• Journal of the Korean Society of Mechanical Technology
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• v.13 no.3
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• pp.1-6
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• 2011

In order to find better performance of heat sink, in this research, different cases were analysed by changing number of slots and shape of fins. Round shape fins which have wide surface showed 24% better heat transfer rate than vertical fins. There were not big discrepancies between 1 slot and 2 slots fins. Consequently, for better performance of heat sink, developments for widening surface and better material for high heat transfer rate are needed.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.12 no.9
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• pp.3808-3814
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• 2011

The prediction of heat transfer and pressure drops in the exchanger passages is a clue to the problem of heat exchanger design. In order to make such predictions for non-Newtonian fluids, it is necessary to know the relation between the viscous properties of the fluid and the wall shear rate in the duct. This study deals with the limits of validity of the power law equation. The useful methodology of the present research involves a consideration of a more general equation which has power law and Newtonian behavior as asymptotes. It isconcluded that use of the power law equation outside of its applicability range can lead to serious errors inpredicting the heat transfer and pressure drops. The present computational results of the friction factors times Reynolds number for shear-thinning fluid flows in a triangular duct are compared with previous published results, showing agreement with 0.13 % in Newtonian region and 2.85 % in power law region. These shear-thinning fluid results also showed the 12% increase of convective heat transfer enhancement compared with Newtonian heat transfer.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.5 no.5
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• pp.421-428
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• 2004

This study concerns the characteristics of boiling heat transfer in two-phase closed thermosyphons with various micro grooves. A study was carried out with the performance of the heat transfer of the thermosyphon having 60 internal micro grooves in which boiling and condensation occur. A plain thermosyphon having the same inner and outer diameter as the grooved thermosyphon is also tested for comparison. Distilled water, methanol, ethanol have been used as the working fluid. The heat flux and the boiling heat transfer coefficient at the evaporator zone are estimated from the experimental results. The experimental results have been assessed and compared with existing correlations. Imura's and Kusuda's correlation for boiling showed in good agreement with experimental results within ${\pm}20{\%}$ in plain thermosyphon.

• Journal of Advanced Marine Engineering and Technology
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• v.38 no.4
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• pp.367-375
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• 2014

In numbers of kinds of heat exchanger, the shell-tube heat exchanger is the most commonly used type of heat exchanger in the industry field. In order to improve the thermal performance of the heat exchanger, this study was analyzed heat transfer characteristics according to arrangement of baffle and direction of baffle and bump phase of baffle about shell-tube heat exchanger using appropriate SST (Shear Stress Transport) turbulence model for flow separation and boundary layer analysis. As the boundary condition for CFD (Computational Fluid Dynamics) analysis, the inlet temperature of shell side was constantly 344 K and the variation of the water flow rate was 6, 12, 18 and 24 l/min. As the result of analysis, zigzag baffle arrangement enhances heat transfer rate and pressure drop. Furthermore, in the direction of the baffle, heat transfer rate is more improved with vertical type and angle $45^{\circ}$ type than existing type, and pressure drop was little difference. Also, the bump shape of baffle surface contributes to heat transfer rate and pressure drop improvement due to the increased heat transfer area. Through analysis results, we knew that the increase of the heat transfer was influenced by flow separation, fluid residual time, contact area with the tube, flow rate, swirl and so on.

• Journal of the KSME
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• v.35 no.7
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• pp.638-646
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• 1995

직접접촉 얼교환 기술은 냉각탑, 접촉급수 가열기 및 공기분리기 등과 같은 장치에 예전부터 이용되어 왔는데, 그 주요한 적용이유는 가열유체와 수열유체의 사이에 일어나는 전열이 일반 열교환기와는 달리 고체벽(금속 열전달표면)을 통과하지 않고 열교환을 함으로써, 종래의 열교 환기에 비하여 상대적으로 설비의 간단화, 부식 및 스케일 부착문제가 경감됨에 따른 적은 유 지보수비 및 높은 열전달률을 얻을수 있는 이점이 있으며, 저 온도차에서의 효율적인 사용이 가능하기 때문이다. 이 글에서는 직접접촉응축 현상의 장점을 이용하는 직접접촉식 교환기의 구조와 형태, 그리고 그 응용분야에 대해서 알아보고자 한다.

