• Bulletin of the Korean Chemical Society
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• 제26권2호
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• pp.217-218
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• 2005

• Journal of Microbiology and Biotechnology
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• 제22권12호
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• pp.1673-1680
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• 2012

In this study, DEAE-corncobs [delignified corncob grits derivatized with 2-(diethylamino)ethyl chloride hydrochloride ($DEAE{\cdot}HCl$)] were prepared as a carrier to immobilize yeast (Saccharomyces cerevisiae) for ethanol production. The immobilized yeast cell reactor produced ethanol under optimized $DEAE{\cdot}HCl$ derivatization and adsorption conditions between yeast cells and the DEAE-corncobs. When delignified corncob grit (3.0 g) was derivatized with 0.5M $DEAE{\cdot}HCl$, the yeast cell suspension ($OD_{600}$ = 3.0) was adsorbed at >90% of the initial cell $OD_{600}$. This amount of adsorbed yeast cells was estimated to be 5.36 mg-dry cells/g-DEAE corncobs. The $Q_{max}$ (the maximum cell adsorption by the carrier) of the DEAE-corncobs was estimated to be 25.1 (mg/g), based on a Languir model biosorption isotherm experiment. When we conducted a batch culture with medium recycling using the immobilized yeast cells, the yeast cells on DEAE-corncobs produced ethanol gradually, according to glucose consumption, without cells detaching from the DEAE-corncobs. We observed under electron microscopy that the yeast cells grew on the surface and in the holes of the DEAE-corncobs. In a future study, DEAE-corncobs and the immobilized yeast cell reactor system will contribute to bioethanol production from biomass hydrolysates.

• Journal of Microbiology and Biotechnology
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• 제7권1호
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• pp.62-67
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• 1997

To enhance the hyperproductive and low energy-consuming ethanol fermentation rate, the thermotolerant yeast S. cerevisiae RA-74-2 cells were immobilized. An efficient immobilization condition was proved to be $1.5{\%}$ (w/v) alginate solution, neutral pH and 20 h activation of beads. The fermentation characteristics and stability at various temperatures were examined as compared with free S. cerevisiae RA-74-2 cells. The immobilized cells had excellent fermentation rate at the range of pH 3-7 at 30-$42^{\circ}C$ in 15-$20{\%}$ glucose media. When the seed volume was adjusted to 0.12 (v/v) (6ml bead/50 ml medium), $11{\%}$ (w/v) ethanol was produced during the first 34 hand $12.15{\%}$ (w/v) ethanol [$95{\%}$ (w/v) of theoretical yield] during the first 60 h in $25{\%}$ glucose medium. In repetitive fermentation using a 2 litre fermentor, 5.79-$7.27{\%}$ (w/v) ethanol [76-$95{\%}$ (w/v) of theoretical yield] was produced during the 40-55 h in $15{\%}$ glucose media. These data suggested the fact that alginate beads of thermotolerant S. cerevisiae RA-74-2 cells would contribute to economic and hyperproductive ethanol fermentation at high temperature.

• KSBB Journal
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• 제10권3호
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• pp.249-256
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• 1995

${\gamma}$-Glutamylcysteine 생산에 있어서 재조합 대장 균 HB101/pGH501만을 이용한 단일세포반응계가 재조합 대장균과 효모를 이용한 흔합서l포반응계보다 반응시간이 짧고 생산농도가 높은 것으로 나타났다. 그러나 생산경제성 측면에서 ATP 재생공정을 위하 여 훈합세포반응계를 사용하였다. 재조합 대장균과 효모를 이용한 혼합세포반응계에서 대장균과 효모의 비율은 1:4가 적합함을 보였고, ATP 재생공정에 사용되는 glucose는 O.5M의 농도에서 가장 효율적 으로 나타났다. 재조합 대장균과 효모를 alginate를 이용하여 고정화하여 반응계로 사용하였을 경우 반 응에 필요한 시간이 걸어지고 생산놓도도 감소되냐 반응계의 안정성은 10% 정도 증가됨을 알 수 있었다. 실험결과 alginate로 고정화된 흔합세포반응계 를 사용하여 ${\gamma}$-glutamylcysteine를 연속 생산할 수 있음을 확인하였다.

