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Applied and Environmental Microbiology, April 2001, p. 1587-1593, Vol. 67, No. 4
Faculty of Science, Swammerdam Institute for
Life Science, University of Amsterdam, 1018 TV
Amsterdam,1 and Faculty of Biology,
Department of Molecular Cell Physiology, Free University, 1081 HV
Amsterdam,2 The Netherlands
Received 22 September 2000/Accepted 29 December 2000
Hexokinase II is an enzyme central to glucose metabolism and
glucose repression in the yeast Saccharomyces cerevisiae.
Deletion of HXK2, the gene which encodes hexokinase
II, dramatically changed the physiology of S. cerevisiae. The hxk2-null mutant strain displayed fully oxidative growth at high glucose concentrations in early exponential batch cultures, resulting in an initial absence of fermentative products such as ethanol, a postponed and shortened diauxic shift, and higher biomass yields. Several intracellular changes
were associated with the deletion of hexokinase II. The hxk2 mutant had a higher mitochondrial
H+-ATPase activity and a lower pyruvate decarboxylase
activity, which coincided with an intracellular accumulation of
pyruvate in the hxk2 mutant. The concentrations of adenine
nucleotides, glucose-6-phosphate, and fructose-6-phosphate are
comparable in the wild type and the hxk2 mutant. In
contrast, the concentration of fructose-1,6-bisphosphate, an allosteric
activator of pyruvate kinase, is clearly lower in the hxk2
mutant than in the wild type. The results suggest a redirection of
carbon flux in the hxk2 mutant to the production of biomass
as a consequence of reduced glucose repression.
Glycolysis plays a central role in
glucose metabolism in the yeast Saccharomyces cerevisiae. It
is the root for many different pathway branches which lead primarily to
the production of biomass, ethanol, and CO2. The first step
in glycolysis is the transport of glucose across the cell membrane by
members of the hexose transporter family (6, 19, 33).
Subsequently, intracellular glucose is phosphorylated to
glucose-6-phosphate. In the yeast S. cerevisiae, there are
three isozymes that phosphorylate glucose: glucokinase (encoded by
GLK1), hexokinase I (encoded by HXK1),
and hexokinase II (encoded by HXK2). These isozymes
have different affinities for glucose and ATP and different
specificities toward other sugars, such as fructose and mannose
(14, 21). Furthermore, there are differences in the
transcriptional regulation of the genes that encode these
hexose-phosphorylating enzymes, depending on the source and the amount
of carbon (16). In contrast to hexokinases from
other organisms, S. cerevisiae hexose kinases are not
inhibited by their product glucose-6-phosphate (for a review, see
reference 7). Instead, the inhibition of
hexokinase II activity by trehalose-6-phosphate (5) may be involved in the regulation of the sugar influx
into glycolysis by trehalose-6-phosphate synthase (40, 41)
and thereby in the regulation of intracellular metabolite pools.
Furthermore, from previous studies it is known that hexokinase
II is involved in glucose repression (for reviews, see references
8 and 13).
Glucose repression is a mechanism that adapts yeast cells for the
fermentation of glucose, the preferred carbon source (for recent
reviews, see references 8 and 13), by repressing a large
number of genes at the level of transcription. Transcription of
SUC2 (encoding invertase), GAL genes (encoding
proteins involved in galactose metabolism), MAL genes
(encoding proteins involved in maltose metabolism), HXK1
(encoding hexokinase I), and genes encoding enzymes of the
glyoxylate shunt, the tricarboxylic acid (TCA) cycle, and
gluconeogenesis are all repressed in the presence of glucose. In
addition, genes involved in respiration and other mitochondrial
activities are repressed by glucose. In S. cerevisiae, glucose repression leads to the occurrence of diauxic growth on glucose.
