• 제목/요약/키워드: wastewater sludge

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저농도 도시하수 처리를 위한 활성슬러지공정에서 HRT 및 SRT가 처리효율에 미치는 영향 (The Effect of HRT and SRT on Treatment Efficiency of Activated Sludge Process for Low Concentration Municipal Sewage)

  • 황규대;김민호;고새봄
    • 상하수도학회지
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    • 제11권1호
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    • pp.64-73
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    • 1997
  • Most of the municipal wastewater treatment plants operated in Korea are designed for high concentrations municipal sewage. However, activated sludge process employed by municipal wastewater treatment plant is operated at low organic loading. The objective of this study was to determine optimum operating condition of activated sludge process for treatment of low concentration municipal sewage. Three bench scale activated sludge reactors were operated to investigate the effect of HRT and SRT on the COD and TSS removal efficiency. The average concentration of TSS, SCOD, SBOD and TKN in influent were 118mg/l, 61mg/l, 21mg/l, and 12mg/l, respectively. The activated sludge reactors operated with various HRT and SRT showed about 89-93% TSS removal efficiency. HRT and SRT does not affect the TSS removal efficiency of actvatied sludge process significantly. However, HRT affected the SCOD removal efficiency slightly. As the HRT decreases from 13hours to 3hours, the SCOD removal efficiency decreases from 67% to 56%. The average effluent TCOD concentration of the reactor operated with 3hours of HRT was approximatly 40-45mg/l. Kinetic coefficient yield (Yt) and decay coefficients(Kd) were 0.594-0.954 mgMLVSS/mgCOD and $0.0197-0.0317day^{-1}$, respectively. Low concentration municipal sewage can be treated with 3 hours of HRT without effluent quality deterioration and SRT does not affect the substrate removal efficiency at this operation condition.

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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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호흡률 측정기를 이용한 제약폐수의 생물학적 활성 측정 (Measurement of Biological Activity in Pharmaceutic Wastewater by Using Respirometer)

  • 이영락;이기용;임지훈;이상훈;문흥만;심상준;이진원
    • KSBB Journal
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    • 제16권2호
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    • pp.183-187
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    • 2001
  • The biological activities of wastewater and sludge taken from the wastewater treatment process of Hyangnam pharmaceutic factories in Hwaseong, Kyeonggi-Do was measured using a respirometer. Oxygen uptake rate (OUR) was used as a tool for measuring biological activity. OUR was measured for varying amounts of sludge and organic chemicals in wastewater, and its toxicity was evaluated. Maximum OUR was observed as 61, 75, and 89 mg O$_2$/L/hr when sludge was added as 3, 5, and 10% of total volume, respectively. When the concentration of organic chemicals was changed to 1,486, 337, and 164 mg COD/L, maximum OUR was 53, 13, 8 mg O$_2$/L/hr, respectively. The toxicity test results showed that there seemed that there seemed to be no observable toxic effect on microbes in pharmaceutic wastewater.

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포기조의 낮은 용존산소로 인한 제지폐수의 슬러지 팽화특성 (Characteristics of Sludge Bulking Caused by Low Dissolved Oxygen in Aeration Tank for Paper Mill Wastewater Treatment)

  • 곽동희;유승준;박종천
    • 한국물환경학회지
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    • 제24권4호
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    • pp.458-464
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    • 2008
  • Bulking phenomena and scum formation are common problem in suspended growth system like the activated sludge plants for wastewater treatment. Apart from wastewater composition, operating conditions, such as mechanical stress by insufficient oxygen supply, are often decisive for the occurrence of a bulking or scumming problem. There were the comparative aeration tanks in terms of sludge bulking caused by the difference of mechanical aeration facilities in the wastewater treatment plant of N paper mill company. In this study the cause of bulking was investigated through not only the biological isolation and identification but also a series of operational data consideration. On the basis of the investigation results for bulking cause, the operational criteria on dissolved oxygen concentration was derived to decrease the bulking problem.

하수슬러지의 에너지 자원화를 위한 마이크로파 건조특성 분석 (Analysis of the Drying Characteristic of Wastewater Sludge by Microwave to Make Energy Resources)

  • 이성민;이윤식
    • 한국지반환경공학회 논문집
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    • 제10권7호
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    • pp.125-133
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    • 2009
  • 하수를 정화하는 과정에서 발생하는 슬러지는 과거 주로 매립되어 왔으나, 2003년 유기성 슬러지의 매립금지라는 폐기물 관리법이 개정됨에 따라 최근에는 주로 해양투기 되어왔다. 그러나 '런던협약 96의정서'에 의해 2011년부터 해양투기도 금지될 예정이어서, 세계 각국은 슬러지의 다양한 처리방법에 대해 노력하고 있다. 우리나라도 예외 없이, 하수슬러지의 합리적인 처리방법을 찾기 위해 현재 많은 전문가들이 노력하고 있으며, 그중 하나가 재생 에너지화이다. 슬러지의 재생 에너지화의 성패는 친환경적이고 경제적인 건조방법에 달려 있다 해도 과언이 아니다. 따라서 본 연구에서는 영동군에서 발생하고 있는 하수슬러지를 재생에너지화하기 위해, 슬러지의 화학적 특성을 분석하여 에너지화 가능성을 검토하고, 마이크로파를 물과 슬러지에 각각 조사하여 슬러지의 건조 특성과 효율성 등을 분석하였다. 그 결과, 영동군하수 슬러지는 중금속 성분이 매우 적고 열량이 3,370kcal/kg 이상으로 재생에너지화하기에 적당함을 확인하였다. 또한, 마이크로파에 의한 슬러지 건조 특성을 분석한 결과, 슬러지 중량 대비 시간의 곡선은 투입 슬러지 량에 관계없이 늘어진 S자 형태의 거동특성을 보임은 물론 그 기울기가 일정함을 확인하였다. 또한, S 곡선을 변곡점 기준으로 세 영역으로 나눌 경우 두 번째 영역에서 건조가 가장 많이 일정하게 발생하며, 전체 건조량의 약 80% 이상임도 확인하였다. 본 결과는 향후 마이크로파를 이용한 full-scale 건조공정에서 투입 슬러지 대비 슬러지 건조량을 예측하는데 적용할 수 있다. 또한 본 실험 결과에 의하면, 마이크로파에 의한 건조능력이 약1.0kg/kW 이상을 보이고 있어 경제성도 갖고 있음을 확인하였다.

