• Advances in nano research
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• 제9권1호
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• pp.59-67
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• 2020

Filter cake formation during rotary drilling operation is an unavoidable scenario, hence there is need for constant improvement in the approaches used in monitoring the cake thickness growth in order to prevent drill-string sticking. This study proposes an improved model that predicts the growth of mud cake thickness overtime with the consideration of the addition of nanoparticles in the formulated drilling fluid system. Ferric oxide, titanium dioxide and copper oxide nanoparticles were used in varying amounts (2 g, 4 g and 6 g), and filtration data were obtained from the HPHT filtration test. The filter cakes formed were further analyzed with scanning electron microscope to obtain the morphological characteristics. The data obtained was used to validate the new filtrate loss model. This model specifically presents the concept of time variation in filter cake formation as against the previous works of constant and definite time. Regression coefficient which is a statistical measure was used to validate the new model and the predicted results were compared with the API model. The new model showed R² values of 99.9%, and the predictions from the proposed filtration model can be said to be more closely related to the experimental data than that predicted from the API model from the SSE and RMSE results.

• 상하수도학회지
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• 제23권2호
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• pp.207-214
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• 2009

This study examines the optimum filtration conditions in pretreatment of seawater desalination by reverse osmosis. For this purpose, Masan bay seawater is treated through a gravity filter column while $FeCl_3$ is added as coagulant. The conditions of coagulantd osage, media depth, filtration rate, and backwash time are evaluated. The study results show that the filtrate quality improved with increasing coagulant dosage, but head loss rapidly increased. After 4mg/L, the unit filter run volume reduced to less than $200m^3/m^2$. Considering the head loss development, 4mg/L is determined as the optimum dosage. The better filtrate qualities are obtained with depth of 100cm than that of 80cm. The two stage filtration, which outperformed the single stage filtration, is suggested for treatment of Masan bay. The filtration rate of 5m/h is decided as the optimum condition considering the head loss development. At 10m/h, the filtrate quality deteriorated even though the extent was minimal, and head loss increased rapidly. The backwash time of 10 min is decided appropriate.

• 한국미생물·생명공학회지
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• 제24권5호
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• pp.540-545
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• 1996

A facultative anaerobe Enterococcus faecium 19-46-4 was used to study the production of an antimicrobial substance in anaerobic conditions. Major part of the antibiotic activity was found in the culture filtrate of the bacterium. The active compound was extracted by an equal volume of iso-butanol and concentrated in vacuo (at 50$\circ$C) before purification by C-18 liguid column chromatography and HPLC. A chromatographically pure compound was obtained by two passages of HPLC columns, The compound appeared as a pale-yellow powder. The yield was about 2.5 mg 1$^{-1}$ culture filtrate. The compound was named as KIST 194. KIST 194 were identified as cholic acid (3$\alpha$, 7$\alpha$, 12$\alpha$-trihydroxy-5$\beta$-cholan 24-oic acid) based on its physico-chemical properties determined by UV, IR, $^{1}H-NMR, $^{13}$C-NMR, El-MS and LC-MS.

• 한국균학회지
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• 제14권4호
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• pp.273-280
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• 1986

Rhizorus oryzae의 생장 및 autolysis에 따른 여러가지 autolytic enzymes의 활성도 변화와 이 autolytic enzyme system을 이용한 원형질체 생성에 관하여 조사하였다. Autolytic·phase의 culture filtrate 내에 함유된 autolytic enzyme은 Rh. oryzae 균사체로부터의 원형질체 생성에 효율적인 세포벽 분해효소로 작용하였으며 Autolytic enzyme중 원형질체 생성은 proteolytic 및 chitosanase activity와 가장 긴밀하게 관련되어 있었다. 이와같은 autolytic enzyme을 이용한 원형질체 생성은 10시간 배양한 균사체에 0.5M mannitol을 사용하였을 때 최고의 수율을 보였으며 원형질 생성의 최적온도 및 pH는 각각 $25{\sim}30^{\circ}C$ 및 $6.0{\sim}6.5$로 나타났다 한편 18시간 배양된 균사체를 osmotic stabilizer와 aut-olytic enzyme을 1 : 1이 되도록 처리하고 5시간 동안 $30^{\circ}C$에서 incubation하여 얻은 원형질체를 주사전자현미경으로 조사한 결과 효소에 의하여 가수분해되는 세포벽 주변으로부터 원형질체가 형성되는 것을 확인하였다.

• 상하수도학회지
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• 제21권6호
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• pp.763-770
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• 2007

There are many design parameters affecting filtration efficiency such as filteration rate, media packing depth, size distribution, and so on. The sphericity, the ratio of the surface area of an equal volume sphere to the real surface area of the particles, is one of major physical characters of media. The effect of sphericity on the performance of anthracite filter has been investigated. Media from eight water treatment plants have been collected. The sphericity of each media has been calculated by using well known headloss equations such as Kozeny equation, Dahmarajah equation etc.. Columns packed with anthracite media having different sphericity have been used to compare headloss development, floc accumulation in the bed, particles in bed water, filtrate turbidities after backwash and so on. The repeated experiments have indicated that the sphericity of anthracite media may not have remarkable influence on the filter performance as it has been suspected. It also has been prospected in the experiment that the media of higher sphericity would store more particles in the bed and give better filtrate quality, if provided that the effective size and the size distribution of media would be the same.

