• 제목/요약/키워드: $A^2O$ biofilm process

검색결과 16건 처리시간 0.027초

생물막 담체를 이용한 실험실 규모 $A_{2}O$공법의 시스템 변형에 따른 고도처리 성능 평가에 관한 연구 (The Study on Evaluating Performances of Lab Sacle-Advanced $A_{2}O$ with Changing System Using Biofilm Process)

  • 김민식;강구영
    • 상하수도학회지
    • /
    • 제26권2호
    • /
    • pp.209-218
    • /
    • 2012
  • Recently, as reinforced water quality standards for wastewater has been announced, more efficient and more powerful wastewater treatment processes are required rather than the existing activated sludge process. In order to meet this demands, we evaluate Task 1-4 about lab scale $A_{2}O$ process using biofilm media. Task 1, 2, and 3 use 'Module A' which has 4 partitions (Anoxic/Anerobic/Oxic/Oxic). Task 4 uses 'Module B' which has 2 partitions including a denitrification reactor with an Inclined plug flow reactor (IPFR) and a nitrification reactor with biofilm media. The denitrification reactor of Module B is designed to be upward flow using IPFR. The result of evaluating at each Task has shown that attached growth system has better capacity of removal efficiency for organic matter and nitrogen with the exception of phosphorus. Task 4 which has the most outstanding removal efficiency has 90.5% of $BOD_{5}$ removal efficiency, 97.8% of ${NH_4}^{+}-N$ removal efficiency, 65% of T-N removal efficiency and 92% of T-P removal efficiency with additional chemical phosphorus removal system operated at HRT 9hr, Qi:Qir 1:2, and BOD/T-N ratio 2.7.

소규모 오수처리를 위한 $A_{2}O$ SBR과 $A_{2}O$ SBBR에서 유입 유기물 농도변화에 따른 염양염류 제거 특성 비교 (A Comparison of Nutrients Removal Characteristics by the Variation of Organics in $A_{2}O$ SBR and $A_{2}O$ SBBR for the Small Sewerage System)

  • 박영식;정노성;김동석
    • 한국환경보건학회지
    • /
    • 제32권5호
    • /
    • pp.451-461
    • /
    • 2006
  • Laboratory scale experiments were conducted to study the conversion of sludge from conventional activated sludge to nitrogen-phosphorus removal sludge using two types of sequencing batch reactor (SBR) systems, a conventional SBR and sequencing batch biofilm reactor (SBBR). The nitrogen and phosphorus removal characteristics were similar between SBR and SBBR and the removal efficiencies were very low when the influent TOC concentrations were low. The nitrogen and phosphorus removal efficiencies in SBR were 96% and 77.5%, respectively, which were higher than those in SBBR (88% and 42.5%) at the high influent TOC concentration. In SBBR, the simultaneous nitrification-denitrification was occurred because of the biofilm process. The variations of pH, DO concentration and ORP were changed as the variation of influent TOC concentration both in SBR and SBBR and their periodical characteristics were cleary shown at the high influent TOC concentration. Especially, the pH, DO concentration and ORP inflections, were cleary occurred in SBR compared with SBBR.

혐기/호기 순산소 생물막공법에 의한 산업폐수의 유기물 및 TKN 제거 성능평가 (Performance Evaluation for the A/O Pure-Oxygen Biofilm (POB) Process on the Removal of Organics and TKN in the Industrial Wastewater)

  • 장암;김홍석;김인수
    • 대한환경공학회지
    • /
    • 제22권5호
    • /
    • pp.837-847
    • /
    • 2000
  • 고농도의 유기물과 질소성분을 포함하는 맥주공장과 석유화학 산업폐수를 처리하기 위하여 실험실 규모의 혐기/호기 순산소-생물막 공정 (POB)이 이용되었다. 그리고 A/O POB process와 장기폭기법의 경제성분석도 수행되었다. TOC 농도기준으로 70에서 150 mg TOC/L 범위의 맥주공장폐수가 유입되었을 때 TOC 제거율은 각각 92% 이상으로 좋은 효율을 보였다. 석유화학폐수의 경우 초기 TOC제거율은 52%로 매우 낮았지만 32일 이후에는 86%의 TOC 제거율을 나타내었으며, TKN의 제거율은 유입부하가 증가함에도 불구하고 27일 이후에 71%의 제거율로 유지되었다. 순산소 생물막공법은 초기 건설비인 순산소 발생장치 (PSA)와 메디아 설치비가 소요되기 때문에 장기폭기법에 비하여 약 2.9배 정도 높았다. 이에 반해서 순산소 생물막공법은 극히 적은 잉여슬러지 발생량과 슬러지의 재순환의 불필요, 낮은 에너지 소요량 등의 많은 장점들로 인하여 운전비와 유지비가 약 2.5배 정도 장기폭기법 보다 적었다. 그러므로 장기적인 측면에서 보면 순산소 생물막공법이 높은 처리효율을 가지면서도 장기폭기법보다 경제적인 것으로 생각된다.

