• Title/Summary/Keyword: 고도하수처리

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The Study of Modified Sequencing Batch Reactor Process for Small Advanced Wastewater Treatment (소규모 고도하수처리를 위한 변형 연속회분식공정에 관한 연구)

  • Han, Woonwoo;Kim, Kyuhyoung
    • Journal of the Korean GEO-environmental Society
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    • v.9 no.3
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    • pp.35-43
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    • 2008
  • This study was carried out to estimate the performance of modified sequencing batch reactor (SBR) process by the application of SBR process for small advanced wastewater treatment plant. Organic, nitrogen and phosphorus were able to remove in the unit reactor by SBR process and it would be able to select the suitable operation method. The plant was operated to achieve high performance with influent control, optimum anoxic/oxic condition using intermediate aeration method, and solid (sludge) /liquid (effluent) separation by modified decanter. The optimum operating mode was 3Cycles a day and intermediate input and aeration. Under these conditions, the treatment efficiencies were good with 60% of designed flow rate and low influent quality. When the influent concentrations of BOD and CODMn were 120.4 mg/L and 95.7 mg/L, respectively. The effluent concentrations of BOD and CODMn were 6.8 mg/L and 11.0 mg/L, respectively. The average removal efficiencies of BOD and CODMn were 94.4% and 88.5%, respectively. The removal efficiencies of T-N and T-P were 69.6% and 73.6%, respectively when the average T-N and T-P concentrations were 32.2mg/L and 4.65mg/L, respectively. The T-N and T-P removal efficiencies were slightly decreased to 58.8% and 68.5%, respectively in the winter season but its were also stable efficiencies. BOD, T-N and T-P were removed by 90%. 67% and 46% respectively in the first anoxic/oxic condition, in addition to T-P was removed by 70% in the second anoxic/oxic condition. From the results, modified sequencing batch reactor (SBR) process is suitable for small advanced wastewater treatment.

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하수처리 프로세서 제어를 위한 감시제어 시스템

  • 김현기;오성권;황희수;우광방
    • 전기의세계
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    • v.39 no.6
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    • pp.67-75
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    • 1990
  • 하수처리 프로세스의 과제로는 우수침수, 수질보존, 자원의 유효이용이 그 주요내용이다. 이에 대응하기 위해 기상, 우량, 하천정보 시스템의 구성, 지식공학응용 우수펌프 운전제어, 하수의 고도처리기술 등의 방법이 행해지고 있다. 하수도는 생활환경의 개선, 침수의 방지, 공공 용수 지역의 수질보존의 측면뿐만 아니라 최근에는 하수도를 자원으로써 이용하는 관점으로부터 시서르이 공간이용, 처리수 및 슬러지의 다목적 활용도 중요한 과제로 되고 있다. 하수도 plant의 전기, 계장 기술을 구성하는 요소 기술은 전기(E), 계장(I), computer(C) 관계하는 기술을 종계로써 하고, 시스템설계로부터 시공까지의 engineering기술을 횡계로 한 통합 시스템 기술이다. 하수도 분야에 있어서의 감시제어 시스템은 종래의 계층화된 수직분산 방식에 덧붙여 계층마다 기능을 나누어 수평분산방식이 진행되고 있고, 최근에는 수직분산, 수평분산의 감시제어 시스템으로 이행하고 있다.

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Determination of Optimal Livestock Wastewater Treatment Process for Linked Treatment in Sewage Treatment Plant (하수처리장 연계처리를 위한 가축분뇨 최적 처리공정 선정에 관한 연구)

  • Kim, Choong Gon;Shin, Hyun Gon
    • Journal of the Korea Organic Resources Recycling Association
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    • v.20 no.3
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    • pp.52-59
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    • 2012
  • As the result of reviewing the linked treatment of water quality for treating process at public livestock wastewater treatment facilities for fair selection of the proper linked process in case of linking sewage treatment plant for livestock wastewater, in case of wastewater processed by bio-reactor that is only biologically-treated, the load factor showed relatively high as 1.67%(base on design quality), 2.59%(base on operation quality) regarding COD and 3.69%(base on design quality), 7.67%(base on operation quality) regarding $COD_{Mn}$ but it is judged that there is nearly no influence on the operation of sewage treatment plan. And, in case of oxidized flotation-treated water & biofiltlation-treated water that are the advanced wastewater treatment, the load factor is approximately 1% and there is concern about the installation of excessive facilities in case of installing the advanced wastewater treatment. So, in case of considering the economic efficiency & stable operation of sewage treatment plant S, it is judged to be desirable to link with wastewater processed by bio-reactor that is biologically-treated.

Modeling the effect of securing environmental flow using wastewater discharge on water qualifies of the three urban rivers in Taejeon (하수처리수를 이용한 하천유지유량 확보에 따른 대전 3대 하천에서의 수질모의)

