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Applied and Environmental Microbiology, June 2001, p. 2677-2682, Vol. 67, No. 6
0099-2240/01/$04.00+0 DOI: 10.1128/AEM.67.6.2677-2682.2001
Copyright © 2001, American Society for Microbiology. All rights reserved.
Metabolic Behavior of Lactococcus lactis MG1363 in
Microaerobic Continuous Cultivation at a Low Dilution Rate
Niels Bang Siemsen
Jensen,
Claus Rix
Melchiorsen,
Kirsten Væver
Jokumsen,
and
John
Villadsen*
Center for Process Biotechnology, Department
of Biotechnology, Technical University of Denmark, DK-2800 Lyngby,
Denmark
Received 7 November 2000/Accepted 20 March 2001
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ABSTRACT |
Minute amounts of oxygen were supplied to a continuous cultivation
of Lactococcus lactis subsp. cremoris MG1363
grown on a defined glucose-limited medium at a dilution rate of 0.1 h
1. More than 80% of the carbon supplied with glucose
ended up in fermentation products other than lactate. Addition of even
minute amounts of oxygen increased the yield of biomass on glucose by more than 10% compared to that obtained under anaerobic conditions and
had a dramatic impact on catabolic enzyme activities and hence on the
distribution of carbon at the pyruvate branch point. Increasing aeration caused carbon dioxide and acetate to replace formate and
ethanol as catabolic end products while hardly affecting the production
of either acetoin or lactate. The negative impact of oxygen on the
synthesis of pyruvate formate lyase was confirmed. Moreover, oxygen was
shown to down regulate the protein level of alcohol dehydrogenase while
increasing the enzyme activity levels of the pyruvate dehydrogenase
complex,
-acetolactate synthase, and the NADH oxidases. Lactate
dehydrogenase and glyceraldehyde dehydrogenase enzyme activity levels
were unaffected by aeration.
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INTRODUCTION |
Homofermentative lactic acid
bacteria (LAB) are used primarily in the dairy industry but may also
prove to be advantageous hosts for production of lactate as a bulk
chemical or of food additives such as bacteriocins or amino acids using
recombinant DNA technology (10, 15). The metabolism of
these bacteria is constrained by the requirement for a balance between
NADH-producing and -consuming reactions. In the absence of external
electron acceptors (e.g., oxygen), the carbon fluxes of catabolism are tightly coupled. In anaerobic culture, glucose may be redox-neutrally converted to lactate or, alternatively, to the mixed acid products formate, acetate, and ethanol in a molar ratio of 2:1:1 (12, 26). However, when oxygen is present in the growth medium, the catabolic carbon fluxes are uncoupled from the redox metabolism due to
the NAD+-regenerating activity of NADH oxidases (NOX). This
oxygen-related potential for redirecting fluxes is used industrially in
connection with the formation of other metabolites such as diacetyl in
fermented milk products. Even submillimolar concentrations of diacetyl
have a strong impact on the taste of buttermilk and cheese
(22). Hence, minute amounts of oxygen may influence an
industrial process greatly. In this light, it is surprising that, to
our knowledge, no investigations have been carried out on the
microaerobic physiology of starter cultures. A number of studies on the
effect of oxygen in fully aerated cultures have been published, but
little light has been shed on the window ranging from anaerobic to
fully aerobic conditions of growth (4, 7, 8, 20).
Interest in the microaerobic physiology of LAB is furthermore spurred
by reports on the extreme sensitivity of pyruvate formate-lyase (PFL)
to oxygen (1, 25) and the negative effect of oxygen on
pfl gene expression (2, 19). Similarly, it has
recently been reported that vigorous aeration reduces the transcription of the adhE gene, which encodes alcohol dehydrogenase (ADH)
in Lactococcus lactis (3). However, to our
knowledge, no data have been published on the effect of controlled
aeration on the ADH enzyme protein level. While oxygen inactivates the
PFL enzyme, the activity levels of other enzymes are stimulated under
aerobic conditions. This is the case for the
-acetolactate synthase
(ALS), the initial step in the conversion of pyruvate to acetoin and diacetyl, and the pyruvate dehydrogenase complex (PDH)
(8).
