Extrusion of metabolites from baker’s yeast during glucose-induced acidification

Extrusion of metabolites (glycerol, lactic, malic, and succinic acid) during the medium acidification caused by resting baker’s yeast supplied with 200mm glucose was studied under aerobic and anaerobic conditions and in the absence and presence of 14mm KCl. The maximum levels of glycerol and of the sum of acids (about 13 and 8mm, respectively) were attained anaerobically; aerobiosis reduced the levels by 40–50 % and the presence of K⁺ ions by another 10–20 %. The time courses of glucose consumption and medium acidification were similar aerobically and anaerobically. The glucose consumption ourves exhibited a short plateau about 2 min after glucose addition, caused probably by a rapid osmotic equilibration of glucose across the cell mambrane. Metabolite extrusion indicates that at high glucose concentrations the alcohol dehydrogenase reaction is supplemented by other reactions aiding in the maintenance of a balanced NAD⁺/NADH ratio in the cells.     

Intracellular pH of baker’s yeast

The distribution of bromophenol blue between the cell and the medium was used to calculate the intracellular pH of yeast. In buffered media the intracellular pH exhibited a plateau at pH _i =5.8 for low external pH values and another at pH _i =7.6 for high external pH values. The production of H ions by the yeast during utilization of glucose is not accompanied by an alkalinization of the cell interior. The pH _i even decreases somewhat in the presence of glucose and K ions.

1. (1)
   Внутриклеточный pH дрожжей вычисляли на основании распределения бромфеноловой сини между клетками и средой.     
   
   

Transport of ethanol in baker’s yeast

Ethanol is transported into various strains of baker's yeast by simple diffusion (no effect of inhibitors and a linear concentration dependence of the initial rate of uptake and final distribution in cells). It distributes itself in 96.6 +/- 16.2% of intracellular water.     

Behaviour of dehydrated baker’s yeast during reduction reactions in a biphasic medium

The behaviour of dry bakers yeast (Saccharomyces cerevisiae type II, Sigma) used as biocatalyst without preliminary growth for the synthesis of 2-heptanol from 2-heptanone in a biphasic system is presented. Cells undergo intracellular trehalose consumption with a stoichiometric ethanol production during the first 15 h of the process. This metabolism is then replaced by acetate accumulation. These reactions are disconnected from the biocatalytic reaction and do not provide reduced cofactors. 2-Heptanone is metabolised by two pathways. The first leads to 2-heptanol (molar yield close to 55%, enantioselectivity higher than 99%, with a slight decrease at the end of the process) and the second corresponds to material incorporation into the biomass. This latter phenomenon is assumed to provide the biocatalyst with the reduced cofactors needed for the reduction process. Overall, the process yielded ca. 1.4 g/l 2-heptanol in 50 h reaction, which is close to that observed with fresh cells previously grown for 15 h.     

On the Mechanism of Brewer’s Yeast Flocculation

Brewer’s yeast appears to flocculate or disperse reversibly in response to the environmental conditions. The yeast and its solubilized cell surface substance show flocculation-dispersion changes according to pH, sugar concentration and flocculation inducing substances. Top fermentative yeasts do not show such a response to the surrounding conditions. Cell surfaces of bottom fermentative yeasts increase in hydrophobicity during a shift from fermentation starting conditions (dispersion of yeast) (high sugar concentration, pH 5.5) to ending conditions ( flocculation) (no sugar, pH 4.2), but this hydrophobicity increase was not seen in the case of top fermentative yeast cells. The contributions of hydrophobic interaction and ionic bonds to flocculence of the yeast were discussed.     

Effect of inhibitors on acid production by baker’s yeast

Glucose-induced acid extrusion, respiration and anaerobic fermentation in baker’s yeast was studied with the aid of sixteen inhibitors. Uranyl(2+) nitrate affected the acid extrusion more anaerobically than aerobically; the complexing of Mg²⁺ and Ca²⁺ by EDTA at the membrane had no effect. Inhibitors of glycolysis (iodoacetamide, N-ethylmaleimide, fluoride) suppressed acid production markedly, and so did the phosphorylation-blocking arsenate. Fluoroacetate, inhibiting the citric-acid cycle, had no effect. Inhibition by uncouplers depended on their pK_a values: 2,4,6-trinitrophenol (pK_a 0.4) < 2,4-dinitrophenol (4.1) < azide (4.7) < 3-chlorophenylhydrazonomalononitrile (6.0). Inhibition by trinitrophenol was only slightly increased by its acetylation. Cyanide and nonpermeant oligomycin showed practically no effect; inhibition by dicyclohexylcarbodiimide was delayed but potent. The concentration profiles of inhibition of acid production differed from those of respiration and fermentation. Thus, though the acid production is a metabolically dependent process, it does not reflect the intensity of metabolism, except partly in the first half of glycolysis.     