  • Kim, Jeong-Kon;Yur, Joong-Hyun;Kim, Woo-Gu
    • Proceedings of the Korea Water Resources Association Conference
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    • 2005.05b
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    • pp.1373-1377
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    • 2005
  • 수질개선을 위한 많은 노력의 결과 대전광역시를 관통하는 대전 3태 하천인 갑천, 유등천, 대전천의 수질은 1990년 초반을 기점으로 많은 개선효과를 보이고 있다. 그러나 도시화에 따른 불투성층의 증가와 저류능력 감소, 치수를 목적으로 한 하도정비 등에 의하여 기저유출량은 과거에 비해 현저히 감소하였으며, 이로 인하여 갈수기에는 유량이 적어 생태적이고 친수적인 다양한 하천기능 수행에 많은 어려움을 초래하고 있다. 그러므로 대전광역시에서는 도심생태하천조성을 위한 방안으로 바람직한 하천기능을 회복하기 위하여 $70,000m^3/day$의 갑천수와 하수처리장에서 고도처리 된 $60,000m^3/day$의 방류수 중 $80,000m^3/day$를 각각 대전천과 유등천 상류지역에 공급하여 하천유지용수로서 사용하는 계획을 수립하였다. 하류지역에서의 갑천수와 고도처리 된 하수처리수를 대전천과 유등천의 상류지역에 하천유지용수로 공급함으로서 대전천과 유등천은 갈수기에도 각각 약 $1m^/sec,\;1.3m^3/sec$ 이상의 유량을 유지할 수 있을 것으로 예상된다. 갑천수와 고도처리수를 유지용수로 사용할 경우에 대한 수질변화를 QUAL2E를 이용하여 모의를 실시하였다. 유등천 합류부에서의 갑천수를 대전천 상류지역에 공급할 경우. 대전천에서의 수질은 $II\~III$등급을 유지할 것으로 보인다. 대전시의 지하철공사에서 발생하는 약 $9,600m^3/day$가량의 용출수와 대청호소수의 상수원수를 이용한 $10,000m^3/day$의 희석수를 유지용수로서 추가적으로 사용할 경우, 대전천의 BOD는 약 0.3mg/L가량의 개선효과가 있을 것으로 예상된다. 2011년 고도처리시설 완공시 방류수의 예상 수질은 BOD 10mg/L, TN 15mg/L, TP 2.0mg/L이하로 이를 유등천 상류부에 공급할 경우 유등천의 수질은 BOD 6.7mg/L, TN 9.80mg/L, TP 0.90mg/L를 나타낼 것으로 예측된다. 고도처리시설의 도입 후 금강 합류점에서 갑천의 예측 BOD는 7.4mg/L로 현재 9.0mg/L에 비하여 개선되지만 이는 금강수계 오염총량 관리계획의 시$\cdot$도 경계지점 목표수질인 5.9mg/L를 만족시키지 못하므로, 이를 만족시키기 위해서는 방류수 BOD 7.2mg/L이하로 처리해야 할 것으로 판단된다.

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Development of Natural and Ecological Wastewater Treatment System for Decentralized Regions and Rural Communities (분산지역 및 농촌마을 하수처리를 위한 자연정화 고도처리 공법 개발)

  • Kim, Song-Bae;Kwon, Tae-Young;Han, Jung-Yoon;Yoon, Chun-Gyeong
    • Korean Journal of Ecology and Environment
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    • v.39 no.4 s.118
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    • pp.489-497
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    • 2006
  • The feasibility of the Natural and Ecological Wastewater treatment System (NEWS) was examined for rural wastewater treatment in Korea. The intermittent trickling biofilter with high hydrophilic filter media was used for pretreatment for suspended solids and organic pollutants. The subsequent constructed wetland with porous granule materials was used for promoting nutrient removal. The results show that the removal efficiencies of the system were high with respect to the water quality parameters except COD. Even if the effluent from the biofilter did not meet the guidelines for wastewater treatment plant effluent in Korea in terms of $BOD_5$ and TN, the final effluent of the system meets the guidelines us to good performance of the constructed wetland. The regression analysis between pollutant loading rate and removal rate indicated that the system could have stable removal for SS, $BOD_5$, TN, and TP in the given influent ranges. The analysis in the winter period indicated that the wetland covered with transparent polycarbonate glass had the statble performance during the winter period dus to increase of temperature inside the wetland without any heating system. With the stable performance, effective poilutant removal, low maintenance, and cost-effectiveness, the NEWS could be considered as an alternative treatment system for decentralized regions and rural communities in Korea.

The Study of Advanced Treatment of Sewage Wastewater by the Electro Coagulation and Oxidation System (전기응집산화를 이용한 하수처리장의 고도처리방안 연구)

  • Lim, Jin-Hwan
    • Journal of the Korean Society for Environmental Technology
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    • v.19 no.6
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    • pp.556-562
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    • 2018
  • Due to the enforcement of effluent water regulation the advance sewage treatment system is needed to retrofit and remodelling. In this case the most important issue is the effluent concentrations of TP and there are a lot of system to reduce its concentration. But biological treatment processes have many restrictions to enhance the removal efficiency of TP. In this study the efficient ECO operating condition to improve and retrofit biological sewage wastewater treatment system is as follow; 1) The treatment efficiency of BOD, TN and TP at the current density of $15mA/cm^2$ was higher than the treatment efficiency at $5mA/cm^2$ in the electrodes arranged with Al-SUS(Stainless Steel) regardless of the reaction time, The TP concentration was 0.1 mg/L or less. Especially, when the reaction time was maintained at 10 min, the TP concentration was 0.06 mg/L or less irrespective of the current density. 2) The change of TP concentration is not influenced by the change of current density and rather the concentration of treated water changes according to the reaction time. In the case of electro coagulation reaction, a few seconds to several minutes are required. However, the reaction time of electro coagulation and oxidation was studied to be more than 10 minutes. 3) As a result, it has been studied that the economical current density of the electro coagulation oxidation process for TN and TP treatment of domestic wastewater is $15mA/cm^2$ or less and the reaction time is 10 minutes.