Growth characteristics of bakers' yeast in ethanol

The influence of temperature (15 degrees -40 degrees C) and pH (2.5-6.0) on the continuous growth of bakers' yeast (Saccharomyces cerevisiae) at steady state in 1% ethanol was investigated. Optimal temperature and pH were 30 degrees C and 4.5, respectively. The short-term effect of ethanol concentration (0.1-10.0%) on the yeast growth was assessed in batch culture. Up to 1% of ethanol, the yeast growth increased in function of the ethanol concentration in the medium. The biomass reached a maximum within the interval of 1-4% of ethanol (7.9 and 31.6 g/L, respectively) and decreased at higher concentrations. The residual ethanol concentration in the medium increased rapidly when the initial ethanol concentration exceeded 4%. The best-fit model obtained for growth inhibition as a function of ethanol concentrations was that of Tseng and Wayman: mu(m)S/)K + S( - i (S - S(theta)). With this model, the specific growth rate (mu) decreased linearly as the ethanol concentration increased between the threshold value (S(theta)) of 11.26 g/L to be fully inhibited at 70.00 g/L (S;) an inhibition constant (i) of 0.0048 g L(-1) h(-1), a maximum specific growth rate (mu(m)) of 0.284 h(-1), and a saturation constant (K) of 0.611 g/L were obtained.     

Production of bakers' yeast in cheese whey ultrafiltrate

A process for the production of bakers' yeast in whey ultrafiltrate (WU) is described. Lactose in WU was converted to lactic acid and galactose by fermentation. Streptococcus thermophilus was selected for this purpose. Preculturing of S. thermophilus in skim milk considerably reduced its lag. Lactic fermentation in 2.3x-concentrated WU was delayed compared with that in unconcentrated whey, and fermentation could not be completed within 60 h. The growth rate of bakers' yeast in fermented WU differed among strains. The rate of galactose utilization was similar for all strains, but differences in lactic acid utilization occurred. Optimal pH ranges for galactose and lactic acid utilization were 5.5 to 6.0 and 5.0 to 5.5, respectively. The addition of 4 g of corn steep liquor per liter to fermented WU increased cell yields. Two sources of nitrogen were available for growth of Saccharomyces cerevisiae: amino acids (corn steep liquor) and ammonium (added during the lactic acid fermentation). Ammonium was mostly assimilated during growth on lactic acid. This process could permit the substitution of molasses by WU for the industrial production of bakers' yeast.     

Computer control of bakers' yeast production

The Biotechnology and Bioengineering study presented here was undertaken to demonstrate the usefulness of computer control for the production of yeast from molasses. A flexible control system was developed by using an on-line computer for the monitoring of cell mass and employing anticipatory control to maintain the maximum productivity. Process disturbances were minimized by employing a multivariable feedback control system to prevent ethanol formation. The control strategy acted to keep overall conversion yield at its maximum level, about 0.5 g cell/ g sugar, while maintaining high volumetric productivity between 3 and 5 g/liter-hr. Results are presented to show the effectiveness of simultaneous anticipatory and feedback contol in overcoming problems of oxygen starvation, molasses quality, and variable inoculum size.     

Phosphorylation-dephosphorylation of pyruvate dehydrogenase from bakers' yeast

The pyruvate dehydrogenase complex was purified to homogeneity from bakers' yeast (Saccharomyces cerevisiae). No pyruvate dehydrogenase kinase activity was detected at any stage of the purification. However, the purified pyruvate dehydrogenase complex was phosphorylated and inactivated with purified pyruvate dehydrogenase kinase from bovine kidney. The protein-bound radioactivity was localized in the pyruvate dehydrogenase alpha subunit. The phosphorylated, inactive pyruvate dehydrogenase complex was dephosphorylated and reactivated with purified pyruvate dehydrogenase phosphatase from bovine heart. Tryptic digestion of the 32P-labeled complex yielded a single phosphopeptide, which was purified to homogeneity. The sequence of the phosphopeptide was established to be Tyr-Gly-Gly-His-Ser(P)-Met-Ser-Asp-Pro-Gly-Thr-Thr-Tyr-Arg. This sequence is very similar to the sequence of a tryptic phosphotetradecapeptide derived from the alpha subunit of bovine kidney and heart pyruvate dehydrogenase: Tyr-His-Gly-His-Ser(P)-Met-Ser-Asp-Pro-Gly-Val-Ser-Tyr-Arg.     