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슬러지계면층 높이변화모델에서 슬러지 침전특성에 대한 영향 (The Effect of Sludge Settling Characteristics on Sludge-Water Interface Height Change Model)

  • 박석균;강선홍
    • 상하수도학회지
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    • 제20권1호
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    • pp.147-155
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    • 2006
  • For the further study of the solids flux theory, several researchers have proposed models to predict sludge settling velocity for each different concentration by using sludge indexes, SVI, SSVI and $SSVI_{3.5}$. It is difficult to apply the above models to predict sludge-water interface height in a batch column because sludge settling velocity changes while sludge settle down. While sludge settle down in a batch column, sludge concentration becomes high. The sludge concentration change is one of the most critical causes of the change of sludge settling velocity. Also, sludge concentration change causes of sludge index to change. SVI is more sensitive than SSVI or $SSVI_{3.5}$ to the change of sludge concentration. Each sludge has physical characteristics of its own which makes the settling velocity for each sludge different. The purpose of this study is to establish the correction factors that are able to compensate the errors derived from each different sludge settling characteristic by using sludge indexes, therefore the correction factors are applicable to the model for the change of sludge-water interface height.

볼-밀 가용화 효과의 향상을 위한 하수슬러지 조건에 대한 연구 (Sewage sludge conditions for promoting solubilization in the ball mill treatment)

  • 이명주;김태형;남양원;황선진
    • 상하수도학회지
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    • 제22권5호
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    • pp.505-510
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    • 2008
  • Excess sludge and raw sludge were treated by ball mill in order to promote solubilization, and it was known that the level of solubilization was higher in excess sludge rather than raw sludge. About solid concentration, with the increase of TS, the amounts of solubilization was increased. And excess sludge was solubilized more effectively with the increase of ball mill treatment time. Especially, in case of excess sludge, within 5 min of ball mill treatment, 6 times of solubilization was achieved compared with raw sludge. The effect of bead size was also tested and 1 mm bead was most desirable when applied to the TS 4% of excess sludge. Particle size decrease by the ball mill treatment was more effective in raw sludge, nevertheless the level of solubilization was always higher in excess sludge. This means that the results of particle analysis could not be understood as a indicator for sludge solubilization. Generally, excess sludge and raw sludge are mixed at the thicker in the STP, but considering a ball mill pretreatment as an alternative for sludge solubilization, it is desirable to treat not raw sludge but excess sludge alone in the aspect of solubilization yield and economical process.

미세 기포에 의한 활성슬러지의 부상특성 (Flotation Characteristics of Activated Sludge by Micro-bubbles)

  • 김성진;강병준;박상욱;이재욱;정흥조;곽동희
    • 상하수도학회지
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    • 제20권4호
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    • pp.501-507
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    • 2006
  • Dissolved air flotation (DAF) has been well known for the gravity separation process. The solids to be separated are transferred from the water body to the water surface using micro-air bubbles. DAF has also been used for enhancing solids-liquid separation of industrial and municipal wastewater by adding a its unit parallel to a sedimentation unit to reduce the hydraulic loading in the sedimentation clarifier. This study was to investigate flotation characteristics of activated sludge by the recent DAF technique without chemical agents. In addition, the effect on temperature in flotation of activated sludge and the thickening degree of activated sludge were studied.

Enzymatic Activities in Petroleum Wastewater Purification System by an Activated Sludge Process

  • Li Yin;Chrost Ryszard J.
    • Journal of Microbiology and Biotechnology
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    • 제16권2호
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    • pp.200-204
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    • 2006
  • The enzymology of an activated sludge system for a petroleum wastewater purification process was investigated. Leucine-aminopeptidase (L-AMP), ${\beta}$-glucosidase (${\beta}-GLC$), and lipase (LIP) were selected for the study. It was found that more than 81.7% of enzymatic activity was associated with microbial cells in the activated sludge floc. The metabolic response of a mixed microbial population to increased phenol concentration showed that L-AMP activity increased in the activated sludge, whereas activities of ${\beta}-GLC$ and LIP decreased, due to the inhibitory effect of the phenol which varied from 100 mg/l to 500 mg/l.

무기슬러지 분리와 슬러지 가용화를 적용한 고효율 호기성 소화기술(CaviTec II)에 의한 슬러지 감량 및 반수류 부하 저감 (Reduction of sludge production and recycled nutrients loading by high-rate aerobic digestion(CaviTec II) with inorganic sludge separation and sludge solubilization)

  • 이동우;배강형;조건상;김성홍
    • 상하수도학회지
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    • 제28권4호
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    • pp.411-417
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    • 2014
  • The performance of the new aerobic digestion system combined with inorganic sludge separation unit and sludge solubilization unit, CaviTec II, is evaluated. Anaerobic digester effluent sludge is used for feed sludge of CaviTec II system. By addition of CaviTec II, the amount of cake generated is reduced by 27%, and the soluble nitrogen is reduced by 92%.