Production of polygalacturonase byByssochlamys fulva

Summary Byssochlamys fulva was grown in two fermentation media using shake flasks, stirred fermentor and disc fermentor under conditions to give maximum production of pectolytic enzymes. Only polygalacturonase activity was detected in the culture filtrates during all fermentations. In all production conditions studied, no evidence of pectin methylesterase, pectin lyase, cellulase or proteinase activities were found. The maximum polygalacturonase activity (4.5 units/ml) was achieved when the microorganism was grown on medium II in shake flasks at pH 4.0–4.5 and 30°C after 12 days of fermentation.     

Exopolysaccharide production by Acremonium persicinum in stirred-tank and air-lift fermentors

Summary Exopolysaccharide production by the fungus Acremonium persicinum was affected by the culture system used. The yields achieved in shake flasks were not obtained in a stirred tank reactor, except at very low stirring speeds (100 rpm). However when grown in an air-lift fermentor, exopolysaccharide levels were similar to those found with shake flask cultures. Results suggest that both dissolved oxygen tension and shear rate may determine the ability of this organism to synthesise this exopolysaccharide. Offprint requests to: R. J. Seviour     

溶氧对Blakeslea trispora分批发酵生产β-胡萝卜素的影响

在摇瓶和5 L发酵罐中研究了溶氧 (DO) 对Blakeslea trispora分批发酵生产β-胡萝卜素的影响,总结了5 L发酵罐中β-胡萝卜素发酵过程中溶氧的变化规律.结果表明,当500 mL摇瓶装液量为50 mL,转速为240 r/min条件下发酵生产β-胡萝卜素产量最大,达到3.416 g/L; 5 L发酵罐中,在搅拌转速为1 000 r/min,通气量为1.5 vvm的条件下,β-胡萝卜素的产量可达到3.712 g/L,略高于摇瓶,这可能是由于5 L发酵罐中的气液传递和混合状况好于摇瓶,促进了产物的合成.     

Effect of Culture Conditions on the Production of d-Galactose Oxidase by Dactylium dendroides

The effects on enzyme production of inoculum size and age, medium composition, and culture conditions were studied in shake flasks and in a pilot-plant fermentor. Using a medium consisting of glucose, yeast extract, and inorganic salts in deionized water, we found that the addition of Cu(++) was essential for the formation of active enzyme. Cultures grown in the absence of added copper produced an inactive enzyme protein which could be activated by 10(-3) M Cu(++). Thiamine fulfilled all requirements for exogenous vitamins for growth and enzyme production. Glucose concentrations higher than 1% markedly suppressed enzyme formation. The mycelium inactivated the enzyme on prolonged incubation of the culture. Mycelial autolysates and sonic extracts were found to contain a thermostable and slowly dialyzable galactose oxidase-inactivating factor. The experiments suggest that this factor operates as a chelating agent which forms complexes with the copper of the enzyme. Copper ions (10(-3) M) prevented enzyme inactivation and restored activity to samples previously inactivated by this factor.     

Enterotoxin production by Vibrio cholerae and Vibrio mimicus grown in continuous culture with microbial cell recycle

We have examined the effect of complete cell recycle on the production of cholera toxin (CT) by Vibrio cholerae and CT-like toxin by Vibrio mimicus in continuous culture fermentations. Complete cell recycle was obtained by filtering culture fluids through Amicon hollow fibers with an exclusion limit of 100,000 daltons (H1P100-20) and returning the concentrated cell slurry to the fermentor. A single 1-liter laboratory fermentor system modified with this recycle loop was capable of producing over 20 liters of cell-free culture filtrate per day. Toxin production in this system was compared with yields obtained in traditional continuous cultures and in shake flask cultures. Yields of CT from V. cholerae 569B in the recycle fermentor were highest at the highest dilution rate employed (1.0 vol/vol per h). The use of complete cell recycle dramatically increased yields over those obtained in continuous culture and equaled those obtained in shake flasks. The concentration of CT in the filtrate was slightly less than half of that measured in culture fluids sampled at the same time. Similarly, V. mimicus 61892 grown in the presence of 50 micrograms of lincomycin per ml produced 280 ng of CT per ml in the recycle fermentor, compared with 210 ng/ml in shake flasks under optimal conditions. The sterile filtrate from this fermentation contained 110 ng/ml.     

