtered through 0.2-µm-pore-size filters and used to determine lactose, galactose, and lactate concentrations by high-performance liquid chromatography, as described previously (20). EPS concentrations were determined twice after consumption of 27 ml of 10 M NaOH in batch cultures by using the method of Degeest and De Vuyst (10). The EPSs were quantified by weighing. Yields were calculated by using the number of moles of carbon of lactose consumed.
Enzyme assays.
Cells in the mid-exponential phase were harvested and washed twice in 50 mM potassium phosphate buffer (pH 7.0). The cells were ruptured in an X-press (AB Biox), and debris was removed by centrifugation at 15,000 x g for 15 min at 4°C. Protein concentrations were determined by the Micro BCA method (Pierce, Rockford, Ill.). All enzyme assays were carried out at 37°C with a Cobas Mira autoanalyzer (Roche) by monitoring the absorbance at 340 nm. The GalK assay mixture contained 100 mM triethanolamine (TEA) buffer (pH 7.8), 5 mM MgCl2, 2 mM phosphoenolpyruvate, 2 mM ATP, 0.25 mM NADH, 4 U of lactate dehydrogenase ml-1, and 3 U of pyruvate kinase ml-1, and the assay was started by adding 10 mM galactose (33). To compensate for NADH oxidase activity in the cell extracts, the activities were calculated from the difference between the slope when the assay was performed with galactose and slope when the assay was performed without galactose. GalT activity was measured in 100 mM TEA buffer (pH 7.8), and the reaction mixture contained 10 mM MgCl2, 1 mM NADP+, 0.25 mM glucose 1,6-diphosphate (GDP), 5 U of glucose 6-phosphate dehydrogenase (G6PDH) ml-1, and 3 U of PGM ml-1. The reaction was started by adding 1 mM UDPglc and 1 mM galactose 1-phosphate (33). GalU and PGM activities were measured in 50 mM TEA buffer (pH 7.2) with 5 mM MgCl2. The GalU assay mixture contained 0.4 mM NADP+, 1 mM UDPglc, 50 µM GDP, 2 U of G6PDH ml-1, and 2 U of PGM ml-1, and the assay was started with 5 mM pyrophosphate (4). The PGM assay mixture contained 0.4 mM NADP+, 65 µM GDP, and 2 U G6PDH ml-1, and the assay was started by adding 1 mM
-G1P (30).
Measurement of intracellular metabolites.
Five-milliliter culture samples were taken after consumption of 21 and 27 ml of 10 M NaOH, frozen in liquid nitrogen, and stored at -80°C. The methods used to extract metabolites and inactivate enzymes were based on the methods described by Gonzalez et al. (16). The frozen samples were placed in a mixture containing 21 ml of boiling 99% ethanol and 2 ml of 1 M HEPES (pH 7.5) and boiled for 5 min. The samples were then cooled and centrifuged for 10 min at 5,000 x g and 4°C, and the supernatants were each reduced to a volume of 4 ml with a Speedvac AES2000 (Savant) vacuum centrifuge. G1P, G6P, UDPglc, and UDPgal contents were measured photometrically by using NADPH-linked assays. Emission was measured at 460 nm after excitation at 350 nm with a TD-700 fluorometer (Turner Designs). In each case an internal standard was added to the sample after completion of the reaction, and the increases in fluorescence observed for the sample and for the standard were used to calculate the concentrations of the metabolites in micromoles per gram (dry weight) of cells. G6P and G1P contents were measured by using the assay of Garrigues et al. (14). Each reaction mixture contained 100 mM TEA (pH 7.8), 20 mM MgCl2, 0.2 mM NADP+, and 2 U of G6PDH ml-1 for the G6P measurement. When the reaction was completed, 1.8 U of PGM ml-1 was added to start G1P consumption. The UDPglc content was determined by mixing 40 mM TEA (pH 7.2), 4 mM MgCl2, 0.4 mM NADP+, 2 U of G6PDH ml-1, 0.05 mM GDP, 1.8 U of PGM ml-1, and 5 mM pyrophosphate. After consumption of G6P and G1P, 0.5 U of GalU ml-1 was added, and the UDPglc content was measured. Finally, 0.2 U of GalE ml-1 was added to measure the UDPgal content. High-performance anion-exchange chromatography (HPAEC) was also used to determine UDPglc and UDPgal contents. The method used was based on the protocol described by Palmieri et al. (28). Separation was performed at a flow rate of 0.6 ml min-1 on a PA10 column with a precolumn (Dionex, Sunnyvale, Calif.) by using a 27 to 35% 0.5 M KH2PO4 gradient from zero time to 20 min; 0.5 M NaOH (flow rate, 0.5 ml min-1) was added after the column before detection by pulsed amperometry with an ED40 detector (Dionex).
