• Proceedings of the Korea Water Resources Association Conference
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• 2003.05b
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• pp.915-918
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• 2003

• Journal of the Korean Crystal Growth and Crystal Technology
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• v.4 no.3
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• pp.210-222
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• 1994

The characteristics of flows, temperatures, and concentrations of oxygen are numerically studies in the Czochralski furnace with a uniform axial magnetic field. Important governing factors to the flow fields include buoyancy, thermocapillarity, centrifugal force, magnetic force, diffusion and segregation coefficients of the oxygen, evaporation coefficient in the form of SiO, and ablation rate of crucible wall. With an assumption that the flow fields have reached the steady state, which means that two velocity components in the meridional plane and circumferential velocity, temperatures, electric current intensity become non-transient, then unsteady concentration field of oxygen has been analyzed with an initially uniform oxygen concentration. Oxygen transports due to convection and diffusion in the Czochralski flow field and oxygen flux through the growing crystal surface has been investigated.

• KSCE Journal of Civil and Environmental Engineering Research
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• v.14 no.4
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• pp.989-997
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• 1994

The major objective of this study is to develop an effective method to estimate ${\alpha}$ and ${\beta}$ in an aeration basin at a conventional activated sludge wastewater treatment plant. A series of unsteady state batch tests were simultaneously performed with clean water and mixed liquor in two batch reactors under identical operational conditions. Oxygen uptake rates (OURs) of the mixed liquor were measured during the tests. The results show that the OURs due to synthesis respiration and endogenous respiration were averaged about $17.96 mg/(l{\cdot}hr)$ and about $12.29mg/(l{\cdot}hr)$, respectively. The corresponding ${\alpha}$ and ${\beta}$ were ranged between 0.65 to 0.95, and between 0.88 to 0.93, respectively. Based on the overall experimental results, the proposed experimental test method and the proposed method for determination of ${\alpha}$ and ${\beta}$ are found to be relatively simple and easy to use in evaluating the characteristics of aeration systems.

• Proceedings of the Korean Society of Fisheries Technology Conference
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• 2000.05a
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• pp.239-240
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• 2000

용존산소는 양식 시설 내 생산량을 결정짓는 중요한 수질 조건으로서, 시설 내 용존산소를 충분히 공급하기 위해 많은 연구자들이 여러 가지 형태의 에어레이터의 고안(Boyd and Tucker, 1979)및 순수산소의 이용에 관해 연구해왔다. 그러나 에어레이터 또는 순수 산소의 이용은 추가 에너지가 필요한데, 송어 양식장에는 전체비용의 13∼15%, 부화장의 경우에는 23%(Petit, 1990) 및 순환여과식 시설에서는 8.6%(Timmons and Aho, 1998)의 경비가 추가된다고 한다. (중략)

• Journal of Aquaculture
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• v.7 no.4
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• pp.239-249
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• 1994

This study was conducted to elucidate mixing characteristics of the media to dertermine hydraulic model parameters of the three phase fluidized bed for the water quality management of aquaculture. The volume and H/D ratio of the reactor were 1.76 Liter and 10.9, respectively. The experimental results showed that variance $(\sigma^2)$ and dispersion number $(D/{\mu}L)$ were above 0.47 and $0.35\~\infty$, respectively. Therefore, the condition of the reactor was almost ideal complete mixing. The dependence of the overall oxygen-transfer coefficient $(K_{La})$ on each experimental variables through a multple linear regression was given by the following equation ; $$K_{La}\;=\;44.9(D_i/D_c)^{-0.4611}\;A_f^{0.8622}\;C_m^{-0.0746}\;d_p^{-0.4302}$$

• Applied Chemistry for Engineering
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• v.10 no.2
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• pp.310-318
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• 1999

The concentration breakthrough curves were examined to predict mass transfer coefficients of nitrogen and oxygen in adsorption column for design data of PSA process. Experimental breakthrough curves for bulk gas flow were compared with theoretical simulation results. For quantitative analysis of the adsorption, coupled Langmuir isotherm was considered and LDF model was used to describe the mass transfer effect. In the experimental and theoretical results, it was found that mass transfer coefficient was not affected by flow rate but strongly affected by pressure. As a result of this tendency, mass transfer resistance in this system was proved to belong to the macropore diffusion controlling region and the mass transfer coefficients could be expressed by exponential functions of pressure change. The mass transfer coefficients for one component, nitrogen or oxygen, were successfully applied to breakthrough curves for bulk mixed gases. The experimental curves were reasonably in consistent with the theoretical curves and the error time was less than 5 percent.

