• Title/Summary/Keyword: COD removal

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Removal of Contaminants Using Natural Purification Method by Sheet Flow (박층류 자연정화공법을 이용한 오염물질의 제거)

  • Kim, Myounghwan;Lee, Du Han;Kim, Won
    • Proceedings of the Korea Water Resources Association Conference
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    • 2018.05a
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    • pp.451-451
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    • 2018
  • 박층류 자연정화공법은 수로의 폭을 넓히고 수심을 낮추어 박층류를 조성하고, 이를 이용하여 하천을 정화하는 공법이다. 박층류가 조성되면 낮은 수심에서 상대적으로 느린 유속 조건이 형성되며 이 때 박층부에 침전된 오염물질은 자갈층 표면에 형성된 생물막에 의해 산화 분해되어 제거된다. 박층류에 의한 오염물질 제거는 생물막의 형성, 생물 산화를 위한 용존산소량 등이 중요한 인자로 작용하며, 박층부를 조성하기 위해서는 수심 10 cm, 유속 30~50 cm/s 의 조건이 적절하다. 본 연구에서는 박층류에 의한 자연정화 성능을 평가하기 위하여 용인시 오산천 일부 구간 고수부지에 사석자갈을 이용한 박층류 자연정화공법이 적용된 차집수로를 설치하고, 오산천으로 유입되는 농수로의 물을 공급하여 오염물질의 농도 변화를 측정하였다. 측정된 항목은 T-N, T-P, COD, DO 등이며, 측정 결과 박층류 자연정화 수로를 유출부에서의 오염물질의 농도가 유입부에서보다 저감되는 것을 확인 할 수 있었다.

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Effective Application Method for Pollution Mitigation Facility of Highway Runoff (고속도로 비점오염저감시설의 효율적 적용 방안)

  • Lee, Yong-Bok;Choi, Sang-Il;Jung, Hyun-Gyu;Bae, Sei-Dal;Jung, Sun-Kook
    • Korean Journal of Soil Science and Fertilizer
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    • v.44 no.6
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    • pp.1264-1271
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    • 2011
  • To build environmentally friendly highways, we testes suitability for unique characteristics of pollution mitigation facility around the highways by evaluating optimal selections and implementation methodologies to minimize loan of non-point pollution substances into water-ways. To do this we categorized EIA target highways into three types ; big drainage basin, small drainage basin, and bridge section as to minimize non-point pollution of highway runoff. The terms of selected facility test based on the Natural and Manufactured Treatment Device were removal efficiency of TSS, BOD, COD, T-N, T-P, compatibility of site selection, economic feasibility, maintenance convenience, and the final mitigation facility.

The Case of Industrial Factory Wastewater Treatment and Reusing by Using of Constructed Wetland (식물정화조를 이용한 공업용 폐수의 정화 및 재활용 사례)

  • 김혜주;이옥하
    • Korean Journal of Environment and Ecology
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    • v.16 no.2
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    • pp.179-187
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    • 2002
  • Constructed wetland was built for industrial factory wastewater treatment with environmentally sound method from July to October, 2000. Ultimately this case study was carried out to conserve water quality of river and underground water and to provide wildlife habitat and rest place for people in the industrial area. The size of constructed wetland was 10m$\times$6m (upper area) with a treatment capacity of 2.5㎥ per day. It was supplied with wastewater 0.625㎥ at intervals of six hours. Vertical flow system was chosen to promote efficiency. Draining layer was built one meter in soil depth out of sand mixed with pebbles in a ratio of two to one. Perennial emergent plants, Phragmites communis, Typha orientalis, Juncus effusus, Iris pseudoacorus, 20 individuals per square meter were planted. In the aspect of reusing, eco-pond was created for increasing biological species diversity and also deck and information signboard were established for the education of environment. As the result of monitoring, it was revealed that the constructed wetland was effective in removal of BOD$_{5}$, COD, T-N, T-P and has being gradually improved as a wildlife habitat(biotope).

