• 한국식품영양학회지
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• 제11권6호
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• pp.640-646
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• 1998

For the production of nonprotein $\alpha$-glucosidase inhibitor from the Streptomyces sp. NS15 strain, effects of initial optimum pH, nitrogen sources, carbon sources, cationic metal ions, agitation speed and aeration rate were investigated. Initial optimum pH of medium was 7.0. The most effective nitrogen and carbon sources were soybean meal 2.0%(w/v) and glucose 1.6%(w/v), respectively. The cationic metal ins had no stimulating effect on inhibitory activity of $\alpha$-glucosidase except Fe2+. Agitation speed and aeration rate were effective at 400rpm and 1vvm, respectively. In the jar-fermenter cultivation for 4 days under optimal culture conditions, the culture broth showed the inhibitory acitivity of 3,200units/ml, which is 25 times higher than that of basic medium (CYM) for porcine intestinal $\alpha$-glucosidase. The inhibitory activity of $\alpha$-glucosidase reached about 3,200units/ml after 4 days of cultivation and decreased gradually for a further two days.

• Journal of Microbiology and Biotechnology
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• 제21권6호
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• pp.652-658
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• 2011

The growth kinetics of Streptomyces noursei NRRL 5126 was investigated under different aeration and agitation combinations in a 5.0 l stirred tank fermenter. Poly-${\varepsilon}$-lysine biosynthesis, cell mass formation, and glycerol utilization rates were affected markedly by both aeration and agitation. An agitation speed of 300 rpm and aeration rate at 2.0 vvm supported better yields of 1,622.81 mg/l with highest specific productivity of 15 mg/l.h. Fermentation kinetics performed under different aeration and agitation conditions showed poly- ${\varepsilon}$-lysine fermentation to be a growth-associated production. A constant DO at 40% in the growth phase and 20% in the production phase increased the poly-${\varepsilon}$-lysine yield as well as cell mass to their maximum values of 1,992.35 mg/l and 20.73 g/l, respectively. The oxygen transfer rate (OTR), oxygen utilization rate (OUR), and specific oxygen uptake rates ($qO_2$) in the fermentation broth increased in the growth phase and remained unchanged in the stationary phase.

• 한국미생물·생명공학회지
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• 제26권6호
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• pp.529-536
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• 1998

용존산소(D.O.) level은 유기산 및 포도당을 혼합한 배지에서 Azotobacter vinelandii UWD의 생장 및 생분해성 고분자(PHBV) 생성에 큰 영향을 주었다. 용존산소 level이 높은 경우(5% D.O.)는 낮은 경우(1% D.O.)에 비해 세포의 생장속도가 약 2배 증가하였으나 PHBV 생성은 D.O.가 낮은 경우 62.3 wt%로 D.O.가 높은 경우에 비해 약 17배 증가하였다. 그러나 B.O. level은 통기(aeration)에 의한 A. vinefandii UWD의 발효특성 연구에 적합한 기준이 아니었다. 공기공급속도를 고정하고 교반속도만을 변화시키는 통기법으로 산소전달속도를 감소시켰을 때 이 균주는 산소소모속도를 그에 따라 대응 감소시킴으써 겉보기 D.O.를 높게(5%) 유지할 수 있었고 이 때 생장이 느려지고 PHBV 양은 57.3 wt%로 증가하였다. 통기가 세포생장 및 PHBV 생성에 미치는 영향을 일관성 있게 설명할 수 있는 기준은 D.O. level이 아니라 산소전달속도였으며 비생장속도는 산소전달속도에 비례하여 증가하였고 PHBV 생산량은 산소전달속도에 반비례하였다.

• 생명과학회지
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• 제20권6호
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• pp.811-818
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• 2010

Sphingomnas paucibilis NK2000 균주를 사용한 젤란의 최적 교반속도 및 통기량은 각각 400 rpm 및 1.0 vvm이었다. 이 균주를 사용하여 젤란의 생산성을 향상시키기 위한 포도당의 최적 첨가시기는 배양을 시작한 36시간이었다. 젤란의 생산성을 향상시키기 위한 5가지 방법, 1) 포도당을 첨가하지 않는 방법, 2) 배양 36시간 후에 포도당을 첨가하지만 교반속도 및 통기량을 변화시키지 않는 방법, 3) 배양 36 시간 후에 포도당을 첨가하고 교반속도를 400 rpm에서 600 rpm으로 변화시키는 방법, 4) 배양 36 시간 후에 포도당을 첨가하고 교반속도를 400 rpm에서 600 rpm으로 증가시키고 통기량을 1.0 vvm에서 1.5 vvm으로 증가시키는 방법 및 5) 배양 36 시간 후에 포도당을 첨가하고 교반속도를 400 rpm에서 600 rpm으로 증가시키고 통기량을 1.0 vvm에서 2.0 vvm으로 증가시키는 방법 등을 실험한 결과, 젤란의 생산성은 각각 5.19, 5.74, 6.73, 7.93, 및 9.40 g/l이었으며, 변환률은 각각 26.0, 19.1, 22.4, 26.4, and 31.3%이었다. 최적의 방법으로 생산한 젤란의 생산농도 및 포도당 전환율은 포도당을 첨가하지 않은 방법으로 생산한 젤란의 생산농도 및 포도당 전환율에 비하여 각각 1.81 및 1.20 배 증가하였다.

