• Journal of Advanced Marine Engineering and Technology
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• 제19권4호
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• pp.17-26
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• 1995

In general existing air conditioning devices, which are carried out by convection heat transfer, are very popular compared with the radiation type air conditioning devices. But perconal convection tpe air conditioning units are unuseful air conditioning type because it handles amount of surrounded air to meet the temperature and humidity. In this view, this study is intended to develope personal dir conditioning units using a radiation type radiator. Liquid Droplet Radiator(L.P.R.) radiates the energy by means of thermal radiation. Radiative energy from L.P.R. is the infrared rays which heat the objects without lose of energy. It is a desirable heating method for the local area within the large room. In this study, the analysis uses the Monte Carlo methd to predict the temperature distribution in the droplet sheet and the net heat flux from the L.D.R.. And for this study and experiment was carried out to analyse the radiative and convective heat transfer characteristics in the L.D.R.. And the experiment was investigated the effects of inlet temperature, feed rate, optical thickness and droplet diameter on heat transfer characteristics of L.D.R.. The obtained results from the numerical and experimental studies of L.D.R. were as follows ; (1) The heat flux of L.D.R. was effected by extinction coefficient of droplet sheet, optical thickness and droplet temperature, surface area and emissivity of the droplet. And it was increased with the temperature, feed rate and optical thickness, on the other hand decreased with increasing of droplet diameter. (2) The experimental results for heat flux was ecalucted below 20% than that of the numerical solution by Monte Carlo method, but the tendency of the variation shows relatively good agreement.

• 한국생산제조학회지
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• 제22권3호
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• pp.380-387
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• 2013

In this study, two finite element (FE) models were developed to evaluate the thermal characteristics of a feeding axis of a CNC lathe. One was used for analysis of heat transfer to identify the temperature distribution of the feeding axis and then, the other was used for analysis of thermal deformation to evaluate its structural behavior based on the temperature distribution. The FE models were based on the test standard for the axial thermal displacement. The feeding velocity was composed of three steps: the ascending, constant, and descending velocities. Therefore, the heat generation and convection coefficient were calculated for each velocity and applied to the thermal FE model. The convection coefficient for the ball screw rotation was based on an experimental equation. The result of the analytical thermal displacement was compared with that of the experimental displacement to verify the finite element models.

• Journal of Advanced Marine Engineering and Technology
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• 제28권3호
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• pp.500-508
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• 2004

The heat transfer coefficients during gas cooling process of carbon dioxide in a horizontal tube were investigated. The experiments are conducted without oil in the refrigerant loop. The main components of the refrigerant loop are a receiver, a variable-speed pump, a mass flow meter, a pre-heater, and a gas cooler(test section). The water loop consists of a variable-speed pump, an isothermal tank, and a flow meter. The gas cooler is a counterflow heat exchanger by cooled water flowing in the annulus. The $CO_2$ flows in the horizontal stainless steel tube. which is 9.53mm in O.D. and 7.75mm in I.D. The gas cooler is 6 [m] in length. which is divided into 12 subsections, respectively. The experimental conditions considered in the study are following range of variables : refrigerant temperature is between 20 and $100^{\circ}C$. mass fluxes ranged from 200 to 400kg/($m^2$.s), average pressure varied from 7.5 to 10.0MPa. The main results were summarized as follows : The friction factors of $CO_2$ in the gas cooler show a relatively good agreement with those predicted by Blasius' correlation. The local heat transfer coefficient in the gas cooler has compared with most of correlations, which are the famous ones for forced convection heat transfer of turbulent flow. The results show that the local heat transfer coefficient of gas cooler agrees well with the correlation by Bringer-Smith except that at the region near pseudo critical temperature. while that at the near pseudo critical temperature is higher than the correlation.

