Effects of medium components on L-ornithine production byBrevibacterium ketoglutamicum

Effects of yeast extract, and ammonium sulfate were investigated on the production of L-ornithine by an arginine auxotroph.Brevibacterium ketoglutamicum in flask and batch cultures. Yeast extract as an arginine source and ammonium sulfate as an inorganic nitrogen source had significant effects on L-ornithine, production and cell growth. L-ornithine production was repressed by the excessive addition of arginine. Reversion of auxotrophic cells to the wild type was observed when the initial yeast extract concentration was too low. There existed optimum concentrations of yeast extract and ammonium sulfate for L-ornithine production. The effects of yeast extract and ammonium sulfate concentrations on the Leudeking-Piret model parameters were examined to analyze, the relationship between cell growth and L-ornithine production.     

Variations of alcohol dehydrogenase activity and fermentative pyruvate,ethanol production of F. equiseti and F. acuminatum depend on the yeast extract and urea concentrations

In this study, pyruvate production of Fusarium equiseti was significantly increased when the yeast extract concentration was raised from 5 to 25 g/L while it was increased to only up to 10 g/L yeast extract in F. acuminatum. Upon supplementation with urea as an alternative nitrogen source, production of pyruvate for both of the Fusarium species were decreased with respect to increase in urea concentration in medium. On the other hand, ethanol production and alcohol dehydrogenase activity of F. equiseti were decreased approximately 1.9- and 1.6-fold with an increase in yeast concentration from 5 to 25 whereas the levels of F. acuminatum were increased 2.3- and 1.8-fold, respectively. In addition, ethanol productions and ADH activities in F. equiseti and F. acuminatum significantly increased on the 12th day up to 15 and 25 g/L urea concentrations, respectively. However, they were significantly decreased under these conditions at higher nitrogen sources. In addition, ethanol production and alcohol dehydrogenase activity in urea supplemented medium were higher than yeast extract supplemented. The results may suggest that the pyruvate, ethanol production and ADH enzyme activity variations and balance between aerobic and anaerobic respiration in F. equiseti and F. acuminatum were effected from yeast extract and urea concentrations in the nutrient medium.     

Optimization of medium composition by response surface methodology for the production of tartaric acid by Gluconobacter suboxydans

The combined effect of sorbitol and yeast extract of the medium on tartaric acid production by Gluconobacter suboxydans, NCIM 2049, was studied in batch fermentation while keeping the temperature (30?°C) and pH (6.2) constant. Response surface methodology was used to obtain quadratic models for the production of tartaric acid. The multiple coefficients of regression between 0.8945 and 0.9820 was obtained during the process. The optimum medium composition comprising 20?kg/m³ sorbitol and 2?kg/m³ yeast extract was verified experimentally by observing the variation of cell mass and tartaric acid production with time.     

Optimization of Banana Juice Fermentation for the Production of Microbial Oil

Apiotrichum curvatum ATCC 20509 (formerly Candida curvata D), a lipid-accumulating yeast, was grown in banana juice. The optimum conditions for biomass production in shake flasks were 30°C growth temperature, efficient aeration, a juice concentration of 25%, and preliminary heat treatment at less than sterilization conditions. Under controlled conditions in a fermentor, 20% banana juice was optimum. High concentrations of yeast extract (0.3%) increased biomass production by 40% but decreased oil production by 30%. A lower yeast extract concentration (0.05%) increased biomass production by 2% and oil production by 25%. The best growth and oil production were observed when asparagine (1.4 g/liter) and mineral salts were added to the banana juice. The addition of minerals seemed to improve the utilization of carbon. Growth inhibition was observed when the fermentor was aerated with pure oxygen, even when additional nutrients were present. A fed-batch process permitted the juice concentration to be increased from 15 to 82%; biomass accumulation was three times higher than in batch fermentations. However, the cellular lipid content was only 30% of dry weight, and chemical oxygen demand reduction was slow and inefficient.     

