• Title/Summary/Keyword: Jar fermentor

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Optimization of Environmental Conditions for Hirudin Production from Recombinant Saccharomyces cerevisiae (재조합 효모를 이용한 Hirudin 발효생산조건의 최적화)

  • 이동훈;서진호
    • KSBB Journal
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    • v.9 no.1
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    • pp.8-15
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    • 1994
  • The research has been carried out to optimize a recombinant S. cerevisine fermentation process for the production of an anticoagulant hirudin. The structural gene coding for hirudin was combined with the GAL10 promoter for controlled expression, the MFal signal sequence for hirudin secretion, and the GAL7 terminator for transcriptional termination. Growth medium composition and environmental conditions were optimized for maximizing cell growth and final hirudin concentration. The optimized conditions included yeast extract 40g/$\ell$, casamino acid 5g/$\ell$, g1ucose 20g/$\ell$, galactose 30g/$\ell$, DO 50% and temperature $30^{\circ}C$. These conditions yielded the specific cell growth rate of $0.13hr^{-1}$, the final cell density of 30g cell/$\ell$ and the final hirudin concentration of 64mg/$\ell$ in the batch fermentation with a 2.5$\ell$ jar fermentor.

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Optimal Conditions for the Production of Exopolysaccharide by Marine Microoranism Hahella chejebsis

  • Ko, Sung-Hwan;Lee, Hyun-Sang;Park, Shin hye;Lee, Hong-Kum
    • Biotechnology and Bioprocess Engineering:BBE
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    • v.5 no.3
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    • pp.181-185
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    • 2000
  • A marine microorganism, strain 96CJ10356 produced exopolysaccharide, designated as EPS-R. To optimize culmize culture conditions for the production of EPS-R, carbon and nitrogen sources, mineral salts, temperature, and pH were exmined. From this study, STN medium for the production of EPS-R was suggested as follows; sucrose 20g, typtone 10g, NaCl 10g, MgSO45g, CaCl21g, KH2PO4 76mg, K2HPO4 83mg, FeCl2 5mg, MnCl2 1mg, NaMoO4 1mg, and ZnCl2 1mg per liter at pH 7.0. About 9.23g/L of EPS-R was obtained from STN medium after cultivation for 120h at $25^{\circ}C$ in a 5-liter jar fermentor with an aearation rate of 0.17 vvm. Apparent viscosity and flocculation activity of the culture broth were increased with the production of EPS-R and the maximal values were 415 cP and 1400 unit/mL against 0.5% activated carbon, respectively.

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Optimum Culture Conditions for the Production of Fructosyl transferase by Aureobasidium pullulans C-23 (Aureobasidium pullulans C-23 균주에 의한 Fructosyl Transferase의 생산 최적 배양조건)

  • 조원태;임재윤
    • Microbiology and Biotechnology Letters
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    • v.18 no.4
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    • pp.417-422
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    • 1990
  • For optimal production of fructosyl transferase in AureobasidiumpuZZulane C-23, the effect of fermentation conditions for cell growth and fructosyl transferase production were investigated. Sucrose was excellent carbon source. Sucrose concentration for the optimum production of fructosyl transferase was 35%. Enzyme productivity was significantly increased by addition of ammonium oxalate and yeast extract. A time course study for the enzyme production by Aureobasidium pullutans C-23 was carried out. At 2 days incubation, the production of intracellular enzyme was maximum. The extracellular enzyme production was found to be increased up to 6 days.

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Optimization of Culture Conditions for D-Ribose Production by Transketolase-Deficient Bacillus subtilis JY1

  • Park, Yong-Cheol;Seo, Jin-Ho
    • Journal of Microbiology and Biotechnology
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    • v.14 no.4
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    • pp.665-672
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    • 2004
  • D-Ribose is a five-carbon sugar used for the commercial synthesis of riboflavin, antiviral agents, and flavor enhancers. Batch fermentations with transketolase-deficient B. subtilis JY1 were carried out to optimize the production of D-ribose from xylose. The best results for the fermentation were obtained with a temperature of $37^{\circ}C$ and an initial pH of 7.0. Among various sugars and sugar alcohols tested, glucose and sucrose were found to be the most effective for both cell growth and D-ribose production. The addition of 15 g/l xylose and 15 g/l glucose improved the fermentation performance, presumably due to the adequate supply of ATP in the xylose metabolism from D-xylulose to D-xylulose-5-phosphate. A batch culture in a 3.7-1 jar fermentor with 14.9 g/l xylose and 13.1 g/l glucose resulted in 10.1 g/l D-ribose concentration with a yield of 0.62 g D-ribose/g sugar consumed, and 0.25 g/l-h of productivity. Furthermore, the sugar utilization profile, indicating the simultaneous consumption of xylose and glucose, and respiratory parameters for the glucose and sucrose media suggested that the transketolase-deficient B. subtilis JY1 lost the glucose-specific enzyme II of the phosphoenolpyruvate transferase system.