Thus, the presence of oxygen in the growth medium influences the
metabolism of LAB not only by loosening the tight coupling between
catabolic carbon fluxes and the redox metabolism but also by affecting
the cellular content of key enzymes. The present investigation was
initiated to determine the effect of different levels of controlled
mild aeration on product formation and hence on in vivo activities of
the enzymes downstream of the pyruvate branch point: PDH, ALS, PFL, and
lactate dehydrogenase (LDH). The effect of oxygen on the synthesis of
PFL and ADH proteins and on the activity of the enzymes NOX, PDH, ALS,
LDH, and glyceraldehyde-3-phosphate dehydrogenase (GAPDH) was
quantified under different growth conditions. As such, the microaerobic
physiology of L. lactis MG1363 was determined and the link
to levels of enzyme protein or activity under the growth conditions
studied was found. To the best of our knowledge, no study of
microaerobic conditions of growth has previously been carried out for a
homofermentative LAB strain.
The relevance of the present study is both academic and industrial.
Diffusion of air into the growth medium brings about a microaerobic
environment at the interface, which may have important implications for
production of flavor-associated secondary metabolites. Academically,
the influence of oxygen on the distribution of pyruvate among four
competing enzymes is a challenge since it involves regulatory control
at several levels (Fig. 1). Continuous
cultivation was the tool of choice for investigating the effects of
varying the dissolved oxygen tension (DOT), since a constant growth
rate can be fixed and the in vivo activities of the product forming pathways can be precisely determined. In this way, we showed that minute amounts of oxygen have a dramatic effect on the resulting end
product profile.

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FIG. 1.
Metabolic network around the pyruvate node. AK, acetate
kinase; PYK, pyruvate kinase. Other abbreviations are defined in
the text.
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MATERIALS AND METHODS |
Strain and culture conditions.
The homofermentative
laboratory strain L. lactis ssp cremoris MG1363
(13) was the only organism used in this study. The organism was grown at 30°C in continuous mode in a baffled bioreactor (Applikon, Schiedam, The Netherlands) with a 1,000-ml working volume
and fitted with a four-blade Rushton turbine rotating at 350 rpm. The
dilution rate (D) was set at 0.1 h
1. The pH
was kept constant at 6.6 by automatic addition of 5 M KOH.
The defined growth medium MS10 (6) was supplemented with
the following components to sustain growth under aerobic conditions: MnCl2, 1.25 × 10
5 g · liter
1; thiamine, 1 mg · liter; thioctic acid, 2.5 mg · liter; and Sigma antifoam 289, 50 µl · liter
1. The concentration of glucose was 3.00 g · liter
1. The medium was added to the previously autoclaved
bioreactor by sterile filtration (pore size, 0.20 µm). A preculture
was prepared by transferring a single colony from a petri dish and
inoculating a tube containing 10 ml of the same medium as above but
where the concentrations of KH2PO4,
K2HPO4, and glucose were 9, 7.5, and 10 g
· liter
1, respectively. The pre-culture was grown at
30°C. The bioreactor was inoculated to an initial biomass
concentration of 1 mg · liter
1. The feed pump was
turned on at the end of the exponential growth phase.
An anaerobic steady state was obtained by introducing 50 ml of
N2 (99.998% pure) · min
1 into the
headspace of the bioreactor. Three different anoxic steady states were
obtained by sparging the reactor with 250 N ml of gas composed of
N2 (99.998% pure) and atmospheric air (at N2/air ratios of 230:20, 200:50, and 125:125) controlled
through the use of two mass flow controllers (Bronkhorst, Holland) per min. At these steady states, DOT was undetectable with a polarographic oxygen sensor (Mettler Toledo). One microaerobic steady state was
obtained when a set point DOT value of 5% of the value in equilibrium
with air (see below) was maintained by feedback regulation of the ratio
of air to N2 fed to the reactor (total flow rate, 250 N
ml · min
1). The oxygen electrode was calibrated by
sparging the bioreactor with air (100% DOT) and with N2
(0% DOT). In pure water at 30°C, a 100% DOT value corresponds to a
saturation oxygen concentration of 2.4 × 10
4
mol · liter
1.
