- Open Access
Competition between pentoses and glucose during uptake and catabolism in recombinant Saccharomyces cerevisiae
© Subtil and Boles; licensee BioMed Central Ltd. 2012
- Received: 21 September 2011
- Accepted: 16 March 2012
- Published: 16 March 2012
In mixed sugar fermentations with recombinant Saccharomyces cerevisiae strains able to ferment D-xylose and L-arabinose the pentose sugars are normally only utilized after depletion of D-glucose. This has been attributed to competitive inhibition of pentose uptake by D-glucose as pentose sugars are taken up into yeast cells by individual members of the yeast hexose transporter family. We wanted to investigate whether D-glucose inhibits pentose utilization only by blocking its uptake or also by interfering with its further metabolism.
To distinguish between inhibitory effects of D-glucose on pentose uptake and pentose catabolism, maltose was used as an alternative carbon source in maltose-pentose co-consumption experiments. Maltose is taken up by a specific maltose transport system and hydrolyzed only intracellularly into two D-glucose molecules. Pentose consumption decreased by about 20 - 30% during the simultaneous utilization of maltose indicating that hexose catabolism can impede pentose utilization. To test whether intracellular D-glucose might impair pentose utilization, hexo-/glucokinase deletion mutants were constructed. Those mutants are known to accumulate intracellular D-glucose when incubated with maltose. However, pentose utilization was not effected in the presence of maltose. Addition of increasing concentrations of D-glucose to the hexo-/glucokinase mutants finally completely blocked D-xylose as well as L-arabinose consumption, indicating a pronounced inhibitory effect of D-glucose on pentose uptake. Nevertheless, constitutive overexpression of pentose-transporting hexose transporters like Hxt7 and Gal2 could improve pentose consumption in the presence of D-glucose.
Our results confirm that D-glucose impairs the simultaneous utilization of pentoses mainly due to inhibition of pentose uptake. Whereas intracellular D-glucose does not seem to have an inhibitory effect on pentose utilization, further catabolism of D-glucose can also impede pentose utilization. Nevertheless, the results suggest that co-fermentation of pentoses in the presence of D-glucose can significantly be improved by the overexpression of pentose transporters, especially if they are not inhibited by D-glucose.
The cost effective production of fuels and chemicals from plant biomass requires efficient conversion of all sugars present in the raw materials. While cornstarch or sugarcane hydrolyzates mainly consist of hexoses, hydrolyzates from lignocellulosic biomass also contain pentose sugars like D-xylose or L-arabinose. The yeast Saccharomyces cerevisiae, traditionally used for industrial ethanol production lacks the ability to ferment pentoses. However, intensive research and genetic engineering approaches during the last years improved the capability of S. cerevisiae for pentose utilization.
D-xylose fermentation by S. cerevisiae was first achieved by expression of a xylose reductase (XR) and a xylitol dehydrogenase (XDH) from Scheffersomyces stipitis. However differences in co-factor specificities of the two enzymes can result in co-factor imbalances, production of varying amounts of xylitol and therefore reduced ethanol yields [1–4]. Another strategy used heterologous expression of genes encoding xylose isomerases. Fungal as well as bacterial xylose isomerases could be functionally expressed and enabled the yeast cells to ferment D-xylose efficiently [5–8].
L-arabinose utilization in S. cerevisiae has been achieved by introducing multi-step oxidoreductive fungal or multi-step bacterial pathways. Similarly to the fungal D-xylose utilization pathway, the fungal L-arabinose pathway employs NADPH- and NADH-dependent redox reactions resulting in severe co-factor imbalances  which could be avoided by introduction of bacterial L-arabinose pathways [10, 11].
