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PubMed2000

Regulation of fermentative capacity and levels of glycolytic enzymes in chemostat cultures of Saccharomyces cerevisiae.

Regulation of fermentative capacity was studied in chemostat cultures of two Saccharomyces cerevisiae strains: the laboratory strain CEN.PK113-7D and the industrial bakers' yeast strain DS28911. The two strains were cultivated at a fixed dilution rate of 0.10 h(-1) under various nutrient limitation regimes: aerobic and anaerobic glucose limitation, aerobic and anaerobic nitrogen limitation on glucose, and aerobic ethanol limitation. Also the effect of specific growth rate on fermentative capacity was compared in glucose-limited, aerobic cultures grown at dilution rates between 0.05 h(-1) and 0.40 h(-1). Biomass yields and metabolite formation patterns were identical for the two strains under all cultivation conditions tested. However, the way in which environmental conditions affected fermentative capacity (assayed off-line as ethanol production rate under anaerobic conditions) differed for the two strains. A different regulation of fermentative capacity in the two strains was also evident from the levels of the glycolytic enzymes, as determined by in vitro enzyme assays. With the exception of phosphofructokinase and pyruvate decarboxylase in the industrial strain, no clear-cut correlation between the activities of glycolytic enzymes and the fermentative capacity was found. These results emphasise the need for controlled cultivation conditions in studies on metabolic regulation in S. cerevisiae and demonstrate that conclusions from physiological studies cannot necessarily be extrapolated from one S. cerevisiae strain to the other.

Journal Article↗
PubMed2000

Productivity enhancement in l-sorbose fermentation using oxygen vector.

Sorbose, an intermediate of Vitamin-C is produced by biological oxidation of sorbitol by Acetobacter suboxydans. The utility of oxygen vector (N-hexadecane) in enhancing the sorbose accumulation and its productivity was examined for sorbitol to sorbose bioconversion process. Shake flask fermentations were conducted using 1% to 6% (v/v) N-hexadecane. Higher sorbose production was observed in shake flask containing 1-4% N-hexadecane as compared to shake flasks without N-hexadecane. A maximum of 82.12 kgm(-)(3) sorbose accumulated in 24 h by the addition of 4% N-hexadecane as against 64.83 kgm(-)(3) sorbose without the addition of N-hexadecane. However, the concentration of sorbose produced in the same time decreased when 5% and 6% N-hexadecane were used. Batch sorbose fermentation conducted using 4% N-hexadecane demonstrated decrease in the process time from 14 h to 12 h. The productivity increased from 14.3 kgm(-)(3) h(-)(1) to 16.7 kgm(-)(3) h(-)(1) when 4% N-hexadecane was used. Fed-batch fermentation using 4% N-hexadecane was over in 20 h with a productivity of 15.9 kgm(-)(3) h(-)(1), and a sorbose accumulation of 311.68 kgm(-)(3) was obtained. The same fed-batch fermentation finished in 25 h when no N-hexadecane was used. A productivity of 12.6 kgm(-)(3) h(-)(1) and a final sorbose accumulation of 316 kgm(-)(3) were obtained. The increase in productivity and lower process time were achieved by the addition of N-hexadecane to the fermentation medium.

Journal Article↗
PubMed2002

Breeding of brewer's yeast by hybridization between a top-fermenting yeast Saccharomyces cerevisiae and a cryophilic yeast Saccharomyces bayanus.

To improve the fermentability of a top-fermenting yeast at low-temperature, we performed hybridization trials between four top-fermenting Saccharomyces cerevisiae strains and a cryophilic yeast Saccharomyces bayanus YM84 with good fermentability at low-temperature. The hybrids selected using 5-bromo-4-chloro-3-indolyl-alpha-D-galactopyranoside were checked with pulsed-field gel electrophoresis and their brewing performance at the low-temperature of 10.5 degrees C was observed using small-scale (2 l) fermentation trials.

Journal Article↗
PubMed2004

Enhanced productivity of human lysozyme by pH-controlled batch fermentation of recombinant Saccharomyces cerevisiae.

