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Applied and Environmental Microbiology, February 2003, p. 740-746, Vol. 69, No. 2
0099-2240/03/$08.00+0 DOI: 10.1128/AEM.69.2.740-746.2003
Copyright © 2003, American Society for Microbiology. All Rights Reserved.
Department of Applied Microbiology, Lund University, Lund, Sweden,1 Department of Microbiology, University of Stellenbosch, Stellenbosch, South Africa2
Received 15 April 2002/ Accepted 10 September 2002
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Recently, a diploid strain of S. cerevisiae (26) was transformed with the genes coding for xylose reductase (XR) and xylitol dehydrogenase (XDH) from the xylose-utilizing yeast Pichia stipitis, as well as with the S. cerevisiae gene encoding xylulokinase (XK) (29a). The resulting transformant, S. cerevisiae TMB 3399, had a maximum specific growth rate of 0.025 h-1 when cultivated in a defined mineral medium supplemented with xylose. Chemical mutagenesis using ethyl methanesulfonate generated mutants with improved growth rate and xylose utilization. The best mutant selected was designated S. cerevisiae TMB 3400 and showed a >5-fold increase in growth rate, 0.14 h-1, when cultivated under the same conditions as S. cerevisiae TMB 3399. The mutant, S. cerevisiae TMB 3400, also showed lower xylitol production than S. cerevisiae TMB 3399 when the strains were cultivated on xylose under oxygen-limited and anaerobic conditions.
Microarray technology permits the quantification of genome-wide mRNA expression (31). The technique offers the possibility to characterize differences in transcription level as a function of strain difference or cultivation condition. In S. cerevisiae, microarray technology has, among other things, been used to compare the mRNA expression during growth under aerobic and anaerobic conditions (25) and during a shift from growth on a fermentable carbon source to growth on a nonfermentable carbon source (10).
To identify genes beneficial for growth on xylose, microarray technology was used to compare mRNA expression in S. cerevisiae TMB 3399 and TMB 3400, as well as the growth of these two strains on glucose and xylose. S. cerevisiae TMB 3399 was cultivated in batch and chemostat cultures at a dilution rate of 0.1 h-1 in a defined mineral medium supplemented with either glucose or a mixture of glucose and xylose. S. cerevisiae TMB 3400 was cultivated under the same conditions, as well as by using a feed containing only xylose. At steady state, samples were withdrawn for microarray analysis; analysis of XR, XDH, and XK activities; and analysis of substrate consumption and product formation.
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S. cerevisiae TMB 3399 and S. cerevisiae TMB 3400 were stored at -80°C and streaked on yeast extract-peptone-dextrose plates 1 day prior to the inoculation of the precultures. A defined mineral medium, including vitamins and trace elements, was used in all fermentation experiments (27). The carbon and energy source consisted of either 10 g of glucose, 10 g of glucose plus 10 g of xylose, or 20 g of xylose liter-1. Antifoam (Dow Corning Antifoam RD Emulsion; BDH Laboratory Supplies, Poole, England) was added at a concentration of 0.5 ml per liter.
The precultures consisted of 100 ml of medium containing 10 g of glucose liter-1 in 1,000-ml baffled shake flasks. They were incubated at 30°C and 140 rpm in an orbital incubator (INR-200; Gallenkamp, Leicester, United Kingdom). The precultures used for the cultivation of S. cerevisiae TMB 3400 on pure xylose were cultivated under the same conditions but with 20 g of xylose liter-1 as the carbon source. The bioreactors were inoculated with 20 mg of cells harvested in the late exponential phase liter-1.
Batch and chemostat fermentation was conducted at 30°C in 2-liter Biostat A bioreactors (B. Braun Biotech International, Melsungen, Germany). The working volume of the bioreactors was 1,200 ml, and 3 M NaOH was used to automatically maintain the pH at 5.5. The airflow rate of 1 liter min-1 was controlled by mass flow meters (HI-TECH; Bronkhorst, Ruurlo, The Netherlands), and the dissolved oxygen tension was at least 30% of the maximum. Duplicate fermentation experiments were performed for each feed composition.
Sampling, preparation of cRNA, microarray analysis, and analysis of substrates and products.
