• 한국환경과학회지
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• 제12권3호
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• pp.281-286
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• 2003

This study was conducted to evaluate the feasibility of ammonia removal by zeolite adsorption in drinking water treatment. In generally, drinking water treatment process is conducted coagulation/flocculation, sedimentation, sand filtration and disinfection. We tested feasibility with two method, one is powdered zeolite dosing to coagulation tank and the other is to substitute granular zeolite for sand of sand filter. In powdered zeolite test, raw water is used tap water with putting of 2 mg/l of NH$_4$$\^$+/-N. Filtration of granular zeolite was conducted with 80 cm of effective column high and 120 m/d of flow rate. At above 100 mg/1 of zeolite dosage, ammonia concentration was decreased below 0.5 mg/l of NH$_4$$\^$+/-N in powdered zeolite test. But, turbidity was increased to 30 NTU by powdered zeolite dosage. That turbidity was scarcely decreased in generally coagulant using condition in drinking water treatment. In granular zeolite test, ammonia was not detected in treated water until 8 days. This result suggest that using of granular zeolite in sand filter could be removal ammonia in winter. But we need regeneration at zeolite filtration for ammonia removal. So, it is to make clear that zeolite regeneration ability was compared KCl with NaCl. The result reveal that KCl was more excellent than NaCl. Optimum regeneration concentration of KCl was revealed 100 mM. Regeneration efficient was not increased at pH range 10∼12.5.

• 한국패류학회지
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• 제25권2호
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• pp.161-171
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• 2009

동해안의 유용 이매패류인 대복 (Gomphina veneriformis; Bivalvia)을 대상으로 기초 생리, 생태적 특성을 파악하기 위해 수온과 염분에 따른 대복의 여과율 변동을 측정하였다. 실험에 사용된 먹이생물은 황색편모조강 Isochrysis galbana (KMCC H-002)를 f/2배지를 이용하여 고농도로 단일배양한 후 사용하였다. 여과율 측정은 간접 측정법을 이용하였고, 실험에 사용된 먹이생물은 광학현미경 하에서 혈구계산판을 이용하여 계수하였다. 수온별 대복의 여과율은 2, 3, 4년생 모두 저온에서 수온이 상승할수록 여과율이 급격히 증가하여 $15^{\circ}C$에서 최대로 나타났으며, 이 후 감소하는 동일한 경향을 보였다. 염분별 대복의 여과율은 2, 3, 4년생 모두 30-35 psu의 염분범위에서 최대로 나타났다. 연령별 대복의 여과율은 수온, 염분변화에 관계없이 2년생 대복이 가장 높은 여과율을 기록했고, 4년생 대복의 여과율이 가장 낮았다. 다항회귀분석 결과 수온별 대복의 여과율 곡선은 모든 연령군에서 대체적으로 저온 구간으로 치우친 경향을 나타내었고 온도계수 $Q_{10}$ 값 역시 저온에서 높게 나타나 저온의 영향을 많이 받는 것으로 나타났다. 염분별 여과율 곡선은 모든 연령군에서 대체적으로 고염 구간으로 치우친 경향이 나타나 저염분으로 갈수록 여과율이 감소한다는 것을 알 수 있었다. 본 연구의 결과로 조하대 부유섭식 이매패류인 대복은 비교적 저온에서 서식하며 넓지 않은 온도범위에서 서식하는 협온성생물이며, 좁은 염분범위에서 높은 여과율을 보이는 협염성종임을 확인할 수 있었다.

• 보존과학연구
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• 통권7호
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• pp.56-86
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• 1986

The aim of this study is to scientifical conservation for the Sin An Ship. The test object is Pinus massoniana and Cunninghamia lanceolata of Sin An Ship's timber .Comtrast object is water soaked fresh wood of Pinus densiflora and Cryptomeria japonica The results were as follows.1. M. C is 280.9% in high degraded Planking board,237.5% in low degraded Planking board,158.6% in fresh wood of Pinus densiflora,222.6% in Bulkhead167.3% in fresh wood of Cryptomeria japonica2. Absorption rate of P.E.G is good at heating condition ($55∼60^{\circ}C$), especially in highdegraded wood.3. The dimensional change of wood during air drying is somewhat shrinked That's 7.22% in low degraded Planking board9.8% in high degraded Planking board and 4.11% in water soaked Pinus densiflora.4. The dimensional change of wood during P.E.G treatment is mostly swollen of wery small quantity.5. Salinity in desalinization tank showed below 50 p.p.m. It's indicate the end of desalinization treatment.6. Filtration with filter paper was possible up to 40% concentration only. Key words :M.c ; Moisture Content, Absorption rate, Dimension change, Salinity, Filtration.

