Nutrient-Enhanced Production of Remarkably High Concentrations of Ethanol by Saccharomyces bayanus through Soy Flour Supplementation

The supplementation of a simple medium with soy flour led to an increase in the specific growth rate and viable cell concentration of Saccharomyces bayanus during fermentation. Increasing the amount of soy flour led to an increase in the maximum number of viable yeast cells and the percentage of glucose fermented. It was possible in 64 h to reach 12.8% (wt/vol) ethanol by adding 4% soy flour (wt/vol) to a simple medium with 300 g of glucose per liter. The aqueous extract from soy flour was nearly as effective as whole-soy flour, whereas the lipidic fraction had no positive effect.     

Rapid production of high concentrations of ethanol bySaccharomyces bayanus: Mechanisms of action of soy flour supplementation

Summary The supplementation of a simple medium with 2% soy flour increased the final ethanol concentration and the rate of fermentation bySaccharomyces bayanus. This improvement could not be attributed to an increase of ethanol tolerance of yeast cells but to the satisfaction of nutritional deficiencies.     

Rapid production of ethanol in high concentration by immobilized cells of Saccharomyces cerevisiae through soya flour supplementation

Summary Ethanol concentration and fermentation productivities were substantially increased when soya extract was added to the fermentation medium using immobilized cells of a locally isolated strain of S. cerevisiae. Very high concentrations, 152 and 162 g/l of ethanol, were obtained from a medium containing 300 and 350 g/l sugars respectively by supplementing the medium with soya extract. The fermentation time was also reduced by more than 50%.     

High gravity fermentation of sugarcane molasses to produce ethanol: Effect of nutrients

Fermentation efficiency of more than 85% was obtained by high gravity fermentation of 33–34°Bx (spec. gravity ≈1.134) molasses medium with certain nutrients, instead of generally employed medium containing ≈16% (w/v) total sugar (spec. gravity ≈1.090) for ethanol fermentation in distilleries to get maximum 80–85% conversion. The fermenting yeast, Saccharomyces, has varied capabilities, depending on the species and nutrition for fermenting the high solids medium. The fermentation period was reduced to 48 h; and the byproducts obtained were less in concentration, upon supplementation with nutrients (or osmoprotectants) like soy flour/wheat bran to the medium in the existing batch fermentation technology. This has been found partly due to improved yeast cell viability during fermentation.     

Improvement of ethanol production in very high gravity fermentation by horse gram (Dolichos biflorus) flour supplementation

AIMS: To determine the effect of osmotic stress on yeast and to investigate the protective role of horse gram flour during very high gravity (VHG) ethanol fermentation. METHODS AND RESULTS: Saccharomyces cerevisiae was inoculated into high sugar (30-40%, w/v) containing medium with and without supplementation of horse gram flour. The fermentation experiments were carried out in batch mode. The effect of 4 or 6% of horse gram flour to the medium on the metabolic behaviour and viability of yeast was studied. Significant increase in ethanol yield up to 50% and dramatic decrease in glycerol production up to 100% was observed in the presence of horse gram flour. The fermentation rate was increased from 3 to 5 days with increased viable cell count. The physical and chemical factors of horse gram flour may aid in reducing the osmotic stress of high gravity fermentation of ethanol as well as enhancing ethanol yield. CONCLUSIONS: It was found that horse gram flour not only reduced fermentation time but also enhanced ethanol production by better utilization of sugar. SIGNIFICANCE AND IMPACT OF THE STUDY: Production of high ethanol concentration by using VHG sugar fermentation eliminates the expensive steps in the conventional process and saves time.     