The expression of pentose converting enzymes in S. cerevisiae is not sufficient for optimal pentose fermentation. Overexpression of xylulokinase or genes of the non-oxidative part of the pentose phosphate pathway turned out to be beneficial as well as overexpression of uptake systems able to transport pentoses [12–15]. Nevertheless, co-consumption of pentoses with D-glucose is still limited and normally S. cerevisiae does not utilize pentoses before D-glucose depletion. This has been attributed to competiton of the sugars during their uptake into the cells. Pentoses like D-xylose and L-arabinose are taken up by S. cerevisiae cells via their hexose uptake systems [14, 16]. Due to the preference of the transporters for D-glucose, pentose uptake is competitively inhibited by D-glucose. Unfortunately, up to now no specific pentose transporters could be functionally expressed in yeast which specifically mediate uptake of only pentoses into S. cerevisiae cells but are not able to transport hexoses or are not inhibited by D-glucose [15, 17–21]
It has never been analyzed whether D-glucose inhibits pentose utilization only during sugar uptake or whether also D-glucose metabolism impairs the simultaneous utilization of pentose sugars. Here we describe the impact of intracellular D-glucose as well as extracellular D-glucose and D-glucose metabolism on pentose utilization in yeast strains expressing bacterial D-xylose and L-arabinose pathways. We used maltose as a non-competitive carbon source as well as hexo-/glucokinase deletion strains to selectively block D-glucose catabolism. Our analyses demonstrate that sugar uptake is the main competitive step to impair co-consumption of pentoses together with D-glucose. Moreover, we demonstrate that overexpression of pentose-transporting hexosetransporters like Hxt7 and Gal2 partially relieves the inhibitory effect of D-glucose on pentose utilization.
The influence of hexose catabolism on pentose utilization in recombinant S. cerevisiae cells
It has been shown that pentoses like D-xylose and L-arabinose are taken up by S. cerevisiae cells via their hexose uptake systems [12, 14, 21, 22]. However, the yeast hexose transporters generally have lower affinities for pentoses than for hexoses . Therefore, it is believed that co-consumption of D-glucose and pentoses is impaired due to the preference of the uptake systems for D-glucose and its competition with pentose sugars. Nevertheless, it has never been investigated whether the further steps of pentose catabolism might also be impaired by the simultaneous catabolism of D-glucose. D-glucose and pentose catabolism share all the enzymes from glycolysis starting with phosphofructokinase.
To distinguish between inhibitory effects of D-glucose on pentose uptake and further pentose catabolism we used maltose as an alternative carbon source in maltose-pentose co-consumption experiments. Maltose is taken up by specific maltose permeases [23, 24] and only hydrolyzed intracellularly by maltases into two D-glucose molecules which are then normally channeled into the glycolytic pathway by hexo-/glucokinases. Therefore, unlike D-glucose maltose utilization does not compete with pentose utilization at the transport level. On the other hand, as transcription of most of the yeast hexose transporters which are able to transport pentoses with sufficient capacities  must normally be induced by glucose or galactose, such transporters had to be overexpressed constitutively in order to ensure sufficient pentose uptake.
Recombinant D-xylose and L-arabinose utilizing strains BWY1-XT and BWY1-AT, respectively, were constructed. Strain BWY1 is derived from CEN.PK2-1 C and has been obtained by evolutionary engineering for improved L-arabinose utilization after expression of genes for a bacterial L-arabinose metabolizing pathway [10, 11]. For D-xylose utilization BWY1 was transformed with plasmids overexpressing a codon-optimized version of the Clostridium phytofermentans xylose isomerase gene , the xylulokinase gene of the fungus Hypocrea jecorina and the yeast hexose transporter gene HXT7 which has been shown to be able to support uptake of D-xylose , resulting in BWY1-XT. For L-arabinose utilization BWY1 was transformed with plasmids overexpressing an optimized bacterial L-arabinose catabolic pathway  and the yeast D-galactose transporter gene GAL2 which has been shown to be able to support uptake of L-arabinose , resulting in BWY1-AT. The strains BWY1-XT and BWY1-AT were able to use D-xylose or L-arabinose, respectively, as the sole carbon and energy sources.
The influence of intracellular D-glucose levels and D-glucose phosphorylation on pentose utilization
D-glucose catabolism might impede simultaneous pentose utilization through inhibition by intracellular D-glucose of enzymes of the D-xylose or L-arabinose catabolic pathways. Especially in the case of D-xylose utilization this is not implausible as xylose isomerases also act as bona fide glucose isomerases . Moreover, intracellular D-glucose could be transported out of the cells via the hexose transporters , and therefore efflux of D-glucose or binding of intracellular D-glucose to the hexose transporters might interfere with pentose uptake.
In order to test possible inhibitory effects, the level of intracellular D-glucose should be raised by eliminating D-glucose phoshorylation. In yeast D-glucose is specifically phosphorylated by hexo- and glucokinases. In contrast, D-xylose must first be converted into D-xylulose which is then phosphorylated by xylulokinase. L-arabinose is first converted into L-ribulose which subsequently is phosphorylated by ribulokinase. Again maltose should be used as the carbon source in order to avoid inhibitory effects of extracellular D-glucose on the uptake of pentoses. Moreover, it has been shown before that hexo-/glucokinase deficient yeast mutants accumulate high intracellular levels of D-glucose when incubated with maltose [27, 28].