  • PDF

무산소/호기생물막반응조와 MF막의 연속처리에 의한 퍼클로레이트와 질산염 제거 (Sequential Anoxic/Aerobic Biofilm Reactors and MF Membrane System for the Removal of Perchlorate and Nitrate)

  • 최혁순
    • 대한환경공학회지
    • /
    • 제35권5호
    • /
    • pp.301-306
    • /
    • 2013
  • 본 연구는 퍼클로레이트($ClO_4{^-}$)와 질산염($NO_3{^-}$)의 직접적인 처리방법으로 무산소/호기생물막반응조와 MF막에 의한 연속처리의 적용 가능성을 조사하였다. 생물막 처리공정은 첫 번째 단계로 퍼클로레이트와 질산염의 제거를 위해 무산소생물막반응조를 이용하였고 두 번째 단계로 이화적 퍼클로레이트와 질산염 환원을 위해 사용된 잔류탄소원의 제거를 위해 호기생물막반응조가 도입되었다. 그리고 마지막 단계로 탁도제거를 위해 중공사형 MF막을 적용하였다. 본 연구에서 102 ${\mu}g/L$ $ClO_4{^-}$와 61.8 mg/L $NO_3{^-}$ (14 mg/L $NO_3$-N)가 유입수로 주입되어 퍼클로레이트는 IC 검출농도 이하(5 ${\mu}g/L$ $ClO_4{^-}$)로 제거되었으며 질산염은 최종 처리수의 농도가 4.4 mg/L $NO_3{^-}$ (1 mg/L $NO_3$-N)로 제거되었다. 탄소원으로 사용된 과잉의 179 mg/L 유입 $CH_3COO^-$는 무산소생물막반응조의 유출수에서 117 mg/L, 호기생물막반응조의 유출수에서 11 mg/L로 감소하였다. 3 NTU의 유입 탁도는 무산소/호기생물막반응조의 유출수에서 1.5와 0.3 NTU였으며 최종 MF막의 유출수에서 0.2 NTU였다. 이 결과는 지표수와 지하수에 포함된 저농도 퍼클로레이트와 질산염 오염의 직접적인 처리방법으로 무산소/호기생물막반응조와 MF막의 연속처리가 적용될 수 있음을 의미하는 것으로 사료된다.

완전침지형 회전매체 생물막 공정에서 포기강도 조절이 동시 질산화/탈질 효율에 미치는 영향 (Effect of Aeration Intensity on Simultaneous Nitrification and Denitrification Efficiency in the Submerged Moving Media Biofilm Process)

  • 김준명;이상민;임경호;김일규;강호
    • 한국물환경학회지
    • /
    • 제24권3호
    • /
    • pp.273-279
    • /
    • 2008
  • Space separation method that use independent reactor for nitrification and other reactor for denitrification has been commonly used for biological nitrogen removal process like $A^2O$ process. However, this method needs large space and complicate pipelines and time separation method such as SBR process have a difficulty in continuous treatment. Thus biological nitrogen removal process which is capable of continuous treatment, easy opeation and space saving is urgently required. In this research, submerged moving media was used for a biofilm process and suspended sludge was used for biological nitrogen removal at the same time. In particular DO environment by controlling air flow rate was investigated for simultaneous nitrification/denitrification. Total nitrogen removal in aeration rate more than $67L/min{\cdot}m^3$ showed 51~53% and rose to 65%, 70% and 78% in $50L/min{\cdot}m^3$, $58L/min{\cdot}m^3$ and $25L/min{\cdot}m^3$ respectively. Total phosphorus removal was very low about 10~20% more than $67L/min{\cdot}m^3$ aeration rates. But total phosphorus removal roses when reduces aeration rate by $58L/min{\cdot}m^3$ low and it showed total phosphorus removal of 72% in aeration rate $25L/min{\cdot}m^3$.

