• Title/Summary/Keyword: Advanced water treatment system

검색결과 202건 처리시간 0.027초

인공신경망 모형을 이용한 급속혼화공정에서 적정 응집제 주입농도 결정 및 응집처리후 탁도의 예측 (Prediction of Turbidity in Treated Water and the Estimation of the Optimum Feed Concentration of Coagulants in Rapid Mixing Process using an Artificial Neural Network Model)

  • 정동환;박규홍
    • 한국물환경학회지
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    • 제21권1호
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    • pp.21-28
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    • 2005
  • The training and prediction modeling using an artificial neural network was implemented to predict the turbidity of treated water as well as to estimate the optimized feed concentration of polyaluminium chloride (PACl) in a water treatment plant. The parameters used in the input layers were pH, temperature, turbidity and alkalinity, while those in output layers were PACl and turbidity of treated water. Levenberg-Marquadt method of feedforward back-propagation perceptron in the neural network toolbox of MATLAB program was used in this study. Correlation coefficients of the training data with the measured data were 0.9997 for PACl and 0.6850 for turbidity and those of the testing data with measured data were 0.9140 for PACl and 0.3828 for turbidity, when four parameters at input layer, 12-12 nodes each at both the first and the second hidden layers, and two parameters(PACl and turbidity) at output layer were used. Although the predictability of PACl was improved, compared to that of the previous studies to use the only coagulant dose as output layer, turbidity in treated water could not be predicted well. Acquisition of more data through several years obtained with the advanced on-line measuring system could make the artificial neural network useful and practical in actual water treatment plants.

Monitoring and Characterization of Bacterial Contamination in a High-Purity Water System Used for Semiconductor Manufacturing

  • Kim, In -Seop;Lee, Geon-Hyoung;Lee, Kye-Joon
    • Journal of Microbiology
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    • 제38권2호
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    • pp.99-104
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    • 2000
  • Hydrogen peroxide has been used in cleaning the piping of an advanced high-purity water system that supplies ultra-high purity water (UHPW) for 16 megabyte DRAM semiconductor manufacturing. The level of hydrogen peroxide-resistant bacteria in UHPW water was monitored prior to and after disinfecting the piping with hydrogen peroxide. Most of the bacteria isolated after hydrogen peroxide disinfection were highly resistant to hydrogen peroxide. However, the percentage of resistant bacteria decreased with time. The hydrogen peroxide-resistant bacteria were identified as Micrococcus luteus, Bacillus cereus, Alcaligenes latus, Xanthomonas sp. and Flavobacterium indologenes. The susceptibility of the bacteria to hydrogen peroxide was tested as either planktonic cells or attached cells on glass. Attached bacteria as the biofilm on glass exhibited increased hydrogen peroxide resistnace, with the resistance increasing with respect to the age of the biofilm regrowth on piping after hydrogen peroxide treatment. In order to optimize the cleaning strategy for piping of the high-purity water system, the disinfecting effect of hydrogen preoxide and peracetic acid on the bacteria was evaluated. The combined use of hydrogen peroxide and peracetic acid was very effective in killing attached bacteria as well as planktonic bacteria.

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리튬 함유 폐액에서의 리튬 농도와 생태독성과의 연관성 연구 (Correlation between Lithium Concentration and Ecotoxicoloigy in Lithium Contained Waste Water)

