• Title/Summary/Keyword: 활성슬러지법

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Cost Analysis of Ocean Outfall and Tertiary Treatment Processes in Suyong Sewage Treatment Plant (수영 하수처리장 방류수의 해중 방류법과 3차 처리시설 설치시 비용 비교 분석)

  • 박해식;조은일;박청길
    • Journal of Environmental Science International
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    • v.8 no.1
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    • pp.115-123
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    • 1999
  • Sewage has been almost treated by secondary treatment process. Secondary-treated effluent of sewage treatment plant caused the pollution of nearby beach. Nitrogen(N) and Phosphorus(P) in effluent water have caused many problems on estuary, such as red tide, eutrophication and aquatic toxicity. Therefore, the effective nitrogen and phosphorus removal from sewage treatment plants is necessary to prevent those pollution problems. However, little sewage treatment plant in Korea is effectively being operated for the removal of the nutrients. This study is analyzed for the effectiveness of cost when tertiary treatment process and Ocean Outfall are applied for the water quality of Suyong Bay After secondary treatment process, the effluent was discharged from the seabed in the depth of 32m of 4000m offshore. Pollutant concentration is decreased as much as the 180 times after the result of initial dilution, so that environmental protection requirement of Suyong Bay can satisfied. This Ocean Outfall process can save the 2.6~3.5 times as much as the cost of construction and operation for tertiary treatment process running over a 20 year.

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Advanced Treatment of Sewage and Wastewater Using an Integrated Membrane Separation by Porous Electrode-typed Electrolysis (분리막/다공 전극형 전기분해 조합공정을 이용한 하.폐수의 고도처리)

  • Choi, Yong-Jin;Lee, Kwang-Hyun
    • Membrane Journal
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    • v.22 no.2
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    • pp.95-103
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    • 2012
  • To treat nitrate and non-biodegradable organics effectively in sewage, industrial wastewater and livestock wastewater, the activated sludge process integrated by a membrane separation and a porous electrode- electrolysis was proposed and its efficiency was investigated. The proposed system was consisted of 3 processes; activated sludge, membrane filtration and electrolysis. In the study, the membrane filtration played a role in reducing the load of the electrolysis to operate the proposed process stably. The electrolysis consisted of a porous electrode to increase the efficiency due to the extension of the specific surface area. Additionally, redox reaction in the electrolysis was induced by decomposing influent water as current was applied. As a result, hydrogen free radicals and oxygen radicals as intermediates were produced and they acted as oxidants to play a role in decomposing non-degradable organics. It was environmentally-friendly process because intermediates produced by porous electrode were used to treat waste matters without supplying external reagent. Experimental data showed that the proposed process was more excellent than activated sludge process. SS removal efficiencies of the proposed process, membrane filtration and activated sludge process were about 100%, about 100% and about 90%, respectively. COD removal efficiencies of the proposed system, membrane filtration and activated sludge process were about 92%, about 84% and about 78%, respectively. T-N removal efficiencies of the proposed system, membrane filtration and activated sludge process were about 88%, about 67%, and about 58%, respectively. The SS data showed that SS was efficiently removed in the single of the membrane filtration. The COD/T-N data showed that COD/T-N of membrane hybrid process was treated by removing a little soluble organics and SS, and that COD/T-N of electrolysis hybrid process was treated by oxidize organics with high removal rate.

호흡율 측정기를 이용한 폐수처리 공정수의 생물학적 활성측정

  • Lee, Yeong-Rak;Lee, Gi-Yong;Im, Ji-Hun;Lee, Sang-Hun;Mun, Hong-Man;Lee, Jin-Won
    • 한국생물공학회:학술대회논문집
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    • 2000.11a
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    • pp.463-466
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    • 2000
  • In this study, it was observed to oxygen uptake rate(OUR) on microbes in activated sludge process. OUR was showed to 43, 55, and $64\;mgO_2/L/hr$ when inoculated microbes mass were 3, 5, and 10%(v/v%). In additon to oxygen was consumed to $4{\sim}42\;mgO_2/L/hr$ as changed substrate concentration. Also, we were measured kinetics coefficient in order to know growth tendency. It was concluded to maximum growth rate$(\;{\mu}\;_{max})$, $2.7\;day^{-1}$, yield coefficient, 0.655, and half-velocity coefficient, 36.11 mg/L.

