• 한국환경과학회지
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• 제21권8호
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• pp.901-907
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• 2012

The objective of this study was to evaluate bacteria removal ability of the metallic silver which was baked silver ion impregnated ceramic filter at heating condition. Silver leaking from baked ceramic filter was tested to sustain bacteria removal for a long time. Silver impregnated ceramic filter could remove E. coli completely at $10^{12}$ MPN/100ml to $10^{13}$ MPN/100ml of influent. However, ceramic filter without silver did not remove E. coli completely under the same condition. After baking, the silver impregnated ceramic filter almost didn't leak out the silver ion from filter. Photo of TEM (Transmission Electron Microscopy) showed that absorbed silver ions remained in ceramic filter after baking process and most of silver were less than 10 nm. According to the increase in the amount of silver in the ceramic filter, removal efficiencies of E. coli were increased but turbidity removal was decreased. It can be accounted that increased removal efficiency of E. coli was from disinfection of silver that is in the ceramic filter. Simulated concentrations of bacteria agree well with the observed experimental effluent concentration data. Moreover, first-order decay coefficients increased to 0.0034/min after silver was added in the ceramic filter. Increase of first-order decay coefficient proves that silver-added ceramic filter can remove bacteria easily.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2002년도 학술대회지
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• pp.819-822
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• 2002

It is necessary for the numerical simulation of 3-dimensional incompressible isotropic decaying turbulence to construct 3-dimensional initial velocity field which resembles the fully developed turbulence. Although the previous velocity field generation method proposed by Rogallo(1981) satisfies continuity equation and 3-dimensional energy spectrum, it has limitation, as indicated in his paper, that it does not produce the higher velocity moments(e. g. velocity derivative skewness) characteristic of real turbulence. In this study, a new velocity field generation method which is able to control velocity derivative skewness of initial velocity field is proposed. Brief descriptions of the new method and a few parameters which is used to control velocity derivative skewness are given. A large eddy simulation(LES) of isotropic decaying turbulence using dynamic subgrid-scale model is carried out to evaluate the performance of the initial velocity field generated by the new method. It was shown that the resolved turbulent kinetic energy decay curve and the resolved enstrophy decay curve from the initial field of new method were more realistic than those from the initial field of Rogallo's method. It was found that the dynamic model coefficient from the former was initially half the stationary value and experienced relatively short transition period, though that from the latter was initially zero and experienced relatively longer transition period.

• 환경위생공학
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• 제8권1호
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• pp.107-116
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• 1993

This study is conducted to investigate treatability by activated sludge process for wastewater from acetaldehyde manufacturing plant. The optimum hydraulic retention time in aeration tank for removal of high strength substrate were measured. The removal efficiency were checked out by hydraulic retention time : 35hr., 40hr. and 45hr., respectively. $COD_{Cr}$, like substances were removed in all hydraulic retention time zone directed for efficiency, but non-biodegradable substances were remained. $COD_{Cr}$ biomass loading was 0.81kg $COD_{Cr}/kgMLVSS$ . day at 35hr. of retention time, 0.34 kg$COD_{Cr}$/kg MLVSS . day at 40hr., and O.l9kg$COD_Cr$/kgMLVSS . day at 45hr. And the mean $COD_{Cr}$, removal efficiency was 65.5%, 81.6% and 83.0%, respectively. And also $COD_{Cr}$, volume loading was 1.01kg$COD_{Cr}/m^3$ day, 0.87kg$COD_{Cr}/m^3$ - day, and 0.79kg$COD_{Cr}/m^3{\cdot }$day, respectively. The basic design parameter obtained is as fallows. The value of Specific substrate removal rate coefficient (k), Yield coefficient(Y) and Decay coefficient($k_d$) was $0.0013day^{-1}$, $0.505kgMLVSS/kgCOD_{Cr}$ and $0.040day^{-1}$, respectively.

• 상하수도학회지
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• 제20권3호
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• pp.329-338
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• 2006

The research aims to provide the basic data for practical applications by correlating the bio-kinetic coefficients with the load of recalcitrant organic matter in box-mill wastewater. The activated sludge process was employed to a Wastewater disposal plant in an industrial setting, increase of consequently leading to the organic load. The parameter values derived by Monod-kinetic analysis were as follows:specific substrate removal rate $K_{max}=0.17day^{-1}$, half saturation constants $K_s=60.37mg/l$, decay coefficient $K_d=0.142day^{-1}$, microbial yield coefficient y = 0.388mg/mg, and max specific growth rate ${\mu}_{max}=0.006day^{-1}$. In view of biodegradability, the $TCOD_{Mn}/TBOD_5$ ratios of inflow and outflow were 1.07 and 1.41, and the $SCOD_{Mn}/SBOD_5$ ratios of inflow and outflow were 1.10 and 1.50, respectively. The higher $TCOD_{Mn}/TBOD_5$ ratio of outflow indicated that metabolites of a microorganism have accumulated in the cells.