Human lysozyme (HLY) was successfully produced by Saccharomyces cerevisiae with a plasmid (pHK501) containing a synthetic HLY gene connected with a native secretion-signal sequence under control of the promoter for the glyceraldehydes-3-phosphate dehydrogenase gene. For large-scale production, batch fermentation was adopted with 1 l SD (Leu(-)) minimal medium in a 2-l jar fermentor. While pH-uncontrolled fermentation gave 42.3 units/ml of HLY over a period of 72-h cultivation, HLY production increased to 74.5 units/ml by performing pH-controlled fermentation, although a longer fermentation time was needed for maximal HLY production. A pH-shift strategy was designed in this study, resulting in higher HLY production and a shorter fermentation time.

Journal Article↗
PubMed1999

Characterization of a PDR1 mutant allele from a clotrimazole-resistant sake yeast mutant with improved fermentative activity.

Clotrimazole-resistant mutants from various sake yeasts show improved fermentative activity in sake mash while retaining their parental advantages for sake making. These mutants also exhibit pleiotropic drug resistance (PDR) phenotypes. To investigate the relationship between the improvement of fermentative activity and PDR phenotypes, a PDR1 mutant allele (pdr1-h176) encoding a transcription factor was cloned from a clotrimazole-resistant mutant, HL176 (MATa/MATalpha), using PCR amplification. The nucleotide sequences of pdr1-h176 and its wild allele were determined. The mutant allele contained a missense point mutation (L309S) that can confer a PDR phenotype on yeast. This amino acid substitution is located in the conserved motif II in the inhibitory domain of Pdr1p, and is very close to the cluster of three mutation points (P298A, K302Q, and M308I) described by Carvajal et al. (Mol. Gen. Genet., 256, 406-415, 1997) in laboratory strains. A PDR1 wild allele of HL163, the parent strain of HL176, was replaced by pdr1-h176 using gene recombination at the homologous site. The resultant transformants (PDR1/pdr1-h176) showed the same PDR phenotype as HL176, and they fermented sake mash efficiently even in the final fermentation stage, while HL163 did not. The amino acid substitution (L309S) in pdr1-h176 was considered to be sufficient to improve the fermentative activity of sake yeast, in addition to conferring the PDR phenotype.

Journal Article↗
PubMedDate not supplied

Production of phytase (myo-inositolhexakisphosphate phosphohydrolase) by Aspergillus niger van Teighem in laboratory-scale fermenter.

The growth and production pattern of phytase by a filamentous fungus, Aspergillus niger van Teighem, were studied in submerged culture at varying agitation rates and controlled and uncontrolled pH conditions. Allowing the initial culture to grow under neutral condition with subsequent decline in pH resulted in increased phytase productivity. A maximum of 141 nkat/mL phytase was obtained when the broth pH was maintained at pH 2.5 as compared to 17 nkat/mL units at controlled pH 5.5. The culture morphology and rheological properties of the fermentation broth significantly varied with the agitation rate. The volumetric oxygen transfer coefficient was determined at different phases of fungal growth during batch fermentation using static gassing out and dynamic gassing out methods. The oxygen transfer coefficient (k(L)a) of the fermenter was found to be 125 h(-)(1) at 500 rpm as compared to 38 h(-)(1) at 200 rpm. The oxygen transfer rates at different phases of growth were significantly affected by cell mass concentration and fungal morphology. During the course of fermentation there was a gradual decline of k(L)a from 97 h(-)(1) on day 2 to 63 h(-)(1) on day 6 of fermentation, after which no significant change was observed. The degree of agitation considerably influenced the culture morphology where shear thinning of filamentous fungus was observed with the increase in agitation.

6-Phytase↗
PubMed1998

Enhancing xanthan fermentations by different modes of glucose feeding

This paper is the fourth in a series aimed at improving the understanding and operation of conventional agitated fermenters for the production of the commercially important gum, Xanthan. In the first, reproducible fermentations were established and this protocol was used in studies of different agitator types and of bulk mixing and dissolved oxygen concentration in the next two. Here, building on the previous work, the influence of different glucose feeding strategies on Xanthan production in a 20-L agitated fermenter under equivalent conditions of agitation and dissolved oxygen is reported. The biological performances in three types of fed-batch cultures (a two-step glucose addition, multiple glucose-pulse feeding and continuous feeding of glucose) are compared to two batch fermentations with different initial glucose concentrations. The work confirmed that improved performance cannot be achieved by increasing the initial glucose concentration above 50 g/L nor by a single 10 g/L pulse addition (initial glucose concentration of 40 g/L) while significant nitrogen is still present. On the other hand, the simple pulse and continuous feeding strategies, after nitrogen has been essentially exhausted and under conditions of nonlimiting dissolved oxygen and similar bulk mixing, can result in a greatly enhanced performance compared to batch fermentations. Using the final Xanthan gum concentration, the yield on glucose and the overall productivity as performance indices, values of 62 g/L, 0.82 g of Xanthan/g of glucose, and 0.72 g/(L.h), respectively, were obtained compared to literature values for conventional stirred bioreactors of 15-30 g/L, 0.27-0.86 g of Xanthan/g of glucose, and 0. 12-0.43 g/(L.h).

