Biosynthesis of invertase by Saccharomyces cerevisiae with sugarcane molasses as substrate

Biosynthesis of invertase by Saccharomyces cerevisiae 01K32 was inversely proportional to the concentration of sugarcane blackstrap molasses included in the medium. In a fermenter, an intracellular invertase activity of 440 U/g dry cells was obtained.     

Flocculation of industrial and laboratory strains ofSaccharomyces cerevisiae

Summary A comparative study has been made of different laboratory and industrial wild-type strains ofSaccharomyces cerevisiae in relation to their flocculation behavior. All strains were inhibited by mannose and only one by maltose. In regard to the stability of these characters in the presence of proteases and high salt concentrations, a relevant degree of variation was found among the strains. This was to such an extent that it did not allow their inclusion in the Flol or NewFlo phenotypes. Genetic characterization of one wild-type strain revealed that the flocculation-governing gene was allelic toFLO1 found in genetic strains.This paper is dedicated to Professor Herman Jan Phaff in honor of his 50 years of active research which still continues.     

Changes in the intracellular concentrations of the adenosine phosphates and nicotinamide adenine dinucleotides ofSaccharomyces cerevisiae during batch fermentation

Significant changes in the intracellular concentrations of adenosine phosphates and nicotinamide adenine dinucleotides were observed during fermentation of grape must by three different strains ofSaccharomyces cerevisiae: S. cerevisiae var.cerevisiae, a typical fermentative yeast strain and two flor-veil-forming strains,S. cerevisiae var.bayanus andS. cerevisiae var.capensis. The intracellular concentration of ATP was always higher inS. cerevisiae var.cerevisiae than in the flor-veil-forming strains. NAD⁺ and NADP⁺ concentrations decreased at faster rates in the flor-veil-forming yeasts than in the other yeast but NADH concentration was the same in all yeasts for the first 10 days of fermentation. NADPH concentration was always lower inS. cerevisiae var.cerevisiae than in the other yeasts and this yeast also showed higher rates of growth and fermentation during the early stages of the fermentation and the presence of non-viable cells at the end of fermentation. In contrast, the flor-veil-forming strains maintained growth and fermentation capabilities for a relatively long time and viable cells were present throughout the entire fermentation process (31 days).The authors are with the Department of Microbiology, Faculty of Sciences, University of Cordoba, Avda. San Alberto Magno s/n, 14004-Córdoba, Spain     

Electron microscopy of germinating ascospores ofSaccharomyces cerevisiae

The wall of mature ascospores ofSaccharomyces cerevisiae showed in sections under the electron microscope a dark outer layer and a lighter inner layer. The latter was composed of a greyish inner part and a light outer part. During germination, the spore grew out at one side and the dark outer layer was broken. Of the light inner layer, the inner greyish part became the wall of the vegetative cell, but the extented part of the cell had a new wall.     

A possible application of ale brewery strains ofSaccharomyces cerevisiae in lager beer production

The physiological characteristics of two strains of brewery ale yeasts,Saccharomyces cerevisiae, with sedimentation abilities, were investigated to see if the strains were suitable for lager beer production. Compared with typical industrial ale strains ofS. cerevisiae and lager strains ofS. uvarum (nowS. cerevisiae), the investigated strains differ in fermentation dynamics, as well as in biological properties. The differences, however, particularly between the two strains and the lager brewing yeasts, were not significant.     

Study of sugarcane pieces as yeast supports for ethanol production from sugarcane juice and molasses

Due to the environmental concerns and the increasing price of oil, bioethanol was already produced in large amount in Brazil and China from sugarcane juice and molasses. In order to make this process competitive, we have investigated the suitability of immobilized Saccharomyces cerevisiae strain AS2.1190 on sugarcane pieces for production of ethanol. Electron microscopy clearly showed that cell immobilization resulted in firm adsorption of the yeast cells within subsurface cavities, capillary flow through the vessels of the vascular bundle structure, and attachment of the yeast to the surface of the sugarcane pieces. Repeated batch fermentations using sugarcane supported-biocatalyst were successfully carried out for at least ten times without any significant loss in ethanol production from sugarcane juice and molasses. The number of cells attached to the support increased during the fermentation process, and fewer yeast cells leaked into fermentation broth. Ethanol concentrations (about 89.73–77.13 g/l in average value), and ethanol productivities (about 59.53–62.79 g/l d in average value) were high and stable, and residual sugar concentrations were low in all fermentations (0.34–3.60 g/l) with conversions ranging from 97.67–99.80%, showing efficiency (90.11–94.28%) and operational stability of the biocatalyst for ethanol fermentation. The results of this study concerning the use of sugarcane as yeast supports could be promising for industrial fermentations. L. Liang and Y. Zhang have contributed equally to this work.     

