• 한국추진공학회지
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• 제6권3호
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• pp.37-43
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• 2002

지금까지 많은 열전달 계수의 측정에 관한 연구가 수행되고 있다. 본 논문에서는 액정을 이용하여 국소 열전달 계수를 측정하는 방법을 다루고 있다. 과도방법과 정상방법을 사용하여 실린더 표면의 지역적인 열전달 계수를 측정하였다. 정상상태일 때는 금박막 필름으로 실린더를 코팅하여 실험하였고, 과도방법일 때는 삽입기법과 바이패스 기법으로 각각 실험하였으며, 두 경우 모두 열풍동을 이용하여 실린더를 가열시키는 방법과 냉각시키는 방법으로 각각 실험하였다. 이와 같은 실험으로 과도방법과 정상방법을 이용하여 실린더표면에서의 대류열전달계수의 측정실험을 수행하고, 각 방법들에 대한 비교분석을 통해 액정을 이용한 열전달 측정방법의 특징들을 살펴보았다.

• 설비공학논문집
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• 제3권5호
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• pp.376-385
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• 1991

The purpose of this paper is to propose basic data on convection heat-transfer coefficients in Ondol-heated room. Surface temperatures and several temperatures around each inside surface of wall, floor and ceiling composed of heating room are measured vertically in Ondol-heated model rooms, and the vertical temperature profiles could be expressed by nonlinear equation models. Also, the convection heat transfer phenomena are analysed from the nonlinear equation models. In the results, the convection heat-transfer coefficients of Ondol heated space are suggested by the term of temperature difference between each wall surface and room air temperature and by the relationship between Nusselt number and Rayleigh number of dimensionless numbers.

• 대한기계학회논문집B
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• 제26권12호
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• pp.1707-1714
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• 2002

This paper deals with the development of a new method that can obtain heat transfer coefficient and reference free stream temperature simultaneously, The method is based on transient heat transfer experiments using two narrow-band TLCs. The method is validated through error analysis in terms of the random uncertainties in the measured temperatures. It is found that the errors could be reduced more than 2 times less. The general method described in this paper is applicable to many heat transfer models with unknown free stream temperature.

• 대한기계학회논문집B
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• 제21권1호
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• pp.57-67
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• 1997

The solidification process of Al 4.5%Cu alloy is numerically studied in the presence of contact resistance between mold and cast. Natural convection is considered in the liquid and mushy regions. The porosity approach is applied to the mushy zone modeling and linear variation of the solid fraction on the temperature is assumed. Results show that the mushy region is wider in the case with a contact resistance compared to the perfect contact condition. The temperature of the cast with a temporal variation in the contact heat transfer coefficient changes very rapidly in the early stage of the casting process compared to that with constant contact heat transfer coefficient.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2003년도 춘계학술대회
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• pp.1473-1478
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• 2003

Scale is formed when hard water is heated or cooled in heat transfer equipments such as heat exchangers, condensers, evaporators, cooling towers, boilers, and pipe walls. When scale deposits in a heat exchanger surface, it is traditionally called fouling. The objective of the present study is to investigate the formation of fouling in a heat exchanging system. A lab-scale heat exchanging system is built-up to observe and measure the formation of fouling experimentally. Water analyses are conducted to obtain the properties of HAN river water. In the present study a microscopic observation is conducted to visualize the process of scale formation. Hardness of HAN-river water is higher than that of tap water in Seoul.

• 한국축산시설환경학회지
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• 제5권2호
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• pp.113-122
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• 1999

온실에서 퇴비화 발효율을 이용하기 위하여 발효율이 토양을 직접 가온하면서 퇴비화하는 퇴비화 하우스를 제작하였다. 퇴비화가 진행되는 동안 각 단계별 열의 발생량과 발생열량이 토양에 전달되는 특성을 분석하였다. 우분과 왕겨를 혼합하여 퇴비화 처리하였다. 퇴비화 과정의 총 70일 동안 391MJ/㎥의 열량이 발생하였으며, 이중 22일의 주발효기간 동안에 약 82%의 열량이 발생하였다. 또한 총 열량중 토양의 지표면의 지표면을 통하여 방출되는 열량을 제외한 260M/㎥의 열량이 지중가온에 이용된 것으로 나타났다. 콤포스트의 열 전도계수는 1.7~0.3W/m$^{\circ}$K이었다. 퇴비화 시스템을 구비한 온실의 주 발효기간의 지중 평균온도는 27.9$^{\circ}C$인 반면, 퇴비화 시스템이 없는 온실의 경우 13.9$^{\circ}C$로 나타나 퇴비화 시스템이 지중 온도증가에 큰 효과를 나타내고 있었다.

• 한국전산유체공학회:학술대회논문집
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• 한국전산유체공학회 2011년 춘계학술대회논문집
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• pp.608-609
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• 2011

In this study, we tried to validate FLUENT solver model and domain setting for the problem of convective heat transfer in multiple tube bank under transitional zone. We have paid special attention to verify proper boundary conditions and the grid convergence. Through validation work, it is found that unsteady solution method with two-dimensional simulation domain can produce reasonable accurate results compared with existing experimental data. Simulation results with steady solution generates relatively large error. We found that both steady and unsteady method for three-dimensional domain shows acceptable accuracy. Further parametric study for deriving correlation from transverse and longitudinal pitch is currently underway.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2003년도 추계학술대회
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• pp.187-192
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• 2003

The heat (mass) transfer characteristics in the tip-leakage flow region of a high-turning first-stage turbine rotor blade has been investigated by employing the naphthalene sublimation technique. The heat transfer data in the tip-leakage flow area for the tip clearance-to-span ratio, h/s, of 2.0% are compared with those in endwall three-dimensional flow region without tip clearance (h/s = 0.0 %). The result shows that the thermal load in the tip-leakage flow region for h/s = 2.0% is more severe than that in the endwall flow region for h/s = 0.0%. The thermal loads even at the leading and trailing edges for h/s = 2.0% are found larger than those for h/s = 0.0%. The tip-leakage flow results in heat transfer augmentations near the tip on both pressure and suction sides in comparison with the mid-span results.

• 설비공학논문집
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• 제15권9호
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• pp.768-778
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• 2003

Numerical analysis has been carried out to investigate laminar convective heat transfer in a tube for supercritical water near the thermodynamic critical point. Fluid flow and heat transfer are strongly coupled due to large variations of thermodynamic and transport properties such as density, specific heat, viscosity, and thermal conductivity near the critical point. Heat transfer characteristics in the developing region of the tube show transition behavior between liquid-like and gas-like phases with a peak in heat transfer coefficient distribution near the pseudocritical point. The peak of the heat transfer coefficient depends on pressure and wall heat flux rather than inlet temperature and Reynolds number, Results of the modeling provide convective heat transfer characteristics including velocity vectors, temperature, and the properties as well as the heat transfer coefficient. The effect of proximity to the critical point is considered and a heat transfer correlation is suggested for the peak of Nusselt number in the tube.

• 한국해양공학회지
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• 제15권2호
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• pp.39-45
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• 2001

With uniform heat generation from the inner surface of the cylindrical heater placed in a cross flow boundary condition, heat flow that is conducted along the wall of the heater creates a non-isothermal surface temperature and non-uniform heat flux distribution. In the present investigation, the effects of circumferential wall heat conduction on convection heat transfer is investigated for the case of forced convection around horizontal circular tube in cross flow of air. The wall conduction number which can be deduced from the governing energy equation should be used to express the effect of circumferential wall heat conduction. It is demonstrated that the circumferential wall heat conduction influences local Nusselt numbers of one-dimensional and two-dimensional solutions.