Effect of Aeration on Growth and Aflatoxin Production by Aspergillus flavus in Submerged Culture

Aspergillus flavus ATCC 15517 produced up to 212 mg per liter of total aflatoxin in submerged culture in aerated (3,000, 6,000, 9,000, and 12,000 ml/min) and agitated medium in 14-liter fermentors with 10 liters of medium consisting of 2% yeast extract and 10% sucrose. Aflatoxin production increased with time. A maximum of 212 mg/liter was produced at 9,000 ml/min aeration, whereas the yield decreased substantially at the lower aeration rates. Two other strains of A. flavus synthesized aflatoxin in smaller quantities.     

A novel recycle batch immobilized cell bioreactor for propionate production from whey lactose

Recycle batch fermentations using immobilized cells of Propionibacterium acidipropionici were studied for propionate production from whey permeate, de-lactose whey permeate, and acid whey. Cells were immobilized in a spirally wound fibrous sheet packed in a 0.5-L column reactor, which was connected to a 5-L stirred tank batch fermentor with recirculation. The immobilized cells bioreactor served as a breeder for these recycle batch fermentations. High fermentation rates and conversions were obtained with these whey media without nutrient supplementation. It took approximately 55 h to ferment whey permeate containing approximately 45 g/L lactose to approximately 20 g/L propionic acid. Higher propionate concentrations can be produced with various concentrated whey media containing more lactose. The highest propionic acid concentration obtained with the recycle batch reactor was 65 g/L, which is much higher than the normal maximum concentration of 35 to 45 g/L reported in the literature. The volumetric productivity ranged from 0.22 g/L . h to 0.47 g/L . h, depending on the propionate concentration and whey medium used. The corresponding specific cell productivity was 0.033 to 0.07 g/L . g cell. The productivity increased to 0.68 g/L . h when whey permeate was supplemented with 1% (w/v) yeast extract. Compared with conventional batch fermentation, the recycle batch fermentation with the immobilized cell bioreactor allows faster fermentation, produces a higher concentration of product, and can be run continually without significant downtime. The process also produced similar fermentation results with nonsterile whey media. (c) 1995 John Wiley & Sons, Inc.     

Homo-fermentative production of d-lactic acid by Lactobacillus sp. employing casein whey permeate as a raw feed-stock

Casein whey permeate (CWP), a lactose-enriched dairy waste effluent, is a viable feed stock for the production of value-added products. Two lactic acid bacteria were cultivated in a synthetic casein whey permeate medium with or without pH control. Lactobacillus lactis ATCC 4797 produced d-lactic acid (DLA) at 12.5 g l^?1 in a bioreactor. The values of Leudking–Piret model parameters suggested that lactate was a growth-associated product. Batch fermentation was also performed employing CWP (35 g lactose l^?1) with casein hydrolysate as a nitrogen supplement in a bioreactor. After 40 h, L. lactis produced 24.3 g lactic acid l^?1 with an optical purity >98 %. Thus CWP may be regarded as a potential feed-stock for DLA production.     

Lactic acid from cheese whey permeate. Productivity and economics of a continuous membrane bioreactor

The economics of incorporating membrane modules in several steps in the conversion of whey permeate to lactic acid was studied. Membrane recycle fermenters operating at a cell concentration of 40 g l^–1 resulted in a productivity of 22.5 g l^–1h^–1 with a lactate concentration of 89 g l^–1 and a yield of 0.89. The membrane units (reverse osmosis for preconcentrating whey permeate, hollow-fiber ultrafiltration for clarification and for cell recycling) contribute about 28% of the total fixed capital costs and less than 5% of the operating cost. The two largest costs are whey transportation and yeast extract, contributing about 35% and 38% to the total product cost of US $ 0.98/kg 85% lactate. Without these two costs, unpurified lactate could be produced for $ 0.27/kg.     

Enhanced Conversion of Lactose to Glycerol by Kluyveromyces fragilis Utilizing Whey Permeate as a Substrate

Kluyveromyces fragilis (CBS 397) is a nonhalophilic yeast which is capable of lactose utilization from whey permeate and high glycerol production under anaerobic growth conditions. However, the optimum yields of glycerol (11.6 mg/ml of whey permeate medium) obtained in this study occurred only in the presence of 1% Na₂SO₃ as a steering agent. The use of other concentrations of Na₂SO₃, as well as 5% NaCl and 1% ascorbic acid, had no or detrimental effects on cell growth, lactose utilization, and glycerol production. Glycerol yields were greater in cultures grown from a light inoculum of K. fragilis than in cultures in which a resuspended mass of cells was introduced into the medium. The results of this study suggest that this strain of K. fragilis may be useful commercially in the utilization of cheese whey lactose and the concomitant production of glycerol.     

