The role of peroxisomes in xylose alcoholic fermentation in the engineered Saccharomyces cerevisiae

Xylose is a second‐most abounded sugar after glucose in lignocellulosic hydrolysates and should be efficiently fermented for economically viable second‐generation ethanol production. Despite significant progress in metabolic and evolutionary engineering, xylose fermentation rate of recombinant Saccharomyces cerevisiae remains lower than that for glucose. Our recent study demonstrated that peroxisome‐deficient cells of yeast Ogataea polymorpha showed a decrease in ethanol production from xylose. In this work, we have studied the role of peroxisomes in xylose alcoholic fermentation in the engineered xylose‐utilizing strain of S. cerevisiae. It was shown that peroxisome‐less pex3Δ mutant possessed 1.5‐fold decrease of ethanol production from xylose. We hypothesized that peroxisomal catalase Cta1 may have importance for hydrogen peroxide, the important component of reactive oxygen species, detoxification during xylose alcoholic fermentation. It was clearly shown that CTA1 deletion impaired ethanol production from xylose. It was found that enhancing the peroxisome population by modulation the peroxisomal biogenesis by overexpression of PEX34 activates xylose alcoholic fermentation.     

Trehalose metabolism in Saccharomyces cerevisiae during alcoholic fermentation

Strains of Saccharomyces cerevisiae accumulated intracellular trehalose up to 105 mg/g cell dry wt with 90% survival. Viability could be correlated to trehalose levels during ethanol fermentation albeit the disaccharide did not seem to contribute to fermentation yields. Trehalose-6-phosphate synthase showed high activity (up to 279 mu/mg protein) even at high residual sucrose concentration (115 g/l) in the wort suggesting to be a response of yeast cells to the osmotic stress conditions.     

Mechanism of proanthocyanidins-induced alcoholic fermentation enhancement in Saccharomyces cerevisiae

Our previous work revealed proanthocyanidins (PAs) could pose significant enhancement on the activity of H⁺-ATPase and fermentation efficiency after a transient initial inhibition (Li et al in Am J Enol Vitic 62(4):512–518, 2011). The aim of the present work was to understand the possible mechanism for this regulation. At Day 0.5 the gene expression level of PMA1 in AWRI R₂ strain supplemented with 1.0 mg/mL PAs was decreased by around 54 % with a 50 % and a 56.5 % increase in the concentration of intracellular ATP and NADH/NAD⁺ ratio, respectively, compared to that of control. After the transient adaptation, the gene expression levels of PMA1 and HXT7 in PAs-treated cells were enhanced significantly accompanied by the decrease of ATP contents and NADH/NAD⁺ ratio, which resulted in the high level of the activities of rate-limiting enzymes. PAs could pose significant effects on the fermentation via glucose transport, the energy and redox homeostasis as well as the activities of rate-limiting enzymes in glycolysis.     

Intensification of alcoholic fermentation upon dehydration-rehydration of the yeast Saccharomyces cerevisiae

Summary In comparison with intact yeast, dehydrated-rehydrated cells of Saccharomyces cerevisiae show significantly higher ethanol production from exogenous substrate under both anaerobic and aerobic conditions, particularly when low concentration (0.1%) of glucose are used. For populations with a higher percentage of viable rehydrated cells (above 70%) a more notable decrease in the Pasteur effect (the difference between the quantity of ethanol formed under anaerobic and aerobic conditions) is observed.     