Growth of Saccharomyces cerevisiae in a chemostat under high glucose conditions

Saccharomyces cerevisiae was grown in a chemostat under high glucose conditions (up to 300 g l^–1). The results support the view that higher glucose feed favors higher ethanol production regardless of the existence of osmotic stress. A low glucose utilization and yield coefficient provides an opportunity to improve continuous fermentation performance in the fuel alcohol industry. The possibility exists of reusing yeast cells and subsequently lower operating costs, and by using an optimal glucose feeding concentration between 100 and 200 g l^–1.     

Reassembly of microtubules in protoplasts ofSaccharomyces cerevisiae after nocodazole-induced depolymerization

Summary By following microtubule neoformation after their complete destruction by nocodazole, we analyzed the pattern of microtubule nucleation in protoplasts ofSaccharomyces cerevisiae. Using immunofluorescence, the drug was shown to induce rapid and complete disassembly of both cytoplasmic and spindle microtubules and to selectively block protoplast nuclear division at a defined stage of the cell cycle. Treated protoplasts placed in a drug-free environment recovered a more abundant microtubular system. The majority of microtubules re-formed at SPBs whereas a minority of free-ended microtubules nucleated in the cytoplasm of the protoplasts without any detectable association with recognizable nucleation sites. Random nucleation of free microtubules might be induced by high amounts of unpolymerized tubulin likely to be present in the protoplasts at the moment of drug release.Abbreviations MT microtubule - NOCO nocodazole - SPBs spindle pole bodies - PMSF phenylmethylsulfonyl fluoride - BSA bovine serum albumine - sMT spindle microtubule - cMT cytoplasmic microtubule - MTOC microtubule organizing center     

Chromium uptake bySaccharomyces cerevisiae and isolation of glucose tolerance factor from yeast biomass

Fermentations with yeastSaccharomyces cerevisiae in semiaerobic and in static conditions with the addition of chromic chloride into the used molasses medium were analysed. It was proved that the addition of optimal amounts of CrCl₃ into the basal medium enhanced the kinetics of alcohol fermentations. The addition of 200 mg/l CrCl₃ into the medium stimulated both the yeast growth and the ethanol production in all experimental conditions. On the other hand, the results showed that Cr³⁺ ions were incorporated into yeast cells during fermentation. Under these conditions the accumulation of Cr³⁺ ions was performed by yeast cells during the exponential growth phase, and with enriched amounts of 30–45 (μg/g_d.m. of cells. Yeast biomass enriched with chromium ions was extracted with 01 mol/l NH₄OH assuming that the extracts had the glucose tolerance factor (GTF). Then the extracts were passed through a gel-filtration column in order to isolate and purify the GTF. The presence of GTF in the purified fractions was determined by measuring the absorbance at 260 nm. It is evident from the obtained results that the added purified fractions enhanced the rates of CO₂ production as well as the glucose utilization during alcoholic fermentation. As expected, the enhancement of both rates depended on the amounts of extracts added to the fermentation substrate. Thus, it is evident that purified extracts contained the GTF compound, and that Cr³⁺ ions were bonded to the protein molecule.     

Phytate dephosphorylation by free and immobilized cells ofSaccharomyces cerevisiae

Summary Saccharomyces cerevisiae in the form of baker's yeast, cells cultivated on a yeast extract-peptone-glucose medium, as well as cells immobilized in 18% (w/v) polyacrylamide gel showed the ability to hydrolyze 1.727 mM sodium phytate solution at 45°C, pH 4.6, in a stirred tank reactor. Seventy percent yield of dephosphorylation was observed after 2 h using a baker's yeast concentration of 5.8 g dry matter per 100 ml. Hydrolytic activity at 1.8–2.0 M Pi min^–1 was observed between 1st and 3rd h of the reaction in cells cultured 24 or 48 h. No inhibition by the substrate was found at sodium phytate concentrations of 0.587–1.727 mM. After 1.5 h of hydrolysis a single, well distinguished peak ofmyo-inositol-triphosphate was the main product found. By means of immobilization the stability of the biocatalyst was enhanced 3.3-fold and reached its half-life at 64 ninety-minute runs.     

