• 한국물환경학회지
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• 제30권3호
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• pp.311-318
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• 2014

The purpose of this study is to investigate the effect of various types of coagulant on dewaterability and settleability of sewage sludge for the application of dewatering process. Cationic organic coagulants and inorganic coagulants of the aluminium base were used; PAC (Poly Aluminium chloride, $Al_2O_3$ 17%) and C-210P (0.2%). After Jar test, PAC 26 mg/L and 0.2% C-210P 55 mg/L was decided as the optimum concentration of the coagulant according to zeta potential measurement. pH, alkalinity and viscosity were measured in all experiments and the data on sedimentation characteristics is analyzed by SDI, SVI sedimentation rate and solid flux. The SRF(Specific Resistance of Filtration) experiment was conducted with the result of single and dual injection system as the dewaterability experiment. As a result, the organic coagulant making large floc has good characteristics of sedimentation and agglutination. Also, it is observed that the organic coagulants injection has a better dewaterability efficiency of coagulants under the condition of the lowest SRF value, followed by dual and inorganic coagulants injection.

• 한국환경보건학회지
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• 제30권1호
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• pp.59-64
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• 2004

This study was carried out to investigate influencing factors of bisphenol A(BPA) removal characteristic in conventional water treatment systems to be connected with coagulation, sedimentation, filtration and disinfection. The result are summarized as follows; In BPA removal, optimal doses of PAC, alum, ferric chloride were 7.5 mg Al/L, 10.0 mg AI/L, 15.0 mg Fek. PAC was most effective coagulant to remove BPA. In coagulation process, BPA removal efficiency were increased about 2％ by adjusting pH of raw water as 6. At temperature rise 1$0^{\circ}C$, BPA removal efficiency were increased 0.94％. but BPA removal efficiency in sand filtration process were under 1 ％ie, so that BPA was almost not removed. At free chlorine dose 1, 2 mg/L, the reaction rate constant k in the BPA removal have been calculated to be 0.397, 0.953 min$^{-1}$ . At free chlorine dose 1, 2 mg/1-, degradation reaction of BPA was completed during 10 min and BFA removal efficiencies were 97.66, 99.99％ at this time.

• 한국물환경학회지
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• 제21권6호
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• pp.676-681
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• 2005

This study was researched for disinfection by-products (DBPs) by preozonation, prechlorination and/or postchlorination. DBPs including trihalomethanes (THMs), haloacetic acids (HAAs), halonitriles, and aldehydes were analyzed by the treatment steps of prechlorination, preozonation, sedimentation, filtration, and postchlorination comparatively. THMs were detected as $52.20{\mu}g/L$ after prechlorination and decreased during sedimentation and filtration process. The HAAs and aldehydes increased more during preozonaiton than prechlorination. However, chlorinated DBPs and aldehydes increased more by postchlorination. Chlorinated DBPs formed by preozonation increased 26% more than the chlorination process. If aldehydes were included in the total DBPs, DBPs increased up to 39% by preozonation. Preozonation could increase the removal efficiency of organic carbon during the coagulation and sedimentation processes. Ozonation might produce aldehydes that are not permitted for drinking water regulations. Also, DBPs were produced by preozonation than by chlorination. These results would bring a need for alternative disinfection studies to decrease DBPs.

• Journal of Advanced Marine Engineering and Technology
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• 제33권8호
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• pp.1187-1195
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• 2009

본 논문은 완전 혼화조를 이용한 폐수처리 공정의 응집특성에 대한 연구를 목적으로 한다. 완전 혼화조 시스템은 유체 저장조, 임펠러가 장착된 3단의 혼화 및 응집부, 응집보조제 및 응집제 주입부, 응집 침전조 그리고 제어부로 구성된다. 실험용 폐수는 터널 공사현장에서 폐수 슬러지를 수거하여 약 1,000NTU의 탁도를 갖도록 만들었다. 응집보조제의 주입량이 증가함에 따라 약 99% 정도까지 탁도 제거율이 증가하였으며, 응집제의 주입량이 일정한 범위 이상으로 증가하면 탁도 제거율이 감소하는 것을 알 수 있다.

