• 한국지반공학회:학술대회논문집
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• 한국지반공학회 2008년도 추계 학술발표회
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• pp.407-426
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• 2008

The bentonite slurry has been used as the stabilize suspension for wet process bored pile construction in Thailand. The bentonite suspension has benefit on filtration in the sand layer, but it creates thick cake film along pile shaft and loose sedimentation at pile toe. The base grouting technique was widely used to rectify the soft base or loose sedimentation problem of bored pile. The base grouting technique was not increased only end bearing capacity, but was also more increase in skin friction capacity of the bored piles. The comprehensive researches on base grouting was carried out by installing PVC casing inside the shaft to allow the drilling through the pile base in order to collect the soil sample below the pile tip. The polymer based slurry recently was used to replace the bentonite slurry to overcome the thick cake film along pile shaft as well as loose sedimentation at pile toe. The extent research on polymer slurry by physical model was performed to verify the real behavior of polymer. The appropriate mixing ratio of polymer was proposed. The design skin friction coefficient, $\beta$ and end bearing coefficient, Nq, for sand layer base on fully instrumented tested pile were proposed. The application on remedial of the lose capacity bored pile with large displacement in Bangladesh was proposed and discussed.

• 대한환경공학회지
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• 제28권3호
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• pp.337-344
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• 2006

응집플록은 그 특성에 따라 분리막 오염에 지대한 영향을 미친다. 기존의 연구결과에서 보면, 자연입자에 의해 형성된 플록함유수는 인공입자에 의한 플록함유수에 비하여 낮은 투과량을 보이는 것으로 나타났다. 따라서 본 연구에서는 응집플록의 특성을 정량적으로 분석하고, 분리막 오염과의 상관성을 알아보고자 하였다. 이를 위해 응집 플록에 대한 image analysis, specific cake resistance 및 cake compressibility 등을 측정하였다. Image 분석은 플록의 fractal dimension을 구하는데 이용되었으며, dimension은 플록의 다공성, 크기나 표면의 거칠기를 표현하는데 유용하게 사용된다. 또한 케익 압축능은 플록이 쌓여 만들어진 막표면층의 특성을 분석하는데 사용되었다. 두 가지의 다른 특성을 가지는 플록으로서 자연입자를 핵으로 하는 응집플록과 카올린 입자를 핵으로 하는 응집플록을 선택하여 실험하였다. 실험결과에 따르면 자연입자와 인공입자에 의해 형성된 플록의 fractal dimension($D_2$) 값은 $1.79{\pm}0.07,\;1.84{\pm}0.06$을 각각 나타내었으며, 이것은 자연입자에 의해 형성된 플록이 인공입자에 의한 것 보다 더 다공성의 느슨한 형태로 존재하고 있다는 것을 나타내는 것이다. 자연입자에 의해 형성된 다공성의 느슨한 플록이 분리막 표면에서 케익층을 형성 할 때에는 상대적으로 쉽게 압축되어 케익비저항이 커지는 것을 확인하였다.

• 멤브레인
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• 제15권1호
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• pp.52-61
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• 2005

폴리에틸렌 정밀여과 모세관막을 이용한 벤토나이트 콜로이드 현탁액의 투과유속 감소특성을 검토하였다. 운전시간이 경과하면서 투과유속이 감소되는 원인은 막표면 위에서 케익층의 성장과 입자들에 의한 세공막힘 때문이었으며, 운전시간이 경과하여 정상상태에 도달하면 투과유속은 케익여과 모델에 의해 지배받는다. 운전압력이 높은 경우의 투과유속 감소는 세공막힘과 케익층이 치밀해졌기 때문이다. 운전압력이 증가함에 따라 J/J₁는 감소하였으며, 0.5 kg/sub f//㎠일 때의 45%, 2.0 kg/sub f//㎠일 때 38%로 감소하였다. 운전압력 0.5 kg/sub f//㎠에서 총 막오염에 대한 성분오염의 비율은 표준세공막힘 14.6%, 완전세공막힘 23.4% 그리고 케익여과 62.0% 이었다. 순환흐름속도의 증가로 인해 투과유속은 증가하였고, 그 효과는 운전압력이 1.0 kg/sub f//㎠일 때가 운전압력 2.0 kg/sub f//㎠ 경우보다 컸다. 세공크기가 0.34 ㎛인 막의 투과유속은 세공의 크기가 0.24 ㎛인 막보다 컸으며, 용액의 농도에 따른 투과유속은 농도가 낮은 용액이 컸다. 세공크기가 0.34 ㎛인 막의 막오염 형태는 유사하지만 농도가 200 ppm인 용액의 경우 1000 ppm인 용액에 비하여 상대적으로 미약한 세공막힘 현상을 보였다.

