• Journal of Plant Biotechnology
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• 제31권1호
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• pp.55-60
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• 2004

지황의 부정근을 이용한 기내묘 생산 체계를 확립하였다. 먼저 지황의 잎절편을 2 mg/L IBA혹은 2mg/L NAA를 첨가한 MS고체배지에 치상하여 부정근을 유도하였다. 고체배지에서의 효율적인 증식조건을 확인하기 위해 다양한 옥신 농도에 따른 배지에 부정근을 치상하여 4주간 배양한 후 증식된 부정근의 수와 길이를 측정한 결과 2mg/L IBA조건에서 최적의 생장을 보였다. 상기실험에서 확립된 부정근 증식조건을 이용하여 액체배양을 실시하였으며, 이를 액체 현탁배양하여 액체조건에서의 증식조건을 확립하였다. 또한, 2mg/L IBA가 첨가된 1/3 MS배지 조건에서 생물반응기에 10g의 부정근을 접종하여 6주간 암배양하여 255g의 부정근을 생산할 수 있었으며, 이렇게 생산된 부정근은 2mg/L BA가 첨가된 MS 고체배지에서 신초를 유도하였다. 신초들은 모두 정상적인 생육을 보이며, 식물체로 생장하였으며, 이들 식물체들은 토양으로 옮겨 순화되었다. 따라서 이러한 증식 체계를 이용하여 지황식물체의 대량증식체계를 확립하였다.

• Journal of Plant Biotechnology
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• 제35권2호
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• pp.155-161
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• 2008

본 연구는 더덕의 부정근 배양조건과 생물반응기를 이용한 대량생산 체계를 확립하고자 수행하였다. 먼저 기내 식물체를 이용하여 잎, 줄기와 뿌리로부터 부정근을 유도하였다. 부정근의 유도는 줄기에서 가장 높은 결과를 보였다. 또한, 오옥신 종류별 (NAA, IBA와 IAA) 처리시 절편당 부정근 유도수는 1.0 mg/L IBA에서 $9.9{\pm}1.2$개로 가장 양호 하였다. 그렇지만 유도된 부정근의 길이생장은 0.1 mg/L IBA에서 가장 활발하였다. 최적조건의 액체배지 조성을 선발하고자 생체중 0.2 g의 부정근을 각각 MS, 1/2 MS 및 1/3 MS 액체배지가 든 250 mL 삼각플라스크에 접종한 결과 1/2 MS 배지에서 가장 양호한 생장을 보였다. 액체배지조건에서 진탕배양된 더덕 부정근으로 5 L 용량의 공기부양식 생물반응기에 4주간 배양한 결과 1/2 MS에 1.0 mg/L IBA가 첨가된 배지에서 대조구에 비해 16배의 증식이 이루어졌다. 본 연구에서는 더덕 식물체를 이용하여 부정근을 유도 및 증식에 필요한 배양 조건을 조사하였고, 유도된 부정근을 공기부양식 생물반응기에서 대량증식 할 수 있었다.

• Journal of Microbiology and Biotechnology
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• 제24권12호
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• pp.1664-1672
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• 2014

In this study, a fibrous bed bioreactor (FBB) was used for $\small{D}$-lactic acid ($\small{D}$-LA) production by Sporolactobacillus inulinus Y2-8. Corn flour hydrolyzed with ${\alpha}$-amylase and saccharifying enzyme was used as a cost-efficient and nutrient-rich substrate for $\small{D}$-LA production. A maximal starch conversion rate of 93.78% was obtained. The optimum pH for $\small{D}$-LA production was determined to be 6.5. Ammonia water was determined to be an ideal neutralizing agent, which improved the $\small{D}$-LA production and purification processes. Batch fermentation and fed-batch fermentation, with both free cells and immobilized cells, were compared to highlight the advantages of FBB fermentation. In batch mode, the $\small{D}$-LA production rate of FBB fermentation was 1.62 g/l/h, which was 37.29% higher than that of free-cell fermentation, and the $\small{D}$-LA optical purities of the two fermentation methods were above 99.00%. In fe$\small{D}$-batch mode, the maximum $\small{D}$-LA concentration attained by FBB fermentation was 218.8 g/l, which was 37.67% higher than that of free-cell fermentation. Repeate$\small{D}$-batch fermentation was performed to determine the long-term performance of the FBB system, and the data indicated that the average $\small{D}$-LA production rate was 1.62 g/l/h and the average yield was 0.98 g/g. Thus, hydrolyzed corn flour fermented by S. inulinus Y2-8 in a FBB may be used for improving $\small{D}$-LA fermentation by using ammonia water as the neutralizing agent.

• 한국산학기술학회논문지
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• 제12권7호
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• pp.3341-3352
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• 2011

본 연구는 간헐적으로 공장폐수가 유입되고 있는 하수처리시설에 대하여 각 단위공정별 운전현황 조사와 수질 측정을 실시하여 운전특성을 파악하고자 하였다. 생물반응조의 운전조건은 MLSS 농도 2,000~3,000 mg/L, HRT 5.3~16.3 시간, SRT 2.8~66.6 일 범위를 나타내었고, SVI는, 최적 범위인 50~150을 상회하여, 200 이상의 측정값이 빈번히 발생하여 슬러지 침강성이 양호하지 않은 것으로 관측되었다. 주요 원인은 공장폐수의 유입에 기인한 것으로 판단되며, 이와 같이 공장폐수 유입 시 생물반응조내의 MLDO가 급격히 상승하고 질산화 효율이 빠르게 감소하며 이차침전지에서는 Pin floc.이 유출되는 현상이 발생하였다. 미생물 관측결과, 다양한 세균 플록과 섬모충류 등이 관측되었으나, Bulking 발생의 원인이 되는 사상균인 Sphaeotilus와 방선균 등도 발견되었다. 단위공정별 처리효율은 평균적으로는 대체로 양호한 처리효율을 나타내고 있었으나 간헐적인 공장폐수 유입의 영향으로 인한 생물반응조의 운전특성의 불안정성으로, 처리효율의 변동성이 크게 나타나고 있었다.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 춘계학술발표대회
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• pp.402-405
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• 2000