돼지 도축폐수 처리를 위한 RABC 공정의 생물막 세균군집 구조 (The Bacterial Community Structure in Biofilms of the RABC Process for Swine Butchery Wastewater Treatment)

  • 성기문;이동근;박성주
    • 미생물학회지
    • /
    • 제47권1호
    • /
    • pp.56-65
    • /
    • 2011
  • 돼지 도축폐수를 처리하는 Rotating Activated Bacillus Contactors (RABC) 공정의 세균군집 특성을 파악하기 위하여 그람양성세균수와 총세균수를 계수하여 기존 고도폐수처리공정인 A2O (Anaerobic-Anoxic-Oxic) 공정과 비교하였다. RABC 공정의 생물막 세균군집구조는 비배양기법인 16S rDNA 염기서열결정법을 이용하여 분석하였다. RABC 공정의 총세균수에 대한 그람양성세균수 비율은 생물막(32%)에 비해 최종포기조(1282%) 및 반송슬러지(958%)에서 현저히 증가한 반면, A2O 공정의 그람양성세균수 비율은 호기조(40%)와 반송슬러지(49%) 모두에서 상대적으로 훨씬 낮았다. 총 9개 문에 해당하는 92개의 클론이 검출되었으며, 이 가운데 최우점 집단은 Proteobacteria (64.1%)와 Actinobacteria (18.4)%로서 이들 2개 문이 전체의 82.5%를 차지하였다. 3번째로 많이 검출된 것은 내생포자형성세균집단이 속하는 Firmicutes (5.4%) 문이었다. 소량 검출된 나머지 6개 문은 Bacteroidetes (3.3%), Chlorobi (2.2%), Nitrospirae (1.1%), Chlorofleix (1.1%), Acidobacteria (1.1%), Fusobacteria (1.1%)의 순이었다. Proteobacteria 문 중에서는 Betaproteobacteria 강 34.8%, Alphaproteobacteria 강 26.1%로서 대부분을 차지하였고, Gammaproteobacteria 강은 3.2%이었다. 내생포자형성세균집단의 비율은 모두 19.4%로서, Firmicutes 문 5.4%와 Actinobacteria 문의 Intrasporangiaceae과 14.0%이었다. 질화세균 및 탈질세균과 관련된 클론 비율 6.5%, 인축적세균과 관련된 클론 비율 5.4%를 기록함으로써 무기영양소 및 악취 제거능력을 가진 세균집단이 RABC 생물막에 많이 서식하고 있음이 확인되었다.

고정상 담체와 은나노 모래여과를 이용한 이중 공정에서 처리수의 중수도 활용에 관한 연구 (A Study on the Utilization of Effluent Treated by Double Process Using Fixed-media and Sand Filter Coated by Nano Silver for Wastewater Reclamation and Reusing System)

  • 선용호
    • KSBB Journal
    • /
    • 제21권4호
    • /
    • pp.317-323
    • /
    • 2006
  • 본 연구는 다가올 물 부족에 따른 하나의 대안으로서 중수도 시스템에 초점을 맞추어, 생활오수를 이용하여 혐기/무산소/호기조의 $A^2O$ 생물막 공법으로 구성된 상향류식 고정상 담체 반응기로 처리한 오수를 하향류식 은나노 모래여과 반응기에 다시 연속 통과시켜 이중 처리하여 얻은 처리수를 중수도에 활용이 가능하지에 대하여 연구하였다. 이중 공정 후 배출수의 pH는 $7.39{\sim}8.06$(평균 7.84) 범위이었고, $COD_{Mn}$$8{\sim}18mg/L$(평균 12.1 mg/L), $BOD_5$$2.1{\sim}10mg/L$(평균 4.9 mg/L)로 중수도 수질 기준에 적합하였다. SS는 $3{\sim}9mg/L$의 범위로 평균 농도가 4.95 mg/L를 나타내면서 SS 제거율이 94.8%로 대부분 법적 기준치 5 mg/L 이하로 처리되어 가능성을 보여 주었다. 대장균군 수의 평균 제거율이 99.1%이었으며, 배출수의 평균 대장균 군수는 65 MPN/100mL이 검출되었으나 중수도 수질 기준에는 불검출로 되어 있으므로 완벽한 제거를 위해서는 0.2 mg/L 이상의 결합잔류염소의 양을 고려한 염소 처리를 하여야 한다. SEM 사진으로부터 은모래 표면에서는 박테리아가 존재하지 않음을 알 수 있었다. 이 외에 중수도 수질 기준에 포함될 가능성이 있는 총질소 및 총인의 제거율은 각각 50.3%와 27.2%이었다.