Journal Article↗
PubMed2005

Conjugated linoleic acid content and organoleptic attributes of fermented milk products produced with probiotic bacteria.

The effect of probiotic bacteria on the formation of conjugated linoleic acid (CLA), microbial growth, and organoleptic attributes (acidity, texture, and flavor) of fermented milk products was determined. Four probiotic bacteria, Lactobacillus rhamnosus, Propionibacterium freudenreichii subsp. shermanii 56, P. freudenreichii subsp. shermanii 51, and P. freudenreichii subsp. freudenreichii 23, were evaluated individually or in coculture with traditional yogurt cultures (Lactobacillus delbrueckii subsp. bulgaricus and Streptococcus salivarius subsp. thermophilus). The lipid source was hydrolyzed soy oil. L. rhamnosus, in coculture with yogurt culture, resulted in the highest content of CLA. Growth and CLA formation of propionibacteria were enhanced in the presence of yogurt cultures. Texture and flavor attributes of fermented milks produced with propionibacteria were significantly different than the fermented milks processed with yogurt cultures. The fermented milks processed with probiotic bacteria in coculture with yogurt cultures demonstrated similar acidity, texture, and flavor as the fermented milk produced with yogurt cultures.

Caseins↗
PubMed2003

Investigation by 13C-NMR and tricarboxylic acid (TCA) deletion mutant analysis of pathways for succinate formation in Saccharomyces cerevisiae during anaerobic fermentation.

NMR isotopic filiation of 13C-labelled aspartate and glutamate was used to explore the tricarboxylic acid (TCA) pathway in Saccharomyces cerevisiae during anaerobic glucose fermentation. The assimilation of [3-13C]aspartate led to the formation of [2,3-13C]malate and [2,3-13C]succinate, with equal levels of 13C incorporation, whereas site-specific enrichment on C-2 and C-3 of succinate was detected only with [3-13C]glutamate. The non-random distribution of 13C labelling in malate and succinate demonstrates that the TCA pathway operates during yeast fermentation as both an oxidative and a reductive branch. The observed 13C distribution suggests that the succinate dehydrogenase (SDH) complex is not active during glucose fermentation. This hypothesis was tested by deleting the SDH1 gene encoding the flavoprotein subunit of the SDH complex. The growth, fermentation rate and metabolite profile of the sdh1 mutant were similar to those of the parental strain, demonstrating that SDH was indeed not active. Filiation experiments indicated the reductive branch of the TCA pathway was the main pathway for succinate production if aspartate was used as the nitrogen source, and that a surplus of succinate was produced by oxidative decarboxylation of 2-oxoglutarate if glutamate was the sole nitrogen source. Consistent with this finding, a kgd1 mutant displayed lower levels of succinate production on glutamate than on other nitrogen sources, and higher levels of oxoglutarate dehydrogenase activity were observed on glutamate. Thus, the reductive branch generating succinate via fumarate reductase operates independently of the nitrogen source. This pathway is the main source of succinate during fermentation, unless glutamate is the sole nitrogen source, in which case the oxidative decarboxylation of 2-oxoglutarate generates additional succinate.

Anaerobiosis↗
PubMed1980

Cell surface measurements in hydrocarbon and carbohydrate fermentations.