Modeling simultaneous glucose and xylose uptake in Saccharomyces cerevisiae from kinetics and gene expression of sugar transporters

A kinetic model for glucose and xylose co-substrate uptake in Saccharomyces cerevisiae is presented. The model couples the enzyme kinetics with the glucose-dependent genetic expression of the individual transport proteins. This novel approach implies several options for optimizing the co-substrate utilization. Interestingly, the simulations predict a maximum xylose uptake rate at a glucose concentration >0 g/L, which suggests that the genetic expressions of the considered transport proteins are of importance when optimizing the xylose uptake. This was also evident in fed-batch simulations, where a distinct optimal glucose addition rate >0 g/L x h was found. Strategies for improving the co-substrate utilization by genetic engineering of the transport systems are furthermore suggested based on simulations.     

Cell-recycle batch fermentation using immobilized cells of flocculent Saccharomyces cerevisiae wine strains

Five, highly flocculeng strains of Saccharomyces cerevisiae, isolated from wine, were immobilized in calcium alginate beads to optimize primary must fermentation. Three cell-recycle batch fermentations (CRBF) of grape musts were performed with the biocatalyst and the results compared with those obtained with free cells. During the CRBF process, the entrapped strains showed some variability in the formation of secondary products of fermentation, particularly acetic acid and acetaldehyde. Recycling beads of immobilized flocculent cells is a good approach in the development and application of the CRBF system in the wine industry.     

Expression of fungal phytase on the cell surface ofSaccharomyces cerevisiae

Phytase improves the bioavailability of phytate phosphorus in plant foods to humans and animals, and reduces the phosphorus pollution of animal waste. We have engineered the cell surface of the yeast,Saccharomyces cerevisiae by anchoring active fungal phytase on its cell wall, in order to apply it as a dietary supplement containing bioconversional functions in animal foods and a whole cell bio-catalyst for the treatment of waste. The phytase gene (phyA) ofAspergillus niger with a signal peptide of rice amylase 1A (Ramy1A) was fused with the gene encoding the C-terminal half (320 amino acid residues from the C-terminus) of yeast α-agglutinin, a protein which is involved in mating and is covalently anchored to the cell wall. The resulting fusion construct was introduced intoS. cerevisiae and expressed under the control of the constitutive glyceraldehydes-3-phosphate dehydrogenase (GPD) promoter. Phytase plate assay revealed that the surface-engineered cell exhibited a catalytically active opaque zone which was restricted to the margin of the colony. Additionally, the phytase activity was detected in the cell fraction, but was not detected in the culture medium when it was grown in liquid. These results indicate that the phytase was successfully anchored to the cell surface of yeast and was displayed as its active form. The amount of recombinant phytase on the surface of yeast cells was estimated to be 16,000 molecules per cell.     

Production of recombinant hirudin in galactokinase-deficientSaccharomyces cerevisiae by fed-batch fermentation with continuous glucose feeding

The artificial gene coding for anticoagulant hirudin was placed under the control of theGAL10 promoter and expressed in the galactokinase-deficient strain (Δgal1) ofSaccharomyces cereivisiae, which uses galactose only as a gratuitous inducer in order to avoid its consumption. For efficient production of recombinant hirudin, a carbon source other than galactose should be provided in the medium to support growth of the Δgal1 strain. Here we demonstrate the successful use of glucose in the fed-batch fermentation of the Δgal1 strain to achieve efficient production of recombinant hirudin, with a yield of up to 400 mg hirudin/L.     

The reconstitution of oxidative phosphorylation in mitochondria isolated from a ubiquinone-deficient mutant ofSaccharomyces cerevisiae

Mitochondria, isolated from the ubiquinone-deficient nuclear mutant ofSaccharomyces cerevisiae E3-24, are practically unable to oxidize exogenous substrates. Respiratory activity, coupled to ATP synthesis, can, however, be reconstituted by the simple addition of ethanolic solutions of ubiquinones. A minimal length of the isoprenoid side chain (3) was required for the restoration. Saturation of the reconstitution required a large amount of exogeneous ubiquinone, in excess over the normal content present in the mitochondria of the wild type strain. A similar pattern of reconstituted activities could be also obtained using sonicated inverted particles. Mitochondria and sonicated particles are also able to carry out a dye-mediated electron flow coupled to ATP synthesis in the absence of added ubiquinone, using ascorbate or succinate as electron donor. This demonstrates that the energy conserving mechanism at the third coupling site of the respiratory chain is fully independent of the presence of the large mobile pool of ubiquinone in the membrane.     

