• 대한토목학회논문집
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• 제11권1호
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• pp.189-196
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• 1991

본(本) 연구(硏究)에서는 침지형(浸漬型) 생물막(生物膜) 반응조(反應槽)에서 온도(溫度)의 변화(變化)가 미생물(微生物) 성상(性狀)과 처리효율(處理効率)에 미치는 영향(影響)을 구명(究明)하였다. 침지형(沈漬型) 생물막(生物膜) 반응조(反應槽)에서 온도와 매체충전율(媒體充塡率)을 변화시켜 얻어진 연구결과를 요약(要約)하면 다음과 같다. 1. 생물막(生物膜) 밀도(密度), 부착미생물량(附着微生物量), 생물막(生物膜)두께는 온도(溫度)와 매체충전량(媒體充塡量)의 변화에 상당한 영향을 받는다. 2. 반응조 내의 총(總) 미생물(微生物) 중 부유미생물(浮遊微生物)이 차지하는 비율은 약 10-50%로 부유미생물(浮遊微生物)이 기질제거(基質除去)에 관여하는 역할을 무시할 수 없음이 입증되었다. 3. 온도와 총 미생물농도에 따른 BOD 제거효율(除去効率)을 나타내는 관계식을 유도할 수 있었다. 4. 본 공법(工法)은 온도변화에 강(強)한 편으로, Van't Hoff-Arrhenius 변형식(變形式)을 이용하여 구(求)한 온도보정계수(溫度補正係數)는 1.042이었다.

• 상하수도학회지
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• 제10권1호
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• pp.112-120
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• 1996

In this study, the porous glass media was utilized as biomass carrier, and the optimum characteristics of this new media in fixed bed biofilm process were investigated. The characteristics of media considered here are a void volume fraction, a specific surface area, and surface characteristics of media. The effect of surface roughness and material could be clearly demonstrated by the fact that the porous glass media showed a good potential for biofilm development. This might results from the fact that biofilm is initially formed in the surface cavities of the media is protect from the shear effect. Therefore, the microcolonies are not readily detached by the fluid shear. In the steady state, biofilm formation along the packing bed depth was different from media to media. The specific area was also an important factor for the attachment of microorganism on the media surface. The specific area was also an important factor for the attachment of microorganism on the media surface. In the case of porous glass media, about $100m^2/m^3$ was enough to obtain a good organic removal efficiency The organic removal efficiency could be improved by increasing the void volume fraction in the reactor, at least 80% was required to obtain a high removal efficiency and prevent clogging. From the analysis of kinetics study, the yield coefficient, Y, was 0.42 mgMLSS/mgSBOD, endogenous respiration coefficient, ke, was $0.12day^{-1}$ and substrate removel coefficient of Mckinney. km, was $16.8hr^{-1}$ for the porous glass media G-2

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2001년도 추계학술발표대회
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• pp.282-285
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• 2001

질산화 생물여과 시스템 내 생물막 안에 존재하는 ammonia oxidizers 및 nitrite oxidizers의 군집 구조 및 공간적 분포를 조사하였다. FISH 분석 결과 생물막 내 숫적으로 우점종을 이루는 미생물은 ammonia oxidizer인 Nitrosomonas spp.로 나타났으며 nitrite oxidizer 인 Nilrospira spp.에 비해 3 ${\sim}$ 5 정도 더 많이 존재하였다. 이는 실협 기간동안 완전한 질산화를 보였지만 반응기가 2 년 이상 nitrite 축적을 위해 높은 free ammonia 농도 빛 낮은 용존 산소 상태에서 운선되어 nitrite oxidizers에 저해를 주었기 때문인 것으로 사료된다. FISH와 결합된 CLSM 관찰 결과 생물막 전체에 걸쳐 ammonia oxidizer가 분포하는 반면 안쪽으로 갈수록 nitrite oxidizers가 분포함을 보였다. 이는 폐수의 ammonium 을 생물막 내 ammon ia oxidizer가 먼저 nitrite로 산화시키고 이를 nitrite oxidizers가 곧바로 nitrate로 산화시키기 때문이다.

• 한국환경보건학회지
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• 제21권2호
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• pp.20-26
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• 1995

The objective of this study is to estimate the effect of the bed expansion and the characteristics of attached biomass in the start-up in the anaerobic fluidized bed reactor(AFBR). The fluidized bed reactor was operated with bacteria supported on the bed of granular activated carbon(GAC). The reactor was operated at 35$\circ$C, 5 kg $COD/m^3\cdot day$ at bed expansion varying from 0 to 100% with soluble glucose wastewater(5,000 mg/l). When the effluent reached a steady state at 100% of bed expansion, maximum COD removal efficiency of 87.3% and 0.031 $m^3CH_4/kg COD_{removed}$ were obtained. At higher bed expansion, COD removal efficiency, methane production rate and biogas production rate increased. Especially, at 50% of bed expansion, the efficiency of the treatment increasedg rapidly in the AFBR. The biomass colonized in the pits and crevices of the GAC particle and no complete biofilm was established in the bioreactor during the experiment.