• 콘크리트학회논문집
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• 제15권2호
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• pp.314-322
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• 2003

콘크리트 구조물의 수화열 저감 방안으로 사용되는 파이프 쿨링 시스템을 적용할 경우 파이프 관 주변의 내부유동에 의한 열전달이 발생하게 된다. 이와 같은 내부유동에 의한 열전달 효과를 정확히 규명하기 위해서는 유수대류계수를 산정하여야 한다. 파이프 쿨링 효과의 규명에 필요한 유수대류계수의 영향인자로는 냉각수의 층난류 여부, 냉각수의 유동속도, 관의 형상 및 열특성 등이 있다. 본 연구에서는 유수대류계수를 산정하기 위한 실험장치를 개발하였으며, 이를 이용하여 강재 및 PVC 파이프에 대한 실험을 수행하였다. 이들 실험결과를 토대로 관의 내부표면이 매끈한 원형관이며 난류흐름을 갖는 내부유동에 대한 유수대류계수 모델식을 제안하였으며, 제안된 모델식은 냉각수의 유속뿐만 아니라 유동관의 재질 및 형상을 고려할 수 있다. 유수대류계수는 관을 흐르는 냉각수의 대류에 의한 열전달 효과를 나타내는 값으로 관의 열전도율 및 관의 직경과는 비례관계에 있으며, 관의 두께와는 반비례관계를 갖는다. 본 연구에서 개발된 유수대류계수 모델식은 이러한 영향을 잘 반영하고 있으나, 강재 파이프에 대해서만 관의 두께 및 직경에 관한 보정계수를 제시하였다. 제안된 모델식에 의한 유수대류 계수와 실험으로부터 구한 유수대류계수를 비교한 결과, 제안된 모델식이 실험값을 정확히 추정하고 있음을 알 수 있었다.

• 한국전산유체공학회지
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• 제18권4호
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• pp.25-34
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• 2013

A numerical study of a laminar natural convection of the CuO-water nanofluid in a square cavity using the Buongiorno's nonhomogeneous model is presented. All the governing equations including the volume fraction equation are discretized on a cell-centered, non-uniform grid employing the finite-volume method with a primitive variable formulation. Calculations are performed over a range of Rayleigh numbers and volume fractions of the nanopartile. From the computed results, it is shown that both the homogeneous and nonhomogeneous models predict the deterioration of the natural convection heat transfer well with an increase of the volume fraction of nanoparticle at the same Rayleigh number, which was observed in the previous experimental studies. It is also shown that the differences in the computed results of the average Nusselt number at the wall between the homogeneous and nonhomogeneous models are very small, and this indicates that the slip mechanism of the Brown diffusion and thermophoresis effects are negligible in the laminar natural convection of the nanofluid. The degradation of the heat transfer with an increase of the volume fraction of the nanoparticle in the natural convection of nanofluid is due to the increase of the viscosity and the decrease of the thermal expansion coefficient and the specific heat. It is clarified in the present study that the previous controversies between the numerical and experimental studies are owing to the different definitions of the Nusselt number.

• 에너지공학
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• 제18권1호
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• pp.1-8
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• 2009

본 논문에서는 알루미나-물 나노유체를 사용하여 자연대류 실험을 수행하였다. 시험공간은 실린더이며 유체층 두께를 조절하여 종횡비는 10.9부터 30.4까지 변화를 주었다. 열전달계수는 순 물의 자연대류 실험과 비슷하게 30분 이내에 정상상태에 거의 도달한 것같이 보이나 경사도가 $0^{\circ}$인 경우 열전달계수가 $1{\sim}2$시간이상 감소하며 일부 종횡비에서는 열전달계수의 변동현상이 10시간이상 측정되었다. 변동형태와 주기는 종횡비와 각도에 따라 다르며 $0^{\circ}$의 경사도에서는 열전달계수의 변동주기가 $60^{\circ}$의 경사도에 비하여 2배 이상 이였다. Rayleigh 수가 $1.0{\times}10^5$ 보다 작은 경우, 평균 Nusselt 수는 $30^{\circ}$의 경사도에서 가장 높게 나타나며 $60^{\circ}$의 경사도에서 가장 낮게 나타났다. 그러나 본 실험결과도 응집된 상태의 나노유체가 사용되었으므로 일반성을 가지고 있지는 않는다.