Steady-state conditions were assumed when the carbon dioxide evolution, oxygen consumption, and OD620 had remained constant for three consecutive volume changes. This occurred at least six volume changes after feed initialization or feed change. Samples were then withdrawn for microarray analysis (2 x 50 ml), enzymatic assays (50 ml), and for the analysis of dry weight, substrate consumption and product formation (50 ml). The biomass concentrations were between 5 and 8 mg ml-1 (Table 1).
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TABLE 1. Feed concentrations, residual substrate concentrations, and specific productivities from chemostat cultivation of S. cerevisiae strains TMB 3399 and TMB 3400 as determined with glucose and xylose as the carbon sources
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Cells for enzymatic activity measurements were washed once with distilled water and treated with yeast protein extraction solution (Y-PER; Pierce, Rockford, Ill.) for 20 min at room temperature. The mixture was centrifuged for 5 min at 4°C and 5,000 rpm, and the supernatant was used for enzymatic assays. XR, XDH, and XK were assayed as previously described (6), but triethanolamine buffer at pH 7.0 was used for the XDH assay instead of glycine buffer at pH 9.0, since the high pH of the glycine buffer caused precipitation of components in the extraction solution.
Glucose, xylose, xylitol, succinate, glycerol, acetate, and ethanol were analyzed by high-pressure liquid chromatography, as has been described previously (29). The composition of the outgoing gas was monitored continuously with a carbon dioxide and oxygen monitor type 1308 (Brüel & Kjaer, Copenhagen, Denmark) (4) by using photoacoustic and magnetoacoustic detection for CO2 and O2, respectively. The cell dry weight was determined by filtering a known volume of the culture broth through a 0.45-µm (pore-size) Supor membrane (Gelman Sciences, Ann Arbor, Mich.). The filter was weighed after being washed with 3 volumes of double-distilled water and dried in a microwave oven for 15 min at 350 W. The cell dry weight was determined in triplicate.
Construction of strains with open reading frame YCR020c overexpressed and deleted.
E. coli DH5
(Life Technologies, Rockville, Md.) was used for the cloning procedures. The p426ADH (ATCC 87377) multicopy vector (14) was used to overexpress the open reading frame YCR020c. This vector contains the ß-lactamase gene, the URA3 selection marker, and an ADH1 promoter and CYC1 terminator. The integrative plasmid YIpXR/XDH/XK (6) was used to introduce the genes encoding XR, XDH, and XK. The strains S. cerevisiae Y00000 (BY4741; MATa his3-
1 leu2
0 met15
0) and S. cerevisiae Y03500 (BY4741; MATa his3-
1 leu2
0 met15
0 YCR020c::kanMX4) were obtained from Euroscarf (Frankfurt, Germany).
Construction of xylose-utilizing strains with overexpression and deletion of YCR020c.
All enzymes used for cloning and restriction analysis were obtained from Fermentas (Vilnius, Lithuania) unless stated otherwise. Standard techniques were used for cloning, transformation, and analysis (1). Chromosomal DNA from S. cerevisiae TMB 3400 was prepared by using the Easy-DNA kit (Invitrogen, Carlsbad, Calif.) and was used as the template for PCR amplification of the open reading frame YCR020C. The PCR product was obtained by using the upstream primer 5'-GCA CTA GTA TGA GCT GTA CCA CTG ATA AGT TA-3' in combination with the downstream primer 5'-GCG AAT TCT TAG GCG TTG TAA CAA GAT TCA AAA-3'. The start codon is indicated in boldface, and the restriction sites for BcuI (SpeI) (upstream primer) and EcoRI (downstream primer) are underlined. The concentrations of nucleotides, Pwo DNA polymerase, primers, and Mg2+ ions were as recommended by the supplier (Roche, Mannheim, Germany). The PCR was performed in a GeneAmp PCR system 9700 (Perkin-Elmer Corp., Norwalk, Conn.), and the conditions employed were as follows: 94°C for 1 min, 55°C for 30 s, and 72°C for 1 min (10 cycles); 94°C for 1 min, 61°C for 30 s, and 72°C for 1.5 min (15 cycles); and 94°C for 1 min, 61°C for 30 s, and 72°C for 2.5 min (10 cycles). The PCR product was purified with the QiaQuick kit (Qiagen, Hilden, Germany) and, together with the vector p426 ADH, it was cleaved with BcuI and EcoRI and ligated with T4 DNA ligase to form the plasmid pFW5.
