• 한국응용과학기술학회지
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• 제34권4호
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• pp.908-914
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• 2017

본 연구는 냉동공조용 열교환기 내 스케일 형성으로 열전달 과정에서 열저항으로 작용하여 냉동공조시스템의 냉각성능이 떨어져 이를 해결하기 위해 전기분해 원리를 이용하여 배관 내 스케일을 자동 제거하는 시스템을 개발하여 그 성능을 실험을 통해 확인하고자 한다. 이전까지는 배관 내 스케일을 2~3년에 한번씩 브러시나 분사 노즐에 의해 기계적으로 배관 내를 청소를 하거나 화학약품을 이용하여 세관하였다. 이러한 세관은 시간이 경과하면 또 관이 오염되어 전열성능이 떨어지고 냉각장치의 운전을 정지하여 반복해야 하는 여러 가지 문제점을 안고 있었다. 따라서 시스템의 정지없이 전기분해 원리를 이용하여 만들어진 처리수를 순환시킴으로서 스케일의 원인물질은 Ca, Mg, $SiO_2$를 고형물 형태로 석출시켜 배관계 외부로 배출시킴으로서 배관내 스케일 발생을 차단하고 기 형성된 스케일을 제거하여 배관의 전열 성능을 유지하고자 하는 것이다. 실험한 결과, 새 배관의 열전달율을 100으로 기준할 경우, 스케일이 형성된 배관의 열전달율은 86.66%이었으며, 스케일이 형성된 배관을 1개월 동안 처리수를 가동했을 경우 열전달율은 90.5%의 수준까지 회복되었으며, 2개월간 운전한 경우 97.86%의 수준까지, 3개월 운전했을 경우 98.72%까지 열전달율이 회복되었다. 비교적 짧은 실험기간이지만 배관내 형성된 스케일의 제거효과를 파악하였으며, 전열성능에도 영향을 미치고 있음을 확인하였다.

• 대한기계학회논문집B
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• 제25권2호
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• pp.180-186
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• 2001

The condensation heat transfer coefficients of pure refrigerants R-22, R-134a, and a binary refrigerant mixture R-410A flowing in a small diameter tube were investigated. The experiment apparatus consists of a refrigerant loop and a water loop. The main components of the refrigerant loop consist of a variable-speed pump, a mass flowmeter, an evaporator, and a condenser(test section). The water loop consists of a variable-speed pump, an isothermal tank, and a flowmeter. The condenser 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 copper tube of 3.38mm outer diameter and 1.77mm inner diameter. The length of test section is 1220mm. The refrigerant mass fluxes varied from 450 to 1050kg/(㎡$.$s) and the average inlet and outlet qualities were 0.05 and 0.95, respectively. The main results were summarized as follows ; in the case of single-phase flow, the heat transfer coefficients increase with increasing mass flux. The heat transfer coefficient of R-410A was higher than that of R-22 and R-134a, and the heat transfer for small diameter tubes were about 20% to 27% higher than those predicted by Gnielinski. In the case of two-phase flow, the heat transfer coefficients also increase with increasing mass flux and quality. The condensation heat transfer coefficient of R-410A was slightly higher than that of R-22 and R-134a. Most of correlations proposed in the large diameter tube showed significant deviations with experimental data except for the ranges of low quality and low mass flux.

• 한국공작기계학회논문집
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• 제10권1호
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• pp.65-70
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• 2001

The hear transfer mechanism initiating the friction welding is examined and a transient three dimensional heat conduc-tion model for the welding of two dissimilar cylindrical metal bars is investigated. The cylindrical metal bars are made of materials made of A2024 and SM 45C. Numerical simulations of heat flow are performed using the finite volume method. Respectively. Commercial FLUENT code is used in the heat flow simulation and maximum temperature and distribution of temperature are calculated. Temperature of friction welded joining face is compared with the temperature distribution measured by experiment and numerical simulation. The maximum temperature of friction welded joining face is lower than melting point of A2024-T6 aluminum alloy using insert metal. The temperature distribution of friction welded join- ing face with insert metal is more uniform than that of without inset metal.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2006년도 하계학술발표대회 논문집
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• pp.111-115
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• 2006

To clarify the hydraulic and thermal characteristics of ice slurry which made from 6.5% ethylene glycol-water solution flow in the double tube and plate type heat exchanger, experimental studies were performed. The mass flux and Ice fraction of ice slurry were varied from 800 to $3,500 kg/m^2s$(or 7 to 17 kg/min) and from 0 to 25%, respectively. During the experiment, it was found that the measured pressure drop and heat transfer rate increase with the mass flux and ice fraction; however the effect of ice fraction appears not to be significant at high mass flux region. At the region of low mass flux, a sharp increase in the pressure drop and heat transfer rate were observed depends on mass flux.

