• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2005년도 생물공학의 동향(XVII)
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• pp.319-323
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• 2005

This study is concerned with development of efficient culture methods for lactic acid fermentation of Lactobacillus sp. RKY2. The cell-recycle repeated batch fermentation using cheese whey and corn steep liquor as raw materials was tried in order to further enhance the productivity of lactic acid. In addition, fermentation efficiencies could be considerably enhanced by cell-recycle continuous culture. Through the cell-recycle repeated batch fermentation, lactic acid productivity was maximized to 6.34 $g/L{\cdot}h,$ which corresponded to 6.2 times higher value than that of the batch fermentation. During the cell-recycle continuous fermentation, the last dry cell weight at the end of fermentation could be increased to 25.3 g/L.

• Journal of Microbiology and Biotechnology
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• 제5권4호
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• pp.229-233
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• 1995

Acremonium chrysogenum was immobilized in ionotropic gel beads to develop semi-continuous production of cephalosporin C (CPC). Barium alginate beads were more stable than calcium alginate or strontium alginate beads in chemically defined media. The gel stability of Ba-alginate was further increased by cross-linking with polyethyleneimine (PEI). The presence of carboxymethyl cellulose inside Ba-alginate beads did not reduce mass transfer resistance. Ba-alginate microbeads that had little diffusion limitation increased CPC production rate 1.6 fold higher than that of normal beads. CPC fermentation with immobilized cells in Ba-alginate microbeads was performed continuously for 40 days by way of repeated fed-batch operations. Mathematical modeling was developed to describe the repeated fed-batch fermentation system. Results of the computer simulation agreed well with the experimental data, which made it possible to predict an optimal feeding rate that could maximize total CPC productions.

• Mycobiology
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• 제40권1호
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• pp.35-41
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• 2012

A repeated batch fermentation system was used to produce ethanol using $Saccharomyces$ $cerevisiae$ strain (NCIM 3640) immobilized on sugarcane ($Saccharum$ $officinarum$ L.) pieces. For comparison free cells were also used to produce ethanol by repeated batch fermentation. Scanning electron microscopy evidently showed that cell immobilization resulted in firm adsorption of the yeast cells within subsurface cavities, capillary flow through the vessels of the vascular bundle structure, and attachment of the yeast to the surface of the sugarcane pieces. Repeated batch fermentations using sugarcane supported biocatalyst were successfully carried out for at least ten times without any significant loss in ethanol production from sugarcane juice and molasses. The number of cells attached to the support increased during the fermentation process, and fewer yeast cells leaked into fermentation broth. Ethanol concentrations (about 72.65-76.28 g/L in an average value) and ethanol productivities (about 2.27-2.36 g/L/hr in an average value) were high and stable, and residual sugar concentrations were low in all fermentations (0.9-3.25 g/L) with conversions ranging from 98.03-99.43%, showing efficiency 91.57-95.43 and operational stability of biocatalyst for ethanol fermentation. The results of the work pertaining to the use of sugarcane as immobilized yeast support could be promising for industrial fermentations.

• KSBB Journal
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• 제25권2호
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• pp.187-192
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• 2010

S. cerevisiae ATCC 24858을 이용한 ethanol 생산에서, aeration 효과를 ethanol 수율, specific ethanol production rate, ethanol 생산성 측면에서 분석하여, 반복 유가식 공정전략을 설계하였다. Ethanol 수율과 ethanol 생산성은 공기를 0.33 vvm 넣었을 때, 공기를 넣지 않고 배양한 것에 비하여 더 큰 값을 보였고, 24시간 마다 배지를 교체한 배양이 36시간 마다 배지를 교체한 배양 보다 더 큰 값을 보였다. 총 ethanol 생산량 값이 가장 큰 경우는 0.33 vvm의 공기를 넣고, 배지를 24시간마다 완전히 갈아주었을 때이고, 이때 가장 많은 703.8 g의 ethanol이 생산되었다.

• KSBB Journal
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• 제10권1호
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• pp.55-62
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• 1995

본 연구에서는 균주로 Saccharomyces ceremszae A Tee 24858을, 초기 당 농도로는 60, 90, 120 및 $150g/\ell$ 을, 1회 발효 시간으로는 1시간 또는 2시간을, 초기 균체농도로는 $17.5g/\ell$ 내지 $53.1g/\ell$ 사이의 값을 사용하여 10회 반복 회분식 실험을 수 행하였다. 이 결과로부터 반복 회분식 실험에서의 평균 초기 균체농도와 에탄올 생산성 사이의 함수 관계를 규명 하여 보았다. 초기 균체농도와 에탄올 생산성 사이의 함수 관계는 초기 균체농도가 증가함에 따라 초기 당 농도에 관계없이 에탄올 생산성이 비 션형적 으로 증가하는 함수 관계를 나타내였다. 초기 당 농도가 $60g/\ell$ 이고, 초기 균체농도가 $34.5g/\ell$ 인 경우 발효는 1시간 내에 완료되었으며 균체의 분리, 새로운 기질의 주입 등의 조작을 고려한 총 10회 반복 회분 실험의 에탄올 생산성은 $26.7g/\ell$.hr이었다. 초기 당 농도가 120gjP 이고 초기 균체농도가 5 50.3gj P 인 경우에도 1시간 내에 발효가 완료되었으 며 이때의 에탄올 생산성은 $48.8g/\ell$.hr이었다. 본 연구에서 수행한 8종류의 10회 반복 회분식 실험을 통하여 얻은 최대 에탄융 생산성은 $53g/\ell$.hr이였다.

