• Journal of Microbiology
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• 제43권3호
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• pp.301-307
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• 2005

The feasibility of laccase production by immobilization of Pleurotus ostreatus 1804 on polyurethane foam (PUF) cubes with respect to media composition was studied in both batch and reactor systems. Enhanced laccase yield was evidenced due to immobilization. A relatively high maximum laccase activity of 312.6 U was observed with immobilized mycelia in shake flasks compared to the maximum laccase activity of free mycelia (272.2 U). It is evident from this study that the culture conditions studied, i.e. biomass level, pH, substrate concentration, yeast extract concentration, $Cu^{2+}$ concentration, and alcohol nature, showed significant influence on the laccase yield. Gel electrophoretic analysis showed the molecular weight of the laccase produced by immobilized P. ostreatus to be 66 kDa. The laccase yield was significantly higher and more rapid in the packed bed reactor than in the shake flask experiments. A maximum laccase yield of 392.9 U was observed within 144 h of the fermentation period with complete glucose depletion.

• Mycobiology
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• 제42권3호
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• pp.249-255
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• 2014

We evaluated a more practical and cost-effective immobilization carriers for ethanol production using the yeast Saccharomyces cerevisiae. Three candidate materials-rice hull, rice straw, and sawdust-were tested for their cell-adsorption capacity and operational durability. Derivatizations of rice hull, rice straw, and sawdust with the optimal concentration of 0.5 M of 2-(diethylamino)ethyl chloride hydrochloride (DEAE HCl) resulted in > 95% adsorption of the initial yeast cells at 2 hr for DEAE-rice hull and DEAE-sawdust and in only approximately 80% adsorption for DEAE-rice straw. In addition, DEAE-sawdust was found to be a more practical carrier for immobilizing yeast cells in terms of operational durability in shaking flask cultures with two different speeds of 60 and 150 rpm. Furthermore, the biosorption isotherms of DEAE-rice hull, -rice straw, and -sawdust for yeast cells revealed that the $Q_{max}$ of DEAE-sawdust (82.6 mg/g) was greater than that of DEAE-rice hull and DEAE-rice straw. During the 404-hr of continuous column reactor operation using yeast cells immobilized on DEAE-sawdust, no serious detachment of the yeast cells from the DEAE-sawdust was recorded. Ethanol yield of approximately 3.04 g/L was produced steadily, and glucose was completely converted to ethanol at a yield of 0.375 g-ethanol/g-glucose (73.4% of the theoretical value). Thus, sawdust is a promising practical immobilization carrier for ethanol production, with significance in the production of bioethanol as a biofuel.

• 미생물과산업
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• 제19권4호
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• pp.2-13
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• 1993

Some microorganisms, including actinomycetes, cyanobacteria, and other bacteria, algae, fungi, and yeast, can accumulate and retain relatively high quantities of heavy metals and radionuclides from their external environments (1-4). Both living and dead cells can be used for biosorptive metal/radionuclide removal from solution. Thus microorganisms and products excreted by or derived from microbial cells (2) may provide an alternative or adjunct to conventional techniuqes of metal removal and recovery. Recent approaches have separated the microbial growth and metal removal process to manipulate production of metal-adsorptive capacity of bacteria and metal removal process. If pre-grown cells are immobilized and used for metal removal, mathematical modeling can be applied to predict immobilized cell reactor behavior under specific process conditions. Waste and microbial adsorbent could be separated from the treated flow in one step. Once treated, the metal waste is concentrated in a small volume of sorbed form for easy metal disposal or recovery.

• 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.

