• 제목/요약/키워드: Sand bed

검색결과 324건 처리시간 0.036초

Movement of Sand around Revetment under Water Pressure Variation

  • HoWoongShon
    • 지구물리
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    • 제6권4호
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    • pp.221-230
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    • 2003
  • Many hydraulic structures are damaged by under flood flow and storm waves year after year. Many cases of dike and breakwater failure are caused by the suck out of sand from behind the revetment. This type of failure will be in close relation to the dynamic behavior of sand bed around the revetment. In this paper, from this point of view we investigated the basic characteristics of such sand movement by small model tests and tried to explanation the hydro- and soil mechanical mechanism of this phenomenon theoretically.

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정수장 급속여과지 역세척 수위변화와 시간에 따른 세척 효율 평가 (Evaluation of a Rapid Sand Filter with Surface Wash and Backwash Conditions)

  • 정용준;민경석
    • 한국물환경학회지
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    • 제20권6호
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    • pp.652-656
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    • 2004
  • Both surface wash and backwash are considered as one of the most important methods that can improve the filtration efficiency in the existing water treatment plant. This study has mainly focused on the improvement of filtering efficiency by controlling surface wash and backwash time, and water level before backwash (when drained up to the trough, when drained up to 10 cm above filter bed, and when drained below 10 cm filter bed). Filtration efficiency was shown a little bit of differences depending on the operating conditions like surface wash injection pressure, the distance control between filter bed and the facility, and the types of surface wash. When the water level before backwash was reached up to 10 cm below filter bed after draining, however, the filtration velocity and the turbidity removal efficiency in the filter bed was improved. When the surface wash followed by backwash is longer, it showed a similar result. Because the proper adjustment of surface washing time makes filtration efficiency higher, therefore, it is necessary to set up the backwash time moderately.

유동층 생물막 반응기에서의 폐수 탈질화 (Denitrification of Wastewater in a Fluidized Bed Biofilm Reactor)

  • 신승훈;서일순;장인용
    • KSBB Journal
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    • 제16권4호
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    • pp.337-343
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    • 2001
  • 탈질화 유동층 생물막 반응기에 모래와 활성탄 입자를 담체로 사용한 결과 다음과 같은 결론을 얻었다. 1. 정상상태 생물막 두께는 부하율이 증가할수록 증가하였다. 2. 활성탄 담체의. 경우 모래 담에의 경우보다 두꺼운 생물막이 형성되었다. 3. 생물막 건조밀도는 생물막 두께가 증가함에 따라 감소 하였다. 4. 모래담체 유동층 생물막 반응기가 질산성질소 제거효율 및 제거속도 면에서 활성탄담체 유동층 생물막 반응기보다 유리하였다. 5. 모래를 담체로 사용하였을 때 반응기 내 최대 균체량은 37 kg/㎥, 최대 질산성질소 제거속도는 21 kg N/㎥d의 값을 각각 나타내었다.

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완속여과 공정에서 표층 생물막 생성 및 제어와 원인조류 규명 (Analysis and effectiveness of biological thin Layer (Schmutzdecke) on the sand surface in slow sand filtration processes)

  • 김성수;박노석;김충환;박종근
    • 상하수도학회지
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    • 제22권3호
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    • pp.289-298
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    • 2008
  • Because of their simplicity, efficiency, and economy, slow sand filters are appropriate means of water treatment for small water systems. Biological activity within the sand bed have the strongest influence on removal efficiency of pollutants by slow sand filtration. This report investigated the microorganisms(algae) of slow sand filtration pilot plant at Y water treatment plant. Data were collected at inflow and slow sand filtration from May to October, 2007. The results indicated that the light exposure was influenced on microorganism in slow sand filtration according to the formation of algal biofilm. The relative contribution of biomass and accumulated particulates to head loss development in slow sand filters requires further study.

