• 멤브레인
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• 제22권4호
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• pp.243-250
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• 2012

본 연구에서는 정수처리용 알루미나 정밀여과 및 광촉매의 혼성공정에서 물역세척 주기(filtration time, FT) 변화의 영향을 알아보고, 탄소 정밀여과막 또는 알루미나 한외여과막을 사용한 기존 결과들과 비교하였다. 물역세척 시간(BT)는 10초로 고정한 채, FT를 2~10분으로 변화시키면서, 그 영향을 180분 운전 후 막 오염에 의한 저항($R_f$), 투과선속(J)과 총여과부피($V_T$) 측면에서 고찰하였다. FT가 감소할수록, $R_f$는 감소하고 J는 증가하여 탄소 정밀여과막 또는 알루미나 한외여과막을 사용한 기존 결과들과 동일하였다. 탁도의 처리효율은 98.1% 이상으로 높게 나타났으며, FT 변화에 의한 영향이 보이지 않아 탄소 정밀여과막을 사용한 기존의 결과와 유사하였다. 한편, 유기물의 처리효율은 FT 8분 조건에서 89.6%로 가장 높았으며, FT 변화의 영향이 보이지 않았고 기존의 결과들보다 다소 높은 유기물 제거율을 보였다.

• 한국습지학회지
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• 제13권2호
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• pp.161-169
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• 2011

본 연구는 여과와 침투기작을 이용한 개선된 여과형 시설의 비점오염물질 처리효율을 평가하고자 수행되었다. 저감시설은 지리학적 기후학적인 인자를 고려하여 기존의 저감시설의 단점을 보완하여 설계되었다. 저감시설의 처리효율 평가는 실험실 규모로 수행되었으며, 3가지 유형의 유속[초기강우(120 mL/min), 일반적인 강우(242 mL/min), 집중호우(500 mL/min)]을 적용하여 실험을 진행하였고, 이를 통하여 수질 분석 및 물수지를 산정하였다. 실험결과, 저감시설의 입자상 물질 제거 효율은 90%이상으로 높게 분석되었다. 3가지의 유속변화 실험 중, 집중호우의 경우에서 11~91% 범위로 낮은 제거효율을 보였는데, 이는 다른 유속에 비해 짧은 체류시간을 갖기 때문으로 판단된다. 또한 저감시설의 물수지 산정결과 침투량은 유출량의 약 1%에 불과하여 향후 저감시설 설계 시, 침투를 증가시키기 위해서 시설하부의 토양치환 등을 통한 침투량 및 저류량을 증가시킬 수 있는 기술적 접근이 필요하며, 이는 오염물질의 저감에 크게 기여할 것으로 판단된다.

• 설비공학논문집
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• 제20권12호
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• pp.820-824
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• 2008

Electret filter media are used in general ventilation filters, disposable respirators, vehicle cabin filters, vacuum cleaners and room air cleaners. There are basic mechanisms of interception, inertial impaction, diffusion, gravitational settling, electrostatic attraction by which an aerosol particle can be deposited onto a fiber in a filter. The ability of fine particle removal strongly depends on the electrostatic forces between particles and polarized fibers. Thus, the stability of the fiber polarization is a major factor in the reliability of electret filters. In this study, the electret filter is made by electrospinning process using Polystyrene which is dissolved by 5 : 5 of Tetrahydrofuran (THF) and Dimethylformamide (DMF). Also the electrical properties and the filtration performances of electrospun filter media are Quantitatively investigated. Electrical properties of electrospun filters have been studied on surface charge potential and surface charge density. Also the filtration performance of the electret filters are evaluated on collection efficiency. The surface charge potential and the surface charge density of electrospun PS filters are increased with increasing applied voltage and saturated at 30 kV of applied voltage. Also collection efficiency of electro spun filters is increased with increasing surface charge potential and surface charge density. But the surface charge potential is decreased by natural decay and it causes deterioration of particle collection efficiency.

• 한국수산과학회지
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• 제55권1호
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• pp.10-16
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• 2022

Interest in effluent treatment is currently increasing and the use of polymetric coagulants is considered as a pretreatment of physical filtration prior to effluent discharge to increase solids recovery. A jar test evaluated effluent treatment efficiency of polymeric coagulants for semi-recirculating aquaculture systems. The particle coagulation efficiency and distribution were evaluated at different polymer dosages in freshwater and seawater effluents. The polymer was added at 0.005-0.08 mL/g of total suspended solids (TSS) in the effluents. TSS in the supernatant after coagulation decreased with increasing polymer dose in the freshwater, while showing no corresponding changes with dose in the seawater. However, in all treatments for both effluents, the removal efficiency was above 90%, regardless of the dose in the tested range. Both the De Brouckere Mean Diameter (DBMD) and volumetric median diameter (VMD) were all above 100 ㎛ in the freshwater effluent. In the seawater effluent, the particle size appeared to be larger than that in freshwater, ranging from 400-1,000 ㎛ for both DBMD and VMD. Considering that the typical pore size of physical filtration in aquaculture is between 60 and 200 ㎛, the use of polymers is expected to improve the practicality of physical filtration for efficient treatment.