• 한국환경보건학회지
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• 제22권1호
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• pp.82-90
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• 1996

The objectives of this study were to examine the start-up method and characteristics of biomass attachment on the media in an anaerobic fluidized bed reactor(AFBR). The media adopted was the granular activated carbon which was successfully capable of adsorbing organics and biomass. The reactor was operated at 5 kg $COD/m^3\cdot day$ and 24hr of HRT. There were important problems in the AFBR's start-up, which has been reported very long and unstable. Therefore, this research was to solve the problem of the start-up and it was performed, comparing two start-up ways that were initial fluidized system and initial static-fluidized system. The results were summarized as follows: (1) On the whole initial static-fluidized system was superior to initial fluidized system in the aspects of biogas production rate, methane content and COD removal efficiency etc. (2) At the steady state methane production rate and recoverable bioenergy of initial static-fluidized system were $2.074 m^3CH_4/m^3\cdot day$, $0.488 m^3CH_4/kgCOD_{removed}\cdot day$, and 81.3kcal/day, respectively. (3) Thickness of biofilm was about $5.11 \mu m$, $\rho_{bw}$ and $\rho_{bd}$ were $1.022 g/cm^3, 0.0953g/cm^3$ respectively. (4) Biomass concentration of fluidized state was about 35 mg/g GAC. In conclusion the efficient method on the start-up of the AFBR using GAC as media was initial static-fluidized system and the period of static state needed to reach steady state was considered about twenty days.

• 한국물환경학회지
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• 제20권5호
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• pp.457-465
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• 2004

The objective of this study is to evaluate the possibility to apply the Moving Bed Biofilm Reactor(MBBR) in the activated sludge treatment process with existing aerobic HRT. Optimal operation conditions were assumed according to the analysis of organic matter and nutrients removal efficiencies depending on loading variations. The process was operated under different conditions: RUN I(HRT=7.14hr, $I{\cdot}R=100%$), RUN II(HRT=6.22hr, $I{\cdot}R=100%$), RUN III(HRT=6.22 hr, $I{\cdot}R=150%$), RUN IV(HRT=6.22hr, $I{\cdot}R=200%$), the TBOD removal efficien cies are 88%, 88.5%, 94.6%, 97.6%, respectively. Overall TSS removal efficiency is 90%, and it is increasing in RUN IV. In the case of Nitrogen, the highest removal efficiency of 90% was observed in RUN III and RUN IV, Nitrification and Denitrification rates are 0.013-0.016kg $NH_3-N/kg$ Mv-d and 0.009-0.019kg $NO_3/kg$ Mv-d, respectively. Phosphorus removal efficiencies are 89.6% in RUN I, 91.5% in RUN II, 84.3% in RUN III, and 76.4% in RUN IV. The process under shorter SRT yields better performance in terms of phosphorus removal. It was noticed that to achieve the effluent phosphorus concentration ofless than 1mg/L and removal efficiency higher than 80%, SRT should not be longer than 10 days. Experimental result shows that HRT of 6.22 hours is suitable for this treatment process, and, as a result, the aerobic reactor including moving media and DO depletion tank have a sufficient effect to the process performance.

• 생명과학회지
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• 제13권6호
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• pp.970-975
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• 2003

생촉매 및 생물막 반응기를 이용한 TCE 생분해는 TCE를 무해한 최종산물로 처리할 수 있는 환경친화적 방법이며, 초기 시설비와 운영비도 낮아 경제성도 우수한 기술로 평가할 수 있다. 그러나, TCE 및 독성 분해산물로 인하여 생촉매 불활성화가 일어나서 장기간 안정된 반응기 운전이 어렵고, TCE와 성장기질사이의 경쟁적 저해로 인하여 처리효율이 저하된다는 단점이 있다. 이러한 문제점을 극복하기 위하여 TCE 처리 단계와 생촉매 재활성화 단계를 구분시킨 2단계 CSTR/TBF 시스템에 대하여 TCE 연속처리용 시스템으로써의 실규모 적용 가능성을 평가해 보았다. B. cepacia 및 M. trichosporium을 생촉매로 사용한 2단계 CSTR/TBF 시스템은 고농도 유입 TCE와 다양한 운전조건에서도 28∼525mg TCE/1$.$day수준의 높은 TCE 처리효율을 안정되게 유지할 수 있어 산업폐가스 처리를 위한 실규모 처리 시스템으로 적용 가능성이 높다고 평가할 수 있었다.

• 한국환경과학회지
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• 제4권3호
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• pp.69-69
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• 1995

• 산업기술연구
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• 제26권B호
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• pp.3-10
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• 2006

In this study, the of MBBR(moving bed biofilm reactor) process for Phosphorus Removal efficiency depending on seasons and the factors affecting phosphorus removal efficiency in the process is evaluated. As a result of experiment, T-P removal efficiency has its highest value in winter, (80.8%). and T-P removal efficiency has its lowest value in autumn, (49%). Optimum SRT for Phosphorus Removal revealed is about 8.8 days and process performs more efficiently as the temperature decreases. It is accepted that nitrate to anaerobic zone is affecting the Phosphorus removal process. With increasing the organic loading rate, Phosphorus removal efficiency also increases. Also, an experiment has been conducted to find out the highest efficiency according to Media existence and it has revealed that Media addition provides better phosphate removal.

• KSBB Journal
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• 제27권3호
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• pp.145-150
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• 2012

This study was accomplished using packed bed column reactors that contain nonsurface-modified polypropylene media and surface-modified media from hydrophobic surface property into hydrophilic property by ion beam irradiation. The objectives of this research was investigated the characteristics of organic compounds removal and microbe attachment from sewage of school cafeteria in these reactors. In 736.8 mg/L of the average inflow $COD_{Cr}$ concentration the reactors with and without surface modification showed 81.8% and 70.3% of average $COD_{Cr}$ removal efficiencies, respectively, which proves the $COD_{Cr}$ removal efficiency of surface-modified media reactor is higher than that of nonsurface-modified media reactor. After 90 days, there were maximum differences between modified system and non-modified system. In that time the maximum removal efficiency of $COD_{Cr}$ was 96.5% in modified system and was 85.2% in non-modified system that showed removal efficiency of surface-modified media system is 11.3% higher than that of nonsurface-modified media system. The average removal efficiency of SS was 80.4% for the surface modified system and 61.6% for the non-modified system under same condition. Also, the reactor of surface-modified media has advantage on microbe attachment and biofilm formation.