Bioinformatic methods.
Protein sequences were downloaded from, and Gapped Blast (2) was performed on, the homepage of the National Center for Biotechnology Information (http://www.ncbi.nlm.nih.gov/). Multiple sequence alignment and construction of neighbor-joining trees were performed with ClustalX (34). Sequence data for S. thermophilus were obtained from the UCL Life Sciences Institute (ISV) website at http://www.biol.ucl.ac.be/gene/genome/.
Nucleotide sequence accession number.
The gene sequence described in this paper has been deposited in the EMBL database under accession number AJ300449.

RESULTS
Role of galU in EPS production.
A gene encoding GalU activity in
S. thermophilus LY03 was identified
and cloned by PCR after multiple alignment of GalU-like proteins
from
Streptococcus strains. The 304-amino-acid protein product
of
galU is 88% identical to GluA of
Streptococcus mutans and
is also closely related to other streptococcal proteins with
the GalU function (Fig.
2). Furthermore, GalU aligns with the
conserved nucleotidyl transferase domain Pfam 483 (E value,
10
-24) (http://www.sanger.ac.uk/Software/Pfam/).
To assess the functionality of
galU, the coding region and the
putative ribosome binding site (5"-AAGGAG-3") (the latter is
identical to the putative ribosome binding site of
Lactococcus lactis [
6]) were placed under control of the
pgmA promoter (
20)
in pFL52. When this plasmid was transformed into
S. thermophilus LY03, the resulting strain, TMB 6003, had GalU activity of 49
mU mg of protein
-1, compared to 5 mU mg of protein
-1 in LY03,
which confirmed that
galU encodes GalU activity.
To investigate if GalU activity in fact limits EPS production in S. thermophilus, TMB 6003 and LY03 were grown in pH-controlled batch cultures in MST medium. Both strains grew with a maximum specific growth rate of about 1.4 h-1, and no significant difference in EPS yields was observed (Table 2). The combined effect of PGM and GalU overexpression was also explored, since this could provide a way to shuttle G6P into UDPglc. Strain TMB 6004, in which galU was placed downstream of pgmA on plasmid pFL46, was constructed. This strain was also grown in batch cultures and compared to LY03 (Table 2). The growth rate of TMB 6004 was similar to that of LY03, but the EPS yield was higher in TMB 6004 (0.31 g mol of carbon-1) than in LY03 (0.17 g mol of carbon-1). Interestingly, the PGM and GalU activities were only 1.5 U mg of protein-1 and 9 mU mg of protein-1, respectively. When only PGM or only GalU was expressed from the same promoter on the same vector, the activities were 7 U mg of protein-1 (20) and 49 mU mg of protein-1, respectively. Plasmid preparations suggested that the lower levels of expression on pFL46 were due to a lower copy number of this plasmid (data not shown).
Galactose metabolism and EPS production.
A galactose-fermenting (Gal
+) strain of
S. thermophilus was
selected by growing LY03 under lactose-limiting conditions.
The resulting strain, TMB 6010, was able to grow on M17 with
galactose as the carbon source, which the parent strain was
unable to do. The galactose-fermenting ability of the strain
could be attributed to mutations in the
galK promoter region,
which enhanced transcription of the
galKTE genes (
37), resulting
in higher activities of the corresponding enzymes (
33). The
GalK and GalT activities were therefore measured and were found
to be about 10 times higher in TMB 6010 than in LY03 (Table
3). However, the accuracy of the GalK measurements suffered
somewhat from significant NADH oxidase activities in the cell
extracts (
18). To further characterize the galactose-grown strain,
the
galK promoter regions of LY03 and TMB 6010 were sequenced,
and a 1-bp insertion was found upstream of the -35 region in
TMB 6010 (Fig.
3). This corresponded to a type I mutation as
proposed by Vaughan et al. (
37). Both strains also had an extra
1-bp insertion in the presumed -10 region compared to
S. thermophilus CNRZ 302.
To investigate if the galactose-negative (Gal
-) phenotype of
S. thermophilus could be the result of a growth advantage, LY03
and TMB 6010 were grown in pH-controlled batch cultures with
50 g of lactose liter
-1. Under these conditions, LY03 grew more
rapidly initially, when lactose was abundant; the maximum specific
growth rate was 1.4 h
-1, compared to 1.2 h
-1 for TMB 6010 (Fig.
4).