Simultaneous production of single cell protein and killer toxin by Wickerhamomyces anomalus HN1-2 isolated from mangrove ecosystem

The yeast Wickerhamomyces anomalus (the previous name was Pichia anomala) HN1-2 isolated from the mangrove ecosystem was found to be able to produce high level of both killer toxin and single cell protein. When the killer yeast cells were grown by batch cultivation in 5-l fermentor, crude protein in the cells, cell mass, reducing sugar, and diameter of the inhibition zone reached 56.0 g per 100 g of cell dry weight, 7.3 g per liter, 9.5 g per liter, and 19.0 mm, respectively within 12 h and this yeast synthesized a large amount of the essential amino acids, such as lysine (7.8%), methionine (1.8%), and leucine (9.0%). The crude killer toxin produced by the killer yeast isolate HN1-2 could kill the cells of Lodderomyces elongisporus, Candida albicans, Metschnikowia bicuspidata, Pichia guilliermondii, Saccharomyces cerevisiae, Yarrowia lipolytica, and Kluyveromyces aestuarii, which were widely distributed in natural marine environments. The results also showed that the undesirable yeast could be avoided during cell growth of the killer yeast.     

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.     

Influence of whey permeate and millet as substrates on thermotolerance of Beauveria bassiana and Metarhizium anisopliae conidia during storage

Conidia from Beauveria bassiana and Metarhizium anisopliae, produced in quarter-strength Sabouraud dextrose agar amended with yeast extract, whey permeate, and millet agar, were exposed to 45°C for 90 min prior to and at 30 d post-storage at 25°C. B. bassiana produced in whey permeate or millet had better thermotolerance than the other treatments after the storage.     

Studies on methanol-oxidizing yeasts

A series of yeast strains utilizing methanol as the only source of carbon and energy were isolated both from soil and waste waters. Growth of the yeasts was studied in a mineral medium with yeast extract at 30°C. Growth parameters, Q_{o 2} and composition of biomass were studied in the strain 11Bh producing in shaken flasks highest yields of biomass. The biomass was found to contain 44% of crude proteins, 2% esterified fatty acids, 3% non-esterified fatty acids, 6% RNA and 0.25% DNA. Amino acid analysis revealed a high content of essential amino acids, lysine, leucine, valine and threonine in particular.     

Biosurfactant Production and Surface Translocation Are Regulated by PlcR in Bacillus cereus ATCC 14579 under Low-Nutrient Conditions

Bacillus cereus ATCC 14579 can respond to nutrient changes by adopting different forms of surface translocation. The B. cereus ATCC 14579 ΔplcR mutant, but not the wild type, formed dendritic (branched) patterns on EPS [a low-nutrient medium that contains 7.0 g K₂HPO₄, 3.0 g KH₂PO₄, 0.1 g MgSO₄·7H₂O, 0.1 g (NH₄)₂SO₄, 0.01 g CaCl₂, 0.001 g FeSO₄, 0.1 g NaCl, 1.0 g glucose, and 125 mg yeast extract per liter] containing 0.7% agar. The dendritic patterns formed by sliding translocation of nonflagellated cells are enhanced under low-nutrient conditions and require sufficient production of a biosurfactant, which appears to be repressed by PlcR. The wild-type and complemented strains failed to slide on the surface of EPS agar because of the production of low levels of biosurfactant. Precoating EPS agar surfaces with surfactin (a biosurfactant produced by Bacillus subtilis) or biosurfactant purified from the ΔplcR mutant rescued the ability of the wild-type and complemented strains to slide. When grown on a nutrient-rich medium like Luria-Bertani agar, both the wild-type and ΔplcR mutant strains produced flagella. The wild type was hyperflagellated and elongated and exhibited swarming behavior, while the ΔplcR mutant was multiflagellated and the cells often formed long chains but did not swarm. Thin-layer chromatography and mass spectrometry analyses suggested that the biosurfactant purified from the ΔplcR mutant was a lipopeptide and had a mass of 1,278.1722 (m/z). This biosurfactant has hemolytic activity and inhibited the growth of several gram-positive bacteria.     

Ethanol production from whey permeate by immobilized yeast cells

The ability of two yeast strains to utilize the lactose in whey permeate has been studied. Kluyveromyces marxianus NCYC 179 completely utilized the lactose (9.8%), whereas Saccharomyces cerevisiae NCYC 240 displayed an inability to metabolize whey lactose for ethanol production. Of the two gel matrices tested for immobilizing K. marxianus NCYC 179 cells, sodium alginate at 2% (w/v) concentration proved to be the optimum gel for entrapping the yeast cells effectively. The data on optimization of physiological conditions of fermentation (temperature, pH, ethanol concentration and substrate concentration) showed similar effects on immobilized and free cell suspensions of K. marxianus NCYC 179, in batch fermentation. A maximum yield of 42.6 g ethanol l^?1 (82% of theoretical) was obtained from 98 g lactose l^?1 when fermentation was carried at pH 5.5 and 30°C using 120 g dry weight l^?1 cell load of yeast cells. These results suggest that whey lactose can be metabolized effectively for ethanol production using immobilized K. marxianus NCYC 179 cells.     