A New Thermophile Strain of Geobacillus thermodenitrificans Having L- Arabinose Isomerase Activity for Tagatose Production

  • Baek, Dae-Heoun;Lee, Yu-Jin;Sin, Hong-Sig;Oh, Deok-Kun
    • Journal of Microbiology and Biotechnology
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    • v.14 no.2
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    • pp.312-316
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    • 2004
  • Five strains, producing bacterial thermostable L-arabinose isomerase, were isolated from Korean soil samples obtained from compost under high temperature circumstances. Among these strains, the CBG-Al showed the highest L-arabinose isomerase activity at $60^\circ{C}$ and was selected as a D-tagatose producing strain from D-galactose. This strain was identified as Geobacillus thermodenitrificans based on the 16S rRNA analysis, and biological and biochemical characteristics. The isolated strain was aerobic, rod-shaped, Gram-positive, nonmotile, and an endospore-forming bacterium. No growth was detected in culture temperature below $40^\circ{C}$. The maximum growth temperature and maximum temperature of enzyme activity were $75^\circ{C}$ and $65^\circ{C}$, respectively. In metal ion effects, $Ca^{2+}$ was the most effective enzyme activator with the reaction rate by 150%. In a 5-1 jar fermentor with 3-1 MY medium, L-arabinose isomerase activity was growth-associated and pH decreased rapidly after the initial logarithmic phase.

Taxonobic Characteristics of Strain Producing MR-387A and B,New Inhibitors of Aminopeptidase M,and their Production (신규의 Aminopeptidase M 저해제 MR-387A와 B를 생산하는 균주의 동정 및 저해제의 생산)

  • Chung, Myung-Chul;Chun, Hyo-Kon;Lee, Ho-Jae;Kho, Yung-Hee
    • Microbiology and Biotechnology Letters
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    • v.22 no.5
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    • pp.447-452
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    • 1994
  • The strain SL-387 which produces new inhibitors of aminopeptidase M, MR-387A and B, was isolated from a soil sample. The strain has branched substrate mycelia, from which aerial hyphae develop in the form of open spirals. Spore surface is smooth. Melanoid and soluble pigme- nts were observed. The isolate contains LL-diaminopimelic acid in its cell wall hydrolysate, and has no pectinolytic activity. The strain SL-387 is closely related to Streptomyces griseoruber and S. naganishii, but is different from these strains in some cultural and physiological characteristics. This strain was, therefore, designated as Streptomyces sp. SL-387. The effects of several carbon and nitrogen sources on the production of the inhibitor were examined. Among them, glucose, galactose, mannose, and xylose were effective as a carbon source and soybean meal, soytone, fish meal, and gluten meal were effective as a nitrogen source. The maximum peak of the inhibitor production in jar fermentor was obtained on the fifth day of culture.

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Improved Production, and Purification of Aclacinomycin A from Streptomyces lavendofoliae DKRS

  • Kim, Wan-Seop;Youn, Deok-Joong;Cho, Won-Tae;Kim, Myung-Kuk;Kim, Hak-Ryul;Rhee, Sang-Ki;Choi, Eui-Sung
    • Journal of Microbiology and Biotechnology
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    • v.5 no.5
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    • pp.297-301
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    • 1995
  • An anthracycline antibiotic, aclacinomycin A (aclarubicin), was produced from a mutant strain of Streptomyces lavendofoliae. The mutant strain which showed a 4-fold higher productivity of aclacinomycin A compared with the parent strain was also found to produce a significantly higher amount of aclacinomycin A than the reported production strain, Streptomyces galilaeus. The aclacinomycin A was produced up to 125 mg/l using potato starch and soybean meal as carbon and nitrogen sources, respectively, on a 3 liter scale fermentation in a 5 liter jar fermentor. The mutant strain also produced significant amount of aclacinomycins Band Y. Aclacinomycin A was isolated from the culture broth by solvent extractions and further purified by silica gel column chromatography. The yield of aclacinomycin A with over 99$%$ purity was found to be over 60$%$ starting from 3 liters of culture broth.

