• Proceedings of the Korea Water Resources Association Conference
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• 2007.05a
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• pp.1189-1193
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• 2007

국내 정수장내 설치되어 있는 혼화기는 대부분 기계식 급속혼화 방식을 채택하여 운영하고 있으며 대부분의 혼화지가 크게 설계되어 설계 변경을 하지 않고서는 혼화 효율을 높이는 한계가 있다. 혼화지내 격벽을 설치하여 혼화 구간을 축소시킴으로써 혼화구간이 큰 구조에 비해 6.27%의 효율이 더 좋은 것으로 나타났으며 격벽이 설치된 혼화구간내에 임펠러는 격벽으로 둘러싸인 유출부쪽(상단부)에서 85.45%로 가장 좋은 효과가 나타났다. 또한 약품위치가 임펠러 하단에 가까우면 혼화효과가 크며 멀 경우에 격벽설치에 따른 혼화효과가 더욱 큰 것으로 나타났다.

• Proceedings of the Korea Water Resources Association Conference
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• 2008.05a
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• pp.842-846
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• 2008

원수의 탁질 중에서 입경이 $10^{-1}$mm이상인 것은 보통침전으로 제거가 가능하지만, 입경이��$10^{-3}mm$이하가 되면 일반적으로 콜로이드입자라고 총칭하며 그대로의 상태로서는 거의 침강되지 않을 뿐만 아니라 급속여과기구에서도 포착되지 않는다. 따라서 급속여과 방식에서는 이와 같은 탁질을 효과적으로 제거하기 위한 전처리로서 응집조작으로 인한 콜로이드상의 탁질을 플록화하여 약품침전이나 급속여과에서 포착되도록 탁질의 성상을 변화시키는 조작이 반드시 필요하다. 또한 양호한 플록을 효과적으로 형성시키는 약품혼화와 플록형성 등을 강구해야 한다. 이에 본 연구에서는 현재 국내에서 운영하고 있는 정수처리시스템의 일부인 혼화지내에 혼화지점의 단면적을 축소시켜 약품혼화효과를 극대화하고 혼화기의 소요동력을 감소시켜 혼화효과를 개선하며 혼화지내 혼화기 운용의 비용 절감 효과를 증가시키기 위한 저에너지형 CF혼화장치를 개발하는데 연구 목적이 있다. 연구결과 CF혼화장치의 설치시 약품 투입 위치에 따라 $2{\sim}6%$정도의 탁도제거율의 상승과 슬러지 높이의 차이를 보이는 것으로 나타났으며 이 실험 결과 약품투입장소에서 혼화지의 Compact화로 인해 급속 혼화를 이룰 경우 더 많은 플록화로 인해 탁도 제거율이 높아지는 것을 알 수 있다.

• Magazine of the Korea Concrete Institute
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• v.10 no.4
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• pp.205-212
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• 1998

Frost damage of a storage tank for chemical admixtures caused by a low temperature in winter and quality deterioration of chemical admixtures have been often reported. However, there have been few regulations and researches related to the frost damage of chemical admixtures and facilities. Therefore, this paper is intend to investigate not only, the freezing points of chemical admixtures such as AE admixtures and water-reducing AE admixtures, etc., but also the quality variation of concrete used with chemical admixtures before freezing and after freeze-thaw cycles. According to the results of experiments, most chemical admixtures except anti-freezing agent and accelerating water-reducing AE admixtures should be kept from being frozen in low winter temperatures. However, full agitation of frozen chemical admixtures dose not cause the problems of concrete related to the quality of chemical admixtures.

• Proceedings of the Korean Fiber Society Conference
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• 2003.10b
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• pp.70-73
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• 2003

최근 들어 poly(trimethylene terephtha)ate)(PTT)를 폴리에스터계 고분자들인 PET, PTN, PBN 등과 블렌드하고 이들의 특성 변화에 대해 검토한 결과가 많이 발표되고 있다. PTT를 PET나 PTN과 블렌드시키면 혼화성이 없으나, 이들 블렌드물을 용융시키면 점차 하나의 T$_{g}$를 나타내어 혼화성을 갖는다[1-3]. 반면에 PTT와 PBN을 블렌드시키면 처음부터 혼화성이 존재한다[4]. 이같이 PTT와 혼합되는 고분자의 종류에 따라 혼화성이 달라지는데, 본 연구는 PTT와 poly(ethylene naphthalate)(PEN)을 블렌드시키면 혼화성이 어떻게 되는가를 검토한 것이다. (중략)

• Journal of the Korea Academia-Industrial cooperation Society
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• v.18 no.2
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• pp.6-13
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• 2017

