• Title/Summary/Keyword: Fermentation conditions

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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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    • v.56 no.2
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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.

Studies on the production of Vinegar from Koryangju Distillers′ Grain (고량주박초 제조에 관한 연구)

  • 김해중;조재선
    • Microbiology and Biotechnology Letters
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    • v.9 no.4
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    • pp.191-196
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    • 1981
  • In order to utilize the Koryangju distillers' grain for the acetic acid fermentation, the extracting methods and effects of the extracts on the fermentations were investigated. The result obtained are as follows. 1. Cold extracting method by which the distillers grain is extracted with 3 times of water for 60 hours at room temperature was better than hot extracting method in terms of the fermentation rate and the quality of vinegar product. 2. Optimum conditions and some results of surface fermentation based on the medium added by the extracts are as follows, optimum amount of the extracts to be added to the medium is 20-30% of total media; acetic acid production rate at log phase was 0.16g/100$m\ell$, hr.; recovery was 91.17%; and the time of 40 hours was required for the completion of fermentation. 3. Organoleptic quality of the vinegar which is produced by adding the extracts was superior to two commercial products examined.

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고정상세포분리기의 개발 및 Cyclosporin A 생산을 위한 고정화 연속배양공정에의 적용

  • Lee, Tae-Ho;Park, Sung-Kwan;Chang, Yong-Keun;Chun, Gie-Taek
    • Microbiology and Biotechnology Letters
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    • v.24 no.6
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    • pp.717-725
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    • 1996
  • We have developed an efficient immobilized cell separator for continuous operation of immobilized fungal cell cultures, and applied this separator to actual fermentation process for the production of cyclosporin A (CyA), a powerful immunosuppressant. In the experiments employing highly viscous polymer (carboxymethyl cellulose) solution, the decantor showed good separating performances at high solution viscosites and fast dilution rates. Air duct and cylindrical separator installed inside the decantor turned out to play key roles for the efficient separation of the immobilized cells. By installing the decantor in an immobilized perfusion reactor system (IPRS), continuous immobilized culture was stably carried out even at high dilution rate for a long period, leading to high productivities of free cells and CyA. Almost no immobilized biomass existed in effuluent stream of the IPRS, demonstrating the effectiveness of the decan- tor system for a long-term continuous fermentation. It was noteworthy that we could obtain these results despite of the unfavorable fermentation conditions, i.e., reduced density of the biosupports caused by overgrowth of cells inside the bead particles and existence of high density of suspended fungal cells (10g/l) in the fermentation broth.

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Highly Time-Resolved Metabolic Reprogramming toward Differential Levels of Phosphate in Chlamydomonas reinhardtii

  • Jang, Cheol-Ho;Lee, Gayeon;Park, Yong-Cheol;Kim, Kyoung Heon;Lee, Do Yup
    • Journal of Microbiology and Biotechnology
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    • v.27 no.6
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    • pp.1150-1156
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    • 2017
  • Understanding phosphorus metabolism in photosynthetic organisms is important as it is closely associated with enhanced crop productivity and pollution management for natural ecosystems (e.g., algal blooming). Accordingly, we exploited highly time-resolved metabolic responses to different levels of phosphate deprivation in Chlamydomonas reinhardtii, a photosynthetic model organism. We conducted non-targeted primary metabolite profiling using gas-chromatography time-of-flight mass spectrometric analysis. Primarily, we systematically identified main contributors to degree-wise responses corresponding to the levels of phosphate deprivation. Additionally, we systematically characterized the metabolite sets specific to different phosphate conditions and their interactions with culture time. Among them were various types of fatty acids that were most dynamically modulated by the phosphate availability and culture time in addition to phosphorylated compounds.

INFLUENCE OF DIRECT-FED MICROBIALS ON RUMINAL MICROBIAL FERMENTATION AND PERFORMANCE OF RUMINANTS: A REVIEW

  • Yoon, I.K.;Stern, M.D.
    • Asian-Australasian Journal of Animal Sciences
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    • v.8 no.6
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    • pp.533-555
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    • 1995
  • Direct-fed microbials (DFM) have been used to enhance milk production in lactating cattle and to increase feed efficiency and body weight gain in growing ruminants. Primary microorganisms that have been used as DFM for ruminants are fungal cultures including Aspergillus oryzae and Saccharomyces cerevisiae and lactic acid bacteria such as Lactobacillus or Streptococcus. Attempts have been made to determine the basic mechanisms describing beneficial effects of DFM supplements. Various modes of action for DFM have been suggested including : stimulation of ruminal microbial growth, stabilization of ruminal pH, changes in ruminal microbial fermentation pattern, increases in digestibility of nutrients ingested, greater nutrient flow to the small intestine, greater nutrient retention and alleviation of stress, however, these responses have not been observed consistently. Variations in microbial supplements, dosage level, production level and age of the animal, diet and environmental condition or various combinations of the above may partially explain the inconsistencies in response. This review summarizes production responses that have been observed under various conditions with supplemental DFM and also corresponding modification of ruminal fermentation and other changes in the gastrointestinal tract of ruminant animals.

