• Journal of Korean Society of Environmental Engineers
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• v.28 no.6
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• pp.613-619
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• 2006

The objectives of this research are to evaluate the effect of membrane materials, particulate matter and membrane pore size on permeate flux. It was shown that the removal efficiency of high MW organic matter more than 10 kDa was lower than that of low MW organic matter for $MIEX^{(R)}$ process. For the change of permeate flux by the pretreatment process, $MIEX^{(R)}+UF$ process showed high removal efficiency of organic matter as compared with coagulation+UF processes, but high reduction rate of permeate flux was presented through the reduction of removal efficiency of high MW organic matter. The pretreatment of the raw water significantly reduced the fouling of the hydrophilic membrane, but did not decrease the flux reduction of the hydrophobic membrane. Flux decline on MF process increased due to the pore clogging, while the permeate flux decline of UF process decreased due to the formation of cake layer. It was shown that particle matter was not effect on MIEX+membrane process. But, for coagulation+membrane process, particle matter was important factor on permeate flux.

• Membrane Journal
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• v.22 no.5
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• pp.359-368
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• 2012

For hybrid water treatment of high turbidity water, we used the hybrid module that was composed of photocatalyst packing between tubular membrane outside and module inside. Photocatalyst was PP (polypropylene) bead coated with $TiO_2$ powder by CVD (chemical vapor deposition) process. Water back-flushing of 10 sec was performed per every period of 10 min to minimize membrane fouling for modified solution was prepared with humic acid and kaolin. Resistance of membrane fouling ($R_f$) decreased as humic acid concentration changed from 10 mg/L to 2 mg/L, and finally the highest total permeate volume ($V_T$) could be obtained at 2 mg/L, which was the same with the previous results. Then, treatment efficiencies of turbidity and humic acid were above 98.9% and 88.7%, respectively. As results of treatment portions of UF, UF + $TiO_2$, and UF + $TiO_2$ + UV processes, turbidity was treated little by photocatalyst adsorption, and photo-oxidation. However, treatment portions of humic acid by adsorption and photo-oxidation were 2.5% and 12.3%, respectively. Compared with the previous results, treatment portions of humic acid by adsorption and photo-oxidation were different depending on membrane material and pore size. As simplified the process, the membrane fouling resistance after 180 minutes' operation ($R_{f,180}$) increased and the final permeate flux decreased a little.

• Journal of the Korean Society of Food Science and Nutrition
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• v.39 no.3
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• pp.455-460
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• 2010

This study was investigated the effect of the ultra filtration (UF) on extending shelf-life and increasing quality of Acer mono sap. To evaluate the quality changes of Acer mono sap before and after UF, crude ash, crude protein, minerals, free sugar, organic acid, pH, total acidity, browning index, turbidity and total microbial number were measured during storage periods at -1, 4 and $10^{\circ}C$. After UF, the ash, minerals, organic acid, total acidity, browning index and turbidity of Acer mono sap were slightly decreased, while the pH was slightly increased, and total microbial number was not detected. After UF, the pH, total acidity, browning index, turbidity and total microbial number of Acer mono sap were very stable during storage periods at -1 and $4^{\circ}C$. During the storage at $10^{\circ}C$, turbidity and total microbial number was slightly increased, while the pH of before UF was decreased and the total acidity, browning, turbidity and total microbial number was increased during storage periods. As the results of this study indicate application of UF on Acer mono sap could extend the shelf-life and quality without loss of natural minerals and useful components.