This study examines the effect of the type and number of orifices in an in-line mixer to improve the mixing performance and pressure loss. Recently, in-line non-power-consuming mixers have been increasingly used to complement mechanical mixers, which have a long dwell time, noise, excessive energy consumption, and high maintenance costs. An in-line mixer with an orifice for efficient mixing in water treatment was examined by numerical analysis using the commercial code FLUENT. The flow characteristics of pressure loss and velocity distribution within the mixer and the mixing efficiency were compared with and without the orifices. The CFD results show that the mixing efficiency was improved, but the pressure loss was increased by the in-line mixer with an orifice. A sensitivity study was also done on the principal parameters.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.7
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• pp.1173-1182
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• 2000

The rapid mixing process has been considered as an important step in water treatment. Since the coagulant dispersion into raw water by rapid mixer can influence on the flocculation and filtration efficiency, many researchers have developed various devices and mixing methodologies. Until now, they focused attention on only coagulant dose, pH. rotating velocity and G value but overlooked the real turbulent flow and mixer geometry in rapid mixer. Therefore this paper questions the significance of turbulent flows in rapid mixer and focuses on the analysis of turbulent fluid in various mixer geometry with CFD(Computational Fluid Dynamics). The results of the jar-tests using various geometries indicate that the turbidity removal rate in a circular jar without baffle is higher than that of a circular with baffle. And the turbidity removal rate in Hudson jar is also founded to be higher than in the circular jar with baffle. The CFD simulation of velocity fields in jar demonstrates that the differences of removal rates among the various geometries are largely due to the formation of the different turbulent fluids fields with different geometries.

• Journal of Korea Water Resources Association
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• v.30 no.6
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• pp.731-741
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• 1997

Optimum design conditions of rapid mixing impellers for an effective Water Treatment Plant operation were experimentally studied by thorough examination of parameters, such as impeller type and detention time. which govern the removal efficiency of turbidity. It was found that the impeller type is one of the major parameters governing the economic power consumption and the efficiency of turbidity removal. The experimental results showed that not only the velocity gradient G but also a new design guide. so called mixing energy per unit volume of raw water, could be used as a design and operation guides for rapid mixing in W.T.P.

• Proceedings of the Korean Society of Propulsion Engineers Conference
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• 2007.04a
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• pp.197-200
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• 2007

This paper presents solid propulsion manufacturing processes. Solid rocket motors propellants are made of several batches of propellant being mixed in mixers and made of continuous mixers. This paper discusses the technology of continuous mix process of Aerojet, US and SNPE Materiaux Energetiques, France.

• Journal of Korean Society of Environmental Engineers
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• v.39 no.12
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• pp.706-713
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• 2017

This study compared and analyzed the water treatment efficiency and the applicability of water treatment plant using the existing Mechanical Rapid-Mixer by introducing the Non-powered Vortex Mixer to the domestic water treatment plant. For this study, fluid flow characteristics and head loss of a Non-powered Vortex Mixer are calculated by Computational Fluid Dynamics (CFD)respectively. The head loss rate inside the mixer was 11.30% when the inflow velocity was 0.5 m/sec, 16.27% at 0.6 m/sec and 21.44% at 0.7 m/sec, the head loss rapidly increased at the optimal velocity of 0.5 m/sec. For the inflow velocity of 0.5 m/sec, the turbulent intensity at the inlet was 2.37% and at the outlet was 7.83%, so there was sufficient mixing strength for the particulate matter and the coagulant. The result of the water quality of the treatment plants with the inflow velocity of 0.38 m/sec that was operated in three years after replacing all 12 units of the existing Rapid-Mixer with the Non-powered Mixer met the standards. Hence, it is possible to reduce the energy consumption of 64,143 ~ 65,306 kWh/year since the Rapid-Mixer is replaced by the Non-powered Vortex Mixer.

• Magazine of the Korea Concrete Institute
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• v.10 no.2
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• pp.155-165
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• 1998

굳지 않은 콘크리트의 슬럼프손실을 저감시키기 위한 목적으로 고로슬래그 미분말 및 플라이애쉬의 혼합비율과 혼화제의 첨가방법을 변화시킨 콘크리트의 믹싱후 경과시간에 따른 슬럼프 변화에 대하여 고찰하였다. 연구결과 보통포틀랜드시멘트에 고로슬래그 비분말 또는 플라이애쉬를 혼합한 콘크리트가 혼화재를 혼합하지 않은 콘크리트보다 슬럼프손실을 줄일 수 있었으며, 고로슬래그 미분말과 플라이애쉬를 각각 50 및 5%를 혼합한 3성분계 콘크리트의 경우 슬럼프손실을 저감시키는데 유효하였다. 또한 혼화제의 일부를 15분후 분할하여 후첨가하는 혼합방법이 굳지않은 콘크리트의 슬럼프손실을 저감시키는데 가장 큰 효과가 있다. 한편 혼화재를 혼합한 3성분계 보통강도용 및 고강도용 콘크리트의 재령 28일까지의 압축강도는 혼화재를 혼합하지 않은 콘크리트보다 작았으나 재령 91일 압축강도는 31% 및 15%정도 크게 증가하였다.