• 대한기계학회:학술대회논문집
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• 대한기계학회 2001년도 추계학술대회논문집B
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• pp.191-198
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• 2001

A numerical analysis of the heat and mass transfer and pressure drop characteristics in modular shell and tube bundle heat exchanger was carried out. Finite Concept Method based on FVM and $k-\varepsilon$ turbulent model were used for this analysis. Condensation heat transfer enhanced total heat transfer rate $4\sim8%$ higher than that of dry heat exchanger. With increasing humid air inlet velocity, temperature and relative humidity, and with decreasing heat exchanger aspect ratio and cooling water velocity, total heat and mass transfer rate could be increased. Cooling water inlet velocity had little effect on total heat transfer.

• 한국환경과학회지
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• 제8권1호
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• pp.61-67
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• 1999

Silicone oil has organic and inorganic properties, and its skeleton is polysiloxane bonding that silicon is bonded hydrogen or organic group. Silicone compounds are very smooth and lubricant properties by low surface tension, low temperature dependence, and nonadhesive properties. Because of these properties, silicone compounds are used as many parts of chemicals, softener, smooth and libricant agents, water-repellent agent, and defoaming agent, etc. Emulsion was prepared with the inversion emulsification method which adopted the agent-in-oil method dissolving the polyoxyethylene(7) tridecyl ether(HLB 12.2) into methoxy terminated poly(dimethyl-co-methyl amino) siloxane and hydroxy terminated poly(dimethyl-co-methyl amino) siloxane in water. At this time, processed emulsion was almost microemulsion. When ratio of emulsifier increases, emulsion is stable bacuause microemulsion is solubilized by emulsion drop size and zeta-potential are decreased. But, when amount of electrolyte is increase, emulsion became unstable because emulsion drop size is increased.

• 한국해양공학회지
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• 제20권4호
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• pp.64-69
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• 2006

A numerical analysis is made to investigate the wave absorption efficiency of a OWC-type wave power generator. Energy absorption by an OWC(Oscillating Water Column) air-chamber is computed in regular waves, taking account of the oscillating surface-pressure, due to pressure drop, across the duct of the air chamber. The problem is formulated in the scope of potential theory and solved by the Localized Finite Element Method(LFEM), based on the classical variational principle. The efficiency of energy absorption is investigated by. changing wave conditions, sea-bottom slope and pressure drop coefficient.

• 설비공학논문집
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• 제16권12호
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• pp.1227-1233
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• 2004

Air handling unit (AHU)'s air filter pressure difference is important for energy consumption and indoor air quality. Both energy Performance data and air filter differential pressure of AHU in real office buildings were monitored and analyzed to investigate quantitatively energy impact as dust buildup level on air filter grows. We also modeled and simulated CAV system using HVACSIM＋ program to examine the energy effect of dust buildup on filters. Through analysis of time series pressure drop data, the filter pressure difference rate has been increased due to cumulative supply air flow rate increase. As filter pressure drop increased to 1 inch water column, it is found that the supply air flow rate was decreased by 10%, the chilled water flow rate was increased by 5.9% and the pump energy consumption was increased to 5.9%.

• 한국유체기계학회 논문집
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• 제10권2호
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• pp.41-45
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• 2007

The shutoff unit was designed to provide rapid insertion of neutron absorbing material into the reactor core to shutdown the reactor quickly and also to withdraw the absorber slowly to avoid a log-rate trip. Four shutoff units were installed on the HANARO reactor but the half-core test facility was equipped with one shutoff unit. The reactor trip or shutdown is accomplished by four shutoff units by insertion of the shutoff rods. The shutoff rod(SOR) is actuated by a directly linked hydraulic cylinder on the reactor chimney, which is pressurized by a hydraulic pump. The rod is released to drop by gravity, when triplicate solenoid valves are de-energized to vent the cylinder. The hydraulic pump, pipe and air supply system are provided to be similar with the HANARO reactor. The shutoff rod drops for 647mm stroke within 1.13 seconds to shut down the reactor and it is slowly inserted to the full down position, 700mm, with a damping. We have conducted the drop test of the shutoff rod in order to show the performance and the structural integrity of operating system of the shutoff unit. The present paper deals with the 647mm drop time and the withdrawal time according to variation of the pool water temperature, the water level and the core flow.