In S. cerevisiae three genes encoding enzymes with hexo-/glucokinase activity are known, HXK1, HXK2 and GLK1[29–31]. To block D-glucose phosphorylation all three genes were deleted in the strain BWY1 by using a recyclable loxP-kanMX-loxP resistance marker , resulting in strain TSY10. The growth properties of TSY10 were characterized on synthetic solid media with various hexoses (D-glucose, D-fructose, D-mannose, D-galactose) as well as maltose or ethanol as carbon sources. TSY10 was also transformed with the plasmids expressing xylose isomerase and xylulokinase, resulting in TSY10-X, and with the plasmids expressing an optimized bacterial L-arabinose catabolic pathway, resulting in TSY10-A, and growth on synthetic solid media with D-xylose and L-arabinose was characterized.
Extracellular D-glucose inhibits pentose consumption
D-xylose is taken up into yeast cells by high- and intermediate-affinity hexose transporters but which have lower affinities for D-xylose than for D-glucose [14, 16]. L-arabinose is taken up mainly by the D-galactose transporter Gal2 [21, 22], which also transports D-glucose with high affinity . As we already ruled out the possibility that intracellular D-glucose levels impede pentose utilization, we next wanted to test the effect of extracellular D-glucose irrespectively of its further catabolism.
Using the hexo-/glucokinase deletion strains, inhibition of pentose consumption was analyzed by adding increasing amounts of D-glucose to the media. As we observed an incidental occurrence of suppressor mutations enabling cells of the hexo-/glucokinase deletion strain to regain their ability to grow on D-glucose media and to utilize D-glucose as the preferred carbon source low amounts of 2-deoxy-glucose (2-DOG), a phosphorylatable but non-metabolizable analogue of D-glucose [35–37], were added to the growth media. Growth of yeast cells is strongly inhibited by 2-DOG but only after its phosphorylation by hexo-/glucokinases. Addition of 2-DOG should ensure that during long term cultivations cells with suppressor mutations could not further propagate and overgrow the cultures. Indeed, already minor amounts of 2-DOG (0.5 g/L) completely blocked growth of hexo-/glucokinase wild-type strains BWY1-X and BWY1-A on D-xylose and L-arabinose, respectively, whereas they did not affect growth and pentose consumption of the corresponding hexo-/glucokinase deletion strain TSY10-X and TSY10-A. Therefore, in all experiments with D-glucose 0.5 g/L 2-DOG was added.
Overexpression of hexose transporters improve pentose utilization in the presence of D-glucose
As consumption of pentoses in the presence of low extracellular D-glucose concentrations was possible, we investigated whether overexpression of Hxt7 or Gal2, transporters with the highest capacities for D-xylose and L-arabinose uptake, respectively [12, 14, 21] might improve pentose utilization in the presence of D-glucose. TSY10-X and TSY10-A were additionally transformed with multicopy vectors expressing HXT7 and GAL2, respectively, both regulated by strong constitutive promoters.
Co-consumption of D-xylose and D-glucose
All so far described recombinant pentose utilizing yeast strains consume pentoses much slower than D-glucose which normally is consumed in only a few hours where pentose utilization just begins to become measurable [38–40]. Therefore, in batch cultures it is difficult to analyze whether those strains are able to co-consume the sugars or not. In order to test this in batch cultures, we aimed to decrease D-glucose consumption to levels similar to pentose consumption. For this, we first wanted to stabilize the hexo-/glucokinase deletion strain genetically. In addition to HXK1, HXK2 and GLK1, one poorly characterized gene, YLR446W, exhibiting homologies to hexokinases had been found in the yeast genome sequence . Although our results indicated that this gene is not directly involved in D-glucose phosphorylation we speculated that it might be involved in the occurrence of the incidental suppressor mutations, and therefore we additionally deleted YLR446W in strain TSY10. The resulting quadruple deletion strain TSY11 exhibited the same growth and fermentation properties as the triple deletion strain TSY10 (data not shown).
Introduction of pentose catabolic pathways into S. cerevisiae enabled this yeast to ferment the lignocellulosic pentoses D-xylose and L-arabinose into ethanol. However, low fermentation rates compared to D-glucose and a lack of pentose utilization in the presence of high D-glucose concentrations are still major obstacles for fermentation of mixed sugar hydrolyzates [38–40]. It is generally assumed that competitive inhibition of pentose uptake by D-glucose is the main problem for simultaneous co-fermentation of D-glucose and pentoses.