深层液体培养法生产沼泽红假单胞菌

根据沼泽红假单胞菌 (Rhodopseudomonaspalustris)在好氧黑暗条件下也可生长的特性 ,采用液体深层培养方法 ,在通气式发酵罐中进行大规模生产。对培养基中的碳源、氮源、生长因子和微量元素进行了优化 ,用正交试验确定了主要培养基成分的添加量和接种量。在 10 0 0mL三角瓶和 2 5L全自动通气式发酵罐上进行了放大试验 ,在适宜工艺条件下培养 2 4h ,菌体浓度可达 6 0亿 /mL。     

Effect of bioreactor configuration on the growth and maturation of Picea sitchensis somatic embryo cultures

Somatic embryo suspension cultures of Picea sitchensis (Sitka spruce) derived from two cell lines, SS03 and SS10, were grown in shake flasks, air-lift, bubble, stirred tank and hanging stirrer bar bioreactors. Cell line SS03 yielded freely suspended and individual stage 1 embryos, while the embryos of SS10 were present in large aggregates. Compared to shake flasks, proliferation in bioreactors resulted in increased biomass; however, cell line morphology influenced the effect of different bioreactor configurations on growth and maturation of embryo cultures. Somatic embryos grown in shake flasks and bioreactors were matured on gelled solid medium and in submerged culture where gelled solid medium was covered with a layer of liquid medium. The number of stage 3 (mature) embryos produced from SS03 in the bubble bioreactor was significantly higher than those from stirred tank and hanging stirrer bar bioreactors with both solid medium and submerged culture. Submerged culture was unsuitable for SS10 embryo maturation. This revised version was published online in June 2006 with corrections to the Cover Date.     

Enterotoxin production by Vibrio cholerae and Vibrio mimicus grown in continuous culture with microbial cell recycle.

We have examined the effect of complete cell recycle on the production of cholera toxin (CT) by Vibrio cholerae and CT-like toxin by Vibrio mimicus in continuous culture fermentations. Complete cell recycle was obtained by filtering culture fluids through Amicon hollow fibers with an exclusion limit of 100,000 daltons (H1P100-20) and returning the concentrated cell slurry to the fermentor. A single 1-liter laboratory fermentor system modified with this recycle loop was capable of producing over 20 liters of cell-free culture filtrate per day. Toxin production in this system was compared with yields obtained in traditional continuous cultures and in shake flask cultures. Yields of CT from V. cholerae 569B in the recycle fermentor were highest at the highest dilution rate employed (1.0 vol/vol per h). The use of complete cell recycle dramatically increased yields over those obtained in continuous culture and equaled those obtained in shake flasks. The concentration of CT in the filtrate was slightly less than half of that measured in culture fluids sampled at the same time. Similarly, V. mimicus 61892 grown in the presence of 50 micrograms of lincomycin per ml produced 280 ng of CT per ml in the recycle fermentor, compared with 210 ng/ml in shake flasks under optimal conditions. The sterile filtrate from this fermentation contained 110 ng/ml.     

Reproducing shake flasks performance in stirred fermentors: production of alginates by Azotobacter vinelandii

Keeping equal the initial power drawn (0.27 W l(-1)) in shake flasks and in a stirred fermentor did not reproduce the behaviour of alginate production by Azotobacter vinelandii. A lower mean molecular weight (1.1x10(6) Da) of the polymer was obtained in the bioreactor as compared to that obtained in shake flasks (1.9x10(6) Da). The reasons for this can reside in the fact that the evolution of the power drawn in the shake flasks could be considerably different to that observed in the stirred bioreactor. A drastic drop in the specific power drawn is expected in the shake flasks as a consequence of the increased viscosity, which caused the liquid not following the movement of the shaker. This was supported by the fact that cultures developed in the fermentor at lower initial power drawn (as low as 0.027-0.056 W l(-1)) or in a culture in which the power drawn was deliberately reduced along cultivation, produced alginates with similar molecular characteristics as that obtained in shake flasks.     