상수 정화법에 관한 연구 (폭기식 다단여과에 의한 호기성균의 생물화학적 산화작용을 응용) (A Study on Purification of Water Works by Multi-filter Bed Method with Aeration(Appliction of Biological Oxidation by Aerobic Microorganism))

  • 정요한;문재규;주흥규;서화중
    • Journal of Preventive Medicine and Public Health
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    • 제5권1호
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    • pp.43-48
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    • 1972
  • 5 bed sand filter, applying biological oxidation, was designed and studied on the treatment of water works. Never using any coagulant agent (drugs), which may cause water pollution in pre-treatment of head water, the auther attempt a high rate filtration by the microorganism (nitrofication bacteria) end plant which populate in multi layer sand beds. The result are as follows : In order to evaluate the oxygen effect on filtration, oxygen was injected in aeration tank attached to each filter tank while filtration, and $NH_3$ was tested as a representaiive ingredient. It was found out that the aeration method was more effective, with over 33% of $NH_3$ removal capacity, than the anerobic and this 5 bed filter showed double removal capacity of $NH_3$ by comparing with conventional sand bed (2 stage bed). According to the examination of two kind of head water, pre-treated with coagulant agent and activated carton, the filtration capacity was affected by the polluted condition of head water, resulting that lower value of pollution and slower velocity of filtration showed more efficiency of $NH_3$ removal. In this experiment $NH_3$ content tested in treated water had a fairly good correlation with others.

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Catalytic Fast Pyrolysis of Tulip Tree (Liriodendron) for Upgrading Bio-oil in a Bubbling Fluidized Bed Reactor

  • Ly, Hoang Vu;Kim, Jinsoo;Kim, Seung-Soo;Woo, Hee Chul;Choi, Suk Soon
    • 청정기술
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    • 제26권1호
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    • pp.79-87
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    • 2020
  • The bio-oil produced from the fast pyrolysis of lignocellulosic biomass contains a high amount of oxygenates, causing variation in the properties of bio-oil, such as instability, high acidity, and low heating value, reducing the quality of the bio-oil. Consequently, an upgrading process should be recommended ensuring that these bio-oils are widely used as fuel sources. Catalytic fast pyrolysis has attracted a great deal of attention as a promising method for producing upgraded bio-oil from biomass feedstock. In this study, the fast pyrolysis of tulip tree was performed in a bubbling fluidized-bed reactor under different reaction temperatures, with and without catalysts, to investigate the effects of pyrolysis temperature and catalysts on product yield and bio-oil quality. The system used silica sand, ferric oxides (Fe2O3 and Fe3O4), and H-ZSM-5 as the fluidized-bed material and nitrogen as the fluidizing medium. The liquid yield reached the highest value of 49.96 wt% at 450 ℃, using Fe2O3 catalyst, compared to 48.45 wt% for H-ZSM-5, 47.57 wt% for Fe3O4 and 49.03 wt% with sand. Catalysts rejected oxygen mostly as water and produced a lower amount of CO and CO2, but a higher amount of H2 and hydrocarbon gases. The catalytic fast pyrolysis showed a high ratio of H2/CO than sand as a bed material.

하상재료에 따른 ADCP의 유량측정 비교 분석 (Comparative Analysis of ADCP Flow Measurement According to River Bed Material)

  • 최진우;홍창수;신경용;이진욱;김정애;조용철;유순주
    • Ecology and Resilient Infrastructure
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    • 제5권3호
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    • pp.156-162
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    • 2018
  • 본 연구는 하상재료에 따른 ADCP의 측정 적합성을 평가하기 위해 하상 재료가 다른 자갈 하상과 모래 하상인 지점에서 ADCP의 유속, 수심 및 유량 자료를 ADV의 측정 결과와 비교 분석하였다. 연구결과 자갈 하상과 모래 하상에서의 ADV와 ADCP를 이용한 유속 분포와 수심 측정 자료는 비슷하게 나타났다. 유량측정 결과 자갈 하상에서 평균 3.5 - 4.8%, 모래 하상에서 평균 0.02 - 3.2%의 상대오차 범위를 나타내어 USGS에서 제시한 평균 오차 5%의 범위보다 작아 신뢰가 높은 결과인 것을 알 수 있었다. 이한 결과는 향후 ADCP의 하천 적용성에 대한 기초자료로 활용될 수 있으며 ADCP의 불확도 평가에 중요한 자료로 이용될 것으로 판단된다.

