• 접착 및 계면
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• 제13권2호
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• pp.85-88
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• 2012

In this paper, the curing reaction of UF resins was investigated by a real time FT-IR method. The curing temperature range of the UF resin was $25{\sim}200^{\circ}C$. It was found that the reactions of UF resin at different temperatures resultedin resins with different cross-linked structures. A real time FT-IR spectroscopy can be considered as a good routine analytical tool for following the progress of UF resin curing.

• 한국환경보건학회지
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• 제26권4호
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• pp.45-48
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• 2000

Reverse osmosis filtration(RO) system and ultrafiltration(UF) system are principally use for domestic home drinking water treatment systems. The object of this study is to make a comparison between two systems in terms of theirs abilities to remove RNA coilphage QB as an indicator of pathogenic enteroviruses. The virus removal ratio of RO system was 99.999%, which was higher than EPA virus treatment guideline(99.99%). In the course of filtration, removal ratios of sediment filter, pre-carbon filter, reverse osmosis membrane and post-carbon filter were 75.000%, 93.208%, 99.997% and 99.999%, repectively. In case of UF system, virus removal ratio was 99.708%. Removal ratios of sediment filter, pre-carbon filter, post-carbon filter and ultrafiltration membration membrane were 71.038%, 91.530%, 98.283% and 99.708%, respecively, in UF steps. Therefore, RO system is more effective than UF system in virus removal.

• International Journal of Internet, Broadcasting and Communication
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• 제14권4호
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• pp.80-87
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• 2022

Lack of sufficient battery capacity is one of the most important challenges impeding the development of wireless sensor networks (WSNs). Recent innovations in the areas of wireless energy transfer and rechargeable batteries have made it possible to advance WSNs. Therefore, in this article, we propose an energy-efficient charging of sensors in a WSN scenario. First, we have formulated the problem as an integer linear programming (ILP) problem. Then a utility function-based greedy algorithm named UGreedy/UF1 is proposed for solving the problem. Finally, the performance of UGreedy/UF1 is analyzed along with other baseline algorithms: UGreedy/UF2, 2-opt TSP, and Greedy TSP. The simulation results show that UGreedy/UF1 performs better than others both in terms of the deadline missing ratio of sensors and the total energy consumption of UAVs.

• 한국막학회:학술대회논문집
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• 한국막학회 1999년도 추계 총회 및 학술발표회
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• pp.77-80
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• 1999

• 한국막학회:학술대회논문집
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• 한국막학회 2000년도 춘계 총회 및 학술발표회
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• pp.27-29
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• 2000

• 한국막학회:학술대회논문집
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• 한국막학회 2000년도 춘계 총회 및 학술발표회
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• pp.93-96
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• 2000

• Membrane and Water Treatment
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• 제9권5호
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• pp.317-325
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• 2018

Polyvinyl chloride (PVC) ultrafiltration (UF) membrane was modified by silica sol in the coagulation bath during non-solvent induced phase separation (NIPS) process. The effects of silica sol concentrations on the morphology, surface property, mechanical strength and separation property of PVC UF membranes were systematically investigated. PVC membranes were characterized by Fourier transform infrared spectroscopy (FTIR), energy dispersive spectroscopy (EDS), scanning electron microscopy (SEM), contact angle goniometry and tensile strength measurement. The results showed that silica had been successfully assembled on the surface of PVC UF membrane. With the increase of silica sol concentration in the coagulation bath, the morphologies of PVC UF membranes changed from cavity structure to finger-like pore structure and asymmetric cross-section structure. The hydrophilicity and permeability of PVC UF membranes were further evaluated. When silica sol concentration was 20 wt.%, the modified PVC membrane exhibited the highest hydrophilicity with a static contact angle of $36.5^{\circ}$ and permeability of $91.8(L{\cdot}m^{-2}{\cdot}h^{-1})$. The structure of self-assemble silica had significant impact on the surface property, morphology, mechanical strength and resultant separation performance of the PVC membranes.

