Effect of feed zone in fed-batch fermentations of Saccharomyces cerevisiae

In production-scale, fed-batch fermentations, feed is often added to a single point at the top of the fermentor, which, combined with poor mixing, results in formation of a "feed zone" rich in nutrients. Frequent exposure of the culture to high concentrations of nutrients in the feed zone for sufficient duration can produce unexpected effects on its performance. The effect of the feed zone was evaluated by conducting aerobic fed-batch fermentations of Saccharomyces cerevisiae with both complex and defined media. The broth was recirculated between a recycle loop and a bench-scale fermentor, and feed was intermittently added into the recycle loop to simulate the circulation of cells through the feed zone. Experiments were carried out for a range of residence times in the recycle loop from 0.5 to 12 min. Biomass yields from the complex-media fermentations were not affected by exposure to high nutrient levels in the recycle loop for residence times up to 12 min. Ethanol consumption was reduced by as much as 50% for residence time in the loop up to 3 min. Very long exposure of yeast cells to excess nutrient levels (12 min) gave acetic acid formation. In a defined medium, the simulated feed zone effect increased biomass yield by up to 10%, but had no effect on ethanol levels. This study indicates that the feed zone effect on biomass yield in yeast fermentation, using complex substrates, will be negligible under fully aerobic conditions.     

Rapid ethanol fermentations using vacuum and cell recycle

Cell recycle and vacuum fermentation systems were developed for continuous ethanol production. Cell recycle was employed in both atmospheric pressure and vacuum fermentations to achieve high cell densities and rapid ethanol fermentation rates. Studies were conducted with Saccharomyces cerevisiae (ATCC No. 4126) at a fermentation temperature of 35°C. Employing a 10% glucose feed, a cell density of 50 g dry wt/liter was obtained in atmospheric-cell recycle fermentations which produced a fermentor ethanol productivity of 29.0 g/liter-hr. The vacuum fermentor eliminated ethanol inhibition by boiling away ethanol from the fermenting beer as it was formed. This permitted the rapid and complete fermentation of concentrated sugar solutions. At a total pressure of 50 mmHg and using a 33.4% glucose feed, ethanol productivities of 82 and 40 g/liter-hr were achieved with the vacuum system with and without cell recycle, respectively. Fermentor ethanol productivities were thus increased as much as twelvefold over conventional continuous fermentations. In order to maintain a viable yeast culture in the vacuum fermentor, a bleed of fermented broth had to be continuously withdrawn to remove nonvolatile compounds. It was also necessary to sparge the vacuum fermentor with pure oxygen to satisfy the trace oxygen requirement of the fermenting yeast.     

Synergistic temperature and ethanol effect on<Emphasis Type="Italic"> Saccharomyces cerevisiae</Emphasis> dynamic behaviour in ethanol bio-fuel production

The impact of ethanol and temperature on the dynamic behaviour of Saccharomyces cerevisiae in ethanol biofuel production was studied using an isothermal fed-batch process at five different temperatures. Fermentation parameters and kinetics were quantified. The best performances were found at 30 and 33°C around 120 g l^-1 ethanol produced in 30 h with a slight benefit for growth at 30°C and for ethanol production at 33°C. Glycerol formation, enhanced with increasing temperatures, was coupled with growth for all fermentations; whereas, a decoupling phenomenon occurred at 36 and 39°C pointing out a possible role of glycerol in yeast thermal protection.     

Temperature profiles of growth and ethanol tolerance of the xylose-fermenting yeasts Candida shehatae and Pichia stipitis

Summary The effect of different ethanol concentrations on the growth of Candida shehatae and Pichia stipitis with xylose as substrate was evaluated in a temperature gradient incubator. The upper limit of the temperature profiles of ethanol tolerance of both yeast strains were similar, although P. stipitis appeared to have a slightly higher ethanol tolerance in the higher temperature range. An increase in the ethanol concentration severely depressed the maximum growth temperature, and also increased the minimum growth temperature slightly. The ethanol tolerance limit of 46–48 g·l^-1 occurred within a narrow temperature plateau of 11 to 22° C. The low ethanol tolerance of these pentose fermenting yeasts is detrimental for commercial ethanol production from hemicellulose hydrolysates.     

The effect of temperature on the kinetics of ethanol production by Saccharomyces uvarum

Summary In view of the interest in high productivity fermentations at increased temperatures, the effect of temperature on the kinetics of ethanol production by Saccharomyces uvarum was investigated in the range 25–43°C. Using a mathematical model and a nonlinear computer simulation package, the kinetic parameters at each temperature were estimated. It was found that the optimal temperature for growth was 34°C, while the specific ethanol production rate was maximal at 37–43°C. Up to 37°C, the inhibitory effects of ethanol on growth and specific ethanol production rate were unaffected by temperature. However, above this temperature, ethanol inhibition increased significantly.     