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연구논문 - "고온성 종균제를 이용한 제지폐수처리에 대한 연구(1)"

  • Lee, Seong-Ho
    • Environmental engineer
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    • s.323
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    • pp.22-27
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    • 2013
  • 종이 펄프 공장의 폐수는 다른 공업에 비해서 폐수량이 많고 오염도가 높다. 목재로부터 종이를 제조하는 경우에 수율은 종이의 종류와 제법에 의해 큰 차이가 있어서 한마디로 말하기는 어렵지만 평균 50~70%로 보는 경우, 목재 성분의 30~50%는 용해 또는 SS의 상태로 폐수중에 존재하기 때문에, 이들이 직접 하천이나 바다에 방류되면 오염의 원인이 된다. 그 때문에 각 공장에서는 목재자원의 종합적인 이용의 입장으로서 제품의 수율을 좋게 하고 동시에 폐수의 양을 감소시키고 폐수에서 유용한 자원을 회수하거나 증해약품의 회수 등을 위하여 연구 및 노력을 계속하고 있는 것이 현 상태이다. 우리 나라의 거의 모든 제지회사에서는 물리적, 화학적 처리법과 생물학적 처리법 중 호기성 처리방법이 주 처리방법으로 사용되고 있으며 탈묵 폐수나 리그닌을 다량 함유하는 폐수의 경우에는 혐기성 처리방법을 이용하기도 한다. 본 실험에서는 우유팩을 재생하여 화장지 제조의 원료로 이용하는 G제지공장의 폐수를 이용하였고, 공장의 원폐수를 부상법으로 1차 처리한 처리수를 실험실로 운반하여 활성슬러지법으로 실험하였다. 처리효율의 영향인자인 HRT를 G제지공장에 맞추어 12시간으로 조정하고 적절한 F/M비(0.23)를 위해 COD와 MLSS가 유지된 후부터 실험을 시작했다. $20^{\circ}C{\sim}560^{\circ}C$까지 $10^{\circ}C$간격으로 온도를 변화시키면서 미생물의 상태변화를 관찰하고, 또한 각 용도에서의 처리수질을 비교해 보았다. 실험조건은 pH는 중성상태(6.5~7.5), DO는 $2{\sim}4mg/{\ell}$, 영양원은 BOD : N : P = 100 : 5 : 1로 맞추고 BOD, COD, SS, SVI를 측정하였으며, 현미경을 통하여 미생물과 Floc를 관찰하였다. $20^{\circ}C$부터 종균제를 초기 운전시 $200mg/{\ell}$ (분말상)을 폭기조에 투여하고 매일 $200mg/{\ell}$를 정기적으로 투입하여 온도변화에 따른 미생물의 상태 및 처리수질을 비교해보았다. 특히 종균제로는 기존의 G제G지공장에서 사용하는 신일 미생물(Bio sound S)종균제와 청림C&C의 종균제(Cell bio P)를 비교 관찰하였다. 고온성 종균제를 두배 투입하여 투입량에 대한 처리효율을 비교하였으며 종균제를 사용하지 않고 운용함으로써 그 차이도 비교할 수 있었다.

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Treatment of dyeing wastewater using Moving Bed Bioractor (부유메디아 생물막 공정을 이용한 염색폐수처리)

  • Shin, Dong-Hoon;Lee, Sang-Hun;Ryu, Seung-Han;Park, Jun-Hyung;Jo, Seog-Jin
    • Proceedings of the Korean Society of Dyers and Finishers Conference
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    • 2011.03a
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    • pp.110-110
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    • 2011
  • 염색공업 폐수는 그 성분이 일반적으로 매우 복잡하며, 작업공정의 가동 사항에 따라 수질 변동이 큰것이 특징으로, 각 공정에서 배출되는 염료, 보조화학물질, PVA(Polyvinyl alchol), 전분, wax 등이 포함되어 있으며 pH가 높고, 색도로 인해 하천에 방류될 경우 확산성이 높아 미생물에 의한 자정작용을 방해하여 하천의 수중생태계를 파괴할 우려가 있다. 이러한 염색산업에서 발생하는 폐수는 일반적으로 응집침전, 부상분리법 등의 전처리한 후 활성오니공정으로 처리하는 방법이 널리 이용되고 있으나, 이들 처리공정으로는 폐수 속에 포함되어 있는 다양한화학적 구조의 색소성분 및 유해물질을 완벽하게 제거하는 것이 어려운 실정이다. 유기물 함량이 높은 염색폐수를 처리하기 위해 제안된 기술로는 산소활성슬러지법, 유동상 및 고정상 생물막법, 포괄고정화법 등이 있다. 이러한 기술들중 기존의 처리공정을 증축없이도 처리효율을 높일 수 있는 방법으로 담체를 이용한 부유메디아 생물막공정(Moving-Bed BioReactor, MBBR)이 있다. 이공정은 미생물이 부착, 성장할 수 있는 공극율과 비표면적이 큰 담체를 이용하므로 반응조내의 부유 미생물 뿐만 아니라 담체에 고농도로 부착된 부착 미생물에 의해서도 유기물을 제거하기 때문에 다른 공정들에 비해 처리효율이 뛰어나고 기존의 활성슬러지 공정에 비해 갑작스러운 부하변동 및 유독성 폐수유입에 대해서도 안정적으로 운전이 가능한 장점이 있다. 본연구에서는 부유메디아 생물반응기(Moving-Bed BioReactor, MBBR)을 이용하여 염색폐수내 $COD_{Mn}$, 색도 및 난분해성 물질인 PVA 저감에 대한 Lab-scale test 수행하였다. 실험에 사용된 염색폐수의 수질은 평균 pH 13, $COD_{Mn}$ 900 mg/L, SS 135 mg/L, 색도 1,134 [C.U.], PVA 593 mg/L였으며, 2L의 반응기를 사용하여 회분식 실험을 수행였다. 본 실험에서는 호기성 미생물에 의한 염색폐수의 생분해가 유지되는데 필요한 최적의 용존산소 농도와 이에 필요한 공기 폭기량을 결정하기 위하여 i) DO uptake rate측정과 ii) 담체의 충진율, iii) COD/N ratio, iv) Air 유량, v) 담체내 흡착제의 종류, vi) $Ca^{2+}$ 첨가가 염색폐수의 생분해에 미치는 영향을 살펴보았다. 운전시간을 7일로 하여 COD, 색도, PVA 등을 측정한 결과 담체를 첨가한 경우가 담체를 첨가하지 않은 경우 보다 제거효율이 뛰어났다. 특히 충진율 30%(C/N 3)의 경우에서 COD, 색도, PVA의 제거율이 각각 평균 65%, 70%, 60%로 가장 높은 제거효율을 나타내었다.