Fermentation of cellodextrins to ethanol using mixed-culture fermentations

The potential for enhancing ethanol production from cellodextrins by employing mixed-culture (Candida wickerhamii-Saccharomyces cerevisiae) fermentations was investigated. Initially, ethanol production was monitored in fermentation medium containing 50 g/L glucose plus 45 g/L cellobiose. Inoculum levels and times of inoculum addition were varied. Of the conditions tested, the most rapid rates of ethanol formation occurred in fermentations in which either C. wickerhamii and S. cerevisiae were coinoculated at a ratio of 57 : 1 cell/mL or in fermentations in which a 10-fold-greater S. cerevisiae inoculum was added to a pure culture C. wickerhamii fermentation after 1 day incubation. These conditions were used to attempt to enhance fermentations in which cellodextrins produced by trifluoroacetic acid hydrolysis of cellulose served as the sole carbon source. Cellodextrins that were not further purified after cellulose hydrolysis contained compounds that were slightly inhibitory to C. wickerhamii. In this case the mixed-culture fermentations produced 12-45% more ethanol than a pure culture C. wickerhamii fermentation. However, if the substrate was treated with Darco G-60 charcoal, the toxic materials were apparently removed and the pure culture C. wickerhamii fermentations performed as well as the mixed-culture fermentations.     

Improving production of hyperthermostable and high maltose-forming alpha-amylase by an extreme thermophile Geobacillus thermoleovorans using response surface methodology and its applications

By cultivating Geobacillus thermoleovorans in shake flasks containing cane molasses medium at 70 degrees C, the fermentation variables were optimized by 'one variable at a time' approach followed by response surface methodology (RSM). The statistical model was obtained by central composite design (CCD) using three variables (cane-molasses, urea and inoculum density). An overall 1.6- and 2.1-fold increase in enzyme production was achieved in the optimized medium in shake flasks and fermenter, respectively. The alpha-amylase titre increased significantly in cane-molasses medium (60 U ml(-1)) as compared to that in the synthetic medium (26 U ml(-1)). Thus the cost of enzyme produced in cane molasses medium (0.823 euros per million U) was much lower than that produced in the synthetic starch-yeast extract-tryptone medium (18.52 euros per million U). The shelf life of bread was improved by supplementing dough with alpha-amylase, and thus, the enzyme was found to be useful in preventing the staling of bread. Reducing sugars liberated from 20% and 30% raw pearl millet starch were fermented to ethanol; ethanol production levels attained were 35.40 and 28.0 g l(-1), respectively.     

Improvements in ethanol concentration and fermentor ethanol productivity in yeast fermentations using whole soy flour in batch,and continuous recycle systems

Summary Ethanol concentrations and fermentor productivities were increased 20.2 and 15.5% at 90 and 95% recycle, respectively, when whole soy flour was added to the feed (2 g/ at 90% recycle, and 1 g/ at 95% recycle) of a continuous yeast fermentation system with recycle of cells and soy flour (soy flour concentrations were 2% at steady state in the fermentor) by UF membranes as compared to controls. The improvements were primarily due to increases in cell concentrations. Similar results were obtained for batch cultures.     

Production of high-purity isomalto-oligosaccharides syrup by the enzymatic conversion of transglucosidase and fermentation of yeast cells

A method for the production of high-purity isomalto-oligosaccharides (IMO) involving the transglucosylation by transglucosidase and yeast fermentation was proposed. The starch of rice crumbs was enzymatically liquefied and saccharified, and then converted to low-purity IMO syrup by transglucosylation. The low-purity IMO produced either from rice crumbs or tapioca flour as the starch source could be effectively converted to high-purity IMO by yeast fermentation to remove the digestible sugars including glucose, maltose, and maltotriose. Both Saccharomyces carlsbergensis and Saccharomyces cerevisiae were able to ferment glucose in the IMO syrup. Cells of S. carlsbergensis harvested from the medium of malt juice were also able to ferment maltose and maltotriose. A combination of these two yeasts or S. carlsbergensis alone could be used to totally remove the digestible sugars in the IMO, coupled with the production of ethanol. The resultant high-purity IMO, including mainly isomaltose, panose, and isomaltotriose made up more than 98% w/w of the total sugars after a 3-day fermentation. When the low-purity IMO was produced from the starch of tapioca flour, 3-day fermentation under the same conditions resulted in IMO with purity lower than that from rice crumbs. For low-purity IMO from rice crumbs, fermentation with washed S. carlsbergensis cells harvested at log phase was the most effective. However, for the low-purity IMO from tapioca flour, incubation with S. cerevisiae for the first 24 h and then supplementing with an equal amount of S. carlsbergensis cells for further fermentation was the most effective approach for producing high-purity IMO.     

