• 상하수도학회지
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• 제23권5호
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• pp.539-545
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• 2009

A feasibility of a pilot scale two-phase anaerobic digestion with ultra filtration system treating garbage leachate were evaluated. The treatment system consisted of a thermophilic acidogenic reactor, a mesophilic methanogenic reactor, and an UF membrane. The average COD removal efficiency of the treatment system was 95% up to the OLR of 3.1 g COD/L/d. The higher COD removal efficiency with membrane unit resulted from the removal of some portion of soluble organics by membrane as well as particulate materials. When the membrane unit was in operation, bulk liquid in acidogenic and methanogenic reactors was partially interchanged, which maintained the acidogenic reactor pH over 5.0 without external chemical addition. Also, with the production of methane in the acidogenic reactor, the organic loading rate of the methanogenic reactor reduced. The initial flux of the membrane unit was $50{\sim}60L/m^2/hr$, but decreased to $5 L/m^2/hr$ after 95 days of operation due to clogging caused by particulate materials such as fibrous materials in garbage leachate. To prevent clogging caused by particulate materials, a pretreatment system such as screening is required. With the improvement with membrane unit operation, the two-phase anaerobic digestion with ultra filtration system is expected to have the possibility of treating garbage leachate.

• 한국식품저장유통학회지
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• 제31권2호
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• pp.235-244
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• 2024

A nonthermally sterilized raw apple vinegar was manufactured using an ultra-fine filtration process (0.2 ㎛ membrane filter) and its quality was comparable to commercially available vinegar products. First, using apple concentrate as a raw material, it was possible to produce non-thermal sterilized Using a two-stage fermentation process of alcohol and acetic acid fermentations, a non-thermally sterilized raw apple vinegar with pH 2.94 and an acidity of 6.20% was produced from an apple concentrate. The fermentation process increased the browning index significantly. However, the fundamental quality parameters of the non-thermal sterilized raw apple vinegar (A) with sterilized apple vinegar (B) did not differ significantly. The pH (2.92-2.95) of apple vinegar (A and B) was higher than that (pH 2.65-2.70) of commercial vinegar (C and D), and the total acidity, which is in the range of 6.20-6.21% and 6.53-6.90%, respectively, was higher in samples C and D than in samples A and B. However, four kinds of organic acids were detected in non-thermal sterilized raw apple vinegar (A), and its total organic acid content (6,245.00 mg%) was significantly higher than that of other samples (B, C, D) (p<0.05). In particular, malic acid content, as a main organic acid in apples, was very high in sample (A) (244.83 mg%) and sample (B) (210.21 mg%), compared to commercial products C (125.78 mg%) and D (86.90 mg%). The total polyphenol content and antioxidant activity of fermented apple vinegar (A, B) were more than twice as high as those of commercial products (C, D). Vinegar A had higher total polyphenol content than vinegar B. The above results suggest it is possible to manufacture and commercialize non-thermal sterilized raw apple vinegar with higher organic acid content and antioxidant properties using ultra-fine filtration.

• 한국막학회:학술대회논문집
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• 한국막학회 1997년도 심포지움시리즈 Jan-97 수처리용 분리막 기술 및 응용
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• pp.55-62
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• 1997

In Japan, the membrane filtration is becoming a common technology for municipal water supply system especially for small plant. 6 years before (1991), the national research project of membrane filtration for small plant has started. The project was named as "MAC 21", MEMBRANE AQUA CENTURY 21. In the project the Ministry of Health and Welfare, 8 universities and 18 water treatment plant companies have been involved. This was the first attempt to research a common theme in joint with government, universities and private companies. After three years, the guide line for membrane filtration application for small plant has been established. This has promoted to install some actual plant. And also, another joint research for "RESEARCH OF MEMBRANE FILTRATION FOR ADVANCED WATER TREATMENT" has started in 1994 and completed in March, 1997. The project was named as MAC21. In the former project the main objectives were removal of turbidity and bacteria from water. However, in new project the objective was establishment of the further advanced membrane filtration technology which would be applicable for trace chemical components removal such as tri-halo-methane pre-courser, agricultural chemicals removal, offensive smell and taste removal and virus removal. For the objectives, application of nanofiltration and hybrid-system, a combination of micro-filtration ultra-filtration with biological, ozone and activated carbon treatment process have been studied. In addition, application of membrane filtration for treatment of back-wash waste water originated from membrane filters and conventional sand filters has.been studied. At the end of March of this year, about 30 membrane filtration plants are actually supplying the water, the total treatment capacity is about 6,000 m$^{3}$/day and another 20 will be installed within one year.led within one year.