S. cerevisiae TMB 3151 was created by integrating the YIpXR/XDH/XK plasmid (6), linearized by digestion with PstI, into the HIS3 locus of the laboratory strain S. cerevisiae CEN.PK 113-11C (MATa his3-
1 ura3-52). S. cerevisiae TMB 3151 was transformed with the plasmids p426ADH and pFW5, resulting in S. cerevisiae strains TMB 3152 and TMB 3155, respectively.
S. cerevisiae strains Y00000 and Y03500 were transformed with the YIpXR/XDH/XK plasmid in the same way as S. cerevisiae CEN.PK 113-11C and were named S. cerevisiae strains TMB 3159 and TMB 3160, respectively.
The recombinant strains, S. cerevisiae TMB 3152, TMB 3155, TMB 3159, and TMB 3160, were cultivated by using the same medium as described above. One-liter shake flasks containing 100 ml of medium supplemented with 20 g of glucose or 10 g of ethanol liter-1, as well as 250-ml shake flasks containing 25 ml of medium supplemented with 10 g of xylulose or 20 g of xylose liter-1 were incubated in a rotary shaker at 30°C. The growth rate was determined by measuring the optical density at 620 nm. Duplicate cultivation experiments were performed for each substrate and strain.
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The biomass yield was ca. 0.47 g of biomass g of consumed carbohydrate-1 for both strains during growth on glucose and glucose plus xylose, whereas it decreased to 0.43 g biomass g of consumed carbohydrate-1 for S. cerevisiae TMB 3400 during growth on xylose only (Table 1). The specific glucose consumption was 247 and 231 mg g of biomass-1 h-1 for S. cerevisiae TMB 3399 and S. cerevisiae TMB 3400, respectively, when cultivated on glucose only. When grown on a mixture of glucose and xylose, S. cerevisiae TMB 3399 gave higher residual glucose and xylose concentrations, 0.09 and 4.6 g liter-1, respectively, than S. cerevisiae TMB 3400, which gave no detectable glucose and only 2.9 g of xylose liter-1. The specific glucose consumption was higher for S. cerevisiae TMB 3399: 160 mg g of biomass-1 h-1 compared to 142 mg g of biomass-1 h-1 for S. cerevisiae TMB 3400. The reverse was true for the specific xylose consumption: 85 mg g of biomass-1 h-1 for S. cerevisiae TMB 3399 and 97 mg g of biomass-1 h-1 for S. cerevisiae TMB 3400. A total of 2.5 mg g of biomass-1 h-1 xylitol was formed during the cultivation of S. cerevisiae TMB 3399. During growth on xylose only, S. cerevisiae TMB 3400 consumed 12.3 g liter-1 of 20.8 g liter-1 in the feed and the specific xylose uptake, 254 mg g of biomass-1 h-1, more than doubled in comparison to cultivation on the mixture of glucose and xylose. A Ks value of 4.9 g liter-1, or 33 mM, was obtained by employing Monod kinetics (16), using D = 0.1 h-1, Dcrit = 0.14 h-1, and s = 12.3 g liter-1. S. cerevisiae TMB 3400 also produced a small amount of xylitol, 1 mg g of biomass-1 h-1. The carbon balances closed within 94 to 103% for all fermentation experiments.
mRNA expression levels.
The mRNA expression levels of the more than 6,000 genes in the genome of S. cerevisiae were monitored simultaneously by using DNA microarrays. In the present investigation, we chose to analyze the mRNA expression levels of the genes encoding sugar transporters and the enzymes involved in xylose metabolism, the pentose phosphate pathway, glycolysis, gluconeogenesis, and galactose metabolism (Table 2), as well as the genes involved in regulation (Table 3). All microarray experiments were performed in duplicate with cells from two independent fermentation experiments.
