• KSBB Journal
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• 제28권2호
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• pp.80-85
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• 2013

The bacterial community structure in a biological reactor fed influent from a wastewater treatment system was investigated by denaturing gradient gel electrophoresis (DGGE) and in situ hybridization. Sludges were collected from three biological reactors (aerobic, oxic, and anoxic tanks) at the M wastewater treatment facility (WTF). The influent of the MWTF consisted of mixed tannery wastewater (40~65%) and seafood wastewater (35~60%). The treatment processes resulted in a removal efficiency for BOD (biochemical oxygen demand) and COD (chemical oxygen demand) of 83.6~98.2% and 72.8~84.6%, respectively for tannery wastewater than for seafood wastewater resulted in greater survival of biomass in the biological reactors and a higher removal of BOD, COD, and T-N of about 8~18%. In contrast, addition of greater amounts of seafood wastewater decreased the amount of biomass in the bioreactors due to the increasing concentration of chromium from that wastewater and it also. The dominant bacterial species during the high seafood wastewater input period were Burkholderia cepacia (JX901049) and an uncultured bacterium (JF247555), while Pseudomonas geniculata (HQ256559) was dominant during the high tannery wastewater input period. Flavobacteriumsp. BF.107 (FM173271) and Hyphomicrobium zavarzinii (Y14306) were dominant under anoxic conditions.

• 한국물환경학회지
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• 제27권5호
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• pp.646-653
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• 2011

The combined system of sequencing batch biofilm reactor (SBBR) and membrane SBR (MSBR) was operated with sewage to evaluate the COD utilization for biological nutrient removal (BNR). The SBBR was operated for nitrification reactor, while denitrifying PAO (dPAO) was cultivated in MSBR with anaerobic-anoxic operation. In the SBBR and MSBR system, the enhanced biological phosphorus removal (EBPR) was successfully achieved with higher N removal. The COD utilization in combined SBBR-MSBR system was significantly reduced compared to ordinary BNR (up to 3.1 g SCOD/g (N+P) and 1.6 g SCOD/g (N+P) with different C/N/P ratio). The results suggest that a dPAO process could effectively reduce carbon energy (=COD) requirement. The combination of oxic-SBBR and anaerobic-anoxic MSBR for dPAO utilization could be an attractive alternative to upgrade the process performance in weak sewage.

• 한국해양환경ㆍ에너지학회지
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• 제9권1호
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• pp.14-20
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• 2006

수산물 가공공장 폐수의 생물학적 처리를 위하여 미생물 강제포획방식인 EMMC 공정을 적용하여 유기물 및 질소의 동시제거 가능성을 평가하였다. 처리도 실험은 도시하수처리장에서 가져온 활성슬러지를 cellulose triacetate를 이용한 gel matrix에 고정시켜 실험을 수행하였다. anoxic조와 oxic조로 구성된 시스템에 유기물 및 질소부하 율을 증가시켜가며 실험한 결과 비교적 안정된 형태의 운전이 가능하였다. 적용 유기물부하는 $0.65{\sim}1.72kgCOD/m^3{\cdot}d$, 총질소 부하는 $0.119{\sim}1.317kgT-N/m^3{\cdot}d$의 범위에서 4단계로 나누어 적용시켰다. 본 연구에 사용한 수산물 가공공장폐수의 경우 공장폐수의 유출수 총질소 농도 규제치인 60 mg/l 이하를 기준으로할 때 T-N의 경우 한계 적용용적부하는 약 $0.3kgT-N/m^3{\cdot}d$인 것으로 나타났다. T-N의 경우는 부하율 증가에 따른 제거효율 저하가 뚜렷하였으나 ${NH_4}^+-N$의 경우는 각 단계별로 부하율을 증가시키면서 실험해본 결과 부하율 증가에도 불구하고 제거 효율 변화는 완만하여 본 실험에 적용한 시스템의 경우 질산화 반응은 부하변동에 관계없이 효율적으로 이루어지는 것으로 평가되었다. 실험 기간 중 Anoxic조의 질산성 질소 제거율은 각 단계별로 평균 $99.51{\sim}98.62%$로 나타났으며 oxic조의 질산화 제거율은 $94.0{\sim}96.9%$로 나타났다. 시스템 전체로는 적용 용적부하율하에서 화학적 산소요구량(COD: Chemical Oxygen Demand)의 경우 $94.2%{\sim}96.6%$, 총질소의 경우 $73.4{\sim}83.4%$ 의 제거효율을 나타내었다.