• 한국막학회:학술대회논문집
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• 한국막학회 2004년도 추계 총회 및 학술발표회
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• pp.237-240
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• 2004

• 한국식품저장유통학회지
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• 제16권5호
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• pp.754-758
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• 2009

본 연구는 폐기되고 있는 대두박을 기능성 식품 원료로 이용하기 위하여 대두박 70%에탄올 추출물로부터 Diaion HP-20 흡착수지를 이용하여 조사포닌을 분리 한 후 이들에 대한 항산화 효과 및 대장암세포 성장 억제효과를 조사하였다. Diaion HP-20 흡착 수지를 이용하여 분획한 물, 20% 및 100% 주정 분획물을 TLC상 확인한 결과 100% 주정분획물에서 조사포닌들이 함유되어 있음을 확인 할 수 있었다. 대두박 조사포닌은 $1,000\;{\mu}g/mL$ 고농도에서 60% 이상의 수소 공여능을 나타내었다. 또한 대두박 조사포닌이 $1,000\;{\mu}g/mL$의 농도로 처리된 흰쥐의 간 균질물에서 MDA의 생성량이 대조군의 $3700\;{\mu}mol\;MDA/g$ liver에 비하여 $1200\;{\mu}mol\;MDA/g$ liver로 낮게 나타내어 대두박 조사포닌은 고농도에서 항산화 효과가 있음을 알 수 있다. 대두박 조사포닌은 인체 대장암(SW480)세포의 성장을 농도 및 시간 의존적으로 억제하였으며, 대두박 조사포닌 $1,000\;{\mu}g/mL$의 농도로 처리군에서는 G1 phase의 비율은 감소한 반면 G2/M phase의 비율은 증가하여 G2/M phase를 억제하는 것을 추측할 수 있었다.

• Membrane and Water Treatment
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• 제9권5호
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• pp.373-383
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• 2018

Fouling by solids and microorganisms is the major obstacle limiting the efficient use of membrane wastewater treatment. In our previous study, two stages microalgae/membrane filtration system was proposed to treat anaerobic digested palm oil mill effluent (AnPOME). This two stages microalgae/membrane filtration system had showed great potential for the treatment of AnPOME with high removal of COD, $NH_3-N$, $PO_4{^{3-}}$, TSS, turbidity, and colour. However, fouling behavior of the membrane in this two stages microalgae/membrane filtration system was still unknown. In this study, empirical models that describe permeate flux decline for dead-end filtration (pore blocking - complete, intermediate, and standard; and cake layer formation) presented by Hermia were used to fit the experimental results in identifying the fouling mechanism under different experimental conditions. Both centrifuged and non-centrifuged samples were taken from the medium with 3 days RT intervals, from day 0 to day 12 to study their influence on fouling mechanisms described by Hermia for ultrafiltration (UF), nanofiltration (NF), and reverse osmosis (RO) filtration mode. Besides, a more detailed study on the use of resistance-in-series model for deadend filtration was done to investigate the fouling mechanisms involved in membrane filtration of AnPOME collected after microalgae treatment. The results showed that fouling of UF and NF membrane was mainly caused by cake layer formation and it was also supported by the analysis for resistance-in-series model. Whereas, fouling of RO membrane was dominated by concentration polarization.

• 감성과학
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• 제5권3호
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• pp.61-66
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• 2002

최근 고감성 PET 사를 이용하여 생산한 PET 직물은 고감성 의류용 직물로서 많이 사용되고 있다. 이러한 고감성 의류용 PET 직물은 다양한 공정을 거치면서 장력이나 열 등의 영향을 받음으로서 사의 물성의 변화를 초래하여 감성 의류용도의 PET 직물에 많은 결점을 유발시킴으로서 직물 생산시 공정조건 설정 등의 어려움에 직면하고 있다. 이러한 고감성 의류에 치명적인 문제를 유발하는 문제점에 관한 감성사 제조시의 공정조건 변화와 관련된 연구논문은 많이 발표가 되지 못하고 있다. 따라서 본 연구에서는 국내 7개 원사 Maker의 cake내의 Denier 별 PET 사의 물성을 균일한 길이의 Layer를 설정하여 분석, 조사하고 Layer 별 물성 차이와 습·건열 열처리 온도에 따른 사의 수축률 등을 비교함으로서 감성 의류용 직물 생산에 필요한 기초 물성 Data를 제공하고 PET 사의 품질향상을 도모함으로서 최종 감성 의류용 직물 소재 개발에 기여할 수 있는 기초자료를 제공하고자 한다.