For all conditions, the gas was sterile filtered (pore size, 0.20 µm
[Whatman, Ann Arbor, Mich.]) before being introduced into the
bioreactor. The off gas was led through a condenser cooled to
lower than
8°C and analyzed for its volumetric content of CO2 and O2 by means of an acoustic gas analyser
(Brüel and Kjær).
A steady state had been reached when at least five retention times
(one retention time being 10 h) had passed since the growth conditions were changed and the concentrations of biomass and carbonated fermentation end products remained unchanged (less than 5%
relative deviation) over the last two retention times.
Analysis of fermentation end products and glucose.
Ethanol,
acetoin, acetate, formate, lactate, and pyruvate were separated by
high-pressure liquid chromatography (AminoHPX-87H column; Bio-Rad,
Richmond, Calif.) at 65°C using 5 mM
H2SO4 flowing at 0.6 ml · min
1 as the eluent. Ethanol and acetoin were quantified
with a Waters 410 refractive index detector (Millipore, Badford,
Mass.), while acetate, formate, lactate, and pyruvate were quantified
with an Waters 486 absorbance detector set at 210 nm.
Glucose was quantified using a glucose dehydrogenase assay (Roche,
Basel, Switzerland) with a Cobas Mira automatic analyzer (Roche).
Determination of bacterial cell dry weight.
Nitrocellulose
filters (pore size, 0.45 µm) were used to determine the cell dry
weight. The filters were tared after having been dried in a microwave
oven at 150 W for 10 min. The biomass from 10 ml of culture was
collected on the filter and washed with 10 ml of distilled water before
being dried and tared as indicated above.
Enzyme assays in vitro.
Enzyme extracts were prepared
essentially as described previously (12). Approximately
100 ml of culture volume was collected from the bioreactor and
centrifuged (6,000 × g for 10 min at 4°C). The
supernatant was discarded, and the biomass washed twice in 200 ml of
0.2% (wt/vol) KCl and subsequently resuspended in 5 ml of a pH 7.2 buffer of the following composition: 45 mM Tris, 15 mM tricarballylic
acid, 20% (vol/vol) glycerol, 1 mM dithiothreitol, and 4.5 mM
MgCl2. The samples were stored at
25°C until analysis. Enzymes were extracted by sonication of cells (five cycles of 30 s
alternating with 60 s of cooling on ice). The resulting extract was clarified by centrifugation (10,000 × g for 10 min
at 4°C) and immediately analyzed for enzyme activity and enzyme
protein levels as specified below. The protein concentration of the
enzyme extract was determined by the assay of Lowry et al.
(18) using bovine serum albumin as standard.
Enzyme activities of LDH, GAPDH, PDH and NOX were determined at 30°C
and pH 7.2. The concentration of NADH was monitored
spectrophotometrically at 340 nm (
= 6.22 × 103
M
1 · cm
1). For PDH activity
determination, however, the concentration of
2-(p-iodophenyl)-3-p-nitrophenyltetrazolium
chloride (INT) was monitored spectrophotometrically at 500 nm (
= 12.4 × 103 M
1 · cm
1). One unit of enzyme was defined as the amount of
enzyme required to produce 1 µmol of product per min.
Enzyme activity assays for LDH, GAPDH, and PDH were performed with
reaction mixtures exactly as described previously (12).
NOX activity was assayed in 1 ml of reaction mixture which contained
100 mM Tris-HCl buffer (pH 7.2) 5 mM MnSO4, and 0.3 mM NADH. Addition of cellular extract initiated the reaction.
ALS was assayed essentially as described previously (5),
in 1 ml of reaction mixture containing 100 mM phosphate buffer (pH
6.5), 0.20 mM cocarboxylase, and 80 mM sodium pyruvate, which was used
to initiate the reaction. After incubation at 30°C for 15 min, 200 µl of 0.5 M HCl was added to stop the reaction and convert
-acetolactate to acetoin. The resulting solution was kept at 45°C
for 30 min, and then acetoin was quantified by the colorimetric method
of Westerfeld (27). The abundance of PFL and ADH in the
total protein pool of the organism was quantified using a sandwich
enzyme-linked immunosorbent assay (ELISA) as described previously
(19). The ELISA signal was corrected for nonspecific
binding by running a series of five doublet measurements where the
amount of total protein applied was varied. The slope linking the ELISA
signal to the amount of total protein was determined. The slopes
obtained were normalized with respect to the slope for the anaerobic
sample, whereby relative PFL (or ADH) protein levels were determined.