• 신재생에너지
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• 제16권1호
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• pp.47-57
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• 2020

In Floating PV (Photovoltaic) systems, PV modules are installed on water by utilizing the surface of idle water such as a reservoir and multipurpose dam. A floating PV system, therefore, has the advantage of efficiency in national land use and improved energy yield owing to cooling effect compared to on-land PV systems. Owing to the limitation of installation environment for a floating PV system, the system, however, has the disadvantage of an increase in transmission distance of DC (Direct current) cables. A longer transmission distance of a DC cable results in greater power loss due to a voltage drop. This leads to a decline in economic feasibility for the floating PV system. In this paper, the economic analysis for 10 floating PV systems installed in a reservoir has been conducted in terms of a change in annual power sales according to the variation of transmission losses depending on the factors affecting the voltage drop, such as transmission distance, cross-section area of underwater cable, the presence of joint box, and PV capacity.

• Journal of Advanced Marine Engineering and Technology
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• 제28권1호
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• pp.65-74
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• 2004

The heat transfer coefficient and pressure drop of $CO_2$(R-744) during gas cooling Process of carbon dioxide in a horizontal tube were investigated experimentally and theoretically. The experiments were conducted without oil in the refrigerant loop. The main components of the refrigerant loop consist of a receiver. a variable-speed pump. a mass flowmeter, an evaporator. and a gas cooler(test section). The main components of the water loop consist of a variable-speed Pump. an constant temperature bath. and a flowmeter. The gas cooler is a counterflow heat exchanger with refrigerant flowing in the inner tube and water flowing in the annulus The test section consists of smooth, horizontal stainless steel tube of 9.53 mm outer diameter and 7.75 mm inner diameter. The length of test section is 6 m. The refrigerant mass fluxes were 200 ~ 300 kg/($m^2{\cdot}s$) and the inlet pressure of the gas cooler varied from 7.5 MPa to 8.5 MPa. The main results were summarized as follows : The predicted correlation can evaluated the R-744 exit temperature from the gas cooler within ${\pm}10%$ for most of the experimental data, given only the inlet conditions. The predicted gas cooley capacity using log mean temperature difference showed relatively food agreement with gas cooler capacity within ${\pm}5%$. The pressure drop predicted by Blasius estimated the pressure drop on the $CO_2$ side within ${\pm}4.3%$. The predicted heat transfer coefficients using Gnielinski's correlation evaluated the heat transfer coefficients on the $CO_2$ side well within the range of experimental error. The predicted heat transfer coefficients using Gao and Honda's correlation estimated the heat transfer coefficients on the coolant side well within ${\pm}10\;%$. Therefore. The predicted equation's usefulness is demonstrated by analyzing data obtained in experiments.

• 한국산학기술학회논문지
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• 제20권1호
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• pp.21-27
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• 2019

그간 소형 제빙기에는 R-404A가 사용되어 왔으나 지구 온난화와 관련하여 대체 냉매 적용이 시급한 실정이다. 본 연구에서는 제빙기에 적용되어 온 R-404A를 대체할 R-448A와 R-449A에 대하여 drop-in test를 수행하였다. 시험은 외기 온도와 증발판에 공급되는 물 온도를 변화시키며 수행되었다. 실험 결과 R-404A의 일 평균 제빙량은 R-448A보다는 5.3%, R-449A보다는 4.2% 크게 나타났다. 이는 R-404A의 기체 밀도가 커서 냉매 순환량이 증가하기 때문으로 판단된다. 한편 R-448A와 R-449A의 제빙량을 비교하면 외기온도나 믈 온도가 낮아 제빙량이 많으면 R-448A가, 외기 온도나 물 온도가 높으면 R-449A가 우수한 성능을 보인다. 일 평균 소비 전력량은 R-448A나 R-449A보다 R-404A에서 대략 10% 크게 나타났다. 한편 성적계수의 경우 R-448A와 R-449A는 거의 동일하고 R-404A의 값보다는 3.0% 크게 나타났다. 현재 R-448A, R-449A의 증발, 응축 열전달에 대한 데이터가 부족한 실정으로 향후 이 부분에 대한 기초 연구가 필요할 것으로 판단된다.

