• 제목/요약/키워드: Water-treatment sludge

검색결과 628건 처리시간 0.033초

Wastewater Treatment Plant Control Strategies

  • Ballhysa, Nobel;Kim, Soyeon;Byeon, Seongjoon
    • International journal of advanced smart convergence
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    • 제9권4호
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    • pp.16-25
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    • 2020
  • The operation of a wastewater treatment plant (WWTP) is a complex task which requires to consider several aspects: adapting to always changing influent composition and volume, ensuring treated effluents quality complies with local regulations, ensuring dissolved oxygen levels in biological reaction tanks are sufficient to avoid anoxic conditions etc. all of it while minimizing usage of chemicals and power consumption. The traditional way of managing WWTPs consists in having employees on the field measure various parameters and make decisions based on their judgment and experience which holds various concerns such as the low frequency of data, errors in measurement and difficulty to analyze historical data to propose optimal solutions. In the case of activated sludge WWTPs, parts of the treatment process can be automated and controlled in order to satisfy various control objectives. The models developed by the International Water Association (IWA) have been extensively used worldwide in order to design and assess the performance of various control strategies. In this work, we propose to review most recent WWTP automation initiatives around the world and identify most currently used control parameters and control architectures. We then suggest a framework to select WWTP model, control parameters and control scheme in order to develop and benchmark control strategies for WWTP automation.

알칼리-오존 동시 전처리된 잉여슬러지로부터 결정화를 이용한 고품질 외부탄 소원 회수 (Recovery of high quality external carbon sources using crystallization from pretreated excess activated sludge by alkali and ozone)

  • 서인석;김홍석;김병균;김연권
    • 상하수도학회지
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    • 제22권6호
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    • pp.641-646
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    • 2008
  • In this research, recovery of high quality organics from excess activated sludge and its potential as a external carbon sources for BNR process was studied. By simultaneous treatment of alkali and ozone, TSS concentration was reduced by 32%, and RBDCOD fraction was increased by 76.2%, and major constitute of produced organic were acetic acid and propionic acid. Also, nitrogen and phosphorus were greatly solubilized. However, because acid-hydrolyzable phosphorus(AHP) was major part of solubilized phosphorus, $NH_4{^+}-N$ and $PO_4{^3}-P$ concentration were insufficient for effective formation of crystal like as MAP(Magnesium Ammonium Phosphate) and hydroxyapatite. By placing BPR reactor before alkali-ozone treatment reactor, $PO_4{^3}-P$ concentration in pretreated sludge was increased by 1.8 times, and improved potential of phosphorus recovery by crystallization. In experiment of crystallization, hydroxyapatite formation was more easily applied than MAP. By hydroxyapatite formation, $SCOD/PO_4-P$ ratio was greatly increased from 32.7 at control to 141.9 at $Ca^{2+}/PO{_4}^{3-}-P$ mole ratio of 2.4. The results based on this study indicated that the proposed system configuration has potential to reduce the excess sludge production, to recover phosphorus in usable forms as well as utilize organics as a external carbon source in BNR process.

자연정화공법에 의한 인공습지에서 효과적인 축산폐수처리를 위한 최적 전처리방법 구명 (Optimum Pre-treatment Method in Constructed Wetlands by Natural Purification Method for Treating Livestock Wastewater)