• 대한환경공학회지
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• 제39권11호
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• pp.613-625
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• 2017

낚시터로 장기 임대중인 농업용 저수지 2곳을 대상으로 낚시터 영향권(effective zone) 2지점의 퇴적물과 비영향권(ineffective zone) 1지점의 퇴적물을 호기(oxic)와 무산소(anoxic) 조건을 조성한 실험실 코어배양법(laboratory core incubation)을 이용해 영양염류 용출시험을 2회씩 실시하였다. 용출 실험동안 상등수 내 DO, EC, pH, ORP의 변화는 낚시터 영향구간과 비영향 구간 사이에 유의할만한 차이는 관측되지 않았으며(p>0.05), 농업용 저수지의 퇴적물-심층수 확산경계면과 유사한 환경으로 조성되었다. 질산성 질소($NO_3{^-}-N$)를 제외하고 암모니아성 질소($NH_4{^+}-N$), 총인(T-P), 인산염 인($PO{_4}^{3-}-P$)이 호기 보다는 무산조 조건에서 통계학적으로 유의한 수준(p<0.05)으로 퇴적물에서 상등수로 더 많은 용출량이 측정되었다. 이는 상등수 내 DO 농도 감소에 따라 미생물 매개의 암모늄화가 촉진되고 질산화 작용이 억제되어 암모니아성 질소가 퇴적물에서 상등수로 확산 용출되고, 퇴적물 표층의 산화층이 환원되어 유기물에 결합된 인과 금속 산화물과 결합된 인의 해리 등을 통해 인산염인이 퇴적물에서 상등수로 확산용출이 가속화되었기 때문이다. 낚시터 영향권과 비영향권 사이 영양염류 용출량(benthic nutrient diffusive flux)값의 차이는 통계학적으로 유의하지 않았다(p>0.05). 따라서 농업용 저수지 내 낚시활동이 퇴적물의 영양염류 용출량을 통계학적으로 유의한 수준으로 증대시키지 않는 것으로 조사되었다. 이러한 결과는 농업용 저수지 설립년도 대비 10여년의 단기간 낚시활동으로 인해 퇴적물 오염 기여도가 비교적 낮고, 코어배양법의 속도제한된 확산(rate-limited diffusion)으로 발생한 것으로 판단된다. 호기와 무산소 조건 모두에서 퇴적물 내 영양염류 총량과 영양염류 용출량 사이에 유의적 상관관계가 도출되지 않았다. 따라서 농업용 저수지 수질오염의 가속화가 낚시활동으로 인한 직접적 원인보다는 유역에서 유입되는 다양한 비점오염원 내 영양염류가 주요 요인으로 판단되며, 영양염류의 용출을 저감하기 위해 포기 및 물순환 등을 통해 심층수의 빈산소화를 억제할 필요가 있다.

• 상하수도학회지
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• 제22권5호
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• pp.497-503
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• 2008

The Oxic-Settling-Anaerobic(OSA) process is a modified activated sludge processes for sludge reduction. It is evaluated that the sludge production in OSA process can decrease to 88% because of biomass decay and kinetic parameter($Y_H$ 0.237mgVSS/mgCOD, $b_H$ $0.195d^{-1}$) in anaerobic reactor, when compared with CAS process. However, it has problems caused by sludge reduction such as increase of nutrient loading. In case that the anoxic condition through the introduction of the intermittent aeration for the enhancement of nitrogen removal ability build up and enough rbCOD is suppled, maximum 88% of nitrogen is removed in the OSA process. If the OSA process optimizing the intermittent aeration cycle is applied to the separate sewage system with high rbCOD fraction, it can be converted to advanced process in terms of the sludge reduction and nitrogen removal, simultaneously.

