• Membrane and Water Treatment
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• 제13권6호
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• pp.313-320
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• 2022

Theoretical calculation results are presented for the enhancement of the water mass flow rate through the hydrophobic micro/nano pores in the membrane respectively on the micrometer and nanometer scales. The water-pore wall interfacial slippage is considered. When the pore diameter is critically low (less than 1.82nm), the water flow in the nanopore is non-continuum and described by the nanoscale flow equation; Otherwise, the water flow is essentially multiscale consisting of both the adsorbed boundary layer flow and the intermediate continuum water flow, and it is described by the multiscale flow equation. For no wall slippage, the calculated water flow rate through the pore is very close to the classical hydrodynamic theory calculation if the pore diameter (d) is larger than 1.0nm, however it is considerably smaller than the conventional calculation if d is less than 1.0nm because of the non-continuum effect of the water film. When the driving power loss on the pore is larger than the critical value, the wall slippage occurs, and it results in the different scales of the enhancement of the water flow rate through the pore which are strongly dependent on both the pore diameter and the driving power loss on the pore. Both the pressure drop and the critical power loss on the pore for starting the wall slippage are also strongly dependent on the pore diameter.

• 대한환경공학회지
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• 제27권8호
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• pp.799-806
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• 2005

응집-UF 정수공정시 응집 전처리 공정에 있어 완속혼합없이 급속혼화만으로 충분한 응집의 효과를 기대할 수 있으며, 급속혼화장치로 in-line static mixer를 사용한 경우가 기존의 back mixer를 사용 한 경우보다 롤은 DOC 제거효율을 얻을 수 있었다. 또한, 적정 주입량인 16 mg alum/L에서 막의 투과 flux 감소가 가장 적게 나타났으며 적정 주입량보다 너무 적거나 또는 너무 많은 경우 모두 막의 투과 fiux 감소가 크게 나타났다. 또한 막의 fouling에 크게 영향을 미치는 것은 hydrophobic 물질로 이는 응집 전처리시 효과적으로 제거되어짐으로써 막의 투과 flux 감소를 줄일 수 있었다.

• 한국산학기술학회논문지
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• 제5권2호
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• pp.174-185
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• 2004

미세기공 중공사형 모듈을 이용한 비분산 막-용매 추출에 의하여 유기오염물을 페수로부터 분리하였다. 시스템은 향류 및 병류로 각각 진행되었으며, 분배계수의 비교로부터 MIBK가 분리용 용매로 선정되었다. 향류의 분리도가 병류보다 우수하였으며, 총괄물질전달계수도 구하였다.

• Macromolecular Research
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• 제11권5호
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• pp.347-351
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• 2003

The hydrophobic ligand-containing hollow polypropylene (PP) membranes were synthesized by the mutual radiation induced graft copolymerization with glycidylmethacrylate (GMA) onto hollow PP membrane followed by the subsequent functionalization with L-phenylalanine. FT-IR, elemental analysis and UV spectroscopy were utilized to characterize copolymer composition, and degree of grafting, functionalization conversion and ${\gamma}$-globulins adsorption. The degree of grafting on the PP surface increased with the reaction time and total dose of E-beam. In the subsquent functionalization, the amount of L-phenylalanine increased with the increase in the degree of grafting and the degree of conversion was about 30%. The ${\gamma}$-globulins adsorption experiments showed that adsorption capacity had a maximum value at pH 8. The ${\gamma}$-globulins adsorption capacity in the basic pH region was higher than in the acidic pH region.

• 한국막학회:학술대회논문집
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• 한국막학회 2003년도 The 4th Korea-Italy Workshop
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• pp.51-55
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• 2003

Membranes made with perfluorinated polymers are of particular interest due to the unique features demonstrated by these materials. Both highly hydrophobic and hydrophilic membranes have been developed from appropriate perfluoropolymers, which were in turn obtained by copolymerization of TFE with special monomers available at the industrial scale. Highly hydrophobic membranes obtained from the glassy copolymers of TFE and 2,2,4 trifluoro-5 trifluoromethoxy-1,3 dioxole (Hyflo $n^{ }$ AD) show properties which make them particularly suited for use in the field of gas-liquid contactors and membrane distillation. Hydrophylic highly conductive proton exchange membranes obtained from the copolymer of TFE and a short-side-chain (SSC) perfluorosulfonylfluoridevinylether (Hyflo $n^{ }$ Ion) find interesting application in the field of fuel cells, especially in view of the current tendency to move to high temperature operation.n.

• 청정기술
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• 제8권3호
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• pp.119-128
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• 2002

분획분자량이 50,000인 acrylonitrile과 vinyl chloride의 공중합체 재질의 한외여과막(KOCH Membrane System, HF1-45-CM50)과 분획분자량이 100,000인 polysulfone 한외여과막(KOCH Membrane System, HF1-43-CM100)을 사용하여 순수에 3% 농도로 희석한 수용성 합성 절삭유의 투과특성을 연구하였다. 친수성 분리막인 HF1-45-CM50은 합성 절삭유의 투과실험에서 높은 투과유속과 오일성분 투과율을 보였으나 소수성 분리막인 HF1-43-CM100의 경우에는 오일 투과율은 HF1-45-CM50과 유사하였으나 투과유속은 훨씬 저하되었는데 이는 합성 절삭유가 소수성 막의 표면을 쉽게 적셔서 친수성 막에 비해 더 심한 막오염을 유발시킨다는 것을 의미한다. 또한 분리막 재질의 특성이 합성 절삭유의 투과특성에 미치는 영향이 분리막의 평균 기공크기의 영향보다 훨씬 더 크다는 사실을 알 수 있었다. 막오염을 감소시키기 위해 질소에 의한 역세척 실험을 수행한 결과 역세척 효과가 친수성 분리막에서는 뚜렷이 나타났으나 소수성 분리막의 경우에는 오히려 투과유속의 감소를 초래하였다. 폐합성 절삭유에 의해 오염된 분리막의 세척실험에서는 세척용액에 분리막을 72시간 이상 침지시킨 후 역세척을 수행할때 가장 높은 투과유속의 회복율을 얻을 수 있었다.

