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Journal of Bacteriology, February 2001, p. 1441-1451, Vol. 183, No. 4
0021-9193/01/$04.00+0 DOI: 10.1128/JB.183.4.1441-1451.2001
Copyright © 2001, American Society for Microbiology. All rights reserved.
Network Identification and Flux Quantification in
the Central Metabolism of Saccharomyces cerevisiae under
Different Conditions of Glucose Repression
Andreas Karoly
Gombert,
Margarida
Moreira dos Santos,
Bjarke
Christensen, and
Jens
Nielsen*
Center for Process Biotechnology, Department
of Biotechnology, Technical University of Denmark, DK-2800, Lyngby,
Denmark
Received 22 June 2000/Accepted 23 November 2000
 |
ABSTRACT |
The network structure and the metabolic fluxes in central carbon
metabolism were characterized in aerobically grown cells of
Saccharomyces cerevisiae. The cells were grown under both
high and low glucose concentrations, i.e., either in a chemostat
at steady state with a specific growth rate of 0.1 h
1 or
in a batch culture with a specific growth rate of 0.37 h
1. Experiments were carried out using
[1-13C]glucose as the limiting substrate, and the
resulting summed fractional labelings of intracellular metabolites were
measured by gas chromatography coupled to mass spectrometry. The data
were used as inputs to a flux estimation routine that involved
appropriate mathematical modelling of the central carbon metabolism of
S. cerevisiae. The results showed that the analysis is very
robust, and it was possible to quantify the fluxes in the central
carbon metabolism under both growth conditions. In the batch culture, 16.2 of every 100 molecules of glucose consumed by the cells
entered the pentose-phosphate pathway, whereas the same relative
flux was 44.2 per 100 molecules in the chemostat. The
tricarboxylic acid cycle does not operate as a cycle in batch-growing
cells, in contrast to the chemostat condition. Quantitative evidence was also found for threonine aldolase and malic enzyme activities, in
accordance with published data. Disruption of the MIG1 gene did not cause changes in the metabolic network structure or in the
flux pattern.
 |
INTRODUCTION |
Since the whole genome of
Saccharomyces cerevisiae has been sequenced
(15), several kinds of analyses have been applied in order
to assign function to orphan genes. In many of these analyses, the aim
has been to determine how the different genes (both the ones with known
function and those open reading frames that have no assigned function)
interact with each other, enabling the cells to take up nutrients,
grow, divide, regulate their metabolism, release products to the
environment, and respond to different stimuli (31).
The different approaches that have been used for this purpose can be
classified as transcriptome, proteome, and metabolome analyses, depending on the type of compounds measured, i.e.,
transcripts, proteins, or metabolites (31). Besides these
approaches, other types of phenotypic investigations have been
performed, such as growth on synthetic or rich media, growth on
different carbon sources, determination of the ability to consume
oxygen, and measurement of enzyme activities in cell extracts. In
recent work, Entian and coworkers (9) showed that the type
and accuracy of the methods used are very important for the
identification of phenotypes in single-deletion mutants.
A very prominent phenotypic investigation method that has been employed
for the analysis of cells in different environments, as well as for the
analysis of different mutants, is the quantification of metabolic
fluxes in cells grown under balanced conditions, such as in a
steady-state chemostat or during the exponential phase of a batch
culture. This quantification can be carried out by metabolite balancing
(30, 40, 41, 42), through which the intracellular fluxes
are calculated from a few measured fluxes by using mass balances for
the intracellular metabolites. For a more accurate quantification of
the fluxes, one may use 13C-labeled substrates followed by
measurements of the isotopomers using gas chromatography and mass
spectrometry (GC-MS) or nuclear magnetic resonance (38).
Thus, balances can be set up for the individual carbon atoms, and this
gives a significant redundancy in the measurements, leading to more
robust flux estimates. The use of 13C-labeled substrates
enables both identification of the metabolic network structure and
quantification of the metabolic fluxes and is therefore referred to as
metabolic network analysis (5).
This kind of analysis can be applied to investigate the metabolic
network of S. cerevisiae, which is known to be under carbon catabolite repression when grown on rapidly fermentable carbon sources
(13). As glucose is often the carbon source present in
laboratory media as well as in industrial processes, this type of
transcriptional control is often termed glucose repression (3,
17). This phenomenon has been known for decades and refers to
the repression of the transcription of genes involved in different cellular functions, such as the uptake and catabolism of alternate carbon sources, respiration, tricarboxylic acid (TCA) cycle enzymes, gluconeogenesis, and peroxisomal functions (3). However,
the mechanism by which yeast cells sense glucose, and how the signal is
transduced from this initial sensing to the actual repression of gene
transcription at the end of the cascade, is not yet fully elucidated.
There is evidence that glucose concentration, rather than glucose
uptake, triggers the glucose-repression cascade (27). There is also evidence that hexokinase PII plays a major role in the
early part of the cascade (10, 20), but it is not known how the signal is transduced from glucose to Snf1p, a protein kinase
that plays a central role in the cascade (3). Snflp phosphorylates Mig1p (29, 32, 39), a protein that binds to
the promoter region of glucose-repressible genes. When glucose levels
are high, Snflp is not active and Mig1p is underphosphorylated and
located in the nucleus, repressing the transcription of genes. When
glucose levels are low, Snflp phosphorylates Mig1p, causing its
migration to the cytoplasm, releasing repression (3).