Production of carbonyl reductase by Metschnikowia koreensis

A new strain of the yeast Metschnikowia koreensis was grown in shake flasks and a stirred bioreactor for the production of carbonyl reductase. The optimal conditions in the bioreactor for maximizing the biomass specific activity of the enzyme were found to be: a medium composed of glucose (20 g/L), peptone (5 g/L), yeast extract (5 g/L) and zinc sulfate (0.3g/L); the pH controlled at 7; the temperature controlled at 25 °C; an agitation speed of 500 rpm; and an aeration rate of 0.25 vvm. In the bioreactor, a biomass specific enzyme activity of 115.6 U/gDCW was obtained and the maximum biomass concentration was 15.3 gDCW/L. The biomass specific enzyme activity obtained in the optimized bioreactor culture was 11-fold higher than the best result achieved in shake flasks. The bioreactor culture afforded a 2.7-fold higher biomass concentration than could be attained in shake flasks.     

Fermentation of recombinant yeast producing hepatitis B surface antigen

Summary Fermentations were performed to determine parameters affecting the expression of hepatitis B surface antigen (HBsAg) in the yeastSaccharomyces cerevisiae containing the HBsAg gene. These studies emphasized inereasing both the relative abundance (HBsAg: cell mass) and total production of HBsAg. Specific activity was increased 70-fold when cells were grown in shake flasks containing nonselective rather than selective medium. The addition of adenine, ammonium sulfate or glucose to the complex medium reduced the production of antigen. Results similar to those achieved in shake flasks were obtained when the growth was performed in fermenters. A nutrient addition system was employed to increase the production of cells and HBsAg. The addition of glucose to the culture medium increased cell mass 6-fold but decreased the production of antigen. This imbalance was corrected by supplementing the glucose with complex nutrients.     

Production of α-amylase in a low cost medium by Bacillus licheniformis TCRDC-B13

A low cost synthetic medium producing large quantities of α-amylase has been developed. Bacillus licheniformis TCRDC-B13 isolated from soil was used for α-amylase production. The α-amylase enzyme of this strain showed excellent stability at high temperatures and over a wide pH range. The low cost medium produced 5 times more enzyme than the high cost synthetic medium (using yeast extract and peptone) in shake flasks. In a 2.6-l fermentor, the enzyme production further doubled.     

Disposable orbitally shaken TubeSpin bioreactor 600 for Sf9 cell cultivation in suspension

Disposable orbitally shaken TubeSpin bioreactor 600 tubes (TS600s) were recently developed for the bench-scale cultivation of animal cells in suspension. Here we compared batch cultures of Sf9 insect cells in TS600s, spinner flasks, and shake flasks. Superior cell growth was observed in TS600s and shake flasks as compared with spinner flasks, and more favorable oxygen-enriched cell culture conditions were observed in TS600s as compared with either spinner or shake flasks. The results demonstrated the suitability of TS600s as a disposable vessel for the cultivation of Sf9 cells in suspension.     

氧化葡萄糖杆菌合成右旋糖酐糊精酶的pH两阶段控制策略

为了进一步提高氧化葡萄糖杆菌右旋糖酐糊精酶的产量,在3 L发酵罐水平上考察了pH(3.5?6.0)对菌体生长和产酶的影响。基于不同pH发酵过程中菌体生长及产物合成的变化,确定了pH两阶段控制策略,即0?6 h时控制pH 5.0,6 h后将pH调至4.0。通过采用这一优化策略,右旋糖酐糊精酶酶活有了较大的提高,可达4.03 U/mL,比不控制pH模式下提高了38.5%,是摇瓶水平的12.5倍,同时发酵时间从47 h缩短为15 h。     

Comparison of Cell Growth and Alkaloid Production of Catharanthus roseus Cells Cultured in Shake Flask and in Bioreactor

The cell growth and alkaloid production of Catharanthus roseus (L.) G. Don cells cultured in the shake flasks with different volumes and in the stirred tank bioreactor (10 L) were compared. Cell dry weight and alkaloid production showed no significant difference in the small volume scale-up shake flasks. When more broths were added to a certain volume in the shake flask, both cell weight and alkaloid production were decreased. The maximum cell dry weight was similar between the cell cultures in the shake flask and the bioreactor, but the alkaloid production of cells was much less in the bioreactor. Gas regime and shear stress were recognized to be the main factors contributing the important effect on alkaloid production during the scale-up processes.     