To ascertain whether a higher flux through the Leloir pathway
could increase EPS production, Gal
+ strain TMB 6010 was also
grown in batch cultures in MST medium, and product formation
was measured (Table
3). The yield of galactose in the supernatant
was lower in TMB 6010 cultures than in LY03 cultures, which
confirmed that TMB 6010 catabolized the galactose moiety of
lactose more effectively. Furthermore, the EPS yields were 0.17
g mol of carbon
-1 in LY03 cultures and 0.24 g mol of carbon
-1 in TMB 6010 cultures, which indicated that increased activity
of the Leloir pathway could affect EPS production. Increased
flux through the Leloir pathway should also increase the availability
of intermediates (for example, G1P) in this pathway, and thus
overexpression of GalU in TMB 6010 could be favorable for EPS
production. We therefore transformed TMB 6010 with pFL52 and
investigated product formation in the resulting strain, TMB
6011 (Table
3). A slight increase in EPS production was detected
compared to the EPS production in TMB 6010, but it is likely
that most of the higher galactose uptake seen in the Gal
+ strains
resulted only in an increase in galactose flux to glycolysis
via PGM. To block this possibility, we constructed a knockout
PGM mutant of TMB 6010 by single-crossover recombination. The
PGM mutant, TMB 6012, was grown under the same conditions as
the other strains, and the enzyme activities and product formation
were measured (Table
3). This strain did not take up as much
galactose as TMB 6010 and TMB 6011. Nevertheless, the EPS yield
with this strain was significantly higher than the EPS yield
with any of the other strains.
Intracellular metabolites.
There are many possible bottlenecks in the complex network of reactions leading to EPS biosynthesis, and to gain a better understanding of the metabolism, we measured the intracellular levels of G1P, G6P, UDPglc, and UDPgal in all the cultures mentioned above, both in the exponential phase (Table 4) and in the late exponential phase (Table 5).
There were some variations in the metabolite levels between the two phases, but some common trends were observed. LY03 and the strain in which both pgmA and galU were overexpressed, TMB 6004, had similar levels of both G6P and G1P; the concentrations were about 2 to 5 µmol g of cells-1. TMB 6003, in which only galU was overexpressed, exhibited higher levels of both of these metabolites than the other Gal- strains, and there was more G6P than G1P. All the Gal+ strains had higher levels of G1P than the other strains. Furthermore, the pgmA knockout strain, TMB 6012, had clearly higher G1P levels than TMB 6010 and TMB 6011. UDPglc and UDPgal contents were measured both enzymatically and by HPAEC (Tables 4 and 5). The concentrations of these metabolites were low, and UDPgal contents could not be measured accurately by enzymatic methods. However, HPAEC revealed that the ratio of UDPglc to UDPgal was constant, about 3:1 (mol/mol), in all samples, and the UDPglc values obtained with the enzymatic and HPAEC methods were similar. It was found that the levels of UDPglc were highest in TMB 6003 among the Gal- strains and in TMB 6011 among the Gal+ strains. Thus, GalU overexpression from pFL52 seemed to have a positive effect on the levels of UDPglc and UDPgal.

DISCUSSION
We investigated how levels of enzyme activities in central carbohydrate
metabolism affect EPS production in
S. thermophilus LY03. As
a first step, a gene coding for GalU activity in
S. thermophilus was identified, cloned, and shown to be functional by homologous
overexpression.
galU is preceded by a gene encoding a putative
NAD(P)
+-dependent glycerol 3-phosphate dehydrogenase, and the
protein product of the sequenced part exhibited 94% identity,
over 102 amino acids, to GpsA (EC 1.1.1.8) of
Streptococcus pyogenes M1 (accession no.
AAK33309), a protein which has also
been identified as GpdA (EC 1.1.1.94; accession no.
P58143).
The same gene organization is found in
S. mutans (
38),
Streptococcus pneumoniae (
23), and
L. lactis (
6). Furthermore, after the
galU gene was cloned, preliminary data from sequencing of
S. thermophilus LMG18311 became available. A BlastP search revealed a putative
protein with 100% identity to GalU of
S. thermophilus LY03 (contig
269___55, bases 7626 to 8546), which was also preceded by a
GpsA/GpdA homologue. GpsA is a key enzyme for phospholipid biosynthesis
in
Bacillus subtilis, and it is regulated on the transcriptional
level (
25). Phospholipids are essential for multiple functions
in the synthesis of fatty acids and in the cell membrane. Interestingly,
a lipid carrier is needed for peptidoglycan biosynthesis and
probably also for EPS biosynthesis, and this provides some rationale
for the genetic organization of the
gpsA and
galU genes.