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RESULTS |
A supply of oxygen leads to an increased yield of biomass on
glucose.
In preliminary experiments with a glucose feed
concentration of 10 g · liter
1, it was observed
that mild aeration of the bioreactor changed the situation of glucose
limitation prevalent under anaerobic conditions to one of glucose
excess at 5% DOT (data not shown). Since our primary interest lay in
studying glucose-limited cultures, the reason for the accumulation of
glucose in the bioreactor was not investigated (previous work
[14] suggests an inhibitory effect of
H2O2 under aerobic conditions and with a high
sugar concentration in the feed). By reducing the concentration of
glucose in the feed to 3 g · liter
1, we were able
to determine five distinct steady states which were all glucose limited
(Table 1). One steady state (steady state
1) was anaerobic, while three (steady states 2 to 4) were mildly
aerated with increasing ratios of air to N2 in the gas feed
but with unmeasurable values of DOT. The final steady state (steady
state 5) was obtained for a measured and controlled DOT value of 5%.
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TABLE 1.
Biomass concentrations and specific rates of sugar and
oxygen uptake as a function of the growth
conditionsa
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The biomass concentration in the bioreactor, and hence the yield of
biomass on glucose, increased with aeration (Table 1). The biomass
concentration for the anaerobic steady state was 0.54 g (cell dry
weight) · liter
1 and increased with aeration to
0.68 g · liter
1 for a culture aerated to a DOT
level of 5%.
A supply of oxygen strongly affects pyruvate metabolism.
Based
on the known dilution rate (D = 0.1 h
1)
and the measured steady-state concentrations of glucose, biomass, and
catabolic products (Tables 1 and 2), we
estimated the specific in vivo activities through the enzymes
metabolizing pyruvate and involved in NAD+ regeneration
(Fig. 2 and 3). For all
five steady states, 94% or more of the glucose carbon was recovered in
biomass and end products. These data furthermore showed that in our
experimental plan, several patterns of behavior ranging from anaerobic
metabolism (ethanol, formate, and acetate besides lactate) to aerobic
metabolism (more acetate, some CO2, but no ethanol or
formate) were covered (Table 2).

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FIG. 2.
Distribution of carbon at the pyruvate branch point as a
function of aeration. As an example, the in vivo specific activity of
PFL at steady state 3 was computed as follows:
rPFL = concentration of formate × dilution rate/biomass concentration = 26.25 (C-mmol · liter 1) × 0.1 (h 1)/0.58 (g [dry
weight] · liter 1 = 4.77 C-mmol · g
(dry weight) 1 · h 1. The in vivo
specific activity of PDH was computed as
rPDH = [(racetate
kinase + rADH)/2] rPFL in millimoles of carbon per gram (dry
weight) per hour.
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FIG. 3.
Synthesis of NAD+ by ADH, LDH, NOX, and PDH
as function of growth conditions. As an example, the in vivo specific
activity through ADH for steady state 2 was calculated as follows:
rADH = (concentration of ethanol) × (moles of NAD+ generated per C-mole of ethanol
generated) × (dilution rate)/(biomass concentration) = 15.92 (C-mmol · liter 1) × 1 (mmol of
NAD+ · C-mmol 1) × 0.1 (h 1)/0.60 (g [dry weight] · liter 1) = 2.65 mmol of NAD+ · g
(dry weight) 1 · h 1. The in vivo flux
through NOX was calculated as rNOX = (number of moles of NAD+ generated per mole of
O2 consumed) × (specific uptake rate of oxygen).
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By measuring the oxygen concentration in the gas inlet and outlet, it
was possible to estimate the actual rate of oxygen consumption (Table
1). This was assumed to be equal to the specific in vivo activity of
the NADH oxidases (Fig. 3), since these presumably are the only enzymes
involved in oxygen consumption in L. lactis.