• 산업기술연구
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• 제31권A호
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• pp.135-145
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• 2011

This study was conducted to analyze the cost effectiveness in line with total phosphorus standard enforcement of public sewage treatment facilities. The additional cost for the total phosphorus removal process was calculated to analyze the cost effectiveness of the advanced water purification process. The analysis results showed that the T-P removal by coagulation sedimentation was more efficient than the advanced water purification facilities in terms of facilities investment cost, and if the coagulation filteration was used for T-P removal, the activated carbon process among the advanced water purification techniques was more efficient in terms of facilities investment cost. In this study, the effects of the T-P removal process that will be additionally introduced according to the tightening of the effluent T-P standard were analyzed within a limit. The actual benefits of improved T-P concentration in the water source will provide diverse values, including the leisure water, environment improvement water, eco-system in the water source and industrial water, in addition to the advanced water purification.

• KSBB Journal
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• 제16권4호
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• pp.332-336
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• 2001

본 연구에서는 정수처리 중에서 BAC(Biological activated carbon) 처리의 생물분해능과 같이 NOM의 생분해성 부분을 제거하고자 로프형 미생물 담체를 침전조에 적용하는 공정을 시도하였다. 다양한 운전조건을 적용하여 DOC와 UV$_{254}$ 그리고, 탁도 제거효과를 평가하였는데, 담체 설치는 일반적인 정수처리 공정을 모사한 pilot plant에 첫 번째로 아무 전 처리도 거치지 않은 팔당원수를 바로 지나도록 하였고(Media 1), 두 번째는 팔당원수를 오존으로만 전처리한 후 지나도록 하였으며(Media 2), 세 번째는 전 오존과 응집-침전과정이 끝난 후 지나도록 하였다(Media 3). 원수의 DOC 농도는 1.3~3.4 mg/L이고, UV$_{254}$는 0.027~0.039 ($cm^{-1}$ /)이며, 탁도는 0.3~4.5 NTU 였다. 평균 DOC 농도는 media 1, 2, 3에서 각각 2.2 mg/L, 1.8 mg/L, 1.3 mg/L를 보였다. 반면에 침전조에서는 1.5 mg/L의 농도를 보여 media 3에서 가장 높은 제거량을 나타내었다. 평균 UV$_{254}$ 값은 media 1, 2, 3에서 각각 0.037 ($cm^{-1}$ /), 0.027 ($cm^{-1}$ /), 0.014 ($cm^{-1}$ /)를 나타내었으며, 침전조에서의 UV$_{254}$ 값은 media 3와 비슷한 0.014 ($cm^{-1}$ /)를 보였다. 평균 탁도는 media 1, 2, 3에서 각각 1.1 NTU, 0.9 NTU, 0.5 NTU를 나타내었다. 위의 결과를 보면 로프형 미생물 담체 침전조는 일반적인 침전 공정에 바로 적용할 수 있는 경제적인 장치로 활용 가능할 것이다.

• 멤브레인
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• 제23권6호
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• pp.460-468
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• 2013

가압식 MF공정의 전처리공정으로 침전지가 없는 혼화/응집공정에서 적정응집제 투입농도선정 및 유기물 제거성능을 평가하였다. 전처리 공정에서 생성된 플럭이 가압펌프의 임펠러에 의해 해체됨을 확인하였으며 원수탁도가 10 NTU 이하로 유입이 될 때, 혼화/응집조와 펌프후단에서 플럭형성을 위한 최적응집제 투입량은 4 mg/L (as PACl 17%)이었다. 이때의 DOC 제거율은 평균 43%이었으며, 응집제투입량을 계속적으로 증가시켜 8 mg/L (as PACl 17%)로 투입을 하였을 때, DOC 제거율은 평균 48%를 나타내어 제거율은 크게 개선되지 않았다. 전처리가 없는 PVDF 가압식 MF공정의 TMP는 0.54 bar에서 운영이 되었으며, 혼화/응집 전처리 공정을 적용하여 운영 시 TMP는 0.41 bar로 안정적인 운영이 가능하였다.

