Lipase production of Aspergillus oryzae

Aspergillus oryzae produced a small amount of lipase (0.05–0.8 U/wet-g of solid medium) in solid cultures, in contrast to the larger amount (0.46 U/ml) in a shake-flask culture in a modified GYP medium containing 2% glucose, 1% yeast extract and 2% Polypepton. Optimum conditions of lipase production in the submerged culture of A. oryzae were determined in terms of pH, composition of medium, and temperature. In a shake-flask culture at 28°C, the maximum amount of lipase increased to 0.78 U/ml upon the addition of 3% soybean oil to the modified GYP medium. In a jar fermentor culture, 30 U/ml lipase activity was obtained after 72 h at 28°C under appropriate conditions. Lipase production was greatly influenced by the culture temperature, and the optimum temperature for lipase production was about 24°C with a narrow temperature range, which was 10 degrees lower than that for the growth. In the submerged cultures, two kinds of lipase at least exhibiting different substrate specificities were also suggested.     

Production of Extracellular Acid Proteases by Aspergillus Clavatus

The production of extracellular acid proteases from Aspergillus clavatus was evaluated in a culture filtrate medium, with different carbon and nitrogen sources. The fungus was cultivated at three different temperatures during 10 days. The proteolytic activity was determined on haemoglobin pH 5.0 at 37 °C. The highest acid proteolytic activity (80 U/ml) was observed in culture medium containing glucose and gelatin at 1%(w/v) at 30 °C at the third day of incubation. Cultures developed in Vogel medium with glucose at 2%(w/v) showed at about 45% of proteolytic activity when compared to the cultures with 1% of the same sugar. The optimum pH of enzymatic activity was 2.0 and the enzyme was stable at pH values ranging from 2.0 to 4.0. The optimum temperature was 40 °C and the half-lives at 40, 45 and 50 °C were 30, 10 and 5 min, respectively. This revised version was published online in July 2006 with corrections to the Cover Date.     

Production of paramylon,a β‐1,3‐glucan,by heterotrophic cultivation of Euglena gracilis on a synthetic medium

Euglena gracilis was cultivated on a synthetic medium of well‐defined components. Biomass and paramylon (β‐1,3‐glucan) concentrations were the most important variables monitored. Mass production in the bioreactor was carried out following studies of operating conditions in shaken flasks. E. gracilis grew best at about 30°C and at a low pH of 3. A pH control was not necessary, although the pH increased considerably at the end of the cultivation processes. Aeration could be performed at low stirrer frequency. Biomass concentrations of about 13–14 g/L were obtained with paramylon mass fractions of 50–60%, by starting with a synthetic medium containing 15 g/L of glucose as the main carbon source.     

The Influence of n-Propanol on the Growth and Conidiation of Pestalotia rhododendri

Pestalotia rhododendri was exposed to vapours from 1 ml propanol solution in water and linear growth, formation of aerial hyphae and production of conidia were determined. A special Petri dish technique was used and maximum stimulation of conidial formation was induced by the vapours from a propanol concentration of 3–4 % (v/v) at 25°C. When propanol was added directly to the medium, a concentration of 1.2 × 10^?2M was optimal for growth and sporulation at 30°C. Sporulation stimulated by propanol was observed at temperatures from 20–32°C, with an optimum at 30°C. Certain observations indicated that an exposure to propanol for 24 hours was enough to induce a stimulated spore production. The stimulation was noticed on different media at 25°C, and was more pronounced at 30°C. One exception was observed. Propanol did not promote sporulation when the fungus was grown on maltagar at 30°C. Propanol 3 ° (v/v) in combination with the standard medium containing (NH₄)₂-tartrate as sole nitrogen source, inhibited the linear growth at 15–20°C, was inactive at 22.5° and 25°C, and stimulated growth at 27.5–31°C. The stimulatory effect was maximal at 30°C. Other media were tested at 25° and 30°C. At both temperatures stimulations of linear growth caused by propanol were observed with a medium containing KNO₃ as sole nitrogen source, and inhibitions with maltagar and another medium containing l -asparaginc as sole nitrogen source. The linear growth could be either inhibited or stimulated while the sporulation was stimulated.     