Synthesis of hydroquinone-α-glucoside by α-glucosidasefrom baker’s yeast

Hydroquinone-α-glucoside was synthesised from hydroquinone and maltose as glucosyl donor by transglucosylation in a water system with α-glucosidase from baker’s yeast. Only one phenolic –OH group was α-anomer-selectively glucosylated. The optimum conditions for transglucosylation reaction were at 30 °C for 20 h with 50 mM hydroquinone and 1.5 M maltose in 100 mM sodium citrate/phosphate buffer at pH 5.5. The glucoside was obtained at 0.6 mg/ml with a 4.6% molar yield with respect to hydroquinone.     

Degradation of Cellular Phospholipids and Softening of Pressed Baker’s Yeast

Variations in lipid components of washings and homogenate of pressed baker’s yeast were investigated during the storage of pressed baker’s yeast at 30°C. Washings represents the substances which had leaked out from cells. Homogenate represents those contained in whole cells. Lipids in yeast washings increased toward softening, the phospholipids in yeast homogenate decreased continuously during storage. Two stages, an earlier period of storage (Stage I) and a later period of storage (Stage II) were observed in the degradation of phospholipids. Free fatty acid which was the main degradation product of phospholipid accumulated in Stage II, particularly at softening. The order in phospholipid degradation was PC>PE>PI + PS (PI>PS). Moreover, when washings of stored yeast at softening were assayed using ¹⁴C-acyl PC, the release of ¹⁴C-acyl fatty acid was observed.

These results suggest that phospholipids were degraded by some phospholipid-deacylating enzymes toward softening. From the results of lipid analysis, we inferred that the responsible enzymes were phospholipases.     

Cell wall polysaccharides: before and after autolysis of brewer’s yeast

Brewer’s yeast is used in production of beer since millennia, and it is receiving increased attention because of its distinct fermentation ability and other biological properties. During fermentation, autolysis occurs naturally at the end of growth cycle of yeast. Yeast cell wall provides yeast with osmotic integrity and holds the cell shape upon the cell wall stresses. The cell wall of yeast consists of β-glucans, chitin, mannoproteins, and proteins that cross linked with glycans and a glycolipid anchor. The variation in composition and amount of cell wall polysaccharides during autolysis in response to cell wall stress, laying significant impacts on the autolysis ability of yeast, either benefiting or destroying the flavor of final products. On the other hand, polysaccharides from yeast cell wall show outstanding health effects and are recommended to be used in functional foods. This article reviews the influence of cell wall polysaccharides on yeast autolysis, covering cell wall structure changings during autolysis, and functions and possible applications of cell wall components derived from yeast autolysis.     

