• 제목/요약/키워드: fed-batch system

검색결과 83건 처리시간 0.022초

Optimization of Medium Composition for Growth of Leuconostoc mesenteroides

  • 김현;엄현주;서동미;한남수
    • 한국생물공학회:학술대회논문집
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    • 한국생물공학회 2003년도 생물공학의 동향(XII)
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    • pp.153-156
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    • 2003
  • The MRS medium is widely used as an optimized medium for the growth of Lactobacillus spp. and also used for the growth of Leuconostoc spp. Leuconostoc mesenteroides shows quite different physicochemical properties compared to Lactobacilli spp. and it is one of the major strain of kimchi fermenting microorganisms with its usefulness in our traditional foods and availability in biotechnology in the future, specifically tailor-made medium is necessary for the growth of Leuconostoc mesenteroides. Sequential experimental designs (Plackett-Burman, fractional factorial, steepest ascent, central composite design and response surface methodology) were introduced to optimize and improve the Leuconostoc medium. Fifteen medium ingredients were investigated and fructose, sodium acetate and ammonium citrate were determined to give a critical and positive effect for cell-growth. The yield of biomass using the optimal medium was improved more than that of the MRS medium and the result of fed-batch culture showed the capability of the improvement in cell mass similar to the E.coli system.

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Enhanced Production of ${\varepsilon}$-Caprolactone by Coexpression of Bacterial Hemoglobin Gene in Recombinant Escherichia coli Expressing Cyclohexanone Monooxygenase Gene

  • Lee, Won-Heong;Park, Eun-Hee;Kim, Myoung-Dong
    • Journal of Microbiology and Biotechnology
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    • 제24권12호
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    • pp.1685-1689
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    • 2014
  • Baeyer-Villiger (BV) oxidation of cyclohexanone to ${\varepsilon}$-caprolactone in a microbial system expressing cyclohexanone monooxygenase (CHMO) can be influenced by not only the efficient regeneration of NADPH but also a sufficient supply of oxygen. In this study, the bacterial hemoglobin gene from Vitreoscilla stercoraria (vhb) was introduced into the recombinant Escherichia coli expressing CHMO to investigate the effects of an oxygen-carrying protein on microbial BV oxidation of cyclohexanone. Coexpression of Vhb allowed the recombinant E. coli strain to produce a maximum ${\varepsilon}$-caprolactone concentration of 15.7 g/l in a fed-batch BV oxidation of cyclohexanone, which corresponded to a 43% improvement compared with the control strain expressing CHMO only under the same conditions.

보울 피이더에서 신경 회로망을 이용한 부품 자세 인식에 관한 연구 (A neural network method for recognition of part orientation in a bowl feeder)

  • 임태균;김종형;조형석;김성권
    • 제어로봇시스템학회:학술대회논문집
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    • 제어로봇시스템학회 1990년도 한국자동제어학술회의논문집(국내학술편); KOEX, Seoul; 26-27 Oct. 1990
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    • pp.275-280
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    • 1990
  • A neural network method is applied for recognizing the orientation o f individual parts being fed from a bowl feeder. The system is designed in such a way that a part can be discriminated and sorting according to every possible stable orientation without implementing any a mechanical tooling. The operation of the bowl feeder is based on a 2D image obtained from an array of fiber optic sensor located on the feeder track. The acquired binary image of a moving and vibrating part is used as input to a neural network which, in turn, determines t he orientation of the part. The main task of the neural network, here is to synthesize the appropriate internal discriminant functions for the part orientation using the part features. A series of the experiments reveals several promising points on performance. Since the operation of the feeder is highly programmable, it is well suited for feeding and sorting small parts prior to small batch assembly work.

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Rapid Purification of Recombinant Human Lipocortin-I Secreted from Saccharomyces cerevisiae

  • Chung, Bong-Hyun;Nam, Soo-Wan
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제5권4호
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    • pp.242-246
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    • 2000
  • Human lipocortin-I was expressed as a secretory product by Saccharomyces cerevisiae harboring an expression system consisting of GAL10 promoter, inulinase signal sequence and lipocortin-I terminator. Fed-batch fermentation was carried out to overproduce recombinant human lipocortin-I. The culture medium was desalted and concentrated by ultrafiltration, and then subjected to hydroxyapatite column chromatography. The lipocortin-I was purified to >98% purity by single-step hydroxyapatite column chromato-graphy. However, it was found that the purified lipocortin-I was a proteolytically-cleaved form which was cleaved immediately after the basic amino acid Lys26.