Transcriptional repression via Mig1p is a dual-type regulation, as the
protein can bind to structural genes as well as to their repressors or
activators. A physiological role for Mig1p has been shown in the
repression of genes involved in the catabolism of sugars such as
galactose, maltose, and sucrose, as well as of the CAT8
gene, which codes for a derepressor of gluconeogenic genes
(19). However, putative binding sites for Mig1p exist in
the promoter region of several other genes which are involved in
central metabolic functions, such as gluconeogenesis and respiration. Furthermore, TCA cycle genes, such as CIT1, CIT3, KGD1,
KGD2, and LPD1, may be indirectly regulated by Mig1p,
as it can bind to the HAP4 gene, which codes for the
transcriptional activator of these TCA cycle genes (19).
Yet, it is not clearly known to what extent glucose repression affects
the central metabolism of S. cerevisiae.
In this work, we grew S. cerevisiae cells under different
conditions of glucose repression. Different environmental conditions were applied both to a reference strain and to a mig1
disruption mutant. Metabolic network analysis was performed by
combining labeling experiments with mathematical modelling
(5).
 |
MATERIALS AND METHODS |
Strains.
Two strains were used throughout this work: the
reference strain CEN.PK113-7D (MATa
MAL2-8c SUC2) and the mig1
disruption mutant T468 (MATa
mig1
::MELI MAL2-8c SUC2), which was
constructed by Birgitte Rønnow, Danisco Cultor, as described
previously (18).
Cultivations.
A total of four cultivations were carried out
in a bioreactor that was specially designed for labeling experiments.
The temperature was controlled at 30°C, the pH was controlled at
5.00 ± 0.05 by addition of 0.5 N NaOH, and the dissolved oxygen
concentration was kept above 60% saturation by introducing sterile air
through a needle and agitating the medium with a magnetic stirrer at
700 min
1. The working volume was 200 ml in the batch
cultures and 150 ml in the continuous cultures, and the volume was kept
constant by withdrawing liquid through a continuously operating pump.
In all cases, cells from yeast-peptone-dextrose (YPD) plates were
transferred to 500-ml baffled flasks containing 100 ml of the following
medium: glucose, 10 g/liter;
(NH4)2SO4, 7.5 g/liter; KH2PO4, 14.4 g/liter; MgSO4
· 7H2O, 0.48 g/liter; trace element solution, 2.0 ml/liter; vitamin solution, 1.0 ml/liter; pH was adjusted to 6.5. After
about 24 h on a rotatory shaker at 30°C and 150 min
1, cells from this preculture were used to inoculate
the bioreactor to an optical density at 600 nm (OD600) of
0.15 in the following medium (44):
(NH4)2SO4, 5.0 g/liter;
KH2PO4, 3.0 g/liter; MgSO4 · 7H2O, 0.5 g/liter; trace element solution, 1.0 ml/liter; vitamin solution, 1.0 ml/liter. In all the labeling
experiments, 100% 1-13C-labeled glucose was used as the
sole carbon source. In the batch cultures, 5 g/liter was used as the
initial glucose concentration, and the cultivations were interrupted in
the late exponential phase after at least 4 generation times, when
cells were still growing at the maximum specific growth rate,
µmax. In the continuous cultures, an initial batch with
2 g of glucose/liter was carried out, after which a solution
containing 2 g of glucose/liter and the same composition as the batch
culture medium was continuously fed to the reactor at a dilution rate
of 0.1 h
1. When steady state was achieved (after time
enough for replacing four times the reactor content, or in other words
after 4 residence times), the feeding medium was switched to a similar
solution containing 2 g of [1-13C]glucose/liter, and
the cultivations were carried on for at least 5 more residence times.
The achievement of steady state was monitored by determining the
absorbance of the culture, and it was later confirmed via analyses of
excreted metabolites and also via labeling incorporation (see Fig. 1).
The trace metal solution had the following composition
(44) (in grams per liter): EDTA, 15;
ZnSO4 · 7H2O, 4.5;
MnCl2 · 2H2O, 0.84;
CoCl2 · 6H2O, 0.30;
CuSO4 · 5H2O, 0.30;
Na2MoO4 · 2H2O, 0.40;
CaCl2 · 2H2O, 4.5;
FeSO4 · 7H2O, 3.0;
H3BO3, 1.0; KI, 0.10. The composition of the
vitamin solution (44) was as follows (in grams per liter):
D-biotin, 0.05; calcium pantothenate, 1.0; nicotinic acid,
1.0; myoinositol, 25.0; thiamine chloride hydrochloride, 1.0; pyridoxol
hydrochloride, 1.0; p-aminobenzoic acid, 0.20.
With the aim of obtaining precise values for batch cultivation
parameters such as the maximum specific growth rate and the cell yield
on glucose for both strains employed in this work, two batch
cultivations were carried out in 4-liter bioreactors, i.e., one
cultivation with each strain. These reactors were equiped with two
Rushton turbines, and the cultivations were performed under the same
temperature, pH, and medium conditions as specified above for the
200-ml reactor. The only difference between the 200-ml and the 4-liter
cultivations was the initial glucose concentration, which was 5 g/liter
in the former and 10 g/liter in the latter.