  • 박종환;서동철;김아름;김성헌;이성태;정태욱;최정호;이상원;조주식;김현욱;허종수
    • 한국토양비료학회지
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    • 제44권3호
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    • pp.425-433
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    • 2011
  • 자연정화공법에 의한 축산폐수처리장에서 효과적으로 축산폐수를 처리하기 위해 인공습지 축산폐수처리 시스템에 전처리방법으로 수생식물여과조와 활성슬러지조를 적용하여 최적 전처리방법을 조사하였다. 또한, 최적 전처리방법을 실제 현장 축산폐수처리장에 연계하여 시공한 후 전처리방법의 효율성과 안전성을 검토하였다. 수생식물여과조와 인공습지를 연계한 소형 축산폐수처리장치에서 최종방류수 중 COD, SS, T-N 및 T-P의 처리효율은 각각 83, 89, 63 및 87%이었다. 활성슬러지조와 자연정화공법을 연계한 소형 축산폐수처리장치에서 최종방류수 중 COD, SS, T-N 및 T-P의 처리효율은 각각 96, 95, 86 및 92%이었다. 수생식물여과조 및 활성슬러지조는 인공습지 축산폐수처리장의 전처리공법으로서 질소와 인 처리효율을 향상시킬 수 있어 고농도의 축산폐수를 안정적으로 처리하기 위해 필요할 것으로 판단된다. 최적 전처리방법을 연계한 실제 현장 축산폐수처리장에서 COD, SS, T-N 및 T-P 의 처리효율은 모든 조건에서 각각 99.8, 99.9, 99.2 및 99.9%으로 높은 처리효율을 보였다.

하수처리시설의 Retrofitting을 위한 파일럿 규모 공기부상공정 연구 (A Pilot Study on Air Flotation Processes for Retrofitting of Conventional Wastewater Treatment Facilities)

  • 박찬혁;홍석원;이상협;최용수
    • 상하수도학회지
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    • 제22권3호
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    • pp.329-336
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    • 2008
  • The pilot study was conducted to evaluate the applicability of air flotation(AF) processes combined with biological nutrient removal(BNR) for the retrofitting of conventional wastewater treatment facilities. The BNR system was operated in pre-denitrification and intermittent aeration; developed ceramic membrane diffusers were installed to separate the solid-liquid of activated sludge at the bottom of a flotation tank. Before performing a pilot scale study, the size distribution of microbubbles generated by silica or alumina-based ceramic membrane diffusers was tested to identify the ability of solid-liquid separation. According to the experimental results, the separation and thickening efficiency of the alumina-based ceramic membrane diffuser was higher than the silica-based ceramic membrane diffuser. In a $100m^3/d$ pilot plant, thickened and return sludge concentration was measured to be higher than 15,000mg SS/L, therefore, the MLSS in the bioreactor was maintained at over 3,000mg SS/L. The effluent quality of the AF-BNR process was 4.2mg/L, 3.7mg/L, 10.6mg/L and 1.6mg/L for $BOD_5$, SS, T-N and T-P, respectively. Lastly, it was revealed that the unit treatment cost by flotation process is lower than about $1won/m^3$ compared to a gravity sedimentation process.

실리카 나노입자에 의한 활성슬러지 활성도 저해 효과 분석 (Inhibition effect of silica nanoparticle on the oxygen uptake rate of activated sludge)

  • 이수미;조진우
    • 상하수도학회지
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    • 제28권1호
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    • pp.47-54
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    • 2014
  • Nanotechnology has become one of the fastest developing technologies and recently applied to a variety of industries. Thus, increasing number of nano materials including various nanoparticles would be discharged into wastewater and consequently entering a biological wastewater treatment process. However, the impact of the nano particles on biological wastewater treatment has not been estimated intensively. In this research, we investigated the effect of silica nanoparticle on the oxygen uptake rates (OURs) of activated sludge used in a conventional wastewater treatment process. The inhibition (%) values were estimated from the results of OURs experiments for the silica nanoparticles with various sizes of 10-15, 45-50, and 70-100 nm and concentrations of 50, 250, and 500 ppm. As results, the inhibition value was increased as the size of silica nano particles decreased and the injected concentration increased. The maximum inhibition value was investigated as 37.4 % for the silica nanoparticles with the size of 45-50 nm and concentration of 50 ppm. Additionally, the effect of size and concentration on the inhibition should be considered cautiously in case that the aggregation of particles occurred seriously so that the size of individual particles was increased in aquatic solution.