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Effective Production of N-Acetyl-$\beta$-glucosamine by Serratia marcescens Using Chitinadceous Waste

  • Kim, Kwang;A. Louise Creagh;Charles A. Haynes
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제3권2호
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    • pp.71-77
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    • 1998
  • The strain of Serratia marcescens QM B1466 produces selectively large amount of chitinolytic enzymes (about 1mg/L medium). Enzymatic hydrolysis of chitin to N-acetyl-${\beta}$-D-glucosamine (NAG) was performed with a system consisting of two hydrolases (chitinase and chitobiase) produced by optimization of a microbial host consuming chitin particles. For the development of Large-scale biological process for the production of NAG from chitinaceous waste, the selection and optimization of a microbial host, particle size of crab/shrimp chitin sources and initial induction time using chitin as a sole carbon source on chitinase/chitobiase production and NAG production were examined. Crab-shell chitin(1.5%) treated by dilute acid and , ball-milled with a normal diameter less than 250m gave the highest chitinase activity over a 7 days culture. Crude chitinase/ chitobiase solution obtained in a 10 L fed-batch fermentation showed a maximum activities of 23.6 U/mL and 5.1 U/mL, respectively with a feeding time of 3 hrs, near pH 8.5 at 30$^{\circ}C$.

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Bioprocess Strategies and Recovery Processes in Gibberellic Acid Fermentation

  • Shukla, Ruchi;Srivastava, Ashok K.;Chand, Subhash
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제8권5호
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    • pp.269-278
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    • 2003
  • Gibberellic acid (GA$_3$) is a commercially important plant growth hormone, which is gaining much more attention all over the world due to its effective use in agriculture and brewing industry. Industrially it is produced by submerged fermentation technique using Ascomycetous fungus Gibberella fujikuroi. Solid state and immobilized cell fermentation techniques had also been developed as an alternative to obtain higher yield of GA$_3$. This review summarizes the problems of GA$_3$ fermentation such as production of co-secondary metabolites along with GA$_3$, substrate inhibition and degradation of GA$_3$ to biologically inert compound gibberellenic acid, which limits the yield of GA$_3$ in the fermentation medium. These problems can be overcome by various bioprocessing strategies e.g. two - stage and fed batch cultivation processes. Further research on bioreactor operation strategies such as continuous and / or extractive fermentation with or without cell recycle / retention system need to be investigated for improvement in yield and productivity. Down stream processing for GA$_3$ isolation is also a challenge and procedures available for the same have been critically evaluated.

Construction of a Genetic System for Streptomyces albulus PD-1 and Improving Poly(ε-ʟ-lysine) Production Through Expression of Vitreoscilla Hemoglobin

  • Xu, Zhaoxian;Cao, Changhong;Sun, Zhuzhen;Li, Sha;Xu, Zheng;Feng, Xiaohai;Xu, Hong
    • Journal of Microbiology and Biotechnology
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    • 제25권11호
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    • pp.1819-1826
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    • 2015
  • Poly(ε-ʟ-lysine) (ε-PL) is a novel bioactive polymer secreted by filamentous bacteria. Owing to lack of a genetic system for most ε-PL-producing strains, very little research on enhancing ε-PL biosynthesis by genetic manipulation has been reported. In this study, an effective genetic system was established via intergeneric conjugal transfer for Streptomyces albulus PD-1, a famous ε-PL-producing strain. Using the established genetic system, the Vitreoscilla hemoglobin (VHb) gene was integrated into the chromosome of S. albulus PD-1 to alleviate oxygen limitation and to enhance the biosynthesis of ε-PL in submerged fermentation. Ultimately, the production of ε-PL increased from 22.7 g/l to 34.2 g/l after fed-batch culture in a 5 L bioreactor. Determination of the oxygen uptake rate, transcriptional level of ε-PL synthetase gene, and ATP level unveiled that the expression of VHb in S. albulus PD-1 enhanced ε-PL biosynthesis by improving respiration and ATP supply. To the best of our knowledge, this is the first report on enhancing ε-PL production by chromosomal integration of the VHb gene in an ε-PL-producing strain, and it will open a new avenue for ε-PL production.