  • 진연호;김보람;김대원
    • 청정기술
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    • 제27권1호
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    • pp.33-38
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    • 2021
  • 리튬계 이차전지의 수요는 휴대전화 및 전기자동차 등의 관련 산업의 폭발적인 성장과 더불어 크게 증가하고 있으며, 한국은 전 세계 이차전지 사업의 40%를 점유하는 리튬 이차전지 제조 강국이다. 폐기된 리튬 이차전지의 경우 대부분은 스크랩 형태로 유가금속 회수 차원에서 재활용되고 있으나, 코발트와 니켈 등 유가금속 회수 후 폐액은 잔류 리튬 농도에 따라 일부 폐기되고 있으며, 제조 공정 시 발생하는 폐액에 관한 연구는 전무하다. 뿐만 아니라 리튬 이온 농도에 의한 수계 오염 가능성에 관한 연구는 시도되지 않았으며 해마다 공공하수처리시설의 방류수 수질기준은 엄격해지고 있다. 본 연구에서는 고성능 장시간 목적으로 사용되는 고니켈계 NCM 양극재 제조 공정에서 전극 코팅을 위한 공정에서 발생하는 폐액에 대하여 분석하고, 폐액 처리공정에 대한 과정을 제시하였다. 제안한 제조 공정 폐액 처리 공정별 리튬 이온의 농도 및 pH 영향에 따른 수질오염 척도인 생태독성과의 연관성에 대하여 수질검사와 함께 물벼룩 생태독성 시험을 통해 상관관계를 분석하였다. 또한, 다른 산업군의 생태독성 시험과의 비교를 통해 향후 리튬 공장 폐액에 대한 현실적인 처리 방안에 대하여 서술하였다.

시공간 동시분할 공정 시뮬레이션을 통한 질소 및 인 제거 최적화 방안 (Optimization of Nitrogen and Phosphorus Removal of Temporal and Spatial Isolation Process by Model Simulation System)

  • 유동진;장덕;신형수;박상민;홍기호;김수영;김명준
    • 한국물환경학회지
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    • 제23권2호
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    • pp.206-215
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    • 2007
  • The objective of this study was to establish the optimal system operating strategies for nitrogen and phosphorus removal through model simulation system built for advanced wastewater treatment targeting on simultaneous temporal/special phase isolation BNR process. The simulation system was built with unit process modules using object modules in GPS-X code. The system was well verified by field experiment data. Simulation study was carried out to investigate performance response to design and operation parameters, i.e. hydraulic retention time (HRT), solids retention time (SRT), and cycle time. The process operated at HRTs of 10~15 hours, longer SRTs, and cycle time of 2 hours showed optimal removal of nitrogen. The HRTs of 10~15 hours, SRTs of 20~25 days, and longer cycle time was optimal for phosphorus removal. Both simulation and field studies showed that optimal operating strategies satisfying both the best nitrogen and phosphorus removals include HRTs ranged 10~15 hours, SRTs ranged 20~25 days, and cycle times of 4~8 hours. The simulation system with modularization of generalized components in BNR processes was, therefore, believed to be a powerful tool for establishing optimal strategies of advanced wastewater treatment.

우리 나라의 하수도현황과 전망 (State of Swerage Systems and Prospects in Korea)

  • 김갑수
    • 환경위생공학
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    • 제8권2호
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    • pp.65-84
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    • 1993
  • This study reviewed the current status and problems of sewerage system in Korea and then proposed possible methods to correct the problems. Also, evaluation of future development in sewerage system is included. It can be summarized as follows : 1. Investment in sewerage system is relatively low . 0.23% of GNP, Considering that the investment portion is 0.35% in OECD and 0.63% in Japan, it should be increased further. 2. The reasons wily the investment in sewerage system is low can be ' (1) Low priority is given to the investment in sewerage system. Local government builds and operates its own wastewater treatment plant. Local government as well as residents prefer to invest their money in roadwork, housing and parks to in wastewater treatment facilities because of greater investment effects. (2) Besides capital investment, more maintenance cost is needed for sewerage system. Proper operation of wastewater treatment facilities requires a well-trained operator. Because of public conception that operation of wastewater treatment facility is a dirty job, it is difficult to find a well-trained operator. (3) It is difficult to estimate the effect of sewerage system (4) Cost required to build and maintain wastewater treatment facility should be paid by people, who benefit from the facility. People to benefit are sometimes different from people to pay. 3. Advanced treatment is necessary to protect the bay aura and raw water source as well as to prevent eutrophication of lakes and ponds. 4. Wastewater treatment facility were mainly build in big cities during the decade of 1980. Followings should be solved first to expand the facilities. (1) Rapid repair and construction of sewer. (2) Technical development of wastewater treatment . Prevention of efficient and economical wastewater . Development of efficient and economical wastewater treatment techniques . Development of high-efficiency treatment using bioreactor . Reuse of wastewater treatment plant effluent (3) Sludge treatment and disposal . Composting of sludge cakes . Development of techniques to reduce the volume of sludge cake : incineration and reuse of sludge ash and slag. (4) Utilization of wastewater treatment facilities . Construction of community parks or sports families(ie, on the tops of the covered aeration tanks and sedimention tanks) Construction of wastewater treatment facilities under ground and of parking facilities and community parks above ground. (5) Education of wastewater treatment personal.