• 환경영향평가
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• 제14권5호
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• pp.263-273
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• 2005

In this study, the major emission procedures and emission characteristics were identified at the site of sewage treatment plant which is one of the major sources of ammonia. At the same time the emission factors and emission rates were estimated. In order to calculate the emission flux, we used a Dynamic Flux Chamber(DFC), which is found to be a proper sampling devise for area sources such as sewage treatment plant. It was found that the most stable sampling condition was when the stirrer's speed of DFC was 120RPM, and it would be the best time to take a sample 60 minutes later after setting the chamber. The relatively higher flux was shown in Autumn compared to summer and winter. Annual ammonia emission rates procedures were calculated as $906.32{\mu}g/activity-ton$, $1,114.72{\mu}g/activity-ton$ and $437.53{\mu}g/activity-ton$ each at the primary settling basin, aeration basin and the final settling basin, respectively. The ammonia emission rate the highest at in the aeration basin according to this test. This results was due to that the surface of aeration basin or the final settling basin is relatively wider than the primary settling basin.

• Journal of Microbiology and Biotechnology
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• 제16권12호
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• pp.1849-1855
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• 2006

It has been shown that the initial conditions of bacterial cultivation are extremely important for the successful production of hyaluronic acid (HA) by fermentation. We investigated several parameters that affect cell growth rate and the productivity and molecular weight of hyaluronic acid--i.e., agitation speed, aeration rate, culture temperature, pH, and pressure--to determine how to optimize the production of HA by Streptococcus zooepidemicus on an industrial scale. Using a 30-1 jar fermentor under laboratory conditions, we achieved maximum HA productivity and biomass when the agitation speed and aeration rate were increased simultaneously. By shifting the temperature downward from 35$^{\circ}C$ to 32$^{\circ}C$ at key levels of cell growth during the fermentation process, we were able to obtain HA with a molecular weight of $2.8{\times}10^6$ at a productivity of 5.3 g/l. Moreover, we reproduced these optimized conditions successfully in three 30-1 jar fermentors. By reproducing these conditions in a 3-$m^3$ fermentor, we were able to produce HA with a molecular weight of $2.9{\times}10^6$ at a productivity of 5.4 g/l under large-scale conditions.

• 공업화학
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• 제17권5호
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• pp.509-516
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• 2006

Rushton turbine, paddle and propeller 임펠러 등 표준적인 임펠러가 부착된 기-액-고 3상교반조에서 고-액간 물질이동계수 $k_L$를 측정하였다. 표준적인 임펠러들에 대한 부유화한계회전수 $N_{js}$는 임펠러 높이와 가스유속에 따라 변했다. 입자부유가 통기에 의존한 Rushton turbine 임펠러의 물질이동계수는 Pgv에만 상관하였다. Rushton turbine, paddle and propeller 임펠러에 대한 물질이동계수 $k_L$은 임펠러의 종류에 의하지 않고 임펠러 위치에 영향을 받았다.

• KSTLE International Journal
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• 제2권2호
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• pp.103-113
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• 2001

The influence of aerated oil on high-speed journal bearing is examined by classical thermohydrodynamic lubrication theory coupled with analytical models for viscosity and density of air-oil mixture in fluid-film bearing. Convection to the walls and mixing with supply oil and re-circulating oil are considered. The live oil surface tension is considered as functions of temperature, API gravity and air volume ratio. With changing eccentricity ratio, it is investigated the effects of air bubbles on the performance of a high-speed plain journal bearing. Just at the moderate eccentricity ratios, even if the involved aeration levels are not so severe and the entrained air bubble sizes are not so small, it is found that the bearing load and friction farce may be changed so visibly for the high speed bearing operation.

• KSTLE International Journal
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• 제2권1호
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• pp.1-11
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• 2001

The influence of aerated oil on a high-speed journal bearing is examined by classical thermohydrodynamic lubrication theory coupled with analytical models for viscosity and density of air-oil mixture in fluid-film bearing. Convection to the walls and mixing with supply oil and re-circulating oil are considered. With changing eccentricity ratio, it is investigated the effects of air bubbles on the performance of a high-speed plain journal bearing. Just at the moderate eccentricity ratios, even if the involved aeration levels are not so severe and the entrained air bubble sizes are not so small, it is found that the bearing load and friction force may be changed so visibly for the high speed bearing operation.

• Environmental Engineering Research
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• 제21권3호
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• pp.233-240
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• 2016

The research aims to study the different flexible rubber tube diffusers used in urban wastewater treatment processes and aquaculture systems. The experiment was conducted in small-scale aeration tank with different physical properties of the tubes that were used as aerators. The volumetric mass transfer coefficient ($k_La$), oxygen transfer efficiency (OTE) and aeration efficiency (AE) were measured and determined to compare the diffusers. Moreover, the bubble hydrodynamic parameters were analyzed in terms of bubble diameter ($d_B$) and rising velocity ($U_B$) by a high speed camera (2,000 frames/s). Then the interfacial area (a) and liquid-side mass transfer coefficient ($k_L$) can be calculated. The physical properties (tube wall thickness, tensile strength, orifice size, hardness and elongation) have been proven to be the key factor that controls the performance (kLa and OTE). The effects of hardness and elongation on bubble formation, orifice size and a-area were clearly proved. It is not necessary to generate too much fine bubbles to increase the a-area: this relates to high power consumption and the decrease of the kL. Finally, the wall thickness, elongation and hardness associated of the flexible tube diffuser (tube No. 12) were concluded, to be the suitable properties for practically producing, in this research.