A new method for yeast recovery in batch ethanol fermentations: Filter aid filtration followed by separation of yeast from filter aid using hydrocyclones

In the Melle-Boinot process for alcohol production, centrifuges are normally used for yeast recovery at the end of a batch fermentation. Centrifuges are expensive equipment and represent an impressive part of the equipment costs in alcohol industries. In the present work, an alternative method for yeast recovery using less expensive equipment was studied. Instead of using centrifuges, yeast was separated from the fermented broth by filter aid filtration, followed by separation of yeast from the filter aid using hydrocyclones. A stainless steel plate-and-frame filter of filtration area 1.14 m² and two 30 mm hydrocyclones, which followed the Bradley and Rietema recommended proportions, were used in this work. The filter aid was perlite. Tests of direct separation of yeast from the fermented broth using the Bradley hydrocyclone proved to be completely unfeasible, since the maximal reduced total efficiency obtained was only 1%. When the hydrocyclones were used to separate perlite from the resuspended filtration cake, the perlite total separation efficiency obtained in the underflow was as high as 95% when using the Bradley hydrocyclone with an underflow diameter of 3 mm. To show the feasibility of the proposed new method of yeast recovery, a complete cycle of experiments, which included fermentation, yeast separation, and new fermentation using the recycled cells, was performed with good results.     

Expression and purification of ubiquitin-specific protease (UBP1) ofSaccharomyces cerevisiae in recombinantEscherichia coli

Truncated form of UBP1, an ubiquitin-specific protease ofSaccharomyces cerevisiae, was overexpressed inEscherichia coli. The hexahistidine residue (His₆) was fused to the N-terminus of truncated UBP1 and the corresponding recombinant protein was purified with high yield by immobilized metal affinity chromatography. The truncated form of UBP1 protein was functional to cleave ubiquitinated human growth hormone as substrate. Effects of pH and temperature were investigated in order to optimize deubiquitinating reactions for the truncated UBP1. Optimum temperature and pH for the cleavage reaction were 40°C and pH 8.0, respectively.     

Effect of C/N ratio and starch concentration on ethanol production from sago starch using recombinant yeast

Recombinant Saccharomyces cerevisiae YKU 131 (capable of expressing glucoamylase) was used to produce ethanol from sago starch. The optimum C/N ratio for ethanol production by the recombinant yeast was 7.9, where 4.7 and 10.1 g/l ethanol was produced from 20 and 40 g/l sago starch, respectively. At sago starch concentration higher than 40 g/l and C/N ratio higher than 10.4, glucoamylase production and rate of starch hydrolysis were reduced, which in turn, reduced ethanol production significantly. The theoretical yield of ethanol based on sago starch consumed in fermentation using 40 g/l was 72.6%. This yield was slightly lower than those obtained in fermentation using soluble starch such as potato and corn starch, which ranged from 80–90% as reported in the literature. However, S. cerevisiae YKU 131 could only utilize 62% of the total amount of starch added to a medium.     

Inactivation by glucose of phosphoenolpyruvate carboxykinase from Saccharomyces cerevisiae

Phosphoenolpyruvate carboxykinase showed high activity in Saccharomyces cerevisiae grown on gluconeogenic carbon sources. Addition of glucose to such cultures caused a rapid loss of the phosphoenolpyruvate carboxykinase activity. Fructose or mannose had the same effect as glucose, while 2-deoxyglucose or galactose were without effect. The inactivation was an irreversible process, since the regain of the activity was dependent of de novo protein synthesis. Cycloheximide did not prevent inactivation. All strains of the genus Saccharomyces tested showed inactivation of their phosphoenolpyruvate carboxykinase upon addition of glucose; this behaviour was not restricted to this genus.Non-Standard Abbreviations FbPase fructose bisphosphatase [EC 3.1.3.11 fructose-1,6-bisphosphate hydrolase] - PEPCK phosphoenolpyruvate carboxykinase [EC 4.1.49 ATP: oxalacetate carboxylase (transphosphorylating)] - YPE yeast-peptone-ethanol A preliminary account of these results was presented at the Fourth International Symposium on Yeasts, Vienna, Austria, July 1974     

Quantification of Saccharomyces cerevisiae viability using BacLight

Yeast viability can be accurately quantified using BacLight, a kit which so far has been used only for bacterial analysis. Upon staining, viable cells can be differentiated from non-viable ones by either confocal laser scanning microscopy (CLSM), epifluorescence microscopy, or flow cytometry. Using Saccharomyces cerevisiae as a model, viabilities quantified by CLSM deviated an average of 1.7% from the actual data, and those determined by flow-cytometry by 1.4%.