Effect of growth conditions and trehalose content on cryotolerance of bakers' yeast in frozen doughs

The cryotolerance in frozen doughs and in water suspensions of bakers' yeast (Saccharomyces cerevisiae) previously grown under various industrial conditions was evaluated on a laboratory scale. Fed-batch cultures were very superior to batch cultures, and strong aeration enhanced cryoresistance in both cases for freezing rates of 1 to 56 degrees C min. Loss of cell viability in frozen dough or water was related to the duration of the dissolved-oxygen deficit during fed-batch growth. Strongly aerobic fed-batch cultures grown at a reduced average specific rate (mu = 0.088 h compared with 0.117 h) also showed greater trehalose synthesis and improved frozen-dough stability. Insufficient aeration (dissolved-oxygen deficit) and lower growth temperature (20 degrees C instead of 30 degrees C) decreased both fed-batch-grown yeast cryoresistance and trehalose content. Although trehalose had a cryoprotective effect in S. cerevisiae, its effect was neutralized by even a momentary lack of excess dissolved oxygen in the fed-batch growth medium.     

Monitoring of Saccharomyces cerevisiae in commercial bakers' yeast fermentation

In the highly competitive market of commercial bakers' yeast, fermentations are operated for maximum efficiency and minimum production cost. In order to maintain competitiveness, the fermentations must be highly consistent with minimum variation in yeast performance, maximum yield on raw materials, and minimum production of undesirable side products. The use of advanced instrumentation is of critical importance to achieving these goals by the production engineer. An in situ optical density probe was used to determine the yeast cell density in full-scale commercial bakers' yeast fermentations. The optical density probe results were compared with oxygen uptake rate analyses, packed cell volume, and off-line measured cell dry weights. The most accurate measurement of cell density was found to be the optical density probe. This instrument allowed the on-line determination of cell density with highly consistent results from fermentation batch to batch and with out the need for intermittent recalibration. (c) 1995 John Wiley & Sons, Inc.     

Characterization of fructose 1,6-bisphosphatase from bakers' yeast

Active nonphosphorylated fructose bisphosphatase (EC 3.1.3.11) was purified from bakers' yeast. After chromatography on phosphocellulose, the enzyme appeared as a homogeneous protein as deduced from polyacrylamide gel electrophoresis, gel filtration, and isoelectric focusing. A Stokes radius of 44.5 A and molecular weight of 116,000 was calculated from gel filtration. Polyacrylamide gel electrophoresis of the purified enzyme in the presence of sodium dodecyl sulfate resulted in three protein bands of Mr = 57,000, 40,000, and 31,000. Only one band of Mr = 57,000 was observed, when the single band of the enzyme obtained after polyacrylamide gel electrophoresis in the absence of sodium dodecyl sulfate was eluted and then resubmitted to electrophoresis in the presence of sodium dodecyl sulfate. Amino acid analysis indicated 1030 residues/mol of enzyme including 12 cysteine moieties. The isoelectric point of the enzyme was estimated by gel electrofocusing to be around pH 5.5. The catalytic activity showed a maximum at pH 8.0; the specific activity at the standard pH of 7.0 was 46 units/mg of protein. Fructose 1,6-bisphosphatase b, the less active phosphorylated form of the enzyme, was purified from glucose inactivated yeast. This enzyme exhibited maximal activity at pH greater than or equal to 9.5; the specific activity measured at pH 7.0 was 25 units/mg of protein. The activity ratio, with 10 mM Mg2+ relative to 2 mM Mn2+, was 4.3 and 1.8 for fructose 1,6-bisphosphatase a and fructose 1,6-bisphosphatase b, respectively. Activity of fructose 1,6-bisphosphatase a was 50% inhibited by 0.2 microM fructose 2,6-bisphosphate or 50 microM AMP. Inhibition by fructose 2,6-bisphosphate as well as by AMP decreased with a more alkaline pH in a range between pH 6.5 and 9.0. The inhibition exerted by combinations of the two metabolites at pH 7.0 was synergistic.     

Effect of sodium chloride on a lipid bilayer

Electrostatic interactions govern structural and dynamical properties of membranes and can vary considerably with the composition of the aqueous buffer. We studied the influence of sodium chloride on a pure POPC lipid bilayer by fluorescence correlation spectroscopy experiments and molecular dynamics simulations. Increasing sodium chloride concentration was found to decrease the self-diffusion of POPC lipids within the bilayer. Self-diffusion coefficients calculated from the 100 ns simulations agree with those measured on a millisecond timescale, suggesting that most of the relaxation processes relevant for lipid diffusion are faster than the simulation timescale. As the dominant effect, the molecular dynamics simulations revealed a tight binding of sodium ions to the carbonyl oxygens of on average three lipids leading to larger complexes with reduced mobility. Additionally, the bilayer thickens by approximately 2 A, which increases the order parameter of the fatty acyl chains. Sodium binding alters the electrostatic potential, which is largely compensated by a changed polarization of the aqueous medium and a lipid dipole reorientation.     