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TABLE 2. mRNA expression levels in S. cerevisiae strains TMB 3399 and TMB 3400 for genes coding for transporters, enzymes involved in xylose metabolism, the pentose phosphate pathway, glycolysis, glyoxylate shunt, gluconeogenesis, and galactose metabolism
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TABLE 3. mRNA levels of genes involved in regulation
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With regard to xylose metabolism, the heterologous genes encoding XR and XDH were not included in the analysis, since they were cloned from P. stipitis and therefore are not represented on the S. cerevisiae DNA microarrays. The expression of S. cerevisiae genes encoding enzymes with XR (YHR104w) (9) and XDH (YLR070c) (19) activities was analyzed. These two genes showed slightly increased expression during growth on only xylose. The XKS1 gene encoding XK was expressed at levels about twice as high in S. cerevisiae TMB 3400 as those in TMB 3399.
SOL3 and GND1, as well as TAL1 and TKL1, encoding enzymes in the oxidative and nonoxidative pentose phosphate pathway, respectively, were expressed at higher levels in S. cerevisiae TMB 3400 than in TMB 3399. Among the genes encoding glycolytic enzymes, HXK1, HXK2, ENO2 and, possibly, YDR516c showed lower expression levels when TMB 3400 was grown on only xylose. Genes encoding the gluconeogenetic enzyme phosphoenolpyruvate carboxykinase and the glyoxalate enzyme isocitrate lyase, as well as genes involved in galactose metabolism, were upregulated in S. cerevisiae TMB 3400 during growth on xylose only.
Among the genes involved in regulation, notably YBR083W and YPR199C were expressed at lower levels in S. cerevisiae TMB 3400 than in TMB 3399 (Table 3). The PET18 gene (YCR020C), which encodes a transcription regulator, was expressed at high levels in S. cerevisiae TMB 3400 during growth on the mixture of glucose and xylose. When S. cerevisiae TMB 3400 was grown on xylose only, the expression of MIG1 and MIG2 was lower, whereas the expression of CAT8 was higher.
Enzymatic activities.
The specific activities of enzymes involved in the initial xylose metabolism, i.e., XR, XDH, and XK, are given in Table 4. All three enzymes displayed higher activities in S. cerevisiae TMB 3400 than in S. cerevisiae TMB 3399 regardless of whether the feed contained only glucose or glucose plus xylose. The specific activity determined in the cell extracts from xylose-grown S. cerevisiae TMB 3400 was very low for all three enzymes.
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TABLE 4. Enzymatic activities of XR, XDH, and XK from chemostat cultivation of S. cerevisiae strains TMB 3399 and TMB 3400 on various feed concentrations of glucose and xylose
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TABLE 5. Maximum specific growth rates of S. cerevisiae strains TMB 3152, TMB 3155, TMB 3159, and TMB 3160 grown in shake flasks in a defined mineral medium supplemented with glucose, ethanol, xylulose, and xylose
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In S. cerevisiae TMB 3400, the genes HXT5 (encoding a hexose transporter), XKS1 (encoding XK), and SOL3 and GND1 (coding for proteins in the oxidative pentose phosphate pathway), as well as, but to a lesser extent, TKL1 and TAL1 in the nonoxidative pentose phosphate pathway, were expressed at higher levels than in the parental strain S. cerevisiae TMB 3399. The higher expression of these genes could explain the improved growth rate of S. cerevisiae TMB 3400 on xylose, as well as its higher xylose uptake from a feed containing a mixture of xylose and glucose.
The HXT5 gene encodes a hexose transporter with moderate affinity for glucose (40 mM) (5). A previous investigation (5) reported abundant HXT5 expression during slow growth on glucose and during growth on nonfermentable carbon sources but, in contrast to our results, this was suggested to be glucose repressed.
When TMB 3400 and TMB 3399 were compared under the same conditions, either with glucose or with the glucose-xylose mixture, the higher XKS1 mRNA expression levels monitored for TMB 3400 (Table 2) agreed well with the higher XK activities measured in the cell extracts (Table 4). That the XK activity in S. cerevisiae TMB 3400 was higher than in TMB 3399 is also in agreement with a previous investigation of an S. cerevisiae strain mutated for improved xylose growth. The enzymatic activity of XK in the mutated S. cerevisiae IM2, with a maximum specific growth rate of 0.08 h-1, was 60% higher than in its parent S. cerevisiae H that has a maximum specific growth rate of 0.03 h-1 (24). Furthermore, XK activities were 5 to 10 times higher in mutants of the natural xylose-utilizing yeasts Pachysolen tannophilus (11) and Candida utilis (12), which were selected for improved utilization of xylose and xylitol, respectively.