• 대한약학회:학술대회논문집
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• 대한약학회 2002년도 Proceedings of the Convention of the Pharmaceutical Society of Korea Vol.2
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• pp.332.2-333
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• 2002

Three alkaline proteases. designated JB-1. JB-2, and JB-3, are extracellular enzymes produced by Bacillus spp. JB411 which was isolated korean soil. They were separated by DEAE-sepharose CL-6B gel. and further purified using ammonium sulfate precipitation. ultra membrane filtration. and Ultrogel AcA gel filtration. The optimun pH values of proteases IB-1. JB-2. and JB-3. were shown to be 9.5. 9.5 and 7.5. respectively. All three proteases were stable in the pH range of 5-11. (omitted)

• 한국수산과학회지
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• 제35권6호
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• pp.639-643
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• 2002

막분리여과 시스템을 이용한 수질환경의 조절과 인공종묘생산 어류의 성장에 미치는 영향을 조사하기 위하여 사육수의 수질분석, 세균상 조사 및 자어의 성장률 등을 조사하여 비교하였다. 실험구는 고압모래여과기구 (SFS)와 막분리여과시스템구 (WS)을 두었으며, 수질에 대해서는 pH, 염분도, $DO,\;SS,\;COD,\;NH_{4}^{+},\;NO_{2}^{-},\;NO^{-},\;DIN,\;DIP$를 분석하였다. 대부분의 분석항목에서는 SFS구와 UFS구에서 큰 차이가 없었으나, 염분도는 SFS구 $33.5\%_{cdot}$, UFS구 $30.2\%_{cdot}$이었으며, 55는 SFS구 15.5mL/L, 7.0mL/L으로써 염분도와 SS에 대해서는 낮은 값을 나타내었다. 세균상 및 총균수의 변동에서 자연해수의 $6{\times}10^{5}CFU/mL$은 SFS구에서 약 1/6의 비율로 낮아지고 9일째 이후 총균수와 Vibrio속이 급격히 증가하고 Acinetobacter속 및 Micrococcus속 세균이 급증하기 시작하였으나, UFS구에서는 Ajteromonas속 세균의 일부가 남아있는 것 이외에 실험기간 중 안정적인 세균상을 유지하였다 성장률은 SFS구가 전장 17.0mm (SGR 14.0)이었으며, UFS구가 18.8mm (SGR 14.3)로서 유의적으로 높은 성장을 나타내었다. 막분리여과시스뎀을 이용하여 무균해수를 종묘생산장에 공급하는 것은 수질환경의 안정과 제균효과에 의해 세균의 증식이 억제되므로 자치어의 사육환경이 안정적으로 유지되어 질 수 있는 것으로 판단된다.

• 한국식품영양과학회지
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• 제40권5호
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• pp.753-758
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• 2011

고로쇠수액의 채취적기인 3월에 채취한 수액과 후기인 4월에 채취한 수액의 이화학적 특성을 비교분석하고, 고로쇠 수액의 품질을 향상시키고자 한외여과 전후의 품질특성을 살펴보았다. 4월에 채취된 고로쇠수액이 3월에 채취된 수액보다 총균수 및 탁도가 높았지만, 한외여과 후 탁도는 비슷한 수준으로 감소하였고 미생물을 검출되지 않았다. 유기산, 총산, 유리당 및 총당 함량은 4월의 고로쇠수액이 3월 수액보다 약간 낮았지만, 조회분과 무기성분은 높은 함량을 나타내었다. 특히 칼슘은 3월과 4월에서 각각 129.40 및 166.38 mg/L로 4월이 높았다. 고로쇠나무 수액의 영양성분은 한외여과 후 약간의 감소를 나타내었지만 채취적기 이후(4월)에 채취되는 수액을 한외여과 할 경우 미생물제거 및 탁도 향상 등 품질을 향상시킬 수 있으며, 무기성분이 더 많이 함유되어 있기 때문에 영양적으로 우수할 것으로 판단되었다.