낙동강 삼각주 북부의 고환경 (The Paleoenvironment of the Northern Part of the Nagdong River Delta)

  • 오건환
    • 한국제4기학회지
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    • 제8권1호
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    • pp.33-42
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    • 1994
  • The study area is filled up by alluvium which can be classified into lower and upper beds by the facies of deposits and their degree of weathering. The lower bed is not of marine but of fluvial. The upper bed is mainly composed of clay and silt or fine sand beds col-ored dark or dark gray which are of neritic or brackish yielding mollusca fossils. The oyster(Crassostrea ariakensis) obstained from the depth of 3m below the present sea level in the upper bed was dated at 4,100 110Y.B.P. and the veneridae(Meretrix lamarck) 1m height above the present delta plain in the old sand bar was dated at 1,700 85Y,B,P. It is therfore concluded that the study area a small kern col of terrestri-al basin prior to postglacial age had experienced the Holocene transgression. Consequently the study area is considered to have been progressively formed under neritic or brackish circumstance before 1,700Y.B.P.

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유동상식 소각로에서 발생되는 폐유동사(廢流動床) 처리 및 재활용 방안 (A Study on Treatment and Recycling of Waste Fluid Sand from the Fluidized Bed Incinerator)

  • 이승원
    • 한국환경과학회지
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    • 제29권11호
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    • pp.1015-1024
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    • 2020
  • Using the waste(sand wastr and boiler ash) in fluidized bed inciverator, lightweight aggregate concrete was produced and a recycling plan was prepated. The first, the result of the leaching test shows that the waste fluid sand and boiler ash did not exceed the effluent standard. This indicates that there is no harmful effect for recycling. The second, in the lightweight aggregate test using waste fluid sand and boiler ash, the sample that combined cement, waste fluid sand, and sand showed the highest compressive strength, and the mix proportion was 10: 7: 3. Lightweight aggregate concrete that combined cement, waste fluid sand, boiler ash, and sand had a low compressive strength by and large. The third, the same results were identified in the relation between the content of SiO2 and that of Na2O. As the SiO2 content is lowered, the overall viscosity and plasticity of the concrete also decrease, which is not a good condition to form concrete. As for Na2O, as the content increases, the viscosity of the sample and the viscosity of the cement are remarkably lowered, and the strength of the finished concrete is lowered. Therefore, it was concluded that the higher the content of SiO2 and the lower the content of Na2O, the more suitable it is to mix with cement to produce concrete. Fourth, from the fluidized bed incinerator currently operated by company A in city B, a total of 14,188 tons/year were discharged as of 2016, including 8,355 tons/year of bottom ash (including waste fluid sand) and 5,853 tons/year of boiler ash. The cost for landfill bottom ash and boiler ash discharged is 51,000 won/ton, and the total annual landfill cost is 723,588,000 won/ year. Assuming that the landfill tax to be applied from the year 2018 is about 10,000 won/ton, and if there is no reduction in waste disposal charge, an additional landfill tax of 141,880,000 won/year will be imposed. Consequently, the sum total of the annual landfill cost will be 865,468,000 won/year. Therefore, if the entire amount is used for recycling, the annual savings of about 8.7 billion won can be expected.

실리카샌드를 이용한 메탄하이드레이트 형성과 분해 (Formation and Decomposition of Methane Hydrate Using Silica Sand)

  • 남성찬;프라빈 링가;피터 앵글래죤스
    • 공업화학
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    • 제19권6호
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    • pp.680-684
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    • 2008
  • Silica sand 내에서의 메탄 하이드레이트($CH_4$ hydrate)의 형성과 분해는 $7.0^{\circ}C$의 온도에서 실험되었다. Silica sand 내에서 형성되는 메탄 하이드레이트의 형성 및 분해 특성을 연구하기 위해 새로운 반응기를 제작하였다. Silica sand bed 내에서 메탄하이드레이트의 형성과 분해되는 동안의 온도변화에 대한 연구를 위해 반응기 내의 주입한 silica sand 높이에 따라 열전대의 위치를 다르게 설치하여 실험하였다. 반응기 내에 가해지는 압력과 온도는 메탄 하이드레이트의 형성과 분해를 발생시키는 요인이다. 메탄 하이드레이트 형성을 위한 가스 흡착곡선과 분해실험을 위한 가스 발생곡선은 실험데이터로부터 결정되었다. 8 MPa의 압력에서 $7.0^{\circ}C$의 온도에서 메탄 하이드레이트 형성 실험을 수행한 결과 70%의 메탄이 하이드레이트로 전환됨을 알 수 있었다. 형성된 메탄 하이드레이트의 분해에 의한 메탄의 회수율은 82%였다.