• KSBB Journal
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• 제14권2호
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• pp.181-187
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• 1999

젖산 생산에 큰 비중을 차지하는 원료비용 절감을 위한 다양한 공업적 질소원의 이용 가능성을 조사하였다. CSL를 사용하여 회분 발효한 결과, CSL 5%배지 발효시 높은 생산성을 보였으며, 정제 CSL을 사용한 배지에서 젖산 생산성은 CSL보다 약 1.21 배 증가율을 보였다. Yeast extract와 CSL 혼합질소원의 배지조성을 변화시켜 LBM5의 젖산 생성정도를 알아본 결과, 조성 비율 1:8일 때 우수한 발효율을 관찰 할 수 있었다. 발효 폐기물의 대체 질소원 사용가능성을 조사하기 위하여 맥주공장에서 부산물로 배출되는 폐효모를 이용하여 발효시에도 CSL 5%와 비슷한 발효율을 얻었다 연속발효 수행결과, 최적의 희석율은 0.05-0.065-1h였으며 젖산 생산성에 있어서 회분발효보다 1.93.0배증가하였다. 한편 초기 순수배지에 들어가는 yeast extract양의 1/3-2/3를 발효폐액에 첨가하여 회분발효 및 연속발효 실험을 수행하여 높은 젖산 생산성을 얻으므로써 공정상 원료비 절감효과를 기대할 수 있어으며 잔류 영양분을 재사용함으로써 폐액량 감소에 따른 처리비용 절감이라는 이중적인 효과를 얻게 되었다.

• KSBB Journal
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• 제5권2호
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• pp.159-165
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• 1990

Ethanol fermentation by Scccharomyces cervisiae was carried out in the cell recycle filter system with a cheap fabric filter having a pore size of 10${\mu}$m. Maximum biomass concentrations up to 85g/1 were obtained, but in practice operational concentrations were between 50 and 80g/1. Ethanol productivity was 42g/1-hr, with an ethanol concentration of 66g/1 and an ethanol yield of over 86%. Continuous operation was possible by applying periodic backflushing. The ethanol fermentation could be carried out without difficulty at a dilution rate up to 0.8h-1 In order to obtain a high cell concentration and ethanol productivity, development of filter module with the larger filtration area is required.

• Biotechnology and Bioprocess Engineering:BBE
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• 제7권6호
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• pp.357-361
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• 2002

Continuous production of lactic acid from glucose by Lactobacillus rhamnosus with cell recycling using an acoustic cell settler was carried out. The performance of the system, such as the concentration of cell and product were compared with the control experiment without recycling. The acoustic settler showed cell separation efficiency of 67% during the continuous operation and the cell concentration in the fermentor with recycle exceeded that of the control by 29%. Com-pared with the control, tactic acid production was increased by 40%, while glucose consumption was only increased by 8%. The higher value of lactic acid production to substrate consumption (Yp/s, product yield coefficient) achieved by cell recycling is interpreted to indicate that the recycled cell mass consumes less substrate to produce the same amount of product than the control Within system environmental changes due to the longer mean cell residence time induced the cells maintaining the metabolic pathways to produce Less by-Product but more product, lactic acid.

• 상하수도학회지
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• 제27권4호
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• pp.489-494
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• 2013

Effects of operating parameters such as hydraulic retention time(HRT), recycle ratio and influent COD concentration on the performance of a continuous flow microbial fuel cell(MFC) were investigated. Decrease of HRT improved mass transfer of substrate to electrogenic microorganisms, therefore resulting in increased electrode voltage and power generation of MFC. Increase of HRT promoted COD removal by elongating retention time for COD removal in MFC. Recycling of effluent increased the COD removal and coulombic efficiencies by returning suspended microorganisms into MFC. Increase of influent COD enhanced COD removal due to the improved mass transfer of substrate. Decrease of coulombic efficiency by the increase of the HRT and influent COD concentration indicated that they enhanced the activities of fermentative bacteria.

• KSBB Journal
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• 제14권4호
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• pp.445-451
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• 1999

E. coli TGI/pDG7 $\alpha$ 와 빵효모의 혼합세포계에 의한 글루타치온 생산을 Aerated Slurry Bioreactor에서 수행하였다. 글루타치온 생산 효소는 34시간 동안 안정성을 보였으며, 글루타치온 수율은 4.6 mM을 유지함을 보였다. 고농도의 혼합세포를 이용한 Aerated Slurry Bioreactor에서 기질의 공급속도가 글루타치온 생산에 미치는 영향을 조사하였다. 세포가 회수되어 기질공급속도 5.2 mL/hr에서 글루타치온의 생산농도는 32시간에서 현탁반응보다 낮아짐을 보였고, 반면 세포가 회수되지 않은 기질공급속도 5.2 mL/hr에서는 22시간 동안 유지되었고 2.6 mL/hr에서는 42시간 동안 유지되었다. 글루타치온의 생산성은 기질공급속도가 10.4 mL/hr에서 25.7 mg/g wet $cell{\cdot}hr$이었으나, 2.6 mL/hr에서는 1.65 mg/g wet $cell{\cdot}hr$이었고 5.2mL/hr에서는 5.28 mg/g wet $cell{\cdot}hr$이었다. 계면활성제(Tween 80)을 사용한 경우, 글루타치온 생산시간을 25시간에서 45시간으로 연장되었다. 글루타치온 생산있어 산소가 세포계의 효소에 산소에 의해 영향을 미칠 것으로 판단되었고, 공기를 질소로 교체하여 글루타치온 생산시간을 40시간으로 연장시켰다.