• 한국환경과학회지
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• 제31권8호
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• pp.677-689
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• 2022

In order to photocatalytically treat organic matter (COD_Cr) and chromaticity effectively, chemical coagulation and sedimentation processes were employed as a pretreatment of the leachate produced from landfill in Jeju Island. This was performed using FeCl₃·6H₂O as a coagulant. For the treated leachate, UV/TiO₂ and UV/TiO₂/H₂O₂ systems were investigated, using 4 types of UV lamps, including an ozone lamp (24 W), TiO₂ as a photocatalyst, and/or H₂O₂ as an initiator or inhibitor for photocatalytic degradation. In the chemical coagulation and sedimentation process using FeCl₃·6H₂O, optimum removal was achieved with an initial pH of 6, and a coagulant dosage of 2.0 g/L, culminating in the removal of 40% COD_Cr and 81% chromaticity. For the UV/TiO₂ system utilizing an ozone lamp and 3 g/L of TiO₂, the optimum condition was obtained at pH 5. However, the treated COD_Cr and chromaticity did not meet the emission standards (COD_Cr: 400 mg/L, chromaticity: 200 degrees) in a clean area. However, for a UV/TiO₂/H₂O₂ system using 1.54 g/L of H₂O₂ in addition to the above optimum UV/TiO₂ system, the results were 395 mg/L and 160 degrees, respectively, which were within the emission standard limits. The effect of the UV lamp on the removal of COD_Cr, and chromaticity of the leachate decreased in the order of ozone (24 W) lamp > 254 nm (24 W) lamp > ozone (14 W) lamp > 254 nm (14 W) lamp. Only COD_Cr and chromaticity treated with the ozone (24 W) lamp met the emission standards.

• 한국해양환경ㆍ에너지학회지
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• 제1권1호
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• pp.39-46
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• 1998

본 연구는 수중에서 PCB로 오염된 연안퇴적물 입자의 입자크기분포의 변화를 시뮬레이션 할 수 있는 수치모델을 제시한다. 이 모델은 입자의 침강과 연직확산과 함께 응집 현상을 포함하며 공간적으로는 연직방향으로 일차원 모델이다 연직방향 메커니즘에 대한 고려는 퇴적물 입자의 수중 체류시간을 계산하기 위함이다. 본 연구에서는 모델을 개발 제시함과 아울러 실제 미국의 한 사례지역에서의 PCB로 오염된 연안퇴적물의 입자크기분포를 사용하여 모델의 시뮬레이션 결과를 제시하였다. 이 결과 모의시간인 48 시간 내에 퇴적물 입자크기 변화가 상당히 진행되며 수중에서 입자크기별로 입자가 다르게 제거됨과 이 과정에서 응집이 중요한 요인이 될 수 있음을 보이고 있다. 본 연구에서 개발 제시된 모델은 준설 등 환경정화사업과 관련 불가피하게 수반될 수 있는 오염퇴적물의 재부유로 인한 오염확산범위를 평가하는데 유용하게 이용될 수 있다.

• Environmental Engineering Research
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• 제13권1호
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• pp.1-7
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• 2008

Recently a new technology called the flexible-fiber deep-bed filter (FDF) claimed to replace the conventional sand filter including coagulation and sedimentation filter (CSF) processes in the water treatment plant. Therefore the life cycle assessment (LCA) approach was applied for evaluating the life cycle impacts of FDF compared with those of CSF. The used LCA softwares were the Simapro 6 and PASS and their life cycle impact assessment (LCIA) methodologies were the Eco-indicator 99 and the Korean Eco-indicator, respectively. The goal of this LCA was to identify environmental loads of CSF and FDF from raw material to disposal stages. The scopes of the systems have been determined based on the experiences of existing CSF and FDF. The function was to remove suspended solids by filtration and the functional unit was $1\;m^3$/day. Both systems showed that most environmental impacts were occurred during the operation stage. To reduce the environmental impacts the coagulants and electricity consumptions need to be cut down. If the CSF was replaced with the FDF, the environmental impacts would be reduced in most of the impact categories. The LCA results of Korean Eco-indicator and Eco- indicator99 were quite different from each other due to the indwelling differences such as category indicators, impact categories, characterization factors, normalization values and weighting factors. This study showed that the life cycle assessment could be a valuable tool for evaluating the environmental impact of the new technology which was introduced in water treatment process.