Engineering of Saccharomyces cerevisiae for efficient anaerobic alcoholic fermentation of L-arabinose

For cost-effective and efficient ethanol production from lignocellulosic fractions of plant biomass, the conversion of not only major constituents, such as glucose and xylose, but also less predominant sugars, such as l-arabinose, is required. Wild-type strains of Saccharomyces cerevisiae, the organism used in industrial ethanol production, cannot ferment xylose and arabinose. Although metabolic and evolutionary engineering has enabled the efficient alcoholic fermentation of xylose under anaerobic conditions, the conversion of l-arabinose into ethanol by engineered S. cerevisiae strains has previously been demonstrated only under oxygen-limited conditions. This study reports the first case of fast and efficient anaerobic alcoholic fermentation of l-arabinose by an engineered S. cerevisiae strain. This fermentation was achieved by combining the expression of the structural genes for the l-arabinose utilization pathway of Lactobacillus plantarum, the overexpression of the S. cerevisiae genes encoding the enzymes of the nonoxidative pentose phosphate pathway, and extensive evolutionary engineering. The resulting S. cerevisiae strain exhibited high rates of arabinose consumption (0.70 g h(-1) g [dry weight](-1)) and ethanol production (0.29 g h(-1) g [dry weight](-1)) and a high ethanol yield (0.43 g g(-1)) during anaerobic growth on l-arabinose as the sole carbon source. In addition, efficient ethanol production from sugar mixtures containing glucose and arabinose, which is crucial for application in industrial ethanol production, was achieved.     

Behaviour of Saccharomyces cerevisiae cells entrapped in a polyacrylamide gel and performing alcoholic fermentation

Summary The behaviour of Saccharomyces cerevisiae cells entrapped in a polyacrylamide gel was studied during their continuous function in an ethanol-producing reactor. Polymerization destroys 40% to 80% of the cells, depending on their physiological state. A three day adaptation phase is required before ethanol production stabilizes and this phase corresponds to an increase in cell concentration in the gels and to protein synthesis. The amounts of DNA, glucan, glycogen and trehalose are different in entrapped and free cells. Microscopic observation shows that 75% to 85% of the cells lose their integrity and that the remainder appear to multiply normally. Within a gel particle, both viability and fermentation activity are heterogeneous. A high percentage of cells have low viability and low fermentation activity. A proportion of cells remains capable of forming colonies and these cells have higher fermentation activity and are preferentially localized at the surface of gel particles.     

Enological properties in wild and commercial Saccharomyces cerevisiae yeasts: relationship with competition during alcoholic fermentation

Commercial yeasts are widely used in winemaking to carry out the alcoholic fermentation; nevertheless, some wild strains may compete with them and even dominate the process. In this research, 21 prevailing wild strains isolated from inoculated musts were chosen in order to study the competition between them and commercial yeasts. Some biotechnological properties which could enhance their performance during the process were also studied, such as vitality, killer factor, resistance to high concentrations of sugar, ethanol and SO₂ or trehalose and glycogen cell content. All yeasts, both commercial and wild strains, showed resistance to the killer toxin and they were all able to growth under adverse conditions. However, vitality and carbohydrate content were strain dependent in around 70% of the cases; the wild strain had a higher vitality and accumulated less trehalose than its commercial counterpart.     

Population size drives industrial Saccharomyces cerevisiae alcoholic fermentation and is under genetic control

Alcoholic fermentation (AF) conducted by Saccharomyces cerevisiae has been exploited for millennia in three important human food processes: beer and wine production and bread leavening. Most of the efforts to understand and improve AF have been made separately for each process, with strains that are supposedly well adapted. In this work, we propose a first comparison of yeast AFs in three synthetic media mimicking the dough/wort/grape must found in baking, brewing, and wine making. The fermentative behaviors of nine food-processing strains were evaluated in these media, at the cellular, populational, and biotechnological levels. A large variation in the measured traits was observed, with medium effects usually being greater than the strain effects. The results suggest that human selection targeted the ability to complete fermentation for wine strains and trehalose content for beer strains. Apart from these features, the food origin of the strains did not significantly affect AF, suggesting that an improvement program for a specific food processing industry could exploit the variability of strains used in other industries. Glucose utilization was analyzed, revealing plastic but also genetic variation in fermentation products and indicating that artificial selection could be used to modify the production of glycerol, acetate, etc. The major result was that the overall maximum CO(2) production rate (V(max)) was not related to the maximum CO(2) production rate per cell. Instead, a highly significant correlation between V(max) and the maximum population size was observed in all three media, indicating that human selection targeted the efficiency of cellular reproduction rather than metabolic efficiency. This result opens the way to new strategies for yeast improvement.     