Sample treatment.
In all cases, 1.5-ml samples were taken
from the cultivation for the determination of absorbance at 600 nm,
which was carried out using a Shimadzu flow spectrophotometer (model
CL-720; Kyoto, Japan). Thereafter, filtration of the remaining sample
volume was carried out on 0.45-µm-pore-size acetate filters
(Osmonics, Minnetonka, Minn.), and the filtrate was frozen at
20°C
and later used for sugar and excreted metabolite analyses.
When the batch cultivations were interrupted (late exponential phase,
after at least 4 generation times, when the glucose concentration was
around 2.7 g/liter), part of the reactor content was used for a dry
cell weight determination, whereas the rest was filtered through a
0.45-µm-pore-size nitrocellulose membrane (Gelman Sciences, Ann
Arbor, Mich.) and washed twice with distilled water, and the wet
biomass obtained was frozen at
80°C and later used for determining
the fractional labeling of intracellular metabolites. When the
continuous cultivations were interrupted (always after steady state had
been achieved), the content of the reactor was treated in the same way
as described above. In the continuous cultivation with the reference
strain, the incorporation of labeling was followed from the point when
the medium containing nonlabeled glucose was switched to the medium
containing labeled glucose. This was performed by collecting samples
from the reactor outlet in centrifuge tubes in an ice-water bath. For
each sample, the liquid was collected during 1 h, which corresponded to
a volume of ca. 15 ml. Subsequently, each sample was centrifuged at
4°C, 3,000 × g for 10 min. After this, the cell
pellet was resuspended in ca. 20 ml of distilled water and centrifuged
again, and the resulting pellet was transferred to Eppendorf tubes
using 1.5 ml of distilled water. Centrifugation was then carried out at 4°C, 5,000 × g for 5 min, and the pellet was frozen
at
80°C and later used for determining the fractional labeling of
intracellular metabolites.
Measurement of sugar and excreted metabolite concentrations.
Glucose, ethanol, glycerol, acetate, succinate, and pyruvate were
separated on an Aminex HPX-87H ion-exclusion column (Bio-Rad, Hercules,
Calif.) at 65°C, using 5 mM H2SO4 as the
mobile phase at a flow rate of 0.6 ml/min. Glucose, ethanol, glycerol,
and succinate were detected on a Waters 410 differential refractometer detector (Millipore, Milford, Mass.), whereas acetate and pyruvate were
detected on a Waters 486 tunable absorbance detector set at 210 nm. The
two detectors were connected in series.
Measurement of fractional labeling of intracellular
metabolites.
For the analysis of the fractional labeling of
intracellular metabolites, ca. 20 mg of wet biomass at
80°C was
transferred to 800 µl of 6 M HCl. The mixture was then separated into
two fractions. One fraction, of ca. 700 µl, was used for determining the fractional labeling of amino acid fragments, whereas the other fraction, of ca. 100 µl, was used for determining the fractional labeling of intracellular glucose. The first fraction was hydrolyzed for 12 to 20 h at 105°C. After this, ca. 800 µl of distilled
water was added to the sample, which was then centrifuged at
3,000 × g for 5 min for separation of the cell debris.
The supernatant was then separated into 200-µl fractions, which were
dried at 105°C. After this, the dried samples were separately
derivatized by two different agents, ethylchloroformate (ECF) and
(N,N)-dimethylformamide dimethyl acetal.
In both cases, the protocol described by Christensen and
Nielsen (6) was employed. The only difference was in the derivatization with ECF, in which trifluoroacetic anhydride was not
added. The second fraction was hydrolyzed for only 20 to 30 min at
105°C, after which 100 µl of distilled water was added. Derivatization of glucose to glucose pentaacetate (GPA) was carried out
according to the protocol described previously (7).
In all cases, the prepared samples were injected into the GC-MS (model
HP-G1723A, Hewlett-Packard). At least two injections were performed for
each derivatization, and the conditions employed were described
previously (6). The output of the measurements is a set of
clusters, each of which corresponds to the intensities of the mass
isotopomers of an amino acid fragment (or of a glucose fragment, in the
case of glucose derivatization). These intensities were corrected for
the natural labeling in the derivative part, as described elsewhere
(22, 23). Finally, the fractional labeling of each
fragment, termed summed fractional labeling (SFL), was calculated with the corrected intensities in the following way (7):
0 · m01-3 + 1 · m11-3 + 2 · m21-3 + 3 · m31-3 SFL(Ala1-3) =
m01-3 + m11-3 + m21-3 + m31-3
where the superscripts indicate the carbon atoms present
in the fragment and mn indicates the corrected
intensity of the mass isotopomer with mn labeled
carbon atoms. In the equation, the fragment of alanine containing all
three carbon atoms of this amino acid was used as an example. It is
important to note that the SFL of a fragment, as calculated from the
GC-MS measurements, is also equal to the sum of the fractional
labelings of the individual carbon atoms in the fragment. Thus, if
SFL(Ala1-3) and SFL(Ala2-3) can be measured,
it is possible to calculate the fractional labeling of C-1 of alanine
by subtracting the latter from the former.
