• KSBB Journal
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• 제5권2호
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• pp.167-173
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• 1990

Acetobacter aceti OLS-130cell을 Ca-alginate gel에 고정시킨 후 유동층 반응기를 이용한 연속적인 식초생산 가능성을 검토하였다. Working volume 2L규모의 유동층 반응기를 사용한 회분식발효를 발효온도 3$0^{\circ}C$, 통기량 1.0VVM에서 초기 ethanol 및 초산농도 3g/l와 27g/l에서 수행한 결과 free cell인 경우 발효 80시간 경과 후 23g/l의 초산이 생성되었으며, 이때 overall productivity는 0.31g/l-hr였고, 고정화 초산균의 bead를 250g/l로 하여 발효를 수행한 결과는 발효 48시간 경과 후 23g/l의 초산이 생성되어 overal productivity는 0.48g/l-hr로서 free cell일 때보다 약 1.5배 높았다. 위의 초산발효조건에서 배양 48시간 이후부터 연속발효를 실시한 결과 배양 90일까지 초산함량 50~55g/l의 식초를 연속적으로 생산하는 것이 가능하였으며, 이때 dilution rate는 $0.12hr^-1$로서 초산생산성은 약 2.76g/l-hr로 최대값을 유지하였으며 회분식 발효에서 free cell인 경우보다는 초산생산성이 약 8.9배, 고정화 세포인 경우보다 약 5. 8배 더 높았다.

• Environmental Engineering Research
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• 제19권3호
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• pp.283-287
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• 2014

Cultivation of microalgae using wastewater exhibits several advantages such as nutrient removal and the production of high valuable products such as lipid and pigments. With this study, two types of wastewater from instant noodle factory; mixed liquor suspended solids (MLSS) and effluents after sedimentation tank were investigated for green microalga Scenedesmus sp. cultivation under laboratory condition. Optimal wastewater dilution percentage was evaluated in 24 wells microplate. MLSS and effluent without dilution showed the highest specific growth rate (${\mu}$) of $1.63{\pm}0.11day^{-1}$ and $1.57{\pm}0.16day^{-1}$, respectively, in which they were significantly (p < 0.05) higher than Scenedesmus sp. grown in BG11 medium ($1.08{\pm}0.14day^{-1}$). Ten days experiment was also conducted using 2000 ml Duran bottle as culture vessel under continuous light at approximately 5000 lux intensity and continuous aeration. It was found that maximum biomass density of microalgae cultivated in MLSS and effluent were $344.16{\pm}105.60mg/L$ and $512.89{\pm}86.93mg/L$ respectively and there was no significant (p < 0.05) difference on growth to control (BG11 medium). Moreover, cultivation microalgae in wastewater could reduce COD in wastewater by 39.89%-73.37%. Therefore, cultivation of Scenedesmus sp. in wastewater from instant noodle factory can yield microalgae biomass production and wastewater reclamation using photobioreactor simultaneously.

• 한국응용약물학회:학술대회논문집
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• 한국응용약물학회 2006년도 Proceedings of The Convention
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• pp.127-130
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• 2006

Coenzyme Q10(CoQ10) is a biological quinine compound that is widely found in living organisms including yeast, plants, and animals. CoQ10 has two major physiological activities:(a)mitochondrial electron-transport activity and (b )antioxidant activity. Various clinical applications are also available: Parkinson's disease, Heart disease, diabetes. Because of its various application filed, the market size of CoQ10 is continuously expanding all over the world. A Japanese company, Nisshin Pharma Inc. is the first industrial producer of CoQ10(1974). CoQ10 can be produced by fermentation and chemical synthesis. In several companies, these two methods are used for the production of CoQ10:chemical synthesis - Yungjin, Daewoong, Nishin Parma; fermentation - Kaneka, Kyowa, Yungjin, etc. Researchs in microbial production of CoQ10 have several steps: screening of producing microorganisms, strain development, fermentation process, purification process, scale-up process, plant production. Several strategies are available for the strain development : Random mutation and screening, directed metabolic engineering. For the optimization of fermentation process, various conditions (nutrient, aeration, temperature, culture type, etc.) are considered. Purification is one of the most important step because the quality of final products entirely depends on its purity. The production cost will be reduced and the quality of the CoQ10 will be impoved by continuous researches in strain development, fermentation process, purification process.

