• International Journal of Aeronautical and Space Sciences
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• 제3권1호
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• pp.95-104
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• 2002

Numerical solution of the full Navier-Stokes equation as well as the energy equation has been obtained for the unsteady natural convection in a rectangular enclosure. One side wall was maintained at very high temperature simulating fires. Especially the effect of surface radiation was taken into account. While the enclosed air was assumed to be transparent, the internal walls directly interacted one another through the surface radiation. Due to a significant temperature difference in the flow field, the equation of state was used instead of the Boussinesq approximation. It was found that the rapid heating of the adiabatic ceiling and floor by the incoming radiation from the hot wall made the evolution at thermo-fluid field highly unstable in the initial period. Therefore, the secondary cells brought about at the floor region greatly affected the heat transfer mechanism inside the enclosure. The heat transfer rate was augmented by the radiation, resulting in requiring less time for the flow to reach the steady state. At the steady state neglecting radiation two internal hydraulic jumps were clearly observed in upper/left as well as in lower/right comer. However, the hydraulic jump in the lower/right comer could not be observed for the case including radiation due to its high momentum flow over the bottom wall. Radiation resulted in a faster establishment of the steady state phenomena.

• 에너지공학
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• 제24권1호
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• pp.97-103
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• 2015

파이프의 길이(Length)와 직경(Diameter), 거칠기(Roughness)에 변화를 주면서 수직 원형관내 자연대류 열전달을 측정하였다. 고부력 조건에 대한 높은 Rayleigh수를 구현하기 위하여 상사성에 기초한 물질전달실험을 수행하였다. Pr수는 2,014였다. 수직 원형관의 길이(L)는 0.1m, 0.3m, 0.5m였으며 이는 Gr수 $4.2{\times}10^7$, $1.1{\times}10^9$, $5.5{\times}10^9$에 해당한다. 각 수직 원형관에 대하여 직경(D)을 0.005m, 0.01m, 0.03m로 변화시키면서 열전달을 측정하였다. 실험결과 모든 직경(D)에 대해서 높이(L) 0.1m에서의 열전달 계수는 Le Fevre의 수직평판에 대한 층류 자연대류상관식과 일치하였다. 동일한 직경(D)에 대해서 길이(L)가 감소할수록 열전달이 증가하였다. 그리고 동일한 길이(L)에 대하여 직경(D)이 증가하였을 때는 열전달이 감소하였다. 파이프 내부 표면에 거칠기를 주어 일반 수직원형관과 열전달을 비교하였을 때, 층류영역에서는 열전달의 차이가 있었으나, 천이영역에서는 열전달 차이가 없었다.

• 대한기계학회논문집B
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• 제35권7호
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• pp.701-708
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• 2011

기울어진 평판에서 발생하는 자연대류 열전달현상을 $R_{a_L}$ $1.69{\times}10^{11}$과 $7.23{\times}10^{12}$에 대하여 실험적으로 연구하였다. 유사성을 이용하여 열전달실험을 물질전달 실험으로 대체하였고 물질전달계로 전기도금계를 사용하였다. 평판의 기울기는 상향수평에서 하향수평까지 $10^{\circ}$씩 변화시켰다. 하향평판에서는 수직 벽면에 대한 자연대류 열전달 상관식에서 g 대신 g $cos{\theta}$로 대체함으로써 열전달계수를 구할 수 있다는 기존의 이론과 일치하는 결과를 얻었다. 상향평판의 경우 경계층이 벽면을 따라 발달되는 경우와 벽면으로부터 박리되는 2가지 영역으로 구분되는데 박리에 따른 열전달 증가를 확인하였다. 아울러 도금패턴을 이용하여 박리지점을 시각화하였고 박리지점에 대한 분석이 수행되었다.

• Journal of the Korean Society for Industrial and Applied Mathematics
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• 제12권4호
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• pp.201-202
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• 2008

Because of the importance of suction or injection in the fields of aerodynamics, space science and many other industrial applications, our present study is motivated. The effect of natural convection on MHD flow past a vertical plate with suction or injection is studied. We have tried to solve the dimensionless governing equations by using finite difference scheme. To ensure the validity of our numerical solutions, we have compared our numerical solutions for temperature and velocity for the case of suction and injection for unit Prandtl number with the available exact solutions in the literature. The corresponding codes were written in Mathematica 5.0 for calculating numerical solutions for temperature and velocity and the comparison between the exact and numerical solutions. For the purpose of discussing the results some numerical calculations are carried out for non-dimensional temperature T, velocity u, skin friction ${\tau}$ and the Nusselt number $N_u$, by making use of it, the rate of heat transfer is studied.