Mathematical modelling.
The SFLs, as described above, were
used as inputs to a mathematical routine that is used for quantifying
the fluxes in the central carbon metabolism of S. cerevisiae. The mathematical framework has been described
previously (7) and will not be shown in detail here.
Briefly, in each iteration of the numerical procedure, a guess is made
on the fluxes and is used for calculating the SFLs via the mathematical
model. Subsequently, two errors are generated: one by comparing the
calculated SFLs with the values measured experimentally (via GC-MS, as
described above), and the other by comparing the guessed fluxes with
the ones measured experimentally. (Alternatively, literature values for
the biomass composition can be used as the measured fluxes). If the sum
of these two errors is smaller then the stored error value, the guess
on fluxes used in this iteration is considered the best one. Otherwise,
this guess is disregarded. A new iteration is started and the process goes on until an acceptable error is achieved.
The model used in this work is shown in the Appendix, indicating both
the reactions considered and the corresponding carbon atom transitions.
The metabolic functions considered were the central ones: the
Embden-Meyerhoff-Parnas (EMP) and pentose-phosphate (PP) pathways, as
well as the TCA cycle. Besides these pathways, other reactions have
been included based on both specific biochemical knowledge of S. cerevisiae and on the labeling results attained throughout this
work (see Results and Discussion for further details). Compartmentation
of some metabolites was crucial for fitting the calculated SFLs to the
measured values (7), and thus oxaloacetate, acetyl
coenzyme A (acetyl-CoA), and pyruvate were separated into two pools
each. The anaplerotic reaction catalyzed by pyruvate carboxylase was
included in the model as a cytosolic step (16, 45), the
reaction catalyzed by threonine aldolase was included as an alternative
biosynthetic route for glycine (24, 28), and the reaction
catalyzed by malic enzyme was included as mitochondrial step, as there
is evidence that it takes place when yeast cells grow on glucose
(1). Excretion of succinate and pyruvate were not included
in the model, as they represent a very small fraction (<0.1%) of the
carbon consumed by the cells as glucose.
In terms of metabolites drained for biosynthesis, two different cell
compositions were considered in terms of macromolecules, one for each
cultivation condition (Table 1). However,
the composition of each type of macromolecule was assumed to be
independent of the cultivation condition. Thus, the amino acid
composition of a protein was assumed to be the same under both
conditions and was taken from Oura (34). Similarly, it was
assumed that the lipid composition was the same under both growth
conditions and was taken from Bruinenberg et al. (2) and
Oura (34). The carbohydrate fraction was assumed to be a
polymer of glucose, and the metabolite drained in this case is
exclusively glucose-6-phosphate. Nucleic acids were considered to be
RNA, as the DNA fraction corresponds to only 0.3% of the dry cell
weight (34). Finally, it was assumed that the cell
composition was the same for both the reference strain and the
mig1 mutant, when compared under the same cultivation conditions. All these approximations are reasonable, as it has been
shown that perturbations in the biomass composition do not significantly alter the final flux patterns (8). Combining all these considerations with the biochemical knowledge of biosynthetic pathways for amino acid synthesis (46), it was possible to
calculate the drain of precursors to biomass under both cultivation
conditions (Table 2). These values were
used as the measured fluxes in the mathematical routine, as described
previously (7).
 |
RESULTS AND DISCUSSION |
Method validation.
In order to check the reproducibility of
the methodology developed and validated previously for the measurement
of SFLs of intracellular metabolite fragments of a filamentous fungus
(6), which was here applied to S. cerevisiae, a
so-called incorporation experiment was performed. This experiment
consisted of a continuous cultivation in which samples were
periodically taken from the reactor outlet during a period of 9 residence times after the feeding solution was switched to the medium
containing labeled glucose. The whole content of the reactor, as
described in Materials and Methods, was the final sample. The
incorporation of label into some of the analyzed metabolite fragments
is shown in Fig. 1 (only selected
fragments are shown, for the sake of clarity). It can be seen that 4 or
5 residence times are enough for the complete incorporation of label
into all fragments, which means that the isotopic steady state is
achieved at this point. First-order kinetics can be used as an
approximation for the incorporation phenomenon, as illustrated in Fig.
1 for all fragments. With first-order kinetics, the SFL is 98.2% of
the isotopic steady-state value after 4 residence times. The results
shown in Fig. 1 also demonstrate the reproducibility of the
measurements, as can be observed from the standard deviations in Table
3, which were calculated based on
independent measurements performed on at least six different samples
obtained after the isotopic steady state had been achieved.

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FIG. 1.
Label incorporation into fragments of selected
intracellular metabolites of S. cerevisiae in a continuous
cultivation. Time zero corresponds to the medium switch from naturally
labeled glucose to [1-13C]glucose as the limiting
substrate. The curves shown assume first-order incorporation kinetics,
according to the equation
SFL = SFLFINAL × (1 e t).
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Several of the results from Table 3 demonstrate the accuracy of the
measurements. It is known that alanine and valine are both derived from
pyruvate. According to the SFL values and the C-atom correspondence
shown in Table 3, it can be seen that the SFLs obtained for all
fragments of these two amino acids are in accordance with each other.