• Proceedings of the Korean Fiber Society Conference
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• 2003.04a
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• pp.275-278
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• 2003

실크 세리신은 누에(Bombyx mori)로부터 얻어지는 천연 거대분자 단백질로서, 누에고치실의 20~30%를 차지하고 있다. 세리신은 외부로의 자극으로부터 피브로인을 보호하는 역할을 하지만, 견사나 견직물을 얻기 위해서는 정련 공정에서 반드시 제거하게 된다. 현재 생산 현장에서는 비누/알칼리 정련법으로 세리신을 제거하고 있는데, 정련 폐액중에 포함되어 있는 세리신 단백질에서 분해된 각종 아미노산과 비누 및 강알칼리 약제로 인해 환경오염의 주된 원인이 되고 있다. (중략)

• Journal of Korean Society on Water Environment
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• v.25 no.1
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• pp.1-6
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• 2009

• Proceedings of the Membrane Society of Korea Conference
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• 1997.10a
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• pp.111-113
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• 1997

1. 서론 : "Engaged type"의 2축 RDM은 housing의 부피에 대한 막면적을 극대화시키고 회전방향을 엇갈리게 함으로서 유체의 겉보기속도를 증가시키고 막표면에서 난류와 2차흐름을(secondary flow)를 형성시켜 농도분극층이 감소하여 막오염을 최소화할 수 있다. 본 연구에서는 2축 RDM으로 실제 열간 압연유 폐수를 적용하여 농축실험을 하였으며 투과 특성과 농축수의 열간 압연유 입자 분포의 변화를 조사하였다.변화를 조사하였다.

• Proceedings of the Korean Fiber Society Conference
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• 1998.10a
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• pp.461-464
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• 1998

막의 면적에 비례되는 막분리 공정의 생산성은 넓은 표면적을 갖는 중공사막의 이용으로 가능해지므로 중공사막에 관한 연구가 활발하게 진행되어 해수의 담수화, 가정용수의 정화 등은 이미 실용화되었다. 해수의 담수화에 이용되는 역삼투(RO)막은 고압 하에서 무기이온의 제거, 가정용수의 정화에 이용되는 UF막은 저압 하에서 분자량이 비교적 큰 이물질의 분리에 사용되는 점이 다르다. 최근에는 해수에서 우라늄을 회수하기 위한 연구를 진행되고 있다. (중략)

• Proceedings of the Membrane Society of Korea Conference
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• 1998.06a
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• pp.171-221
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• 1998

막분리기술은 이제 분리, 정제만의 단순한 개념이 아니며 고도분리정제와 자원재활용등이 복합적으로 해결되는 효율적 공정으로서 "Zero discharge" 및 "Closed-loop System" 으로서의 개념을 가지고 있다. 이것은 Clean Technology의 개념으로서 Membrane기술의 향후 Vision이라고 할 수 있다. 국내에 적용되고 있는 UF/MF막의 용도는 다음과 같다. -수처리분야, 가정용정수기, 폐수처리분야, 식품/생물공정 분야, 전착도장, 흡수식 냉동기의 LiBr 용액정제, 흡수식 냉동기의 LiBr 용액정제

• Proceedings of the Korea Information Processing Society Conference
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• 2005.05a
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• pp.1057-1060
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• 2005

현재 상용 운영체제에서 사용되고 있는 AdvFS 파일시스템은 기존의 전통 Unix 파일시스템에 비하여 On-line 확장성,부하의 균형,성능 등에서 우수함을 가지고 있다. 본 논문은 AdvFS의 메타데이타 관리방법에 대하여 기술한다, 먼저 디스크 접근 시간에서 UFS의 inode의 구조보다 우수한 새로운 BMT 구조와 빈 디스크 공간관리 방법에 대해 고찰한다.그리고 Unix File System(UFS) 보다 우수함을 성능평가를 통하여 AdvFS 구조가 성능을 향상 시킴을 보이고 있다.

• Proceedings of the Membrane Society of Korea Conference
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• 1991.10a
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• pp.4-8
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• 1991

The characterization of pore properties (mean pore size and pore size distribution) of the active layer in a UF membrane is important not only in order to obtain information about the factors affecting pore formation during membrane manufacturing but also to understand deeply the mechanism of solute and solvent transport through pores. Many methods of characterizing quantitatively the pore properties of UF membranes have been suggested in the literature: solvent and gas flow measurement, bubble point determination, electron microscopy, gas adsorption/desorption measurement, rejection measurement etc. But most of these methods involve time-consuming procedures and involve some wellknown problems and uncertainties.