• 설비공학논문집
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• 제17권11호
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• pp.1022-1027
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• 2005

An experimental study is conducted to investigate the characteristics of the ion wind generated by the electric field between a needle electrode and the parallel plate electrodes. The ion wind enhances heat and mass transfer between the surface and the surrounding gas. Moreover such enhancement makes no noise or vibration. This study is conducted to develop the electronic cooling device. The measured gas velocities and heat transfer coefficients are proportional to the applied voltage. The heat transfer coefficient can be increased as compared with a natural convection. The maximum enhancement of heat transfer obtained in this system is $47\%$ for 3 W in heat transfer rate.

• 대한기계학회논문집
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• 제18권5호
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• pp.1264-1274
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• 1994

Heat transfer performance of integral-fin tube which is used in recipro turbo refrigerator or high compact heat exchangers is studied. Eight tubes with trapezoidal shaped integral-fins having fin densities from 748 to 1654 fpm and 10, 30 internal grooves are tested. A plain tube having the same(inner and outer) diameter as the fin tubes is also tested for comparison. Pool boiling heat transfer of R-11 is investigated experimentally and theoretically on single tube arrangement. The refrigerant evaporates at saturation state of 1 bar on the outside tube surface and heat is supplied by not water which circulates inside of the tube. From the result of eight fin tubes and one plain tube tested, a tube having 1299 fpm-30 grooves shows the best performance. A maximum overall heat transfer coefficient of this tube is about 4000 $W/m^{2}K$ at 2.8m/s of water velocity. The maximum heat transfer enhancement (i.e., the ratio of overall heat transfer coefficients of finned to plain tubes)is about 2.1.

• 융합정보논문지
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• 제9권12호
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• pp.147-156
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• 2019

동심 이중관에서 기본유체 물과 나노입자 산화알미늄의 혼합인 나노유체를 적용한 대향유동을 유한체적법의 수치적 방법으로 열전달 특성을 규명하였다. 고온유체는 내부 원형관으로 흐르며 열을 외부 환형관으로 흐르는 저온유체로 전달한다. 고온유체와 저온유체의 체적유량 및 나노입자의 체적농도를 변수로 두어 열전달 및 유동 특성을 조사했다. 결과는 나노입자의 체적농도와 체적유량의 증가함에 따라 열전달 성능이 증가함을 보였다. 외부와 내부 관 모두에서 나노유체인 경우가 기본유체보다 나노입자의 체적농도가 8%일 때 나노유체가 열전달 성능이 최대 17% 증가하는 것을 확인했다. 또한 기본유체에 비해 환형관의 대류열전달 계수는 최대 31% 증가함을 보였으며 열교환기의 유용도는 약 20%가 상승함을 확인하였다. 하지만 나노입자의 체적농도가 8%일때 마찰인자가 최대 136% 커지는 것을 확인하였다.

• 한국터널지하공간학회 논문집
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• 제12권3호
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• pp.223-237
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• 2010

본 연구에서는 화재에 의한 콘크리트의 단면손실과 역학적 특성을 저하하는 주요 요인 가운데 온도증가율, 즉 초기가열구배를 변화시키면서 모의화재실험을 수행하였다. 그리고 수행된 모의화재실험에서 관찰된 단면손실을 모사하기 위하여 요소제거모델을 활용한 유한요소해석법에 의해 열전달해석을 수행하였다. 이때 모의화재실험결과와 수치해석결과가 가장 일치하는 대류열전달계수를 반복적인 해석과정을 통해 도출하였다 이상의 과정으로부터 얻어진 초기가열구배에 따른 대류열전달계수의 변화를 조사한 결과, 각 초기가열구배별 대류열전달계수의 변화는 분수함수 형태로 근사시킬 수 있었다. 최종적으로 모의화재실험으로부터 도출된 초기가열구배별 대류열전달계수의 변화 결과를 내삽하여 다양한 초기가열구배에 따른 화재경과시간별 대류열전달계수의 변화를 추정할 수 있는 수식을 함께 제시하였다.