Production of laccase byBotrytis cinerea and fermentation studies with strain F226

After induction, seven strains ofBotrytis cinerea released into the culture broth considerable amounts of laccase in a brief production time. The set-up of a suitable production process was studied with a selected strain in a 10-L fermenter. The optimum fermentation conditions were a 3% inoculum with a high degree of sporulation, a simple medium containing 20 g L^–1 of glucose and 2 g L^–1 of yeast extract at pH 3.5, 2 g L^–1 gallic acid as inducer, added after 2 days of growth, an agitation speed of 300 rpm, an aeration rate of 1.2 vvm and a temperature of 24°C. By optimizing the culture conditions, the enzyme activity reached 28 U ml^–1 in 5 days with a specific activity of 560 U mg^–1 protein. The best procedure to obtain a suitable crude enzyme preparation was concentration of the supernatant medium to 10% of the initial volume by ultrafiltration, followed by a fractional precipitation with ethanol. The optimum pH and temperature for laccase activity were 5.5 and 40°C, respectively, with syringaldazine as the substrate.     

Ethanol production by yeast at supraoptimal temperatures

Summary Experiments were performed to investigate growth and alcohol production by yeast cells at high temperatures. Raising the temperature from 30.0°C to 39.0°C resulted in the desired effect: less growth and higher ethanol productivity.At temperatures above 39.6oC,however, cell death predominates.     

Ethanol inhibition of D-xylulose fermentation by Schizosaccharomyces pombe

Summary The kinetics of the utilization of D-xylulose by the yeast Schizosaccharomyces pombe has been examined under anaerobic batch conditions. The inhibitory effect of ethanol on xylulose uptake and ethanol production was studied at pH 6.0 and 30°C. Ethanol had little or no effect on the sugar uptake rate, but end product inhibition was observed on ethanol production. This non-competitive inhibition was linear with respect to ethanol concentration between 0 and 60 g/l. A kinetic model for the alcoholic fermentation of xylulose is presented.     

Factors affecting broth viscosity and coenzyme Q10 production by Agrobacterium species

Summary In the production of coenzyme Q₁₀ (CoQ₁₀) by Agrobacterium sp. the culture broth becomes highly viscous. In an attempt to improve the production process, the effects of chemical and physical factors on broth viscosity and CoQ₁₀ production were studied, using Agrobacterium sp. KY-8593. A particular concentration ratio of sugar to ammonium-nitrogen (NH₄–N) in the medium could effectively enhance CoQ₁₀ production without increasing broth viscosity. An increase in culture temperature to between 32°C and 34°C lowered broth viscosity without reducing CoQ₁₀ production. NH₄–N concentration and temperature had a correlative effect on broth viscosity. At a temperature of about 33°C, there was a wide range of NH₄–N concentration which was optimal for both broth viscosity and CoQ₁₀ production. In optimal conditions with 8% sugar the apparent broth viscosity was reduced to less than 10 pseudo-cP and CoQ₁₀ production was increased to more than 80 mg/l.     

Enhanced production of bioethanol from waste of beer fermentation broth at high temperature through consecutive batch strategy by simultaneous saccharification and fermentation

Malt hydrolyzing enzymes and yeast glycolytic and fermentation enzymes in the waste from beer fermentation broth (WBFB) were identified by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE). A new ‘one-pot consecutive batch strategy’ was developed for efficient bio-ethanol production by simultaneous saccharification and fermentation (SSF) using WBFB without additional enzymes, microbial cells, or carbohydrates. Bio-ethanol production was conducted in batches using WBFB supernatant in the first phase at 25–67 °C and 50 rpm, followed by the addition of 3% WBFB solid residue to the existing culture broth in the second phase at 67 °C. The ethanol production increased from 50 to 102.5 g/L when bare supernatant was used in the first phase, and then to 219 g ethanol/L in the second phase. The amount of ethanol obtained using this strategy was almost equal to that obtained using the original WBFB containing 25% solid residue at 33 °C, and more than double that obtained when bare supernatant was used. Microscopic and gel electrophoresis studies revealed yeast cell wall degradation and secretion of cellular material into the surrounding medium. Scanning electron microscopy (SEM) and Fourier transform infrared spectroscopy (FTIR) supported the existence of enzymes in WBFB involved in bioethanol production at elevated temperatures. The results of this study will provide insight for the development of new strategies for biofuel production.     

