• 제목/요약/키워드: wastewater flow

검색결과 671건 처리시간 0.029초

피압 단순 관로 체제에서의 인버스 임피던스를 이용한 수압기반 유속추정기술 (A pressure based flow velocity estimation technique using inverse impedance for simple pressurized pipeline systems)

  • 이정섭;고동원;최두용;김상현
    • 상하수도학회지
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    • 제36권4호
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    • pp.219-228
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    • 2022
  • In this study, we propose a flow velocity evaluation scheme based on pressure measurement in pressurized pipeline systems. Conservation of mass and momentum equations can be decomposed into mean and perturbation of pressure head and flowrate, which provide the pressure head and flowrate relationship between upstream and donwstream point in pressurized pipeline system. The inverse impedance formulations were derived to address measured pressure at downstream to evaluation of flow velocity or pressure at any point of system. The convolution of response function to pressure head in downstream valve provides the flow velocity response in any point of the simple pipeline system. Simulation comparison between traditional method of characteristics and the proposed method provide good agreements between two distinct approaches.

Si 입자를 함유한 반도체 세정폐수의 한외여과 특성 [II] -Polyolefin 관형막에 의한 투과분리- (Permeation Behavior of Semiconductor Rinsing Wastewater Containing Si Particles in Ultrafiltration System -II. Permeation Characteristics of Tubular Membrane)

  • 남석태;여호택;전재홍;이석기;최호상
    • 멤브레인
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    • 제9권1호
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    • pp.36-42
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    • 1999
  • 본 연구에서는 Si 미립자를 함유한 반도체 세정폐수의 관형막을 이용한 한외여과특성을 검토하였다. 관형막의 시간변화에 따른 투과유속의 감소현상은 막표면에 형성된 케익층의 증가 및 기공막힘에 기인하며, cross flow는 케익여과에 의한 막오염 형태를 보였으나 dead-end flow는 기공막힘과 케익여과에 의한 혼합형태를 보였다. Cross Flow의 케익저항의 크기는 3.16$\times$$10^{12}$ ~4.34$\times$$10^{12}$ $m^{-1}$ 였고, dead-end flow 는 6.6 $\times$$10^{12}$ ~12.19$\times$$10^{12}$ $m^{-1}$였다. 운전초기의 흐름형태에 따른 투과유속은 cross flow 가 dead-end flow 의 약 7 배였다. Cross flow 투과유속은 약 42 $\ell$/$m^2$ hr, 용질배제율은 약 96 % 였으며, 분리막공정을 거친 투과수 중의 Si 입자의 평균크기는 20nm였다.

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Estimation of BOD in wastewater treatment plant by using different ANN algorithms

  • BAKI, Osman Tugrul;ARAS, Egemen
    • Membrane and Water Treatment
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    • 제9권6호
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    • pp.455-462
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    • 2018
  • The measurement and monitoring of the biochemical oxygen demand (BOD) play an important role in the planning and operation of wastewater treatment plants. The most basic method for determining biochemical oxygen demand is direct measurement. However, this method is both expensive and takes a long time. A five-day period is required to determine the biochemical oxygen demand. This study has been carried out in a wastewater treatment plant in Turkey (Hurma WWTP) in order to estimate the biochemical oxygen demand a shorter time and with a lower cost. Estimation was performed using artificial neural network (ANN) method. There are three different methods in the training of artificial neural networks, respectively, multi-layered (ML-ANN), teaching learning based algorithm (TLBO-ANN) and artificial bee colony algorithm (ABC-ANN). The input flow (Q), wastewater temperature (t), pH, chemical oxygen demand (COD), suspended sediment (SS), total phosphorus (tP), total nitrogen (tN), and electrical conductivity of wastewater (EC) are used as the input parameters to estimate the BOD. The root mean squared error (RMSE) and the mean absolute error (MAE) values were used in evaluating performance criteria for each model. As a result of the general evaluation, the ML-ANN method provided the best estimation results both training and test series with 0.8924 and 0.8442 determination coefficient, respectively.

새로운 피혁폐수 처리제에 관한 연구; I. 새로운 유기 응결제의 개발 (A study on new treatment chemical for leather wastewater; I. Development of new organic coagulant)

  • 정맹준;이철재;한성욱
    • 한국산업융합학회 논문집
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    • 제9권4호
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    • pp.323-330
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    • 2006
  • As the interest in environmental pollution resulting from recent industrial development is converging, wastewater treatment problem of dying processing is one of important pending issue. Usually, flow mediation earth and settling pond etc. of processing plant to handle water or wastewater. Mediation is the wastewater that flowed past settling pond than material of heavy particles, water weight colloid particles that big solids are removed but are suspensibility material settlement exclusion impossible. So, we need flocculation and coagulation action to remove materials from this colloid state. For flocculation and coagulation action chemical agents to add back, addition of chemical agents forms floc of could settle size. That is, shorten the sedimentation time and quality of processing water because promoting sedimentation doing to do fines or suspended solids and colloid can materials large size and also, flocculation to annex efficiency of filtration augment. Therefore, I executed this research to prove that improving organic matter and chromaticity of treated water of processing epochally using organic coagulant informed positive ion co-polymerization superior in color wastewater through this research.