Effect of Specific Growth Rate on Fermentative Capacity of Baker’s Yeast

The specific growth rate is a key control parameter in the industrial production of baker’s yeast. Nevertheless, quantitative data describing its effect on fermentative capacity are not available from the literature. In this study, the effect of the specific growth rate on the physiology and fermentative capacity of an industrial Saccharomyces cerevisiae strain in aerobic, glucose-limited chemostat cultures was investigated. At specific growth rates (dilution rates, D) below 0.28 h⁻¹, glucose metabolism was fully respiratory. Above this dilution rate, respirofermentative metabolism set in, with ethanol production rates of up to 14 mmol of ethanol · g of biomass⁻¹ · h⁻¹ at D = 0.40 h⁻¹. A substantial fermentative capacity (assayed offline as ethanol production rate under anaerobic conditions) was found in cultures in which no ethanol was detectable (D < 0.28 h⁻¹). This fermentative capacity increased with increasing dilution rates, from 10.0 mmol of ethanol · g of dry yeast biomass⁻¹ · h⁻¹ at D = 0.025 h⁻¹ to 20.5 mmol of ethanol · g of dry yeast biomass⁻¹ · h⁻¹ at D = 0.28 h⁻¹. At even higher dilution rates, the fermentative capacity showed only a small further increase, up to 22.0 mmol of ethanol · g of dry yeast biomass⁻¹ · h⁻¹ at D = 0.40 h⁻¹. The activities of all glycolytic enzymes, pyruvate decarboxylase, and alcohol dehydrogenase were determined in cell extracts. Only the in vitro activities of pyruvate decarboxylase and phosphofructokinase showed a clear positive correlation with fermentative capacity. These enzymes are interesting targets for overexpression in attempts to improve the fermentative capacity of aerobic cultures grown at low specific growth rates.The quality of commercial baker’s yeast (Saccharomyces cerevisiae) is determined by many parameters, including storage stability, osmotolerance, freeze-thaw resistance, rehydration resistance of dried yeast, and color. In view of the primary role of baker’s yeast in dough, fermentative capacity (i.e., the specific rate of carbon dioxide production by yeast upon its introduction into dough) is a particularly important parameter (2).In S. cerevisiae, high sugar concentrations and high specific growth rates trigger alcoholic fermentation, even under fully aerobic conditions (6, 18). Alcoholic fermentation during the industrial production of baker’s yeast is highly undesirable, as it reduces the biomass yield on the carbohydrate feedstock. Industrial baker’s yeast production is therefore performed in aerobic, sugar-limited fed-batch cultures. The conditions in such cultures differ drastically from those in the dough environment, which is anaerobic and with sugars at least initially present in excess (23).Optimization of biomass productivity requires that the specific growth rate and biomass yield in the fed-batch process be as high as possible. In the early stage of the process, the maximum feasible growth rate is dictated by the threshold specific growth rate at which respirofermentative metabolism sets in. In later stages, the specific growth rate is decreased to avoid problems with the limited oxygen transfer and/or cooling capacity of industrial bioreactors (10, 27). The actual growth rate profile during fed-batch cultivation is controlled primarily by the feed rate profile of the carbohydrate feedstock (4, 22). Generally, an initial exponential feed phase is followed by phases with constant and declining feed rates, respectively (8).From a theoretical point of view, the objective of suppressing alcoholic fermentation during the production phase may interfere with the aim of obtaining a high fermentative capacity in the final product. Process optimization has so far been based on strain selection and on empirical optimization of environmental conditions during fed-batch cultivation (e.g., pH, temperature, aeration rate, and feed profiles of sugar, nitrogen, and phosphorus [5, 10, 23]). For rational optimization of the specific growth rate profile, knowledge of the relation between specific growth rate and fermentative capacity is of primary importance. Nevertheless, quantitative data on this subject cannot be found in the literature.The chemostat cultivation system allows manipulation of the specific growth rate (which is equal to the dilution rate) while keeping other important growth conditions constant. Similar to industrial fed-batch cultivation, sugar-limited chemostat cultivation allows fully respiratory growth of S. cerevisiae on sugars (21, 37, 39). This is not possible in batch cultures, which by definition require high sugar concentrations, which lead to alcoholic fermentation, even during aerobic growth (6, 18, 37). Thus, as an experimental system, batch cultures bear little resemblance to the aerobic baker’s yeast production process. Indeed, we have recently shown that differences in fermentative capacity between a laboratory strain of S. cerevisiae and an industrial strain became apparent only in glucose-limited chemostat cultures but not in batch cultures (30).The aim of the present study was to assess the effect of specific growth rate on fermentative capacity in an industrial baker’s yeast strain grown in aerobic, sugar-limited chemostat cultures. Furthermore, the effect of specific growth rate on in vitro activities of key glycolytic and fermentative enzymes was investigated in an attempt to identify correlations between fermentative capacity and enzyme levels.     

Activation of Yeast Mitochondrial Translation: Who Is in Charge?

Mitochondrial genome has undergone significant reduction in a course of evolution; however, it still contains a set of protein-encoding genes and requires translational machinery for their expression. Mitochondrial translation is of the prokaryotic type with several remarkable differences. This review is dedicated to one of the most puzzling features of mitochondrial protein synthesis, namely, the system of translational activators, i.e., proteins that specifically regulate translation of individual mitochondrial mRNAs and couple protein biosynthesis with the assembly of mitochondrial respiratory chain complexes. The review does not claim to be a comprehensive analysis of all published data; it is rather focused on the idea of the “core component” of the translational activator system.     