Under anaerobic conditions, pyruvate was distributed between mainly two
enzymes: LDH and PFL (steady state 1 in Fig. 2). As aeration was
increased (steady states 2 and 3), the flux through the PFL was not
affected, showing that this enzyme, although reported to be extremely
sensitive to oxygen (1, 19, 25, 29) may function even when
L. lactis consumes oxygen. On further increase of aeration
(steady state 4), PFL activity was dramatically reduced, and at steady
state 5, with 5% DOT, the activity was practically zero. PDH displays
a behavior opposite to that of PFL. There was no activity in steady
states 1, 2, and 3, but gradually the synthesis of acetyl coenzyme A
(acetyl-CoA) was taken over by PDH. There was no obvious trend in LDH
activity with increasing aeration. The ALS activity was close to zero
in all five steady states, which confirms that lactococci produce only
minor amounts of acetoin in the absence of citrate as an alternative
source for pyruvate.
Under anaerobic conditions, LDH and ADH were the main enzymes
responsible for the reoxidation of NADH produced in glycolysis (steady
state 1 in Fig. 3). Even the most modest supply of oxygen (steady
states 2 and 3) clearly resulted in NOX taking over the NAD+-regenerating role of ADH, while the LDH flux remained
almost constant. The in vivo activity of PFL was virtually unaffected by modest aeration, whereas the in vivo ADH activity was observed to
drop as soon as oxygen became available (Fig. 2 and 3). A further increase in aeration resulted in NOX being the major enzyme responsible for the oxidation of NADH, with LDH contributing only modestly. PDH
activity results in the formation of NADH; therefore, PDH contributed
negatively to the NAD+ balance for steady states 4 and 5.
Aeration affects the enzyme levels.
The in vitro levels of
GAPDH and of enzymes downstream of the pyruvate branch point were
determined in an attempt to obtain the pattern of regulation triggered
by the presence of oxygen in the medium (Table
3). An increase in aeration had no effect on the enzyme activity levels of GAPDH, while the flux through the
enzyme, quantified as the specific rate of glucose uptake, decreased
with increasing aeration (Table 1). This was surprising since
increasing aeration was expected to reduce the ratio of NADH to
NAD+ (9, 23), hence relieving the inhibitory
effect of an elevated ratio on GAPDH activity (11). The
data therefore suggest that the enzyme was insensitive to the putative
variation of the NADH/NAD+ ratio. This led us to believe
that the ratio, even for the anaerobic steady state, was so low that it
hardly had any inhibitory effect on the in vivo activity of the GAPDH
enzyme. The level of LDH in vitro activity was not affected by
increasing aeration.
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TABLE 3.
Specific in vitro activities of GAPDH, NOX, LDH, PDH, and
ALS and protein levels of ADH and PFL as function of culture
conditionsa
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The specific in vitro activities of PDH, ALS, and NOX increased with
aeration (Table 3), which correlates with the observed in vivo specific
activities of these enzymes (Fig. 2 and 3).
The low but nonzero in vitro activities of PDH and NOX for steady state
1 were, however, surprising, since these enzymes are not normally
associated with anaerobiosis. Although no gaseous oxygen was supplied
to the bioreactor, the medium feed contained dissolved air, which was
the only conceivable source of oxygen under these circumstances since a
continuous flushing of the headspace of the bioreactor with
N2 (99.996% pure) ensured that no atmospheric oxygen could
enter the bioreactor. It was necessary to determine whether the minute
supply of oxygen through the liquid feed was inducing the expression of
the genes encoding NOX and PDH or whether a low "dormant" level of
these enzymes ensured a state of preparedness of the organism in case
the growth environment turned aerobic. NOX and PDH activities were
therefore also assayed in protein extracts of cells grown in batch
cultures on the same growth medium with 10 g of lactose · liter
1. Lactose was preferred to glucose, since a
specific growth rate of 0.15 h
1 is obtained on lactose,
i.e., a growth rate similar to the dilution rate of 0.1 h
1. Strictly anaerobic conditions were ensured by
thoroughly flushing the growth medium with N2 prior to
inoculation and maintaining a N2 blanket during the
cultivation. NOX was not detectable in these cell extracts, while PDH
showed a clear activity of 0.07 µmol/min/mg. Lack of detectable NOX
activity for strictly anaerobic conditions implies that the organism is
not ready for a radical switch from strictly anaerobic to aerobic
conditions. Under the glucose-limited fermentation conditions used in
this study, even traces of oxygen were sufficient to induce NOX
synthesis, as observed in the cell extracts taken from the anaerobic
steady state.
