• 제목/요약/키워드: sewage disposal rate

검색결과 32건 처리시간 0.027초

수초·골재 하수처리장의 투수속도 (The Infiltration Velocity of a Sewage Disposal System with Water Plant and Gravel Bed)

  • 정동양
    • 한국환경복원기술학회지
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    • 제6권3호
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    • pp.29-34
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    • 2003
  • This paper describes the effects of sewage amount, temperature, and years in operation on the infiltration rate of a sewage disposal system. The self-purifying sewage disposal system, which is typically used in rural areas, consists of reeds and fine gravel. Water plants are planted on the gravel bed which provides the habitat for microbes. The basic process is that the gravel bed filters incoming sewage. Thus this system requires the smooth flow of sewage through the gravel. However, the efficiency of the disposal system will be lowered if the gravel bed is clogged with sewage sludge. A three year study shows that infiltration rate slows down significantly until the 7th day, depending on the sewage amount and the temperature. After the 7th day, the infiltration rate remains almost constant. In addition, the infiltration rate decreases as the temperature falls. It also decreases as the number of years in operation increase. But there is no significant change in the infiltration rate after the 7th day, independent of the temperature, the sewage amount, and years in operation. In order to take advantage of high infiltration rate, which improves the efficiency of the disposal system in its early stages, having two gravel beds and using them alternatively will be efficient. This operation method is called intermittent load and makes the disposal system last longer. The water plant roots above the gravel bed make the effective filtration possible because they delay accumulation of the sewage sludge and stabilize the filtration ability.

하수슬러지 처리기술 동향 및 최적화 처리방안 (Treatment, Disposal and Beneficial Use Option for Sewage Sludge)

  • 최용수
    • 수도
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    • 제24권5호통권86호
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    • pp.29-44
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    • 1997
  • Sewage sludge produced in Korea was 1,275,800 tons (dewatered sludge cake) per year in 1996, which is 3,495 tons per day, 0.303% of 11,526,100 tons per day of sewage treated in 79 sewage treatment plants. Sludge production has been and will be increasing in accordance with construction of new facilities for sewage treatment. Most of the sludge is currently disposed by landfill and ocean dumping, but it is becoming difficult to find suitable sites for landfill, particularly in big cities such as Seoul. In addition, rapid increase of landfill cost is anticipated in a near future. Current trend for sludge disposal in advanced countries is land application. Over the past 10 to 20 years in the United States, sludge management practices have changed significantly, moving from disposal to beneficial use. They use biosolid for utilization instead of sludge for disposal. Under the Clean Water Act of 1972, amended in 1987 by Congress, the U.S. EPA was required to develop regulations for the use and disposal of sewage sludge. The EPA assessed the potential for pollutants in sewage sludge to affect public health and the environment through a number of different routes of exposure. The Agency also assessed the potential risk to human health through contamination of drinking water sources or surface water when sludge is disposed on land. The Final Rules were signed by the EPA Administrator and were published (Federal Register, 1993). These rules state that sewage sludge shall not be applied to land if the concentration of any pollutant in the sludge exceeds the ceiling concentration. In addition, the cumulative loading rate for each pollutant shall not exceed the cumulative pollutant loading rate nor should the concentration of each pollutant in the sludge exceed the monthly average concentration for the pollutant. The annual pollutant loading rate generally applies to applications of sewage sludge on agricultural lands. The most popular beneficial use of sewage sludge is land application. The sludge has to be stabilized for appling to land. One of the stabilization process for sewage sludge is lime stabilization process. The stabilization process is consisted of the stabilizing process and the drying process. Stabilization reactor can be a drum type reactor in which a crossed mixer is equipped. The additive agents are a very reactive mixture of calcium oxide and others. The stabilized sludge is dried in sun drier or rotary kiln.

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ONE구동 열풍건조시스템을 이용한 하수슬러지 감량화를 위한 열적거동 연구 (A Study on the thermal Kinetics for Disposal of Sewage Sludge Using Thermal Wind Drying of One mechanical Power)

  • 배해룡;하상안
    • 유기물자원화
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    • 제13권2호
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    • pp.74-84
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    • 2005
  • 본 연구의 목적은 열풍건조를 이용하여 슬러지를 감량화하는 과정에서 발생되는 열적거동을 조사하는데 있다. 실험에서 중요한 운전매개변수는 공급되는 건조온도가 $130{\sim}170^{\circ}C$와 증발속도 WD를 변화시켜 실행하였다. 슬러지내 수분을 증발하는 과정에서 열적거동의 변화에 미치는 영향인 주요매개 변수는 공급되는 온도변화에 따른 건조시간, 슬러지내 수분함량, 슬러지의 고형물량에 따른 결과를 조사하였다. WD=0.95m/s의 조건에서 $170^{\circ}C$의 건조온도에서 수분이 증발되는 포화점은 95분과 $130^{\circ}C$에서 120분에서 조사되었다. 열풍의 의한 증발속도가 1.0 m/s로 일정할 때 건조온도가 130와 $150^{\circ}C$일 때 보다 $170^{\circ}C$인 경우가 증발율이 더 높게 나타났고, 건조기 온도가 $130^{\circ}C$인 경우는 WD=1.0 m/s일 때 WD=0.5 m/s 보다 증발율이 높게 나타남을 볼 수 있었다.