• 방사성폐기물학회지
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• 제12권1호
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• pp.1-6
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• 2014

우라늄으로 오염된 토양을 복원하기 위해 실규모의 동전기제염장치로 제염하는 과정에서 많은 산폐액이 발생한다. 발생한 산폐액에 CaO를 가해 우라늄수산화물을 침전시켜 여과한 다음, 방사성 폐액을 줄이기 위하여 이 용액을 재사용하였다. 그러나 이 용액을 동전기에 재사용할 경우, 높은 농도의 칼슘 때문에 양극실에서 음극실로 용액이동 속도가 감소하여 여과포의 약화, 전선 부식, 음극면에 산화물 부착 등의 문제점이 발생하였다. 이 문제들을 해결하기 위하여 재생액에 황산을 넣어 $CaSO_4$로 침전시켜 칼슘을 제거하였다. 칼슘이 제거된 재생액을 사용하여 소형 동전기 장치에서 20 일간 토양제염 실험을 수행한 결과는 세척후 토양내 우라늄 잔류 농도가 0.35 Bq/g로 감소하였으며, 이는 증류수 제염한 결과와 유사하게 나타났다.

• 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.

• 대한환경공학회지
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• 제33권11호
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• pp.783-789
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• 2011

하수처리장에서 발생되는 잉여슬러지가 고온 호기 소화 반응을 거치면 슬러지부피가 크게 감소하게 된다. 그러나 고온 호기 소화 상등액에는 고농도의 유기물, 질소 및 인이 함유되어 있기 때문에 이들을 별도로 제거해 주어야만 한다. 본 연구에서는 고농도의 질소와 인의 제거에 많이 사용되는 방법인 Struvite 결정화 공법을 이용하여 고온 호기 소화 여액에 함유되어 있는 질소와 인을 제거하였다. 대상폐수의 암모니아성 질소와 인산염인의 평균농도는 각각 1716.5 mg/L 및 325.5 mg/L였다. 최적의 결정화 반응 조건을 결정하기 위하여 $Mg^{2+}$와 $PO_4^{3-}$의 주입량, pH, 교반 시간($t_d$), 교반 강도(G), 결정핵 주입 그리고 반응 온도를 결정하였다. Struvite 결정화 반응시 마그네슘원으로 $MgCl_2{\cdot}6H_2O$, 인산염인염의 원으로 $K_2HPO_4$를 이용하였다. 질소와 인의 제거를 위한 $Mg^{2+}:PO_4^{3-}:NH_4^+$의 적정 주입 몰비는 2 : 1 : 1과 2 : 2 : 1로 압축되었는데 각각의 주입 몰비에 따른 암모니아성 질소 및 인산염인의 제거효율은 전자의 경우에 각각 71.6% 및 99.9%였고, 후자의 경우에는 93.8%와 98.6%였다. Struvite 결정화 반응에서 반응 시간($t_d$)과 교반 강도(G)는 암모니아성 질소와 인산염인의 제거율에 큰 영향을 미치지 않았다. 또한 결정핵 주입과 온도의 영향에서도 같은 결과가 나타났다. 그러나 결정핵의 주입량이 증가함에 따라 슬러지 발생량이 감소하였으며, 온도의 증가에 따라 생성된 슬러지의 부피는 증가하는 것으로 나타났다.

• 한국분말재료학회지
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• 제19권6호
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• pp.398-404
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• 2012

This paper describes the spherical ammonium diuranate gel particles which are the intermediated material of the $UO_2$ microsphere for an VHTR(very high temperature reactor) nuclear fuel. The characteristics of the intermediate-ADU gel particles prepared by AWD(ageing, washing, and drying) and FB(fluidized-bed) apparatus were examined and compared in a sol-gel fabrication process. The electrical conductivity of washing filtrate from the FB treating and the surface area of dried-ADU gel particles were higher than those of AWD treating. Also, an internal pore volume in dried-ADU gel particles showed a more decrease in AWD treatment than FB treatment because of decomposition of PVA affected by the washing time. However, the internal microstructures of ADU gel particles were similar regardless of the process variation.

• 약학회지
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• 제1권1호
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• pp.1-2
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• 1948

The finely powdered entire harbs of Polygala japonica Houttuyn, a drug known as Yong Shin-Cho in Korea, were boiled with methanol and from the filtered extract the methanol was distilled off under diminished pressure and the aqueous solution of the residue was evaporated to dryness after being mixed with ignited magnesia. The dried mass was boiled with absolute alcohol, the filtered clear liquid was evaporated to a small volume and the precipitate Saponin produced by mixing with ether was filtered off. When the filtrate was again evaporated to the thickness of a syrup and allowed to cool for a few days in an ice box, crystalls were separated out in about 5% yield, which formed colorless columns, M. P. 142.deg., from methanol and had the formula $C_{6}$ $H_{12}$ $O_{5}$. On heating it with acetic acid anhybride and sodium acetate, its tetraacetyl derivative $C_{6}$ $H_{8}$ $O_{5}$(C $H_{3}$CO)$_{4}$ was obtained and which formed colorless needles, M. P. 62-5.deg., from ethanol. Their melting points, results of elementar analysis and other characteristics agreed with that of Polygalitol and its derivative. Finally they were proved to be identical with Polygalitol and its derivative, respectively, through determination of mixed melting points with the samples. Polygalitol was isolated from several plants of genus polugala e. g. P. amara, P. vulgaris, P. teunifolia, P. senega etc. The authors added to them another instance of identifying Polygalitol from the plant of genus polygala.olygala.