• 유기물자원화
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• 제20권3호
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• pp.21-24
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• 2012

본 연구에서는 폐기물 자원화 공정에서 발생하는 음폐수를 UF 분리막을 결합한 혐기성 소화 파일럿 에서 처리하면서 혐기성 소화효율, 바이오가스 생산량과 운전인자를 도출하였다. 운전방식은 막내부에서 외부로 고액분리가 이루어지는 가압식이었으며, 투과 플럭스는 15∼20 LMH, 막간 차압은 $1{\sim}3 kgf/cm^2$였다. 분리막 운전은 직접순환방식으로 운전한 결과, 메탄조의 수질악화로 간접순환방식으로 운전하였다. 유입수의 TCOD 와 SCOD 는 각각 113 g/L, 62 g/L 이었고, 유출수의 TCOD 와 SCOD는 각각 25 g/L, 12 g/L 이었다. TCOD 및 SCOD 제거효율은 각각 77% 및 81%였다. 하지만 UF 공정을 추가했을 때는 제거효율이 93% 및 86%로 증가하였다.

• Journal of the Korean Wood Science and Technology
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• 제48권2호
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• pp.136-153
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• 2020

In this paper, the influence of initial formaldehyde/urea (F/U) molar ratios on the performance of low molar ratio (1.0) urea-formaldehyde (UF) resin adhesives has been investigated. Two initial F/U molar ratios, i.e., the first and second initial molar ratios were used for the alkaline addition reaction. Three levels of the first initial F/U molar ratios (2.0, 3.0, and 4.0) and two levels of the second initial molar ratios (2.0 and 1.7) were employed to prepare a total of six UF resins with an identical final molar ratio (1.0). The basis properties, functional groups, molecular weight, crystallinity, and thermal curing properties of the UF resins were characterized in detail. Higher levels (3.0 and 4.0) of the first initial F/U molar ratio provided the UF resins with better properties (non-volatile solids content, viscosity, gelation time, pH, and specific gravity) than those of the resins prepared with the conventional level F/U molar ratio of 2.0. Statistical analysis suggested that combining the first and second initial molar ratio of 4.0 with 1.7 would result in UF resins with greater adhesion strength and lower formaldehyde emission than those of the resins prepared with other molar ratios. The results showed that higher levels of the first initial molar ratio resulted in a more branched structure, as indicated by GPC, FTIR, DSC, XRD, and greater adhesion strength than those of the other UF resins with an identical final molar ratio of 1.0.

• 대한환경공학회지
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• 제30권11호
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• pp.1139-1145
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• 2008

응집-막분리 공정의 적용시 전처리 응집공정에서 응집조건에 따라 발생하는 플럭 생성특성을 파악하고 생성된 플럭 특성에 따른 막투과 플럭스의 영향을 살펴본 결과 인공시수와 낙동강 원수에서 전처리 응집공정을 적용시 급속교반 후 용존성 유기물질(자연유기물질)이 미세 플럭의 형성으로 인하여 입자상 유기물질로 전환이 발생하였으며 급속교반초기 10초 사이에 용존성 유기물이 입자상 물질로 전환되었다. 또한 응집제 주입량이 0.025 mM as Al (7.5 mg/L Alum) 이었을 경우 입자 전환율 K값이 크게 나타나고 있었으나 0.05 mM (15 mg/L Alum)이상으로 응집제 주입량이 증가할 경우 K값은 감소하였으며 0.15 mM까지 유사한 값을 보이고 있었다. 낙동강 원수를 이용하여 전처리 공정으로 응집 공정을 적용시 UF 단독공정에 비하여 투과 flux 감소는 상당히 낮게 나타났으며 투과 flux 변화는 응집공정에 의하여 형성되는 입자크기 분포에 의존하였으며 응집조건에 따른 투과 flux 실험결과 급속교반-UF공정과 급속교반-완속교반-UF공정의 투과 flux는 유사하게 나타났다. 막의 재질에 따른 투과 flux 실험결과 소수성 재질의 막에 비하여 친수성 재질의 막이 투과 flux가 높게 유지되었으며 응집제 자체의 금속성분에 의한 막오염 영향은 나타나지 않았다.