• 유기물자원화
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• 제14권1호
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• pp.151-159
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• 2006

런던협약의 영향으로 슬러지 처리의 중요성이 대두되고 있는 실정이므로 본 연구는 슬러지 처리에 대한 개선방안의 제시를 목적으로 유기성 폐수 및 하수처리장 슬러지를 대상으로 JAR test 및 교반장치를 부착한 침강 column을 이용하여 응집효율이 침강특성에 미치는 영향에 대한 실험을 실시하였으며 다음과 같은 결과를 얻었다. 최적의 침강효율을 얻기 위한 최소의 응집제 투여농도는 200mg/L의 경우로 나타났으며. 200mg/L 이상으로 PAC가 투여될 경우 각각의 임계슬러지 영역의 크기에서는 큰 변화가 없는 것으로 나타났다. 따라서 200mg/L로 투여되었을 때의 Clarification Rate(CR)은 임계슬러지 침강높이 비율이 0.4로 나타났으므로 CR = (Ho-Ht) / Ho = 1-0.4=0.6 로 산정되었다. MLSS농도가 높아질수록 슬러지 계면 침강속도는 감소하였으나 MLSS농도가 1,000mg/l 이상으로 증가하면 오히려 침강속도는 증가하는 것으로 나타났다. 이는 슬러지 농도가 1,000mg/l 이상으로 증가하게 되면 압밀침전영역으로 전이되어 상호작용에 의한 응집에 영향을 미치게 됨으로써 오히려 floc 형성에 긍정적인 영향을 미치기 때문이다. 슬러지 응집계면의 침강속도는 유기폐수 활성슬러지의 평균 침강속도 $4.25{\times}10^{-3}/min$보다 하수처리장 슬러지의 평균 침강속도가 $28.66{\times}10^{-3}/min$로 6.7배 높은 것으로 나타났다. 유기성 폐수 활성슬러지는 PAC의 투여량이 200mg/l 이하일 때는 침강속도 증가율보다 CR의 증가율이 더 컸으나 200mg/l 이상일 때는 CR의 증가율보다 침강속도 증가율이 더 커졌음을 알 수 있었다. 그러나 하수슬러지의 경우는 PAC 투여량이 증가함에 따라 CR의 변화율에는 차이가 적었으나 침강속도는 200m/l 이상일 때 차이가 급격히 증가하였다. 따라서 응집제 투여효과는 상등수의 SS제거율 효과보다는 MLSS의 침강속도에 더 큰 영향을 미치는 것을 알 수 있다.

• 한국환경과학회:학술대회논문집
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• 한국환경과학회 1999년도 임시총회 및 가을 학술발표회 초록집 The Korean Environmental Sciences Society
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• pp.61-62
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• 1999

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2001년도 추계학술발표대회
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• pp.533-536
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• 2001

본 연구는 제약폐수 처리에 있어서 폐수처리장내의 미생물 활성을 최대로 하여 운전효율을 높이는 것을 목적으로 하고 있다. 각 부하에 따른 영향을 살펴보고 각종 동력학 계수를 측정하여 실제 폐수처리 공정에 있어서 최적의 조건으로 운전할 수 있도록 하는 것이 목적인데, 이에 MLSS 부하, COD 부하에 따른 결과들을 구할 수 있었다. 반복실험을 통하여 더욱 정확한 동력학 계수를 측정할 수 있으리라 기대한다.

• 한국미생물·생명공학회지
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• 제23권6호
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• pp.763-769
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• 1995

As a mean to recover photosynthetic bacterial(PSB) cells and its practical uses in food industrial wastewater treatment, various biodegradable polyelectrolytes were first investigated for flocculation of suspended colloids in the PSB treatment process of soybean curd wastewater. Anionic polyelectrolytes such as sodium alginate and carrageenan were not effective but a cationic polyelectrolyte chitosan isolated from Portunus trituberclatus showed very effective flocculation activity. The concentration of chitosan, pH and temperature of wastewater for maximal flocculation were 40 mg/l, pH 7 and room temperature, respectively. Test using deacetylated chitosan to various degree showed higher flocculating activities in samples deacetylated over 75% and time for maximum flocculation was 40 min by stirring slowly under the above optimal conditions. Chitosan was not only effective to flocculate cells but also removed COD and MLSS of the wastewater. COD of 42% and MLSS of 87% were removed by addition of chitosan to the soybean curd wastewater treated with PSB.

• 한국환경보건학회지
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• 제33권6호
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• pp.493-496
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• 2007

The influences of contact time and ratio of food to microorganism (F/M) on uptake of wastewater organic matter in a short contact process were investigated using three activated sludge batch reactors fed with synthetic wastewater, sewage and livestock wastewater. About 64% of influent soluble chemical oxygen demand (SCOD) in the synthetic wastewater and 61% of SCOD in the sewage and 43% of SCOD in the diluted livestock wastewater were adsorbed into the activated sludge within 30 min. The specific mass of organic matter uptaken in the synthetic wastewater was 55 mg SCOD/g mixed liquor suspended solids (MLSS). In the same manner, 20 and 14 mg SCOD/g MLSS were calculated as the values in the sewage and livestock wastewater, respectively.

