• KSBB Journal
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• 제24권1호
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• pp.89-95
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• 2009

Biodiesel (fatty acid alkyl esters), which is produced from sustainable resources such as vegetable oil, animal fat and waste oils, have used to as substitutes for petro-diesel. In this study, we investigate the performance of 30 L and 300 L pilot-scale biodiesel production system using alkali-catalyst transesterification from soybean oil and rapeseed oil produced at Jeju island in Korea. The 30 L-scale biodiesel production was performed to in the condition of reaction temperature $65^{\circ}C$, catalyst amount 1% (w/w) and oil to methanol molar ratio 1 : 8. At that reaction condition, the fatty acid methyl ester contents of product are above 98% within reaction time 30 min. Also, the conversion yield of over 98% was obtained in 300 L-scale biodiesel production system using rapeseed oil and soybean oil. The quality of biodiesel produced from reaction system was satisfied to recommended quality standard of Korea. Our results may provide useful information with regard to the scale-up of more economic and efficient biodiesel production process.

• KSBB Journal
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• 제24권3호
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• pp.303-311
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• 2009

Bi-staged pH process 하의 jar fermenter system에서 영지의 액체배양 시 효율적인 균사체 및 세포의 다당 생산을 위한 용존산소의 영향을 조사하고, 산소이동용량계수와 발효조 조작변수와의 상관관계를 해석하여 scale up의 조건을 검토, 확립하였다. 교반속도에 따른 용존산소의 농도변화를 살펴본 결과, hi-staged pH process에서 배양 $2{\sim}4$일에 용존 산소의 급격한 감소를 보였으나 용존 산소의 제한은 일어나지 않고, 다시 증가하는 경향을 보였으며, 교반속도가 증가할수록 감소 폭과 깊이는 증가하는 경향을 보였다. 다당 생성은 대수 증식기 이후의 용존 산소농도가 $40{\sim}80%$ 범위일 때 가장 높았으며, 이 보다 낮거나 높은 경우 다당의 생성은 저해되었다. 교반 및 통기에 따른 산소이동용량계수 ($k_La$)와 통기속도 (Vs), 교반속도 (N) 및 impeller 지름 (Di)의 자료로부터 중회귀분석한 결과, 이들 사이의 관계는 다음 식으로 표현할 수 있었다. $$k_La=0.555{\times}Vs^{0.42}{\times}(N^3{\times}Di^2)^{0.33}\;(R^2=0.925,\;p<0.05)$$ 2.6 L 발효조의 경우, 15.43 g/L의 최대 다당 생산량은 400 rpm 및 1 vvm에서 얻어졌으며, 2.6 L 발효조의 최적 산소이동용량계수 값을 적용한 20 및 75 L 발효조에서의 scale up 시험 결과는 서로 잘 일치하였다. 최대의 다당생성을 위한 산소전달계수의 감은 $85.4{\pm}26.70\;h^{-1}$이었다.

• Journal of Microbiology and Biotechnology
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• 제2권2호
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• pp.98-101
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• 1992

Continuous production of fructo-oligosaccharides employing a packed bed reactor charged with immobilized cells of Aureobasidium pullulans was investigated. The optimum conditions for reactor operation were a feed concentration of 860 g/l; a feed rate, expressed as superficial space velocity of $0.2\;h^{-1}$, and a temperature of $50^\circ{C}$. Under these optimum conditions, the productivity of the reactor was $180\;g/l\cdot{h}$. Initial activity was maintained for more than 100 days. The reactor was successfully scaled up to a production scale of 1000l.

• KSBB Journal
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• 제21권2호
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• pp.103-109
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• 2006

H. erinaceum의 기능성 소재화 연구의 일환으로, 지금까지 체계적으로 연구된 바 없는 H. erinaceum의 액체배양을 시도하고. 이 버섯의 서로 다른 생물반응기하의 액체배양 특성을 규명하고 대량생산을 검토하였다. 5 L 용량의 jar fermenter와 air-lift fermenter에서의 액체배양의 비교실험을 통해 air-lift fermenter의 사용이 종균 배양에 적합한 것으로 나타났으며, 형태 분석을 통해 적정 크기($2{\sim}4mm$)의 pellet 형태의 유지가 대량 생산의 중요인자인 것을 규명하였다. Air-lift fermenter 하의 배양을 종균으로 하고, 적정 크기의 pellet을 유지하는 500 L까지의 jar fermenter를 사용한 회분 배양의 scale-up 실험결과, 30 및 500 L에서의 교반 및 통기속도는 각각 200 rpm, 1 vvm 및 150 rpm, 1 vvm이었다. 이 조건하에서 배양의 전 기간 중 적정 pellet을 유지하였으며, 최대 균사체량은 약 $13{\sim}14g/L$이었다.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2005년도 생물공학의 동향(XVII)
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• pp.123-123
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• 2005