• Biotechnology and Bioprocess Engineering:BBE
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• 제7권4호
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• pp.234-236
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• 2002

A process for the production of mannitol from fructose (5% to 25%) using Leuconostoc mesenteroides NRRL B-1149 was investigated. Fermentations were carried out In batch or fed-batch fermentations without aeration at 28$\^{C}$, pH 5.0. When 5% fructose was used In batch culture fermentation, the yield of mannitol was 78% of that expected theoretically. When the frurtose concentration was Increased to 10%, the yield dropped to 59.6% of the theoretical value. However, In the fed-batch culture, using 10% fructose, the yield was 81.9% of the theoretical value. In a 15% fruttose fed-batch culture, with 5% fructose being added initially and the other 10% fructose being added as a continuous supply the final yield was 83.7% of the theoretical yield. When 20% fructose was used In the same manner, the yield was 89.5% of theoretical yield.

• 한국미생물·생명공학회지
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• 제20권6호
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• pp.663-667
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• 1992

산업적으로 산도 17.0 이상의 고산도 시초를 생산하기 위하여 반연속식인 1st stage와 유가식인 2nd stage로 구성된 two stage 초산 발효를 온도 $30^{\circ}C$, 교반속도 600rpm, 통기량 0.1vvm에서 실시하였다. 1st stage에서 초기 에탄올 농도를 $50.0g/{\ell}$, 잔류 에탄올 농도를 $5.0g/{\ell}$로 정하여 반연속적으로 초산발효를 하고, 2nd stage에서 발효시간의 경과에 따라 에탄올을 유가식으로 첨가하여 초산발효액내의 에탄올 농도를 $5.0g/{\ell}$에서 $10.0g/{\ell}$로 유지했을 때 산도가 17.6인 고산도 식초를 생산 할 수 있었으며, 또한 이때의 최대 초산 생산성은 $3.3g/{\ell}{\cdot}hr$였다.

• 한국약용작물학회:학술대회논문집
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• 한국약용작물학회 2006년도 Proceedings of The Convention of The Korean Society of Applied Pharmacology
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• pp.127-130
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• 2006

Coenzyme Q10(CoQ10) is a biological quinine compound that is widely found in living organisms including yeast, plants, and animals. CoQ10 has two major physiological activities:(a)mitochondrial electron-transport activity and (b)antioxidant activity. Various clinical applications are also available : Parkinson's disease, Heart disease, diabetes. Because of its various application filed, the market size of CoQ 10 is continuously expanding all over the world. A Japanese company, Nisshin Pharma Inc. is the first industrial producer of CoQ10(1974). CoQ10 can be produced by fermentation and chemical synthesis. In several companies, these two methods are used for the production of CoQ10:chemical synthesis - Yungjin, Daewoong, Nishin Parma; fermentation - Kaneka, Kyowa, Yungjin, etc. Researchs in microbial production of CoQ10 have several steps: screening of producing microorganisms, strain development, fermentation process, purification process, scale-up process, plant production. Several strategies are available for the strain development : Random mutation and screening, directed metabolic engineering. For the optimization of fermentation process, various conditions (nutrient, aeration, temperature, culture type, etc.) are considered. Purification is one of the most important step because the quality of final products entirely depends on its purity. The production cost will be reduced and the quality of the CoQ10 will be impoved by continuous researches in strain development, fermentation process, purification process.

• Preventive Nutrition and Food Science
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• 제2권1호
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• pp.66-70
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• 1997

A mixed-culture of Gluconobacter suboxydans IFO 3172 and Saccharomyces uvarum IFO 0751 was per-formed in a synthetic medium. the optimal inculum ratio of G. suboydans and S. uvarum for mixed-culture fermentation was 150:1. The optimum pH, incubation temperature and aeration rate for mixed-culture fer- mentation were 5.0, 3$0^{\circ}C$ and 2.25vvm, reapectively. As a result of batch pure-and mixed-culture fer-mentation, specific growth rate in pure-culture of both strain was lower than that in mixed-culture. The yield of cell mass from S. uvarum exclusively decreased. The growth rate of the mixed-culture was very similar to the pure-culture in the begining of culture, but it has been decreased after 16hrs. In the mean time, S. uvarum in mixed-culture fermentation could grow due to fructose converted, but it could not row in pure-culture fermentation. Thus, the relationship was a sort of commensalism. The kinetic parameters cal-culated through steady-state results during continuous fermentations are as follows :{TEX}$$\mu$_{max1}${/TEX}=0.118({TEX}$h^{-1}${/TEX}), {TEX}$Ks_{1}${/TEX}=0.330(g/L),:{TEX}$$\mu$_{max2}${/TEX}=0.162({TEX}$h^{-1}${/TEX}), {TEX}$Ks_{2}${/TEX}=0.038(g/L). The yield of bacterial cell mass relatively constant, but yield of yest cell mass was gradually decreased.