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미세기포 오존과 생물여과 시스템을 이용한 생활하수의 3차 처리에 관한 연구 (Tertiary Treatment of Sewage by Micro Bubble Ozone and BAF System)

  • 강동한;장영호;김종수;김극태
    • 한국물환경학회지
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    • 제27권6호
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    • pp.877-884
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    • 2011
  • In this paper, the removal characteristics of dissolved organic carbon (DOCs) by micro bubble ozonation process and $O_3/UV$ process were comparatively studied. In the point of DOC removing reaction coefficient, micro bubble ozonation system and $O_3/UV$ process had not significant difference, $0.0120sec^{-1}$ and $0.0141sec^{-1}$. Therefore micro bubble ozonation process is more suitable for tertiary treatment of sewage in the point of installation and maintenance cost-reducing. The optimum ozone injection rate was 2.0 g $O_3/g$ DOC and HRT was 3 min for the micro bubble ozonation process. The removal efficiency of DOC and SUVA in micro bubble ozonation system was 32.8% and 58.3% respective. Biological aerated filter (BAF) process was installed to remove soluble organic material increased by micro bubble ozonation system. And the effluent BOD of BAF was below 1.0 mg/L. In the view of cost-effectiveness, $O_3/BAF$ process was more profitable than $O_3/UV/BAF$ process for tertiary treatment of sewage. In order to nitrify ammonia in the BAF process completely, $NH_4{^+}-N$ concentration in the influent water of BAF should be designed considering low water temperature in the winter season.

세라믹 정밀여과에 의한 고도정수처리 시스템에서 물 역세척 시간 및 주기의 영향 (Effect of Water-back-flushing Time and Period in Advanced Water Treatment System by Ceramic Microfiltration)

  • 박진용;이혁찬;조재형
    • 멤브레인
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    • 제18권1호
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    • pp.26-34
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    • 2008
  • 본 연구에서 처리수를 이용한 주기적인 역세척은 세라믹 정밀여과에 의한 고도정수처리 시스템에서 막오염을 저감하고 투과선속을 향상시키고자 수행되었으며, 물 역세척 주기(FT) 및 시간(BT)의 영향과 최적 운전조건을 규명하고자 하였다. FT의 영향을 알아보기 위해 일정한 BT 3초에서 FT를 $30{\sim}120$초로 변화시켰고, BT 영향 실험에서 일정한 FT 120초에서 BT를 $3{\sim}12$초로 변화시켰다. 그리고 다른 운전변수인 막간압력차는 1.52 bar, 물 역세척 압력 0.98 bar, 유입유량 0.5 L/min, 공급액의 온도 $20^{\circ}C$로 일정하게 유지하였다. 그 결과, 일정한 BT 3초에서 본 실험 범위의 최적 FT는 30초로, 이것은 빈번한 역세척이 막오염의 저감에 더 효과적임을 의미한다. 그러나 너무 짧은 BT로 인하여 FT의 영향은 크지 않았다. 한편, 일정한 FT 120초에서 BT가 증가함에 따라 막오염에 의한 저항($R_f$)은 감소하고 투과선속(J)과 무차원화한 투과선속 ($J/J_o$)은 증가하는 경향을 나타내어, 최대 BT인 12초에서 가장 많은 총여과부피($V_T$)를 얻을 수 있었다.