For instance, the SFL of the fragment Ala116 (or Ala99) corresponds to
half the value of the fragment Val144 (or Val127) in all cultivations.
Similar observations can be made for the SFLs of threonine and
aspartate fragments, which are both derived from oxaloacetate.
In the case of batch cultivations, it has been also observed that the
measurement of labeling of intracellular metabolite fragments is the
same when cells are harvested in the middle of the exponential phase
(OD600, 1.1) or in the late exponential phase
(OD600, 1.3) (data not shown). A similar finding was also reported for Escherichia coli (37).
Yield coefficients.
In Table 4,
the yield coefficients are presented for biomass formation on glucose,
as well as for the main metabolites excreted during aerobic cultivation
of S. cerevisiae. These coefficients provide an idea of the
overall metabolic fluxes in the cell. It can be seen that cells
cultivated in the chemostat present pure respiratory metabolism, as
there is no excretion of metabolites to the medium. In contrast, cells
grown in the batch cultures present respiro-fermentative metabolism,
leading to excretion of metabolites to the medium, which results in a
lower biomass yield on glucose. It can also be seen that there is an
apparently smaller excretion of metabolites coupled with a slightly
higher biomass yield on glucose in the mig1 mutant compared
to that in the reference strain in the batch cultivation. However, in
the chemostat it is difficult to draw any quantitative conclusions when
the two strains are compared with each other in terms of metabolite
yields, as the concentration range of metabolites for detection after
high-performance liquid chromatography separation and the available
sample volume for cell concentration measurements in terms of dry
weight from the 200-ml reactors are both very low. Thus, it is not
possible to affirm that dry weights of 0.52 and 0.46 g are
necessarily different from each other.
Influence of Mig1p on network structure.
From an analysis of
the results presented in Table 3, the first remarkable observation is
that almost no difference in the SFLs is found when the two strains are
compared under the same cultivation condition. The observation that the
data are the same in both chemostats might be explained by the fact
that the cells are not under glucose-repressing conditions and thus
there is no binding of Mig1p to the promoter of repressible genes. In
this case, a different phenotype in terms of fluxes would not be
expected in cells that do not express the MIG1 gene compared
with the reference strain. On the other hand, it is known that Mig1p
binds to glucose-repressible genes, at least in the case of
SUC2, when cells are grown under glucose-repressing
conditions (5, 12, 15, 19, 21), which is the case for the
batch cultivations performed in this work (the high specific growth
rate and the residual glucose concentration in the reactor should be
enough for provoking repression). With the measurements performed in
this work, it is not possible to affirm that Mig1p is binding to the
central metabolic genes of S. cerevisiae, which present
putative binding sites for this protein. However, the results from the
batch cultivation with the mig1 mutant do indicate that the
central metabolism is tightly regulated through pathways that operate
in parallel to the Mig1p pathway, either by avoiding its binding to the
genes or by eliminating the effect that this binding would have on the
metabolic fluxes. In the case of gluconeogenic functions, it is known
that the activation of gene expression, mediated by Sip4p and Cat8p,
plays a more important role than that of repression by Mig1p (5,
35). Thus, gluconeogenic fluxes do not occur in mig1
cells. However, a relief in the repression of respiratory and TCA-cycle
genes could be expected in the batch cultivation with the
mig1 mutant, and this would have yielded a different SFL
pattern for the internal metabolites than that of the reference strain.
The fact that the results are very similar to each other when both
strains are compared under the same cultivation condition also points
to the robustness and reproducibility of the methodology employed,
besides the issues presented above.
Network identification: qualitative inspection of SFL data.
It
can be seen from Table 3 that the SFLs of a considerable number of
amino acid fragments, as well as of glucose, could be measured by the
GC-MS technique employed (6). With these measurements, it
was possible to assess the SFLs of some key metabolites in the central
metabolic pathways of S. cerevisiae, namely the EMP and PP
pathways and the TCA cycle. Inspection of the SFLs allows
identification of the network structure (in terms of the activity of
different pathways), which is the first step in metabolic network
analysis. In the discussion below, no separate analysis will be made
with respect to the mig1 mutant strain, as the SFL data
obtained for this strain were not significantly different from the data
obtained for the reference strain.
(i) Glycine biosynthesis.
In the case of glycine, it is
supposed that its precursor is serine, which in turn is exclusively
generated from 3-phosphoglycerate (46). However, the
results from the chemostats show that the SFL of the fragment Gly175
(or Gly144) is higher than the value obtained for the fragment Ser175.
This indicates that there is another route for the formation of
glycine, which causes an increase in the SFL of this amino acid. Three
genes from S. cerevisiae were cloned and characterized, the
inactivation of which are required to generate auxotrophy for glycine
(25). Two of these genes, denominated SHM1 and
SHM2, encode the mitochondrial and cytosolic serine
hydroxymethyltransferases (SHMs), respectively. The third gene,
denominated GLY1, was assigned no function. Later, two
independent investigations (24, 28) reported that the gene
GLY1 of S. cerevisiae encodes a threonine
aldolase that catalyzes the cleavage of threonine into glycine and
acetaldehyde. Thus, when grown on glucose, two pathways exist for the
biosynthesis of glycine: one starting at 3-phosphoglycerate via serine
and another starting at oxaloacetate via threonine. When cells are
grown on nonfermentable carbon sources, e.g., ethanol and acetate, a
third pathway is the major source of glycine. In this case, glyoxylate
is converted into glycine via the reaction catalyzed by the enzyme
alanine-glyoxylate aminotransferase (28). However, the
gene coding for this enzyme has not yet been found. As this pathway is
not operative under growth on glucose, the analysis performed here
points towards the activity of threonine aldolase, and therefore this
reaction has been included in the mathematical model for flux
calculations (see Appendix).
