• 제목/요약/키워드: fermentation medium

검색결과 861건 처리시간 0.029초

Effect of Abiotic Factors on Fumosorinone Production from Cordyceps fumosorosea via Solid-State Fermentation

  • Tahir Khan;Dong-Hai Hou;Jin-Na Zhou;Yin-Long Yang;Hong Yu
    • Mycobiology
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    • 제51권3호
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    • pp.157-163
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    • 2023
  • Cordyceps fumosorosea is an important species in the genus of Cordyceps, containing a variety of bioactive compounds, including fumosorinone (FU). This study was a ground-breaking assessment of FU levels in liquid and solid cultures. The present study focused on the impacts of solid-state fermentation (SSF) using solid substrates (wheat, oat, and rice), as well as the effects of fermentation parameters (pH, temperature, and incubation period), on the generation of FU. All the fermentation parameters had significant effects on the synthesis of FU. In a study of 25 ℃, 5.5 pH, and 21 days of incubation period combinations calculated -to give maximal FU production, it was found that the optimal values were 25 ℃, 5.5 pH, and 21 days, respectively. In a solid substrate medium culture, FU could be produced from SSF. At 30 days, a medium composed of rice yielded the most FU (798.50 mg/L), followed by a medium composed of wheat and oats (640.50 and 450.50 mg/L), respectively. An efficient method for increasing FU production on a large scale could be found in this approach. The results of this study might have multiple applications in different industrial fermentation processes.

Lactobacillus sporgenes에 의한 젖산칼슘 생산 II. 젖산 칼슘 제조 (The Production of Calcium Lactate by Lactobacillus sporogenes II. Production of Calcium Lactate)

  • 이계근;김영만;민경찬
    • 한국식품영양학회지
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    • 제1권2호
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    • pp.102-107
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    • 1988
  • Production of calcium lactate very useful for medical supplies of Ca-therapy was obtained by lactic acid fermentation of lactobacillus sporogenes, a spore forming lactic acid bacterium. Corn steep liquor 1%, soybean enzyme hydrolysate 3%, yeast extract powder 2% can substitute for yeast extract and peptone as nutrient sort traces in fermentation medium using 10% glucose concentration. In the calcium lactate production medium containing yeast extract powder 2%, glucose 18%, CaCO3 12%, the lactic acid fermentation was carried out at 45$^{\circ}C$ for 4days with continuous agitation of 100 rpm. As results, fermentation yield was 97.5%. The five steps such as protein coagulation, decolorizing evaporating, crystallizing, and drying were carried out to harvest calcium lactate from 10l of supernatant of fermented medium to be removed cell and CaCO3. As results, 2065.0g of white crystal calcium lactate dihyrate was recovered and a yield of 84.9% was obtained.

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Medium optimization for keratinase production by a local Streptomyces sp. NRC 13S under solid state fermentation

  • Shata, Hoda Mohamed Abdel Halim;Farid, Mohamed Abdel Fattah
    • Journal of Applied Biological Chemistry
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    • 제56권2호
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    • pp.119-129
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    • 2013
  • Thirteen different Streptomyces isolates were evaluated for their ability to produce keratinase using chicken feather as a sole carbon and nitrogen sources under solid state fermentation (SSF). Streptomyces sp. NRC 13S produced the highest keratinase activity [1,792 U/g fermented substrate (fs)]. The phenotypic characterization and analysis of 16S rDNA sequencing of the isolate were studied. Optimization of SSF medium for keratinase production by the local isolate, Streptomyces sp. NRC13S, was carried out using the one-variable-at-a-time and the statistical approaches. In the first optimization step, the effect of incubation period, initial moisture content, initial pH value of the fermentation medium, and supplementation of some agro-industrial by-products on keratinase production were evaluated. The strain produced about 2,310 U/gfs when it grew on chicken feather with moisture content of 75% (w/w), feather: fodder yeast ratio of 70:30 (w/w), and initial pH 7 using phosphate buffer after 8 days. Based on these results, the Box-Behnken design and response surface methodology were applied to find out the optimal conditions for the enzyme production. The corresponding maximal production of keratinase was about 2,569.38 U/gfs.

