• Membrane Journal
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• v.4 no.1
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• pp.38-45
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• 1994

The experiment was conducted to evaluate the effects of variables in preparing TFC membrane by interfacial polymerization. Obtained results are as follow: As the concentration of MPD increses, the rejection rate incresed, the total volume flux was decresed. As the dipping time in MPD solution increases, the rejection rate increased, the total volume flux was increased until reach optimum point. As the dipping time in TMC solution increses, the total volume flux increased, the rejection rate was increased until reach optimum point. As the curing temperature increases, the total volume flux increased was an optimum point in the rejection rate. Since the quantity of generating hydrochloric acid was small, the required quantity of NaOH for neutriliztion was small. The post-treatment with ethanol, isopropanol and water in the temprerature ranging of $5~7^{\circ}C$ brought an increment of the rejection and the total volume flux, For water temperature ranging of $5~7^{\circ}C$was the optimum temperature in the post treatment.

• Proceedings of the Korea Water Resources Association Conference
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• 2005.05b
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• pp.377-382
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• 2005

하도내에 설치된 3개의 구조물이 모두 제거된 상태에서 원형하천의 합류부 하류의 유량이 $Q_{100}=12,090m^3/sec$인 경우에 대해 본류와 지류의 유량비($Q_s/Q_m$)가 0.99, 0.85, 0.72, 0.67, 0.57로 변화하는 경우의 유량을 실험유량으로 사용하여 수리모형실험을 수행하였다. 하도의 구조물이 제거된 경우 합류부로 근접할수록 서서히 증가한 수위는 합류부를 지나면서 급격히 감소한다. 이때 본류와 지류의 유량비($Q_s/Q_m$)가 감소할수록 합류부에서 증가된 수위는 하류쪽으로 이동하며 합류부 이후에서의 감소폭이 작아지며 각 단면에서의 수위변화율은 합류부 상류 구간에서는 감소하고 합류부 하류 구간에서는 증가하고 있다. 또한 합류부에 가까울수록 횡단면에서의 수위차는 증가하여 합류부 중심 직하류 단면에서 최대를 보이는데 유량비가 감소할수록 합류부 횡단면에서의 수위차는 하류구간에서는 감소하며 합류부 상류구간에서는 증가한다. 합류구간의 유속변화에 있어서는 합류부에 가까울수록 평균유속이 감소하다가 합류부에서 증가하기 시작하여 합류부 중심 직하류 단면에서 평균유속이 최대를 나타내며 최대유속의 변화율은 합류부 하류구간보다 합류부 상류구간에서 더 크게 나타난다. 합류지역의 주흐름구간은 합류점 이후 구간에서 합류점 부근의 평균 유속보다 큰 유속을 보이는 구간으로 유량비가 감소하면 주흐름구간의 폭이 증가하며 하도의 하류쪽으로 이동하기는 하나 유량비에 의한 영향은 크지 않다.

• Journal of the Korean Society of Fisheries and Ocean Technology
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• v.40 no.3
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• pp.214-224
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• 2004

A large cage system for the purpose of fishes farming in the open sea was influenced by various forces from the ocean environment. The deformation of the cage by these forces affects the safety of the cage itself, as well as that of the cultivated creatures. In this research, theoretical model was established to analyzing dynamic movement influenced by current for cage. Also, to increase the accuracy of calculations, the reduction ratio of flow speed acquired using the flume tank experiment. Applying the reduction ratio of flow speed to the numerical calculation, the calculation values were compared with the measured values in the flume tank experiment using cage model. The results were as follows ; 1. When the flow speed of the flume tank is fixed, the decrease of the velocity of flow which is passed the upper panel side is proportion to the increase of porosity ratio of netting. 2. When the porosity ratio is fixed, the increase of the velocity of flow which is passed the upper panel side is proportion to the increase of velocity of flow. 3. When the porosity ratio and the flow speed of the flume tank are fixed, the decrease of the velocity of flow which is passed the upper panel side is proportion to the increase of attack angle. 4. As a result of comparison between the underwater shape by simulation which is applying the reduction ratio of flow speed from the experiment using plane netting and that by model experiment, it was found out that the result of the simulation was very close to that of model gear within ${\pm}$ 5 % error range.