Production of the immunosuppressant cyclosporin A by a new soil isolate,Aspergillus fumigatus,in submerged culture

Cyclosporin A (CyA) has received meticulous attention owing to its immunosuppressive and biological activities. In this study, a soil isolate, capable of producing CyA, was named Zag1 strain and identified as Aspergillus fumigatus based on macroscopic and microscopic characteristics, 18S rDNA sequence, and phylogenetic characteristic analysis. To maximize the production of CyA, the fungal culture was grown under various fermentation conditions including selection of the cultivation medium, agitation rate, fermentation time, incubation temperature, pH value, inoculum nature, and medium volume. A simple medium (pH 5.0) containing 5% maltose as a carbon source and 2% potassium nitrate as a nitrogen source favored the highest CyA production when the fermentation process was maintained at 120 rpm for 9 days and at 30 °C using 3% standard inoculum of 5-day-old. The final CyA titer under these conditions was intensified to 2.23–3.31-fold, as compared with the amount obtained with seven types of basal media. A. fumigatus Zag1 appears to possess a good biotechnological potential for CyA production under favorable culture conditions.

     

Production and Characterization of an Exopolysaccharide by Yeast

Antarctic yeast strains were investigated for exopolysaccharide biosynthesis and the Sporobolomyces salmonicolor AL₁ strain was selected. It was studied for exopolysaccharide biosynthesis on different carbon and nitrogen sources. The investigations showed that sucrose and ammonium sulphate were suitable culture medium components for polymer biosynthesis. Exopolysaccharide formation by the yeast strain was accompanied by a decrease in the culture medium pH value from the initial pH 5.3 to pH 1.7–2.0. During the biosynthetic process, the dynamic viscosity of the culture broth increased to the maximum value of 15.37 mPas and the polysaccharide yield reached 5.63 g/l on a culture medium containing 5.00% sucrose and 0.25% ammonium sulphate at a temperature of 22 °C for 120 h. The crude polysaccharide obtained from Sp. salmonicolor AL₁ featured high purity (90.16% of carbon content) and consisted of glucose (54.1%), mannose (42.6%) and fucose (3.3%). Pure mannan containing 98.6% of mannose was isolated from it.     

Regulation of in vitro Ptr-toxin Production by Pyrenophora tritici-repentis Isolates by Environmental Parameters and Accumulation of Ptr-toxin in Culture over Time

Previous work has demonstrated the production of a low molecular weight toxin (designated Ptr-toxin) by isolates of Pyrenophora tritici-repentis (Died.) Drechs., the cause of tan spot of wheat (Triticum aestivum). Before the mechanisms by which Ptr-toxin is produced are understood, conditions for optimal toxin production must be identified. This study defined glucose concentration, light and temperature for optimal fungal growth and accumulation of Ptr-toxin in a defined mineral salts-glucose liquid medium. The accumulation of Ptr-toxin in culture was monitored over a 21-day period. The growth of six P. tritici-repentis isolates increased significantly over the range of 0.05–5.0% glucose; however, the greatest accumulation of Ptr-toxin was observed at 1 and 2% glucose. Significant increases in fungal dry weights were observed at 23 and 30°C, although the effect of temperature on toxin production remains questionable. No significant influence of light on growth and Ptr-toxin production was observed. Ptr-toxin continues to accumulate in culture over the 21-day period tested in this study. The results of the present study reveal much about the specific isolates included but little information upon which generalizations may be based. As such, screening numerous P. tritici-repentis isolates for Ptr-toxin production under one set of conditions appears to be unreliable.     

Intracellular polysaccharide of an anaerobic psychrophile <Emphasis Type="Italic">Clostridium algoriphilum</Emphasis>

Polysaccharide was revealed in the cytoplasm of spore-forming Clostridium algoriphilum 14D1 = VKM B-2271 = DSM 16153 grown on glucose at 5°C. This polymer was isolated, purified, and identified as a glycogen-like compound based on analysis of its hydrolysis products. The ratio of the polysaccharide to the dry biomass weight did not change in the course of culture growth. Limitation of C. algoriphilum 14D1 growth by nitrogen resulted in a doubling of the polysaccharide/dry biomass ratio. The transition of C. algoriphilum 14D1 cells from optimal conditions into carbon-free medium resulted in utilization of intracellular polysaccharide. The amount of polysaccharide was shown to depend on glucose concentration, type of the carbon substrate, and growth temperature. Future investigations of polysaccharide functions in C. algoriphilum 14D1 cells are discussed.     