Acinetobacter calcoaceticus was grown in 11-liter batch fermentations with hexadecane or sodium citrate as the sole source of carbon. Surface and interfacial tension measurements of the microbial broth indicated that surface-active compounds were being produced only during growth on the hydrocarbon substrate. Contact angle measurements of an aqueous drop on a smooth lawn of cells in a hexadecane bath indicated a highly hydrophobic surface of the cells in the initial stages of the hydrocarbon fermentation (120 degrees contact angle). At this stage, the entire cell population was bound to the hydrocarbon-aqueous interface. The contact angle dropped rapidly to approximately 45 degrees after 14 h into the fermentation. This coincided with a shift of the cell population to the aqueous phase. Thus, the cells demonstrated more hydrophilic characteristics in the later stages of the fermentation. Contact angles on cells grown on sodium citrate ranged from 18 to 24 degrees throughout the fermentation. The cells appear to be highly hydrophilic during growth on a soluble substrate. From the contact angle and aqueous-hydrocarbon interfacial tension, the surface free energy of the cells was calculated along with the cell-aqueous and cell-hydrocarbon interfacial tension. The results of these measurements were useful in quantitatively evaluating the hydrophobic nature of the cell surface during growth on hydrocarbons and comparing it with the hydrophilic nature of the cell surface during growth on a soluble substrate.

Journal Article↗
PubMed1981

Carbohydrate Fermentation by Streptococcus cremoris and Streptococcus lactis Growing in Agar Gels.

When lactic streptococci were embedded in agar gels and incubated at 30 degrees C, the end products of carbohydrate fermentation depended on the initial cell density, which determined the subsequent distribution and size of colonies in the gel. With high initial cell densities, microcolonies formed close together and lactose and glucose were converted almost entirely to lactate. However, inoculation with a small number of cells, which then grew to form widely spaced and comparatively large colonies, resulted in up to 30% diversion of end product, usually to formate, ethanol, and acetate. In these "low-colony-density" gel cultures, the initial rate of fermentation was exponential and only lactate was formed. However, this rate then became linear and fermentation became progressively more heterolactic. Streptococcus lactis ML(8) was the only strain among the 10 tested which remained homolactic. Incubation at temperatures either above or below the optimum for growth and metabolism decreased the diversion to end products other than lactate. The change from homo- to heterolactic fermentation appears to be caused by carbohydrate depletion in the vicinity of the colony, so that fermentation is then limited by the diffusion of substrate. Growth of cells on gel surfaces exposed to air resulted in up to 40% diversion of end product from lactate, mainly to CO(2), acetoin, 2,3-butanediol, and acetate. Six of the 12 Streptococcus cremoris strains tested remained homolactic under these aerobic conditions, whereas all 8 of the S. lactis strains tested, including ML(8), were heterolactic.

Journal Article↗
PubMed1983

Selection of wine yeasts for growth and fermentation in the presence of ethanol and sucrose.

To optimize the conversion of carbohydrates to ethanol, strains of several Saccharomyces species were examined for the ability to grow and ferment in a range of sucrose and ethanol concentrations. A total of 632 wine yeasts, most of them isolated from wineries in Andalusia and Extremadura, southwestern Spain, were subjected to screening and selection. Growth and fermentative capacity in different ethanol and sucrose concentrations varied from one strain to another. There was no correlation between growth and fermentative capacity. The best 35 strains grew in 15% ethanol and fermented in 18% ethanol. Ethanol accumulated, although at a reduced rate, after the cells stopped growing. Most yeast strains were highly fermentative in 50% sucrose. Some of them effectively utilized the carbohydrates of the culture, yielding final ethanol concentrations of > 14%. Of the 35 selected strains, 16 were promising for genetic analysis and breeding because of their capacity to sporulate. These strains were homothallic, and their spores were viable. The meiotic products analyzed so far were also homothallic.

Journal Article↗
PubMed1984

Fermentation of 6-Deoxyhexoses by Bacillus macerans.

Under anaerobic conditions Bacillus macerans ATCC 7068 fermented 6-deoxyhexoses (l-rhamnose, l-fucose, and d-fucose) to a mixture of 1,2-propanediol (PD), acetone, H(2), CO(2), and ethanol. The final PD concentration was proportional to the amount of l-rhamnose fermented ( approximately 0.9 mol of PD per mol of rhamnose). PD was not produced from hexoses (e.g., d-glucose or l-mannose), despite active fermentation of these substrates. Relative to the fermentation of d-glucose, the fermentation of l-rhamnose was accompanied by a twofold reduction in yield of H(2), CO(2), and cell mass. Exposure of cell extracts to l-rhamnose resulted in the transient appearance of an aldehyde intermediate. Cell extracts contained a pyridine nucleotide-linked lactaldehyde reductase activity which converted synthetic d- or l-lactaldehyde to PD. The data suggest an Embden-Meyerhof pathway for 6-deoxyhexose catabolism, with the formation of lactaldehyde by a conventional aldolase cleavage reaction and subsequent reduction to PD.