• Membrane Journal
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• v.15 no.4
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• pp.338-348
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• 2005

The permeate flux decline on microfiltration capillary membrane operation was investigated with inorganic colloidal solutions. The permeate flux of the alumina solution is two times higher in average than that of the bentonite solution. The flux decline with increase in operation time was less in the alumina solution than in the bentonite solution. The rate of initial flux decline until 10 min was higher on the bentonite solution over the alumina solution. The decline in permeate flux was due to both the cake formation and the pore blocking. The latter effect was higher in the operation of the bentonite solution. In comparing the ratio of each fouling component to the total fouling fur the $1.0\;kg_f/cm^2$ TMP condition, complete blocking was $9.35\%$, standard blocking was about $6.82\%$ and cake filtration was $83.83\%$, respectively. With the increase in cross flow velocity, the permeate flux increased by $6.0\%$ for the alumina solution and by 14.0 for the bentonite solution. With the increase in average pore size fromm $0.24\;{\mu}m\;to\;0.34\;{\mu}m$, the permeate flux increases 1.61 times for the alumina solution and 1.76 times far the bentonite solution.

• Clean Technology
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• v.5 no.2
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• pp.69-78
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• 1999

Separation characteristics of cutting oil-in-water emulsions were studied experimentally by using various kinds of flat-type microfiltration and ultrafiltration membranes. For ultrafiltration membranes the permeation behavior of cutting oil emulsions obeys the film model, whereas a significant deviation from the model was observed for ASYPOR microfiltration membranes. The experimental data obtained for all the membranes showed that the effect of operating pressure on the permeation flux of oil-in-water emulsions is not very significant. At low transmembrane pressures the permeation flux decreased gradually with increasing filtration time, whereas the permeation flux at high transmembrane pressures decreased steeply for early filtration time. However, every flux eventually reached a constant value that depends only on the applied transmembrane pressure. For the hydrophobic polycarbonate microfiltration membrane the permeation flux increased with the filtration time. The critical permeation pressures were also determined from the data obtained from unstirred cell experiments.

• Fire Science and Engineering
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• v.27 no.6
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• pp.15-20
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• 2013

The convective heat transfer coefficient, emissivity, and flame heat flux on the surface of Duglas fir are estimated by using repulsive particle swarm optimization. The surface temperature, mass loss rate, and ignition time are measured for various incident heat fluxes from a cone heater of the cone calorimeter. The calculated surface temperatures obtained by using the optimized convective heat transfer coefficient, emissivity and flame heat flux on the surface in this study match well with those obtained from the test. The maximum error between the predicted and measured surface temperatures for the three different external heat fluxes is within 2% showing reasonable agreements. The methodology proposed in this study can be used to obtain various values related to heat transfer on a flaming surface that are difficult to measure in experiments.

• Proceedings of the Korea Water Resources Association Conference
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• 2007.05a
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• pp.527-531
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• 2007

