• Membrane Journal
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• v.15 no.1
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• pp.70-83
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• 2005

By supplying air intermittently in various mode, the effects of oxic/anoxic time ratio and air scrubbing in aeration condition on the membrane flux and permeability were investigated. When suction pump stops, vacuum pressure remains inside the suction pump. Therefore, the effect of remaining vacuum pressure in the suction pump on fouling of membrane was investigated. The effect of EPS (Extra cellular Polymeric Substance) which is generated due to the long SRT and high concentration of MLSS and the dose of coagulant on the membrane were also investigated. The suitable oxic/anoxic time ratio for the best removal efficiency of organic matter and nitrogenous matter was 40 minutes (Oxic) : 20 minutes (Anoxic). At this time ratio, alum was dosed into the aeration tank. The result of dosing alum was that the concentration of alum solution might affect nitrification and denitrification. To remove 1 mg/L of phosphorus in MBR process, it needs 0.75 mg/L of alum solution.

• 한국신재생에너지학회:학술대회논문집
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• 2010.06a
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• pp.67.1-67.1
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• 2010

Triple junction solar cell을 위한 a-SiGe middle cell의 조건별 광학적 특성에 관한 연구를 실시하였다. a-SiGe I층은 GeH4 유량, 압력, H2 dilution ratio를 변화시켜 제조하였으며 전기적, 광학적 특성을 비교하여 최종적으로 선택된 조건을 triple junction solar cell에 적용하였다. a-SiGe I층은 Ge contents가 증가함에 따라 band gap은 감소하고 45% 이상의 조건에서는 700nm 전후 파장의 투과율이 감소하며, 압력이 감소함에 따라 band gap은 소폭 감소하나 700nm 전후 파장의 투과율은 증가하였다. 그리고 H2 ratio가 증가함에 따라 band gap은 소폭 감소하나 투과율에는 큰 변화가 없었다. 상기 결과를 바탕으로 최종적으로 선택된 조건에서 triple-junction solar cell을 제작하여 평가한 결과 초기 변환효율 9%의 결과를 얻었다.

• Membrane Journal
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• v.25 no.3
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• pp.216-222
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• 2015

The method measuring LEP (liquid entry pressure) was optimized to evaluate the wettabilities of hydrophobic membranes which might affect long-term durability of membrane in MD (membrane distillation) process. Conductivity of the permeate was monitored to measure the LEPs of PE (polyethylene) and PVDF (polyvinylidene di-fluoride) hollow fiber membranes from highly concentrated synthetic feed water of 20 wt% NaCl. Holding time over 5 min and the ratio of membrane area to the tank volume more than $10m^2/m^3$ were required to ensure LEP value.

• Proceedings of the Membrane Society of Korea Conference
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• 1997.04b
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• pp.3-10
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• 1997

제염농축공정은 증류, 증발법을 일반적으로 사용하나, 에너지 절약차원에서 전기투석 (Electro dialysis)장치를 증발기 선단에 도입한 복합공정을 국내에서도 사용하고 있는 실정이다. 그러나, 전기투석장치는 전기적인 소모와 막의 재생, 교체처리비가 문제점이 되므로 역삼투 장치를 제염농축 공정 최선단에 도입한 복합공정을 이용할 경우 전기 투석 및 증발 복합공정에 비해 40%의 에너지 절감 효과를 기대할 수 있다. 이와 같은 장점에도 불구하고 역삼투 공정은 공급용액의 삼투압보다 큰 적용압력을 막표면에 가하여 물질분리를 수행하므로 농축공정에서 유발되는 배제액 농도의 상승은 삼투압의 증가를 일으켜 실적적용압력의 효과를 떨어뜨리게 되며 결과적으로 농축효과를 감소시키게 된다. 본 연구에서는 효과적인 염농축 공정을 위하여 막모듈 투과부에 고농도 삼투압 감소액(osmotic sink solution)을 향류식(막투과흐름을 맞받아치며 흐르는 방식)으로 유입시키는 향류식 역삼투 (counter-current reverse osmosis, CCRO) 나권형 모듈을 고안 제작하였으며, 제작된 모듈을 기존 역삼투 공정과 향류식 염삼투 공정에 적용하여 염농축도의 성능을 상호 비교하고 염농축에 관계되는 공급농도, 공급유량, 투과유량, 배제유량, 향류 유입유량, 압력구배, 삼투압차 및 농축단수 등의 인자들을 이용하여 두 공정에 대한 염농축 분리조작의 제반조건과 제작된 모듈 내의 농축관련 특성을 실험 및 수치적으로 비교, 고찰하였다.

• Membrane Journal
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• v.32 no.6
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• pp.383-389
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• 2022

Membrane separation process is an important technique utilized for various applications. This separation process proceeds due to a driving force such as concentration gradient, pressure or electrical potential gradient etc. Pervaporation is one of the separation process based on solution-diffusion mechanism. The pressure of the permeate side is reduced by creating vacuum and separation is driven due to pressure difference. Purity of the fuel or chemical like ethanol or isopropyl alcohol are improved by dehydration process through porous zeolite membrane. These membranes have high thermal, chemical, mechanical stability. This review is classified mainly into two different sections: Ethanol and bio-oil dehydration by zeolite membrane.