Arachidonic Acid Production by Fungi

After preliminary screening, Mortierella alpina and Mortierella elongata were compared with respect to arachidonic acid content. M. alpina ATCC 16266 produced 2.1 g of arachidonic acid per liter in media containing 10% glucose while the highest percentage of arachidonic acid in lipid (43.3%) was observed at a glucose concentration of 2%. Arachidonic acid content in lipids increased to 66% during storage.     

Thermoanaerobacter ethanolicus Growth and Product Yield from Elevated Levels of Xylose or Glucose in Continuous Cultures

The performance of Thermoanaerobacter ethanolicus was evaluated in continuous culture with media containing concentrations of xylose (8 to 20 g/liter) greater than those previously reported. The ethanol yield declined from to 0.42 to 0.29 g of ethanol per g of xylose consumed when input xylose was increased from 4 to 20 g/liter. Yields of both total C₂ and C₃ products from consumed xylose and of cell biomass from ATP produced declined as the input xylose concentration was increased, which was not the case when glucose was the substrate. This suggested that yeast extract functioned as a significant energy and carbon source for cells in fermentations of xylose but not of glucose. The feasibility of this interpretation was confirmed by (i) the calculation of the products theoretically obtainable from yeast extract and (ii) the observation of significant quantities of fermentation products in inoculated sugar-free media. Markedly different patterns of metabolism for the two sugar substrates were also evidenced by the cell yield for glucose being twice that of xylose at elevated sugar concentrations. It was noted that caution must be exerted when results obtained at low xylose concentrations are extrapolated to predict those which can be obtained at higher concentrations.     

Laboratory-scale production of acetoin plus diacetyl by Enterobacter cloacae ATCC 27613

Conditions for the laboratory-scale production of acetoin plus diacetyl by Enterobacter Cloacae ATCC 27613 were studied. Thirty-five g acetoin plus diacetyl/50 g sucrose were obtained when fermentation was carried out in 2. 5 liter medium containing 12.5 g peptone and 12. 5 g yeast extract, at pH 7.0, in a 5 liter conical flask on a shaker (240rpm) at 28–30°C for 48 hr. Recovery of pure diacetyl was 85% of the total plus diacetyl.     

Optimization of fermentation conditions for ethanol production from whey

Summary Optimal conditions for ethanol production in 7% whey solutions by the yeast Candida pseudotropicalis ATCC 8619 included initial pH of 4.57 and 30°C. Complete fermentation of the available lactose took place without supplementary nutrients; additions of nitrogen or phosphorus salts, yeast extract or corn steep liquor resulted in increased yeast production and lower ethanol yields. A positive correlation was observed between increases in yeast inocula and lactose utilization and ethanol production rates; 8.35 g/l of ethanol was obtained within 22 h by using yeast inoculum of 13.9 g/l. No differences in fermentation rates or ethanol yields were observed when whole or deproteinized whey solutions were used. Concentrated whey permeates, obtained after removal of the valuable proteins from whey, can be effectively fermented for ethanol production.     

Production of thermotolerant entomopathogenic fungal conidia on millet grain

Thermotolerance of entomopathogenic (insect-killing) fungi should be seriously considered before industrialization. This work describes the feasibility of millet grain as a substrate for production of thermotolerant Beauveria bassiana (Bb) GHA and ERL1170 and Metarhizium anisopliae (Ma) ERL1171 and ERL1540 conidia. First, conidial suspensions of the Bb isolates, produced on millet grain in polyethylene bags, were exposed to five temperatures (43–47°C) at 15-min intervals for up to 120 min (experiment I). Agar-based quarter-strength (¼) Sabouraud dextrose agar supplemented with yeast extract (SDAY) and whey permeate media served as controls. Millet-grain-based culture was superior in producing the most thermotolerant Bb conidia, followed by whey permeate agar and ¼SDAY-based cultures. Secondly, to compare the thermotolerance of conidia produced at the same conditions, the Bb isolates were then produced on agar-based millet powder medium, with ¼SDAY and whey permeate agar media as controls, and the two Ma isolates were added (experiment II). They were then exposed to the same temperatures as above. More thermotolerant Bb and Ma conidia were produced on millet powder agar than on whey permeate agar and ¼SDAY overall. These results suggest that millet grain can be used as a substrate to produce thermotolerant conidia in a mass production system.     