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인공습지 오수처리시설의 처리성능에 관한 연구 (Study on the Performance of Constructed Wetland System for Sewage Treatment)

  • 윤춘경
    • 한국농공학회지
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    • 제42권4호
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    • pp.96-105
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    • 2000
  • Field experiment was performed from August 1996 to December 1999 to examine the performance of constructed wetland system for wastewater treatment in rural area. The constructed wetland system was installed in Konkuk University and the effluent from septic tank of school building was used as an influent to the treatment basin. The treatment basin was composed of sand bed with planted reed. From August 1996 to June 1998 the hydraulic loading rate was fixed with about 15.63cm/day and theoretical detention time was 1.38 days, and from July 1998 to December 1999 the hydraulic loading rate was about 6.25cm/day and theoretical detention time was 3.5days. It worked continuously even during winter time, and the sewage flowed without freezing even when average daily air temperature was below -1$0^{\circ}C$. Average removal rate of BOD , COD, and SS was about 70%, T-P removal rate was about 50.8% , and T-N removal rate was 23.9%. The reason for poor T-N removal might be due to high influent concentration and short retention times. At the later years BOD and COD removal rates were increased , and SS and T-P removal rates did not change significantly , but T-N removal rates were decreased. The effluent of the wetland system often effluent water quality standards for sewage treatment plant, therefore, further treatment would be required if the effluent need to be discharged to the public water. Wetland system involves relatively large land area and could be suitable for rural area. Therefore, utilization of reclaimed sewage for agricultural purpose or subsequent land treatment is recommended as a ultimate disposal of sewage for agricultural purpose or subsequent land treatment is recommended as a ultimate disposal of sewage in rural area.

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유동층 생물반응기의 구조변화에 따른 하수처리 (Sewage Disposal by Different Structure of Fluidized Bed Biofilm Reactor)

  • 박종만;이재용;김철경;고창웅;김남기
    • 상하수도학회지
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    • 제18권2호
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    • pp.181-187
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    • 2004
  • The purpose of this study is to investigate the biofilm reactors capable of doing high efficiency treatment. Vertical fluidized bed biofilm reactor(VFBBR) and spiral fluidized bed biofilm reactor(SFBBR) was used for their performence in biodegradation of artificial sewage. The factors influencing the efficiency of those reactors were compared with difference of physical condition. They had same size but different structure to gain access of its unique characteristics. When recycle solution with flow rate of 22 mL/min and artificial sewage with flow rate of 2~10 mL/min were fed into two reactors in aerobic state, the average $COD_{cr}$, removal rate for biodegradation of SFBBR was greater than VFBBR. After reactor feed sewage was constantly maintained as flow rate of 4 mL/min and the recycle solution were changed to 10~32 mL/min respectively, the average $COD_{cr}$ removal rate of artificial sewage in SFBBR was greater than VFBBR. In this experiment for addition of support media into two reactors SFBBR was 4.1% excellent than VFBBR. Above all, SFBBR excelled VFBBR in boidegradation of organic matter in sewage.

이중주파수 초음파를 이용한 도시하수슬러지의 전처리 특성 및 비메탄활성도에 관한 연구 (Pretreatment Characteristics and Specific Methanogenic Activity of Municipal Sewage Sludge by Dual Frequency Sonication)

  • 정병길;장성호;성낙창
    • 한국환경과학회지
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    • 제16권2호
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    • pp.211-218
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    • 2007
  • The objectives of this study have been carried out to investigate the solubilization of municipal sewage sludge by single and dual frequency ultrasonic pretreatment, and the methane production characteristics of pretreated sewage sludge by specific methanogenic activity test for sewage sludge reduction. The waste activated sludge was collected from thickened tank of Suyoung sewage treatment plant in Busan city, and its concentration was adjusted to 1.0% total solids. Ultrasonic frequency was varied 15, 20, 15+20 kHz, and acoustic density was used a maximum 176W/L. The dual frequency ultrasonic pretreatment was found to be more effective than single frequency ultrasonic in the solubilization rate and methane production. The $SCOD_{Cr}/TCOD_{Cr}$, rate were 15.2%, 13.9%, 17.0% with single frequency of 15 kH2, 20 kHz, dual frequency of 15+20 kHz, respectively. The application of dual frequency ultrasound for sewage sludge pretreatment can be interest for sewage treatment plants having problems in sludge treatment and disposal.