The higher expression of HXT5, XKS1, SOL3, and GND1, as well as of TKL1 and TAL1, in S. cerevisiae TMB 3400 could be due to an altered expression of one or several transcription regulators acting on these genes. The transcription factors coded for by YCR020C, YBR083W, and YPR199C were differently expressed in S. cerevisiae TMB 3400 and TMB 3399. The open reading frame YCR020C encodes the transcription factor Pet18p, which was expressed at higher levels in S. cerevisiae TMB 3400 than in S. cerevisiae TMB 3399 during growth on the mixture of glucose and xylose. The decision to investigate the influence of PET18 on xylose utilization was based on its reported effect on carbon utilization. Mutants defective in PET18 have been reported to be unable to grow on nonfermentable carbon sources (30). However, the strain in which PET18 was deleted was capable of growth on ethanol. Furthermore, xylose growth seemed to be unaffected by deleting and by overexpressing PET18. The transcription factors encoded by YBR083W and YPR199C deserve further attention and their effect on xylose utilization in S. cerevisiae will be reported in a forthcoming study.
The development of the superior xylose-utilizing S. cerevisiae TMB 3400 allowed us to perform a physiological comparison, as well as a comparison of mRNA expression levels, between growth levels on xylose and glucose. The first chemostat cultivation of a recombinant S. cerevisiae strain on xylose as the sole carbon source is presented here. S. cerevisiae TMB 3400 consumed ca. 40% of the xylose in the feed. This permitted us to determine the Ks value for xylose (33 mM), which is ca. 60 times higher than the corresponding value reported for growth on glucose (0.55 mM) (27). The biomass yield was lower on xylose than on glucose; therefore, S. cerevisiae TMB 3400 apparently cannot obtain as much energy from xylose as from glucose, which points toward a difference in the metabolism of these substrates. The gluconeogenetic gene encoding phosphoenolpyruvate carboxykinase and the glyoxylate gene encoding isocitrate lyase were upregulated during growth on xylose. When carbon is channeled through the glyoxylate shunt, ATP (GTP) is lost due to a reduced flux between succinyl coenzyme A and succinate. A lower ATP yield may be responsible for the lower biomass yield of S. cerevisiae TMB 3400 on xylose than on glucose. In a previous investigation, batch cultivation of S. cerevisiae TMB 3399 and 3400 showed biomass yields of 0.39 and 0.41 g of biomass g of xylose-1, respectively (29a). The fact that both the transformant S. cerevisiae TMB 3399 and the mutant S. cerevisiae TMB 3400 displayed similar biomass yields on xylose indicates that the lower biomass yield on xylose is not due to a mutation. The genes encoding phosphoenolpyruvate carboxykinase and isocitrate lyase are upregulated by CAT8 (3, 17, 18), which in turn is repressed by the glucose transcription regulator Mig1p (8). Our results show higher mRNA levels of CAT8 and lower expression of MIG1 during growth on xylose in comparison to growth on glucose.
MIG1 also regulates genes involved in galactose metabolism. The analysis of S. cerevisiae TMB 3400 showed that galactose permease, galactokinase, galactose 1-phosphate uridyl transferase and UDP-glucose 4-epimerase were expressed at higher levels during growth on only xylose in comparison to growth on glucose or on a combination of glucose and xylose. In the presence of glucose, MIG1 causes repression of the transcription of genes involved in galactose metabolism (15). However, galactose has been reported to be necessary for the full initiation of transcription (23, 32), and it remains to be elucidated whether the increased expression of these genes in S. cerevisiae TMB 3400 is mediated by xylose or is due to a mutation.
Some of the genes encoding glycolytic enzymes, notably HXK2, showed lower expression levels when TMB 3400 was grown on only xylose. It has been demonstrated that the induction of glycolytic genes requires increased concentrations of metabolites in the early stages of glycolysis (7, 13, 20). These concentrations might be insufficient for the full induction of glycolysis during xylose growth.
We thank Carl A. K. Borrebaeck for providing the facilities for DNA microarray analysis.
Present address: Biochemistry, Division for Chemistry, Karlstad University, Karlstad, Sweden. ![]()
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