제주특별자치도 상수도 기후위기 적응대책 연구 (A study on adaptation measures to climate crisis for water supply system of Jeju Special Self-Governing Province)

  • 김진근
    • 상하수도학회지
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    • 제37권6호
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    • pp.447-456
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    • 2023
  • Risk assessment on Jeju Special Self-Governing Province(JSSGP)'s water supply facilities and establishment of adaptation measures for climate crisis factors were implemented. JSSGP's vulnerability to the climate crisis was high in the order of drought, heat wave, heavy rain and strong wind. As a drought adaptation measure, policies of water saving and revenue water ratio improvement were considered. As for the heat wave adaptation measure, the introduction of an advanced water treatment process was suggested in response to the increase of algae cell number which resulting in taste and odor problem. As for heavy rain adaptation measures, the installation and operation of automatic coagulant injection devices for water purification plants that take turbid surface water were proposed. As a measure to adapt to strong winds, stabilization of power supply such as installation of dual power line was proposed in preparation for power outages. It is expected that water facilities will be able to supply high-quality tap water to customers even under extreme climate conditions without interruption through risk assessment for climate crisis factors and active implementation of adaptation measures.

DOF(Dissolved Ozone Flotation) 시스템을 이용한 하수처리장 방류수의 고도처리에 대한 연구 (Advanced Secondary Wastewater Treatment Using the DOF (Dissolved Ozone Flotation) System)

  • 이병호;김상희
    • 상하수도학회지
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    • 제19권6호
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    • pp.767-774
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    • 2005
  • The DOF (Dissolved Ozone Flotation) system was used to treat the effluent of the secondary wastewater treatment plant. The DOF system uses ozone instead of air, while DAF (Dissolved Air Flotation) uses air. Moreover, since the solubility of ozone is higher than air, the DOF system produces larger volume of micro-bubbles than the DAF system does. Thus, the DOF system performs better than the DAF system in floating ability. The DOF system could remove 70% of turbidity to an average of 0.59NTU in effluent from 2.31NTU in influent. The removal efficiency of absorbance measured with UV-254 in the effluent of the DOF system was 63%, while only 19% was removed by the DAF system. the DOF system removed 84% of the color from 25~26CU to 4CU, while DAF system removed 42% of the color to 15 CU. The CODMn removal efficiency of the DOF system was 34%, 6.8mg/l of effluent $COD_{Mn}$ concentratin, while it was 20%, 8.3mg/L of effluent $COD_{Mn}$ concentratin, to use the DAF system. Microbial bacteria such as coliform bacteria, and heterotrophic bacteria were removed over 99% by the DOF system, and 42~45% by the DAF system. That is, Microbial bacteria were almost completely destroyed by the DOF system. To sum up with, the DOF system was found to be very effective to treat effluent of the wastewater treatment plant.

고도정수처리용 대용량 오존발생시스템 개발 (The Development of Ozone Generation System with High Capacity for Advanced Water Treatment Process)

  • 이형호;김영배;서길수;조국희
    • 대한전기학회:학술대회논문집
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    • 대한전기학회 1999년도 하계학술대회 논문집 E
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    • pp.2001-2003
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    • 1999
  • Recently the ozone generation system is well used for cleaning the contaminated water by using the strong oxidization effects of ozone. Ozone generation system is composed of ozone generation device, air or oxygen supply device and high voltage apply device. In this paper, commercial frequency was applied to the wire typed conductor. The ozone concentration was measured with air or oxygen as a supplied gas, which can be used as basic data for the development of ozonizer system.

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