• 한국광학회지
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• 제12권3호
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• pp.225-229
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• 2001

강유전성 고분자인 P(VDF-TrFE) 공중합체의 전기광학계수의 완화현상을 고찰하였다. 이 고분자인 전기광학계수는 단순 반사법에 의해 측정하였고 완화현상은 KWW 확장된 지수 함수꼴로 분석하였다. Tc 근방에서 극화시킨 공중합체들은 시간적으로 더 안정적이였고 온도에 의존하는 완화시간$au$를 Arrhenius 형태로 분석하여 50mol%의 TrFe를 가진 공중합체가 28mol%를 가진 공중합체보다 활성화에너지가 더 컸다. 이를 통해 $60^{\circ}C$에서 극화시킨 50mol%의 TrFE를 가진 공중합체가 더안정적임을 알 수 있다.

• 수산해양기술연구
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• 제17권1호
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• pp.41-47
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• 1981

The characteristics of septic tank sludges were investigated and the kinetic coefficients in the aerobic biodegradation were evaluated from bach treatability tests. Using an unbiased statistical method, the estimated values, k (substrate removal rate coefficient) =0. 0175hr-1 at 17\ulcornerC, K. (Michaelis Menten constant) = 248mg/ e, a (cell yield coefficient)=0.625, and Kd (cell decay coefficient:' =0. 00192hr-1 were obtained based on biodegradable COD(mg/ \ulcorner) and volatile suspended solids(mg/\ulcorner). The relationship between COD and BOD, COD (mg/\ulcorner) =2. 1 BOD(mg/\ulcorner) +250, also was established for the septic tank sludges. Dilution was inevitable for the grit removal because of the high viscosity of the sludges. An aerobic activated sludge process rather than anaerobic processes was recommended for the removal of soluble organics after the removal of grit and suspended solids. A multi-stage activated sludge process was adapted for this highly concentrated and not easily-degradable waste. It was estimated that a four-stage activated sludge process would require 40 hours retention time compared to 92 hours for a single-stage process, 52 hours for a double-stage process, and 46 hours for a three stage process in order to achieve an effluent quality of 84mg/ e COD( 40mg/ e BOD) with about 4, OOOmg/ \ulcorner MLSS from an influent quality of I, 500mg/ t COD(714mg/.e BOD), while multi-stages beyond four stage would not save the required retention time significantly.

• 대한지하수환경학회지
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• 제6권2호
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• pp.95-100
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• 1999

토립자 표면에서의 흡착에 의한 토양에서의 탄화수소계 화합물의 지연효과는 잘 알려진 현상이다. 본 연구에서는 배치시험과 주상시험을 수행함으로써 사질토양에서 Benzene의 이동성에 대한 지연효과를 조사하였다. 배치시험을 위하여 토양시료와 다양한 초기농도의 Benzene 용액을 48시간 반응시켰고. 초기용액과 평행상태의 Benzene 용액의 농도를 HPLC를 이용하여 분석하였다. 주상시험은 파괴곡선으로 알려진 시간에 따른 용액의 농도를 측정함으로써 수행되었다. 추적자로는 10 g/L 농도의 KCI과 0.88 g/L의 Benzene 용액을 사용하였고 .각각의 용액을 토양시료의 상부경계면에 순간주입한 후 정상류 상태에서 배출구로 빠져나온 용탈수의 농도를 EC-meter와 HPLC를 이용하여 측정하였다. 배치시험의 결과로부터 linear adsorption isotherm에 의한 분배계수가 측정되었고 주상시험 조건의 용적밀도 및 함수율을 고려한 지연계수가 산정되었다. 주상시험의 결과 i) Benzene의 첨두농도는 KCl 첨두농도보다 상당히 낮았으나. ⅱ) 첨도농도의 도달시간은 거의 일치하였다. 첨두농도의 도달시간이 일치한다는 결과는 지연효과가 일어나지 않았다는 것을 지시하며, 배치시험의 결과로부터 산정된 지연계수를 고려하여 예측된 파과곡선은 Benzene의 주상시험 결과와 일치하지 않았다. Benzene 농도의 뚜렷한 감소를 설명할 수 있는 유일한 방법은 convection-dispersion equation(CDE) 모델에서 비가역 흡착에 의한 농도의 절대적 감소를 고려하는 감쇄계수(decay or sink coefficient)를 적용해야 하는 것으로 판단된다.

