• 제목/요약/키워드: Piggery Wastewater

검색결과 68건 처리시간 0.027초

소규모 축산폐수 처리를 위한 RBC/AFBR공정의 Package화 (Package of RBC/AFBR process for small-scale Piggery Wastewater Treatment)

  • 임재명;권재혁;류재근
    • 환경위생공학
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    • 제11권2호
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    • pp.43-52
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    • 1996
  • Using rotating biological contactor(RBC) with artificial endogenous stage and aerobic fixed biofilm reactor(AFBR), organic material removal and biological nitrification of piggery wastewater has been studied at a pilot plant. RBC was operated in the endogenous phase at a interval of every 25 days. The concentration of COD, BOD and TKN in influent wastewater were from 2,940 to 3,800 mg/L, from 1,190 to 1,850 mg/L and from 486 to 754 mg/L respectively. The maximum active biomass content represented as VSS per unit aera was $2.0mg/cm$^{2}$ and biofilm dry density of $17mg/cm^{3}$ was observed at biofilm thickness of $900{\;}{\mu}m$. It was observed that the pilot scale RBC/AFBR process exhibited 72 percentage to 93 percentage of BOD removal, In order to obtain more than 90 percentage of BOD removal, the organic loading rate to the RBC/AFBR process should be maintained less than $0.09{\;}m^{3}/m^{2}{\cdot}day(125.9g{;\}BOD/m^{3}{\cdot}d$. The TKN removal efficiencies was from 45.5 to 90.9 percentage according to vary influent loading rate, It was estimated that the RBC/AFBR process consumed approximately 6.2 mg/L(as $CaCO_{3}$) of alkalinity per 1 mg/L of $NH_{3}$-N oxidized as the nitrification took piace.

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화학적 응집을 이용한 생물학적 돈분폐수 처리수의 색도제거 (Removal of Color from a Biological Piggery Wastewater Treatment Effluent by Chemical Coagulation)

  • 박노백;서태경;최우영;전항배
    • 대한환경공학회지
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    • 제30권10호
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    • pp.1047-1053
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    • 2008
  • 돈분폐수 처리수의 색도를 제거하기 위해 최적의 응집 조건에 대하여 평가하였다. 유출수의 용존 유기 탄소 농도는 227.3 mg/L, 색도는 2,430 CU, 탁도는 22.1 NTU, 그리고 UV$_{254}$는 3.7 cm$^{-1}$이었다. 유출수의 소수성 유기물은 55.3%, 반친수성 유기물은 17.4%, 그리고 친수성 유기물은 27.3%로 세분화하였다. 또한, 겉보기 분자량 분포는 0.5 K 이하, 0.5$\sim$1 K, 1$\sim$10 K, 10$\sim$30 K 및 30 K 이상은 각각 74.2%, 7.3%, 5.5%, 7.1% 및 5.9%이었다. 최적의 pH 및 응집제 주입량을 결정하기 위해 유동전류계를 사용하였다. 황산알루미늄과 염화 제 2철의 최적 응집제 주입량 및 pH는 각각 5.84 mM, pH는 5.3이며, 9.25 mM, pH는 5.0이었다. 최적의 응집 조건에서 황산알루미늄과 염화 제 2철은 각각 91.9%와 98.7%로 높은 색도 제거 효율을 얻었다. 생물학적 처리를 거친 돈분폐수는 화학적인 응집으로 색도제거에 좋은 성과를 보여주었다.

이상혐기공정의 축산폐수 공공처리시설 적용 가능성에 관한 실험적 연구 (A Study on the Evaluation of Two-Phase Anaerobic Process for Public Livestock Wastewater Treatment Plant)