Lipid content and cryotolerance of bakers' yeast in frozen doughs

The relationship between lipid content and tolerance to freezing at -50 degrees C was studied in Saccharomyces cerevisiae grown under batch or fed-batch mode and various aeration and temperature conditions. A higher free-sterol-to-phospholipid ratio as well as higher free sterol and phospholipid contents correlated with the superior cryoresistance in dough or in water of the fed-batch-grown compared with the batch-grown cells. For both growth modes, the presence of excess dissolved oxygen in the culture medium greatly improved yeast cryoresistance and trehalose content (P. Gélinas, G. Fiset, A. LeDuy, and J. Goulet, Appl. Environ. Microbiol. 26:2453-2459, 1989) without significantly changing the lipid profile. Under the batch or fed-batch modes, no correlation was found between the cryotolerance of bakers' yeast and the total cellular lipid content, the total sterol content, the phospholipid unsaturation index, the phosphate or crude protein content, or the yeast cell morphology (volume and roundness).     

Metabolic regulation of aminoacyl-tRNA synthetase biosynthesis in bakers' yeast.

The specific activities of 15 aminoacyl-tRNA synthetases in Saccharomyces cerevisiae were measured after growth under a variety of conditions that produced a range of cell-doubling times. The specific activity of each synthetase increased as cell-doubling time decreased. Control experiments eliminate the possibility that these results are due to preferential recovery of synthetases, or to the presence of activators in the faster growing cultures or inhibitors in the slower growing ones. These observations run counter to the expectation that synthetases in bacteria and yeast are negatively regulated by free amino acids, or, more likely, by aminoacyl-tRNA. In fact, as the growth medium was enriched, generation times decreased, and synthetase and aminoacyl-tRNA levels increased. It is suggested that cytoplasmic aminoacyl-tRNA synthetases may be more or less coordinately controlled such that their response to growth follows the pattern observed for ribosome production and RNA synthesis. This suggests the possibility of coordinated response of genes for components of the protein synthetic apparatus.     

Regulatory aspects of bakers' yeast metabolism in aerobic fed-batch cultures

A highly instrumented computer-coupled bioreactor is used to investigate metabolic changes of Saccharomyces cerevisiae in aerobic fed-batch systems which are generally applied in bankers' yeast manufacture. The four types of metabolism (oxidation of glucose, aerobic fermentation, oxidation of glucose and ethanol, and oxidation of ethanol) appearing in such systems are characterized by four significant fermentation parameters: Respiratory quotient (RQ), glucose uptake rate (Q_g), ethanol turnover rate (Q_EtOH), and growth yield on glucose (Y_g). Below the critical glucose concentration glucose and ethanol are utilized simultaneously. The shift from aerobic fermentation to nondiauxic growth on glucose and ethanol is not only dependent on glucose concentration. but also on the precultivation on cells. The uptake of ethanol is controlled by the glucose supply except in the case when ethanol is limiting; the oxygen uptake rate (Q_o2), however, is unaffected by the ratio of Q_g and Q_EtOH. Critical glucose concentration is not a constant value for a particular strain, but varies corresponding to the nutritional state of the cells.     

Purification and properties of alpha-mannosidase from bakers' yeast.

The yeast alpha-mannosidase [EC 3.2.1.24] was purified 1160-fold from the crude extract of the autolysate. The purified preparation was practically free from alpha-glucosidase, beta-glucosidase, alpha-galactosidase, beta-galactosidase, beta-mannosidase, and beta-N-acetylhexosaminidase activities. After the separation of yeast mannan during the purification procedures the enzyme became unstable but could be stored at 5 degrees C for three weeks with 50% loss of activity. The purified enzyme hydrolyzed both aryl and alkyl mannosides, but hydrolysis of yeast mannan proceeded slowly. Yeast mannan and Zn2+ increased the enzyme catalyzed hydrolysis of p-nitrophenyl mannoside, whereas NaN3, monoiodoacetate and methyl alpha-D-mannoside acted as inhibitors. The molecular weight was estimated to be 450,000 by gel filtration.     

Inactivation of bakers' yeast glucose-6-phosphate dehydrogenase by aluminum

Preincubation of yeast glucose-6-phosphate dehydrogenase (G6PD) with Al(III) produced an inactive enzyme containing 1 mol of Al(III)/mol of enzyme subunit. None of the enzyme-bound Al(III) was dissociated by dialysis against 10 mM Tris-HCl, pH 7.0, containing 0.2 mM EDTA at 4 degrees C for 24 h. Citrate, NADP+, EDTA, or NaF protected the enzyme against the Al(III) inactivation. The Al-(III)-inactivated enzyme, however, was completely reactivated only by citrate and NaF. The dissociation constant for the enzyme-aluminum complex was calculated to be 4 x 10(-6)M with NaF, a known reversible chelator for aluminum. Modification of histidine and lysine residues of the enzyme with diethyl pyrocarbonate and acetylsalicylic acid, respectively, inactivated the enzyme. However, the modified enzyme still bound 1 mol of Al(III)/mol of enzyme subunit. Circular dichroism studies showed that the binding of Al(III) to the enzyme induced a decrease in alpha-helix and beta-sheet and an increase in random coil. Therefore, it is suggested that inactivation of G6PD by Al(III) is due to the conformational change induced by Al(III) binding.