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1 Biology Center, Department of Biology, University of Minho, 4710-057 Braga, Portugal
2 Centro de Recursos Microbiológicos (CREM), Faculty of Sciences and Technology, New University of Lisbon, 2829-516 Caparica, Portugal
3 Proenol – Industria Biotecnológica Lda., 4405-194 Canelas, V. N. Gaia, Portugal
4 Life and Health Sciences Research Institute (IVCS), School of Health Sciences, University of Minho, 4710-057 Braga, Portugal
Correspondence
Cecília Leão
cleao{at}ecsaude.uminho.pt
| ABSTRACT |
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| INTRODUCTION |
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During grape-must fermentation, the most physiologically relevant hexose transporters (Hxt1p–Hxt4p, and Hxt6/7p), which accept both glucose and fructose as substrates, show distinct expression patterns in accordance with their regulatory and kinetic properties (Reifenberger et al., 1997
; Perez et al., 2005
). In general, the lower affinity of hexose transporters for fructose compared with glucose explains the prevalence of fructose towards the end of fermentation. The role of sugar transport in yeast strains used to relaunch the fermentation process remains to be elucidated.
Recently, because of the increasing demand for better quality wines, the winemaking industry has turned its attention to the non-Saccharomyces yeast species that are usually present in the grape-must microflora (Fleet, 2003
). Conceivably, the non-Saccharomyces yeasts might also be useful for the reinoculation of stuck fermentations. Among these yeasts, Zygosaccharomyces bailii emerges as a possible good candidate, as it is known for its frutophilic character, and for high resistance to both ethanol and acetic acid (Sousa et al., 1996
; Pina et al., 2004b
). On the other hand, Torulaspora delbrueckii, a yeast species closely related to Saccharomyces cerevisiae, is already used to improve aroma development in wine production (Ciani & Maccarelli, 1998
; Plata et al., 2003
). Since genetically modified wine yeasts cannot be marketed in most wine-producing countries, a combination of desired traits to enhance fermentation performance, and avoid stuck fermentations, may be achieved by traditional strain breeding of wine-associated yeasts.
The general aim of the present work was to assess different yeast species for their ability to restart stuck fermentations, and to evaluate environmental factors conditioning an efficient performance. To that end, we compared commercial and non-commercial Saccharomyces wine-associated strains, and two fermentative non-Saccharomyces species, under conditions prevailing in stuck wine fermentations. Special attention was given to relationships between fructose consumption rates and the resistance of sugar transport to ethanol. Furthermore, a hybrid strain combining the high ethanol and acetic acid tolerance of T. delbrueckii, and the high fructose consumption capacity of S. cerevisiae, was obtained, and compared with its parental strains.
| METHODS |
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ura3-52 his3-11,15 leu2-3,112 MAL2 SUC2 GAL MEL) by deleting all but one of the HXT1–HXT7 genes (Reifenberger et al., 1997Stock cultures were maintained at 4 °C on YPDA medium (2 % glucose, 0.5 % yeast extract, 1 % peptone and 2 % agar; all w/v). For the experimental work, yeast strains were grown in YPD medium (2 % glucose, 1 % peptone and 0.5 % yeast extract; all w/v) up to the exponential (OD640 approx. 0.4) or stationary growth phase (OD640 approx. 4.0), at 26 °C and 140 r.p.m. Ethanol-adapted cells were obtained either after growth for different periods (at 26 °C and 140 r.p.m.) in YPD medium supplemented with the desired ethanol concentration, or after serial cultivation of the yeast (at 16 °C and 140 r.p.m.) in SF synthetic medium [2.5 % (w/v) fructose, 1 % (w/v) yeast extract, 2 % (w/v) peptone, 12 % (v/v) ethanol and 0.06 % (v/v) acetic acid, pH 3.7] simulating a stuck fermentation, until fructose was exhausted from the medium.
Cell viability assays.
Yeast cells in exponential growth phase (OD640 approx. 0.4) in YPD medium were harvested by centrifugation, and aseptically transferred to YPD containing 18 % (v/v) ethanol and 0.06 % (v/v) acetic acid, and incubated at 20 °C and 140 r.p.m. Samples were taken periodically for 2 h, and plated in duplicate on YPDA medium. The number of c.f.u. was determined after incubation for 2–3 days at 30 °C. Survival curves are represented as the percentage of viable cells as a function of incubation time.
Fermentations.
