• Korean Chemical Engineering Research
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• v.46 no.5
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• pp.983-987
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• 2008

Computational simulation has been performed to design optimally the filtration system for IGCC pilot plant. It was analyzed how the different inflow pattern influences the flow field and the particle behavior in a filter vessel. The particle loading onto the filter surface lowers significantly and decreases dramatically with particle size when the dusty gas flows into the filter vessel with a shroud tube through a tangential inlet setup tangentially on the vessel outer wall. However, the particle loading is considerably high when the dusty gas enters the filter vessel through a normal inlet setup vertically on the vessel top wall, and the decrease of the particle loading with particle size is not steeper compared with the tangential inflow pattern.

• Proceedings of the Korea Water Resources Association Conference
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• 2009.05a
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• pp.2009-2013
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• 2009

일반적으로 비닐하우스내의 농작물 경작은 자연환경과 차단된 조건에서 작물을 집약적으로 재배하므로 비료의 사용량이 많아 오염원으로 작용하고, 휴작기에 비닐을 제거 방치하므로 비닐 표면에 집적된 오염물은 강우 시 유출되어 이들로 인한 주변 하천수 및 지하수 오염을 가중시킨다. 따라서 팔당호 유역내 하천 부지에서 비닐하우스 등이 집단화 되어 있어 이로 인해 팔당호 유역내 수질에 영향을 미칠 것으로 판단된다. 또한 팔당호 유역내 하천부지에서 대단위 비닐농가가 집단적으로 조성되어 있는 것으로 조사되었으며, 팔당호 유역내 산발적으로 비닐하우스 농가가 형성되어 있는 것으로 조사되었다. 이들 비닐하우스로부터 비강우시에는 유출 오염수는 없는 것으로 파악되었으나, 강우 시 강우유출수가 표면 유출되는 과정에서 오염수가 팔당호로 직접 유입되어 팔당호 수질에 영향을 미치는 것으로 파악되었다. 팔당호 유역의 비닐하우스 경작에 의한 수질특성 조사 결과, SS 농도는 북한강 $372{\sim}446$ $mg/{\ell}$, 남한강 $488{\sim}547$ $mg/{\ell}$, 경안천 $345{\sim}415$ $mg/{\ell}$로 조사되었으며, BOD 농도는 북한강 $12.2{\sim}15.3$ $mg/{\ell}$, 남한강 $13.3{\sim}16.8$ $mg/{\ell}$, 경안천 $15.6{\sim}18.8$ $mg/{\ell}$으로 조사되었고, COD 농도는 북한강 $23.9{\sim}26.8$ $mg/{\ell}$, 남한강 $25.2{\sim}26.0$ $mg/{\ell}$, 경안천 $26.4{\sim}32.9$ $mg/{\ell}$로 조사되었다. 또한 T-N 농도는 북한강 $17.39{\sim}23.64$ $mg/{\ell}$, 남한강 $17.87{\sim}22.09$ $mg/{\ell}$, 경안천 $18.34{\sim}19.55$ $mg/{\ell}$으로 조사되었으며, T-P 농도는 북한강 $1.425{\sim}1.795$ $mg/{\ell}$, 남한강 $1.519{\sim}1.767$ $mg/{\ell}$, 경안천 $1.727{\sim}1.827$ $mg/{\ell}$로 조사되었다. 또한, 오염부하량으로부터 산정된 비닐하우스의 하천에 미치는 오염부하기여율은 SS의 경우 17.3%, BOD 4.5%, COD 5.2%, T-N 11.0%, T-P 7.4%로 조사되었다. 이는 비닐하우스 농가에서 유출되는 SS 및 T-N, T-P 오염부하량이 하천에 미치는 영향이 상대적으로 높다는 것을 의미하며, 이는 비닐하우스 주변이 주로 나대지로 되어 있고 비료 또는 영양물질이 많기 때문인 것으로 판단된다. 그러나 탄소성 유기물질을 나타내는 BOD 및 COD의 오염부하기여율은 주변 토양과 큰 차이를 보이지 않았다. 결국 비닐하우스의 재배는 토양 표면피복의 효과적인 관리 및 영양물질에 대한 관리가 이루어지지 않을 경우 팔당호에 영향을 미칠 수 있을 것으로 판단된다.