Bacterial growth and the concentrations of cyclic nucleotides inLegionella pneumophila cultures

The growth kinetics ofLegionella pneumophila, and the rates of DNA and RNA synthesis in this organism, are qualitatively similar to that of other gram negative organisms of clinical importance. After a brief stationary phase, culture viability is rapidly lost. This loss of viability is not associated with detectable cell lysis or with significant breakdown of cellular DNA; it is, however, preceded by the rapid breakdown of approximately 50% of the cumulatively labeled RNA. During logarithmic growth in buffered yeast extract broth, bacterial cells secreted into the medium large amounts of cyclic GMP at both 37°C and room temperature, while those grown in a buffered synthetic broth did not. Cyclic AMP increased moderately during stationary phase at 37°C and room temperature in both media. Neither added cyclic AMP nor added cyclic GMP influenced the rate of growth ofL. pneumophila in either broth, with or without 1-methyl-3-isobutyl-xanthine, a phosphodiestease inhibitor. Dibutyrul cyclic AMP and 8-bromo cyclic GMP individually or in combination also had no effect on growth.     

The involvement of trehalose in yeast stress tolerance

Summary A total of 12 yeast strains from various genera were examined for their ability to produce ethanol in the presence of high concentrations of glucose. From these studies, the yeastsTorulaspora delbrueckii andZygosaccharomyces rouxii were observed to the most osmotolerant. These osmotolerant yeast strains were also observed to possess high concentrations of intracellular trehalose. Futhermore, these strains were found to be tolerant to long-term storage at –20°C and to storage at 4°C in beer containing 5% (v/v) ethanol. Cells containing high trehalose levels at the time of freezing or cold storage exhibited the highest cell viabilities. Trehalose concentration was observed to increase during growth on glucose, reaching a maximum after 24–48 h. Increasing the incubation temperature from 21 to 40°C also resulted in an increase in intracellular trehalose content. These results suggest that trehalose plays a role in enhancing yeast survival under environmentally stressful conditions.     

The effect of temperature,pH, and initial glucose concentration on the kinetics of ethanol production by Zymomonas mobilis in batch fermentation

Summary Zymomonas mobilis, strain ATCC 10988, was used to evaluate the effects of pH (5.0 to 8.0), temperature (30°C to 40°C), and initial glucose concentration (75 g/l to 150 g/l) on the kinetics of ethanol production from glucose using batch fermentation. Specific ethanol production rate was maximum and nearly constant over a pH range of 6.0 to 7.5. End-of-batch ethanol yield and specific growth rate were insensitive to pH in the range of 5.0 to 7.5. End-of-batch ethanol yield was maximum and nearly constant between 30°C and 37°C but decreased by 24% between 37°C and 40°C. All other kinetic parameters are greatest at 34°C. End-of-batch ethanol yield is maximum at an initial glucose concentration of 100 g/l. Specific growth rate reaches a maximum at 75 g/l, but specific ethanol production rate decreases throughout the range. The optimum initial glucose concentration of 100 g/l gives the highest ethanol yield at a specific ethanol production rate less than 10% below the maximum observed.     

Biotechnical utilization of wood carbohydrates after steaming pretreatment

Summary Birch wood was used as raw material to study the effect of steaming pretreatment on the characteristics, enzymatic hydrolysis and fermentation of cellulose and hemicellulose. The cellulose remained undissolved in the fibres after steaming, but the degree of polymerization decreased and the surface area increased with increasing steaming temperature. The yield in enzymatic hydrolysis with T. reesei and A. niger cellulases increased from 40 to 75% of theoretical when the pretreatment temperature was increased from 170 to 210°C at a residence time of 10 minutes. The glucose released was fermented to ethanol by yeast without interference of toxic compounds. After steaming, the hemicellulose was mainly in the form of xylo-oligomers. The average chain length decreased with increasing temperature. Only the monomeric sugars were fermented to ethanol by Fusarium oxysporum. After steaming at 210°C toxic decomposition products inhibited the fermentation completely. In aerobic conditions also the xylo-oligomers were metabolized.     

Production of extracellular inulinase in high-cell-density fed-batch cultures of Kluyveromyces marxianus

The production of extracellular inulinase (\-1,2-d-fructan fructanohydrolase, EC 3.2.1.7) was studied in fed-batch cultures of the yeast Kluyveromyces marxianus CBS 6556 at 30 and at 40° C. At both temperatures, the final biomass concentration exceeded 100 g·l^–1 and more than 2 g enzyme. L^–1 of culture supernatant was produced. The biomass yield on O₂ at 40° C was substantially lower than at 30°C. Nevertheless, at 40° C a growth rate of 0.20 h^–1 could be maintained for a longer period than at 30° C. The unexpected higher O₂-transfer rate at 40°C is probably due to a lower viscosity of the culture broth. The 40°C fermentation took only 33 h as compared to 42 h at 30° C. These results indicate that K. marxianus is a promising host for the extracellular production of heterologous proteins under the control of the inulinase promoter.     

Interacting effects of time,temperature, pH and simple sugars on biomass and toxic metabolite production by three Alternaria spp.