• Korean Chemical Engineering Research
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• 제46권3호
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• pp.639-645
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• 2008

십자형 응집-한외여과 막분리 공정 운전시 응집조건에 따른 영향을 살펴보면 급속교반-UF 공정과 응집-침전-UF 공정에서 투과 flux의 변화는 크게 나타나지 않았으며 UF막의 막오염 억제 측면에서는 응집전처리공정으로서 1분간의 짧은 급속혼화만으로도 충분한 것으로 나타났다. 교반강도에 따른 투과 flux의 변화결과 교반강도에 따라 형성되는 floc의 크기가 거의 유사하게 형성되어 교반강도에 따른 영향은 나타나지 않았다. 응집제 주입량에 따른 투과 flux변화를 살펴보면 응집제 주입량이 증가함에 따라 유기물의 제거가 크게 일어나 유기물 부하의 감소와 floc의 크기가 증가함에 따라 다공성 케이크층의 형성에 따른 막저항의 감소로 인하여 투과 flux가 향상되었다. 막의 재질과 전처리 응집공정적용에 따른 여과메카니즘 분석결과 막의 재질에 따라서는 친수성 재질의 막에 비하여 소수성 재질의 막의 경우 막의 공극속으로 입자의 침투가 발생하여 침적 흡착되는 현상과 막의 표면에서 형성되는 cake층에 의한 투과 flux 감소가 주원인이 되었으며 응집공정을 전처리공정으로 적용시 UF단독공정에 비하여 막오염 발생이 저감되었다.

• Genomics & Informatics
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• 제14권2호
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• pp.53-61
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• 2016

Toxoplasma gondii is an intracellular Apicomplexan parasite and a causative agent of toxoplasmosis in human. It causes encephalitis, uveitis, chorioretinitis, and congenital infection. T. gondii invades the host cell by forming a moving junction (MJ) complex. This complex formation is initiated by intermolecular interactions between the two secretory parasitic proteins-namely, apical membrane antigen 1 (AMA1) and rhoptry neck protein 2 (RON2) and is critically essential for the host invasion process. By this study, we propose two potential leads, NSC95522 and NSC179676 that can efficiently target the AMA1 hydrophobic cleft, which is a hotspot for targeting MJ complex formation. The proposed leads are the result of an exhaustive conformational search-based virtual screen with multilevel precision scoring of the docking affinities. These two compounds surpassed all the precision levels of docking and also the stringent post docking and cumulative molecular dynamics evaluations. Moreover, the backbone flexibility of hotspot residues in the hydrophobic cleft, which has been previously reported to be essential for accommodative binding of RON2 to AMA1, was also highly perturbed by these compounds. Furthermore, binding free energy calculations of these two compounds also revealed a significant affinity to AMA1. Machine learning approaches also predicted these two compounds to possess more relevant activities. Hence, these two leads, NSC95522 and NSC179676, may prove to be potential inhibitors targeting AMA1-RON2 complex formation towards combating toxoplasmosis.

• 한국막학회:학술대회논문집
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• 한국막학회 2004년도 Proceedings of the second conference of aseanian membrane society
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• pp.7-10
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• 2004

Reversed micelles (RMs) are nanometer-scale molecular assemblies in organic media. Their surface films (membranes) are composed of surfactant molecules normally holding two hydrocarbon hydrophobic chains. Di-2-ethylhexyl sulfosuccinate (AOT), which is a negatively charged molecule, is most popular surfactant utilized to form reversed micelles.(omitted)

• 한국기후변화학회지
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• 제7권3호
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• pp.249-256
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• 2016

Porous $Al_2O_3$ hollow fiber membranes were successfully prepared by dry-wet spinning/sintering method. The SEM image shows that the $Al_2O_3$ hollow fiber membrane consists mostly of sponge pore structure. The contact angle and the breakthrough pressure were $126^{\circ}$ and 1.91 bar, respectively. This results indicate that the $Al_2O_3$ hollow fiber membranes were successfully modified to hydrophobic surface. The hydrophobic modified $Al_2O_3$ hollow fiber membranes were assembled into a membrane contactor system to separate $CO_2$ from a model gas mixture of the flue gas at elevated gas velocity. The $CO_2$ absorption flux was enhanced when the gas velocity increased from $1{\times}10^{-3}$ to $6{\times}10^{-3}$ m/s. Whereas the $CO_2$ absorption flux was decreased with the number of hollow fiber membrane of a module because of the concentration polarization. Furthermore, we developed an lab-scale $Al_2O_3$ hollow fiber membrane contactor modules and their system (i.e., $CO_2$ absorption using the $Al_2O_3$ membrane and monoethanolamine (MEA)) that could dispose of over $0.02Nm^3/h$ mixture gas (15% $CO_2$) with the removal efficiency higher than 95%. The results can be useful in a field of the membrane contactor for $CO_2$ separation, helping to design and extend a equipment.