• Journal of Advanced Marine Engineering and Technology
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• 제37권8호
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• pp.816-821
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• 2013

본 논문은 자연대류 상에서 수동적으로 냉각되는 다양한 하이브리드 휜들과 핀 휜의 열성능에 대한 수치연구결과를 보고한다. 연구된 하이브리드 휜들은 basic hybrid fin (BHF), hollow hybrid fin (HHF), solid hybrid fin (SHF) 이다. 다양한 방열율에 대한 HF들과 PF의 열성능을 조사하기 위해 CFD 휜 모델이 개발되었다. 휜들의 열성능은 각각의 휜에 대해 휜 베이스 면적에 대한 열전달계수, $h_a$와 질량에 대한 열전달계수, $h_m$ 을 정량화하여 분석되었다. 연구결과는 SHF의 $h_a$가 PF 보다 23% 더 큼을 보여주고, HHF의 $h_m$은 PF 보다 무려 140% 더 크며, HHF의 질량기반 성능, 즉 $h_m$은 BHF 보다 40% 더 우수함이 밝혀졌다.

• 설비공학논문집
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• 제8권1호
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• pp.120-139
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• 1996

Experiment was performed to study the heat transfer characteristics in 27 kinds of 15 : 1 scale models of multi-louverred fin heat exchangers with a wide range of variables(R $e_{Lp}$ =100~1, 800, $L_p$/F$p$=0.3~0.9, $\theta$=20$^{\circ}$~40$^{\circ}$). Thermofoil heaters were used to heat the louver fins and the local average Nusselt number for each louver in the louver array was obtained at constant wall temperature conditions. Correlations are developed to predict the heat transfer characteristics and drag coefficients. Generally, the heat transfer characteristics in the multi-louvered fins is shown to be similar to those of the laminar heat transfer on a flat plate. As the Reynolds number, the louver pitch to fin pitch ratio$L_p$/F$p$and the louver angle($\theta$) increase respectively, the average Nusselt number increases, but the variation of average Nusselt number as a function of the louver angle is smaller than that as a function of the louver pitch to fin pitch ratio. In case of$L_p$/F$p$ <0.5, the average Nusselt number of the 3rd louver is especially lower than the others, it is expected that it is due to the flow structure such as a recirculation flow and a flow separation.

• 대한기계학회논문집
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• 제17권5호
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• pp.1276-1293
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• 1993

본 연구는 위에서 언급된 모델보다 훨씬 폭이 큰 23.5mm 루버 핀형 방열기용 열교환기를 모델로 삼고, 레이놀즈수가 500 이하인 저 레이놀즈수(100, 300, 500), 루버 각(22˚,24˚,28˚) 및 핀 피치 와 루버 피치의 비 Fp /Lp(1.23, 1.5) 등의 변화 에 따른 핀 내부의 유동, 전열 특성 및 압력분포등의 영향을 유한차분법으로 수치해석 하였다. 또한 동일한 루버 핀에대해 13:1 모델을 제작하여 염료주입법에의한 유동의 가시화 실험을 하였으며, 그 결과를 수치해석 결과와 비교 검토하였다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2004년도 추계학술대회
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• pp.1046-1051
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• 2004

A plate-fin-tube heat exchanger used for a $SF_{6}$ gas-insulated transformer is extremely important since the dissipation of the heat generated from inside coils has a significant effect on the performance as well as the durability of the transformer. The heat exchanger consists of corrugated plate fins and staggered array tube bundles for coolant. In order to find out heat transfer and pressure drop characteristics, series of numerical analyses for plate fins with enhanced surface geometries were conducted. Based on the results of the numerical analyses, an improved model of the plate fin has been proposed.

• 대한기계학회논문집
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• 제17권9호
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• pp.2358-2372
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• 1993

In this study, the computer modeling for prediction of the performance of fin-tube heat exchanger using alternative refrigerant, HFC-134a was developed and the computer program for calculating the various properties of HFC-134a and the existing refrigerant CFC-12 and HCFC-22 was made. The heat exchanger modeling is based on a tube-by-tube approach, which is capable of analysis for the complex coil array. Performance of each tube is analyzed separately by considering the cross-flow heat transfer with external airstream and the appropriate heat and mass transfer relationships. A performance comparison according to the different refrigerants is provided using this developed model. As the result of this study, total heat transfer rate of evaporator and condenser using HFC-134a were found higher than that of using CFC-12 for the same operating conditions. When the mass flow rate of HFC-134a was less than CFC-12 about 18. 16%, the cooling capacities of evaporator were found to be the same.