Fine measurement of ergosterol requirements for growth of Saccharomyces cerevisiae during alcoholic fermentation

Yeasts can incorporate a wide variety of exogenous sterols under strict anaerobiosis. Yeasts normally require oxygen for growth when exogenous sterols are limiting, as this favours the synthesis of lipids (sterols and unsaturated fatty acids). Although much is known about the oxygen requirements of yeasts during anaerobic growth, little is known about their exact sterol requirements in such conditions. We developed a method to determine the amount of ergosterol required for the growth of several yeast strains. We found that pre-cultured yeast strains all contained similar amounts of stored sterols, but exhibited different ergosterol assimilation efficiencies in enological conditions [as measured by the ergosterol concentration required to sustain half the number of generations attributed to ergosterol assimilation (P₅₀)]. P₅₀ was correlated with the intensity of sterol synthesis. Active dry yeasts (ADYs) contained less stored sterols than their pre-cultured counterparts and displayed very different ergosterol assimilation efficiencies. We showed that five different batches of the same industrial Saccharomyces cerevisiae ADY exhibited significantly different ergosterol requirements for growth. These differences were mainly attributed to differences in initial sterol reserves. The method described here can therefore be used to quantify indirectly the sterol synthesis abilities of yeast strains and to estimate the size of sterol reserves.     

Effect of anisothermal conditions on the kinetics of alcoholic fermentation by Saccharomyces cerevisiae

A comparison between isothermal and anisothermal alcoholic fermentation is made in this paper. Important differences were observed: in some anisothermal operations maximum rates of CO₂ production were reached towards the end of fermentation. Cultures with different initial nitrogen or biotin concentrations showed the importance of thermal conditions for the completion of the reaction. They indicated that the notion of the limiting nutrient does not have the same technological significance with respect to the mode of temperature processing. Thus, some studies at the laboratory scale should not be carried out under isothermal conditions, especially not within temperature ranges which may be critical for cell viability. This is, for example, the case with enological studies about red wine processing.     

Kinetics of volatile metabolites during alcoholic fermentation of cane molasses by Saccharomyces cerevisiae

Summary The kinetics of ethanol, acetaldehyde, ethyl acetate and fusel alcohols during alcoholic fermentations on cane molasses by Saccharomyces cerevisiae have been obtained via an in-situ gas membrane sensor connected to a gas chromatograph. Various operation parameters have been investigated such as inoculum rate, molasses concentration, operation mode (batch, fed-batch). The modification of fusel alcohols kinetics in response to addition of amino acids has been studied as well as the assimilation of two intermediary aldehydes (isovaleraldehyde and isobutyraldehyde) in the fusel alcohol synthesis pathway. Offprint requests to: M.-N. Pons     

Gaseous environments modify physiology in the brewing yeast Saccharomyces cerevisiae during batch alcoholic fermentation

Aims:  To investigate the impact of different gaseous atmospheres on different physiological parameters in the brewing yeast Saccharomyces cerevisiae BRAS291 during batch fermentation.
Methods and Results:  Yeasts were cultivated on a defined medium with a continuous sparging of hydrogen, helium and oxygen or without gas, permitting to obtain three values of external redox. High differences were observed concerning viable cell number, size and metabolites produced during the cultures. The ethanol yields were diminished whereas glycerol, succinate, acetoin, acetate and acetaldehyde yields were enhanced significantly. Moreover, we observed major changes in the intracellular NADH/NAD⁺ and GSH/GSSG ratio.
Conclusions:  The use of gas led to drastic changes in the cell size, primary energy metabolism and internal redox balance and E _h . These changes were different depending on the gas applied throughout the culture.
Significance and Impact of the Study:  For the first time, our study describes the influence of various gases on the physiology of the brewing yeast S. cerevisiae . These influences concern mainly yeast growth, cell structure, carbon and redox metabolisms. This work may have important implications in alcohol-related industries, where different strategies are currently developed to control better the production of metabolites with a particular attention to glycerol and ethanol.     