• 한국물환경학회지
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• 제31권5호
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• pp.523-532
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• 2015

Hydrocyclone is widely used in industry, for its simple design, high capacity, low maintenance and low operational cost. The objective of this study is to develop hydrocyclone coagulation and filtration system. The system is made of hydrocyclone ballasted coagulation with polyaluminium chloride silicate (PACS) and upflow filter to treat micro particles in urban storm runoff. Roadside sediment particles (< $200{\mu}m$) was mixed with tap water to make various turbid suspensions to simulate urban storm runoff. The filter cartridge was filled with polyethylene media system and ran 1hr per everyday and total operation time were 8.19hrs and backwashing everyday after end of operation. The operation condition of flowrate was $8.2{\sim}11.9m^3/day$ (mean $10.1m^3/day$) and surface overflow rate (SOR) based on filter surface area was $45.5{\sim}65.9m^3/m^2/day$ (mean $55.7m^3/m^2/day$). The range of PACS dosage concentration was 14.0~31.5 mg/L. As the results of operation, the range of removal efficiency of turbidity, SS were 81.0~95.8% (mean 89.5%) 81.8~99.0% (mean 91.4%), respectively. An increase of filtration basin retention time brought on increased of removal efficiency of turbidity and SS, and increase of SOR brought on decreased of removal efficiency. During the first flush in urban area, storm runoff have an high concentration of SS (200~600 mg/L) and the filtration bed becomes clogged and decreased of removal efficiency. Backwashing begins when the drainage pipe valve at the filtration tank bottom is completely open (backwashing stage 1). Backwashing stage 2 was using air bubbles and water jet washing the media for 5 mins and open the drainage valve. After backwashing stage 1, 2, 61.83~64.04%, 18.53~27.51% of SS loading was discharged from filtration tank, respectively. Discharged SS loading from effluent was 7.12~14.79% and the range of residual SS loading in fliter was 2.26~5.00%. The backwashing effects for turbidity, SS were 89.5%, 91.4%, respectively. The hydrocyclone coagulation and filtration with backwashing system, which came out to solve the problems of the costly exchange filter media, and low efficiency of removing micro particles of filter type nonpoint treatment devices, is considered as an alternative system.

• 대한환경공학회지
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• 제35권7호
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• pp.518-524
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• 2013

다목적 여과저류지에서 모래여재의 여과수 여과능, 적정한 표층폐색 제거주기 그리고 오염제거효율 등 설계와 운영요소를 파악하기 위하여 서로 다른 3가지 입경의 낙동강 준설토를 채운 파일럿 규모의 테스트베드를 운영하였으며, 여과저류지에서의 다양한 인공하천의 유속을 모사하기 위하여 표류수 유속을 0~40 cm/sec로 단계적으로 변화시켰다. 운영결과 여재표층의 슬러지를 7~13일의 주기로 제거함으로써 여과수량을 5~3 $m^3/m^2-day$로 유지할 수 있었고, 여과수량과 여재입경 그리고 표류수 유속 등의 차이에 의한 여과수의 수질차이가 없음을 알 수 있었다. 대부분의 오염제거는 표층 50 cm 부근에서 발생함을 알 수 있었고, 여과거리 2.4 m에서의 오염제거율은 탁도 80~95%, COD 20~30%, BOD 75~90%, T-N 5~20% 그리고 T-P 20~60%로, 주로 입자성 오염물의 제거율이 높은 것으로 나타났다.

• 공업화학
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• 제26권2호
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• pp.229-233
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• 2015

본 연구에서는 폐암을 유발하는 발암물질이며 다양한 문제의 원인이 되고 있는 유해물질인 미세먼지 제거특성을 조사하였다. 변수로는 습도, 초기미세먼지 주입량, 유속을 고려하였다. 실험결과 습도가 높은 경우 제거에 소요되는 시간동안 평균 농도는 낮아지지만, 최종농도에는 큰 차이가 없었다. 세 가지 초기미세먼지주입량의 변화는 모두 비슷한 제거경향을 나타내었다. 또한 유속이 0.6 m/s에서 0.3 m/s로 변할 경우 제거소요시간이 약 1.4배 증가하는 결과가 관찰되었다. 본 연구에서는 습도, 미세먼지 주입량, 유속 중 미세먼지 제거에 가장 큰 변화를 보이는 것은 유속으로 관찰되었다.