Biomass and toxic metabolite production by Altemaria hemicota, A. solani and A. tenuis in modified Czapek Dox broth (mCDB) as affected by incubation time (up to 4 wk) temperature (6, 15 and 25 °C), pH (3.0, 5.0 and 8.0) and sugars (glucose, fructose and sucrose) was studied. Biomass production was greatest at 25 ° C and pH 8.0 but toxin production was enhanced at 15 °C. In general, biomass production was promoted by up to 9% glucose and sucrose and 6% fructose; however, toxin production was simultaneously reduced by elevated sugars in mCDB over a 4-wk incubation period.     

Characterisation of a novel thermotolerant yeast, Kluyveromyces marxianus var marxianus: development of an ethanol fermentation process

The fermentation characteristics of the novel, thermotolerant, isolate Kluyveromyces marxianus var marxianus were determined to evaluate its aptitude for use in an ethanol production process. Sustainable growth was not observed under anaerobic conditions, even in the presence of unsaturated fatty acid and sterol. A maximum ethanol concentration of 40 g L⁻¹ was produced at 45°C, with an initial specific ethanol production rate of 1.7 g g⁻¹ h⁻¹. This was observed at ethanol concentrations below 8 g L⁻¹ and under oxygen-limited conditions. The low ethanol tolerance and low growth under oxygen-limited conditions required for ethanol production implied that a simple continuous process was not feasible with this yeast strain. Improved productivity was achieved through recycling biomass into the fermenter, indicating that utilising an effective cell retention method such as cell recycle or immobilisation, could lead to the development of a viable industrial process using this novel yeast strain. Received 14 February 1998/ Accepted in revised form 19 May 1998     

Broth recycle in a yeast fermentation

Fermentation is a water-intensive process requiring treatment of large amounts of effluent broth. It is desirable to increase the ratio of product produced to the volume of effluent by minimizing the discharge of effluent from the fermentation process. A study of recycling spent fermentation process. A study of recycling spent fermentation broth for the subsequent fermentation was carried out with Apiotrichum curvatum an oleaginous yeast, as the working culture. Spent broth from a defined medium was recycled t replace as much as 75% of the water and salts for subsequent batches and this was repeated for seven sequential batches without affecting cell mass and lipid production. A 64% vlume reduction of wastewater was achieved in this manner. However, when using whey permeate as the medium, lipid production dropped after three consecutive recycle operations at 50% recycle, and after two consecutive recycle operations at 75% and 100% recycle. Accumulation of ions in the broth appeared to be responsible for the inhibition. An ion exchange step was able to eliminate the ion buildup and restore fermentation performance. (c) 1994 John Wiley & Sons, Inc.     

Temperature-dependent dimorphism of the yeastArxula adeninivorans Ls3

Arxula adeninivorans Ls3 is described as an ascomycetous, arthroconidial, anamorphic, xerotolerant yeast, which was selected from wood hydrolysates in Siberia. By using minimal salt medium or yeast-extract-peptone-medium with glucose or maltose as carbon source it was shown that this yeast is able to grow at up to 48° C. Increasing temperatures induce changes in morphology from the yeast phase to mycelia depending on an altered programme of gene expression. This dimorphism is an environmentally conditioned (reversible) event and the mycelia can be induced at a cultivation temperature of 45° C. Depending on the morphology of strain Ls3 (yeast phase or mycelia) the secretion behaviour as well as the spectrum of polypeptides accumulated in the culture medium changed. The activities of the accumulated extracellular enzymes glucoamylase and invertase were 2 to 3 times higher in cultures grown at 45° C than in those grown at 30° C. While the level of the glucoamylase protein secreted from mycelia between 45 and 70 hours did not change, biochemical activity decreased after a cultivation time of 43 hours. It was shown that this effect depended on both the catabolic repression of the glucoamylase by glucose and the thermal inactivation of this enzyme in media without or with low concentrations of starch or maltose.     

Selection at the alcohol dehydrogenase locus of Drosophila melanogaster: Effects of ethanol and temperature

Drosophila melanogaster larvae were subjected to 10 generations of selection on 6% ethanol at 17, 25, and 30°C. For each temperature there was a significant (P<0.01) increase in the frequency of the Adh isoallele. Controls with no ethanol showed no change in the frequency of the Adh ^F isoallele. Larvae subjected to stronger selection on 8% ethanol confirmed the results. When adults of various ages were subjected to 16 and 32°C, the ADH^F isoenzyme retained its twofold advantage in activity over ADH^S regardless of the temperature. The same result was obtained with larvae at 16 and 35°C. Although some effect of temperature was demonstrated, it was concluded that the effect was not strong enough for temperature to be a selective factor under the conditions studied. However, ethanol is a strong selective factor for laboratory populations.