맥주발효 폐액을 이용한 미생물 셀룰로오스 생산 (Production of Bacterial Cellulose Using Waste of Beer Fermentation Broth)

  • 박중곤;현승훈;안원술
    • Korean Chemical Engineering Research
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    • 제44권1호
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    • pp.52-57
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    • 2006
  • 에탄올과 함께 탄소, 질소원을 함유한 맥주 폐 발효액을 저렴한 대체배지로 사용하고 Gluconacetobacter hansenii PJK(KCTC 10505 BP) 균주를 이용하여 미생물셀룰로오스를 생산하였다. 맥주 폐 발효액은 기본배지보다도 탄소원과 질소원이 풍부하였으며 미량의 황과 4% 이상의 에탄올을 함유하였다. 진탕배양에서 맥주 폐 발효액을 사용하여 생산된 셀룰로오스량은 기본배지를 사용하여 생산된 셀룰로오스량과 필적하였다. 교반배양에서는 셀룰로오스 생산균주($Cel^+$ 균주)가 셀룰로오스를 생산하지 못하는 균주($Cel^-$ 돌연변이주)로 전환되는 률은 낮았지만 셀룰로오스 생산량은 감소하였다.

응집성 효모를 이용한 연속 알코올 발효 (Continuous Alcohol Fermentation by a Flocculating Yeast)

  • 남기두;이인기;조훈호
    • 한국미생물·생명공학회지
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    • 제19권5호
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    • pp.487-490
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    • 1991
  • 효모 재순환계에 의한 당밀의 연속발효를 하였다. 단계적으로 YPD배지 농도를 10g/l에서 183.5g/l로 증가시킨 후 최종 발효배지는 당밀로 하였다. 최고의 효모농도는 25g/l였고, 운전중 평균 효모농도는 23.5g/l으로 종래 회분식보다 3.4배 높았다. 최적 발효조건은 180g/l의 당밀배지를 공급하였을 때 교반속도 500rpm, 희석을 0.037$h^{-1}$였다. 이 조건을 645시간 연속 운전하였으며 최고 알코올 생산성은 4.9g$l\cdot h$로서 이때의 희석율은 0.091$h^{-1}$, 알코올 농도는 53.9g/l이었다.

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Factors affecting the final antibiotic titer of sisomicin fermentation

  • 이상한;김성욱;신철수
    • 한국미생물생명공학회:학술대회논문집
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    • 한국미생물생명공학회 1986년도 추계학술대회
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    • pp.514.2-514
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    • 1986
  • Since sisomicin which is produced by Micromonospora inyoensis is an intracellular antibiotic, the final antibiotic titer to be attained depends singnificantly on the cell mass in fermentation broth. Cobalt ion in medium was indispensable for getting a high antibiotic titer. However, in the presence of cobalt ion in medium, the antibiotic production proceeded up to about 4 days and thereafter stopped. From the experiments on theaddition of cobalt ion to culture medium, it was shown that the antibiotic production stopped due to the other physiological properties of cells rather than the accumulation of antibiotic in cells.

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Ethanol Fermentation in Lactose Medium Using a Fusant Strain of Saccharomyces cerevisiae and Kluyveromyces fragilis

  • Lee, Chu-Hee;Yang, Sun-A;Rho, Ju-Won;Lee, Seung-Yup
    • Journal of Microbiology and Biotechnology
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    • 제2권2호
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    • pp.108-114
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    • 1992
  • The fermentative characteristics in ethanol production from lactose, with increased ethanol tolerance, of a fusant yeast strain constructed by protoplast fusion of Saccharomyces cerevisiae and Kluyveromyces fragilis were studied. The ethanol tolerance of this strain was increased to 8.0%, compared with the parent K. fragilis. During batch ethanol fermentation the optimal cultivation conditions for this fusant yeast were an initial pH of 4.5, a culture temperature $30^\circ{C}$. stirring at 100 rpm without aeration in 10% lactose medium (supplied with 1.0% yeast extract). Using this fusant strain in whey fermentation to ethanol, maximum ethanol production reached 3.41% (w/v) (theoretical yield; 66.7%) after a 48 hour cultivation period.