• 한국미생물·생명공학회지
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• 제20권3호
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• pp.348-354
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• 1992

SUC2 유전자를 가진 재조합 Saccharomyces cerevisiae의 invertase 생산성을 향상시키기 위하여 균체 생육과 유전자 발현에 미치는 아미노산과 용존산소 농도의 영향을 연구하였다. 균체 생육과 invertase 발현에 적합한 leucine과 histidine의 최적 첨가량은 탄소원인 포도당에 대한 비율로서 나타내어 0.03g/g glucose와 0.04g/g glucose였다. 회분배양에서는 통기량이 적을수록 invertase 비활성이 증가하였다. 희석율 0.09h에서 용존산소농도를 조절한 연속배양에서는 요존산소농도가 감소함에 따라 유전자 발현이 잘되어 5 포화 이하일때 invertase 비활성이 급격히 증가하여 통기를 하지 않은 조건에서 125.54KU/g cell의 최고 비활성을 얻었다.

• 한국환경과학회지
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• 제25권11호
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• pp.1541-1554
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• 2016

To understand the characteristics of vanadium leaching from soils formed by the weathering of basalts, paleo soil at Gosan, Jeju Island, Korea, and several present-day soils from neighboring areas were collected. Leaching experiments were carried out by two approaches: 1) batch experiments under various geochemical conditions (redox potential (Eh) and pH) and 2) continuous leaching experiments under conditions similar to those of natural environments. From the batch experiments, leached vanadium concentrations were highest under alkaline (NaOH) conditions, with a maximum value of $2,870{\mu}g/L$, and were meaningful (maximum value, $114{\mu}g/L$) under oxidizing ($H_2O_2$) conditions, whereas concentrations under other conditions (acidic-HCl, $neutral-NaHCO_3$, and $reducing-Na_2S_2O_3$) were negligible. This indicated that the geochemical conditions, in which soil-water reactions occurred to form groundwater with high vanadium concentrations, were under alkaline-oxidizing conditions. From the continuous leaching experiments, the pH and leached vanadium concentrations of the solution were in the ranges of 5.45~5.58 and $6{\sim}9{\mu}g/L$, respectively, under $CO_2$ supersaturation conditions for the first 15 days, whereas values under $O_2$ aeration conditions after the next 15 days increased to 8.48~8.62 and $9.7{\sim}12.2{\mu}g/L$, respectively. Vanadium concentrations from the latter continuous leaching experiments were similar to the average concentration of groundwater in Jeju Island ($11.2{\mu}g/L$). Furthermore leached vanadium concentrations in continuous leaching experiments were highly correlated with pH and Al, Cr, Fe, Mn and Zn concentrations. The results of this study showed that 1) alkaline-oxidizing conditions of water-rock (soil) interactions were essential to form vanadium-rich groundwater and 2) volcanic soils can be a potential source of vanadium in Jeju Island groundwater.

• 한국미생물·생명공학회지
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• 제29권4호
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• pp.240-247
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• 2001

본 연구에서는 동물세포 배양장치를 개발키 위한 기초연구로서 초미세 통기법이 산소 전달 속도와 세포의 생존율에 미치는 영향에 대해 알아보았다. 통기 장치로 통기 구멍 크기가 다른 microsparger 를 사용하였을 때, 모형 반응기 내에서 측정한 산소 전달계수(k$_{L}$a)는 microsprager의 통기 구멍 크기가 작아질수록 현저히 증가하였다. 이는 공기 방울들과 매질 사이의 접촉 면적이 증가했기 때문인 것으로 판단된다. 두 가지 다른 형태의 임펠러 (square-pitch marine impeller 와 $45^{\circ}$) pitched flat blade impller) 를 사용하여 교반하였을 때, $k_{L}$ a 값은 marine impeller 를 사용하였을 때 다소 높았다. $100\mu\textrm{m}$ 이하의 통기 구멍을 가진 microsparger 를 사용하여 직접 통기가 세포에 미치는 손상에 대해 알아본 결과, 세포들의 손상 정도는 통기 속도가 증가할수록, 공기방울 크기가 작아질수록 더 커졌다. 2.5 L 용량의 소형 세포 반응기에 $0.5\mu\textrm{m}$ 의 통기 구멍 크기를 가진 micro-sparger를 장치하여 세포를 배양한 결과 , 지속적인 통기시에는 세포의 생존율이 80% 이하로 떨어지고, 정상적인 성장을 하지 못하였다. 그러나 용존 산소 농도가 20% 이하로 떨어졌을 때에만 통기하였을 때 세포는 정상적으로 자랐으며 세포 생존율도 대수기 전반에 걸쳐 90% 이상을 유지하였다.