The mechanism governing glucose repression is not yet well understood,
and several regulatory pathways seem to be involved. A central role for
hexokinase II is apparent (13). The absence of
hexokinase II causes derepression of high-affinity glucose transport (26, 37) encoded by at least HXT7
(20, 28). Also, the synthesis of hexokinase I
(11), invertase (encoded by SUC2), maltase,
malate dehydrogenase (12), galactokinase, cytochrome
c reductase, and cytochrome c oxidase
(27) is no longer repressed by glucose in hxk2 mutants.
Several properties of hexokinase II may be involved in glucose
repression. Previously, the sugar-phosphorylating activity of
hexokinase II was suggested to be directly correlated to the extent of glucose repression (24). Overproduction of
hexokinase I (encoded by HXK1) restored glucose
repression in a hxk2 mutant; however, overexpression of
GLK1 (encoding glucokinase) did not (35).
Hexokinase II is a phosphoprotein in vivo (44), which suggests a regulatory function. Both hexokinase I and
hexokinase II exist in two isoforms in vitro, a monomeric form
and a dimeric form, which have different affinities for glucose
(1). Phosphorylation at serine-15 converts
hexokinase II to the monomeric form (1, 18), which
seems to be essential for glucose repression (32). Furthermore, a dual cytosolic-nuclear localization of
hexokinase II has been demonstrated (31). In the
nucleus, the hexokinase II protein participates in a regulatory
DNA-protein complex necessary for glucose repression of the
SUC2 gene (17). Thus, there are strong
connections between glucose repression and hexokinase II, in
terms of both metabolic and regulatory activity.
Many previous studies have been dedicated to the role of
hexokinase II in glucose repression; we present here the first
comprehensive physiological characterization of S. cerevisiae cells deleted in hexokinase II during
aerobic batch growth with glucose as a carbon source, from exponential
growth on glucose to the diauxic shift and subsequent growth on ethanol.
We have shown that the deletion of HXK2 in S. cerevisiae results in a Crabtree-negative or Crabtree-diminished
phenotype: the strain displayed completely oxidative growth during
aerobic batch cultivation on glucose, with a high biomass yield.
Ethanol production begins only after continued growth on glucose.
Overproduction of the separate enzymes of glycolysis does not increase
the glycolytic flux (36). We think that changing
regulatory pathways rather than overexpressing particular enzymes, may
be a more fruitful approach to alter yeast physiology and to divert
glucose metabolism into desired pathways, e.g., the production of
biomass or the production of heterologous proteins in the presence of
abundant glucose.
Strain and growth conditions.
S. cerevisiae
wild-type strain CEN.PK113-7D (MATa
MAL2-8c SUC2) provided by P. Kötter (Frankfurt,
Germany) was used for a PCR-based gene disruption of HXK2.
Primers described in this study were constructed by Isogen BV
(Maarssen, The Netherlands). The HXK2 gene was replaced by a
kanMX cassette in CEN.PK113-7D to create strain KY116 as
follows: using primer AK53
(GTTGTAGGAATATAATTCTCCACACATAATAAGTACGCTAATTCGTACGCTGCAGGTCGAC; the underlined nucleotides correspond to the DNA immediately 5' of the HXK2 open reading frame) and primer AK54
(AAAAGGGCACCTTCTTGTTGTTCAAACTTAATTTACAAATTAAGTATCGATGAATTCGAGCTCG; the underlined nucleotides correspond to the DNA 3' of the
HXK2 open reading frame) the kanMX cassette of
plasmid pFA6a-kanMX4 (45) was amplified using the Expand
PCR kit as recommended by the manufacturer (Roche Diagnostics,
Mannheim, Germany). The resulting PCR product was transformed into
competent CEN.PK113-7D as previously described (15). After
2 h of cultivation in YEPD medium (1% yeast extract, 2% peptone,
2% glucose), the transformed cells were plated on solid YEPD medium
(2% agar) containing geneticin at 200 µg ml
0099-2240/01/$04.00+0 DOI: 10.1128/AEM.67.4.1587-1593.2001
Copyright © 2001, American Society for Microbiology. All rights reserved.