생물학적 질소제거시 운전조건의 변화가 N2O 발생에 미치는 영향 (Effects of Operational Condition on N2O Production from Biological Nitrogen Removal Process)

  • 장현섭;김태형;이명주;황선진
    • 상하수도학회지
    • /
    • 제23권5호
    • /
    • pp.547-555
    • /
    • 2009
  • The objectives of this research were focused on the effects of various operating parameters on nitrous oxide emission such as C/N ratio, ammonia concentration and HRT in the hybrid and suspension reactors. With the decreasing of C/N ratios, $N_2O$ emission rates in the both processes were increased because organic carbon source for denitrification was depleted. In case of biofilm reactor operated using medium, $N_2O$ release from the nitrification was not affected by the variation of ammonia concentration. But in the suspension reactor, $N_2O$ production from the nitrification was rapidly increased with the increase of ammonia. Nitrite accumulation caused by undesirable nitrification conditions could be a important reason for the increase in the $N_2O$ production from the aerobic reactor. And rapid increase in $N_2O$ production was reflected by the decrease of HRT, similar to the results observed in the results of ammonia loading changes. So it could be said that it is very important to put in consideration both its optimum conditions for wastewater treatment efficiency and suitable conditions for $N_2O$ diminish, simultaneously, in order to development an eco-friendly and advanced wastewater treatment, especially in BNR process.

Effect of citrate coated silver nanoparticles on biofilm degradation in drinking water PVC pipelines

  • Nookala, Supraja;Tollamadugu, Naga Venkata Krishna Vara Prasad;Thimmavajjula, Giridhara Krishna;Ernest, David
    • Advances in nano research
    • /
    • 제3권2호
    • /
    • pp.97-109
    • /
    • 2015
  • Citrate ion is a commonly used reductant in metal colloid synthesis, undergoes strong surface interaction with silver nanocrystallites. The slow crystal growth observed as a result of the interaction between the silver surface and the citrate ion makes this reduction process unique compared to other chemical and radiolytic synthetic methods. The antimicrobial effects of silver (Ag) ion or salts are well known, but the effects of citrate coated Ag nanoparticles (CAgNPs) are scant. Herein, we have isolated biofilm causative bacteria and fungi from drinking water PVC pipe lines. Stable CAgNPs were prepared and the formation of CAgNPs was confirmed by UV-visible spectroscopic analysis and recorded the localized surface plasmon resonance of CAgNPs at 430 nm. Fourier transform infrared spectroscopic analysis revealed C=O and O-H bending vibrations due to organic capping of silver responsible for the reduction and stabilization of the CAgNPs. X-ray diffraction micrograph indicated the face centered cubic structure of the formed CAgNPs, and morphological studies including size (average size 50 nm) were carried out using transmission electron microscopy. The hydrodynamic diameter (60.7 nm) and zeta potential (-27.6 mV) were measured using the dynamic light scattering technique. The antimicrobial activity of CAgNPs was evaluated (in vitro) against the isolated fungi, Gram-negative and Gram-positive bacteria using disc diffusion method and results revealed that CAgNPs with 170ppm concentration are having significant antimicrobial effects against an array of microbes tested.

목장형 유가공장의 미생물 분석 및 저감기술 적용 평가 (Evaluation of Microbial Analysis and Application of Reduction Technology in a Dairy Factory)

  • 김종희;이은선;김부민;함준상;오미화
    • Journal of Dairy Science and Biotechnology
    • /
    • 제41권4호
    • /
    • pp.203-210
    • /
    • 2023
  • Bacterial contamination negatively affects the quality, functionality, and safety of dairy products. Adherent populations of bacteria, referred to as biofilms, grow on the surfaces of dairy processing equipment and are the primary cause of dairy contamination. In addition, microorganisms present in the farm environment and dairy factory can contaminate the Clear-In-Place (CIP) line through raw milk transport pipes; therefore, exhaustive management is required. In dairy manufacturing facilities, biofilm formation is controlled using CIP systems that primarily require sodium hydroxide and nitric acid. However, the leakage or incomplete removal of these potently active compounds can be harmful to humans. In the present study, we compared the eradication of Escherichia coli and other bacteria using commercially available combinations of sodium hypochlorite (NaClO) and citric acid, which are recognized by the Korean Ministry of Food and Drug Safety (MFDS) as food disinfectants. When considered in the CIP system of the field manufacturing process, E. coli was not detected (compared to detection before treatment), and other bacteria were detected at 0-32 culture-forming units (CFU)/cm2. The residual amount of chlorine ions after CIP treatment was similar to that in tap water, and there was no significant difference in the overall components of the fermented dairy products. Therefore, the NaClO/citric acid CIP system can be safely applied in dairy manufacturing processes.