• Journal of Preventive Medicine and Public Health
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• 제5권1호
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• pp.43-48
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• 1972

5 bed sand filter, applying biological oxidation, was designed and studied on the treatment of water works. Never using any coagulant agent (drugs), which may cause water pollution in pre-treatment of head water, the auther attempt a high rate filtration by the microorganism (nitrofication bacteria) end plant which populate in multi layer sand beds. The result are as follows : In order to evaluate the oxygen effect on filtration, oxygen was injected in aeration tank attached to each filter tank while filtration, and $NH_3$ was tested as a representaiive ingredient. It was found out that the aeration method was more effective, with over 33% of $NH_3$ removal capacity, than the anerobic and this 5 bed filter showed double removal capacity of $NH_3$ by comparing with conventional sand bed (2 stage bed). According to the examination of two kind of head water, pre-treated with coagulant agent and activated carton, the filtration capacity was affected by the polluted condition of head water, resulting that lower value of pollution and slower velocity of filtration showed more efficiency of $NH_3$ removal. In this experiment $NH_3$ content tested in treated water had a fairly good correlation with others.

• 한국대기환경학회지
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• 제31권1호
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• pp.54-62
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• 2015

Small scale paint overspray booths are being operated nationwidely, for repair of passenger car body parts. paint aerosols are emitted from the paint overspray booth in operations. In paint overspray booth operations without ventilation system and air pollutants collection unit, it may land on nearby equipment. In this study a removal of sticky paint aerosol for application of the small-scale overspray paint booth. it's cause the surface of filter bag from generated sticky paint aerosol. To remove adhesion of paint aerosol the agglomerating agents are injected and mixed with sticky paint aerosols prior to reach the filter bag. The paint spray rate was set as $10{\pm}5g/min$ from air-atomized spray guns in the spray booth, injection rate of agglomerating was $10{\pm}5g/min$ in the mixing chamber. The filtration velocity including air pollutants varied from 0.2 m/min to 0.4 m/min. Bag cleaning air pressure was set as $5.0kg_f/min$ for detaching dust cake from surface of filter bag. Bag cleaning interval at the filtration velocity of 0.2 m/min was around 3 times longer than that of the 0.4 m/min. The residual pressure drop maintained highest value at the highest filtration velocity. Fractional efficiency of 99.952%~99.971% was possible to maintain for the particle size of 2.5 microns. Total collection efficiency at the filtration velocity of 0.2 m/min was 99.42%. During this study we could confirm high collection efficiency and long cleaning intervals for the test with filtration velocity of 0.2 m/min indicating an optimal value for the given dimensions of the test unit and test operating conditions.

• 상하수도학회지
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• 제19권1호
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• pp.38-46
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• 2005

In this research, we tried to combine the coagulation/sedimentation process as pre-treatment with UF membrane filtration to reduce the membrane fouling and to improve the permeate water quality. We used the Jet Mixed Separator (JMS) as coagulation/sedimentation process. We observed that the HPC and E.Coli can't be removed through the direct UF memebrane filtation of surface water. The removal efficiency of dissolved organic substances, indicated by E260 and DOC, was 40% and 15%, respectively. However, the removal efficiency of it increased two time as a result of combination of JMS process as coagulation/sedimentation pre-treatment. This was resulted from the formation of high molecular humic micro-floc through JMS process. The accumulation amount of irreversible cake layer which was not removed by backwashing was less than direct UF membrane filtration of surface water. Moreover, the loading rate of fouling induced substances, such as humic substances and suspended substances, on membrane surface decreased drastically through JMS process. As a result, the accumulation amount of irreversible cake on membrane surface was decreased.

• 한국대기환경학회지
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• 제11권4호
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• pp.361-367
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• 1995

This study has been carried out to investigate the filteration performance of Electrostatically Stimulated Fabric Filter(ESFF) at high temperature condition. The electric field was maintained parallel to the fabric surface. The benefits of ESFF are lower residual pressure drop, improvement of fine particle removal efficiency and increasing reduced rate of pressure drop during a filteration cycle, stable operation at higher filtering velocities. According to the variance of filtering velocities and dust loadings, the results are summarized as follows; By imposing an electric field on the filter, the reduced rate of pressure drop was 7.sim.18% at room temperature, and when filtering velocity was 1.8m/min and dust loading was 1g/m$^{3}$, the value of reduced rate of pressure drop was shown the highest. Under the electric field around the filter, the reduced rate of pressure drop was 10.sim.35% at high temperature, and when filtering velocity was 1.8m/min and dust loading was 1g/m$^{3}$, the value of reduced rate of pressure drop was shown the highest. Most of all, at high temperature, the value of reduced rate of pressure drop was resulted to 25%. Also the collecting efficiency was shown clearly improved. By the SEM photo analysis, the number of penetrated particles at the Conventional Fabric Filter was approximately two times that of Electrostatically Stimulated Fabric Filter.