Physiological Properties of Saccharomyces
cerevisiae from Which Hexokinase II Has Been Deleted
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ABSTRACT
Top
Abstract
Introduction
Materials and Methods
Results
Discussion
References
![]()
INTRODUCTION
Top
Abstract
Introduction
Materials and Methods
Results
Discussion
References
![]()
MATERIALS AND METHODS
Top
Abstract
Introduction
Materials and Methods
Results
Discussion
References
1 (G418;
Roche Diagnostics) and incubated at 30°C. G418-resistant isolates
were tested for the proper integration of the kanMX cassette at the HXK2 locus by analytical PCR using the TaqPlus Long
PCR kit with the primers AK60 (GACGAAATACGCGATCGCTGT) and
AK61 (GCCGAACATTTCAAAGTCAACC) as recommended by the
manufacturer (Stratagene, La Jolla, Calif.).
Sample extraction. For the determination of the protein concentration, 1.2 ml of the culture was centrifuged for 1 min at 14,000 × g. The pellet was resuspended in 1.2 ml of 1 M NaOH.
Samples for the determination of extracellular metabolites were prepared by adding 100 µl of 35% (vol/vol) perchloric acid (PCA) to 1 ml of the culture supernatant. Samples were neutralized before analysis with 55 µl of 7 M KOH. After centrifugation (1 min at 14,000 × g) the supernatant was filtered through 0.45 µm (pore-size) nylon syringe filters (Alltech, Deerfield, Ill.). Samples for the determination of intracellular metabolites were prepared by addition of 100 µl of 35% (vol/vol) PCA to 600 µl of culture and put on ice. Samples were neutralized within an hour after extraction with 145 µl of 2 M K2CO3. For the preparation of enzyme extracts 10 ml of culture was centrifuged for 5 min at 4,000 × g at 4°C. The pellet was resuspended in 0.6 ml of 20 mM potassium phosphate buffer (pH 7) and extracted by vigorous shaking for 15 min with 0.5 g glass beads (diameter of ca. 0.45 × 10
3 m) at 4°C. To inhibit
serine protease activity, 1 µM phenylmethylsulfonyl fluoride (PMSF;
dissolved in dimethylsulfoxide [DMSO]) was added.
For the determination of mitochondrial H+-ATPase activity,
10 ml of culture was centrifuged for 5 min at 4,000 × g at 4°C. The pellet was resuspended in 100 µl of buffer
containing 500 mM mannitol, 1 mM ATP, 2 mM EDTA, 0.2% (wt/vol) bovine
serum albumin, 10% methanol, and 10 mM
-aminocaproic acid in 0.1 M
Tris-HCl (pH 7.5) and then extracted by vigorous shaking for 30 min
with 0.2-g glass beads (diameter of ca. 0.45 × 10
3
m) at 4°C (42). To inhibit protease activity, 1 µM
PMSF (in DMSO) was added. ATPase activity was measured in the complete extract.
Analyses. Protein concentrations were determined by the method of Lowry et al. (23) using fatty-acid-free bovine serum albumin (Sigma, St. Louis, Mo.) as a standard. Extracellular metabolites were determined by means of high-performance liquid chromatography (LKB, Bromma, Sweden) with a Rezex organic acid analysis column with an 8-µm particle size, 8% cross-linking, and a hydrogen ionic form (Phenomex, Torrance, Calif.) at a temperature of 45°C and with 7.2 mM H2SO4 as the eluent. Detection was done by using an RI-1530 refractive index detector (Jasco, Tokyo, Japan). Peak integration and data processing were done with Borwin (Le Fontanil, France) chromatography software. Intracellular metabolites were determined by NAD(P)H-coupled enzymatic reactions (2). Intracellular concentrations were calculated by assuming that 1 mg of protein corresponds to 3.75 µl of intracellular volume (9, 34, 39). Enzyme activities were determined at 30°C and pH 7.0 by NAD(P)H-coupled enzymatic reactions (38). Mitochondrial ATPase activity (azide-sensitive ATP hydrolysis) was determined by subtracting the azide-insensitive ATPase activity from the total ATPase activity. Total ATPase activity was measured at 30°C at pH 8.0 with 0.5 mM phosphoenolpyruvate, 6 mM MgCl2 · 6H2O, 85 mM sucrose, 5 mM ATP, 35 mM Tris-HCl, 0.3 mM NADH, 50 µM antimycin A, 5 U of pyruvate kinase per ml, and 5 U of lactate dehydrogenase per ml (42). The reaction was started with crude enzyme extract. The azide-insensitive ATPase activity was measured with the same reaction mixture in the presence of 5 mM NaN3. Protein, intracellular metabolites, and enzyme activities were measured on a COBAS-FARA automatic analyzer (Roche Diagnostics).