  • 오성모;김문호;배윤선;박철휘
    • 상하수도학회지
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    • 제21권3호
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    • pp.331-339
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    • 2007
  • The purpose of this study was to investigate the biodegradability and performance of organic removal and methane production rate when treating piggery wastewater using a pilot scale two-phase anaerobic system operated up to a volumetric rate of $10m^3/day$. The pilot scale two-phase anaerobic process is consisted of a continuous-flow stirred-tank reactor (CFSTR) for the acidification phase and an Upflow Anaerobic Sludge Blanket reactor (UASB) for the methanogenesis. The acidogenic reactor played key roles in reducing the periodically applied shock-loading and in the acidification of the influent organics. The acidogenic CFSTR was operated at organic loading rates (OLR) between 1.8 and $14.4kgCOD/m^3{\cdot}day$, and the UASB reactor was operated between 0.5 and $5.6kgCOD/m^3{\cdot}day$. A stable maximum biogas production rate was $81m^3/day$ and the methane conversion rate of the organic matter varied from 0.30 to $0.42L\;CH_4/g\;COD_{removed}$(0.40) at hydraulic retention time (HRT) above 3.5days. The methane contents ranged from 73 to 82% during the experimental period. It is known that most of the removed organic matter was converted to methane gas, and the produced biogas might be high quality for its subsequent use.

돼지 축분자원화물의 발생 및 배출부하 원단위 산정에 관한 연구 (A study on the estimation of unit load generation and discharge from livestock resources of piggery)

  • 한기봉;강영희;윤지현;임재명;원철희;최승철
    • 유기물자원화
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    • 제14권3호
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    • pp.91-100
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    • 2006
  • 본 연구에서는 돼지 분 뇨 및 폐수의 오염물 부하를 조사 및 분석함으로써 다양한 형태의 돼지 돈사로부터 발생 및 배출되는 오염물 부하 원단위를 산정한 결과는 다음과 같다. 오염물질의 발생부하 원단위는 돼지의 성장단계에 비례하여 증가하였으나, 돈사의 형태에 따른 발생부하 원단위는 각 돈사별 평균값을 고려할 때 큰 차이를 보이지 않았다. 3계절과 생체 중량을 고려한 평균 분뇨 발생량은 분이 1.49kg/head/d, 뇨가 3.08kg/head/d로서 총 4.57kg/head/d가 발생하였다. 돈사의 형태와 계절을 고려한 최종적인 평균 오염물질 발생부하 원단위는 BOD 199.5g/head/d, $COD_{cr}\;413.5g/head/d$, T-N 27.8g/head/d, T-P가 5.3g/head/d로 나타났다. 시멘트 돈사에서 배출되는 폐수의 배출부하 원단위는 BOD 31.3g/head/d, $COD_{cr}\;95.6g/head/d$, T-N 8.9g/head/d, T-P가 3.1g/head/d로 조사되었다. 분의 수거율(80%, 90%)을 고려한 분의 발생부하 원단위와 시멘트 돈사의 폐수발생 원단위의 합을 슬러리 돈사의 배출부하 원단위와 비교 시, 오염물질과 항목별로 다소의 차이는 있으나 거의 유사하였다.

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활성슬러지-인공습지 공법에 의한 돈사폐수처리시스템에서 오염물질의 분획별 정화효율 평가 (Evaluation of Treatment Efficiencies of Pollutants under Different Pollutant Fractions in Activated Sludge-Constructed Wetland System for Treating Piggery Wastewater)

  • 김성헌;서동철;박종환;이충헌;최정호;김홍출;하영래;조주식;허종수
    • 한국환경농학회지
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    • 제31권4호
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    • pp.344-350
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    • 2012
  • 돈사폐수의 분획별 및 우리나라 기후변화 특성에 대한 활성슬러지-인공습지 공법에 의한 돈사폐수처리장의 대응성을 검토하기 위하여 오염물질 분획별 및 계절별 수처리효율을 조사하였다. 오염물질 분획별 수처리효율을 조사한 결과 최종 방류수의 COD는 213.5 mg/L정도로 soluble형태가 71.5 mg/L, insoluble형태가 142 mg/L정도이었고, SS함량은 118 mg/L정도로 volatile형태가 102 mg/L, fixed형태가 15.5 mg/L정도이었으며, 최종 방류수의 T-N함량은 47.8 mg/L 정도로 dissolved형태가 12.8 mg/L, suspended형태가 35.0 mg/L정도이었다. 또한 방류수의 T-P함량은 3.05 mg/L정도로 dissolved형태가 1.13 mg/L, suspended형태가 1.93 mg/L정도이었다. 활성슬러지-인공습지 공법에 의한 돈사폐수처리장에서 계절별 수처리효율을 조사한 결과 COD, SS 및 T-P의 처리효율은 98, 99 및 99%이상으로 계절에 따라 별 다른 차이 없이 높은 처리효율을 보였고, T-N 처리효율은 여름 (99.5%)${\geq}$가을 (99.1%)${\geq}$겨울 (98.7%)${\geq}$봄 (98.2%)의 순으로 여름철에 가장 높은 처리효율을 보였다.