• Microbiology and Biotechnology Letters
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• v.35 no.3
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• pp.226-230
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• 2007

In order to achieve high-level expression of interferon-${\alpha}1$ (IFN-${\alpha}1$) during fed-batch fermentation of recombinant E. coli, effects of oxygen supply and induction temperature on the expression of recombinant proteins were evaluated. Supplementation of oxygen and its transfer into cells is one of the most important parameters involved in the design and operation of mixing-sparging equipment for bioreactors. Generally, higher oxygen supply stimulates cell growth of aerobic microorganism and consequently the amount of products is increased. In this study, the optimum aeration strategy for the higher production of IFN-${\alpha}1$ during fed-batch fermentation of recombinant E. coli was surveyed. The growth of the cells was also monitored with four different concentrations of dissolved oxygen (DO; limiting, 20%, 35%, 50%) conditions. The DO was controlled by varying aeration rates of air and pure oxygen. Oxygen uptake rate (OUR) and specific oxygen uptake rate (SOUR) were evaluated and compared for the enhanced growth and induction of the cells and IFN-${\alpha}1$, respectively. We confirmed that increased DO by additional oxygen supply, up to 35%, can improve the production of IFN-${\alpha}1$ during the fermentation.

• KSBB Journal
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• v.17 no.2
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• pp.142-147
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• 2002

The decomposition of hydrogen peroxide was used for supplementing the oxygen during batch xanthan fermentations in a bubble column bioreactor in order to escape the oxygen transfer limitation that occurred at the high viscosity of culture broths. The xanthan production, however, was inhibited reversibly by dosing hydrogen peroxide. On the other hand, fluidized particles of glass beads with 8 mm diameter led to high gas-liquid oxygen transfer rates in three-phase fluidized beds, which resulted in higher space-time yields of the xanthan production compared to in the bubble column bioreactors.

• Nuclear Engineering and Technology
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• v.27 no.4
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• pp.619-625
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• 1995

발전소 계통의 부식의 원인은 여러가지가 있으나 그 중 용존산소에 의한 덴팅이나 점식등은 증기발생기에 심각한 영향을 줄 수 있다. 용존산소를 제거하는 방법은 기계적 방법과 환원제를 사용하는 화학적 방법, 그리고 촉매를 이용하는 방법등이 있는데 이중 촉매를 이용하는 방법이 우수한 것으로 평가되고있다. 본 연구는 촉매탑을 이용하여 용존산소를 제거하는 공정에 있어서 여러가지 촉매를 사용하여 용존산소가 제거되는 것을 실증하였고 각 촉매의 성능을 비교하였다. 그 결과 Lewatit OC-1045 촉매가 가장 우수한 성능을 보였다. 촉매탑 실험시 물질전달 계수를 측정하고 이 값과 촉매탑 모델링을 이용하여 실제 발전소 계통에 부착시켜 응용할 수 있는 촉매탑 설계를 수행하였다.

• Journal of Korea Water Resources Association
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• v.35 no.5
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• pp.511-523
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• 2002

In order to develop the weir with high reaeration efficiency, the reaeration experiments at linear weir, ogee spillway type weir, and labyrinth weirs were conducted and the results were compared. The effect of roughened crest was also analyzed. It was found from the experiments that the oxygen transfer efficiency at the ogee spillway type weir was the lowest and that at the linear weir was second lowest among the weirs used in the experiments. It was also revealed that the reaeration efficiencies of the labyrinth weirs increase as the included angles become smaller. The roughened crest which causes the disintegration of overflow was found to increase the reaeration efficiency significantly. On the basis of the results of the experiments, the pilot construction of the labyrinth welt with included angle of 30 degree was made. The labyrinth weir was made up by assembling the frame and then filling the ripraps into the frame. The ripraps were exposed at the crest to split the overflow. The average value of oxygen transfer efficiency observed at the pilot weir was 0.18. It is expected that the results from the experimental study and the field data of the pilot weir would serve for the improvement of water quality by the weirs with high reaeration efficiency.