To investigate the influence of further D-glucose metabolism on pentose utilization independent of the competition at the uptake level we used the alternative carbon source maltose as a non-competitive transport substrate. Indeed, we found that pentose consumption was impaired by simultaneous maltose utilization (Figure 1). As maltose did not impair pentose utilization in a hexo-/glucokinase mutant strain an inhibitory effect of maltose on pentose uptake can clearly be excluded. Hexose and pentose catabolism converge at the level of phosphofructokinase. Therefore, hexose catabolism might impair pentose utilization on the level of a limiting glycolytic enzyme activity. On the other hand, hexose catabolism could negatively affect regulation of enzymes of the pentose phosphate pathway used for the catabolism of pentoses. Moreover, the results do not exclude the possibility that during the utilization of D-glucose when fluxes are higher than during the utilization of maltose there might be an even stronger impact of D-glucose catabolism on pentose utilization.
Xylose isomerases are well known to also act as bona fide glucose isomerases converting D-glucose into D-fructose . Therefore, it might be possible that intracellular D-glucose competes with D-xylose at the level of xylose isomerase. Moreover, it is known that intracellular D-glucose can be transported out of the cells via the hexose transporters . Therefore, increased levels of D-glucose within the cells might negatively influence pentose uptake. In this sense, recently it has been shown that the binding of intracellular D-glucose inhibits the yeast D-glucose sensor Snf3 which has high homologies with the hexose transporters . However, our results with hexo-/glucokinase mutant strains in the presence of maltose could prove that even increased intracellular D-glucose levels did not interfere with pentose isomerization or uptake.
Pentose consumption analyses of the hxk/glk null strains confirmed that extracellular D-glucose inhibits pentose consumption in a concentration dependent manner. Increasing concentrations of D-glucose gradually decreased pentose consumption, both in the case of D-xylose as well as L-arabinose (Figure 4). Nevertheless, this experiment and also the co-consumption experiment with the hexokinase-limited mutant strain clearly show that principally co-consumption is possible as long as D-glucose concentrations are low enough.
Accordingly, overexpression of those hexose transporters with a high capacity for D-xylose uptake, Hxt7 [12, 14], or L-arabinose uptake, Gal2 , partially relieved the inhibitory effects of extracellular D-glucose (Figure 5). Especially in the case of L-arabinose consumption it turned out that constitutive overexpression of GAL2 was quite beneficial. This probably is mainly due to the strong repression of the endogenous GAL2 gene in the presence of D-glucose [44–46]. Gal2 is the only hexose transporter of S. cerevisiae that can effectively transport L-arabinose [21, 22]. Therefore, a constitutive overexpession of GAL2 is a prerequisite to allow efficient L-arabinose uptake in the presence of D-glucose. In the case of D-xylose, most of the D-xylose-transporting hexose transporters like HXT7 are even inducible by low concentrations of D-glucose but are repressed by high concentrations [47, 48]. This might explain why D-xylose consumption was less inhibited than L-arabinose consumption by low concentrations of D-glucose as these even induced higher D-xylose transport capacities. Indeed, this would also be in accordance with earlier observations demonstrating that low glucose concentrations (down to 0.1 g/L) increase xylose utilization  although we could not observe this with the lowest glucose concentrations used in our study (1 g/L). It was speculated that, beside other effects, increased xylose uptake might be responsible for this.
Our results show that co-fermentation of D-glucose and pentoses can be improved either by keeping D-glucose concentrations on a low level or by the expression of specific heterologous pentose transporters that are not inhibited by D-glucose. Indeed, using prefermentation and fed-batch systems to minimize initial D-glucose concentrations D-xylose utilization could recently be increased in a simultaneous saccharification and co-fermentation (SSCF) process [50, 51]. Moreover, in E. coli co-consumption of D-glucose and D-xylose could be demonstrated just by eliminating catabolite repression by D-glucose of D-xylose specific transporters xylE or xylFGH [52, 53]. On the other hand, Ha et al.  recently engineered a xylose fermenting S. cerevisiae strain for simultaneous fermentation of xylose and cellobiose by expressing a specific cellobiose transporter together with an intracellular β-glucosidase.
For future perspective, a pentose-fermenting hexo-/glucokinase deletion strain might be an interesting screening system to select for mutants able to ferment pentoses in the presence of increasing concentrations of D-glucose, e.g. via evolutionary engineering . Reintroduction of hexokinase activity should then result in strains able to consume pentoses even in the presence of higher concentrations of D-glucose.