Growth and sporulation of Metarrhizium anisopliae and Beauveria bassiana on media containing various peptone sources

Two entomogenous fungi, Metarrhizium anisopliae and Beauveria bassiana, were cultured in liquid culture media containing various commercial peptone sources to determine the effect of the sources on growth and sporulation. Each fungus responded differently to the various peptone sources. Tryptone, Casitone, and yeast extract were effective for mycelial growth of M. anisopliae; however, yeast extract was the most effective in production of spores. Soytone Casitone, Neopeptone, and casein hydrolysate were used effectively for mycelial growth of B. bassiana, but the latter two were not as effective for production of spores. Gelatone and Peptone (Bacteriological) were not effective for production of growth or sporulation for either fungus.     

Statistical Screening of Medium Components for Recombinant Production of Pseudomonas aeruginosa ATCC 9027 Rhamnolipids by Nonpathogenic Cell Factory Pseudomonas putida KT2440

Rhamnolipids (RLs) produced by the opportunistic human pathogen Pseudomonas aeruginosa are considered as potential candidates for the next generation of surfactants. Large-scale production of RLs depends on progress in strain engineering, medium design, operating strategies, and purification procedures. In this work, the rhlAB genes extracted from a mono_RLs_producing strain of P. aeruginosa (ATCC 9027) were introduced to an appropriate safety host Pseudomonas putida KT2440. The capability of the recombinant strain was evaluated in various media. As a prerequisite for optimal medium design, a set of 32 experiments was performed in two steps for screening a number of macro-nutritional compounds. In the experiments, a two-level fractional factorial design resolution IV was followed by a two-level full factorial one. By means of this approach, it was observed that glycerol, yeast extract, and peptone have significant positive influence on recombinant RLs production while the yeast extract/peptone two-factor and glycerol/yeast extract/peptone three-factor interactions have considerable negative effects. A wide range of variation from 0 to 570 mg/l was obtained for RLs production during the screening experiments indicating the importance of medium optimization. The results point out the opportunity for possible higher yields of RLs through further screening, mixture/combined mixture designs, and high-cell-density cultivations.     

Stress-induced formation of echinatin and a metabolite, 5′-prenyl-licodione,in cultured Glycyrrhiza echinata cells

The production of a retrochalcone, echinatin, by isoflavone-rich Glycyrrhiza echinata (M-2) cultured cells was stimulated by the addition of yeast extract or calcium alginate beads to the culture medium. Combined addition of yeast extract and cycloheximide suppressed the formation of retrochalcone, suggesting de novo synthesis. A new metabolite was isolated from the induced cells and its structure was determined to be 1-[2,4-dihydroxy-5-(3-methyl-2-butenyl)phenyl]-3-(4-hydroxyphenyl)-1,3-propanedione (5′-prenyl-licodione).     

Medium optimization for the production of avermectin B1a by Streptomyces avermitilis 14-12A using response surface methodology

Response surface methodology was employed to optimize the composition of medium for the production of avermectin B1a by Streptomyces avermitilis 14-12A in shaker flask cultivation. Corn starch and yeast extract were found to have significant effects on avermectin B1a production by the Plackett–Burman design. The steepest ascent method was used to access the optimal region of the medium composition, followed by an application of response surface. The analysis revealed that the optimum values of the tested variables were 149.57 g/l corn starch and 8.92 g/l yeast extract. A production of 5128 mg/l, which was in agreement with the prediction, was observed in verification experiment. In comparison to the production of original level (3528 mg/l), 1.45-fold increase had been obtained.     

Medium optimization for the production of cold-active beta amylase by psychrotrophic Streptomyces MIUG 4 alga using response surface methodology

The aim of this work was to optimize the cultural and production parameters using statistical approach to the synthesis of cold-active beta amylase by Streptomyces MIUG 4 Alga in submerged fermentation (SmF). The process parameters influencing the enzyme production were identified using the Plackett-Burman design. Among the various parameters screened, the concentrations of glycerol, starch, and yeast extract were the most significant. The optimum levels of these significant parameters determined employing the response surface methodology (RSM) and central composite design (CCD) were as follows: glycerol (4.00%), starch (2.00%) and yeast extract (0.5%). By using the optimal fermentation medium! the cold-active beta amylase production was increased up to 246.62 AU, an approximate 2.6-fold improvement over the previous production (93.32 AU) with un-optimized medium. This is the first report on production of cold-active beta amylase by psychrotrophic Streptomyces sp. The present study indicates that the cold-adapted extracellular beta amylase of Streptomyces MIUG 4 Alga may have considerable potential for industrial application owing to its properties.     