• Journal of Korea Society of Industrial Information Systems
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• v.29 no.1
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• pp.117-123
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• 2024

Bubbles generated in water receive an upward buoyant force due to the density and pressure difference of the surrounding fluid. Additionally, the behavior, shape, and heat exchange process of bubbles vary depending on the viscosity, surface tension, rising speed, and size difference with the surrounding fluid. In this study, we modeled speed, and heat transfer of a high-temperature single bubble rising in a cylindrical water tank. For this purpose, velocity, and temperature of the bubbles were calculated using theoretical equations, to be compared with numerical simulation results. The numerical analysis was performed using a commercial software, and the stability of the numerical analysis with mesh size was confirmed through calculation of the grid convergence index. The numerical analysis of the rising speed and temperature of a single bubble showed the values to converge when the minimum cell size was 1/160 of the bubble diameter, and the temperature decrease was confirmed to be the same as that of the surrounding fluid within 0.05 seconds.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.37 no.8
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• pp.753-758
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• 2013

In this study, two proposals for the wall heating preconverter of an MCFC are numerically studied to resolve hot temperature generation near the wall by the low thermal conductivity of the catalyst. The numerical results show that the inserted porous cupper plates on the catalyst evidently improve heat transfer and realize more uniform reforming in the preconverter. The calculated results for the preconverter with a circumference empty space of catalyst located at center, 1/2 and 4/5 from center line are compared. The circumference empty space located at 1/2 position shows better results than other cases, but the positive effect on the uniform reforming process is less than in the case of inserted cupper porous plates on the catalyst.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2011.05a
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• pp.191-191
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• 2011

유체 플라즈마 공정(SPP)은 최신 나노기술과 열전달 유체 기술이 융합된 나노유체(Nanofluids)를 제조하는 공정이다. 본 연구에서는 이런 유체 플라즈마 공정에서 공정시간과 음극파워비율에 따라 금 나노유체 제조시 사용되는 전극에 미치는 영향을 알아보기 위해 특성분석을 실시하였다. 그 결과 전극의 양극에서는 염화금 이온이 전극에 증착되었고 음극에서는 부식에 의해 무게가 감소하였다.

• Transactions of the Korean Society of Mechanical Engineers
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• v.8 no.5
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• pp.505-515
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• 1984

동일한 물리적인 인자와 경계조건하에서, 서로 다른 두 개 이상의 유동이나 열전달이 발생되는 다중정상상태에 대한 현상은 최근 자연과학이나 공업분야에서 매우 중요시 되어지고 있다. 그 한 예로서 -0.1988<.betha.<0 영역에서 쐐기면에 따른 유동현상이 다중정상상태가 됨을 Stewrtson에 의해 밝혀진 바 있다. 이 영역에서 주위유체가 공기(Pr=0.72)이고, 쐐기 면이 여러 가지 열유속을 가지는 경우에 대해서 강제대유열전달을 multiple shooting방법으로 현론해석하 였다. 그 결과, 상이한 두 개의 열전달매개변수 즉 다중해가 얻어져서 다중정상상태의 강제대류 열전달이 일어남을 알았다.

• Transactions of the Korean Society of Mechanical Engineers
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• v.10 no.5
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• pp.706-712
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• 1986

The unsteay heat transfer from an isothermal circular cylinder in fluctuating cross flow is simulated numerically, for the case where the amplitude of the oscillating velocity is small compared with the mean velocity. By solving the linear perturbation equations derived from the unsteady full Navier-Stokes and the energy equations, the amplitude and the phase of heat transfer response are obtained in the range of Reynolds number R$_{3}$ < 40. The effects of the velocity, the cylinder radius and the frequency on the response are expressed graphically in terms of the normalized velocity and the cylinder radius.