Ethanol production from corn cob hydrolysates by <Emphasis Type="Italic">Escherichia coli</Emphasis> KO11

Corn cob hydrolysates, with xylose as the dominant sugar, were fermented to ethanol by recombinant Escherichia coli KO11. When inoculum was grown on LB medium containing glucose, fermentation of the hydrolysate was completed in 163 h and ethanol yield was 0.50 g ethanol/g sugar. When inoculum was grown on xylose, ethanol yield dropped, but fermentation was faster (113 h). Hydrolysate containing 72.0 g/l xylose and supplemented with 20.0 g/l rice bran was readily fermented, producing 36.0 g/l ethanol within 70 h. Maximum ethanol concentrations were not higher for fermentations using higher cellular concentration inocula. A simulation of an industrial process integrating pentose fermentation by E. coli and hexose fermentation by yeast was carried out. At the first step, E. coli fermented the hydrolysate containing 85.0 g/l xylose, producing 40.0 g/l ethanol in 94 h. Baker's yeast and sucrose (150.0 g/l) were then added to the spent fermentation broth. After 8 h of yeast fermentation, the ethanol concentration reached 104.0 g/l. This two-stage fermentation can render the bioconversion of lignocellulose to ethanol more attractive due to increased final alcohol concentration. Journal of Industrial Microbiology & Biotechnology (2002) 29, 124–128 doi:10.1038/sj.jim.7000287 Received 20 February 2002/ Accepted in revised form 04 June 2002     

Combined use of three methods for high concentration ethanol production by Saccharomyces cerevisiae

Summary Ethanol concentration and fermentation productivity using Saccharomyces cerevisiae were substantially increased in shake flask cultures with a normal inoculum by combining 3 methods: (a) by making nutrient additions to the standard medium for ethanol production, (b) by immobilizing the cells in alginate beads and (c) by using a glucose step-feeding batch process. Ethanol concentration by free yeast was improved from 5.9% (w/w) to 9.6% (w/w) when a further 0.8% yeast extract and 1% animal peptone were added to the standard 30% (w/v) glucose nutrient medium. This was further increased to 12.8% (w/w) by using alginate immobilized yeast. The ethanol concentration was increased again, to 15.0% (w/w) by using the glucose step-feeding batch process.     

Optimization of process variables for minimization of byproduct formation during fermentation of blackstrap molasses to ethanol at industrial scale

Aims: To investigate the effect of molasses concentration, initial pH of molasses medium, and inoculum’s size to maximize ethanol and minimize methanol, fusel alcohols, acetic acid and aldehydes in the fermentation mash in industrial fermentors. Methods and Results: Initial studies to optimize temperature, nitrogen source, phosphorous source, sulfur supplement and minerals were performed. The essential nutrients were urea (2 kg in 60 m³), 0·5 l each of commercial phosphoric acid and sulfuric acid (for pH control) added at the inoculum preparation stage only. Yields of ethanol, methanol, fusel alcohols, total acids and aldehydes per 100‐l fermentation broth were monitored. Molasses at 29°Brix (degree of dissolved sugars in water), initial pH 4·5, inoculum size 30% (v/v) and anaerobic fermentation supported maximum ethanol (7·8%) with Y_P/S = 238 l ethanol per tonne molasses (96·5% yield) (8·2% increase in yield), and had significantly lower values of byproducts than those in control experiments. Conclusions: Optimization of process variables resulted in higher ethanol yield (8·2%) and reduced yield of methanol, fusel alcohols, acids and aldehydes. Significance and Impact of the Study: More than 5% substrate is converted into byproducts. Eliminating or reducing their formation can increase ethanol yield by Saccharomyces cerevisiae, decrease the overall cost of fermentation process and improve the quality of ethanol.     

Magnesium limitation and its role in apparent toxicity of ethanol during yeast fermentation

The rate of ethanol production per milligram of cell protein begins to decline in the early stage of batch fermentation before high concentrations of ethanol have accumulated. In yeast extract-peptone medium (20% glucose), this initial decline appears to be related to growth and to result in part from a nutrient deficiency. The addition of yeast extract, peptone, and ashed preparations of these restored the ability of glucose-reconstituted medium (in which cells had been previously grown) to support vigorous growth. Magnesium was identified as the active component. Supplementing fermentations with 0.5 mM magnesium prolonged exponential growth, resulting in increased yeast cell mass. The addition of magnesium also reduced the decline in fermentative activity (micromoles of CO2 evolved per hour per milligram of protein) during the completion of batch fermentations. These two effects reduced the time required for the conversion of 20% glucose into ethanol by 1/3 with no measurable loss in ethanol yield (98% of theoretical maximum yield). It is possible that some of the reported beneficial effects of complex nutrients (soy flour and yeast extract) for ethanol production also result from the correction of a simple inorganic ion deficiency, such as magnesium.     

