• 한국해안해양공학회:학술대회논문집
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• 한국해안해양공학회 2008년도 발표논문집
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• pp.56-59
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• 2008

• 한국해안해양공학회:학술대회논문집
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• 한국해안해양공학회 2008년도 발표 논문집 제17권
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• pp.56-59
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• 2008

• 대한기계학회:학술대회논문집
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• 대한기계학회 2001년도 춘계학술대회논문집E
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• pp.777-782
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• 2001

In this study, we used In-line orifice mixer for efficient chemicals mixing in water treatment. The method of using In-line orifice mixer has been already proved the improvement of water treatment efficiency. Numerical study was performed using FLUENT, a commercial code, to standard design and production of effective In-line orifice mixer. As variable for exactly standardizing, a proper ratio between an outer diameter of cone and a diameter of pipe, a distance between cone and orifice, a determination of orifice diameter for an optimal mixing, a distance between injection nozzle's position and cone, Numerical study has been performed for optimal standard and analyzed flow field on a basis of turbulent intensity in an orifice downstream.

• 센서학회지
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• 제14권1호
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• pp.47-51
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• 2005

An active ${\mu}$-mixer is important in Bio-MEMS and ${\mu}$-TAS. The mixing state depends on some kinds of factors including the intensity of ultrasonic radiation. We have visualized the mixing state of the mixing chamber with radiation time and presented the influence of the driving voltage in this research. It will be possible to compare the performances of the ultrasonic radiation parts used in the active ${\mu}$-mixer using this method.

• 한국전산유체공학회:학술대회논문집
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• 한국전산유체공학회 2001년도 추계 학술대회논문집
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• pp.132-137
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• 2001

We used In-line orifice mixer for efficient chemicals mixing in water treatment. The method of using In-line orifice mixer has been already proved the improvement of water treatment efficiency. Code of computational fluid dynamics for numerical analysis was performed using FLUENT, a commercial code. As variable for exactly standardizing, a proper ratio between an outer diameter of deflector and a diameter of pipe, the distance between deflector and orifice, a determination of orifice diameter fur an optimal mixing, a distance between injection nozzle's position and cone, Numerical study has been performed for optimal standard and analyzed flow field on a basis of turbulent intensity in an orifice downstream.

• 대한환경공학회지
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• 제35권11호
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• pp.803-808
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• 2013

본 연구의 목적은 칼슘염을 함유한 레미콘 슬러지를 이용하여 불소함유폐수를 물에 난용성인 $CaF_2$ 화합물 형태로 침전시켜 처리하는데 있어 pH, 레미콘슬러지 주입량, Seed물질 주입량, 교반속도, 교반시간의 최적 조건을 도출하고자 하는데 있다. 실험결과 레미콘 슬러지를 이용한 대상폐수의 $CaF_2$ 침전 반응에서 함수율 및 불소의 제거효율 등을 고려할 경우 최적의 pH 6, 레미콘 슬러지 주입량은 10 g/L, Seed 물질 주입량은 2 g/L, 교반속도은 100 rpm, 교반시간은 60 min으로 관찰되었다. 이 때 Seed 물질의 주입은 불소제거효율에는 영향이 없는 것으로 나타났지만 침전물의 형성이 되는 반응을 촉진시키고 플럭형성을 원활하게 하여 고액 분리가 잘 되어 함수율이 낮아지는 결과가 나타났다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2001년도 춘계학술대회논문집E
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• pp.542-547
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• 2001

A non-intrusive Planar Laser-Induced Fluorescence(PLIF) technique was applied to study the turbulent mixing process in a Rushton turbine reactor. Instantaneous and ensemble averaged concentration fields are obtained by measuring the fluorescence intensity of Rhodamine B tracer excited by a thin Nd:Yag laser sheet illuminating the whole center plane of the stirred tank. The gray level images captured by a 14-bit cooled CCD camera can be transformed to the local concentration values using a calibration matrix. The dye injection point was selected at the tank wall with three quarter height (3/4H) from the tank bottom to observe the mixing characteristics in upper bulk flow region. There exist distinct two time scales: the rapid decay of mean concentration in each region after the dye infusion reflects the large scale mixing while the followed slow decay reveals the small scale mixing. The temporal change of concentration probability functions conjectures the two sequential processes in the batch type mixing. An inactive column of water existed above the impeller disk, in which the fluid rotates with the shaft but is isolated from the mean bulk flow.

• 대한기계학회논문집B
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• 제26권8호
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• pp.1145-1152
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• 2002

A non-intrusive Planar Laser-Induced Fluorescence(PLIF) technique was applied to study the turbulent mixing process in a Rushton turbine reactor. Instantaneous and ensemble averaged concentration fields was obtained by measuring the fluorescence intensity of Rhodamine B tracer excited by a thin Nd:Yag laser sheet illuminating the whole center plane of the stirred tank. The gray level images captured by a 14-bit cooled CCD camera could be transformed to the local concentration values using a calibration matrix. The dye injection point was selected at the tank wall with three quarter. height (3/4H) from the tank bottom to observe the mixing characteristics in upper bulk flow region. There exist distinct two time scales: the rapid decay of mean concentration after the dye infusion reflects the large scale turbulent mixing while the fellowed slow decay reveals the small scale molecular mixing. The temporal change of concentration variance field conjectures the two sequential processes for the batch type mixing. An inactive column of water is existed above the impeller disk, in which the fluid rotates with the shaft but is isolated from the mean bulk flow.

• 한국수자원학회논문집
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• 제30권6호
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• pp.731-741
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• 1997

동일한 원수에 대하여 탁도제거 지배인자를 변화시켜가며 임펠러 형태별 탁도제거효율을 비교함으로써 관습적으로 설계 운영해오던 혼화과정의 문제점과 정수장의 최적 혼화저건을 만족시킬 수 있는 혼화기의 임펠러 타입 및 체류시간에 대한 운전기준을 제시하고자 하였다. 실험결과 혼화기의 종류는 탁도제거 효율을 물론 정수장의 경제적 운영을 위한 전력비 절감에도 효과가 있는 것으로 판명되었다. 또한 혼화지와 혼화기 설계기준에 일반적으로 활용되어 오던 속도구매 G이외에도 원수의 단위체적당 필요한 혼화에너지를 제시하여 정수효율은 물론 정수장의 경제적 운영효과를 극대화시킬 수 있는 참고자료로 제시하였다.

• 대한환경공학회지
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• 제33권5호
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• pp.307-313
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• 2011

본 연구는 고농도의 불소가 함유된 LCD 폐수를 처리하는데 있어, 칼슘원에 따른 제거 효율과 경제성에 부합되는 조건을 도출하여 실제 현장에 적용하는데 목적이 있다. 이를 위하여 칼슘원으로 $CaCl_2$, $Ca(OH)_2$ 및 $CaCO_3$를 이용하여 각각 pH, 칼슘주입량, 반응시간 및 교반속도의 변화에 따른 특성을 관찰하였다. 그 결과 $CaCl_2$의 경우 pH 7, 칼슘주입량 0.4[Ca]/[F] (mol / mol), 1시간, 200 rpm으로 결정되었고, $Ca(OH)_2$의 경우 pH 7, 칼슘주입량 30 mL/L, 1시간, 200 rpm으로 결정하였으며, $CaCO_3$의 경우 pH 4, 칼슘주입량 30 mL/L, 1시간, 200 rpm으로 적용하는 것이 최적조건이라고 판단되었다. 그러나 현장의 상황에 따라 적용 조건의 변경이 가능하다.