• Journal of the Korean Society for Aeronautical & Space Sciences
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• v.30 no.3
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• pp.77-86
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• 2002

위성은 일단 한 번 발사하고 나면 운용궤도상에서 수리 및 회수가 거의 불가능하기 때문에 위성에 들어가는 모든 개발 부품들은 완벽한 설계, 충분한 해석, 고 작업도의 제작, 그리고 다양한 시험이 반드시 수반되어야 한다. 위성시스템에서 전자 소자의 신뢰성에 영향을 주는 인자는 다양하다. 과도한 열은 전자소자의 실패를 유발해서 결과적으로는 전체 위성의 실패를 유도할 수 있다. 이 논문에서는 다목적 실용위성 2호의 고전력 소산 전장품의 열부하 완화를 위한 방안을 경우별로 연구 비교하였다. 고전력 소산 전장품의 열부하를 완화하기 위해서는 하우징 두께의 증가가 필요하며, 전력조절기의 다이오드나 트랜지스터처럼 전력소산이 큰 소자에 대해서는 장착위치를 변경하거나 장착 부분의 열전도율을 증가시키는 방법이 필요하다. 또한 전력조절기처럼 장착면이 좁은 경우에는 복사의 영향이 크며, 이러한 전장품의 열부하를 완화하기 위해서는 주위 벽면의 온도를 낮추거나 하우징 표면 방사율을 증가시키는 방법이 효과적임이 알 수 있다.

• Publications of The Korean Astronomical Society
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• v.6 no.1
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• pp.1-15
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• 1991

원반 및 해일로의 이중역 (two-zone) 모형을 바탕으로하여 나선은하의 화학적 진화 모형을 만들었다. 모형의 검증을 위하여 구체적인 수치계산을 수행하고 그 결과를 태양 부근에서 관측된 중원소 분포 등, 화학적 진화와 관련된 제반 관측 사실과 비교함으로써 은하계의 진화를 추론하였다. 모형의 수치계산 결과에 의하면 나선은하의 화학적 진화는 헤일로외 붕괴 과정과 별탄생율에 크게 의존하며, 원반의 초기질량함수와 별탄생율에 따라 서로 다른 양상을 보인다. 태양 부근 원반의 중원소 분포 등을 성공적으로 설명할 수 있는 진화 모형에서, 별탄생율은 가스의 질량 또는 표면밀도의 멱승에 비례하거나 시간에 따라 단조 감소하는 지수함수로써 표현되며, 초기질량함수는 헤일로에서는 다양한 형태의 함수 모두로써 가능하지만, 원반의 경우에는 시간에 따라 변화하는 질량함수를 채택하여야 한다. 우리 은하의 헤일로의 고속붕괴 모형에서는 시간에 따라 지수함수로 변화하는 별탄생율이 관측과 부하되지만, 반면 저속붕괴의 경우에는 가스 질량의 멱함수로 표현되는 별탄생율이 관측과 부합된다.

• Korean Journal of Environmental Agriculture
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• v.18 no.3
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• pp.209-214
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• 1999

Objective of the research is to estimate neutralization capacity and to determine practical running parameters required in packing tower design of waste oyster shells using Bohart-Adams equation. It is expected that waste oyster shells are able to be recycled for removal of heavy metals through neutralization of plating wastewater because those contain approximate 93% $CaCO_3$. By applying the results of the continuous experiment to Bohart-Adams equation, service time decreases in the order of Cr>Fe>Cu, while removal efficiencies of metals become less in the order of Fe>Cr>Cu.

• Korean Journal of Fisheries and Aquatic Sciences
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• v.33 no.4
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• pp.367-372
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• 2000

A series of experiment was conducted to investigate the relationship between ammoia removal rate and ammonia loading rates in seawater filtering system using rotating biological contactor (RBC). In this experiment, RBC system was consisted of rotating polyvinyl film disks, which provided $12 m^2$ of total effective surface area in $0.075 m^3$ of volume. $NH_4Cl$ was added by $10{\~}150 g$ as a ammonia nitrogen source to determine ammonia removal rate in RBC system. Relationship between time required for ammonia removal (y: hour) and nitrogen inputted ($x: NH_4-N mg/l$) in RBC system was as followed: $y=3.51+7.76 lnx (r^2=0.936)$. At ammonia concentration $2 mg/l$, it took 10 hour for removal of ammonia in the RBC system. However, at ammonia concentration of $5 and 16.5 mg/l$, it took 16 and 27 hours, respectively. There was a decreasing tencency of an increasing ammonia in the rearing water. Finally, the ammonia removal rate in the RBC system increased with the rise of total ammonia concentration up to $16.5 mg/l$.