Changes in Chemical Components of Chungkugiang Prepared with Small Black Bean (소립검정콩 청국장의 화학성분 변화)

  • 손미예;권선화;성찬기;박석규;최상도
    • Journal of Life Science
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    • v.11 no.3
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    • pp.284-290
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    • 2001
  • Changes in chemical components of small black bean chungkugjang(SBBC) added with kiwi and radish as foodstuffs to repress off-odor and enhance the quality of SBBC suring fermentation were investigated. Optimal pretreatment conditions of small black bean suitable to the fermentation of chungkugjang were 3 hrs of soaking time 1.5 times of ratio of water to black bean. 1.0 atm of high pressure, 20 min of heating time, cutting and crushing of heat-treated black bean. Moisture content of SBBC was remarkably lower than that of soybean chungkugjang(SBC) as control. Crude protein of SBBC was in the range 23.37∼25.71% and higher than that of SBC, Crude lipid of SBBC was lower than that of SBC. Crude lipid of SBBC added with kiwi and radish paste was decreased than that of SBBC without two foodstuffs. pH of SBBC were rapidly increased to 24 hrs of fermentation and gradually increased thereafter. Total acidity was shown to be reversely decreased as compared to pH tendency. Reducing sugar was increased to 24 hrs of fermentation and then decreased. In SBBC and SBC, potassium was the most abundant followed by phosphorus, magnesium and calcium.

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Continuous Ethanol Fermentation Using Starchy Raw Material in Pilot Scale Multi-stage CSTR (Pilot Scal Multi-stage CSTR에서 전분질 원료의 연속 에탄올발효)

  • 남기두;이인기;조훈호;최명호;김운식
    • Microbiology and Biotechnology Letters
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    • v.20 no.3
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    • pp.324-328
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    • 1992
  • In order to develop more economic processes, continuous ethanol fermentation from starchy raw materials in a pilot scale multi-stage CSTR was investigated. Ethanol fermentation could be successfully operated for 30 days with naked barley and 60 days with cassava, respectively. Starchy raw materials used for this study were ground and passed through a 20-mesh sieve for low temperature cooking. Under the optimized conditions, the overall productivity of cassava was $1.27g/{\ell}{\cdot}h$ with an ethanol concentration of 9.51% (v/v), which was higher about 2 times than that obtained from a conventional batch system in industrial scale.

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Succinic Acid Production by Continuous Fermentation Process Using Mannheimia succiniciproducens LPK7

  • Oh, In-Jae;Lee, Hye-Won;Park, Chul-Hwan;Lee, Sang-Yup;Lee, Jin-Won
    • Journal of Microbiology and Biotechnology
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    • v.18 no.5
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    • pp.908-912
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    • 2008
  • To achieve a higher succinic acid productivity and evaluate the industrial applicability, this study used Mannheimia succiniciproducens LPK7 (knock-out: ldhA, pflB, pta-ackA), which was recently designed to enhance the productivity of succinic acid and reduce by-product secretion. Anaerobic continuous fermentation of Mannheimia succiniciproducens LPK7 was carried out at different glucose feed concentrations and dilution rates. After extensive fermentation experiments, a succinic acid yield and productivity of 0.38 mol/mol and 1.77 g/l/h, respectively, were achieved with a glucose feed concentration of 18.0 g/l and $0.2\;h^{-1}$ dilution rate. A similar amount of succinic acid production was also produced in batch culture experiments. Therefore, these optimal conditions can be industrially applied for the continuous production of succinic acid. To examine the quantitative balance of the metabolism, a flux distribution analysis was also performed using the metabolic network model of glycolysis and the pentose phosphate pathway.

Screening of Thermotolerant Yeast Strain for Ethanol Fermentation (Ethanol 발효를 위한 내열성 효모 균주의 Screening)

  • Ryu, Beung-Ho;Nam, Ki-Du;Kim, Hae-Sung;Kim, Dong-Seuk;Ji, Young-Ae;Jung, Soo-Ja
    • Microbiology and Biotechnology Letters
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    • v.16 no.4
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    • pp.265-269
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    • 1988
  • For the purpose of developing new thermotolerant yeast strains for ethanol fermentation, yeasts were isolated from molasses and screened for their fermentation ability at elevated temperatures. Three candidate strains were screened. These strains preferred pH 5.0 and 34$^{\circ}C$ for their ethanol production. Under such conditions the three strains showed average ethanol productivity of 75g ethanol per liter of fermentation broth in n synthetic medium containing glucose as substrate. These strains were identified as Saccharomyces cerevisiae and Kluveromyces marxianus.

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전분당 부산물로부터 유기산 생산 및 농축에 관한 연구 : 1. 유기산 균주 Propionibacterium acidipropionici의 발효 특성

  • Jin, Seon-Ja;Choe, Cheol-Ho;Ju, Yun-Sang;Lee, Ui-Sang
    • 한국생물공학회:학술대회논문집
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    • 2000.04a
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    • pp.129-132
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    • 2000
  • The main objectives of the study were to find optimum fermentation conditions of Propionibacterium acidipropionici for the production of organic acids. Three strains of Propionibacterium acidipropionici were selected for batch fermentation. Nutrients and environmental conditions on cell growth were defined by series of experiments. The optimum conditions of peptone, yeast extract, pH were determined to be 1.5%, 0.75%, $5.5{\sim}7.5$, respectively. Among the straines of P. acidipropionici selected for the experiment, ATCC4965 was the best in terms of total productivity and cell yield, which values were 0.29g total acids/L/h and 0.26 g dry cell/g glucose, respectively.

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