Growth and β-Glucan 10C3K Production by a Mutant of Alcaligenes faecalis var. myxogenes in Defined Medium

A defined medium was developed in which Alcaligenes faecalis var. myxogenes 10C3 mutant K produced a large quantity of β-glucan 10C3K. The medium contained 4% glucose together with 0.1% citrate, succinate or fumarate as the carbon source, 0.15% (NH₄)₂HPO₄ as the nitrogen source and mineral salts. When NaNH₄HPO₄, KNO₃ or urea was used at a concentration of 0.03% nitrogen as the sole nitrogen source, salts of organic acid were not needed in addition to glucose.

In culture medium containing phosphate buffer (M/15, pH 6.5~8.0) large amounts of polysaccharide were formed and its yield from the 4% glucose added was about 50%. Thus, it was shown that polysaccharide production is enhanced greatly if a suitable pH for polysaccharide production is maintained during incubation.     

Fermentative production of shikimic acid: a paradigm shift of production concept from plant route to microbial route

Different physiological and nutritional parameters affect the fermentative production of shikimic acid. In our study, Citrobacter freundii initially produced 0.62 g/L of shikimic acid in 72 h. However, when process optimization was employed, 5.11 g/L of shikimic acid was produced in the production medium consisting of glucose (5.0 %), asparagine (4.5 %), CaCO₃ (2.0 %), at pH 6.0, when inoculated with 6 % inoculum and incubated at 30 ± 1 °C, 200 rpm for 60 h. Preliminary fed-batch studies have resulted in the production of 9.11 g/L of shikimic acid on feeding the production medium by 20 g/L of glucose at 24 h of the fermentation run. Production of similar amount of shikimic acid was observed when the optimized conditions were employed in a 10-L bioreactor as obtained in shake flask conditions. A total of 9.11 g/L of shikimic acid was produced in 60 h. This is approximately 14.69-fold increase in shikimic acid production when compared to the initial un-optimized production conditions. This has also resulted in the reduction of the production time. The present study provides useful information to the industrialists seeking environmentally benign technology for the production of bulk biomolecules through manipulation of various chemical parameters.     

Determination of the Chemical Form of Fluorine in Tea Infusions by 19F-NMR

A novel marine ice-nucleating bacterium, KUIN-5, was isolated from a marine algae, Monostroma latissum. Strain KUIN-5 was identified as a Pseudomonas sp. from its characteristics and taxonomies; the optimum temperature and pH for its growth were 25°C and 6.0, respectively. When strain KUIN-5 was aerobically cultured in Carlucci-Pramer medium (pH 6.0) for 50 h at 25°C, the highest ice-nucleating activity of the cells among the media for marine bacteria was obtained, and the ice-nucleating temperature, T₅₀, was indicated to be ? 3.2°C. Also, the optimum concentration of NaCl for the growth in this medium, which was prepared with distilled water instead of seawater, was 2.0% (w/v) and then the ice-nucleating activity was inversely proportional to the NaCl concentration. Moreover, when strain KUIN-5 was cultured in Davis medium under optimum conditions, it produced insoluble polysaccharide (IPS) in the culture. The maximum amount of IPS production by strain KUIN-5 was 84.5 mg/ml of medium under optimum conditions. Therefore, this IPS was isolated and could be identified as cellulose, based on TLC or HPLC of the acid hydrolysate, and GC-MS of the acetylated polyalcohol prepared by periodate oxidation and Smith degradation of this polysaccharide. This is the first report of cellulose production by a marine ice-nucleating bacterium.     

Production of highly active fungal milk-clotting enzyme by solid-state fermentation

Abstract

Cheese production is projected to reach 20 million metric tons by 2020, of which 33% is being produced using calf rennet (EC 3.4.23.4). There is shortage of calf rennet, and use of plant and microbial rennets, hydrolyze milk proteins non-specifically resulting in low curd yields. This study reports fungal enzymes obtained from cost effective medium, with minimal down streaming, whose activity is comparable with calf and Mucor rennet. Of the fifteen fungi that were screened, Mucor thermohyalospora (MTCC 1384) and Rhizopus azygosporus (MTCC 10195) exhibited the highest milk-clotting activity (MCA) of 18,383?±?486?U/ml and 16,373?± 558?U/ml, respectively. Optimization exhibited a 33% increase in enzyme production (30?g wheat bran containing 6% defatted soy meal at 30?°C, pH 7) for M. thermohyalospora. The enzyme was active from pH 5–10 and temperature 45–55?°C. Rhizopus azygosporus exhibited 31% increase in enzyme production (30?g wheat bran containing 4% defatted soy meal at 30?°C, pH 6) and the enzyme was active from pH 6–9 at 50?°C. Curd yields prepared from fungal enzyme extract decreased (5–9%), when compared with calf rennet and Mucor rennet. This study describes the potential of fungal enzymes, hitherto unreported, as a viable alternative to calf rennet     