Optimization of some variables that affect the synthesis of laccase by Pleurotus ostreatus

The influence of initial pH, concentration of yeast extract, inducer, type of enzyme releaser and buffer system on the composition of a medium for laccase production by Pleurotus ostreatus DM-1513 was investigated. A 2⁵ full factorial experimental design was initially employed to evaluate the effects of these variables on the enzyme synthesis. Data analysis showed that low pH and high yeast extract concentration values, as well as the absence of both an inducer and a buffer system, had positive effects on the secreted enzyme levels, whereas the type of enzyme releaser did not have a significant effect. The highest levels of laccase activity (489–540?U/l) were obtained in optimization experiments using media with initial pH between 6.0 and 6.5 and yeast extract concentrations of 0–0.25%     

Augmented cellulase production by Bacillus subtilis strain MU S1 using different statistical experimental designs

The production of cellulase by Bacillus subtilis MU S1, a strain isolated from Eravikulam National Park, was optimized using one-factor-at-a-time (OFAT) and statistical methods. Physical parameters like incubation temperature and agitation speed were optimized using OFAT and found to be 40?°C and 150?rpm, respectively, whereas, medium was optimized by statistical tools. Plackett-Burman design (PBD) was employed to screen the significant variables that highly influence cellulase production. The design showed carboxymethyl cellulose (CMC), yeast extract, NaCl, pH, MgSO₄ and NaNO₃ as the most significant components that affect cellulase production. Among these CMC, yeast extract, NaCl and pH showed positive effect whereas MgSO₄ and NaNO₃ were found to be significant at their lower levels. The optimum levels of the components that positively affect enzyme production were determined using response surface methodology (RSM) based on central composite design (CCD). Three factors namely CMC, yeast extract and NaCl were studied at five levels whilst pH of the medium was kept constant at 7. The optimal levels of the components were CMC (13.46?g/l), yeast extract (8.38?g/l) and NaCl (6.31?g/l) at pH 7. The maximum cellulase activity in optimized medium was 566.66?U/ml which was close to the predicted activity of 541.05?U/ml. Optimization of physical parameters and medium components showed an overall 3.2-fold increase in activity compared to unoptimized condition (179.06?U/ml).     

Inhibitory Effect of Autoclaving Whey-Based Medium on Propionic Acid Production by Propionibacterium shermanii

Propionic acid production by Propionibacterium shermanii was compared in pasteurized and autoclaved whey-based media. Propionic acid production decreased with increasing whey concentration in autoclaved media but not in pasteurized media. Increasing the yeast extract concentration from 5 to 10 g/liter greatly reduced the inhibitory effect of autoclaving.     

A complete industrial system for economical succinic acid production by Actinobacillus succinogenes

An industrial fermentation system using lignocellulosic hydrolysate, waste yeast hydrolysate, and mixed alkali to achieve high-yield, economical succinic acid production by Actinobacillus succinogenes was developed. Lignocellulosic hydrolysate and waste yeast hydrolysate were used efficiently as carbon sources and nitrogen source instead of the expensive glucose and yeast extract. Moreover, as a novel method for regulating pH mixed alkalis (Mg(OH)₂ and NaOH) were first used to replace the expensive MgCO₃ for succinic acid production. Using the three aforementioned substitutions, the total fermentation cost decreased by 55.9%, and 56.4 g/L succinic acid with yield of 0.73 g/g was obtained, which are almost the same production level as fermentation with glucose, yeast extract and MgCO₃. Therefore, the cheap carbon and nitrogen sources, as well as the mixed alkaline neutralize could be efficiently used instead of expensive composition for industrial succinic acid production.     

Optimization of culture medium for cordycepin production using Cordyceps militaris mutant obtained by ion beam irradiation

The effect of medium components on cordycepin production by Cordyceps militaris mutant obtained by ion beam irradiation was investigated. According to the response surface analysis using a central composite design for the prospective mutant G81-3, the predicted optimal concentrations of glucose as the carbon source and the yeast extract as the nitrogen source were 86.2 g/l and 93.8 g/l, respectively, and 6.84 g/l cordycepin was obtained. To date, this is the highest value for cordycepin production. The optimal concentrations of glucose and yeast extract for cordycepin production of the mutant was much higher than that of control (wild strain) and the cordycepin production was 2.79 times higher. Therefore, this new mutant will be a promising strain for future higher cordycepin production at industrial levels.     