• 한국축산시설환경학회지
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• 제14권2호
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• pp.113-118
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• 2008

Sequencing batch operation consists of fill, react, settle and decant phases in the same reactor. Operation consists of anaerobic, anoxic and oxic (aerobic) phases when nutrient removal from the wastewater is desired. Since the same reactor is used for biological oxidation (or mixing) and sedimentation in aerobic and anaerobic SBR operations, capital and operating costs are lower than conventional activated sludge process and conventional anaerobic digestion process, respectively. Therefore, Aerobic SBR and Anaerobic SBR operations may be more advantageous far treatment of small volume animal wastewater in rural areas.

• 한국응용과학기술학회지
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• 제22권1호
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• pp.62-70
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• 2005

Step-feed process for biological nitrogen removal were analyzed numerically for the each unit and final total nitrogen(TN) effluent by water quality management(WQM) model and the results were compared data from these wastewater treatment plants. No bugs and logic error were occurred during simulation work. All of the simulation results tried to two times were obtained and both results were almost same as this model has become good reappearance. It was concluded that most of nitrogen removal occurred in the first oxic tank. Thus the controlling of the first anoxic tank may be more important in term of nitrogen removal. Also each unit of simulation result was kept good relationship with that of measured data. Accordingly this WQM model has good reliance. Finally, WQM model can predict final TN effluent within ${\pm}6.0mg/{\ell}$.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 추계학술발표대회 및 bio-venture fair
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• pp.451-454
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• 2000

This study was carried out to investigate the effects of hydraulic backwash load and porous ceramic media on the biological nitrogen removal efficiencies of a biological aerated filter. An upflow anoxic-oxic biological aerated filter(AO-BAF) with porous ceramic media can remove nitrogen by nitrification and denitrification in single unit. After the AO-BAF backwash, nitrogen removal efficiency was lowest and gradually increased to the steady state. Nitrification efficiency, however, showed the opposite result. It is likely that the biofilms are exposed to aerobic condition as the excess biofilms were sloughed off by backwashing

• 환경위생공학
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• 제7권1호
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• pp.45-56
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• 1992

The Anaerbic Anoxic/oxic process is one of the biological treatment methods to remove nitrogen and phosphorus effectively which are nutritional elements for eutrophication. Supernatant of primary sediment of Anaerobic digester is used as a carbon source instead of methanol methanol supply in usual A$_{2}$/O process. The efficiency of the following treatment processes are as follow : 1) Changing recycle ratio in the usual A$_{2}$/O process without the stage of Anaerobic digester. 2) Changing recycle ratio in the usual A$_{2}$/O process with the supernatant supply of the Anaerobic digester. In the result of comparison, changing recycle ratio is almost no effect in the removal of phosphorus, however the effect of removal in nitrogenous substance are remarkable, and the effect of Anaerobic digester is not as effective as expected because the BOD removed in the digester partly, the rate of phosphorus to the BOD exceed pertinent range.

• Journal of Microbiology
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• 제45권3호
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• pp.205-212
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• 2007

Anoxygenic photosynthesis, performed primarily by anoxygenic photosynthetic bacteria (APB), has been supposed to arise on Earth more than 3 billion years ago. The long established APB are distributed in almost every corner where light can reach. However, the relationship between APB phylogeny and source environments has been largely unexplored. Here we retrieved the pufM sequences and related source information of 89 pufM containing species from the public database. Phylogenetic analysis revealed that horizontal gene transfer (HGT) most likely occurred within 11 out of a total 21 pufM subgroups, not only among species within the same class but also among species of different phyla or subphyla. A clear source environment feature related phylogenetic distribution pattern was observed, with all species from oxic habitats and those from anoxic habitats clustering into independent subgroups, respectively. HGT among ancient APB and subsequent long term evolution and adaptation to separated niches may have contributed to the coupling of environment and pufM phylogeny.