Accumulation of Nicotinamide Adenine Dinucleotide in Baker’s Yeast by Secondary Culture

A study was made to determine a method for the production of NAD using baker’s yeast, and a suitable secondary culture condition for the accumulation of NAD was established. From the study the following results were obtained: Nicotinamide, nicotinic acid and adenine were effective on the accumulation of NAD. However, ribose or tryptophan — one of the precursor of NAD — was not effective. NaF, KCN or NaN₃ — metabolic inhibitors — inhibited the accumulation of NAD. Baker’s yeast obtained from commercial source was cultured secondarily in the medium containing 0.3% adenine, 0.6% nicotinamide in 0.2 M K₂HPO₄ (50% fresh yeast was added), pH 4.5. Under this optimal condition, NAD content reached about 12 mg/g dry cells (corresponding to 2.0 mg/ml medium), and it corresponded to about 20 times that of the initial content.     

Purification and Properties of a Thermo-labile Antigen from Baker’s Yeast Cells

A thermo-labile antigen (TLA) on the yeast cell surface was isolated from a yeast cell autolyzate and purified to a homogeneous state by chromatography on an immunoadsorbent affinity column. The molecular weight of TLA was about 1.45 x 10⁵ on SDS-polyacrylamide gel electrophoresis and about 1.5 x l0⁵ on gel chromatography on Sephadex G-200. The TLA contained 74.5% protein and 25.5% sugar. It was characterized by high contents of glycine, glutamic acid, serine and aspartic acid. Half-cystine, methionine, histidine and arginine were not found. The sugar moiety was composed of galactose, mannose, N-acetylglucosamine and fucose. The antigenic determinant of TLA was distinct from that of cell wall mannan in the Ouchterlony immunodiffusion test. No precipitin line against anti-TLA serum was observed, when TLA was heated at 90°C for 10 min. Oxidation with periodate had little effect on antigenicity, but digestion with Pronase or treatment with protein denaturants resulted in loss of the antigenicity. These results suggest that the protein moiety plays an important role as the antigenic determinant of TLA. Moreover, the antiserum specific to TLA agglutinated fresh yeast cells, and the distribution of TLA was apparent on the yeast cell surface by immunofluorescence staining. These findings suggest that TLA molecules were exposed on the outer surface of the yeast cell wall.     

Incorporation of 14C-Tyrosine into Soluble Ribonucleic Acid from Baker’s Yeast

The incorporation of ¹⁴C-tyrosine into S-RNA catalyzed by a partially purified tyrosine activating enzyme from baker’s yeast was observed. The maximum incorporation was shown in the presence of 5 μmoles of ATP, 10 μmoles of MgCl₂ and 10~100 μmoles of KCl in the reaction mixture of total volume of 1ml, at pH 7.8 when 1.2 mg of S-RNA, 0.1 μmole of ¹⁴C-tyrosine and 400 μg of enzyme protein were used. Beyond the concentration of ATP, MgCl₂ and KCl described above, the tendency of inhibition was observed. The incorporation was strongly inhibited by pCMB and reactivated by cysteine. Manganese and calcium ions were effective as substitutes for magnesium. S-RNA used was prepared from whole baker’s yeast cell with phenol, but S-RNA obtained from the supernatant of the ground yeast had lost its incorporating activity.     

Degradation of Phospholipids and Liquefaction of Pressed Baker’s Yeast by Acetic Acid Vapour

When pressed baker’s yeast (Saccharomyces cerevisiae) was exposed to the vapour of acetic acid, autolysis of yeast cells was induced in 3 or 4 hr. In order to elucidate the mechanism of the autolysis caused by the AcOH-treatment, we investigated variations in the lipid content of yeast cells during the treatment. The degradation of phospholipids and the accumulation of free fatty acids occurred within 3 hr. Formic acid exerted a similar effect on the pressed yeast. The effect of propionic acid was not seen in 3hr but was after 18 hr. When the homogenate of fresh yeast cells was incubated in the acidic region below pH 4.5 for 1 hr, phospholipids were hydrolyzed and free fatty acids were accumulated. Such deacylation of phospholipids was observed even at pH 6 on incubation for 12hr, but not observed at pH 7 or above pH 9. At pH 8, although phospholipids were somewhat degraded, free fatty acids almost never accumulated but diacylglycerol did accumulate.

Therefore, yeast cells have inherently phospholipid-acylhydrolases and, on AcOH-treatment, such enzymes may degrade membrane phospholipids to induce the autolysis of pressed yeast.