Soybean bio-refinery platform: enzymatic process for production of soy protein concentrate,soy protein isolate and fermentable sugar syrup

Soybean carbohydrate is often found to limit the use of protein in soy flour as food and animal feed due to its indigestibility to monogastric animal. In the current study, an enzymatic process was developed to produce not only soy protein concentrate and soy protein isolate without indigestible carbohydrate but also soluble reducing sugar as potential fermentation feedstock. For increasing protein content in the product and maximizing protein recovery, the process was optimized to include the following steps: hydrolysis of soy flour using an Aspergillus niger enzyme system; separation of the solid and liquid by centrifugation (10 min at 7500×g); an optional step of washing to remove entrapped hydrolysate from the protein-rich wet solid stream by ethanol (at an ethanol-to-wet-solid ratio (v/w) of 10, resulting in a liquid phase of approximately 60 % ethanol); and a final precipitation of residual protein from the sugar-rich liquid stream by heat treatment (30 min at 95 °C). Starting from 100 g soy flour, this process would produce approximately 54 g soy protein concentrate with 70 % protein (or, including the optional solid wash, 43 g with 80 % protein), 9 g soy protein isolate with 89 % protein, and 280 ml syrup of 60 g/l reducing sugar. The amino acid composition of the soy protein concentrate produced was comparable to that of the starting soy flour. Enzymes produced by three fungal species, A. niger, Trichoderma reesei, and Aspergillus aculeatus, were also evaluated for effectiveness to use in this process.     

Production of α-galactosidase by a novel actinomycete <Emphasis Type="Italic">Streptomyces griseoloalbus</Emphasis> and its application in soymilk hydrolysis

α-Galactosidase production by a newly isolated actinomycete Streptomyces griseoloalbus under submerged fermentation was investigated. The influence of initial pH of medium, incubation temperature, inoculum age and inoculum size on α-galactosidase formation was studied. Various carbon sources were supplemented in the medium to study their effect on enzyme production. The influence of the concentration of locust bean gum on enzyme production also was optimized. Optimization of process parameters resulted in a highest α-galactosidase activity of 20.4 U/ml. The highest α-galactosidase activity was obtained when the fermentation medium with initial pH 6.0 and containing 1% locust bean gum as growth substrate was inoculated with 10% (v/v) of 72 h grown inoculum and incubated at 30°C. The hydrolysis of flatulence-causing oligosaccharides in soymilk by the enzyme was also investigated. Thin layer chromatographic analysis of enzyme-treated soymilk samples showed the complete hydrolysis of soy oligosaccharides liberating galactose, the final product.     

Magnesium limitation and its role in apparent toxicity of ethanol during yeast fermentation.

The rate of ethanol production per milligram of cell protein begins to decline in the early stage of batch fermentation before high concentrations of ethanol have accumulated. In yeast extract-peptone medium (20% glucose), this initial decline appears to be related to growth and to result in part from a nutrient deficiency. The addition of yeast extract, peptone, and ashed preparations of these restored the ability of glucose-reconstituted medium (in which cells had been previously grown) to support vigorous growth. Magnesium was identified as the active component. Supplementing fermentations with 0.5 mM magnesium prolonged exponential growth, resulting in increased yeast cell mass. The addition of magnesium also reduced the decline in fermentative activity (micromoles of CO2 evolved per hour per milligram of protein) during the completion of batch fermentations. These two effects reduced the time required for the conversion of 20% glucose into ethanol by 1/3 with no measurable loss in ethanol yield (98% of theoretical maximum yield). It is possible that some of the reported beneficial effects of complex nutrients (soy flour and yeast extract) for ethanol production also result from the correction of a simple inorganic ion deficiency, such as magnesium.     