하천내에서 작은 물고기의 국지적인 회유 또는 이동 습성은 먹이를 구하고, 산란 및 성장과 집단에서 분산하고, 위험으로부터 도피하는 것에 밀접한 연관이 있다. 하천의 합류부와 연결부에 제방(levee), 도로(road) 등이 설치되는 경우 일반적으로 암거형태의 인공수로로 상 하류를 연결되는데, 암거내 수리특성상 평수시 저유량, 고유속, 저수심의 수리특성을 보인다. 이러한 수리특성은 물고기가 이동하는데 장애(barrier)가 되어 생태적으로 하천내 종다양성 감소와 일부 어종의 멸종을 초래한다. 어도 설치시 설계기준에서 가장 주목할 부분은 어도를 이용할 대상어종의 범위와 유영능력이다. 하천설계기준(2005, 한국수자원학회)에서 제시된 물고기의 유영능력은 대부분 국외 어종을 대상으로 외국에서 실험한 결과를 이용하고 있다. 그러므로 이러한 기준이 국내 어종에 대해 적합한지에 대한 검토가 필요하다. 본 실험의 목적은 국지회유성인 피라미와 각시붕어가 인공수로를 통과할 때의 유영행동 중 소상성공율과 유영속력을 평가하고자 함이다. 유영행동의 실험방법은 Brett(1967)에 의해 제안된 2가지 방법인 증진유속방법과 고정유속 방법중에서 물고기의 이동경로와 소상능력을 확인하기에 용이한 고정유속방법을 사용하였다. 또한, 효과적인 실험을 위해 실험어종(피라미 100마리, 각시붕어 100마리)이 실험 중에 최적의 건강상태를 유지할 수 있도록 물고기의 적응 기간(24시간)과 실험 중 휴식기간을 두었다. 실험결과 체형이 방추형(fujiform)인 피라미의 경우 평균유속 $0.7{\sim}0.8m/s$구간에서 소상성공율이 61%에서 26%로 급격하게 하락하는 현상이 나타났다. 그리고 측편형(compressiform)의 체형을 가진 각시붕어의 경우 평균유속 0.4m/s에서 소상성공율이 25%로 나타났으며 그 이상의 유속에서는 10%이하로 나타났다. 실험어종의 이동경로를 분석한 결과 대부분 수로바닥에 밀착하여 최저유속구간을 이용하여 이동하는 것으로 나타났으며, 이동경로의 지점유속은 평균 유속의 70%정도로 나타났다. 실제 하천에 설치된 인공수로가 생태통로의 기능을 유지하기 위해서는 평상시 수리특성이 대상어종의 유영능력을 초과하지 않도록 설계되어야 한다. 특히, 하천에 설치된 인공수로의 길이가 $5{\sim}10m$정도일 경우라면 피라미의 소상 가능성을 50% 이상 확보하기 위해서는 평수시 설계유속이 0.7m/s를 초과하지 않아야 할 것으로 판단된다.

• Membrane Journal
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• v.22 no.2
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• pp.135-141
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• 2012

This study was carried out to find the optimum coagulation conditions for ceramic microfiltration process of Y water treatment plant. When pH of raw water from Y Dam was adjusted to 7, the efficiency of coagulation was the best and the optimun dosage of coagulant was 3 mg/L(as $Al_2O_3$) for turbidity of raw water less then 10 NTU in Jar test. In mini module test, the decay rate of specific flux was the lowest when PAC (poly Aluminum Chloride) was used among coagulants and pH was adjusted to 7. The decay rate of specific flux for raw water turbidity of 10~30 NTU was greatly decreased with increase of dosage of coagulant (PAC) while the rate was not significantly decreased for turbidity more than 50 NTU. In conclusion, the optimum dosage of PAC (11% as $Al_2O_3$) was 30 and 50 mg/L for raw water turbidity of less than 10 NTU and more than 50 NTU, respectively. The dosage of PAC should be increased linearly 30 to 50 mg/L depending on raw water turbidity of 10 to 50 NTU.

• Korean Journal of Food Science and Technology
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• v.35 no.1
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• pp.72-76
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• 2003

Ultrafiltration (UF) tests performed on traditional soy sauce (kanjang) using UF flat membrane test cell unit with thin film laminar flow similar to the spiral type membrane module in batch operations revealed reduction in permeate flux is proportional to the logarithm values of volume reduction ratio of the retentate kanjang at different feed rate of kanjang. Feed rate of 1.5 L/min was found to be adequate for long-term UF operation of kanjang using the test unit attached with MW cut-off size of 200,000 dalton polyoleffin plastic membrane in batch operation with the least concentration polarization. The higher the feed rate of kanjang, the lower the permeability of total nitrogen and NaCl, resulting in lower optical density at 500 nm and lower permeability of minerals such as Cu, Mn, and Mg. Microbial cells were completely rejected regardless of the feed rate, whereas most free amino acids were not.

• Membrane Journal
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• v.10 no.4
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• pp.230-233
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• 2000

The aqueous glucose solution was separated by the membrane distillation with hydrophobic pojytetrafluoroethylcnc microfiltration membrane, The nominal pore size of the membrane was 0.2${\mu}m$. As the operating temperature increased from 40$^{\cirt}C$ to 70$^{\cirt}C$, the membrane permeation flux increased from 3.6 LMH to IL2 LlVIH, but the glucose rejection decreased 99% to 65% Also, the permeation nux and rejection decreased 25% and 6%, respectively, as the concentration of glucose solution increased 2 wt% to 4 wt%.