• 제목/요약/키워드: L-continuous

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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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막분리를 이용한 미생물 재순환 연속 알콜발효에 관한 연구 (A Study on Continuous Alcohol Fermentation with Cell Recycle by Means of Membrane Separation)

  • 이준형;목영일허병기
    • KSBB Journal
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    • 제7권2호
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    • pp.139-143
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    • 1992
  • 본 연구에서는 균주 S. cerevisiae ATCC 24858을 막분리를 이용한 미생물 재순환 연속에탄올 발효시스템에 적용하여 희석비 (0.3, 0.5, $0.7hr^{-1}$)와 주입기질의 당농도 (50, 100, 150, 200g/l)에 따른 균체농도 및 알콜생산성의 변화관계를 규명하여 보았다. 주입기질 당농도50g/l, 희석비$0.3hr^{-1}$ 내지 당농도200g/l, 희석비 $0.7hr^{-1}$ 사이의 실험범위에서 균체농도는 12g/l내지 107g/l 사이에, 알콜생산성은 7.0g/l 내지 55.6g/l 사이에 분포되었다. 더욱이 알콜생산성은 회분식 발효의 생산성에 비하여 최소 307배 내지 최대 29.3배 까지 증가하였다. 또한 본 연구의 실험범위에 대한 에탄올 평균수율은 0.42로써 이론수율의 82%였으며 회분식 수율보다 약간 상회하였다.

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연속흐름 모형실험장치를 이용한 전로슬래그에 의한 인산염 제거 (Phosphate removal by the continuous flow pilot plant with converter slag)

  • 이상호;황정재
    • 상하수도학회지
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    • 제28권4호
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    • pp.453-459
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    • 2014
  • The excessive concentration of phosphorus in the river and reservoir is a deteriorating factor for the eutrophication. The converter slag was used to remove the phosphate from the synthetic wastewater. Influencing factors were studied to remove soluble orthophosphate with the different particle sizes through the batch and the column experiments by continuous flow. Freundlich and Langmuir adsorption isotherm constants were obtained from batch experiments with $PS_A$ and $PS_B$. Freundlich isotherm was fitted better than Langmuir isotherm. Regression coefficient of Freundlich isotherm was 0.95 for $PS_A$ and 0.92 for $PS_B$, respectively. The adsorption kinetics from the batch experiment were revealed that bigger size of convert slag, $PS_A$ can be applied for the higher than 3.5 mg/L of phosphate concentration. The pilot plant of continuous flow was applied in order to evaluate the pH variation, breakthrough points and breakthrough adsorption capacity of phosphate. The variation of pH was decreased through the experimental hours. The breakthrough time was 1,432 and 312 hours to 10 mg/L and 50 mg/L for the influent concentration, respectively. The breakthrough adsorption capacity was 3.54 g/kg for 10 mg/L, and 1.72 g/kg for 50 mg/L as influent phosphate concentration.

Production of Lactococcal Bacteriocin using Repeated-Batch and Continuous Cultures

  • Yoo, Jin-Young
    • Journal of Microbiology and Biotechnology
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    • 제2권4호
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    • pp.284-287
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    • 1992
  • Repeated-batch and continuous cultures of Lactococcus sp. 1112-1 were carried out for bacteriocin production using a glucose-casein medium. Repeated-batch culture did not efficiently enhanced the bacteriocin production. Continuous production was possible at the dilution rate of 0.4 $h^{-1}$. Maximum specific production rate ($Q^p$), bacteriocin production and biomass at the dilution rate were 347, 136 IU/g/h, 2, 121 IU/ml and 2.45 g/L, respectively.

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Continuous high cell density culture of Anaerobiospirillum succiniciproducens with membrane filtration for the production of succinic acid

  • 이평천;이우기;이상엽;장호남
    • 한국생물공학회:학술대회논문집
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    • 한국생물공학회 2000년도 추계학술발표대회 및 bio-venture fair
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    • pp.338-341
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    • 2000
  • An internal membrane bioreactor system was employed for continuous succinic ac id production from glucose in order to prove its performance and practicality. Succinic acid-producing Anaerobiospirillum succiniciproducens required more $CO_2$ for the proper growth and succinic acid production in cell recycled continuous culture than in batch culture. The maximum productivity obtained in cell recycled continuous culture was about 3.3 g/L-h which was ca. 3.3 times higher than that obtained in batch culture.

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Uniform Ergodicity and Exponential α-Mixing for Continuous Time Stochastic Volatility Model

  • Lee, O.
    • Communications for Statistical Applications and Methods
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    • 제18권2호
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    • pp.229-236
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    • 2011
  • A continuous time stochastic volatility model for financial assets suggested by Barndorff-Nielsen and Shephard (2001) is considered, where the volatility process is modelled as an Ornstein-Uhlenbeck type process driven by a general L$\'{e}$vy process and the price process is then obtained by using an independent Brownian motion as the driving noise. The uniform ergodicity of the volatility process and exponential ${\alpha}$-mixing properties of the log price processes of given continuous time stochastic volatility models are obtained.