• 한국전산유체공학회:학술대회논문집
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• 한국전산유체공학회 2000년도 추계 학술대회논문집
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• pp.66-71
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• 2000

In the present study a numerical simulation is performed on a natural convection inside a square cavity with a vibrating bottom wall. The heat transfer coeffcients for various amplitudes of the bottom wall vibration were compared to the case without the bottom wall excitation. From the results, it is seen that the local temperature distribution in a cavity becomes more uniform as the amplitude of the bottom wall vibration is increased. Also, it was seen that the heat transfer coefficient increased on the heating wall as the applied amplitude increased.

• 대한기계학회논문집
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• 제15권2호
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• pp.654-660
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• 1991

Natural convection heat transfer in a horizontal annulus from an inner tube with two vertical fins has been studied for the effects of dimensionless fin length and Rayleigh number. The maximum local Nusselt number of inner tube was obtained at .theta. = 145.deg. and that of outer cylinder at .theta. = 0.deg. for the case of $l_{F}$=0.3 Local Nusselt number distributions for the lower fins show higher values than that of the upper fins. The mean Nusselt number of inner tube was increased with the values of dimensionless fin length. The mean Nusselt number can be represented in an exponential function of Grashof number at various fin lengths. As compared with experimental and numerical results, isotherms and local Nusselt number show good agreement.t.

• 태양에너지
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• 제12권1호
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• pp.25-33
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• 1992

정상상태에서 고온부가 존재하는 밀폐공간내의 자연대류 열전달을 $Gr=1.5{\times}10^5$, Pr=0.71 및 $k_s/k_f=14710$ 조건에서 경사각을 변화시켜 연구하였다. 고온부는 밀폐공간 면적의 1/25 을 차지하고 형상비는 1.0이다. 전체평균 누셀트 수는 경사각을 증가시키면 감소하였고 ${\theta}=90^{\circ}$인 경우가 ${\theta}=0^{\circ}$ 일때보다 14% 낮게 나타났다.

• 태양에너지
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• 제4권2호
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• pp.43-49
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• 1984

Experiments were performed to study freezing on a finned vertical tube when either conduction in the solid or natural convection in a liquid controls the heat transfer. Conduction is the controlling mode when the liquid is at its fusion temperature, whereas natural convection controls when the liquid temperature is above the fusion value. The liquid was housed in a cylinderical containment vessel whose surface was maintained at a uniform, time-invariment temperature during a data run, and the freezing occurred on a finned vertical tube positioned along the axis of the vessel. The phase change medium was n-octacosan, a paraffin which freezes at about $61^{\circ}C$. For conduction-controlled freezing, the enhancement of the frozen mass due to finning is greatest when the frozen layer is thin and decrease as the layer grows thicker. The degree of enhancement is generally less than the surface area ratio of the finned and unfinned tube.

• 오토저널
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• 제10권1호
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• pp.26-32
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• 1988

A study has been conducted experimentally on the natural convection heat transfer characteristics of fin arrays on a horizontal flat plate in air. The effects of fin heights and Rayleigh numbers are mainly investigated. The experimental results are as follows; 1. The mean fin and mean total Nusselt numbers increase as dimensionless fin heights increase at 0.67.leg.H/s.leg.1.67. The mean plate Nusselt numbers increase in case of upward facing fins, but they decrease in case of downward facing fins. 2. The mean Nusselt numbers increase as Rayleigh numbers increase. 3. The mean fin surface Nusselt numbers has its maximum outside surface (Y$_{1}$) where there is no interference from each other fin. 4. The mean total Nusselt numbers in case of upward facing fins increase by 47% and 26%, respectively at H/S=0.67 and 1.67 than those in case of downward facing fins for Ra$_{s}$=6.50*10$^{3}$.>.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2005년도 동계학술발표대회 논문집
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• pp.539-545
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• 2005

In this paper, the thermal characteristics of natural convection in a rectangular cavity with nanofluids such as water-based nanofluids containing alumina are theoretically investigated with a new model of the thermal conductivity for nanofluids presented by Jang and Choi and various models for effective viscosity. In addition, based on theoretical results, the effects of various parameters such as the volume fraction, the temperature, and the size of nanoparticles on free convective instability and heat transfer characteristics in a rectangular cavity with nanofluids are suggested.