Modeling of Recycling Oxic and Anoxic Treatment System for Swine Wastewater Using Neural Networks

  • Park, Jung-Hye;Sohn, Jun-Il;Yang, Hyun-Sook;Chung, Young-Ryun;Lee, Minho;Koh, Sung-Cheol
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제5권5호
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    • pp.355-361
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    • 2000
  • A recycling reactor system operated under sequential anoxic and oxic conditions for the treatment of swine wastewater has been developed, in which piggery slurry is fermentatively and aerobically treated and then part of the effluent is recycled to the pigsty. This system significantly removes offensive smells (at both the pigsty and the treatment plant), BOD and others, and may be cost effective for small-scale farms. The most dominant heterotrophic were, in order, Alcaligenes faecalis, Brevundimonas diminuta and Streptococcus sp., while lactic acid bacteria were dominantly observed in the anoxic tank. We propose a novel monitoring system for a recycling piggery slurry treatment system through the use of neural networks. In this study, we tried to model the treatment process for each tank in the system (influent, fermentation, aeration, first sedimentation and fourth sedimentation tanks) based upon the population densities of the heterotrophic and lactic acid bacteria. Principal component analysis(PCA) was first applied to identify a relationship between input and output. The input would be microbial densities and the treatment parameters, such as population densities of heterotrophic and lactic acid bacteria, suspended solids(SS), COD, NH$_4$(sup)+-N, ortho-phosphorus (o-P), and total-phosphorus (T-P). then multi-layer neural networks were employed to model the treatment process for each tank. PCA filtration of the input data as microbial densities was found to facilitate the modeling procedure for the system monitoring even with a relatively lower number of imput. Neural network independently trained for each treatment tank and their subsequent combined data analysis allowed a successful prediction of the treatment system for at least two days.

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고온호기성 소화공정 배가스 처리를 위한 바이오필터 성능평가 (Performance Evaluation of Biofilter Treating Autothermal Thermophilic Aerobic Digestion Offgas)

  • 배병욱;최기승
    • 한국물환경학회지
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    • 제26권5호
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    • pp.732-739
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    • 2010
  • Two combined autothermal thermophilic aerobic digestion (ATAD) and biofilter (BF) systems were operated to treat the piggery wastewater and the ammonia offgas. Experimental results indicated that the organic removal efficiency of ATAD-2, operated with oxygen, was higher than that of ATAD-1, operated with air. The concentration of ammonia in ATAD-2 offgas was higher compared to ATAD-1 offgas, but the total amount of ammonia produced from ATAD-2 was less than that from ATAD-1 due to the lower oxygen flowrate. The ammonia gas produced from both ATAD reactors was successfully removed by the BF. The BF-1, connected with ATAD-1, removed 93% of ammonia at the loading rate of $9.4g\;NH_3-N/m^3/hr$. The BF-2, connected with ATAD-2, removed 95% of ammonia gas at the loading rate of $8.1g\;NH_3-N/m^3/hr$. As the nitrification process continued, pH value of recirculating solution continuously decreased due to the accumulation of nitrate. When the ammonia loading rate was less than $22.7g\;NH_3-N/m^3/h$, the proper replacing cycle of recirculating solution was in the range of 10 to 11 days. Almost 90% of total mass of nitrogen fed into the each BF was confirmed from the mass balance on nitrogen.