Biomass production and alcoholic fermentation performance of Saccharomyces cerevisiae as a function of nitrogen source

Nitrogen limitation is one of the most common causes for stuck or sluggish fermentation. A broad range of values have been reported as the minimum nitrogen concentration necessary for the completion of alcoholic fermentation. We have analyzed the minimum nitrogen concentration required to yield the maximum biomass (nitrogen reference value) using a microwell plate reader to monitor fermentation with different nitrogen sources and sugar concentrations. The biomass yield was dependent on the amount of available nitrogen, the nature of nitrogen source, and the sugar concentration in the medium. Nevertheless, achieving the maximum biomass was not sufficient to ensure the completion of the alcoholic fermentation, because the fermentation of 280?g?sugar?L(-1) stuck, regardless of the nature and concentration of nitrogen source. However, a mixture of five amino acids (Leu, Ile, Val, Phe and Thr) as the nitrogen source allowed for maximum sugar consumption. Analysis of cell vitality by impedance showed a significant improvement in the vitality for cells fermenting using this amino acid combination.     

Comparative proteomic analysis of alcoholic fermentation employing a new environmental strain of Saccharomyces cerevisiae

The aim of this study was to investigate the biochemical pathways induced during must fermentation employing the Saccharomyces cerevisiae, strain Z622, isolated from the traditional wine area of Zitsa (Epirus, Greece). Proteomic analysis (two-dimensional gel electrophoresis followed by nano-LC ESI-MS/MS) was used to assess the protein profile response of strain Z622 cultured in Debina grape must, yeast extract–malt extract (YM) or minimal medium (MM) under fermentation conditions, at the beginning and at the end of fermentation. The proteomic results and their analysis with Gene Ontology (GO) terms revealed that the intracellular proteins induced in yeast cells grown exclusively in Debina grape must during the early stage of fermentation were mainly involved in amino acid metabolism, glycolysis and sterol formation. These three pathways reflect the adaptation of the cell to the fermentative metabolism. During the late stage, several enzymes were induced due to starvation conditions or to participation in defence mechanisms against oxidative stress and protein degradation. Several of the identified enzymes have not previously been reported to be induced during wine fermentation and thus the results presented here can contribute to a better understanding of how S. cerevisiae cells adapt to wine fermentation.     

Continuous alcoholic fermentation of glucose/xylose mixtures by co-immobilized Saccharomyces cerevisiae and Candida shehatae

Viable Saccharomyces cerevisiae and Candida shehatae cells were co-immobilized in a composite agar layer/microporous membrane structure. This immobilized-cell structure was placed in a vertical position between the two halves of a double-chambered, stainless-steel bioreactor of original design and applied to the continuous alcoholic fermentation of a mixture of glucose (35 g dm⁻³) and xylose (15 g dm⁻³). Various dilution rates and initial cell loadings of the gel layer were tested. Simultaneous consumption of the two sugars was always observed. The best fermentation performance was obtained at low dilution rate (0.02 h⁻¹) with an excess of C. shehatae over S. cerevisiae in the initial cell loading of the gel (5.0 mg dry weight and 0.65 mg dry weight cm⁻³ gel respectively): 100% of glucose and 73% of xylose were consumed with an ethanol yield coefficient of 0.48 g g total sugars⁻¹. In these conditions, however, the ethanol production rate per unit volume of gel remained low (0.37 g h⁻¹ dm⁻³). Viable cell counts in gel samples after incubation highlighted significant heterogeneities in the spatial distribution of the two yeast species in both the vertical and the transverse directions. In particular, the overall cell number decreased from the bottom to the top of the agar sheet, which may explain the low ethanol productivity relative to the total gel volume. Received: 26 February 1998 / Received revision: 15 April 1998 / Accepted: 19 April 1998