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RESULTS |
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Physiological changes.
During aerobic batch growth on 1%
glucose, distinct growth phases could be distinguished in wild-type
S. cerevisiae (Fig. 1; for a
description of wild-type yeast batch growth, see reference 22). In a first exponential growth phase, the glucose was
metabolized predominantly to ethanol and CO2, with the
minor products of fermentation being glycerol, acetate, and pyruvate
(Fig. 2 and 3). Both
the protein concentration and the optical density of the culture
increased exponentially at a rate of approximately 0.38 h
1. The specific CO2 evolution rate was 800 nmo1 min
1 mg of protein
1, and the specific
O2 consumption rate was 65 nmol min
1 mg
of protein
1, resulting in a respiratory quotient
(RQ, where RQ = CO2/O2) of approximately
12 during exponential growth (Fig. 3). This RQ is indicative of
respirofermentative growth. Only a small part of the glucose was
respired, whereas the rest was fermented primarily to ethanol. As a
consequence of the production of ethanol, which has a relatively high
energy content, the growth yield was low. On a C-molar basis, 71% of
the glucose was converted to ethanol and CO2, 2% was
converted to CO2 via the TCA cycle, 13% was converted to
biomass, 5% was converted to glycerol, 2% was converted to acetate,
and 0.5% was converted to pyruvate; which gives an incomplete carbon
recovery of 93.5%. At least a part of the missing carbon can be
accounted for by ethanol evaporation (i.e., substantial amounts of
ethanol were measured in the off-gas by means of a cold trap).
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1), and
it slowed further to a rate of 0.22 h
1 at later stages of
growth on glucose. The protein content per optical density unit was
lower in the hxk2 mutant during exponential growth on
glucose (between 5 and 25% more protein per optical density unit in
the wild-type yeast), possibly as a consequence of differences in the
cellular makeup between the wildtype and hxk2 mutant (e.g.,
storage carbohydrates). Most striking, during early exponential growth
the hxk2 mutant consumed much less glucose than the
wild-type strain, and no products of fermentation could be detected in
the culture supernatant (Fig. 2). During this period glucose was only
converted into biomass and CO2 in contrast to the wild
type, which produced ethanol during exponential growth on glucose. In
the hxk2 mutant glucose was completely converted by
oxidative metabolism, as evidenced by an RQ of 1 (Fig. 3).
The hxk2 mutant decreased O2 uptake rate and
increased CO2 evolution, resulting in an increase in the RQ
to a maximum of 2.5, which is still much lower than for the wild type
during fermentative growth. These changes in gas metabolism coincided
with the production of fermentative products such as ethanol, acetate,
glycerol, and pyruvate (Fig. 2). On a C-molar basis, 25% of the
glucose was converted to ethanol and CO2, 14% was
converted to CO2 via the TCA cycle, 48% was converted to
biomass, 6% was converted to glycerol, and 6% was converted to
acetate (carbon recovery of 99%).