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Cellular Lipid Formation by Petroleum Hydrocarbon Fermentation (石油炭化水素 醱酵에 의한 脂質의 生成)

  • Park Tai Won;Suh Hyung Joon
    • Journal of the Korean Chemical Society
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    • v.21 no.6
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    • pp.449-452
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    • 1977
  • The effect of carbon number of hydrocarbon used as a carbon source in the production of cellular lipid of Rhodotorula sp. and its fatty acid composition were investigated. Using Rhodotorula sp. on n-tetradecane and n-hexadecane whose carbon numbers are even, fermentation was carried out in a jar fermentor of 2 liter-capacity at $28^{\circ}C$, with pH range of 4.0∼4.6 and at oxygen flowing rate of 0. 4 vvm and agitation velocity of 1000 rpm. Drying the produced cell after completion of fermentation, cellular lipid was extracted from the cell using soxhlet extractor and examined its fatty acid composition by gas-liquid chromatography. Cellular lipid content in the cell produced on n-tetradecane and n-hexadecane were 12.0 % and 25,8 % on the basis of dry cell weight, respectively and their fatty acids were mostly even numbered in carbon number.

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Submerged Culture of Phellinus linteus for Mass Production of Polysaccharides

  • Lee, June-Woo;Baek, Seong-Jin;Kim, Yong-Seok
    • Mycobiology
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    • v.36 no.3
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    • pp.178-182
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    • 2008
  • In order to increase the mycelial production of Phellinus linteus, which exhibits potent anticancer activity, some ingredients of the medium used to culture P. linteus were investigated. The optimal medium composition for the production of Phellinus linteus was determined to be as follows: fructose, 40 g/l; yeast extract, 20 g/l; $K_2HPO_4$, 0.46 g/l; $K_2HPO_4$, 1.00 g/l; M$MgSO_4\cdot7H_2SO$, 0.50 g/l; $FeCl_2\cdot6_2O$, 0.01 g/l; $MnCl_2\cdot4H_2O$, 0.036 g/l; $ZnCl_2$, 0.03 g/l; and $SuSO_4\cdot7H_2O$, 0.005 g/l. The optimal culture conditions were determined to be as follows: temperature, 28$^{\circ}C$; initial pH, 5.5; aeration, 0.6 vvm; and agitation, 100 rpm, respectively. Under optimal composition and conditions, the maximum mycelial biomass achieved in a 5 l jar fermentor was 29.9 g/l.

Optimization of Large Scale Culture Conditions of Bacillus ehimensis YJ-37 Antagonistic to Vegetables Damping-off Fungi (채소류 모잘록병균에 길항하는 Bacillus ehimensis YJ-37의 대량배양 최적조건)

  • 주길재;김진호
    • Journal of Life Science
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    • v.12 no.3
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    • pp.242-249
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    • 2002
  • The optimal culture conditions in 500$m\ell$ flask suture, 5$\ell$ jar fermenter and 2,000 $\ell$ large stale culture were investigated to maximize the production of antibiotic on Rhizoctonia solani AC4, the causal agent of vegetables damping-off, by the strain Bacillus ehimensis YJ-37. Starch (1.5%) as a carbon source, peptone (0.6%) as a nitrogen source and MgC1$_2$(0.15%) as a metal ion in the medium containing N $a_2$HP $O_4$(0.3%) showed the highest production of the antibiotic(s) in a rotary shake (200 rpm). Optimal initial pH of the culture medium, culture temperature and culture time for the antibiotic(s) production were pH 8.0, 32$^{\circ}C$ and 54hrs, respertively. Under the optimal renditions in flask culture, cell growth and antifungal activity (clear zone size) were 1.42 $\times$ 10$^{8}$ cfu/$m\ell$ (21g-DCW/ $\ell$) and 13.9 mm, respectively. In 5 $\ell$ jar fermenter (medium 3 $\ell$), optimal air flow, agitation speed and culture time for the antibiotic(s) production were 2 vvm, 200 rpm and 48hrs, respectively. Under the optimal conditions in 5 $\ell$ jar fermenter, tell growth and antifungal activity were 2.06 $\times$ 10$^{8}$ cfu/$m\ell$ (30g-DCW/ $\ell$) and 13.4 mm, respectively. Under the culture conditions of air flow (30 vvm) and agitation speed (200 rpm) at 32$^{\circ}C$ for 10 days in 2,000 $\ell$ large scale culture (medium 1,800 $\ell$, pH 8.0), cell growth and antifungal activity were 0.81$\times$10$^{8}$ cfu/$m\ell$ (12g-DCW/ $\ell$) and 8.6 mm, respectively.