• 한국환경과학회:학술대회논문집
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• 한국환경과학회 2002년도 봄 학술발표대회 발표논문집
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• pp.249-250
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• 2002

• 상하수도학회지
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• 제19권1호
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• pp.25-30
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• 2005

In order to decrease the high costs of membrane process, we have tried to develop two alternatives to membrane; a cartridge type filter and a metal membrane were tested for the high permeation flux with low cost and low energy. This research mainly focused on three points; 1) operation with high permeation flux by using of a cartridge type filter and a metal membrane, 2) removals of the filterable organic materials (FOC) by pretreatments for the membrane fouling control, and 3) advanced wastewater treatment by SMBR process with intermittent aeration and high MLSS. An Intermittently aerated membrane bioreactor using a submerged micro filter (cartridge type) was applied in laboratory scale for the advanced wastewater treatment. To minimize membrane fouling, intermittent aeration was applied inside of the filter with $3.0kg_f/cm^2$. The experiments was conducted for 6 months with three different HRTs (8, 10, 12 hr) and high MLSS of 6,000 and 10,000mg/L. The filtration process could be operated up to 50 days with permeation flux of 500LMH. Regardless of the operating conditions, more than 95% of COD, BOD and SS were removed. Fast and complete nitrification was accomplished, and denitrification was appeared to be the rate-limiting step. More than 75% T-N could be removed due to the endogenous denitrification. T-P removal efficiency was increased to 80% under the condition of MLSS 10,000mg/L.

• 한국물환경학회지
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• 제21권1호
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• pp.29-33
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• 2005

In order to recycle the waste material and to develop the thickening unit of waste activated sludge from wastewater treatment facilities, the filtration bio-reactor equipped with a shadow mask filter module was employed for this work from which the operating properties and parameters were drawn. The sludge thickening and filtration unit is made of cylindrical acryl tank(12cm i.d. ${\times}$ 58cm height: working volume of 6L), where the flat-sheet type of shadow mask filter module(pore size: 220~250um, opening area: 34.8~39.6%) was installed and the effluent was withdrawn from the effluent port at the lowest point of the reactor, and the filtration was performed only by the hydraulic pressure. For evaluating the operating performance of this reactor, some parameters such as the solid-liquid separation of different biomass concentrations, the water quality of filtrate, the aeration cleaning time and the cleaning effect were investigated. Depending on the MLSS concentrations, the different time to withdraw 3L of filtrate was required in which the longer filtration time was necessary for the higher MLSS concentrations caused by the thicker formation of cake layer: 40 minutes for 5,000 mg/L, 70 minutes for 10,000 mg/L and 100 minutes for 15,000 mg/L, where the concentrations of SS were 8.9, 6.7 and 6.5 mg/L, respectively. Under the same operating conditions (the intensity of aeration cleaning: 80 L/min, MLSS: 10,000 mg/L), the proper aeration cleaning time was revealed 30 seconds, and the stable formation of cake layer was in the range of 10 to 15 minutes. Therefore, the shadow mask considered as a waste material can be of use as a filter material for the sludge thickening system.

• 한국전산유체공학회지
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• 제10권2호
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• pp.38-47
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• 2005

Substructuring methods are often used in finite element structural analyses. In this study a multi-level substructuring(MLSS) algorithm is developed and proposed as a possible candidate for finite element fluid solvers. The present algorithm consists of four stages such as a gathering, a condensing, a solving and a scattering stage. At each level, a predetermined number of elements are gathered and condensed to form an element of higher level. At the highest level, each sub-domain consists of only one super-element. Thus, the inversion process of a stiffness matrix associated with internal degrees of freedom of each sub-domain has been replaced by a sequential static condensation of gathered element matrices. The global algebraic system arising from the assembly of each sub-domain matrices is solved using a well-known iterative solver such as the conjugare gradient(CG) or the conjugate gradient squared(CGS) method. A time comparison with CG has been performed on a 2-D Poisson problem. With one domain the computing time by MLSS is comparable with that by CG up to about 260,000 d.o.f. For 263,169 d.o.f using 8 x 8 sub-domains, the time by MLSS is reduced to a value less than $30\%$ of that by CG. The lid-driven cavity problem has been solved for Re = 3200 using the element interpolation degree(Deg.) up to cubic. in this case, preconditioning techniques usually accompanied by iterative solvers are not needed. Finite element formulation for the incompressible flow has been stabilized by a modified residual procedure proposed by Ilinca et al.[9].

• 한국물환경학회지
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• 제20권6호
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• pp.571-576
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• 2004

Since anaerobic/anoxic/oxic process, which is a typical mainstream biological nitrogen and phosphorus removal process, utilizes influent organic matter as an external carbon source for phosphorus release in anaerobic or anoxic stage, influent COD/T-P ratio gives a strong influence on performance of phosphorus removal process. In this study, a bench scale experiment was carried out for SBR process to investigate nitrogen and phosphorus removal at various influent COD/T-P ratio and nitrate loadings of 23~73 and 1.6~14.3g $NO_3{^-}-N/kg$ MLSS, respectively. The phosphorus release and excess uptake in anoxic condition were very active at influent COD/T-P ratios of 44 and 73. However, its release and uptake was not obviously observed at COD/T-P ratio of 23. Consequently, phosphorus removal efficiency was decreased. In addition, the phosphorus release and uptake rate in anoxic condition increased as the nitrate loading decreased. Specific denitrification rate had significantly high correlation with organic materials and nitrate loadings of the anoxic phase too. The rate of phosphorus release and uptake in the anoxic condition were $0.08{\sim}0.94kg\;S-P/kg\;MLSS{\cdot}d$ and $0.012{\sim}0.1kg\;S-P/kg\;MLSS{\cdot}d$, respectively.