Fermentations were carried out at 20 °C and 120 r.p.m., under oxygen limitation, in 250 ml rubber-stopped flasks containing 150 ml SF medium. The fermentation medium was inoculated with yeast strain (4x106 cells ml–1) grown under the conditions described above.
To determine the sugar concentrations in the growth medium, the cultures were sampled, and immediately centrifuged at 16 100 g for 3 min. The supernatant was frozen, and stored at –20 °C until it was analysed. Quantitative analysis of sugar was based on the 3,5-dinitrosalicylic acid assay method (Miller, 1959).
Glucose-uptake assays.
For glucose-uptake assays, [U-14C]glucose, with a specific activity of 317 mCi mmol–1 (11.73 GBq mmol–1; Amersham), was used. S. cerevisiae strains were grown as described above. The cells were subsequently harvested by centrifugation, washed twice with cold water, suspended in water to a cell density of 35–45 mg ml–1 (dry wt), and kept on ice. Zero-trans influx of labelled glucose was determined at 26 °C as follows. A 10 µl volume of cell suspension was mixed with 30 µl 0.1 M potassium phosphate buffer (pH 5.0). For the determination of the effect of ethanol on glucose transport, 12 % (v/v) ethanol was added to the buffer. The cell suspension was incubated for 5 min, and the reaction was started by adding 10 µl of an aqueous solution of [U-14C]glucose at the desired concentration. After a 5 s incubation, 4.5 ml chilled water was added, and the mixture was immediately filtered through glass-fibre filters (GF/C filters; Whatman). The cells on the filter were washed with 15 ml chilled water, and the filter was immediately transferred into a vial containing 5 ml scintillation OptiPhase HiSafe II liquid (LKB Scintillation Products). The radioactivity was counted with a Packard Tri-Carb 2200 CA liquid scintillation counter (Packard Instrument), with correction for disintegrations per minute. Non-specific binding of radiolabelled sugar to the yeast cells and filter was determined in parallel by adding ice-cold water immediately before the addition of the labelled sugar. For each sugar concentration, the reaction was performed in triplicate, and standard deviation values were below 10 %.
Generation of hybrids.
Hybrids were generated by protoplast fusion between S. cerevisiae PYCC 5792 and T. delbrueckii Bio-J32. Each parental yeast strain was grown to stationary growth phase (OD640 approx. 4.0), harvested by centrifugation (4500 g for 5 min), washed twice with ice-cold water, and pelleted cells were suspended in PT solution (0.1 M Tris/HCl, pH 7, 0.01 M EDTA, 1 M KCl, and 0.1 M β-mercaptoethanol) to a final concentration of 108 cells ml–1. The cells were incubated at 30 °C for 30 min, with gentle agitation (70 r.p.m.), and then harvested by centrifugation (4500 g for 5 min), washed once with 1 M KCl, and suspended in P solution [0.05 M potassium phosphate buffer, pH 7.5; 1 M KCl and 200 U lyticase (Sigma) ml–1], followed by an incubation period of 120 min at 30 °C, with gentle agitation (70 r.p.m.). After at least 80 % protoplast formation, determined by microscope observation, the suspension was centrifuged for 10 min at 6000 g, washed three times with 1 M KCl, and suspended in 0.4 M CaCl2 to a final concentration of 5x107 cells ml–1. For protoplast fusion, 1 ml suspensions of each strain (S. cerevisiae PYCC 5792 and T. delbrueckii Bio-J32) were mixed, and centrifuged at 4500 g for 10 min. The supernatant was discarded, and the pellet was suspended in the residual volume (about 0.2 ml), followed by the addition of 2 ml 35 % PEG containing 15 % DMSO. After 30 min incubation at 30 °C, 200 µl of the suspension was combined with 8 ml agar (1.5 %, w/v) and 1 M KCl, at 45 °C, and quickly poured onto YPDA plates containing 18 % (v/v) ethanol. The plates were then incubated for 4–5 days, at 30 °C, until colony formation.
| RESULTS |
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50 %), and these strains were unable to complete fermentation during the same set period (Fig. 5
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| DISCUSSION |
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Another factor influencing the rate at which fructose was consumed under conditions mimicking stuck wine fermentations was the physiological state of the yeast. Stationary cells of S. cerevisiae PYCC 5792 performed as well as exponential-phase ethanol-pre-adapted cells, and adaptation of stationary-phase cells to ethanol did not improve their performance. Cells in the stationary phase of growth are well known for their capacity to accumulate trehalose, express heat-shock proteins and modulate membrane composition (Werner-Washburne et al., 1993
); these factors have been described as contributing to the ethanol-stress response (Piper, 1995
; Alexandre et al., 2001
). Our results support the recommendation of wine yeast suppliers to pre-adapt the cells to ethanol before using them as an inoculum to restart stuck fermentations.