• 한국식품영양과학회지
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• 제39권3호
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• pp.455-460
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• 2010

본 연구에서는 고로쇠수액의 품질 및 저장성을 향상시키고자 한외여과 방법을 이용하여 한외여과 전후의 이화학적 특성과 저장 중 미생물 및 품질변화를 관찰하였다. 여과 전후 수액의 조회분, 조단백질, 무기성분, 유리당, 유기산 함량, pH, 총 산도 등 이화학적 특성에는 큰 변화가 없었으며, 여과 후 갈색도 및 탁도는 감소하였고 수액 내 미생물은 검출되지 않았다. 여과 전 수액의 pH는 저장 중 감소하였고, 총 산도, 갈색도 및 탁도는 증가하는 경향이었으나 여과 후 수액은 큰 변화가 없었다. 여과 전 수액의 초기 미생물수는 $1.7{\times}10^3\;CFU/mL$에서 저장 중 $4.7{\times}10^4\;CFU/mL$까지 증가하였고, 여과 후 수액의 미생물수는 -1과 $4^{\circ}C$ 저장 중 62일 동안 검출되지 않았으나 $10^{\circ}C$에서는 $4.8{\times}10^2\;CFU/mL$로 검출되었다. 이상의 결과로부터 한외여과는 수액의 이화학적 특성의 변화를 유발하지 않으면서 효과적으로 미생물을 제어할 수 있어 수액의 저장성을 향상시킬 수 있을 것으로 판단된다.

• 한국막학회:학술대회논문집
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• 한국막학회 1995년도 추계 총회 및 학술발표회
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• pp.102-105
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• 1995

The membrane separation process is being utilized to save energy in various fields such as the food, biotechnology, chemical, enviromental fields. Especially the use of ceramic membrane among various inorganic membranes is expected to expand to their excellent thermal, chemical and mechanical resistance. In this presentation, we would like to explain our ceramic membrane CEFILT MF for microfiltration and CEFILT UF for ultra-filtration, and the purification of fermentation products as the application example using CEFILT MF.

• 한국막학회:학술대회논문집
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• 한국막학회 1999년도 춘계 총회 및 학술발표회
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• pp.113-114
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• 1999

• 상하수도학회지
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• 제18권6호
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• pp.770-777
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• 2004

Three pilot-scale membrane systems were operated using lake water as influent in this study. Microfiltration (MF) membrane with pore size of 0.01 m was used in Systen I of which filtration mode was set at constant pressure of $1kgf/cm^2$. Ultrafiltration (UF) membranes with molecular cutoff (MWCO) of 80,000 and 13,000 were used in System II-1 and II-2, respectively. Constant flow mode was applied at the range between 0.7 and $1.5m^3/m^2{\cdot}d$ (average of $1.1m^3/m^2${\cdot}d) for System II-1 and between 0.37 and $1.65m^3/m^2{\cdot}d$ (average of $1.18m^3/m^2{\cdot}d$) for System II-2. In System I, the flux changed from $1m^3/m^2{\cdot}d$ to $0.2m^3/m^2{\cdot}d$ during the operation time of 5 months. System II showed recovery of 94% under the allowable maximum pressure of $3kgf/cm^2$ during the same operation period. From these results, the efficient operation was observed in constant flow mode with respect to filtration time and recovery. Average filtrate turbidity showed 0.0071 NTU in System I and 0.0054 NTU in System II, which implied that high turbidity removal was obtained in both MF and UF systems with no significant difference between MF and UF. From the fact that membrane flux depends largely on membrane type and operation mode, a guideline of optimum design and operation should be suggested for application of membrane systems to full scale water treatment.