• 한국미생물·생명공학회지
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• 제21권4호
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• pp.366-372
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• 1993

The aim of this study was to find out the rapid fermentation of soy sauce from koji hydrolyzate using column type reactor packed with immobilized yeast cells. Each immobilized cell of Zygosaccharomyces rouxii BH-90 and Candida versatilis BH-91 in the packed column type reactor produced 2.8% ethyl alcohol and 18mg/l 4-ethylguaiacol over 96 hours under the optimal condition. Continuous fermentation was performed by immobilized Z. rouxii BH-90 packed in column type reactor. Immobilized Z. rouxii BH-90 produced 2.30~2.85% ethyl alcohol during 30 days, and decreased gradually from 40 days to 80 days. Also C. versatilis BH-91 produced 4-ethylguaiacol at the constant rate of 16~18mg/l and decreased gradually after 40 days. Final product of soy sauce contained 2.8% ethyl alcohol and 18mg/l 4-ethylguaiacol. However, amino acid compositions of final products were consisted of predominantly glutamic acid, leucine, arginine, aspartic acid, lysine and valine, which were more than 50% of total amino acid.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1987년도 한국자동제어학술회의논문집; 한국과학기술대학, 충남; 16-17 Oct. 1987
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• pp.637-642
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• 1987

In immobilized cell reactors, effective cell mass is a very important parameter which must be estimated during operation for control and regeneration of biocatalyst. In this report, the effective cell mass in immobilized cell reactor was studied using a sequential estimation method. An immobilized yeast reactor was operated in batch recycle mode. The states of the immobilized cell reactor could be estimated from the process data using an extended Kalman filter.

• 한국미생물·생명공학회지
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• 제19권4호
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• pp.390-397
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• 1991

효모를 Ca-alginate에 고정화하여 회분발효에서 glucose로부터 에탄올을 생산하여 다음의 결과를 얻었다. 100g wet weight/l($4.3 \times 10^9$ cell/l)의 효모를 pH 7.0, 2% 농도의 Ca-alginate에 고정화하였다. 10 beads volume이 에탄올 생산에 최적이었고 30일 (720 시간) 동안 bead의 수명이 지속되었다. 회분식 발효에서 온도안정성은 고정화 효모의 경우 30~$40^{\circ}C$였으며 free cell의 경우 30~$37^{\circ}C$였다. pH 안정성은 pH 4.0~9.0였으며, 에탄올생산 최적 당농도는 15%였다. 최적조건에서 에탄올수율은 0.45, 생산된 에탄올 농도는 67.6g/l 그리고 에탄올 생산성은 1.99g/l.h로 각각 나타났다.

• Mycobiology
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• 제42권3호
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• pp.305-309
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• 2014

We investigated a novel process for production of ethanol from glycerol using the yeast Pachysolen tannophilus. After optimization of the fermentation medium, repeated-batch flask culture was performed over a period of 378 hr using yeast cells immobilized on Celite. Our results indicated that the use of Celite for immobilization of P. tannophilus was a practical approach for ethanol production from glycerol, and should be suitable for industrial ethanol production.

• 기술사
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• 제21권2호
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• pp.13-18
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• 1988

A Study for ethanol fermentation with immobilized yeast that is entrapped to Ca-alginate beads and batch system was carried out using molasses as substrate. The results are as follows. 1. The yield of alcohol fermentation is more efficacious then that of conventional fermentation process. The beads were used 15times and got a result of fermentation yield rate 89. 57％∼92.35％f, which is comparable with the rate of 86.3％ gained from the conventional fermentation process. 2. The concentration of Ca-alginate was 1∼5％ For long run use (2520 hours) it is necessary 2％ or more concentration of Ca-alginate. 3. The amount of the yeast cells for entrap to Ca-alginate beads was required 1.0g (indried material) or more for 200g Ca-alginate beads.

• KSBB Journal
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• 제15권5호
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• pp.438-443
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• 2000

맥주의 숙성기간을 단축시키기 위해 네 종류의 고정화용 담체를 활용한 고정화 효모 반응기를 시험하였다. 전발효가 끝난 Green Beer (GB)를 효모를 제거하고 열처리할 경우 처 리온도가 높을수록 전구체인 $\alpha$-acetolactate의 diacety 1로의 전 환율이 낮고 전환속도도 빨라 $70^{\circ}C$이상의 온도에서는 4분이면 충분하였다 GB 중의 산소농도는 전구체에서 DA로의 변환율에 매우 큰 영향을 끼쳤는데 그 농도가 낮을수록 전환율이 낮았으며 0.1 ppm 이하의 농도에서는 거의 대부분의 전 구체가 DA이외의 물칠로 전환되었다. 열처리한 전발효 맥주 를 HAN, G-2, FLO, GDC 담체 column에 $\alpha$, 체류시간 80-150분으로 통과시킬 경우 diacety I 농도를 상품 맥주의 품질로 적합한 0.1 ppm이하로 떨어뜨릴 수 있어서 시험한 담체 모두 맥주 숙성용 효모고정화용 답체로의 실용화 가능 성이 있었다. 이 때 세라믹 담체 column의 경우 GDC 담체 column에 비해 미발효된 잔당의 발효에 의한 새로운 DA 전 구체의 생성이 많았다. 위와 같은 방법으로 생산한 맥주를 공장에서 기존의 방법으로 생산한 맥주와 맛을 비교한 결과 미세한 차이가 있으나 불쾌한 느낌을 주는 이취등은 발견되지 않아 고정화 효모 반응기에 의한 고속 숙성공정의 현장적 용 가능성이 높음을 확인할 수 있었다.