• Korean Chemical Engineering Research
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• 제47권1호
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• pp.46-53
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• 2009

본 연구에서는 비이온 계면활성제 $C_{12}E_5$ 수용액과 비극성 탄화수소 오일 시스템에 대한 상평형 및 동적 거동 실험을 수행하였다. 온도를 증가시킴에 따라 oil-in-water(O/W) microemulsion(${\mu}E$)이 excess 오일상과 평형을 이루는 2상 영역으로부터 middle-phase ${\mu}E$이 excess water, excess 오일상과 각각 평형을 이루는 3상 영역을 거쳐서 water-in-oil(W/O) ${\mu}E$이 excess 물상과 평형을 이루는 2상으로 전이되었다. 또한 탄화수소 오일의 사슬 길이가 증가할수록 상전이 온도가 증가하였다. O/W ${\mu}E$이 존재하는 낮은 온도 조건에서는 비극성 오일의 종류와 상관없이 오일이 계면활성제 마이셀에 의하여 가용화되어 시간에 따라 크기가 선형적으로 감소하였다. 한편 middle-phase ${\mu}E$을 포함한 3상이 형성되는 조건에서는 매우 낮은 계면장력으로 인하여 오일이 수용액 상에 빠른 속도로 가용화되었고 작은 drop 형태로 유화되었다. 반면에 W/O ${\mu}E$의 2상을 형성하는 온도에서는 과포화로 인하여 일어나는 자발적 유화 현상과 물과 계면활성제의 오일상으로의 확산으로 인한 오일의 크기가 증가하였다. 비극성 탄화수소 오일과 계면활성제 수용액 사이의 시간에 따른 계면장력을 $25^{\circ}C$에서 측정한 결과, 탄화수소 오일의 사슬 길이가 증가함에 따라 평형에서의 계면장력 값과 평형에 도달하는데 소요되는 시간이 모두 증가하였다.

• 공업화학
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• 제20권5호
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• pp.473-478
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• 2009

본 연구에서는 $C_{10}E_5$ 비이온 계면활성제 수용액과 비극성 탄화수소 오일 시스템에 대한 상평형 및 동적 거동 실험을 수행하였다. 온도를 증가시킴에 따라 oil in water (O/W) microemulsion (${\mu}E$)이 excess 오일상과 평형을 이루는 2상 영역으로부터 middle-phase ${\mu}E$이 excess water, excess 오일상과 각각 평형을 이루는 3상 영역을 거쳐서 water in oil (W/O)${\mu}E$이 excess 물상과 평형을 이루는 2상으로 전이되었다. 또한 탄화수소 오일의 사슬 길이가 증가할수록 상전이 온도가 증가하였다. O/W ${\mu}E$이 존재하는 낮은 온도 조건에서는 비극성 오일의 종류와 상관없이 오일이 계면활성제 마이셀에 의하여 가용화되어 시간에 따라 크기가 선형적으로 감소하였고, 가용화 속도는 탄화수소 오일의 사슬 길이를 증가시킴에 따라서 감소하였다. 한편 middle-phase ${\mu}E$을 포함한 3상이 형성되는 조건에서는 매우 낮은 계면장력으로 인하여 오일이 수용액 상에 빠른 속도로 가용화되었고 작은 drop 형태로 유화되었다. 반면에 W/O ${\mu}E$의 2상을 형성하는 온도에서는 과포화로 인하여 일어나는 자발적 유화 현상과 물과 계면활성제의 오일상으로의 확산으로 인한 오일의 크기 증가가 관찰되었다. 비극성 탄화수소 오일과 계면활성제 수용액 사이의 시간에 따른 계면장력을 $25^{\circ}C$에서 측정한 결과, 탄화수소 오일의 사슬 길이 증가에 따라 평형에서의 계면장력 값과 평형에 도달하는 데 소요되는 시간이 모두 증가하였다.