The metabolism of the folate coenzymes is another point to be
discussed. When the flux calculations were first made for the chemostat, the reaction corresponding to the decarboxylation of glycine
was included in the model, but the estimated flux was zero (results not
shown). This is in accordance with published results (26),
which indicate that the generation of C-1 units is mainly carried out
by SHM and that the glycine cleavage system only takes place when the
former enzyme is inactive. Thus, it was decided to not include this
reaction in further calculations, and the corresponding reaction is not
shown in the Appendix.
(ii) Compartmentation of pyruvate.
It is known that valine is
derived from mitochondrial pyruvate, as the first step in its
biosynthetic route, catalyzed by acetolactate synthase, is
mitochondrial (12). However, it is not yet known in which
compartment alanine biosynthesis takes place, as there are putative
alanine aminotransferases both in the cytosol and in the mitochondrion.
Thus, it was decided to separate the pyruvate pool into two
compartments in the model (see Appendix), although as already mentioned
above, the SFLs of alanine and valine were not different from each other.
(iii) Compartmentation of acetyl-CoA.
The SFLs of amino acids
derived from more than one precursor, i.e., leucine, isoleucine,
lysine, and phenylalanine, can be used to gain an insight into
metabolism. Subtracting the SFL of the fragment Val127 from that of the
fragment Leu158, it is possible to assess the SFL of the C-2 atom of
acetyl-CoA (39.9% in the batch cultivation with the reference strain,
37.7% in the batch cultivation with the mig1 mutant, 33.0%
in the chemostat with the reference strain, and 31.2% in the chemostat
with the mig1 mutant). This probably represents the SFL of
mitochondrial acetyl-CoA, as the biosynthetic step of leucine formation
catalyzed by the enzyme
-isopropylmalate synthase is located in the
mitochondrion (36). Subtracting the SFL of the fragment
Pro142 from that of the fragment Lys156, it is also possible to assess
the SFL of the C-2 atom of acetyl-CoA (38.6% in the batch cultivation
with the reference strain, 36.3% in the batch cultivation with the mig1 mutant, 31.7% in the chemostat with the reference
strain, and 30.6% in the chemostat with the mig1 mutant).
This probably represents the SFL of acetyl-CoA in the nucleus, as the
biosynthetic step of lysine formation catalyzed by the two homocitrate
synthase isoenzymes (Lys20p and Lys21p) occurs in the nucleus
(4). In the model for flux calculations, this acetyl-CoA
was included as cytosolic, as a means of differentiating it from the
mitochondrial acetyl-CoA. In spite of the fact that the SFL values for
mitochondrial and nonmitochondrial acetyl-CoA were not significantly
different from each other, compartmentation of this metabolite proved
to be important for minimizing the error in the calculations.
(iv) Malic enzyme.
Concerning the SFL of phenylalanine, which
is known to be synthesized from erythrose-4-phosphate and
phosphoenolpyruvate, it is possible to see from the fragment Phe143
that the phosphoenolpyruvate C-1 and C-2 atoms have a lower SFL when
compared to the SFL of pyruvate C-1 and C-2 atoms, as assessed from the
fragment Val143. This observation points towards the activity of
another pathway for pyruvate formation besides the pathway catalyzed by
pyruvate kinase. Boles and coworkers (1) have shown that
malic enzyme (Mae1p), the role of which still remains quite intriguing,
is active when S. cerevisiae grows on glucose. This enzyme
catalyzes the mitochondrial conversion of malate to pyruvate and may
therefore explain the differences between the SFLs of pyruvate and
phosphoenolpyruvate, as mentioned above. The reaction catalyzed by
malic enzyme was also included in the model (see Appendix and Fig. 2).
(v) TCA cycle.
When the batch cultivation is compared to the
chemostat, significant differences are observed. In the former case, it
becomes clear that respiro-fermentative metabolism occurs and that the TCA cycle is not operating as a cycle, as such, but rather as two
branches. This can be deduced from the SFL of the C-2 atom of
aspartate, which is equal to 2.0%, indicating that this carbon atom
cannot originate from
-ketoglutarate but is rather coming from
pyruvate via the anaplerotic reaction catalyzed by pyruvate carboxylase, which is cytosolic (16, 45). The C-2 atom of aspartate (which reflects that of oxaloacetate) can only originate from
the C-2 atom of pyruvate or from the C-3 and C-4 atoms of
-ketoglutarate, considering the symmetric intermediates of the TCA
cycle. As the SFLs of the proline and glutamate fragments were much
higher than that of aspartate, it can be concluded that C-2 of
oxaloacetate can only arise from pyruvate, which is reflected in the
valine fragment and which in turn presents low labeling in the C-1 and
C-2 atoms. On the other hand, in the chemostats cells grow with purely
respiratory metabolism. In this case, the C-2 atom of aspartate has an
SFL of 12.0%, indicating that it is at least in part formed from
-ketoglutarate (based on the high label in the proline and glutamate
fragments and the low label in the valine fragments).