Effects of ascorbic acid and uracil on exo-polysaccharide production with Hericium erinaceus in liquid culture

Hericium erinaceus is a well known edible and medicinal mushroom used in East-Asia. Recently, H. erinaceus has attracted a lot of attention owing to its antitumor, immuno-modulatory, and cytotoxic effect. It has been postulated that the fruiting body of H. erinaceus contains a polysaccharide that is similar to β-D-glucan, which is known to have antitumor activity against Sarcoma 180. However, optimized liquid culture conditions for enhanced polysaccharide productivity have yet to be developed, which is a necessary step for industrial applications. Therefore, the aim of this study was to determine the optimal liquid culture conditions for maximum polysaccharide production. In shake flask cultures, the optimal concentration of ascorbic acid was found to be 2.0 g/L, which prevented the broth from changing color from yellow to black. The optimal culture conditions were determined to be 23°C, 200 rpm, and a 10% inoculum size, at an uncontrolled initial pH. In addition, the modified medium contained 20 g/L glucose, 10 g/L yeast extract, and 2.0 g/L ascorbic acid. The maximum mycelial biomass and exo-polysaccharide (EPS) production in the modified medium containing uracil was 13.43 and 1.26 g/L, respectively.     

Optimization of single cell protein production from cassava starch (Rhizopus oligosporus)

The fermentation pattern of cassava starch utilization was investigated at 37°C using Rhizopus oligosporus UQM 145 F and eight different media. Depending on the medium used, the addition of zinc or zinc plus iron to a combination of calcium plus manganese switches the fermentation from glucose accumulation to biomass (single cell protein) production. Complete starch hydrolyzation was obtained in both cases, with a complete glucose utilization resulting in 24 g biomass containing 30% true protein per 100 g cassava starch (= 7.45 g SCP/100 g substrate) in 24 hours. In the case of glucose accumulation, biomass was kept low and 15.5 g/l glucose representing 57.3% of starch supplied were obtained in 36 hours. R. oligosporus UQM 145 F grows well between 30° and 45°C. At 45°C and pH 5.0, 7.0 g SCP/100 g substrate were obtained, which rose to 8.6 g if cassava starch is replaced by ground cassava tuber.     

Characterization of a reptilian epithelioid skin cell line derived from the green sea turtle,Chelonia mydas

Summary A continuous line of epithelioid cells was established from explant skin tissues of the green sea turtle,Chelonia mydas. These cells, designated GTS, have been subcultured more than 60 times in commercially available mammalian cell culture medium supplemented with 5% bovine calf serum. Of those temperatures tested, optimal growth was achieved at 30°C although replication occurred between 16 and 37°C. These cells may be held as monolayers at 8°C or stored frozen in growth medium containing 10% dimethylsulfoxide at −70 or −196°C. The modal number of 55 chromosomes per cell is in agreement with the heterogametic female diploid number of this species. The GTS line represents the first established culture of normal epithelioid skin cells to be reported for a poikilothermic species.     

Chemostat production of pediocin SM‐1 by Pediococcus pentosaceus Mees 1934

Production of the bacteriocin pediocin SM‐1 by Pediococcus pentosaceus Mees 1934 was investigated in pH‐controlled batch and chemostat cultures using a complex medium containing glucose, sucrose or fructose. In chemostat cultures operated at 150 rpm, 30°C, 60% dissolved oxygen tension, pH 6.5, and D = 0.148 h^?1, the pediocin titer reached 185 AU/mL representing an increase of 32% compared with batch cultures in which glucose was used as the carbon source. Pediocin biosynthesis was markedly affected by the growth rate of the producer microorganism. For all carbon sources tested, pediocin production appeared to take place only at dilution rates lower than μ_max. However, only glucose supported production at the very low dilution rate of 0.05 h^?1 indicating a direct regulation of pediocin biosynthesis by the carbon source. Glucose supported higher biomass productivity and higher pediocin titers and yields compared with the other sugars used. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1481–1486, 2015     

A Novel Culture Method for High Level Production of Heterologous Protein in Saccharomyces cerevisiae

A high level production system for heterologous protein by cold culture of yeast transformants at 15°C was developed. The yeast transformants, carrying a plasmid containing cDNA for Aspergillus oryzae α-amylase (Taka-amylase A) or human lysozyme synthetic DNA, were cultivated in a selective medium for 1 or 2 days until full growth at 30°C. The yeast cells were harvested by centrifugation from the culture fluid and then were transferred to YPD medium. These inoculated broths were incubated for 2 days at 15°C and then for another 2 days at 30°C. By the cold culture method described above, higher amounts of Taka-amylase A (28.6 mg/liter) and human lysozyme (6.1 mg/liter) were produced by the yeast transformants compared to those by conventional methods.