• Nuclear Engineering and Technology
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• 제26권1호
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• pp.19-31
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• 1994

기사용 핵연료 저장조에 대한 열수력 해석과 관련된 인자들이 열수력 해석에 미치는 영향에 대한 분석을 수행하였다. 기사용 핵연료에서 발생하는 붕괴열(decay heat)을 제거하기 위해 일어나는 자연 순환(natural circulation)현상을 모사하기 위해 단순화된 유동망(simplified flow network)해석 모델을 사용하였다. 기사용 핵연료 저장조의 각 셀에 저장되는 연료 집합체에서 발생하는 붕괴열을 제거하기 위해 흐르는 유량의 압력 손실량이 자연순환을 일으키는 밀도차이에 의해 생성되는 구동력(driving force)과 평형을 이루는 관계를 이용하여 지배 방정식을 유도하였다. 그러나 유량, 저항 계수, 붕괴열, 밀도 등의 변수들이 서로 종속 관계를 갖기 때문에 반복 계산을 통해 해를 얻게 된다. 본 해석을 적용한 영광 3, 4호기의 경우, 12채널을 고려하였고 사용되는 입력 (저항 계수, 붕괴열)을 보수적으로 결정하였다. 본 연구를 통해 영광 3, 4호기 기사용 핵연료 저장조의 열수력 특성을 구하였다. 또한 유동로를 따라 형성되는 유동 저항중에 기하학적 요인에 의한 압력 손실은, 기사용 핵연료 저장조의 경우 압력 용기내의 유동과 달리 천이 영역(transition region)이 존재하게 되므로 Reynolds수에 민감한 것을 알 수 있다. 간극 유동은 조밀화된 연료 집합체 (consolidated fuel assembly)가 아닌 경우 무시할 수 있었다.

• 한국환경농학회지
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• 제14권1호
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• pp.7-14
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• 1995

하천 수질관리 모델인 QUAL2E를 남강에 적용한 결과는 다음과 같다. 1. 모델변수의 민감도 분석 결과는 BOD, DO의 경우 BOD decay rate constant, 영양염류인 경우 Org-N oxidation rate constant, $NH_3-N$ oxidation rate constant, Org-P decay rate constant가 각 수질인자에 중요한 변수로 작용하였다. 2. 모델보정 결과를 보면 실측치와 예측치의 상관성은 DO, BOD의 경우 r=0.93, 0.94로 높은 상관성을 보였으며 영양염류인 경우는 질산성 질소가 r=0.61이었으나, 그 외는 r=0.90 이상으로 나타났다. 3. 모델검증 결과는 보정시보다 상관성이 떨어졌으나 DO, $NO_3-N$의 경우 r=0.68, 0.45로 낮고 그 외는 r=0.75이상으로 높은 편으로 나타났다. 4. 유량과 부하량의 변화에 대하여 하류 40.5 Km 이후의 BOD 농도변화는 적었으나, 하수종말처리장 건설이후 유량과 부하량을 변화시켜 수질농도를 예측한 결과 하류 40.5 Km 이후는 함안천의 영향을 받을 것으로 예측되었다.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 1998년도 총회 및 춘계 학술발표회 논문집
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• pp.43-49
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• 1998

Retardation effect of heavy metals in soils caused by adsorption onto the surfaces of solids particles is well known phenomena. The adsorption of metal ions has been recognized more strong in clay mineral and organic matter contents rather than sands and gravels. In this study, we investigated the retardation effect in two sandy soils by conducting batch and column tests. The column tests were conducted to obtain the relationship between concentration and time known as breakthrough curve (BTC). We applied pulse type injection of ZnCl$_2$solution on the inlet boundary and monitored the effluent concentration at the exit boundary under steady state condition using EC-meter and ICP-AES. Batch test consisted of an equilibrium procedure for fine fractions collected from two sandy soils for various initial ZnCl$_2$concentrations, and analysis of Zn ions in equilibrated solution using ICP-AES. The results of column test showed that i) the peak concentration of Zn analyzed by ICP was far less than that detected by EC-meter for both soils and ii) travel times for peak concentration were more less identical for two different monitoring techniques. The first result can be explained by ion exchange between Zn and other cations initially present in the soil particles since ICP analysis showed a significant amount of Ca, Mg ions in the effluent. From the second result, we found that retardation effect was not present in these soils due to strong cation exchange capacity of Zn ion over other cations since we did not apply a solution containing more adsorptive cations such as Al. The result of batch test also showed high distribution coefficients (K$_{d}$) for two soils supporting the dominant ion exchange phenomena. Based on the retardation factor obtained from the Kd, we predicted the BTC using CDE model and compared with the BTC of Zn concentration obtained from ICP The predicted BTC, however, disagreed with the monitored in terms of travel time and magnitude of the peak concentrations. The only way to describe the prominent decrease of Zn ion was to introduce decay or sink coefficient in the CDE model to account for irreversible decrease of Zn ions in liquid phase.e.