순산소 활성오니공정을 이용한 제지폐수처리의 동력학적 해석 (Kinetic Analysis for Paper-mill Wastewater Treatment Using Pure Oxygen Activated Sludge Process)

  • 김성순;정태학
    • 상하수도학회지
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    • 제14권2호
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    • pp.157-163
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    • 2000
  • An experimental study was conducted to evaluate the treatment efficiency of paper-mill wastewater using pure oxygen activated sludge process. Effects of hydraulic retention time (HRT) and organic loading on process performance and kinetics were investigated. The raw paper-mill wastewater(BOD concentration ${\leq}500mg/L$) and the effluent from dissolved air flotation(DAF) treatment(BOD concentration ${\geq}500mg/L$) were used as influent for pure oxygen activated sludge process. Average BOD removal efficiencies were above 89.3% under 6hours or longer of HRT, while under 3hours of HRT they decreased to about 82%. With the effluent from DAF process, the half saturation constants($K_S$) and the maximum specific substrate removal rate($K_{max}$) were 85 mg/L and 2.25 L/day, respectively. However, with the raw paper-mill wastewater, both $K_S$ and $K_{max}$ increased to 156 mg/L and 3.84 L/day, respectively. The microbial yield coefficient(Y) and the decay coefficient($K_d$) were 0.46 gVSS/gBOD and 0.03 L/day, respectively, with effluent from DAF process. While, Y and $K_d$ were 0.24 gVSS/gBOD and 0.035 L/day, respectively, with the raw paper-mill wastewater.

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총인 수질기준강화를 위한 국내 하수종말처리장의 물리화학적처리 특성조사 및 경제성 분석 (Survey of Physicochemical Methods and Economic Analysis of Domestic Wastewater Treatment Plant for Advanced Treatment of Phosphorus Removal)

  • 박혜영;박상민;이기철;권오상;유순주;김신조
    • 대한환경공학회지
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    • 제33권3호
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    • pp.212-221
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    • 2011
  • 우리나라의 공공하수처리시설은 생물학적 인 제거공정을 운전하고 있으나, '12년부터 지역구분(I, II, III)에 따라 각각 0.2, 0.3 및 0.5 mg/L로 강화되는 방류수수질기준을 준수하기 위해서는 화학물질을 이용한 추가적인 인 처리시설을 적용할 필요성이 대두되었다. 강화된 총인의 수질기준을 만족하기 위해 적용된 물리화학적 처리기술 성능의 구체적인 운영자료 구축을 위하여, 화학적 응집제 사용 중인 인 처리시설 중 모범적으로 가동하고 있는 국내 시설의 운영 데이터를 분석하여 처리성능을 평가하였다. 또한, jar 테스트를 이용해 물리화학적 인 제거공정 적용 시 최적 응집제 주입율 도출, 인 제거 및 슬러지 발생특성을 관찰하고 약품비용과 슬러지 발생증가량을 산정하여 실처리장에 응집제 적용 시 예상되는 경제성 분석을 하였다. 활성슬러지를 이용한 jar 테스트 결과, 0.5와 0.2 mg/L 이하의 총인 농도를 달성하기 위해 필요한 최소한의 응집제(황산알루미늄, 폴리염화알루미늄)의 주입농도는 각각 25와 30 mg/L (as $Al_2O_3$)이며, 2차 처리수의 경우에는 동일한 총인 농도를 달성하기 위해 요구되는 응집제 주입농도가 활성슬러지에 비해 약 1/12~1/3 수준으로 감소하였다. jar 테스트 결과, 활성슬러지에 응집제를 주입할 경우에 고형물 농도가 약 10~11%가 증가할 것으로 예측되었다. 한편, 활성슬러지에 응집제를 주입하는 경우의 응집제(황산알루미늄) 구입비는 2차 처리수에 주입하는 경우에 비해 약 4~10배 정도가 증가할 것으로 산정되었다. 또한, 슬러지 발생량은 약 4~10배 정도 증가할 것으로 예측되었다.