Heterologous protein productions using YEp, YCp, and YIp types of yeast expression vectors with ADH1 or GAPDH promoter by the cold culture method showed effective productivity of about 2-fold compared to those by the conventional method of culture at 30°C. The high level production of heterologous protein by this method was not specific to the S. cerevisiae strains examined.     

Optimization of culture conditions and bench-scale production of anticancer enzyme L-asparaginase by submerged fermentation from Aspergillus terreus CCT 7693

L-Asparaginase amidohydrolase (EC 3.5.1.1) has received significant attention owing to its clinical use in acute lymphoblastic leukemia treatment and non-clinical applications in the food industry to reduce acrylamide (toxic compound) formation during the frying of starchy foods. In this study, a sequential optimization strategy was used to determine the best culture conditions for L-asparaginase production from filamentous fungus Aspergillus terreus CCT 7693 by submerged fermentation. The cultural conditions were studied using a 3-level, central composite design of response surface methodology, and biomass and enzyme production were optimized separately. The highest amount of biomass (22.0?g·L^?1) was obtained with modified Czapek–Dox medium containing glucose (14?g·L^?1), L-proline (10?g·L^?1), and ammonium nitrate (2?g·L^?1) fermented at 37.2?°C and pH 8.56; for maximum enzyme production (13.50?U·g^?1), the best condition was modified Czapek–Dox medium containing glucose (2?g·L^?1), L-proline (10?g·L^?1), and inoculum concentration of 4.8?×?10⁸ espore·mL^?1 adjusted to pH 9.49 at 34.6?°C. The L-asparaginase production profile was studied in a 7?L bench-scale bioreactor and a final specific activity of 13.81?U·g^?1 was achieved, which represents an increase of 200% in relation to the initial non-optimized conditions.     

Production of a New Acidic Polysaccharide,Succinoglucan by Alcaligenes faecalis var. myxogenes

A slimy non-spore-forming bacterium strain 10C3 isolated from soil was motile with peritrichous flagella and named Alcaligenes faecalis var. myxogenes. Studies were made on the conditions necessary for maximal production of a new acidic succinoglucan polysaccharide by this strain in shaken cultures. Much production was observed with sucrose, glucose, xylose, galactose, cellobiose, maltose, fructose, mannose and rhamnose. The yield was greatest with sucrose and decreased in order with the above sugars from about 36 to 23 per cent. The most suitable medium contained 4 per cent sugar, 0.5 per cent yeast extract and one per cent calcium carbonate in tap water. The optimum temperature was 28°C.     

Repeated pH-stat fed-batch fermentation for rhamnolipid production with indigenous Pseudomonas aeruginosa S2

Rhamnolipid is one of the most commonly used biosurfactants with the ability to reduce the surface tension of water from 72 to 30 mN/m. An indigenous isolate Pseudomonas aeruginosa S2 possessing excellent ability to produce rhamnolipid was used as a model strain to explore fermentation technology for rhamnolipid production. Using optimal medium and operating conditions (37°C, pH 6.8, and 250 rpm agitation) obtained from batch fermentation, P. aeruginosa S2 was able to produce up to 5.31 g/l of rhamnolipid from glucose-based medium. To further improve the rhamnolipid yield, a pH-stat fed-batch culture was performed by maintaining a constant pH of 6.8 through manipulating glucose feeding. The effect of influent glucose concentration on rhamnolipid yield and productivity was investigated. Using the pH-stat culture, a maximum rhamnolipid concentration (6.06 g/l) and production rate (172.5 ml/h/l) was obtained with 6% glucose in the feed. Moreover, combining pH-stat culture with fill-and-draw operation allowed a stable repeated fed-batch operation for approximately 500 h. A marked increase in rhamnolipid production was achieved, leading to the best rhamnolipid yield of approximately 9.4 g/l during the second repeated run.