• 상하수도학회지
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• 제32권2호
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• pp.77-87
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• 2018

In this study, the effects of operating conditions on the formation of reversible and irreversible fouling were investigated in the filtration using ceramic membrane for water treatment process. The effect of coagulation pretreatment on fouling formation was also evaluated by comparing the performance of membrane filtration both with and without addition of coagulant. A resistance-in-series-model was applied for the analysis of membrane fouling. Total resistance (RT) and internal fouling resistance (Rf) increased in the membrane filtration process without coagulation as membrane flux and feed water concentrations increased. Internal fouling resistance, which was not recovered by physical cleaning, was more than 70% of the total resistance at the range of the membrane flux more than $5m^3/m^2{\cdot}day$. In the combined process with coagulation, the cake layer resistance (Rc) increased to about 30-80% of total resistance. As the cake layer formed by coagulation floc was easily removed by physical cleaning, the recovery rate by physical cleaning was 54~90%. It was confirmed from the results that the combined process was more efficient to recover the filtration performance by physical cleaning due to higher formation ratio of reversible fouling, resulted in the mitigation of the frequency of chemical cleaning.

• 한국물환경학회지
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• 제21권1호
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• pp.29-33
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• 2005

In order to recycle the waste material and to develop the thickening unit of waste activated sludge from wastewater treatment facilities, the filtration bio-reactor equipped with a shadow mask filter module was employed for this work from which the operating properties and parameters were drawn. The sludge thickening and filtration unit is made of cylindrical acryl tank(12cm i.d. ${\times}$ 58cm height: working volume of 6L), where the flat-sheet type of shadow mask filter module(pore size: 220~250um, opening area: 34.8~39.6%) was installed and the effluent was withdrawn from the effluent port at the lowest point of the reactor, and the filtration was performed only by the hydraulic pressure. For evaluating the operating performance of this reactor, some parameters such as the solid-liquid separation of different biomass concentrations, the water quality of filtrate, the aeration cleaning time and the cleaning effect were investigated. Depending on the MLSS concentrations, the different time to withdraw 3L of filtrate was required in which the longer filtration time was necessary for the higher MLSS concentrations caused by the thicker formation of cake layer: 40 minutes for 5,000 mg/L, 70 minutes for 10,000 mg/L and 100 minutes for 15,000 mg/L, where the concentrations of SS were 8.9, 6.7 and 6.5 mg/L, respectively. Under the same operating conditions (the intensity of aeration cleaning: 80 L/min, MLSS: 10,000 mg/L), the proper aeration cleaning time was revealed 30 seconds, and the stable formation of cake layer was in the range of 10 to 15 minutes. Therefore, the shadow mask considered as a waste material can be of use as a filter material for the sludge thickening system.

• 상하수도학회지
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• 제25권5호
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• pp.681-689
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• 2011

Submerged membrane bio-reactor (SMBR) has several advantages such as high MLSS, long SRT, and low F/M ratio at wastewater treatment. So, this has widely applied over the world and many studies have been conducted. However, membrane fouling remains an inevitable problem. This study was investigated using bench-scale SMBR with three poeration modes. Raw waters were prepared by addition of starch, acetic and fibric acid to recovery water of zeolite. The efficiency of nitrification and COD were very stable as about 95% and 80%, respectively. And critical flux was 128.8L/$m^{2}$/hr. The result of biodegradability test was following values at the each mode : Ss+Xs/$C_{T}$=81.7%, 35.1% and 45.3%, $X_{I}+S_{I}/C_{T}=18.3%$, 64.9% and 54.7%. When particulate matters such as $X_{I}$ and $X_{S}$ in influent are increased, membrane fouling will take place more and more. A relative ratio of filtration resistance to the fouling occurred by the cake layer was increased when increased the portion of $X_{I}$ and polysaccharide. It was thought that the formation of cake layer was promoted due to bond between $X_{I}$ and vicid material s generated from the polysaccharide.