Batch culture system and continuous culture system were used to investigate the removal of disperse dye using several white rot fungi. White rot fungi used in the study were Coriolus hirsutus IFO 4917, Lenzites betulina IFO 6266, Coriolus versicolor IFO 30340 and Phanerochaete chrysosporium IFO 31249. The results of the batch culture experiment showed that white rot fungi used in this study had excellent dye removal abilities. Phanerochaete chrysosporium IFO 31249 was especially effective on the removal of disperse dyes. And continuous treatment of disperse red-60 was studied under bioreactor with vertical matrix using Phanerochaete chrysosporium IFO 31249. The removal efficiency of disperse red-60 were more than 95% in 0.20 ${\sim} 1.50 $hr^{-1}$ dilution rate and 90% in $1.83h^{-1}$ dilution rate.

• Journal of Microbiology and Biotechnology
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• 제2권1호
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• pp.41-45
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• 1992

Shikonin production was examined in a bubble column bioreactor system with the hairy roots of Lithosphermum erythrorhizon. The volumetric productivity was higher than those obtained from other reactor configurations with free or immobilized cells of the same cell line. The productivities of the bubble column reactor, with and without a product absorption trap, were 7.4 and 4.5 mg of shikonin/l/d, respectively. This indicated the importance of the product removal in the design and operation of the shikonin production system with hairy root culture.

• 한국고분자학회:학술대회논문집
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• 한국고분자학회 2006년도 IUPAC International Symposium on Advanced Polymers for Emerging Technologies
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• pp.259-259
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• 2006

PAU is the block copolymer consists of a small amount of a small amount of poly(${\gamma}-methyl-L-glutamate$) (PMLG) and the polyurethane. The urethane segments are hydrophobic and then strongly interact with the other hydrophobic materials such as PTFE, and the PMLG segments with the ${\alpha}-helix$ structure possess the cytocompatibility. Therefore, PAU can be easily coated onto the PTFE fiber and acts as an artificial extracellular matrix with the high cytocompatibility Results shows, the immobilization, cultured and functions of porcine hepatocytes is greatly improved.

• 한국막학회:학술대회논문집
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• 한국막학회 1998년도 추계 총회 및 학술발표회
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• pp.150-152
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• 1998

Now the lack of water is serious problem all over the world because of the growth of population and expansion of industrial activities. So wastewater recycle and reuse is essential in many countries. One of the most popular wastewater treatment processes is conventional activated sludge system. In spite of significant degree of treatment rate the biological process has some operational difficulties and capital disadvantages. In conventional activated sludge process, sludge settling condition is getting worse in case of sludge bulking, it is common that overall process fails due to wash-out of biomass causing low concentration of MLSS in the aeration tank. Because of the absence of claifier the membrane bioreactor(MBR) process is less affected by such problems.

• 상하수도학회지
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• 제22권3호
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• pp.367-372
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• 2008

This study configured the conventional $A^2O$ (Anaerobic-Anoxic-Aerobic bioreactor) system which the fixed media immersed into the anoxic reactor(Named PFR system : Plug Flow Reactor) for evaluating the removal efficiency of nitrogen in the wastewater. The experimental equipment was a cylinder which was consist of 4 pleated PE Pipes(Length 330M, Diameter 100mm) including 2 rope shape media. As a result, the average effluent T-N removal efficiency of the conventional $A^2O$ system was 17.9, 40.3, 50.6, 44.6% in each mode, but the average effluent T-N removal efficiency of the PFR system could achieve 38.8, 57.1, 71.8, 65.4% in each mode. It indicated that the PFR system caused to the increasing of C/N ratio that effected to the increasing of the denitrification efficiency. Not only the effective T-N removal efficiency but also the controllable install space will give advantages for retrofitting of the wastewater treatment plant with the conventional treatment system to the PFR system.

• Biotechnology and Bioprocess Engineering:BBE
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• 제2권2호
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• pp.77-81
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• 1997

Removal of nitrogen compound from waste water is essential and often accomplished by biological process. To prevent washout and to develop an efficient bioreactor, immobilization of sutibal microorganisms could be sensible approach. Strains and permeabilized cell encapsulated in cellulose nitrate microcapsules and immobilized on polystyrene films were prepared by the method described in the previous study. In the wastewater treatment system, nitrification of ammonia component is generally known as rate controlling step. To enhance the rate of nitrification, firstly nitrifying strains Nitrosomonas europaea(IFO14298), are permeabilized chemically, and immobilized on polystyrene films and secondly oxidation rates of strain system and permeabilized strain system are compared in the same condition. with 30 minute permeabilized cells, it took about 25 hours to oxidize 70% of ammonia in the solution, while it took about 40 hours to treat same amount of ammonia with untreated cells. All the immobilization procedures did not harm to the enzyme activity and no mass transfer resistance through the capsule well was shown. In the durability test of immobilized system, the system showed considerable activity for the repeated operation for 90 days. With these results, the system developed in this study showed the possibility to be used in the actual waste water treatment system.