• Membrane Journal
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• v.14 no.3
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• pp.207-217
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• 2004

In this study, we prepared nanofiltration membrane by applying the interfacial polymerization method as a way of manufacturing composite membranes. We have examined the effects of various preparation factors such as monomer concentration and composition, thermal curing condition, post treatment condition. In addition to preparation conditions, we also monitored the effects of operation conditions such as feed solution concentration and operation pressure on the permeation properties of the resulting nanofiltration membrane. We intended to increase the permeation rate of nanofiltration membrane by the enlargement of effective surface area using additives during interfacial polymerization step. With increasing the monomer concentration, membrane permeation rate are decreased with maintaining almost constant rejection. With respect to curing condition, with increasing the curing temperature both permeation rate and rejection are decreased. With increasing the ratio of MPD in amino monomer composition, permeation rate decreased drastically with high rejection. With increasing the feed solution concentration, both permeation rate and rejection decreased. Both permeation rates and rejection increased with increasing the operating pressure. Nanofiltration membrane have higher surface roughness with increasing additive concentration in the case of using MPD contained amine composition than using piperazine alone. Permeation rates are much lower than the nanofiltration membrane prepared by piperazine.

• Membrane Journal
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• v.22 no.1
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• pp.1-7
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• 2012

We make a studyof the hydrogen permeability and chemical stability of $Nb_{56}Ti_{23}Ni_{21}$ metal alloy membrane. For this purpose, we produced the $Nb_{56}Ti_{23}Ni_{21}$ membrane which has 10 mm diameter and 0.5 mm thick, and experiment the hydrogen transport properties under two kinds of feed gas ($H_2$ 100%; $H_2$ 60% + $CO_2$ 40%) at $450^{\circ}C$C with variation of absolute pressure.The maximum hydrogen permeation flux was $5.58mL/min/cm^2$ in the absolute pressure 3 bar under pure hydrogen. And each case of feed gases about gas composition, the permeation fluxes were satisfied with Sievert's law, and the hydrogen permeation flux decreased with decrease of hydrogen partial pressure irrespective of temperature and pressure. After permeation test, we experiment the stability and durability of $Nb_{56}Ti_{23}Ni_{21}$ alloy membrane for carbon dioxide by XRD analysis.

• Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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• 2010.06a
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• pp.387-387
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• 2010

최근 ZnO 박막은 투명 박막, 태양전지, LED 등으로의 응용을 위한 새로운 기능성 박막으로 활발히 연구되어 지고 있다. ZnO 기반의 투명 박막 트랜지스터는 상온에서 증착 가능하여 유리기판을 이용한 광학소자와 플라스틱 기판을 이용한 플럭서블 소자 같은 차세대 전자소자를 구현 할 수 있다. 본 연구에서는 RF Magnetron Sputtering System을 이용하여 coming 1737 유리기판 위에 ZnO 박막을 공정압력에 따라 증착하고, 투명 반도체에 적합한 활용을 위한 구조적, 광학적 분석을 실시하였다. 박막 증착 조건은 초기 압력 $1.0{\times}10^{-6}$Torr, RF 파워는 100W, Ar 유량은 100sccm, 그리고 증착온도는 상온이었다. 증착 압력은 $7.0{\times}10^{-3}$, $2.0{\times}10^{-2}$, $7.0{\times}10^{-2}$Torr로 변화시켰다. 표면 분석 (SEM, AFM) 결과 증착압력이 고진공으로 변화함에 따라 결정립들이 감소하였고 RMS roughness값이 낮아졌다. 그리고 XRD 분석을 통해 피크강도는 증가하고 FWHM은 감소함을 보이고 있는데 이는 결정성이 좋아짐을 나타낸다. 그리고 광학 투과도를 통해 가시광 영역에서의 높은 투과도(85% 이상)을 확인하였고, 고진공으로 변화함에 따라 밴드갭이 넓어지는 것을 확인하였다.

• Korean Journal of Food Science and Technology
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• v.29 no.2
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• pp.279-283
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• 1997

Membrane separation technology was applied to prepare high quality persimmon juice from persimmon, which is produced in large quantities in Korea. The influences of time, pressure, and temperature on permeate flux were studied during concentration by reverse osmosis. The chemical components of retentate were also analyzed. The permeate flux was higher as the operating temperature and pressure were increased, and was influenced more strongly by operating pressure than temperature. Maximum concentration by reverse osmosis employed in this study in the oBrix scale was about 30. Retention percentage of sugar in the persimmon juice which was concentrated by membrane separation system was more than 90% and was not influenced by operating conditions. Retention percentage of volatile components in the same process was more than 60%; it was increased as operating temperature was decreased and pressure was increased.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.7
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• pp.1183-1191
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• 2000

Operating conditions for reduction of membrane fouling in treatment of dissolved organic matter by UF membrane process were investigated by pilot-scale plant using various operating conditions. As inlet pressure increased, increament of transmembrane pressure and flux decline were faster. The reason was due to the increase in adsorption of dissolved organic matter and the development of cake layer compression on the membrane surface. When efficient pressure (the difference of pressure between backwash and transmembrane pressures) was high, small amount of pollutant was retained on the membrane surface. When backwash was frequently conducted, low concentration of pollutant was maintained in recycling water. Therefore, backwash could be efficiently conducted with high efficient pressure and high frequency. Fouling rate was correlated with backwash and inlet pressures, recovery rate and cumulative permeated volume. Among the operating parameters backwash pressure was most closely related to fouling rate and inlet pressure was next to backwash pressure. It seems that the fouling was strongly related to pressure which leads to the cake layer compression and adsorption of dissolved organic matter.