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Evaluation of monthly environmental loads from municipal wastewater treatment plants operation using life cycle assessment

  • Piao, Wenhua;Kim, Ye-jin
    • Environmental Engineering Research
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    • 제21권3호
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    • pp.284-290
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    • 2016
  • Life cycle assessment (LCA) methodology can be used to assess impacts on the environment that might be generated during treatment of wastewater and sludge treatment. In this work, LCA methodology was suggested to evaluate monthly environmental impact of wastewater treatment plants (WWTPs). Two field scale WWTPs, A2/O process and conventional activated sludge process (CAS), were selected as target plants and the operational data were collected from those plants. As the function units, the unit volume of treated wastewater of $1m^3$ and 1 kg T-N eq. removed were selected. The environmental effect of target WWTPs operation were assessed as impact categories such as global warming potential, eutrophication potential, and so on. From monthly profiles of each index, it was shown that the environmental impact of WWTPs has seasonal patterns influenced by the influent flow rate variation causing higher impacts in winter than summer. This is due to the fact that there were no significant increase in the electricity consumption and chemical usage during the summer while the treated volume of wastewater was increased.

Candida utilis를 이용한 furfural 함유 식품가공 폐수의 처리 (Treatment of Food Processing Wastewater bearing Furfural by Candida utilis)

  • 박기영;정진영
    • KSBB Journal
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    • 제18권4호
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    • pp.272-276
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    • 2003
  • 혐기성 미생물에 저해가 되는 물질을 포함하는 고농도 폐수의 효모에 의한 처리에 관하여 연구하였다. 폐수는 furfural 부산물이 배출되는 식품가공 공정의 배출폐수를 대상으로 실험하였다. 본 연구에서는 호기성 효모의 일종인 Candida utilis가 실험에 적용되었다. 회분 실험을 통하여 본 폐수는 혐기성 미생물에 저해 영향을 주는 것으로 밝혀졌다. 본 공정의 최적 온도는 25에서 45$^{\circ}C$이었으며 효모의 성장에 적당한 pH는 4에서 8사이임을 알 수 있었다. 연속실험 결과, 체류시간 1일 이상에서 COD가 90% 이상 제거되었다. 그러나 유출수 중의 유기물 농도는 여전히 다소 높은 것으로 조사되었다. 따라서 동력학적으로 해석하여 추정한 결과 남은 유기물은 대부분은 용존 미생물 생성물 (SMP, Soluble Microbial Product)에서 기인하는 것으로 판단되었다.

하수처리를 위한 간헐 방류식 장기폭기 공정에서 아질산염의 축적에 영향을 미치는 인자 (Factors affecting nitrite build-up in an intermittently decanted extended aeration process for wastewater treatment)

  • 안규홍;박기영;이형집
    • 상하수도학회지
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    • 제13권1호
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    • pp.51-60
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    • 1999
  • An intermittently-aerated, intermittently-decanted single-reactor process (KIDEA process : KIST intermittently decanted extended aeration process) was applied for nitrogen removal from wastewater. Synthetic wastewater with chemical oxygen demand (COD): nitrogen (N) ratio of approximately 5.25: 1 was used. The average COD removal efficiency reached above 95%, and under optimal conditions nitrogen removal efficiency also reached above 90%. This process consisted of 72 minute aeration, 48 minute settling and 24 minute effluent decanting with continuous feeding of influent wastewater from the bottom of the reactor, and did not require a separate anoxic mixing-phase. In this process, nitritation ($1^{st}$ step of nitrification) was induced but nitratation($2^{nd}$ step of nitrification) was suppressed. Main factors responsible for the accumulation of nitrite ion in the experimental condition were free ammonium and dissolved oxygen. This condition of nitrite build-up accelerated by continuous feed flow in the bottom of the KIDEA reactor because of high concentration of ammonia nitrogen in the influent. This research provides one of answers to control nitrate build-up.

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영가철 충진 복극전해조를 이용한 질산성질소 및 대장균의 연속식 제거 (Continuous Removal of Nitrate and Coliform using Bipolar ZVI Packed Bed Electrolytic Cell)

  • 정주영;박정호;최원호;박주양
    • 상하수도학회지
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    • 제25권5호
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    • pp.651-658
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    • 2011
  • Nitrate is a common contaminant in industrial wastewater and ground water. The maximum contaminant level set by EPA for nitrate of 10 mg/L as N. In this study, nitrate was removed using bipolar ZVI packed bed electrolytic cell that maximized the contact area between each electrode and contaminants under 600 V. Also this study investigates the simultaneously deals with removal of ammonia by operating air stripping tower. In addition to the air stripping also helped to precipitate iron ions to the form of iron oxides. Bipolar ZVI packed bed electrolytic cell was also effective in removing coliform by electrical power. In the continuous experiments for the simulated wastewater (initial nitrate for 25 mg/L as N), maximum 96.3% removal of nitrate was achieved in the applied 600 V at the flow rate of 6 mL/min.

하구환경의 생태적 설계 (Ecological Design of Estuarine Environment)

  • 양홍모
    • 한국조경학회지
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    • 제23권2호
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    • pp.167-181
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    • 1995
  • An Ecocomplex is proposed for ecological design of the estuarine environment of Han River, which is designed upon an alternative mamagement concept of estuarine environment. The concept reveals interrelationships among estuary, delta region and urban inland with inputs/outputs and feedbacks among them. The Ecocomplex emphasizes an integration of wastewater treatment with aquaculture, agriculture and recreation, and carries out ecological treatment, recycling, and harvest processes. A module of wastewater treatment pond system is employed in the Ecocomplex, which treats a flow of 3,786 ㎥/day and is composed of a four-facultative-pond series. Treatment ponds stabilize wastewater discharged from the urban area, and concurrently produce algae for commercial or recreational fish farming. Effluent from treatment and fish ponds is reused for agricultural production. Through the waste-algae-fish-vegetable-recreation processes, wastewater from the urban settlement is recycled back to the urban ecosystem. This resource-conserving design approach can maintain a sustainable urban ecosystem, managing an estuarine environment more naturally, healthly, and economically.

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