(vi) PP pathway.
Another observation is that the amino acid
fragments originating from precursor metabolites in the EMP pathway,
such as 3-phosphoglycerate and pyruvate, present lower SFLs in the
chemostat than in the batch cultivation. This is due to the higher PP
pathway flux in the former. A high PP pathway flux is required when the
biomass yield is high, because a relatively larger amount of glucose
has to be used for generation of NADPH. A high PP pathway flux gives lower SFLs for the lower glycolytic intermediates, since
decarboxylation of glucose-6-phosphate carried out in the first
steps of the PP pathway removes exactly the C-1 atom of this molecule,
which is the one that receives the label from
[1-13C]glucose.
The higher SFL observed for the glucose-6-phosphate fragment in the
batch culture, when compared to that in the chemostat, reflects the
lower PP pathway flux in the former case, as less fructose-6-phosphate
is being converted back to glucose-6-phosphate by glucose-6-phosphate
isomerase; this in turn causes a smaller "dilution" of the label in
the C-1 atom of glucose-6-phosphate (Fig.
2).

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|
FIG. 2.
Fluxes in the central metabolism of S. cerevisiae (reference strain). Values in bold correspond to
respiro-fermentative metabolism (batch cultivation). Values in italics
correspond to respiratory metabolism (chemostat). All the fluxes shown
are net fluxes. For reversible reactions, the degree of reversibility
is indicated in parentheses by the normalized exchange flux, calculated
according to the formula
vexch[0,1] = (vexch)/(vexch + vnet).
All fluxes are relative to a glucose uptake of 100 (arbitrary units).
Abbreviations: G6P, glucose-6-phosphate; F6P, fructose-6-phosphate;
G3P, glyceraldehyde-3-phosphate; PEP, phosphoenolpyruvate; PYR,
pyruvate; ACA, acetaldehyde; ACE, acetate; AcCoA, acetyl-CoA; OAA,
oxaloacetate; MAL, malate; FUM, fumarate; 2-KG, 2-ketoglutarate.
|
|
Metabolic fluxes.
The analysis above, concerning the
identification of the network structure, was made by inspecting the
measured SFLs in a qualitative or semiquantitative manner. By combining
these measurements with a suitable mathematical model, it was possible
to quantify the fluxes in the central metabolism of S. cerevisiae. In this way, it was possible to compare cells growing
in a chemostat at steady state, with a specific growth rate of 0.1 h
1, with cells growing in a batch cultivation, with
µmax = 0.37 h
1, in a quantitative
fashion. The process of estimating fluxes is characterized by the
process of finding the most suitable model that describes the
metabolism under investigation, in a sort of trial-and-error process,
which is based on biochemical knowledge and appropriate assumptions
(with the aim of both fixing nondefined biochemical details and
avoiding numerical problems in the calculations). The most suitable
model for the experiments performed in this work is the one shown in
the Appendix. The same model was suitable for both cultivation
conditions investigated.
The estimated fluxes for both cultivation conditions investigated are
shown in Fig. 2. In Table 5, the values
of the calculated and the measured SFLs are shown and give an
indication of the accuracy of the calculations performed. From these
data, it can be seen that almost all SFLs calculated using the
mathematical model presented in the Appendix are similar to the
measured values if a deviation of one absolute unit for the SFLs is
accepted. Reversibility is shown in Fig. 2 for the key reversible
reactions in terms of the normalized exchange fluxes. The reversibility in the transaldolases and transketolases in the PP pathway are not
shown because the number of measurements of SFLs of the compounds in
this pathway does not allow a precise estimation of the reversibility of these reactions. However, the net flux values for these reactions did not change significantly when different calculations were performed.
A first observation that can be made is on the PP pathway flux. It can
be seen that the value of 44.2 for the chemostat is much higher than
16.2 obtained for the batch cultivation (both values are relative to a
glucose uptake of 100 arbitrary units). This is in accordance with the
higher need of NADPH for anabolic purposes in the former case
(Ysx = 0.5 g/g). In the latter case, although the
protein content in the cells is higher (Table 1), ethanol was the main
product arising from glucose catabolism, and the cell yield was about
0.1 g/g. If the specific uptake rate of glucose, which was 15.9 mmol/g
(dry weight)/h in the batch culture and 1.17 mmol/g (dry weight)/h in
the chemostat, is multiplied by the calculated relative PP pathway
flux, it is possible to observe that the absolute flux through the PP
pathway is actually higher in the batch culture (2.57 mmol/g [dry
weight]/h) than in the chemostat (0.51 mmol/g [dry weight]/h),
reflecting the higher general glycolytic flux in respiro-fermenting
cells compared to respiratory cells. Different values for the PP
pathway flux have been reported. Gancedo and Lagunas (14)
reported that the PP pathway accounts for only 2.5% of the total
metabolism of glucose when cells are grown on glucose and ammonia. This
value was calculated from measurements on the radioactivity of the
CO2 produced by cells growing in shake flask cultures. Due
to the reversibility of the glucose-6-phosphate isomerase-catalyzed
reaction, this method is likely to give an underestimation of the PP
pathway flux. The amount of NADPH required for biomass formation has
been estimated to be 831 or 931 mmol per 100 g (dry weight)
(2, 34). Using these values it is possible to make an
estimation of the PP pathway flux if we consider that this pathway is
the sole route for NADPH formation. With a biomass yield of 0.5 g (dry weight)/g glucose, for each 100 mmol of glucose consumed 9 g
(dry weight) are formed, and 74.8 or 83.8 mmol of NADPH are required.