After glucose exhaustion and a lag period, which is shorter than for
the wild type (Fig. 1 and 3), the hxk2 mutant metabolized and grew on the fermentative products of glucose metabolism. As in the
wild type, this process occurred with an RQ of ca. 0.6. The growth on
fermentative products was shorter than for the wild-type cells since
the amount of fermentative products produced was lower during the
preceding exponential growth on glucose. As with the wild-type, a small
increase in the RQ was observed at the end of growth as a consequence
of acetate metabolism.
We measured growth, glucose consumption, and the start of ethanol
production by the hxk2 mutant at initial glucose
concentrations of between 0.5 and 8%. The exponential growth rates of
both the wild-type and the hxk2 mutant strains decreased
with increasing initial glucose concentrations. The growth rate of the
wild-type decreased from 0.39 h1 at 0.5% initial glucose
to 0.34 h
1 at 8% initial glucose, and for the
hxk2 mutant it decreased from 0.32 h
1 at 0.5%
initial glucose to 0.18 h-1 at 8% initial glucose. The
onset of ethanol production was not associated with the residual
concentration of glucose (results not shown). Additionally, the onset
of ethanol production was not a consequence of an insufficient
dissolved oxygen tension during batch growth on 1% glucose. Dissolved
O2 did not drop below 90% of air saturation during any
stage in growth for either the wild-type or the hxk2 mutant
strains (results not shown). The onset of ethanol production was
associated with the biomass concentration of the cultures and started
at a protein concentration of approximately 0.25 g
liter
1 irrespective of the initial glucose concentration.
Intracellular changes.
In both the wild type and the
hxk2 mutant the metabolite pattern continuously changes
during growth on 1% glucose (Fig. 4). The intracellular concentrations of glucose-6-phosphate,
fructose-6-phosphate, and ATP decreased during exponential growth
on glucose in both strains. The intracellular concentration of
fructose-1,6-bisphosphate decreased in the wild type but remained
relatively low and constant in the hxk2 mutant. The total
concentration of the adenine nucleotides decreased in both the
wild-type strain and the hxk2 mutant. The concentrations of
ADP and AMP were marginally higher in the hxk2 mutant. The
onset of fermentation in the hxk2-null mutant coincided with
an intracellular accumulation of pyruvate. From a comparison between
the culture supernatant and an extract of the total culture we
concluded that pyruvate accumulated intracellularly and was not
excreted, whereas the wild type excreted the pyruvate (data not shown
and Fig. 2); levels of up to 40 mM intracellular pyruvate were estimated.
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DISCUSSION |
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Aerobic batch growth on 1% glucose of wild-type S. cerevisiae is characterized by respirofermentative metabolism. The energy necessary for exponential growth is partly generated by respiration (i.e., the oxidation of glucose to CO2 via the TCA cycle and oxidative phosphorylation) and partly by fermentation (i.e., the conversion of glucose to fermentative products, primarily ethanol). Oxidative growth yields more ATP per glucose molecule than fermentative growth. The production of ethanol from glucose under aerobic growth conditions is referred to as the Crabtree effect. The Crabtree effect has been ascribed to a limited capacity of the mitochondrial respiratory chain or to an overflow of metabolism at the level of pyruvate (29). In the industrial production of yeast biomass the formation of ethanol is undesirable, and industrial fermentations are designed to avoid it. The production of ethanol (or other metabolites) is accompanied by reduction of biomass yield and is related to inhibition of yeast growth and poor performance during subsequent fermentation (43). Furthermore, the production of fermentative products results in a diauxic shift; first, the cells grow on glucose, and then they have to adapt to growth on the fermentative products. Production of fermentative products can be avoided by means of fed batch cultivation of the yeast. The culture is fed below a critical dilution rate and is mixed vigorously by aeration to avoid local high concentrations of glucose and/or low concentrations of dissolved O2.