Optimization of medium composition for improving biomass production of Lactobacillus plantarum Pi06 using the Taguchi array design and the Box-Behnken method

An immune-enhancing strain, Lactobacillus plantarum Pi06, isolated from a healthy infant was used for biomass production following optimization of the medium in shake-flask culture. Preliminary studies showed that commercial MRS medium and cultivation under static conditions generated higher biomass production than four other tested media with or without a shaking condition. The selected medium composition, consisting of glucose, yeast extract, soy peptone, ammonium citrate, and corn steep liquor, was further optimized using a systematic method that integrated the Taguchi array design and the Box-Behnken method. The response effects of these factors were first investigated using Taguchi design under an L ₁₆ (4⁵) array. The suggested medium composition, derived from Statistica 7.1 using the Taguchi design, was applied to cultivate cells and a biomass of 7.16 g dry cell weight (DCW)/L was obtained. Response surface methodology based on the Box-Behnken method for the three response variables of glucose, yeast extract, and corn steep liquor was then used to further increase the biomass level to 8.94 g DCW/L. The resulting optimum medium consisted of 35 g/L glucose, 35 g/L yeast extract, and 40 mL/L corn steep liquor. Compared with the initial medium, the biomass yield was improved from 4.31 to 8.94 g DCW/L, an enhancement of approximately 107%.     

Toxins of the entomophagous fungus Beauveria bassiana. II. Effect of nitrogen sources on formation of the toxic protease in submerged culture

A series of 24 nitrogen sources including inorganic, organic nonprotein, proteins and complex natural media were examined to determine their stimulatory effects on the production of a toxic proteolytic complex in Beauveria bassiana in submerged cultures. It was found that this effect is enhanced by the sources in the order presented. The best sources are maize meal, yeast extract, and beef extract. The production optimum on these sources occurs on the third day of fermentation. The composition of the protease complex may be influenced by the type of nitrogen source.     

Screening of Ganoderma strains with high polysaccharides and ganoderic acid contents and optimization of the fermentation medium by statistical methods

Polysaccharides and ganoderic acids (GAs) are the major bioactive constituents of Ganoderma species. However, the commercialization of their production was limited by low yield in the submerged culture of Ganoderma despite improvement made in recent years. In this work, twelve Ganoderma strains were screened to efficiently produce polysaccharides and GAs, and Ganoderma lucidum 5.26 (GL 5.26) that had been never reported in fermentation process was found to be most efficient among the tested stains. Then, the fermentation medium was optimized for GL 5.26 by statistical method. Firstly, glucose and yeast extract were found to be the optimum carbon source and nitrogen source according to the single-factor tests. Ferric sulfate was found to have significant effect on GL 5.26 biomass production according to the results of Plackett–Burman design. The concentrations of glucose, yeast extract and ferric sulfate were further optimized by response surface methodology. The optimum medium composition was 55 g/L of glucose, 14 g/L of yeast extract, 0.3 g/L of ferric acid, with other medium components unchanged. The optimized medium was testified in the 10-L bioreactor, and the production of biomass, IPS, total GAs and GA-T enhanced by 85, 27, 49 and 93 %, respectively, compared to the initial medium. The fermentation process was scaled up to 300-L bioreactor; it showed good IPS (3.6 g/L) and GAs (670 mg/L) production. The biomass was 23.9 g/L in 300-L bioreactor, which was the highest biomass production in pilot scale. According to this study, the strain GL 5.26 showed good fermentation property by optimizing the medium. It might be a candidate industrial strain by further process optimization and scale-up study.     