In vitro protein levels of PFL and ADH were quantified by an ELISA.
This assay does not allow the active and inactive forms of PFL to be
distinguished. Hence, the total amount of PFL protein, relative to the
anaerobic steady state, was measured. The assay nevertheless made
possible an estimation of the impact of oxygen on the levels of ADH and
PFL, which has not been possible before because of the extreme
difficulty in measuring this activity (Table 3). While the
oxygen-related trend observed for PFL was expected (2,
19), no actual correlation between controlled microaerobic conditions and intracellular PFL protein levels had been established. Furthermore, to our knowledge, no reports are available on the influence of small amounts of oxygen on in vitro protein levels of ADH.
Except for LDH, it appears that oxygen in minute amounts triggers a
response affecting the in vitro levels of enzymes downstream of the
pyruvate branch point. This response created the potential for
redirecting the carbon flux from the combination of PFL and ADH toward
PDH and ALS. Furthermore, the increased activity of NOX under aerobic
conditions helped to regenerate NAD+ consumed in the glycolysis.
Regulation of in vivo activities. (i) PFL.
For steady states 2 and 3, the specific in vivo activity of PFL was unaltered compared to
the anaerobic level. This was the case despite the approximately two
fold-lower PFL protein level observed for steady states 2 and 3 (Table
3). This shows that the PFL protein level was not limiting for formate
synthesis under the anaerobic conditions studied here. It is doubtful
that the limitation of PFL activity under anaerobic conditions could be attributed to the intracellular levels of glyceraldehyde-3-phosphate and dihydroxyacetone phosphate, both allosteric inhibitors of the
enzyme (25), since it has been shown that at a comparable dilution rate (D = 0.12 h
1), the
intracellular levels of the two metabolites are far below the values
which would lead to inhibition (28).
From a certain aeration level (steady states 3, 4, and 5), the presence
of oxygen seems to have a dominating control over the in vivo activity
of PFL and hence on the flux to formate. This may be due to the
observed down regulation of PFL synthesis or, alternatively, to
irreversible inactivation of PFL (19). The ratio of
inactive to active PFL protein may have increased with aeration since
absolutely no formate synthesis was observed for steady state 5 in
spite of a significant in vitro protein level, which should have
sustained a detectable production of formate if the enzyme had been
fully active (Fig. 4).

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FIG. 4.
In vivo specific activity of PFL versus the
intracellular level of the enzyme (sum of active and inactive forms),
expressed as a percentage of the amount found under anaerobic
conditions of growth. Horizontal error bars represent the standard
deviations of five duplicate determinations of the protein in the
sample. Vertical error bars representing the standard deviation of
three determinations of the in vivo specific activity of the enzyme are
not visible since the standard deviations were low on the scale of the
figure.
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(ii) ADH.
Ethanol synthesis decreased drastically on slight
aeration (Table 2), which is ascribed partly to a reduced protein level of ADH in the cell (Table 3). Furthermore, the sigmoidal shape of the
relationship linking flux through ADH to the in vitro ADH level
suggests that increased aeration lowered the NADH/NAD+
ratio, leading to a higher degree of inhibition of ADH (Fig. 5). It appears from our data that the ADH
protein level present under anaerobic conditions does not limit the
rate of ethanol synthesis. The same conclusion was reached for the PFL
protein level and formate synthesis.

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FIG. 5.
In vivo specific activity of ADH versus the
intracellular level of the enzyme, expressed as a percentage of the
amount found under anaerobic conditions of growth. Error bars are
defined in the legend to Fig. 4. Steady states 4 and 5 are both close
to the origin.