Journal Article↗
PubMed1984

Alcoholic Fermentation of d-Xylose by Yeasts.

Type strains of 200 species of yeasts able to ferment glucose and grow on xylose were screened for fermentation of d-xylose. In most of the strains tested, ethanol production was negligible. Nineteen were found to produce between 0.1 and 1.0 g of ethanol per liter. Strains of the following species produce more than 1 g of ethanol per liter in the fermentation test with 2% xylose: Brettanomyces naardenensis, Candida shehatae, Candida tenuis, Pachysolen tannophilus, Pichia segobiensis, and Pichia stipitis. Subsequent screening of these yeasts for their capacity to ferment d-cellobiose revealed that only Candida tenuis CBS 4435 was a good fermenter of both xylose and cellobiose under the test conditions used.

Journal Article↗
PubMed1984

Fermentation of cellodextrins by different yeast strains.

The fermentation of cellodextrins by eight yeast species capable of fermenting cellobiose was monitored. Only two of these species, Torulopsis molischiana and T. wickerhamii, were able to ferment beta-glucosides with a degree of polymerization between one and six. These two species showed exocellular beta-glucosidase activity. Four other species were able to ferment cellotriose, and the last two species only fermented cellobiose. These latter six species produced a beta-glucosidase capable of attacking cellodextrins, but this enzyme was endocellular.

Journal Article↗
PubMed1986

High-Efficiency Carbohydrate Fermentation to Ethanol at Temperatures above 40 degrees C by Kluyveromyces marxianus var. marxianus Isolated from Sugar Mills.

A number of yeast strains, isolated from sugar cane mills and identified as strains of Kluyveromyces marxianus var. marxianus, were examined for their ability to ferment glucose and cane syrup to ethanol at high temperatures. Several strains were capable of rapid fermentation at temperatures up to 47 degrees C. At 43 degrees C, >6% (wt/vol) ethanol was produced after 12 to 14 h of fermentation, concurrent with retention of high cell viability (>80%). Although the type strain (CBS 712) of K. marxianus var. marxianus produced up to 6% (wt/vol) ethanol at 43 degrees C, cell viability was low, 30 to 50%, and the fermentation time was 24 to 30 h. On the basis of currently available strains, we suggest that it may be possible by genetic engineering to construct yeasts capable of fermenting carbohydrates at temperatures close to 50 degrees C to produce 10 to 15% (wt/vol) ethanol in 12 to 18 h with retention of cell viability.

Journal Article↗
PubMed1989

Effect of yeast hulls on stuck and sluggish wine fermentations: importance of the lipid component.

The effect of yeast hulls (yeast ghosts) on sluggish or stuck white wine fermentations was studied. The enhancing effect on yeast growth and fermentation rate displayed by the hulls was shown to be similar to the effect provided by lipid extract from the same hulls. Unsaturated fatty acids and sterols were incorporated into the yeast from lipid extracts during fermentation carried out under oxygen-limited conditions. Adsorption of toxic medium-chain fatty acid (decanoic acid) onto the yeast hulls took place through a dialysis membrane. However, when the hulls were placed inside a dialysis bag, the increase in yeast growth and fermentation rate seen when freely suspended hulls were used did not occur. Accordingly, the effect of yeast hulls in preventing stuck fermentations cannot be attributed only to the adsorption and consequent removal of medium-chain fatty acids from the juice.

Journal Article↗
PubMed1993

Occurrence of killer yeasts in spontaneous wine fermentations from the tuscany region of Italy.

The occurrence of killer yeasts in an area of Tuscany (central Italy) was studied. Killer yeasts were found in 88% of spontaneous wine fermentations from 18 wineries. The incidence of killers varied with respect to fermentation stage and vintage period, increasing from the first vintage to successive ones and from the commencement to the end of fermentation. At the end of fermentation, the proportion of killer strains relative to total yeast population was below 25% in 15 cases, above 75% in 6 cases, from 25 to 50% in 5 cases, and from 50 to 75% in 3 cases. Karyotype analysis also showed a mixed killer population in the fermentations in which the killers dominated.

Journal Article↗