• 한국식품과학회지
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• 제29권2호
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• pp.343-347
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• 1997

Lactobacillus brevis, L. fermentum과 L. plantarum의 혼합젖산균을 사용하여 배양조건이 밀가루 용액의 발효에 미치는 영향을 살펴보았다. 온도변화에 따른 pH와 총적정산도의 변화를 살펴본 결과 pH의 감소와 총적정산도의 증가가 가장 크게 나타난 $35^{\circ}C$를 밀가루 발효의 최적온도로 선정하였다. 5L발효조에서 질소가스를 1.0 vvm으로 첨가한 혐기적 조건보다 공기를 첨가한 호기적 조건에서 총적정산도의 증가와 pH의 감소가 더 크게 나타났다. 최적 산소공급 조건을 찾기 위하여 통기량을 1.0 vvm으로 고정하고 교반속도를 달리하여 밀가루 용액의 발효한 결과 총적정산도가 가장 크게 나타난 교반속도 250 rpm에 해당되는 산소 전달속도상수 $60\;hr^{-1}$에서 최적이었다. 선정된 최적 배양조건에서 밀가루 발효액의 생산성을 높이기 위하여 반복비율을 변화시키면서 pH-stat를 이용한 반복 유가식 배양을 수행하였다. 반복비율이 증가할수록 반복 간격시간은 증가하였으나 밀가루 발효의 최대 작동시간은 감소하였다. 최적 반복비율을 결정하기 위하여 단위시간 당 배양부피 당 생산된 밀가루 발효액의 부피와 최대가동시간 동안 배양부피 당 생산된 총 밀가루 발효액의 부피를 살펴본 결과 20%의 반복비율에서 최대값을 나타내었다. 혼합젖산균을 이용한 밀가루용액의 유가식 배양에서 최적조건은 배양온도 $35^{\circ}C$, 통기량 1.0 vvm, 산소전달속도 $60\;hr^{-1}$, 반복비율 20%로 나타났다.

• Journal of Microbiology and Biotechnology
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• 제24권5호
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• pp.629-638
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• 2014

This study describes an alternative mixed culture fermentation technology to anaerobically convert lignocellulosic biomass into butyric acid, a valuable product with wide application, without supplementary cellulolytic enzymes. Rice straw was soaked in 1% NaOH solution to increase digestibility. Among the tested pretreatment conditions, soaking rice straw at $50^{\circ}C$ for 72 h removed ~66% of the lignin, but retained ~84% of the cellulose and ~71% of the hemicellulose. By using an undefined cellulose-degrading butyrate-producing microbial community as butyric acid producer in batch fermentation, about 6 g/l of butyric acid was produced from the pretreated rice straw, which accounted for ~76% of the total volatile fatty acids. In the repeated-batch operation, the butyric acid production declined batch by batch, which was most possibly caused by the shift of microbial community structure monitored by denaturing gradient gel electrophoresis. In this study, batch operation was observed to be more suitable for butyric acid production.

• 한국미생물·생명공학회지
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• 제23권6호
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• pp.723-729
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• 1995

A flocculating sugar tolerant yeast strain was isolated from fermenting Takju. This strain was identified as Saccharomyces cerevisiae CA-1 according to the Lodder's yeast taxonomic studies. The isolated yeast could grow in 50% glucose and in 7% ethanol in the YPD medium. It's optimal growth temperature, initial pH, shaking rate and initial glucose concentration for ethanol fermentation showed 35$\circ$C, 4.5, 150 rpm, 15%, respectively. Ethanol concentration was 63 g/l in 20% glucose after 24 hours, fermentation yield was 0.49 g-ethanol/g-glucose in 10% glucose after 24 hours and ethanol productivity was 3.09 g/l$\cdot $h in 10% glucose after 12 hours in batch fermentation. Repeated batch fermentation was possible for over 50 days and ethanol yield, ethanol productivity and substrate conversion rate were 0.39-0.50 g/g, 1.63-2.08 g/l$\cdot $h and more than 99%, respectively during these periods.

• Journal of Microbiology and Biotechnology
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• 제23권4호
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• pp.511-517
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• 2013

In this work, a fibrous bed bioreactor with high specific surface area and good adsorption efficacy for S. cerevisiae cells was used as the immobilization matrix in the production of ethanol. In batch fermentation, an optimal ethanol concentration of 91.36 g/l and productivity of 4.57 g $l^{-1}\;h^{-1}$ were obtained at an initial sugar concentration of 200 g/l. The ethanol productivity achieved by the immobilized cells was 41.93% higher than that obtained from free cells. Ethanol production in a 22-cycle repeated batch fermentation demonstrated the enhanced stability of the immobilized yeast cells. Under continuous fermentation in packed-bed reactors, a maximum ethanol concentration of 108.14 g/l and a productivity of 14.71 g $l^{-1}\;h^{-1}$ were attained at $35^{\circ}C$, and a dilution rate of 0.136 $h^{-1}$ with 250 g/l glucose.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2005년도 생물공학의 동향(XVI)
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• pp.81-81
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• 2005