Production of docosahexaenoic acid byThraustochytrium roseum

Summary When threeThraustochytrium stains were cultivated in liquid media containing 2.5% starch and 0.2% yeast extract, initial pH 6.0, with shaking under fluorescent light for five days at 25°C, similar biomass yields were observed (9.7–10.3 g L^–1). Contents of docosahexaenoic acid (DHA) in biomass varied: 0.15, 3.55 and 6.40% w/w forT. striatum ATCC 24473,T. aureum ATCC 34304 andT. roseum ATCC 28210, respectively. In further studies,T. roseum produced a maximum titer of 0.85 g of DHA per liter of culture broth. The DHA content of total lipids ranged from 46–49% w/w.     

A new medium for spore production of <Emphasis Type="Italic">Blakeslea trispora</Emphasis> using response surface methodology

Optimization of the medium components which enhance sporulation of the two mating types of the fungus Blakeslea trispora ATCC 14271 and ATCC 14272 (a heterothallic Zygomycota producing carotene) was achieved with the aid of response surface methodology (RSM). Glucose, corn steep liquor, yeast extract, and ammonium sulfate were investigated as carbon and nitrogen sources in a basal medium. RSM was adopted to optimize the medium in order to obtain a good growth of the fungus as a prerequisite for enhanced sporulation. In the second step, the basal medium was supplemented with different trace elements which significantly affect sporulation (i.e. CuSO₄·5H₂O, FeCl₃·6H₂O, Co(NO₃)₂·6H₂O, and MnCl₂·4H₂O). Central composite design proved to be valuable in optimizing a chemically defined solid medium for spore production of B. trispora. The composition of the new solid medium to enhance spore production by B. trispora (ATCC 14271) is as follows (per liter): 7.5 g glucose, 3.2 g corn steep liquor, 1.7 g yeast extract, 4.1 g ammonium sulfate, 6 mg CuSO₄·5H₂O, 276 mg FeCl₃·6H₂O, 2 mg Co(NO₃)₂·6H₂O, and 20 g agar (pH 6.0). Practical validation of this optimum medium gave spore number of 1.2 × 10⁸ spores/dish which is 77% higher than that produced in Potato Dextrose Agar (PDA). In the case of B. trispora (ATCC 14272) the new solid substrate for enhanced sporulation consists of (per l) 6.4 g glucose, 3.3 g corn steep liquor, 1.4 g yeast extract, 4.3 g ammonium sulfate, 264 mg CuSO₄·5H₂O, 485 mg FeCl₃·6H₂O, 223 mg MnCl₂^.4H₂O, and 20 g agar (pH 6.0). Spore numbers of 2 × 10⁷ spores/dish were obtained on the new medium by B. trispora (ATCC 14272), which is 95% higher than that produced on PDA. The results corroborated the validity and the effectiveness of the models. The new media considerably improved sporulation of both strains of B. trispora compared to the production of spores on PDA, which is the medium usually used for sporulation of the fungus.     

Influence of growth supplements on lactic acid production in whey ultrafiltrate by Lactobacillus helveticus

Summary Investigations have been carried out on lactic acid production by Lactobacillus helveticus CNRZ 303 in whey ultrafiltrate. Addition of beet molasses was investigated with good results, although yeast extract proved to be more effective. The size of inoculum and the preculture medium also played a significant role in determining the amount of lactic acid produced during the fermentation process. High lactose consumption (94.09%), together with good lactic acid production (26.09 g/l) and yield (0.90%), were obtained in whey ultrafiltrate supplemented with 1% (w/v) beet molasses (WUM), with a 10% (w/v) inoculum and peptonized milk as preculture medium. Although these results were similar to those obtained when yeast extract was used as supplement, the maximum volumetric productivities proved to be quite different, and were definitely higher with yeast extract. Offprint requests to: L. Chiarini     

Extracellular Formation of O-Butylhomoserine by Anaerobes

Clostridium BB–264, Cl. acetobutyricum 314–48, Cl. kaneboi, Cl. saccharoperbutylacetonicum and other two strains of Cl isolated recently produced an unidentified ninhydrin-positive compound in medium containing 5 % glucose, 1 % ammonium acetate, 0.1 % potassium dihydrogen phosphate, 0.04 % magnesium sulfate, 0.001 % ferrous sulfate, 0.1 % yeast extract, 10 μg/liter of biotin and 1 % calcium carbonate.

This ninhydrin-positive compound was eluted with solvent composed of butanol: acetic acid: water (4: 1: 2) by chromatography on cellulose powder column. It was crystallized from ethanol and then identified as an amino acid, O-butylhomoserine (Abbrev. as O-BHSer). Yield of this amino acid increased by adding homoserine or butanol to the medium. The increase was also recognized with addition of glycine, lysine, serine, threonine or valine. The formation of this amino acid was repressed by adding methionine to the medium.

Gas pressure to the culture is one of the important factors that make the amino acid formation by anaerobes possible.