As every glucose-6-phosphate molecule that enters the PP pathway
generates two molecules of NADPH, a flux of 37.4 or 41.9 mmol per 100 mmol of glucose taken up is obtained, which is not far from the value
estimated here. Applying the same reasoning for fermenting cells with a
Ysx of 0.1 g (dry weight)/g, values of 7.5 or 8.4 mmol
can be calculated for the PP pathway flux. In the case of fermenting
cells, the value estimated in our work is higher (16.2 mmol). It is
important to note that our analysis is based on two main issues. First,
we were able to assess the SFL of glucose-6-phosphate with a high
degree of reliability (Table 3), and second, the reversibility of the
reaction catalyzed by glucose-6-phosphate isomerase has been included
in the calculations (Appendix and Fig. 2).
Concerning the TCA cycle, it can be seen that it operates in a cyclic
manner in cells grown in the chemostat, whereas it operates as two
branches in the cells grown in the batch cultivation, one of which is
oxidative, leading to
-ketoglutarate, and one of which is reductive,
leading to fumarate. It can be seen in Fig. 2 that the flux leading
from
-ketoglutarate to fumarate is zero in respiro-fermenting cells,
and the net flux leading from fumarate to oxaloacetate is also zero,
although there is an exchange flux in this case. To our knowledge this
is the first report of this in vivo observation. Succinate and
succinyl-CoA are not included in the model, and it is therefore not
possible to identify exactly where the cycle is interrupted. The
compartmentation of oxaloacetate was a key point in fitting the
calculated SFLs to the measured values, as the anaplerotic
reaction catalyzed by pyruvate carboxylase and the reaction catalyzed
by malic enzyme take place in different compartments.
The inclusion of malic enzyme in the model was the only way of
accounting for the differences found in the SFLs of pyruvate and
phosphoenolpyruvate. Although enzyme activity measurements and Northern
blot analyses indicate that the malic enzyme-catalyzed reaction
presents a higher flux in a batch culture at maximum specific growth
rate than in a chemostat with D = 0.1 h
1
(1), our results indicate similar flux values under both
cultivation conditions (Fig. 2). The physiological reasons for this
observation and for the general role of malic enzyme remain to be elucidated.
The formation of glycine by two different routes, namely via SHM- and
threonine aldolase-catalyzed reactions, has been included in the model.
Our results show a higher contribution to glycine formation from the
SHM-catalyzed reaction compared to the threonine aldolase-catalyzed reaction (Fig. 2). However, some
published results (25) show that growth is more affected
when the GLY1 gene (coding for threonine aldolase) is
deleted compared to growth after deletion of both the SHM1
and SHM2 genes.
Conclusions.
Metabolic network analysis, as applied in the
present work to cells of S. cerevisiae, is a tool that can
be utilized for the quantitative inspection of metabolism. The first
step in this analysis is the identification of the network structure,
which is basically achieved by combining the inspection of the SFLs of
intracellular metabolites, as measured by GC-MS, with biochemical knowledge. This step may bring insight into which enzymes are active
and which ones are not active and if there is an unknown reaction
taking place under the cultivation condition under investigation or in
specific mutant cells. The second step in this analysis is a
consequence of the first one. A mathematical model describing the
metabolic network, as identified in the first step, combined with the
measured SFLs with the aim of estimating the metabolic fluxes. These
data can be used for the quantitative comparison of cells grown under
different environmental conditions or for the comparison of different
mutants. Besides yielding important physiological information for
well-characterized species, such as the activities of the PP pathway,
TCA cycle, threonine aldolase, and malic enzyme, as shown in this work
with S. cerevisiae, metabolic network analysis is a
promising tool for investigating other poorly characterized species
with potential biotechnological applications.
 |
APPENDIX |
The model used for flux calculations is given in Table
A1.
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|
TABLE A1.
Model used for flux calculations; the C atom
transitions, which are used by the flux estimation routine, are also
indicated
|
|
 |
ACKNOWLEDGMENTS |
Andreas Karoly Gombert gratefully acknowledges financial support
by CAPES (Brasília, Brazil), grant number BEX1098/98-5. Margarida Moreira dos Santos acknowledges Fundação para a
Ciência e Tecnologia (Portugal) for financial support.
 |
FOOTNOTES |
*
Corresponding author. Mailing address: Center for
Process Biotechnology, Department of Biotechnology, Technical
University of Denmark, Building 223, DK-2800, Lyngby, Denmark. Phone:
45 45 25 2696. Fax: 45 45 88 4148. E-mail: jn{at}ibt.dtu.dk.
Present address: Department of Chemical Engineering, University of
São Paulo, São Paulo, Brazil.
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