Our results suggest that co-fermentation of pentoses in the presence of D-glucose can significantly be improved by the overexpression of pentose transporters, especially if they are specific for the pentoses and not inhibited by D-glucose. On the other hand, this could lead to other limitations further downstream in the co-metabolism of both kind of sugars.
Strains and media
S.cerevisiae strains and plasmids used in this study
S. cerevisiae strain or plasmid
Relevant genotype or phenotype
Source or reference
MAT a leu2-3,112 ura3-52 trp1-289 his3- _1 MAL2-8 c SUC2
MAT a leu2-3,112 ura3-52 trp1-289 his3- _1 MAL2-8 c SUC2; unknown beneficial mutations for L-arabinose utilization
BWY1 with plasmids YEplac181_opt.Xi, p423pPGK1-XKS Tr
BWY1 with plasmids p423H7-synthIso, p424H7-synthKin, p425H7-synthEpi
BWY1 with plasmids YEplac181_opt.Xi, p423pPGK1-XKS Tr, p426_HXT7
BWY1 with plasmids p423H7-synthIso, p424H7-synthKin, p425H7-synthEpi and pHL125re
MAT a leu2-3,112 ura3-52 trp1-289 his3- _1 MAL2-8 c SUC2 Δhxk1::loxP
Δglk1::loxP Δhxk2::loxP; unknown beneficial mutations for L-arabinose utilization
TSY10 with plasmids YEp181_pHXT7-optXI_Clos and p423pPGK1-XKS Tr
TSY10 with plasmids YEp181_pHXT7-optXI_Clos, p423pPGK1-XKS Tr and p426_HXT7
TSY10 with plasmids p423H7-synthIso, p424H7-synthKin and p425H7-synthEpi
TSY10 with plasmids p423H7-synthIso, p424H7-synthKin, p425H7-synthEpi and pHL125re
MAT a leu2-3,112 ura3-52 trp1-289 his3- _1 MAL2-8 c SUC2 Δhxk1::loxP
Δglk1::loxP Δhxk2::loxP Δylr446w::loxp-kanMX-loxp; unknown beneficial mutations for L-arabinose utilization
TSY11 with plasmids YEp181_pHXT7-optXI_Clos, p423pPGK1-XKS Tr, p426_HXT7 and pRS314pUBR2-HXK1
2 μ-plasmid; URA3 marker gene
DNA-template for amplification of HXT7
2 μ-plasmid; HXT7 under control of shortened HXT7-promoter and CYC1-terminator; URA3 marker gene
2 μ-plasmid; GAL2 under control of ADH1- pomoter, URA3 marker gene
2 μ-plasmid; codon-optimized araA of B. licheniformis under control of shortened HXT7-promoter and CYC1-terminator; HIS3 marker gene
2 μ-plasmid; codon-optimized araB of E. coli under control of shortened HXT7-promoter and CYC1-terminator; LEU2 marker gene
2 μ-plasmid; codon-optimized araD of E. coli under control of shortened HXT7-promoter and CYC1-terminator; TRP1 marker gene
DNA-template for amplification of loxP-kanMX-loxP gene resistance marker
Cre-recombinase under control of GAL1 promoter; URA3 marker gene
2 μ-plasmid; codon-optimized xylose isomerase gene of C. phytofermentans under control of shortened HXT7-promoter and CYC1-terminator; LEU2 marker gene
Boles, lab stock
2 μ-plasmid; xylulokinase gene of H. jecorina under control of PGK1-promoter and CYC1-terminator; HIS3 marker gene
Boles, lab stock
Yeast centromere vector; TRP1 marker gene
P. Kötter, Frankfurt, Germany
Yeast centromere vector; HXK1 of S. cerevisiae behind UBR2-promoter and HXK1-terminator; TRP1 maker gene
S. cerevisiae was grown in synthetic complete (SC) medium (1.7 g/L Difco yeast nitrogen base without amino acids and 5 g/L ammoniumsulfate), supplemented with amino acids but omitting the selective plasmid markers nutrients as described previously , containing various carbon sources.