• Journal of Advanced Marine Engineering and Technology
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• 제14권4호
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• pp.57-66
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• 1990

In the design of an electric power plant, the capacity to meet the peak load demand is one of the important factors to be considered. This peak load usually occurs when the most of the cooling air conditioning systems are being operated during daytime in summer season, which inevitably entails the construction of an additional electric power plant. This study is aimed to carry out a basic experiment for the development of a cooling air conditioning system using the ice energy by the surplus electric power during the night-time. The experimental apparatus consists of four major parts; (1) the heating section consisting of the air duct and I.D. fan, (2) the cold section with the ice chamber, (3) the bundle of heat pipes made in a form of the staggered arrangement with ${C_y}/{d_o}$=2.0 and ${C_x}/{d_o}$=1.73, (4) the refrigerator system to cool down the ice chamber. This study involves an intensive experiment concerning the convective heat transfer of the air flow surrounding the bundle of heat pipes. This major experimental parameters are the amount of working fluid, the velocity of air and the working temperature. The major findings of the present study are as follows; (1) The optimum amount of the working fluid necessary for the horizontal heat pipes is much more than that for the vertical type. (2) The convective heat transfer coefficients of the air are coincided with the empirical equations of Grimson and ${\breve{Z}ukauskas}$. (3) The equation of the mean heat transfer coefficient obtained in the present study is ${N_um}=0.32 {Re_max^{0.63}}$.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2000년도 춘계학술대회논문집B
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• pp.104-107
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• 2000

Evaporative heat transfer characteristics of carbon dioxide has been investigated. Experiment has been carried out for seamless stainless steel tube with outer diameter of 9.55 mm and inner diameter of 7.75 mm. Direct heating method is used for supplying heat to the refrigerant was uniformly heated by electric current which was applied to the tube wall. The saturation temperature of refrigerant is calculated from the measured saturation pressure by using an equation of state. Inner wall temperature was calculated from measured outer wall temperature, accounting for heat generation in the tube and heat conduction through the tube wall. Mass Quality of refrigerant was calculated by considering energy balance in the preheater and the test section. Heat fluxes were set at 12, 16, 20, 23, and $27kW/m^2$, mass fluxes were controlled at 212, 318, 424, and $530 kg/m^2s$, and saturation temperature of refrigerant were adjusted at 0, 3.4, 6.7 and $10.5^{\circ}C$. From this study, heat transfer coefficients of carbon dioxide have been provided with respect to quality for several mass fluxes, heat fluxes. Finally, the experimental results in this study are compared with the correaltion by Gungor and Winterton(1987).

• 대한기계학회논문집B
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• 제38권3호
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• pp.255-262
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• 2014

판형열교환기의 증발과정에서 오일에 위한 영향을 알아보기 위해 마이크로 기어 펌프를 이용한 냉매-R134a 순환 성능실험 장치를 구성하여, 증발열전달 실험을 수행하였다. POE 오일을 펌프를 이용하여 냉매 질량 유량에 비례하도록 0~5%를 첨가하여, 오일순환량에 따른 열전달계수 변화를 측정하였다. 오일순환율이 증가할수록 R134a 증발 열전달계수는 감소하며, 압력손실은 증가한다. 질량유량 80 g/s, 증발 온도 $30^{\circ}C$ 일 때, 오일 순환율 2%조건에서 무오일 대비 약 10%의 열전달계수가 감소하였고, 압력손실은 약 10% 증가하였다.

• Journal of Advanced Marine Engineering and Technology
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• 제36권8호
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• pp.1016-1023
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• 2012

열교환기는 다수의 원관으로 구성하고 있기 때문에 원관 주위에서 국소열전달과 압력강하의 해석, 크기의 성능과 추산, 경제성으로 설계 시 중요한 역할을 한다. 본 연구에서는 어긋나기배열 직교류 열교환기에서 물의 온도 및 공기량 변화에 따른 대류열전달계수, 대수평균온도차, 압력손실 등을 고찰하기 위하여 실험 및 해석을 수행하였다. 본 열교환기는 관군이 5행 7열 어긋나기배열로서 구성하였으며, 실험 및 해석 조건은 물의 온도는 $40^{\circ}C{\sim}65^{\circ}C$ 범위이고, 공기량은 $5.0{\sim}12.3m^3/s$ 범위이다. 그 결과로서 물의 온도 및 유량을 증가함에 따라 공기밀도가 감소하여 유속도 낮아지는 특성을 보여 레이놀즈수가 감소하고, 공기량 증대로 평균열전달계수가 증가하여 전열성능은 향상됨을 알 수 있었고, 압력손실도 증가하였다. 그리고 해석결과로서는 열전달율의 경우는 약 8~12%, 압력강하는 약 0.01~7.5% 오차를 나타내어 본 연구의 적합성을 평가할 수 있었다.

• 대한설비공학회지:설비저널
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• 제17권3호
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• pp.230-237
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• 1988

An experiment was carried out to study the condensation heat transfer enhancement of horizontal circular cylinders with varying outside surface configurations. The refrigerant used is Freon-22 and the test condensing temperature is 34.1C. Pin-finned tube shows about 2.5-3.5 times higher overall heat transfer coefficient compared to that of smooth surface tube, thus has larger encomic benifit for condenser design. The condensation heat transfer coefficient was shown to increase as the fin-pitch of the pin-finned tube decreases for film Reynolds number larger than 100.

• 설비공학논문집
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• 제12권5호
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• pp.457-465
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• 2000

An experiment was carried out to evaluate the thermal performance of the wire-coil inserts method. Tested were the smooth tubes with the wire-nil inserts of various pitch and helix angle combinations. Test fluids were the 50%-solution of the ethylene glycol and the Hue water. Heat transfer coefficient and friction factors were deduced from the measured values of temperatures, flowrates and pressure drops. A unified dimensionless correlation for the heat transfer coefficients was developed as a function of the pitch to diameter ratio, the Reynolds number and the Prandtl number. An exergy analysis was performed to evaluate an optimal operating condition with the wire-coil inserts.