• Korean Journal of Ecology and Environment
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• v.35 no.1 s.97
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• pp.28-35
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• 2002

The effect of physical parameters on water quality was analyzed using monitoring data of 193 agricultural reservoirs. The retention time of reservoirs ($t_d$) ranged between 10 and 140 days, and the ratio of drainage area (DA) to reservoir surface area (SA) was between 10 and 120. Both ratios of DA/SA and total area (TA)/ reservoir storage (ST) in Korean agricultural reservoirs were relatively greater than those in natural lakes in other countries. As retention time was plotted against DA/SA ratio, it was shorter in Korean reservoirs than natural lakes. The semi-logarithmic relationship between TA/SA and t>$t_d$ was $t_d\;=\;42.21(TA/ST)^{-1}$ (n = 50, $R^2\;=\;0.89$). While areal loading of total phosphorus (TP) was below $4\;gTP{\cdot}m^{-2}{\cdot}yr^{-1}$ in general, it exceeded $10\;gTP{\cdot}m^{-2}{\cdot}yr^{-1}$ in reservoirs where DA/SA ratio was greater than 100, which implies that areal loading of TP increases as DA/SA ratio increases. Chl-a concentration was positively related with the mean depth of reservoir, implying the higher Chl-a concentration with deeper the mean depth. Therefore, the deeper reservoir might be advantageous in water quality management perspective if other morphological conditions are similar. The empirical regression equation using physical parameters was also suggested in the estimation of TP concentration in the reservoirs. Combined information presented in this paper might be applicable to the water quality management in agricultural reservoirs.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.15 no.5
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• pp.3336-3344
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• 2014

The purpose of this study is small scale coagulation module is developed and demonstrated through a lab-scale test. Recent as a sewage treatment rate increases, have heightened the interest in the necessity on the nonpoint source and developing a small processing unit has been increased. Coagulation sedimentation module in this study is additional growth of floc through swirling in the outside zone, reduction of microstructure floc number and the internal settling zone through vertical/level flow complex sedimentation method after the coagulation process precipitation method as an effective high separation efficiency can be divided was also assessed. Coagulation sedimentation module can increase the load factor was 4.4 times compared to conventional clarifier base on the same volume and surface area through vertical/level flow. In this study, this process was selected formation and maintenance of swirling and uniform flow distribution in the internal settling zone as an important design factor, to derive its FLUENT was used to characteristics of the flow model. Through the simulation of swirling, influent velocity, dimensions of external basin, hopper depth of bottom cone was determined and through analysis of velocity distribution, flow distribution detailed specifications are derived like as diameter and number of effluent hole. Lab-scale($120{\ell}/hr$) test results, influent of 300~800 NTU to less than 10 NTU without polymer feeding was able to operate in the 20minutes retention time(surface loading rate $37.3m^3/m^2$-day), and through analysis FLUENT the possibility of using design parameters were derived.

• Journal of Korean Society of Water and Wastewater
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• v.17 no.4
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• pp.528-533
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• 2003

Bubble size is one of the most important parameters affecting DAF (Dissolved-Air-Flotation) process. It is generally known that small bubbles are preferred. However, the fact seems to be based on the particle removal efficiency at contact zone only, without considering separation zone. Besides, the effect of bubble size on the overall DAF process has not been fully investigated yet. Therefore, the effect of bubble size on collision efficiency, collision chances, and surface loading rate is calculated using theoretical models, and the results are discussed in this paper.

• Journal of Korean Society of Water and Wastewater
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• v.20 no.1
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• pp.138-146
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• 2006

The characteristics of backwash and concentrate discharges depend upon the quality of the water being treated and the net recovery of the membrane system. This paper is to indicate a design methods on the capacities of residuals treatment facilities in membrane processes for drinking water. We operated a demonstration membrane plant with a recovery rate of 90% for designing G-water treatment plant. We investigated on design parameter (optimum coagulant dosage and surface loading rate etc.) to design efficiently the residuals treatment facilities. The settling test was conducted with 1m columns dosing PACl to kaolin and membrane residuals under the experimental condition that discharge permit was under a 60mg/L. When the quantity of membrane residuals was $1,575m^3/day$, the estimated results for 1st thickener demonstrated the surface loading rate of 14.4m/day, detention time of 5.83hr, available depth of 3.5m.