• 한국미생물·생명공학회지
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• 제22권3호
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• pp.277-282
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• 1994

In batch cultures of Lactobacillus delbrueckii, cell growth and lactic acid production were affected by two main factors, inhibition by lactic acid and limitation by nutritional components. In order to increase th productivity significantly, a continuous stirred tank reactor with cell recycle was employed. A cell desnity of 145g dry weight/l and a volumetric productivity of 73 g/l$\cdot $h were obtained with an effluent concentration of 85 g/l lactic acid. The productivity achieved by this system was 23-fold higher than those obtained by the corresponding batch cultivations. Once the lactic acid concentration reached the steady steady state, lowering the yeast extract concentration caused the reduction of the lactic acid concentration without affection the biomass concentration. Finally, the formation of D-lactate was investgated. During the various cultures, a small amount of D-lactate always formed, even thought a majority of lactate was L-isomer, It was supposed that the relative amount of the D-lactate was affected by glucose limitation, and there seems to exist a certain relationship between the concentration of D-lactate and acetate.

• Biotechnology and Bioprocess Engineering:BBE
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• 제10권3호
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• pp.284-288
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• 2005

Baker's yeast was disrupted in a 1.4-L stainless steel horizontal bead mill under a continuous recycle mode using 0.3 mm diameter zirconia beads as abrasive. A single pass in continuous mode bead mill operation liberates half of the maximally released protein. The maximum total protein release can only be achieved after passaging the cells 5 times through the disruption chamber. The degree of cell disruption was increased with the increase in feeding rate, but the total protein release was highest at the middle range of feeding rate (45 L/h). The total protein release was increased with an increase in biomass concentration from 10 to $50\%$(w/v). However, higher heat dissipation as a result of high viscosity of concentrated biomass led to the denaturation of labile protein such as glucose 6-phosphate dehydrogenase (G6PDH). As a result the highest specific activity of G6PDH was achieved at biomass concentration of $20\%$(ww/v). Generally, the degree of cell disruption and total protein released were increased with an increase in impeller tip speed, but the specific activity of G6PDH was decreased substantially at higher impeller tip speed (14 m/s). Both the degree of cell disruption and total protein release increased, as the bead loading increased from 75 to $85\% (v/v)$. Hence, in order to obtain a higher yield of labile protein such as G6PDH, the yeast cell should not be disrupted at biomass concentration and impeller tip speed higher than $20\%(w/v)$ and 10 m/s, respectively.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2001년도 추계학술발표대회
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• pp.541-544
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• 2001

One of the most promising TCE treatment systems is trickling biofilter (TBF), in which monooxygenase, the corresponding enzyme for initiating growth substrate oxidation, fortuitously transforms TCE via cometabolism. TCE. however. is not easily treated by simple cometabolic biotransformation. This is mainly due to the toxicity of TCE to microbial cell and monooxygenase. In this study, we cleveloped and operated a two-stage CSTR/TBF system for the long-term continuous treatment of TCE. In the two-stage biotransfon11ation system, CSTR with cell recycle from TBR was coupled to the TBR for the reactivation of the cells deactivated during TCE degradation.

• KSBB Journal
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• 제16권5호
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• pp.511-515
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• 2001

TCE및 TCE 분해산물의 높은 독성으로 인하여 TCE 분해 효소 및 세포 불활성화가 일어나서 장기간 안정되게 반응기 운전이 어렵다는 단점을 극복하고, TCE와 성장기질사이의 경쟁적 저해관계로 인한 처리효율 감소도 막기 위하여 TCE분해단계와 세포 및 효소 재활성화 단계를 구분시킨 2단계 CSTR/TBF 시스템을 개발하였다. B. ceapcia G4를 분해 미생물로 사용하였으며, 탄소원인 phenol과 공기 및 배지가연속적으로 공급되는 CSTR에서 효소 및 세포 재활성를 도모하고, TBF에서는 폐가스에 포함된 기사의 TCE를 공기와 함께 공급하여 B. cepcia G4 미생물막에의한 TCE가 분해되도록 구성하였다. 2단계 CSTR/TBF 시스템은 유입 TCE 농도가 15pp $m_{v}$까지도 100% 수준의 처리 효율을 보여주었으며, 고농도의 TCE를 안정적으로 장기간 처리할 수 있었다.다.

• KSBB Journal
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• 제19권6호
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• pp.484-488
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• 2004

본 연구에서는 식품부산물을 원료로 사용하여 회분식 발효를 통한 Propionibacterium acidipropionici의 유기산 생산성을 검토하고 세포재순환식 연속발효를 통해 유기산의 대량생산을 위한 기초자료를 마련하고자 하였다. CSL의 함유량에 따른 회분식 발효를 실시하여 균주의 생산성이 최대가 되는 발효조건을 구하여 연속 발효공정에 적용하였다. 희석률을 $0.1{\sim}0.2\;hr^{-1}$로 변화시키며 세포재순환식 연속발효를 실시한 결과 $0.2\;hr^{-1}$에서 최대 세포량은 150 g drycell/L으로 회분식 발효에 비해 21배 증가하였으며, 유기산의 최대 생산성은 3.32 g total acids/L/h로서 13배가 향상된 것으로 나타났다. 따라서 이 발효공정을 scale-up한다면 유기산뿐만 아니라 바이오매스 자원으로서 세포량의 대량생산도 가능할 것으로 판단된다.