• Journal of Microbiology and Biotechnology
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• 제23권10호
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• pp.1434-1444
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• 2013

We established a two-step production process using immobilized S. cerevisiae and P. stipitis yeast to produce ethanol from seaweed (U. pertusa Kjellman) hydrolysate. The process was designed to completely consume both glucose and xylose. In particular, the yeasts were immobilized using DEAE-corncob and DEAE-cotton, respectively. The first step of the process included a continuous column reactor using immobilized S. cerevisiae, and the second step included a repeated-batch reactor using immobilized P. stipitis. It was verified that the glucose and xylose in 20 L of medium containing the U. pertusa Kjellman hydrolysate was converted completely to about 5.0 g/l ethanol through the two-step process, in which the overall ethanol yield from total reducing sugar was 0.37 and the volumetric ethanol productivity was 0.126 g/l/h. The volumetric ethanol productivity of the two-step process was about 2.7 times greater than that when P. stipitis was used alone for ethanol production from U. pertusa Kjellman hydrolysate. In addition, the overall ethanol yield from glucose and xylose was superior to that when P. stipitis was used alone for ethanol production. This two-step process will not only contribute to the development of an integrated process for ethanol production from glucose-and xylose-containing biomass hydrolysates, but could also be used as an alternative method for ethanol production.

• 한국미생물·생명공학회지
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• 제21권4호
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• pp.373-380
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• 1993

When the cells of yeast K35 were immobilized in Ca-alginate gel, cell concentration and viability decreased as alginate concentration increased. Considering the results, 2% (w/v) Ca-alginate concentration would be suitable. Among various concentrations of additives and cross-lin-king agent, the addition of 1.67% (w/v) of bentonite together with 0.33% (v/v) of glutaraldehyde (ABG bead) resulted in the highest ethanol production of 1.8%(w/v), using YPD medium containing 2% glucose. ABG bead seemed to be more resistant to phosphate ion than Ca-alginate bead. 0.33%(w/v) of phosphate was a proper concentration for the ethanol production by ABG bead. Scanning electron microscopic observation depicted that the immobilized cells on the bead surface were coated by alginate gel and that the cells in the internal bead were cross-linked with alginate matrix. When repeated-batch culture was performed with ABG bead for 40 days in a packed-bed reactor, ethanol concentration of about 90~110 g/l-gel was maintained. Cell viability was maintained around 70%, and outgrowing cell concentration was below 6.3% of total cell concentration. Consequently, the results showed that ABG head was a potential carrier for continuous production of ethanol compared to conventional Ca-alginate bead.

• Applied Biological Chemistry
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• 제39권1호
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• pp.1-8
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• 1996

Saccharomyces cerevisiae의 고정화 및 현탁 세포로 구성된 연속식 생물반응기에서 에탄올 생성시 지질 첨가 영향을 연구하였다. 여러가지 배양조건하에서 에탄을 생산량 및 현탁 세포의 알코올 탈수소효소(alcohol dehydrogenase, ADH)의 비활성도를 측정하였다. 무통기 조건하에서 ergosterol과 oleic acid를 세포 배양액에 첨가하였을때, 에탄을 생산량과 균체 생육이 현저히 증가하였으나, 알코올 탈수소효소의 비활성도는 영향을 받지 않았다. 특히 무통기 조건 및 통기 조건하에서 얻어진 현탁 세포간의 알코올 탈수소효소의 비활성도는 차이가 없었다. 계면활성제 첨가시에도 에탄올 생성, 균체 생육, 알코올 탈수소효소의 비활성도가 크게 증가하였다. 고농도($40\;g/{\ell}$ 이상) 에탄올에 노출된 세포배양액에 ergosterol과 oletic acid 첨가시에도 에탄올 생성량, 균체 생육, 알코올 탈수소효소의 비활성도가 증가하였으나, 계면활성제 첨가시에는 효과가 없었다. 따라서, 지질 첨가효과는 저농도 에탄을 조건에 비해 고농도 에탄을 존재시 크게 작용하였다. 여러가지 매양조건에서 얻어진 현탁 세포의 알코올 탈수소효소의 isozyme patteren을 전기영동법에 의해 조사한 결과 ADH I으로 추정되는 한개의 isozyme만이 확인되었으며, isozyme의 이동거리는 세포의 배양조건에 따라 약간의 차이가 있었다. 에탄올 생성량과 알코올 탈수소효소의 비활성도사이의 상관관계는 성립되지 않았으며, 알코올 탈수소효소의 비활성도보다는 균체량이 에탄올 생성에 더 중요한 인자로 작용하였다.