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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광산배수의 적극적 처리시설에서 발생하는 슬러지 특성 평가 (Evaluation of Characteristics of Sludge generated from Active Treatment System of Mine Drainage)

  • 김정은;지원현
    • 자원환경지질
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    • 제56권4호
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    • pp.409-419
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    • 2023
  • 산성광산배수 처리방법은 적극적 처리방식과 소극적 처리방식이 일반적으로 사용되고 있으며, 이때 발생되는 부산물인 슬러지는 국내에서 약 5천 톤/년으로 발생하고 있다. 본 연구는 적극적 처리방식 중 물리·화학적 처리방식으로 정화 후 발생되는 슬러지의 특성을 조사하여 재활용 가능여부를 검토하기 위함이다. 5개소(D, H, S, T, Y) 수질정화시설의 슬러지의 특성을 물리·화학적 분석을 통해 검토하였다. 그 결과 pH는 pH 5.86 ~ pH 7.89로 측정되었고, 수분함량은 51 % ~ 82 %로 분석되었으며, 입자크기는 대부분 25 ㎛보다 작은 미립자로 구성되었음을 확인할 수 있었다. ICP-OES를 이용한 슬러지 내 무기물질 분석결과, Al, Fe, Mn의 농도범위는 각각 1,189 mg/kg ~ 129,344 mg/kg, 106,132 mg/kg ~ 338,011 mg/kg, 3,472 mg/kg ~ 11,743 mg/kg로 조사되어 고농도로 존재함을 확인 할 수 있었다. 그 외 무기물질 중 중금속류에 대해서는 T-슬러지는 As와 Zn, D-슬러지는 Cd, H-슬러지는 Ni, S-슬러지는 Zn, Y-슬러지는 Cd의 농도가 토양오염우려기준을 초과하였다. 또한 슬러지의 용출 특성을 알기위해 폐기물 용출시험(KSLT) 및 TCLP 시험을 진행하였다. 슬러지 재활용시 용출되어 지하수에 미치는 영향 확인을 위해 지하수 수질기준(생활용수) 20개 항목에 대하여 수행하였다. 용출시험결과 특정유해물질 16개 항목에서 모두 불검출로 확인되었으며, 일반항목 4개 항목에 대해서는 모두 생활용수 기준치 이내로 만족하였다. XRD, SEM-EDS의 분석결과, 슬러지는 주로 방해석, 석영의 패턴을 보였으며, 높은 Fe, O의구성비율로철수산화물이높은비중을차지하는것으로보였다. 이를 통해서 비매체접촉형 방식의 재활용의 가능성이 있을 것으로 판단된다.

에너지 생산형 하수처리장을 위한 가용 기술과 통합관리 방안 (Available Technology and Integrated Management Plan for Energy-positive in the Sewage Treatment Plant)

  • 송민수;김형호;배효관
    • 한국물환경학회지
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    • 제36권1호
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    • pp.55-68
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    • 2020
  • Because of the intensified environmental problems such as climate change and resource depletion, sewage treatment technology focused on energy management has recently attracted attention. The conversion of primary sludge from the primary sedimentation tank and excessive sludge from the secondary sedimentation tank into biogas is the key to energy-positive sewage treatment. In particular, the primary sedimentation tanks recover enriched biodegradable organic matter and anaerobic digestion process produces methane from the organic wastes for energy production. Such technologies for minimizing oxygen demand are leading the innovation regarding sewage treatment plants. However, sewage treatment facilities in Korea lack core technology and operational know-how. Actually, the energy potential of sewage is higher than sewage treatment energy consumption in the sewage treatment, but current processes are not adequately efficient in energy recovery. To improve this, it is possible to apply chemically enhanced primary treatment (CEPT), high-rate activated sludge (HRAS), and anaerobic membrane bioreactor (AnMBR) to the primary sedimentation tank. To maximize the methane production of sewage treatment plants, organic wastes such as food waste and livestock manure can be digested. Additionally, mechanical pretreatment, thermal hydrolysis, and chemical pretreatment would enhance the methane conversion of organic waste. Power generation systems based on internal combustion engines are susceptible to heat source losses, requiring breakthrough energy conversion systems such as fuel cells. To realize the energy positive sewage treatment plant, primary organic matter recovery from sewage, biogas pretreatment, and co-digestion should be optimized in the energy management system based on the knowledge-based operation.