Treatment of Dyeing Wastewater Using Polyamid Ro-Membranes After the Pretreatment with Chemical Coagulants (화학응집제에 의한 전처리 후 폴리아미드 RO-분리막에 의한 염색폐수처리)

  • Jegal Jonggeon;Mo Joonghwan;Hwang Jeong-Eun;Lee Kew-Ho;Kim Jaephil
    • Membrane Journal
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    • v.14 no.3
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    • pp.230-239
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    • 2004
  • Treatment of a dyeing wastewater was carried out using polyamide RO-membranes. Before applying the wastewater to the membrane process, it was pretreated with various chemical coagulants such as alum, ferric chloride and HOC-100A. In order to see the effect of the pretreatment on the membrane separation process, the optimum conditions for the coagulation and sedimentation process were sought. As a result, by the pretreatment, for all the coagulants used, the chemical oxygen demand (COD) and UV-absorbance of the wastewater were lowered by more than 70%. The pretreated wastewater was then applied to the membrane process. The effect of the coagulants used for the pretreatment on the membrane fouling was studied. From this study, it was found that the HOC-100A was the best out of the coagulants used for the removal of the materials that could cause membrane fouling.

조류를 이용한 유기성 폐수 처리 시스템과 물벼룩 성장 조건

  • Jo, Jae-Hun;Kim, Jun-Hwi;Lee, Jeong-Seop;Yun, Seong-Myeong;Kim, Si-Uk
    • 한국생물공학회:학술대회논문집
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    • 2001.11a
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    • pp.568-571
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    • 2001
  • Food wastewater eluted from the three-stage methane fermentation system developed in this lab showed high concentrations of TCOD, BOD, T-N and T-P. Because the effluent of biological filter chamber (BFC) still had high concentration of nitrogen and organic material, the effluent was treated with algal periphyton system using algae. The removal rates of COD, T-N and T-P wer 96, 98 and 91%, respectively, in this system. The grown algae could digested byy waterfleas using the ecological food chain system. Food wastewater is better than algal culture medium for growth of waterflea, Moima Macrocopa. During 12days, the individual of waterflea increased to 180 in the food wastewater containing a T-N concentration of 150 mg/ ${\ell}$.

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Formation of Sedimentation Pool within Irrigation Reserviors for Water Quality Improvement (저수지 수질개선을 위한 저수지 내 침전지 조성)

  • 박병흔
    • Magazine of the Korean Society of Agricultural Engineers
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    • v.42 no.1
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    • pp.73-82
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    • 2000
  • Large quantitive of polllutants are washed into reservoirs during storm events. These polllutants contribute to eutrophication, such as algal blooms and fish kills. This study was conducted for the purpose of assessing the pollutant removal possibilities of sedimentation pool formed by deep dredging of a reservoir inlet. Water quality data were collected in the Masan reservoir, whose inlet has been dredged deep like sedimentation pool. The average concentration of chemical oxygen demand(COD) , toatal nitrogen(T-N) and total phosphrous(T-P) in the deep dredged area were 8.7 ~20.5mg/ι (T-N), 0.17~0.84mg/ι(T-P), which were 4.9%(COD), 29.0%(T-N) and 44.8%(T-P) higher than those of middle part of the reservior. The texture of sediment in the dredged area was silty loam, while that of the middle part was sandy clay loam. Organic matter contents, T-N and T-P of the bottom soil in the dredge area showed higher values than the middle part of the reservoirs. From these results, it was considered thedeep dredged area in the inlet of reservoir might play a key role to settle pollutant particulate. Based on the result of water quality analysis, deep dredging of the reservoir inlet could be assessed to reduce T-N and T-P of the reservoir about 6.5% , 8.3%, respectively. However, the effect of the sedimentation pool would be raised if the settled particles were taken into account in assessing water quality improvement for the reservoir. Accordingly, dredging of a reservoir inlet to make a shape of sedimentation pool is recommended for water quality improvement of reservoir in the stage of dredging plan.

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Treatment of Livestock Wastewater with Coagulant-loess (황토를 이용한 축산폐수의 처리에 관한 연구)

  • Park, Jin-Hee;Kim, Bo-Guk;Won, Chan-Hee
    • Journal of Korean Society of Environmental Engineers
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    • v.22 no.10
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    • pp.1799-1808
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    • 2000
  • To investigate the applicability of loess as a coagulant. the optimum conditions of coagulation and efficiency comparison of several coagulants (PAC, PACS, LAS) in chemical treatment of livestock wastewater were performed. As a result, the optimum mixing ratio of loess and lime(CaO) was 3:7. The optimum dosage of the mixed coagulant was 30 g/L. The optimum speed for rapid mixing of the mixed coagulant was 200 rpm at 1 min. and the optimum speed for slow mixing was 50 rpm at 10 min. The mixed coagulant showed the removal efficiency of turbidity, SS, BOD, $COD_{cr}$. T-P and TKN to 95.8%, 92.5%, 71.6%, 71.1%, 98.2% and 32.5%, respectively, which was better than other several coagulants. The mixed coagulant was possible to use as substitutional coagulants of traditional coagulant, and the producted sludge can use as a soil amendments.