For serial dilution growth assays, cells growing in exponential phase were collected and resuspended in sterile water to an OD600 nm of 1. Cells were serially diluted in 10-fold steps, and 5 μl of each dilution was spotted on agar plates. In aerobic batch cultivations, S. cerevisiae was grown in SC medium supplemented with maltose, D-glucose, D-xylose or L-arabinose as carbon sources and buffered at pH 6.3 with 20 mM KH2PO4. Plasmids were amplified in Escherichia coli strain DH5α (Gibco BRL, Gaithersburg, MD) or strain SURE (Stratagene, La Jolla, CA). E. coli transformations were performed via electroporation according to the methods of Dower et al., 1988 . E. coli was grown on LB (Luria-Bertani) medium with 40 μg/ml ampicillin for plasmid selection.
Construction of hxk-null strains
Primers used for gene deletions
Yeast transformations were carried out as described previously [58, 59]. As induction of the D-galactose-inducible, D-glucose-repressible Cre recombinase on plasmid pSH47 by D-galactose appeared to have deleterious effects on cells containing several loxP sites, we routinely used maltose (which has a weaker repressive effect than D-glucose) to induce/derepress loxP-Cre recombination. The hexokinase genes were deleted successively in the following order: HXK1, GLK1, HXK2 and YLR446W selecting for G418 resistance on yeast extract-peptone medium with 10 g/L maltose or 20 g/L ethanol (after deletion of GLK1).
Construction of plasmids
The coding region of HXT7 from S. cerevisiae was amplified by PCR from YEpkHXT7 and cloned into the linearized vector p426H7 (URA3) by recombination cloning, employing the procedure already used in Wieczorke et al. (29) and omitting the six histidine codons. The coding region of HXK1 with 300 bp downstream of the open reading frame was amplified with primers (HXK1_for_UBR2: 5'-TAGCTACTTAACAAGCACGCATGGTTCATTTAGGTCCAAAGAAACCACAGGC-3'; HXK1_Term_rev: 5'-GAAAAACCGTCTATCAGGGCGATGGCCCACTACGTGAACCATCACCAAAGCAATGGATTATGCCATAAG-3') from genomic DNA of CEN.PK2-1 C with homologous regions to the pRS314 vector at its 3'-end and to the UBR2-promoter at its 5'-end. For the UBR2-promoter a fragment of 500 bp upstream of the UBR2-open reading frame was amplified with primers (UBR2_Prom_for: 5'- GTGGAATTGTGAGCGGATAACAATTTCACACAGGAAACAGCTATCCCCCGTTTAGAGGAAGG -3'; UBR2_Prom_rev: 5'-GCCTGTGGTTTCTTTGGACCTAAATGAACCATGCGTGCTTGTTAAGTAGCTA -3') from genomic DNA of CEN.PK2-1 C with homologous regions to the open reading frame of HXK1 and to the pRS314 vector. Both fragments were fused by cloning them into the linearized (Bam HI, Xho I) pRS314 vector by recombination cloning. Yeast transformations of plasmid DNA from yeast cells were carried out as described above [58, 59]. Molecular techniques were performed according to published procedures .
Cultures (50 ml) were grown in 300-ml flasks at 30°C with constant shaking at 180 rpm. Precultures were grown in SC medium containing 20 g/L L-arabinose or 20 g/L D-xylose. Cells were washed with sterile water and inoculated in SC medium containing various combinations of carbon sources (L-arabinose, D-xylose, D-glucose, D-maltose, 2-deoxy-glucose). Dry biomass was determined by filtering 10 ml of the culture through a pre-weighted nitrocellulose filter (0.45 μm pore size; Roth, Germany). The filters were washed with demineralized water, dried in a microwave oven for 20 minutes at 140 W, and weighted again. All growth assays and sugar consumption analyses were carried out at least in duplicate.
The concentrations of sugars were determined by high-performance liquid chromatography (Dionex BioLC) using a Nugleogel Sugar 810 H exchange column (Macherey-Nagel GmbH & Co, Germany). The column was eluted at the temperature of 65°C with 5 mM H2SO4 as a mobile phase with a flow rate of 0.6 ml/min. Detection was done by means of a Shodex RI-101 refractive-index detector. Chromeleon software (version 6.50) was used for data evaluation.
We would like to thank Alexander Farwick (Goethe-University Frankfurt, Germany) for providing the plasmids YEp181_pHXT7-optXI_Clos and p423pPGK1-XKS Tr.
We thank Johannes Wess for his help in constructing the hexo-/glucokinase deletion strains. We thank Dr. Peter Kötter (Goethe-University Frankfurt, Germany) for providing the plasmid pRS314. Part of this work has been supported by the EC 7th Framework program (NEMO project) and Butalco GmbH, Huenenberg, Switzerland.
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