Yeast strains with (null) mutations in HXK2 have a reduced growth rate and reduced glucose repression at higher glucose concentrations (this study and reference 12). This reduction suggests that hexokinase II and/or glucose repression are necessary to regulate glucose metabolism for fast growth at high external glucose concentrations. However, elimination of hexokinase II, an enzyme central in glucose repression, does not result in severe growth defects or apparent changes in cell morphology (results presented in this study and results not shown). Instead, a yeast strain with a null mutation in HXK2 displays fully oxidative growth at high glucose concentrations in early exponential batch cultures, resulting in an initial absence of fermentative products such as ethanol, a postponed and shortened diauxic shift, and higher biomass yields.
Changes in intracellular properties resulting from the absence of the hexokinase II protein are apparent (this study and references 11, 12, 20, 26-28, and 37). Hexokinase II is the dominant hexose-phosphorylating enzyme during exponential growth on glucose. Only when glucose declines do the other hexose-phosphorylating enzymes, hexokinase I and glucokinase, appear (14, 16). Mutations in the genes encoding hexokinase I (HXK1) and glucokinase (GLK1) do not have significant effects on glucose repression. However, overexpression of HXK1 can restore glucose repression in an hxk2 mutant (35). Overproduction of glucokinase on the other hand was not sufficient to restore glucose repression. Hexokinase I, like hexokinase II but in contrast to glucokinase, exists in both monomeric and dimeric states (25). This similarity suggests that the hexose-phosphorylating activity itself is not directly related to glucose repression, yet there might be a relation between the presence of the different oligomers and glucose repression. In this study we show that the hxk2 mutant and the wild type have comparable hexose-phosphorylating activities during exponential growth on glucose. This finding contradicts the hypothesized relationship between glucose repression and hexose-phosphorylating capacity. However, the in vitro phosphorylating capacity might be similar in the different strains, yet the affinities of the glucose-phosphorylating enzymes differ strongly (21), thus the in vivo phosphorylating activity or the resulting metabolite pools cannot be excluded as direct regulators of glucose repression.
During growth on glucose, the fructose-phosphorylating activity of the hxk2 mutant increases, while the glucose-phosphorylating activity remains constant. This result suggests an increase in hexokinase I, since fructose is not phosphorylated by glucokinase and the ratio of fructose over glucose phosphorylation is ca. 1.3 for hexokinase II and ca. 3 for hexokinase I (16).
High-affinity glucose transport is subject to glucose repression (3, 4, 33). In wild-type yeast the kinetics of glucose transport are determined predominantly by low-affinity transporters at high concentrations of glucose. When the glucose concentration declines, glucose is transported primarily by high-affinity transporters (e.g., references 10 and 46). In a strain in which HXK2 is deleted, high levels of high-affinity glucose transporters are found even at high concentrations of glucose (3, 28). Steady-state intracellular metabolite levels are determined by the transport step and the subsequent metabolic machinery. The changes in inhibition of hexokinase activity by trehalose-6-phosphate or in the interaction with trehalose-6-phosphate synthase and the presence of high-affinity glucose transport activity in the hxk2-null mutant during growth at high glucose concentrations may change the concentration of intracellular metabolites (e.g., intracellular glucose or glucose-6-phosphate) and thereby relieve glucose repression.
Both intracellular glucose and glucose-6-phosphate might act as signal molecules for glucose repression. Entian et al. (12) showed that intracellular concentrations of glucose-6-phosphate, fructose-6-phosphate, and fructose-1,6-bisphosphate are comparable in the wild-type and the hxk2 mutant grown on different carbon sources. However, intracellular metabolites were not monitored during growth but were measured in cells harvested at an arbitrary point (after 36 h of growth). In our experiments, both glucose and ethanol metabolism were finished by 36 h, which may indicate that in the experiment described by Entian et al. the cells were no longer exponentially growing on glucose. Here we show that the concentrations of glucose-6-phosphate, fructose-6-phosphate, and ATP change during growth on 1% glucose and yet are comparable in the wild type and in the hxk2-null mutant.