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Statistical Characteristics of An Advanced Wastewater Treatment Plant for Leather Industry (피혁폐수 고도처리시설의 통계학적 특성)

  • Yang, H.J.;Kwon, O.S.;Kim, J.H.;Kim, S.H.;Lee, S.J.;Jung, D.I.
    • Journal of Korean Society on Water Environment
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    • v.23 no.5
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    • pp.740-747
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    • 2007
  • The advanced wastewater treatment plant of leather industry was selected to evaluated with its effluent water quality and statistical characteristics. Most of pollutants removal efficiencies were over 90% as well. And 95% reliability of effluent concentration were 106.8 mg/L of $COD_{mn}$, 72.04 mg/L of TN. However Effluent quality of TN exceeds the regulated limit. The range of coefficient of variation (CV) were between 0.18 and 2.49. Also, coefficient of reliability (COR) were between $0.03(BOD_5){\sim}0.63(COD_{mn})$ and 0.43 in terms of T-N, $Z_{l-a}$(Normalized Percentiles) value were 55.7 and 2.25 in terms of $BOD_5$ and T-N as shown in the following table.

Optimal Treatment of Molasses Wastewater Using UASB Process (UASB 공정에 의한 당밀폐수의 최적처리 방안)

  • Huh, Kwan-Yong;Jeong, Eui-Geun;Chung, Yoon-Jin;Yoo, Sang-Keun
    • Journal of Korean Society of Water and Wastewater
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    • v.11 no.2
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    • pp.112-127
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    • 1997
  • The purpose of this study is to get optimum operating factors of Upflow Anaerobic Sludge Blanket (UASB) reactor by introducing methods that make it to reduce inhibition possible in each process wastewater treatment. The used substrates, concentrated corn starch liquid (CSL) wastewater, modified starch, filtering and decoloring wastewater, ion refining wastewater, and mixed wastewater including modified starch and not including modified starch, are generated from molasses process. The seeding sludge is the digested sludge that had been applied to molasses wastewater. Batch test to reduce the inhibition factors that might be existed in each wastewater was examined. Based on the this test, the optimum operating factors according to alkalinity and pH variation was studied through the continuous test using three 5.5 L UASB reactor. The first reactor added $NaHCO_3$ to control alkalinity. The hydraulic retention time (HRT) reduced to 8 hours and the organic loading rate increased gradually. The second reactor changed the pH of influent from 7.0 to 6.0 using NaOH. The third reactor was operated without changes to compare the above two reactors. As the result, the inhibition in concentrated CSL wastewater was removed by adding iron (II). When trace metals were added to mixed wastewater not including modified starch, the digestability by gas production rate increased to more fifty percentage than mixed wastewater that was not adding the trace metals. The reason that the inhibition did not decreased in spite of adding trace metals and nutrients was influenced by high concentration generated during the acid fermentation. The UASB reactors using the mixed wastewater with the most effective performance were operated as 500 mg/L as $CaCO_3$ alkalinity and 6.0 pH at steady state, and at this time, the gas production rates were 283 and 311mL gas/g $COD_{added}$. The COD removal rates were 84.7 and 86.3%, respectively.

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Mixture treatment of food waste and sewage sludge using pilot scale anaerobic digester (Pilot scale 2단 혐기성 소화조를 이용한 음식물쓰레기와 하수슬러지의 혼합처리)

  • Park, Nam-bae;Lee, Heon-Mo;Lee, Byung-Heon
    • Journal of the Korea Organic Resources Recycling Association
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    • v.7 no.2
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    • pp.47-55
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    • 1999
  • Recently, the treatment of that wastes according to increase of food waste has been a great problem of modern society for long time. This study was aimed to evaluate possibility for food waste and sewage sludge mixture treatment using pilot scale two-phase anaerobic digester. Pilot scale two-phase anaerobic digestion system was performanced at 1 : 9 mixture ratio of food waste and sewage sludge infield. The detention time of digester was 20days. The average COD and VS removal efficiencies in organic loading rate $3.03kg\;TCOD/m^3-day$ were 57.7 and 47.7%, and the gas production rate and methane content were $0.4m^3/kg$ VS-day and 65.3%, respectively. TS, VS and VS/TS(%) of mixing tank were 4.44%, 2.59% and 58.34%, respectively and TS. VS and VS/TS(%) of digester in steady state were 3.32%, 1.39% and 41.90%, respectively, Through this study. it was possible to accomplish effective mixture treatment of the sewage sludge and food waste.

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