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Streptomyces peucetius subsp. caesius와 S. platensis사이의 원형질체 융합균주의 발효특성 (The Fermentation Characteristics of the Interspecific Protoplast Fusant of S. peucetius and S. platensis)

  • 임미송;이강만
    • 약학회지
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    • 제38권6호
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    • pp.749-755
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    • 1994
  • An interspecific fusant strain, Streptomyces MS1 was obtained by protoplast fusion between S. peucetius subsp. caesius and S. platensis. We studied on the fermentation characteristics of the fusant strain. The fermentation products of the fusant MS1 was identical with S. peucetius, but its production of anthracycline was more stable than S. peucetius under various fermentation conditions in regard to acidogenesis of fermentation broth. The optimal medium composition for anthracycline production by fusant MS1 as follows: sucrose 2.0%, glucose 1.0%, soytone 0.7%, $CaCO_3$ 0.2%, $KH_2PO_4$ 0.013%, casamino acids 0.01%, $K_2SO_4$ 0.025%, $MaCl_2\;6H_2O$ 1.024%, 5M $CaCl_2\;5H_2O$ 0.4%, 1N NaOH 0.7%, 20% L-proline 1.5%. In this condition, the productivity of anthracycline was $80{\sim}100\;{\mu}g/ml$.

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Propionibacterium shermanii에 의한 비타민 $B_{12}$의 생성에 영향을 미치는 배지첨가물들에 대한 연구 (Study on the Effects of Supplemented Factors on the Production of Vitamin $B_{12}$ by Propionibacterium shermanii)

  • 김지영;김공환;김경자;구양모
    • 약학회지
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    • 제38권5호
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    • pp.614-620
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    • 1994
  • Following the study on the fermentation conditions influencing the production of vitamin $B_{12}$ by Propionibacterium shermanii(Korean J Biotechnol. Bioeng. 7,126-131, 1992), the effects of some factors supplemented in the medium on the production of vitamin $B_{12}$ were studied. Maximum production of vitamin $B_{12}$ was observed when $Co^{+2}$ was supplemented at the concentration of 2-4 ppm in the fermentation medium. Increase of the supplemented $Co^{+2}$ to 12 ppm did not inhibit the growth of the organism, but it accelerated the lysis of the organism. In the literature, peptone was reported to activate the biosynthesis of vitamin $B_{12}$. Examination of the effect of peptone on the growth and the production of vitamin $B_{12}$ showed that at early stage more vitamin$B_{12}$ was observed in the supplemented medium, but no difference was observed in the later stage of fermentation. Examination of the time for addition and the amount of 5,6-dimethylbenzimidazole, a precursor known to influence the production of vitamin $B_{12}$, showed that a maximum yield of vitamin $B_{12}$ was observed when 15 mg/L was added to the fermentation medium after 2 days' incubation. The effect was comparable with the increase of the production of vitamin $B_{12}$ when the fermentation condition was changed to aerobic condition after 2 days' culture under anaerobic condition.

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Fed-Batch Sorbose Fermentation Using Pulse and Multiple Feeding Strategies for Productivity Improvement

  • Giridhar, R.;Srivastava, A.K.
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제5권5호
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    • pp.340-344
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    • 2000
  • Microbial oxidation of D-sorbitol to L-sorbose by Acetobacter suboxydans is of commercial importance since it is the only biochemical process in vitamin C synthesis. The main bottleneck in the batch oxidation of sorbitol to sorbose is that the process is severely inhibited by sorbitol. Suitable fed-batch fermentation designs can eliminate the inherent substrate inhibition and improve sorbose productivity. Fed-batch sorbose fermentations were conducted by using two nutrient feeding strategies. For fed-batch fermentation with pulse feeding, highly concentrated sorbitor (600g/L) along with other nutrients were fed intermittently in four pulses of 0.5 liter in response to the increased DO signal. The fed-batch fermentation was over in 24h with a sorbose productivity of 13.40g/L/h and a final sorbose concentration of 320.48g/L. On the other hand, in fed-batch fermentation with multiple feeds, two pulse feeds of 0.5 liter nutrient medium containing 600g/L sorbitol was followed by the addition of 1.5 liter nutrient medium containing 600g/L sorbitol at a constant feed rate of 0.36L/h till the full working capacity of the reactor. The fermentation was completed in 24h with an enhanced sorbose productivity of 15.09g/L/h and a sorbose concentration of 332.60g/L. The sorbose concentration and productivity obtained by multiple feeding of nutrients was found to be higher than that obtained by pulse feeding and was therefore a better strategy for fed-batch sorbose fermentation.

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