• 멤브레인
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• 제2권2호
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• pp.122-128
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• 1992

여러 크기의 이중실관 생물 반응기에서의 Aspergillus niger(KCTC 1232)를 이용한 구연산 생산 실험을 수행하였다. 초종 세포농도는 세포 성장구간 기준으로 300g/l에 달하였다. 공기와 산소의 공급 조건하에서의 단위 용적당의 생산성은 각각 0.63, 0.02g/l.h였고 이는 회분식 발효에 대해 10, 16배 증가한 결과이다. 공급배지의 초기 pH는 구연산의 생산에 중요한 요소이며 pH가 낮을수록 높은 구연산 생산수율을 얻을 수 있었다. Scale-up의 가능성을 알아보기 위해 반응기 unit와 배지의 공급속도를 변화시킨 결과 반응기 unit와 배지 공급속도의 증가는 기질의 높은 소비속도로 인해 생산성의 증가를 가져왔다.

• Fisheries and Aquatic Sciences
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• 제25권10호
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• pp.525-536
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• 2022

Photosynthetic bacteria (PSB) attract considerable interest as useful microorganisms; nevertheless, a generalized culture technique has not been previously reported owing to difficulty in their cultivation. Therefore, a simple culture technique suitable for public use was investigated. Among the PSB tested, the strain Rhodobacter azotoformans EBN-7 was the most suitable for scale-up production because it showed the highest specific growth rate (0.20 h^-1) on basal medium. In scale-up cultivation (500 L), R. azotoformans EBN-7 showed 4.50 × 10¹⁰ colony-forming units mL^-1 (number of viable cells), dry cell weight of 26.8 g/L, and a specific growth rate of 0.15 h^-1. Cultivation using this final culture broth (as seed culture) in a 15 L simple reactor was successful, with maintenance of cell activity evident. For use as seed culture, the maximum allowable preservation period of R. azotoformans EBN-7 at 4℃ was 3 months. When R. azotoformans EBN-7 cultivated in a simple technique was applied to shrimp aquaculture water, NH₄⁺-N was reduced from 0.61 mg/L to 0.24 mg/L (by 60.7%) in 4 days in comparison with the control. Thus, this simple culture technique using R. azotoformans EBN-7 has the potential for a good removal efficiency of NH₄⁺-N, making seed culture easier and suitable for public use.

• Biotechnology and Bioprocess Engineering:BBE
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• 제9권4호
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• pp.274-277
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• 2004

Production of green fluorescent protein (GFP) as a model foreign protein using different culture scales under co-expression of Vitreoscilla hemoglobin (VHb) in the industrial Escherichia coli strain W3110 (a K12 derivative), was examined. It was found that the VHb co-expressing W3110, exhibited an exceptional and sustained production ability during cell cultures using different scales, while the VHb non-expressing strain showed variable production levels. This high and sustained production ability indicates that the VHb co-expressing E. coli W3110, could be successfully employed for practical large-scale production cultures without the need for serious consideration of scale-up problems.

• Biotechnology and Bioprocess Engineering:BBE
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• 제5권2호
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• pp.118-122
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• 2000

A comlementary call line CR2 is curretly used to propagte the Disabled Infectious Single Cycle Herpes Simplex Virus Typee2 (DISC HSV-2) on a small Iaboratory scale upto 15 L. These cultures are initiated by passaging the cells from roller bottle cultures. Whilst this is suitable for the laboratory scale it is totally impractical for use in seeding an industrial manufacturing scaled version of the culture. It is paramount to have a robust system for passaging cells from a small microcarrierier culture system to a larger one by a serial subculturing regime. Here we report on the successes we have had in our laboratory in scaling up out production system for the DISC HSV-2 from small 1-L cultures to a 50-L vessel with the maintenance of the viral productivity. Ease of use, reproducibility and the need to minimise overall production time were factors which were taken into consideration whils developing our procedures. We were aware of the need to keep a production train simple and as short as possible as this was the amall scale study for an envisaged manufacturing process.

• Bulletin of the Korean Chemical Society
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• 제24권3호
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• pp.397-399
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• 2003