• Journal of Advanced Marine Engineering and Technology
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• 제29권8호
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• pp.862-869
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• 2005

A study on convective cooling characteristics has been done in the channels with heat pipes and associated Plane fins Analysis with FLUENT V5.0 lies its Purpose on the possible enhancement of heat transfer capability between an existing three in-line arrayed heatpipes and an extending four in-line arrayed heatpipes with increasing channel width. Numerical analysis is limited to the laminar flow in an isolated flow channel by employing cyclic boundary conditions for calculation purposes. Friction factors for three and four in-line arrayed heatpipes are compared with experimental results. In addition, temperature behavior at the plate fin for the three in-line arrayed heatpipes is compared with experiment. Friction factors and overall channel heat transfer coefficients (and/or Nusselt numbers) are presented as a function of Reynolds number. An increase of number of heatpipes and channel width reults in a decrease of the friction factor and doesn't not result in an increase of heat transfer performance. However. considering the 25$\%$ increase of heat load accompanies with maximum 8$^{\circ}C$ rise of average temperature of heat pipes, the four in-line array with the increase of channel width of heat pipe heat sink can be considered appropriate.

• 대한기계학회논문집B
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• 제35권5호
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• pp.467-472
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• 2011

본 연구는 LED 조명기구와 같은 원형 모양에 적합한 원형 히트싱크의 주위의 열유동을 실험 및 해석적으로 분석하였다. 기존 복사 열전달을 고려하지 않은 상관식을 이용하여, 추가적으로 복사 열전달을 해석적으로 계산하였다. 본 해석 모델의 타당성을 실험적으로 확인하였다. 이 모델을 바탕으로 휜의 형상 및 열유속을 인자로 하여 히트싱크 평균 온도의 변화를 살펴보았다. 그 결과 열전달 성능을 최대로 할 수 있는 최적 휜의 길이가 존재하였고, 방사율이 클수록 형상 인자의 변화가 복사 열전달 변화에 미치는 영향이 상대적으로 감소하였다.

• 설비공학논문집
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• 제16권4호
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• pp.340-348
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• 2004

The air and refrigerant side heat transfer performances are key parameters to improve heat transfer efficiency of the heat exchanger including the fan performance. Design of the fins, treatment of the tube inside, tube diameter and tube array effect heat transfer performance of the heat exchanger. The heat exchanger is used as a condenser at cooling mode and used as an evaporator at heating mode in the heat pump system. The heat pump system uses R410A as the refrigerant. The heat exchangers are consisted with 7 mm diameter tubes with slit-type fins. The study was conducted with variation of arrangement of the refrigerant path and air flow rate and refrigerant pressure drop and heat transfer rate were measured with a code tester. The capacity of the 3 path heat exchanger is more efficient than 2 or 4 path heat exchangers in heating or cooling modes.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2009년도 하계학술발표대회 논문집
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• pp.1172-1176
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• 2009

In the present study, natural convection over a heat sink with a horizontal circular base and rectangular fins was numerically analyzed. To calculate natural convection heat transfer, the assumptions of ideal gas and laminar flow were made for air. Flow patterns around the heat sink were chimney-like. The resultant temperature distribution on the circular base appeared almost uniform. Parametric studies were performed to compare the effects of fin length, fin height, the ideal number of fins, and heat flux on the average temperature of a heat sink and the average heat transfer coefficient from the heat sink array. Correlation to predict the average Nusselt number was presented.

• 한국안전학회지
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• 제16권4호
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• pp.22-28
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• 2001

Heat transfer and pressure distribution for heat exchanger type of domestic gas boiler are different from shape, pitch, thickness of fin and array of pipe respectively. In order to measure the pressure distribution across the heat exchanger, a suction type wind tunnel was constructed and velocity distribution was measured for pilot tube(4 point) of rack type. The experiments were performed for 5 different air flow mass, rpm=3,6,9,12,15 and transverse axis of heat exchanger(x-length) is 5cm respectively. Results showed that above 9.5m/s, pressure distribution dispersion for wet type of heat exchanger is on the increase and above 5.5m/s, pressure distribution dispersion for dry type of heat exchanger is on the increase. Also, pressure distribution dispersion by comparing two different types heat exchanger, dry type of heat exchanger showed a higher augmentation than wet type of heat exchanger.