Increasing Secretion of a Bivalent Anti-T-Cell Immunotoxin by Pichia pastoris

The bivalent anti-T-cell immunotoxin A-dmDT390-bisFv(G₄S) was developed for treatment of T-cell leukemia and autoimmune diseases and for tolerance induction for transplantation. This immunotoxin was produced extracellularly in toxin-sensitive Pichia pastoris JW102 (Mut⁺) under control of the AOX1 promoter. There were two major barriers to efficient immunotoxin production, the toxicity of the immunotoxin for P. pastoris and the limited capacity of P. pastoris to secrete the immunotoxin. The immunotoxin toxicity resulted in a decrease in the methanol consumption rate, cessation of cell growth, and low immunotoxin productivity after the first 22 h of methanol induction. Continuous cell growth and continuous immunotoxin secretion after the first 22 h of methanol induction were obtained by adding glycerol to the methanol feed by using a 4:1 methanol-glycerol mixed feed as an energy source and by continuously adding a yeast extract solution during methanol induction. The secretory capacity was increased from 22.5 to 37 mg/liter by lowering the induction temperature. A low temperature reduced the methanol consumption rate and protease activity in the supernatant but not cell growth. The effects of adding glycerol and yeast extract to the methanol feed were synergistic. Adding yeast extract primarily enhanced methanol utilization and cell growth, while adding glycerol primarily enhanced immunotoxin production. The synergy was further enhanced by decreasing the induction temperature from 23 to 15°C, which resulted in a robust process with a yield of 37 mg/liter, which was sevenfold greater than the yield previously reported for a toxin-resistant CHO cell expression system. This methodology should be applicable to other toxin-related recombinant proteins in toxin-sensitive P. pastoris.     

Enhanced 2′-Fucosyllactose production by engineered Saccharomyces cerevisiae using xylose as a co-substrate

2′-Fucosyllactose (2′-FL), a human milk oligosaccharide with confirmed benefits for infant health, is a promising infant formula ingredient. Although Escherichia coli, Saccharomyces cerevisiae, Corynebacterium glutamicum, and Bacillus subtilis have been engineered to produce 2′-FL, their titers and productivities need be improved for economic production. Glucose along with lactose have been used as substrates for producing 2′-FL, but accumulation of by-products due to overflow metabolism of glucose hampered efficient production of 2′-FL regardless of a host strain. To circumvent this problem, we used xylose, which is the second most abundant sugar in plant cell wall hydrolysates and is metabolized through oxidative metabolism, for the production of 2′-FL by engineered yeast. Specifically, we modified an engineered S. cerevisiae strain capable of assimilating xylose to produce 2′-FL from a mixture of xylose and lactose. First, a lactose transporter (Lac12) from Kluyveromyces lactis was introduced. Second, a heterologous 2′-FL biosynthetic pathway consisting of enzymes Gmd, WcaG, and WbgL from Escherichia coli was introduced. Third, we adjusted expression levels of the heterologous genes to maximize 2′-FL production. The resulting engineered yeast produced 25.5 g/L of 2′-FL with a volumetric productivity of 0.35 g/L∙h in a fed-batch fermentation with lactose and xylose feeding to mitigate the glucose repression. Interestingly, the major location of produced 2′-FL by the engineered yeast can be changed using different culture media. While 72% of the produced 2′-FL was secreted when a complex medium was used, 82% of the produced 2′-FL remained inside the cells when a minimal medium was used. As yeast extract is already used as food and animal feed ingredients, 2′-FL enriched yeast extract can be produced cost-effectively using the 2′-FL-accumulating yeast cells.     

Growth media effects on morphology and 17β-HSD activity in the fungusCurvularia lunata

The filamentous fungusCurvularia lunata has enzymatic activities of biotechnological significance. Its 11β-hydroxylase actvity produces hydrocortisone, and its 17-ketosteroid reductase (17β-HSD) activity is important in the production of 17β-hydroxysteroids. We have examined the effects of different media on the 17β-HSD activity, and on the morphology and ultrastructure ofC. lunata in the search for a correlation between high enzymatic activity, morphology and ultrastructure. The highest 17β-HSD activity per dry weight ofC. lunata was seen in Czapek medium, while more product per volume was formed in malt extract broth. In all growth media tested, the highest 17β-HSD activity coincided with the exponential phase of growth. In Czapek broth medium, fungal hyphae formed pellets, while in malt extract and yeast nitrogen base broth media, the fungus formed branched hyphae dispersed throughout the media. Scanning electron microscopy revealed differences in the thickness of hyphal cells; those of the fungus grown in Czapek and yeast nitrogen base media were much thicker than those in malt extract medium. Transmission electron microscopy showed melanized cell walls in the fungus grown in malt extract and Czapek media, but not in yeast nitrogen base medium. Our results show that theC. lunata with the highest 17β-HSD activity grow as dispersed, melanized mycelia with thin hyphae.