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DISCUSSION |
Under anaerobic conditions, pyruvate is converted to lactate by
LDH and to acetyl-CoA and formate by PFL. Acetyl-CoA fuels the
synthesis of lipids, of acetate through acetate kinase, and of ethanol
through ADH. ATP production accompanies the synthesis of acetate,
whereas ethanol production regenerates NAD+ consumed in the
glycolysis and in the biomass synthesis. By supplying oxygen to the
growth medium, NAD+ regeneration was taken over by NADH
oxidases, whereby the organism can redirect the flux from ethanol to
increased acetate synthesis, thus producing more ATP. This led to a
higher yield of biomass on glucose and clearly demonstrates that ATP
synthesis limits biomass formation when the organism is grown at a
dilution rate of 0.1 h
1 under anaerobic conditions. NOX
most probably displayed a higher affinity for NADH than did ADH,
judging from the decrease in specific ethanol production as oxygen was introduced.
Oxygen, even at undetectable levels, triggered a response down
regulating the capacity of the PFL-ADH pathway and increasing the in
vitro activity levels of ALS, NOX, and PDH. In contrast, GAPDH and LDH
in vitro activity was not affected by increasing aeration. A
significant redirection of carbon at the pyruvate branch point ensued
from the altered enzyme levels. Our results show that PFL and PDH can
function simultaneously, although this requires fine-tuned conditions
of growth.
The anaerobic product spectrum consisting of formate, acetate, ethanol,
and lactate was replaced with the aerobic product pattern (acetate,
CO2, and lactate) for low values of DOT (5% DOT,
corresponding to 13 µmol of O2 · liter
1). This underlines the strong influence of low
oxygen levels on a continuous cultivation operated at low dilution rate.
We ascribe the lack of acetoin synthesis to the rather low level of the
glycolytic flux obtained for D = 0.1 h
1
used in our study. This prevents a large pool of intracellular pyruvate
from building up; because of the low affinity of ALS for pyruvate
(16, 24), a high intracellular concentration of pyruvate
(e.g., by decomposition of citrate) is needed if carbon is to be
directed through ALS.
The molecular mechanism of oxygen action is unknown, but it is
reasonable to assume that oxygen plays a significant role on the level
of gene expression and hence on enzyme levels. Increased aeration
diminished the synthesis of PFL and ADH proteins while raising the
activity levels of ALS, NOX, and PDH. Furthermore, oxygen is known to
irreversibly inhibit PFL by inducing peptide bond cleavage. The
presence of oxygen will probably also change the NADH/NAD+
ratio and thus the in vivo activity of enzymes involving this pair of
cofactors (GAPDH, PDH, LDH, ADH, and NOX). We have tried hard to
measure NADH in cellular extracts on a fluorometer by using an
enzyme-linked assay described previously (12), but the
presence of interferences in the extract, particularly under aerobic
conditions, impeded the analysis (16). This has prevented us from confirming a correlation between the NADH/NAD+
ratio and the in vivo specific activities of the enzymes mentioned above.
Preliminary results from our laboratory show that the oxygen-induced
regulatory cascade leading to higher ALS, NOX, and PDH activity is not
only controlled by aeration but also subjected to glucose repression
(data not shown).
This work demonstrates the strong impact of a minute oxygen supply on
pyruvate metabolism and suggests that both altered gene expression and
varied redox levels play a predominant role in regulation of this metabolism.
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FOOTNOTES |
*
Corresponding author. Mailing address: Center for
Process Biotechnology, Department of Biotechnology, Building 223, Technical University of Denmark, DK-2800 Lyngby, Denmark. Phone: (45)
45252668. Fax: (45) 45884148. E-mail:
john.villadsen{at}biocentrum.dtu.dk.
Present address: Chr. Hansen AS, DK-2970 Hørsholm, Denmark.
Present address: Novo Nordisk AS, DK-2880 Bagsværd, Denmark.
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Applied and Environmental Microbiology, June 2001, p. 2677-2682, Vol. 67, No. 6
0099-2240/01/$04.00+0 DOI: 10.1128/AEM.67.6.2677-2682.2001
Copyright © 2001, American Society for Microbiology. All rights reserved.
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