Aspergillus awamori와 Zymomonas mobilis로 구성된 혼합고정화 배양계의 에탄올 생산에 미치는 Neupectin-L의 영향 (Effect of Neupectin-L on Ethanol Production from Raw Starch Using a Co-Immobilized Aspergillus awamori and Zymomonas mobilis)

  • 이상원;조용운;김홍출;박석규;성낙계
    • Applied Biological Chemistry
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    • 제40권2호
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    • pp.89-94
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    • 1997
  • Aspergillus awamori(A)와 Zymomonas mobilis(Z)로 구성된 혼합고정화 배양계(A-Z 36계)의 특성을 이용하여 생전분으로 부터 직접 에탄올생산을 행할 때 투입되는 에너지를 절약할 목적으로 비가열살균 배양법을 검토하였다. A-Z 36계에 의한 비가열살균 배양은 배지에 함유된 세균 때문에 어려웠다. Sorbic acid, benzoic acid, dehydroacetic acid, p-hydroxybenzoic acid, Vantocil IB, Neupectin-L 등의 여러 가지 살균제 중에서 Vantocil IB와 Neupectin-L은 잡균의 오염없이 대조구와 비슷한 속도로 기질을 분해하였다. 0.1% Neupectin-L은 대조구보다 약간 높은 6.9 g/l(대조구 : 6.4 g/l)의 에탄올을 생산하였다$(Y_{p/s}:0.39)$. 0.1% Neupectin-L을 첨가한 유가배양에서는 2%기질을 기본으로 5회분의 기질을 첨가하여 34 g/l 에탄올을 얻어 2.0 g/l/day의 생산성을 나타내었다.

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효소공정에 의한 트립토판 생산 (Production of L-Tryptophan by Enzymatic Processes)

  • 이인영;안경섭;김의환;이선복
    • 한국미생물·생명공학회지
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    • 제20권1호
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    • pp.73-78
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    • 1992
  • Tryptophanase를 이용하여 트립토판 합성시 인돌의 효소활성 저해를 억제하기 위하여 유가식 조업, 유기용매 이상계의 사용, 그리고 cyclodextrin의 첨가등에 대하여 연구하였다. 효소 농도가 0.5mg/ml일때 인돌 농도 0.4mM 부근에서 트립토판 생성이 가장 빨랐으며 그 이상에서는 효소활성이 심한 저해를 받았다. 초기 인돌 농도가 20mM일 때는 27시간 반응후 인돌의 전환율이 20인데 비하여 반응기내 인돌 농도를 5mM 이하로 유가식 조업을 하였을 때 전환율이 80%로 향상되었다.

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Effects of pH and Carbon Sources on Biohydrogen Production by Co-Culture of Clostridium butyricum and Rhodobacter sphaeroides

  • Lee, Jung-Yeol;Chen, Xue-Jiao;Lee, Eun-Jung;Min, Kyung-Sok
    • Journal of Microbiology and Biotechnology
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    • 제22권3호
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    • pp.400-406
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    • 2012
  • To improve the hydrogen yield from biological fermentation of organic wastewater, a co-culture system of dark- and photo-fermentation bacteria was investigated. In a pure-culture system of the dark-fermentation bacterium Clostridium butyricum, a pH of 6.25 was found to be optimal, resulting in a hydrogen production rate of 18.7 ml-$H_2/l/h$. On the other hand, the photosynthetic bacterium Rhodobacter sphaeroides could produce the most hydrogen at 1.81mol-$H_2/mol$-glucose at pH 7.0. The maximum specific growth rate of R. sphaeroides was determined to be 2.93 $h^{-1}$ when acetic acid was used as the carbon source, a result that was significantly higher than that obtained using either glucose or a mixture of volatile fatty acids (VFAs). Acetic acid best supported R. sphaeroides cell growth but not hydrogen production. In the co-culture system with glucose, hydrogen could be steadily produced without any lag phase. There were distinguishable inflection points in a plot of accumulated hydrogen over time, resulting from the dynamic production or consumption of VFAs by the interaction between the dark- and photo-fermentation bacteria. Lastly, the hydrogen production rate of a repeated fed-batch run was 15.9 ml-$H_2/l/h$, which was achievable in a sustainable manner.