Nutritional regulation of actinomycin-D production by a new isolate of Streptomyces sindenensis using statistical methods

Production of actinomycin-D, by an isolate, S. sindenensis, was optimized by statistical methods. Fructose peptone and NaNO3 were found to be critical for antibiotic production. In the second step, their concentrations were optimized with Central Composite Design and Response Surface Methodology. Fructose, peptone and NaNO3 at 2.55, 0.309 and 0.114% respectively gave approximately 261% higher yield (289 mg/l). Cultivation in fermentor at 600 rpm agitation and 1.5 vvm aeration with optimized medium gave 3.56 folds higher yield (365 mg/l) as compared to the yields in shake flasks using normal production medium (80 mg/l).     

Effects of cultivation conditions on the production of natamycin with Streptomyces gilvosporeus LK-196

Natamycin is a very attractive antifungal agent with wide applications in medical and food industries. In order to improve the productivity of natamycin, the effects of cultivation conditions were investigated with Streptomyces gilvosporeus LK-196 in the shake flasks and 30-L fermentors. The results showed that dissolved oxygen and shear force would affluence the biosynthesis of natamycin significantly. The high concentration of natamycin (2.03g/L) was achieved under the suitable culture conditions in the shake flask scale. Further investigations in 30-L fermentors showed that the optimal pH was controlled at 6.0 during the whole bioprocess, and the dissolved oxygen level should be more than 30% by adjusting the aeration and agitation rates for high production of natamycin. Under these optimal conditions the high concentration of natamycin (3.94g/L) was achieved with Str. gilvosporeus LK-196 in the 30-L fermentor. Finally, the high-level fermentation process was successfully scaled up to 1000-L fermentors and 18,000-L fermentors in the pilot plant.     

Factors influencing the growth and respiration of rat cerebral astrocytes in primary culture

Cell densities and respiratory rates of astrocytes from neonatal rat brain grown in primary culture were determined after 20–30 days in vitro. Cells grown in flasks reached lower densities (g DNA/cm²) and higher protein: DNA ratios than cells grown in petri dishes. Respiratory rates were lower for cells grown in flasks compared to cells grown in dishes. The pH of the medium in flasks fell below 6.9 between feedings while the pH of the medium in dishes remained at about 7.2. Cells grown in dishes with the medium pH adjusted to 6.8 also showed lower final cell densities, higher protein: DNA ratios, and lower respiratory rates, compared to cells grown under similar conditions at pH 7.5. Intermediate values of each parameter were found in cells grown at pH 7.5 for one week and then at 6.8 for 20 days. We conclude that the effects of ambient pH account for the differences in growth characteristics and respiratory rates of astrocytes grown in dishes versus those grown in flasks.     

Variation of oxygen requirement with plasmid size in recombinant Escherichia coli

We have previously found an inverse relationship between certain cell growth parameters and plasmid size for a series of recombinant Escherichia coli strains containing pUC8 or one of a series of pUC8 recombinant derivatives. To extend these results we investigated whether there was a similar variation among our strains in oxygen requirement, which might be related to the differences in growth. During logarithmic growth in shake flasks, oxygen uptake by E. coli strain JM103 containing an 8.7-kb pUC8 derivative (pBS5) was 2.5 times that of JM103 harboring pUC8 (2.7 kb) and 7.5 times that of plasmid-free JM103. Supplementing the medium with acetate eliminated both the growth disadvantage of and the increased oxygen uptake by the strain harboring pBS5 compared with that containing pUC8. In all cases oxygen consumption decreased drastically as cells began and then continued into stationary phase, and no significant difference was seen among the three strains at these times. When the three strains were grown in a fermentor with continuous monitoring of oxygen levels, plasmid-free JM103 outgrew JM103 containing pUC8 or pBS5 at three levels of aeration. The latter two strains grew identically when aeration was high; their growth curves diverged, however, when aeration was low. In the fermentor experiments the point at which the growth of the three strains diverged was coincident with the point of oxygen depletion in the cultures.