Fermentative Production of Exocellular Glucans by Fleshy Fungi

Two specimens of higher fungi produced exocellular β-1, 3-glucans when their mycelial forms were cultivated under submerged aerobic conditions. Plectania occidentalis NRRL 3137 consumed up to 6% glucose or xylose with about 30% conversion to polymer in a medium composed of hydrolyzed soy protein, salts, and thiamine. A 5% inoculum was used in a 10-day shaken fermentation. After dilution of the culture liquors and partial disruption of mycelia with a blender, solids were removed by centrifugation, and the polymer was precipitated by the admixture of 2 volumes of ethyl alcohol. A second polymer was formed in 40 to 65% yield by fermentation with Helotium sp. NRRL 3129, which in the imperfect stage would be identified as Monilia sp. It consumed up to 4% glucose, fructose, mannose, or sucrose in 60 to 72 hr. A 2% inoculum in a medium composed of commercial defatted soy flakes, phosphate, and thiamine in tap water gave a satisfactory fermentation. This polymer was precipitated by the addition of 0.5 volume of ethyl alcohol. Both organisms have a broad pH optimum on the slightly acidic side and did best at about 25 C.     

Effect of soy skim from soybean aqueous processing on the performance of corn ethanol fermentation

The feasibility of using soy skim, a co-product of the aqueous processing of soybeans, in ethanol production from corn was evaluated. Specific growth rates were compared when Saccharomyces cerevisiae was grown in soy skim and peptone-yeast extract media supplemented with glucose. Such soy skim was proved to be a good nitrogen source for yeast growth. Next, fermentation of dry-ground corn to ethanol using soy skim as the media was simulated on 1.5-L scale. Replacing water with soy skim increased the initial ethanol production rates by 4-32% while final ethanol yield was about 39 g/100 g dry corn, similar to the result when water was used. Solid and protein contents in the finished beer increased with the addition of soy skim. Thus, replacing water in corn-ethanol fermentation with soy skim is feasible, and may improve the economics of both aqueous soybean processing and corn ethanol fermentation.     

Kinetics of growth and ethanol production on different carbon substrates using genetically engineered xylose-fermenting yeast

Saccharomyces cerevisiae 424A (LNH-ST) strain was used for fermentation of glucose and xylose. Growth kinetics and ethanol productivity were calculated for batch fermentation on media containing different combinations of glucose and xylose to give a final sugar concentration of 20+/-0.8 g/L. Growth rates obtained in pure xylose-based medium were less than those for media containing pure glucose and glucose-xylose mixtures. A maximum specific growth rate micro(max) of 0.291 h(-1) was obtained in YPD medium containing 20 g/L glucose as compared to 0.206 h(-1) in YPX medium containing 20 g/L xylose. In media containing combinations of glucose and xylose, glucose was exhausted first followed by xylose. Ethanol production on pure xylose entered log phase during the 12-24h period as compared to the 4-10h for pure glucose based medium using 2% inoculum. When glucose was added to fermentation flasks which had been initiated on a pure xylose-based medium, the rate of xylose usage was reduced indicating cosubstrate inhibition of xylose consumption by glucose.     

休哈塔假丝酵母HDYXHT-01利用木糖生产乙醇的发酵工艺优化

采用Plackett-Burman (PB) 方法和中心组合设计 (Ccentral composit design,CCD) 对休哈塔假丝酵母Candida shehataeHDYXHT-01利用木糖发酵生产乙醇的工艺进行优化。PB试验设计与分析结果表明：硫酸铵、磷酸二氢钾、酵母粉和接种量是影响木糖乙醇发酵的4个关键因素,以乙醇产量为响应目标,采用CCD和响应面分析法 (Response surface methodology,RSM),确定了木糖乙醇发酵的最佳工艺为：硫酸铵1.73 g/L、磷酸二氢钾3.56 g/L、酵母粉2.62 g/L和接种量5.66％,其他发酵条件为：木糖80 g/L,MgSO4·7H2O 0.1 g/L,pH 5.0,培养温度30 ℃,装液量100 mL/250 mL,摇床转速140 r/min,发酵时间48 h,在该条件下发酵液中乙醇产量可以达到26.18 g/L,比未优化前提高了1.15倍。