Our observations in the first stage of this work led us to assess the role of sugar transport on the fructose consumption capacity. Notably, a direct correlation between fructose-consumption and glucose (as indicative of fructose)-uptake rates was detected (Table 1
, Fig. 3
) when comparing cells in different physiological conditions (stationary-, exponential- and exponential-phase pre-adapted to ethanol). This correlation was reinforced by the observation that sugar transport systems less affected by high ethanol concentrations (12 %, v/v) are more likely to be associated with a better capacity of the yeast strains to act as restarters in stuck fermentations (Fig. 5
), and by the results obtained with the F1-11 hybrid. The comparative analysis of individual S. cerevisiae Hxt transporters concerning their putative contribution to the overall sensitivity of the yeast towards ethanol was not very enlightening. The laboratory strain we used as a reference (Table 2
) behaved differently from the best-performing commercial strain (Fig. 5
). While glucose transport in the laboratory strain was more resistant to ethanol during the exponential phase of growth, exponential-phase cells of the best-performing commercial strains were significantly more sensitive than stationary cells (Fig. 4); this finding is more in line with present knowledge on this topic. Our results revealed that all the relevant glucose transporters (Hxt1p–Hxt7p), with the exception of Hxt2p, showed different sensitivities to ethanol as a function of the growth stage. Hxt3p and Hxt1p are known to be highly expressed during the exponential growth phase (Reifenberger et al., 1997
; Luyten et al., 2002
); mutants expressing only Hxt3p or Hxt1p displayed a lower level of ethanol inhibition, contradicting the general phenotype of oenological strains. A similar result was obtained with the high-affinity transporters Hxt6p and Hxt7p, which are known to be expressed in late-exponential phase and during stationary phase. Hxt6p and Hxt7p were found to be more sensitive to ethanol, in disagreement with the lower glucose-transport inhibition observed in stationary-phase cells of the commercial S. cerevisiae strains, but justifying the phenotype of the reference laboratory strain. It is noteworthy that stationary-phase cells of the HXT5+ strain were the most resistant to ethanol inhibition of glucose transport (Table 2
). The HXT5 gene is induced by stress conditions (Buziol et al., 2002
), and it is co-expressed with genes involved in reserve carbohydrate metabolism (Verwaal et al., 2002
). The transcript levels of HXT5 increase upon glucose depletion from the growth medium (Diderich et al., 2001
). These data, together with our results, point to a potentially relevant contribution of the Hxt5 transporter to the lower sensitivity to ethanol found in stationary-phase cells of commercial S. cerevisiae strains. The results also suggest that manipulating the expression of a given transporter could have an impact on the ability of the yeast strain to remove fructose from media with high ethanol concentrations. In line with the crucial role of sugar transporters throughout vinification, it has been shown recently that the expression of a mutated form of the Hxt3 transporter could increase the rate of fructose consumption during a simulated wine fermentation (Guillaume et al., 2007
).
Two specific aspects of our work open new perspectives to the wine-making industry, and should be emphasized. One is the utilization of natural breeding programmes to combine desirable traits of wine-associated species and/or strains for the vinification process. The example given in this work is particularly relevant since mixed starter cultures containing T. delbrueckii and S. cerevisiae are already on the market to take advantage of the flavour-enhancing properties of T. delbrueckii. The generated hybrid, in addition to its potential to restart stuck fermentations, may also be useful to conduct an entire fermentation that benefits from its flavour properties. Our results also clearly demonstrate that cell survival in the presence of high concentrations of ethanol and acetic acid is not per se a good parameter to consider in a strain selection programme for efficient ethanolic fermentation processes; this is in contrast to currently accepted ideas. Instead, higher productivity seems to be associated with the ethanol tolerance of sugar transport. Therefore, we propose that the assessment of glucose transport in the presence of a high ethanol concentration is a good test for preliminary selection of yeast strains that are suitable to restart stuck wine fermentations.
| ACKNOWLEDGEMENTS |
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Edited by: M. Schweizer
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Received 10 July 2007;
revised 10 October 2007;
accepted 23 October 2007.
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