• 한국막학회:학술대회논문집
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• 한국막학회 1999년도 Energy Saving Membrane Separtion Systems 에너지 절약형 막분리 시스템
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• pp.93-116
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• 1999

MF membrane element was specially designed for water purification and VSA process which can solve the fouling problem. Especially VSA process is developed for the SK Chemicals' asymmetric microfiltration hollow fiber membranes. In case of outside-to-in filtration process, MF membrane element showed the excellent flux stability caused by cleaning ability of VSA process . Simultaneous back-washing with VSA consideratbly enhances cleaning efficiency. From the result the possibility of the replacement of chemical coagulation and sand filtration process with newly developed VSA process was revealed.

• 한국대기환경학회:학술대회논문집
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• 한국대기환경학회 2001년도 추계학술대회 논문집
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• pp.389-390
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• 2001

Deposition of polydisperse aerosols by Brownian diffusion was studied analytically using the penetration efficiency of monodisperse aerosols combined with the correlations among the moments of lognormal distribution functions. The analytic solutions so obtained were validated using the exact solution were applied to recalculate the filtration efficiencies of the existing experimental data for various filtration conditions. (omitted)

• 한국막학회:학술대회논문집
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• 한국막학회 1999년도 The 7th Summer Workshop of the Membrane Society of Korea
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• pp.63-66
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• 1999

MF membrane element was specially designed for water purification and VSA process which can solve the fouling problem. Especially VSA process is developed for the SK Chemical's asymmetric microfiltration hollow fiber membranes. In case of outside-to-in filtration process, MF membrane element showed the excellent flux stability caused by cleaning ability of VSA process. Simultaneous back- washing with VSA considerably enhances cleaning efficiency. Form the result, the possibility of the replacement of chemical coagulation and sand filtration process with newly developed VSA process was revealed.

• 대한환경공학회지
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• 제36권4호
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• pp.251-257
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• 2014

본 연구는 RO 해수담수화 전처리 공정으로써 응집 및 여과공정에 대하여 수행되었다. RO 시스템은 충분하고 안정적인 전처리를 통하여 RO 막오염을 완화 할 수 있는 우수한 수질을 공급할 수 있어야 한다. 본 실험은 RO 막 공정의 전처리로서 다양한 응집제 주입량, 응집 교반 강도 및 시간, 탁도, 여과속도 실험 조건을 사용하여 응집과 여과공정의 효과를 조사하기 위하여 수행되었다. 본 연구 결과 적합한 RO 공급수로 적절한 SDI 값을 나타내기 위한 최적 전처리 조건은 응집 pH 6.5, 탁도 4 NTU 이상 그리고 여재 충진 높이가 550 mm 이상인 것으로 나타났다. 그러나 응집교반 강도, 응집제 주입농도와 여과속도는 여과효율에 비교적 큰 영향을 미치지 않은 것으로 나타났다.

• 한국해양바이오학회지
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• 제9권1호
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• pp.8-13
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• 2017

Cost-effective microalgae harvesting methods are necessary for economical production of algal biodiesel. In this study, membranes with various pore sizes and materials were examined for their potentials in application to gravity-filtration of Tetraselmis sp. KCTC12432BP. For this test, 10 L of Tetraselmis sp. culture (2 g/L) was loaded on each membrane and filtration rates were measured. Among the tested materials, a woven cotton fabric showed the fastest water drain rate (0.73 L/hr) without serious cell leakage. Cell density of the concentrates after filtration was 6.8 g/L, indicating 3.4-fold concentration compared with the initial algal culture. The result suggests that the woven cotton fabric could serve as filtration membrane for harvesting Tetraselmis sp. among the tested ones.

• 한국물환경학회지
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• 제37권6호
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• pp.433-441
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• 2021

The aim of this study was to optimize the ozonation and ceramic membrane integrated process for greywater reclamation. The integrated process is a repeated sequential process of filtration and backwash with the same ceramic membrane. Also, this study used ozone and oxygen gas for the backwashing process to compare backwashing efficiency. The study results revealed that the optimum filtration and backwash time for the process was 10 minutes each when comparing the filtrate flow and membrane recovery rate. The integrated process was operated at three different operating conditions with i) 10 minutes for filtration and 10 minutes for ozonation, ii) 10 minutes for filtration and 10 minute for oxygen aeration, and iii) continuous filtration without any aeration for synthetic greywater. The integrated process with ozone backwashing could produce 0.55 L/min of filtrate with an average of 18.42% permeability recovery, while the oxygen backwashing produced 0.47 L/min and 6.26%, respectively. And without any backwashing, the integrated process could produce 0.29 L/min. This shows that the ozone backwash process is capable of periodically recovering from membrane fouling. The resistance of the fouled membrane was approximately 34.4% for the process with ozone backwashing, whereas the resistance was restored by 10.8% for the process with oxygen backwashing. Despite the periodical ozone backwashing and chemical cleaning, irreversible fouling gradually increased approximately 3 to 4%. Approximately 97.6% and 15% turbidity and TOC were removed by ceramic membrane filtration, respectively. Therefore, the integrated process with ozonation and ceramic membrane filtration is a potential greywater treatment process.