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Synthesis of Butenes through Butanol Dehydration over Catalyst Prepared from Water Treatment Sludge (정수 슬러지로부터 제조된 촉매 상에서 부탄올 탈수반응을 통한 부텐 제조)

  • Kim, Goun;Bae, Junghyun;Choi, Hyeonhee;Lee, Choul-Ho;Jeon, Jong-Ki
    • Korean Chemical Engineering Research
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    • v.53 no.1
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    • pp.121-126
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    • 2015
  • The objective of this study is to evaluate the catalytic potential of the porous material prepared from water treatment sludge. The textural properties of the catalyst were studied using $N_2$ adsorption and desorption isotherms, scanning electron microscope, and X-ray diffraction. The pellet-type catalyst prepared using water treatment sludge is determined to be a material that contains mesopores as well as micropores. The specific surface area of the catalyst is $157m^2/g$. Acidic characteristics of the catalyst are analyzed by temperature-programmed desorption of ammonia and infrared spectroscopy of adsorbed pyridine. 2-Butanol dehydration reaction was carried out in a fixed bed catalytic reactor. Yields of 1-butene, trans-2-butene, and cis-2-butene at $350^{\circ}C$ were 25.6 wt%, 19.2 wt%, and 29.9 wt%, respectively. This catalytic activity of the catalyst based on water treatment sludge in 2-butanol dehydration is due to the acid sites composed of Bronsted acid sites and Lewis acid sites. It was confirmed that the catalyst based on water treatment sludge can be utilized to produce $C_4$ olefin through butanol dehydration.

Intracellular Concentrations of NAD(P), NAD(P)H, and ATP in a Simulated Oxic-settling-anaerobic (OSA) Process (OSA 공정의 세포 내 ATP, NAD(H), NADP(H) 농도)

  • Ventura, Jey-R Sabado;Nam, Ji-Hyun;Yang, Benqin;Na, Ri;Kil, Hyejin;Nam, Deok-Hyeon;Kang, Ki-Hoon;Jahng, Deokjin
    • Journal of Korean Society on Water Environment
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    • v.31 no.6
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    • pp.599-609
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    • 2015
  • In order to investigate why OSA (oxic-settling-anaerobic) process produces less sludge than CAS (conventional activated sludge) process, sequential cultivation through 1st aerobic-anaerobic-2nd aerobic conditions, were carried out. Then, the intracellular concentrations of adenosine triphosphate (ATP), nicotinamide adenine dinucleotide (NAD and NADH), and nicotinamide adenine dinucleotide phosphate (NADP and NADPH) were monitored for these three stages. Results showed that the concentrations of these energy substances rapidly decreased through time in both aerobic and anaerobic conditions but the anaerobic culture contained the lower energy level than aerobic culture. The 2nd aerobic culture that experienced anaerobic condition showed lower concentration of these energy substances than those of the 1st aerobic culture. Meanwhile, the anaerobic culture corresponding to the sludge holding stage of OSA was subjected to different soluble chemical oxygen demand (SCOD) levels, detention time, and temperature to evaluate the effects of these variations on the energy level difference between the 1st and 2nd aerobic stages. The lower the SCOD concentration, the longer detention time; and the higher temperature in the anaerobic stage tended to further reduce the intracellular level of the 2nd aerobic culture. On the average, the intracellular energy level of the anaerobic and 2nd aerobic stage were 57.73% and 39.12% of the 1st aerobic culture, respectively. These indicated that the insertion of an anaerobic stage between two aerobic stages could lower the intracellular energy levels, hence the lower the sludge in OSA than CAS process. Moreover, manipulation of the operating conditions of the intervening anaerobic stage can change intracellular energy levels thereby controlling sludge production.