The ATP/AMP ratio might act as a signal for glucose repression by modulating the Snf1 kinase activity (47). The Snf1 kinase is required for the transcription of glucose-repressed genes. However, the role of the ATP/AMP ratio in glucose repression has been called into question (13). In our experiments, the ATP/AMP ratios are similar in the wild type and in the hxk2 mutant, in spite of the dramatically different states of glucose repression, which suggests that the hypothesis that the ATP/AMP ratio triggers glucose repression is incorrect.
The concentration of fructose-1,6-bisphosphate decreased in wild-type yeast during growth on glucose. In the hxk2 mutant the concentration of fructose-1,6-bisphosphate is lower than in the wild type during growth in glucose medium. Fructose-1,6-bisphosphate is an allosteric activator of pyruvate kinase. Pyruvate kinase is the enzyme that converts phosphenolpyruvate into pyruvate in the last step of glycolysis. The reduced levels of pyruvate decarboxylase and the decreased activation of pyruvate kinase in the hxk2 mutant might be directly responsible for the redirection of carbon flux from the production of ethanol to the production of biomass.
In the wild type the culture density and culture protein concentration remained constant for approximately 5 h after glucose exhaustion. During this diauxic shift the O2 consumption and CO2 evolution decreased strongly; however, they increased again soon, a finding indicative of the reinitiation of metabolism, yet the arrest in growth persisted (Fig. 1 and 3). This lag indicates that the adaptation, involving the conversion of enzymes of the metabolic machinery, is an energy-consuming process. In the hxk2 mutant the adaptation period seemed to be ca. 1 hour (Fig. 1 to 3), which suggests that at least some of the mRNA or enzymes necessary for growth on ethanol were already present. This hypothesis is confirmed by the depressed mitochondrial H+-ATPase activity.
The hxk2 mutant began fermentation after the glucose had been partially consumed. This delay was unexpected, since as the concentration of glucose declines during growth we expected glucose repression and flux through glycolysis to decline as well. Possible explanations for these results include: (i) the dissolved O2 concentration may have been too low, resulting in a limited supply of O2 at elevated concentrations of biomass; (ii) a vitamin or nutrient other than glucose may have been depleted after a certain amount of biomass was produced (30); or (iii) intracellular accumulation of metabolites may have caused an overflow of metabolism into fermentation or else affected the expression of particular genes, e.g., the accumulation of intracellular glucose may result in glucose repression.
For the oxidative degradation of glucose to CO2 and biomass, O2 must be present. Oxygen limitation forces yeast to fermentative glucose metabolism to acquire energy for growth. However, in our experiments, the dissolved O2 levels never dropped below 90% (both in the wild type and in the hxk2 mutant strains); therefore, we conclude that the O2 supply was not limiting.
The intracellular accumulation of pyruvate in the hxk2 mutant during growth on glucose was unexpected. Apparently, the hxk2 mutant either actively transports pyruvate back into the cell or is unable to excrete pyruvate effectively (see reference 30). The ongoing accumulation of pyruvate might result in the overflow of metabolism to the production of ethanol, which is initially not present as a result of the low pyruvate decarboxylase activity.
Furthermore, the increase in hexokinase I activity during growth on glucose in the hxk2 mutant may be responsible for glucose repression at the onset of ethanol production.
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ACKNOWLEDGMENTS |
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We thank Arthur Kuiper for technical assistance and acknowledge Joost Teixeira de Mattos for critically reading the manuscript.
This work was supported by the Foundation for Chemical Research (SON), which is subsidized by The Netherlands Organization for Scientific Research (NWO), The Netherlands Association for Biotechnological Research Centers (ABON), and the European Union through grant no. BIO4-CT95-0107 of the BIOTECH program.
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FOOTNOTES |
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* Corresponding author. Mailing address: Instituut voor Interdisciplinaire Opleidingen (I2O), Sarphatistraat 104, 1018 GV Amsterdam, The Netherlands. Phone: 31 (20) 525 5510. Fax: 31 (20) 525 5505. E-mail: k.van.dam{at}chem.uva.nl.
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