건조 하수 슬러지의 열분해 및 고정층 연소 특성 연구 (Pyrolysis and combustion characteristics of dried sewage sludge in a fixed bed reactor)

  • 김민수;이용운;박진제;류창국
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2014년도 제49회 KOSCO SYMPOSIUM 초록집
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    • pp.29-32
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    • 2014
  • The practical route for disposal of sewage sludge becomes energy recovery by combustion after its ocean dumping is banned in 2012 in Korea. Due to the high moisture content, however, sewage sludge is required to be dried before transport and combustion. In this study, pyrolysis and combustion characteristics of dried sewage sludge was investigated in a small-scale fixed bed reactor in order to provide fundamental data for energy recovery of the fuel. As the first step of combustion, the primary products of pyrolysis were analyzed in a fixed bed reactor for the condensable volatiles (tar), non-condensable gases, and char. For the combustion characteristics, another fixed bed reactor was constructed to monitor the weight and temperature of the fuel particles during ignition and combustion under different air flow rates. The test results were used to derive the ignition and burning rates.

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전라남도 농촌지역의 생활환경시설 격차 분석 - 도로 및 상하수도 정비수준을 중심으로 - (A Study on the Basic Infra-Structure Disparities in Jeollanam-do Rural Areas - With Special Reference in Rural Roads, Public Water and Sewage Disposal Services -)

  • 윤치욱;최수명;김영택;박용진
    • 농촌계획
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    • 제18권2호
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    • pp.69-79
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    • 2012
  • This study was carried out to analyze the disparities of basic living infrastructure between Guns(rural counties), and between Eups/Myuns(rural districts) in Jeollanam-do province. For the purpose of this study, dimensions of regional disparity in basic living structure were measured by 3 components ; road, public water service and sewage disposal. By utilizing the published statistics, this study has examined 8 Guns(counties) containing Eup and Myon in Jeollanam-do province which can represent 4 different rural areal types, respectively, i,e. mountainous, semi-mountainous, flat and seashore areas. The data acquisition time of this study is fixed on end of 2009 year in order for possible collections of the most recent published statistics. It presents evidence on the magnitude and evolution of discussion of regional disparities between Guns(counties), and between Eup & Myon, and between Myons in Jeollanam-do province even though infrastructure provision level of Jeollanam-do rural areas are much more improved than the past. Concludingly, the existing disparities in this area is meaningful and so, it should be seriously reconsidered when deciding local government's budget allocation priority.

폐플라스틱용기 미디어를 활용한 오수고도처리 (Advanced Treatment of Sewage Using Waste Plastic Vessel Media)

  • 김재용;엄명헌;안대현;심명진
    • 공업화학
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    • 제17권1호
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    • pp.58-61
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    • 2006
  • 본 연구는 폐플라스틱용기 미디어 산화공법을 이용하여 유체 및 산소전달 효율 향상을 위한 개조 방법과 미생물 부착특성을 향상시키는 방법을 통하여 오수고도처리 함을 목적으로 하고 있다. 또한 실험실 규모의 실험에서 최적의 담체 층진율과 충진 방법을 도출함으로써, 실 규모 설비를 위한 최적 설계 인자와 운전인자를 확보하고, 오수의 고도처리를 위한 다양한 운전조건을 제공하여 폐플라스틱 용기를 미생물 담체로 사용할 경우 생물학적 반응에 의해서 분해 될 때 소비되는 산소량과 오수중에 현탁되어 있는 유, 무기성 부유물과 질소 제거가 이루어지는 메카니즘을 규명하고 오수 처리 효율 향상을 위한 운전인자 도출을 목표로 한다.

음식물찌꺼기 산발효산물과 하수슬러지의 혼합비 및 유기물부하가 병합처리에 미치는 영향 (Effects of Mixing Ratio and Organic Loading Rate of Acid Fermented Food Wastes and Sewage Sludge on the Anaerobic Digestion Process)

  • 안철우;박진식;장성호
    • 한국환경농학회지
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    • 제25권3호
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    • pp.247-256
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    • 2006
  • 본 연구에서는 실험실 규모의 혐기성 소화 실험을 통하여 고온산발효를 거친 음식물찌꺼기 산발효액과 하수슬러지의 적정 혼합비와 유기물 부하율에 따른 반응조 운전특성을 분석하여 실제 플랜트에 적용가능성을 검토하여 얻은 결론은 다음과 같다. 음식물지꺼기 고온 산발효액과 하수슬러지를 혼합하여 반연속식으로 혐기성 소화실험을 실시한 결과 유기물 부하율 3.3 gVS/L.d(혼합비 1:1)에서 최적인 것으로 평가되었는데, 이때 SCOD 제거효율은 평균 74.2%, VS 제거효율은 73.6%, 주입된 VS당 생성된 가스량은 $0.440{\ell}/g\;Vs_{add}.d$였으며 평균 메탄 함량은 66.5%로 나타났다. 이는 기존에 음식물찌꺼기를 하수처리장의 중온 소화조에서 처리할 때의 유기물 부하보다 높아 효율성, 경제성에서 유리한 것으로 판단되었다.