Poly-$\beta$-hydroxybutyrate 생산을 위한 연속배양에서 포도당 및 암모늄 농도의 영향 (Effects of Glucose and Ammonium Concentrations in Continuous Culture for Poly-$\beta$-hydroxybutyrate Production)

  • 이용우;유영제
    • 한국미생물·생명공학회지
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    • 제20권5호
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    • pp.597-606
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    • 1992
  • Alcaligenes eutrophus 균주로 poly-Beta-hydroxybutyrate(PHB) 생산을 위한 연속배양 공정의 성능에 미치는 희석비율, 주입 포도당 및 염화암모늄농도의 영향에 대하여 연구하였다. 주입 기질농도가 일정할때( 주입 포도당농도=20g/l, 주입 염화암모늄농도=2g/l), 생체성장속도와 PHB생성속도는 희석비율이 각각 0.1, $0.06h^{-1}$에서 최고 값을 나타냈고, $0.13h^{-1}$에서 세포가 전부 배출되었다. 희석비율이 증가함에 따라 비PHB 생성속도는 계속 증가하였지만 PHB 축적비는 50%에서 25%로 감소하였다. 세포농도는 주입 염화암모늄농도가 2g/l일 때 최고값을 나타내었고, 그 이상의 농도에서는 감소하였다. 이 실험결과로 암모늄에 의한 기질저해가 있음을 알 수 있었다. 주입 포도당농도가 30g/l에서 세포농도는 최고값을 나타냈지만 PHB 농도는 계속 증가하였따. 모델속도식에 대한 매개변수는 도식적 방법과 매개변수 추정으로 구하였고 희석비율, 주입 포도당농도, 주입 염화암모늄농도의영향에 대하여 모사한 결과 실험데이타와 잘 일치하였다.

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Development of continuous process for the production of Exo-biopolymer with Cordyceps militaris

  • Kim, Kyoung-Ju;Lee, Jung-Heon
    • 한국생물공학회:학술대회논문집
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    • 한국생물공학회 2003년도 생물공학의 동향(XIII)
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    • pp.243-245
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    • 2003
  • The continuous fermentation process for exe-biopolymer production with Cordyceps militaris has been developed in this research. With the change of dilution rate, biopolymer production has been changed and the maximal biopolymer production has been achieved when the dilution rate was 0.0225/hr. The maximum mycelium concentration and biopolymer concentration were 8 g/L and 4.2 g/L, respectively.

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JOINT SPATIAL NUMERICAL RANGES OF OPERATORS ON BANACH SPACES

  • Yang, Youngoh
    • 대한수학회보
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    • 제26권2호
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    • pp.119-126
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    • 1989
  • Throughout this paper, X will always denote a Banach space over the complex numbers C, and L(X) will denote the Banach algebra of all continuous linear operators on X. Operator will always mean continuous linear operator. An n-tuple of operators T$_{1}$,..,T$_{n}$ on X will be denoted by over ^ T=(T$_{1}$,..,T$_{n}$ ). Let L$^{n}$ (X) be the set of all n-tuples of operators on X. X' will denote the dual space of X, S(X) its unit sphere and .PI.(X) the subset of X*X' defined by .PI.(X)={(x,f).mem.X*X': ∥x∥=∥f∥=f(x)=1}.

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상향식 연속주조법으로 제조한 Ai-Ni 공정복합재료의 응고조직 및 기계적 성질 (Microstructures and Mechanical Properties of Al-Ni Eutectic Composite by Upward Continuous Casting)

  • 권기균;홍준표;이계완
    • 한국주조공학회지
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    • 제10권1호
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    • pp.50-56
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    • 1990
  • Continuous casting of the $Al-Al_3Ni$: eutectic composite was carried out by the upward continuous casting process. The morphology of the eutectic growth and the stability of solid-liquid interface were investigated under various growth conditions in an upward continuous casting. The effect of growth conditions on the mechanical properties of the $Al-Al_3$ Ni eutectic composit was also investigated, and the results were compared with those by the Bridgman method. As for the results, it was possible to get the planar solid-liquid interface at the condition of $G_L/R$$1.04{\times}10^3^{\circ}Csec/mm^2$. And the inter-rod spacing of $Al-Al_3Ni$ eutectic composite was decreased with the increase of pulling speed. The reduction of inter-rod spacing & value of $G_L/R$ caused the increase of ultimate tensile strength in $Al-Al_3Ni$: eutectic composite. The ultimate tensile strengths of $Al-Al_3Ni$ by the upward continuous casting were higher then those by the Bridgman method.

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