전자선 전처리 방법을 이용한 염색폐수내 난분해성 물질의 제거

  • Yu, Dae-Hyeon;Park, Chi-Gyun;Lee, Jae-Gwang;Lee, Byeong-Jin;Lee, Myeon-Ju;Choe, Jang-Seung;Han, Beom-Su
    • Proceedings of the Korean Environmental Sciences Society Conference
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    • 2005.05a
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    • pp.370-372
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    • 2005
  • 본 연구는 전자선을 이용하여 염색폐수에 함유되어 있는 난분해성 물질을 생물학적으로 분해가 용이한 물질로 전환시키는 한편 전환되어진 물질을 표준 활성슬러지법을 이용하여 생물학적 처리함으로 처리효율을 극대화 하는 전자선이용 염색폐수 정화기술을 개발하기위해 수행하였다. 종합 염색폐수에 1 kGy의 전자선 전처리를 한 후 생물학적 처리를 연계하였을 때 0.1 이상의 생분해도 증가를 나타냈으며 오염부하량 변화에 따른 미생물 활동도역시 안정적이었다. 또한 물벼룩을 이용한 생태독성 평가에서도 2.49의 원폐수 독성이 2.16이하로 감소함을 확인하였다. 난분해성 물질에 대한 전자선 전처리의 효과를 확인하기 위하여 대표적인 난분해성 물질인 TPA 인공폐수를 대상으로 전자선 가속기 전처리한 결과40 % 이상 처리효과를 얻을 수 있었다. 이러한 결과로 보아 전자선 전처리와 생물학적 처리공정의 연계로 보다 효과적인 염색폐수의 처리가 가능할 것으로 사료된다.

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The Treatment of Concentrated Organic Alcoholic Distillery Wastewater by the Fluidized-Bed Biofilm Reactor (생물막 유동층 반응기에 의한 주정공장의 고농도 유기성 폐수처리)

  • 김동석;장희재
    • KSBB Journal
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    • v.6 no.4
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    • pp.345-350
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    • 1991
  • The purpose of this study is to investigate biomass characteristics and organic removal efficiency by changing superficial upflow velocity and organic loading rate in treating alcoholic distillery wastewater. Since the biomass concentration and the thickness of biofilm are very sensitive to superficial upflow velocity, a high concentration of biomass could be achieved by decreasing superficial upflow velocity that lowered the organic removal efficiency. Therefore, superficial upflow velocity should be controlled as to give optimum conditions and removal efficiency. Generally, activated sludge system shows 70% COD removal efficiency at$1.5kgCOD/m^3{\cdot}day$, but the fluidized-bed biofllm reactor shows 80% COD removal efficiency even at 6kgCOD/$m^2{\cdot}day$.

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Removal of Nitrogen and Phosphorus by Activated Sludge Process Combined with Aluminum Corrosion (알루미늄 부식을 적용한 활성슬러지법에서 질소 및 인 제거)

  • Choi Hyung Il;Cheong Kyung Hoon;Park Sang Il;Paik Ke Jin
    • Journal of Environmental Health Sciences
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    • v.31 no.2 s.83
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    • pp.172-178
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    • 2005
  • A laboratory experiment was performed to investigate simultaneous removal of phosphorus and nitrogen from raw sewage by intermittently aerated activated sludge process packed with aluminum and silver plate. Two continuous experimental process, i.e. an intermittently aerated activated sludge process, and an intermittently aerated activated sludge process with an aluminum and silver plate packed into the reactor were compared. The pitting corrosion of aluminum does not affect the performance of the biological treatment. The amounts of Al eluted from aluminum plate 17 mg to 60.6 mg in this experimental conditions, and Al/P mole ratio were from 3.31 to 11.25. The total nitrogen removal efficiency in Run E were $60.6\%$ at the HRT of 12 hours. The effluent $PO_4-P$ concentration as low as $1.0\;mg/\iota$ could have been obtained during the continuous experiment in Run E at HRT of 12 hours.