Once the galU gene had been identified, we investigated the effect of overexpressing the gene alone or in combination with other genes that have been shown to be crucial for polysaccharide production in various bacteria (6, 17). Tenfold overexpression of the genes coding for PGM (20) or GalU separately did not influence EPS production. However, EPS production was almost doubled when the specific activities of both enzymes were doubled at the same time. This indicates that there could be some kind of channeling of metabolites or other regulatory effects, since the measured levels of G6P, G1P, and UDPglc were not significantly different in TMB 6004 and LY03. It has also been observed previously that the levels of PGM, GalU, and GalE were high under conditions under which EPS production was high (9), but the flux-controlling function of these enzymes was not established. Our results also underline the fact that the result of overexpression of single genes in complex metabolic networks is often difficult to predict due to competition from different reactions for substrates and cofactors. Much of the recent work in metabolic engineering has also shown that single interventions in metabolic pathways are not sufficient to improve the yields of desired products, while multiple interventions are more likely to be successful (31). Boels et al. (6) found that homologous overexpression of galU in L. lactis NIZO B40 led to an eightfold increase in the levels of UDPglc and UDPgal. However, there was no effect on EPS production. The EPS produced by this strain contains rhamnose, and it was proposed that the availability of dTDP-rhamnose could limit EPS biosynthesis or that the level of expression of the eps gene cluster is the limiting factor. On the other hand, Gilbert et al. (15) found that heterologous expression of the S. pneumoniae type 3 capsule in L. lactis could be increased by coexpression of cps3U, which encodes a GalU enzyme. Our results suggest that there was an increase in the levels of UDPglc and UDPgal when galU was overexpressed and that the Glc1P/UDPglc ratios were lower (Tables 4 and 5). The EPS from LY03 has recently been shown to contain glucose, galactose, and N-acetylgalactosamine (22), and UDP-N-acetylgalactosamine could thus be a limiting precursor in addition to UDPglc and UDPgal. However, another recent study indicated that production of this precursor is not a limiting factor for EPS production in LY03 (11). It is therefore more probable that the lack of effect on EPS production in TMB 6003 is due to downregulation of EPS biosynthesis enzymes. Little is known about regulation of the eps operon in S. thermophilus, even though the product of the first gene, EpsA, shows similarity to the cps operon transcription activator CpsA in Streptococcus agalactiae (8). However, the physiological conditions that affect regulation of these enzymes are not known.
To obtain overexpression of the galKTE genes, we selected a strain under lactose-limited conditions. Interestingly, this strain did not grow as fast as the parent strain when lactose was abundant. This was probably due to the fact that lactose transport by LacS is energetically more favorable when LacS works as a galactose-lactose antiporter than when lactose uptake is driven by proton symport (13). The growth advantage could explain why Gal+ strains that are repeatedly transferred in milk, in which lactose is abundant, become Gal-.
As expected from increased flux through the Leloir pathway, all of the Gal+ strains contained higher levels of G1P than the other strains. However, the concentrations of the UDP sugars were apparently not affected, although the EPS levels were higher. It should be emphasized that the levels of UDP sugars were low with significant standard deviations. Thus, it was difficult to determine whether the observed positive effect on EPS levels was due to elevated UDP sugar levels or upregulated EPS biosynthesis. However, the fact that the Gal+ strain lacking PGM activity, TMB 6012, accumulated very high levels of G1P and also produced more EPS than all of the other strains indicates that G1P is forced towards EPS biosynthesis in this strain.
The results of this study clearly show that it is possible to enhance production of EPSs in S. thermophilus by altering the expression of enzymes that are involved in supplying EPS precursors. Higher levels of PGM and GalU together led to a proportional increase in the EPS yield, although no effect could be seen when either enzyme was overexpressed alone. It will be interesting to see if further co-overexpression of pgmA and galU leads to even higher levels of EPSs. However, if strains are to be used for in situ production in food, it may be difficult to achieve simultaneous overexpression of these two genes by food-grade genetic methods. More promising is the strategy of selecting a galactose-fermenting strain and then knocking out pgmA by classical mutagenesis or by internal deletion in the pgmA gene with the help of a food-grade system for gene deletion (5, 24). Nevertheless, to further improve the EPS yields for production of polysaccharides as additives, further studies of the regulation of EPS biosynthesis on the transcription and enzyme levels are required.

ACKNOWLEDGMENTS
This work was supported by European Community FAIR Programme
contract CT-98-4267.

FOOTNOTES
* Corresponding author. Mailing address: Applied Microbiology, Center for Chemistry and Chemical Engineering, Lund Institute of Technology, Lund University, P.O. Box 124, SE-221 00 Lund, Sweden. Phone: 46-46 222 3412. Fax: 46-46 222 4203. E-mail:
Peter.Radstrom{at}tmb.lth.s.


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Applied and Environmental Microbiology, February 2002, p. 784-790, Vol. 68, No. 2
0099-2240/02/$04.00+0 DOI: 10.1128/AEM.68.2.784-790.2002
Copyright © 2002, American Society for Microbiology. All Rights Reserved.
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