• Journal of Advanced Marine Engineering and Technology
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• 제14권4호
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• pp.57-66
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• 1990

In the design of an electric power plant, the capacity to meet the peak load demand is one of the important factors to be considered. This peak load usually occurs when the most of the cooling air conditioning systems are being operated during daytime in summer season, which inevitably entails the construction of an additional electric power plant. This study is aimed to carry out a basic experiment for the development of a cooling air conditioning system using the ice energy by the surplus electric power during the night-time. The experimental apparatus consists of four major parts; (1) the heating section consisting of the air duct and I.D. fan, (2) the cold section with the ice chamber, (3) the bundle of heat pipes made in a form of the staggered arrangement with ${C_y}/{d_o}$=2.0 and ${C_x}/{d_o}$=1.73, (4) the refrigerator system to cool down the ice chamber. This study involves an intensive experiment concerning the convective heat transfer of the air flow surrounding the bundle of heat pipes. This major experimental parameters are the amount of working fluid, the velocity of air and the working temperature. The major findings of the present study are as follows; (1) The optimum amount of the working fluid necessary for the horizontal heat pipes is much more than that for the vertical type. (2) The convective heat transfer coefficients of the air are coincided with the empirical equations of Grimson and ${\breve{Z}ukauskas}$. (3) The equation of the mean heat transfer coefficient obtained in the present study is ${N_um}=0.32 {Re_max^{0.63}}$.

• 대한기계학회논문집B
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• 제20권2호
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• pp.720-729
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• 1996

An analysis of convective boiling heat transfer for refrigerant mixtures is performed for an annular flow to investigate the degradation of the heat transfer rate. Annular flow is selected in this study because a great portion of the evaporator in the refrigeration and air conditioning system is known to be in the annular flow regime. Mass transfer effect due to composition difference between liquid and vapor is included in this analysis, which is considered to be one of driving forces for the mass transfer at the interface. Due to the concentration gradient at the interface the mass transfer is interfered, so is the evaporative heat transfer at the interface. The mass transfer resistance makes the interface temperature slightly higher and, as a result, the heat transfer coefficients decrease compared with those without mass transfer effects. The degradatioin of the heat transfer rate reaches its maximum at a certain composition. The composition difference between vapor core and vapor at the interface has a direct effect on the temperature difference between the vapor core and the interface and the degradation of the heat transfer rate. Correction factor $C_{F}$ for the mixture effects is added to the correlation for pure substances and the flow boiling heat transfer coefficients can be calculated using the modified equation.n.

• Journal of Advanced Marine Engineering and Technology
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• 제28권1호
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• pp.65-74
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• 2004

The heat transfer coefficient and pressure drop of $CO_2$(R-744) during gas cooling Process of carbon dioxide in a horizontal tube were investigated experimentally and theoretically. The experiments were conducted without oil in the refrigerant loop. The main components of the refrigerant loop consist of a receiver. a variable-speed pump. a mass flowmeter, an evaporator. and a gas cooler(test section). The main components of the water loop consist of a variable-speed Pump. an constant temperature bath. and a flowmeter. The gas cooler is a counterflow heat exchanger with refrigerant flowing in the inner tube and water flowing in the annulus The test section consists of smooth, horizontal stainless steel tube of 9.53 mm outer diameter and 7.75 mm inner diameter. The length of test section is 6 m. The refrigerant mass fluxes were 200 ~ 300 kg/($m^2{\cdot}s$) and the inlet pressure of the gas cooler varied from 7.5 MPa to 8.5 MPa. The main results were summarized as follows : The predicted correlation can evaluated the R-744 exit temperature from the gas cooler within ${\pm}10%$ for most of the experimental data, given only the inlet conditions. The predicted gas cooley capacity using log mean temperature difference showed relatively food agreement with gas cooler capacity within ${\pm}5%$. The pressure drop predicted by Blasius estimated the pressure drop on the $CO_2$ side within ${\pm}4.3%$. The predicted heat transfer coefficients using Gnielinski's correlation evaluated the heat transfer coefficients on the $CO_2$ side well within the range of experimental error. The predicted heat transfer coefficients using Gao and Honda's correlation estimated the heat transfer coefficients on the coolant side well within ${\pm}10\;%$. Therefore. The predicted equation's usefulness is demonstrated by analyzing data obtained in experiments.

• 대한토목학회논문집
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• 제29권5A호
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• pp.531-541
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• 2009

본 연구에서는 강도수준(30, 50 및 70 MPa)에 따른 고유동 자기충전 콘크리트의 수화발열 특성을 알아보기 위하여 2성분계 및 3성분계 고유동 자기충전 콘크리트를 제조하여 일반콘크리트와 수화열, 응결 및 역학적 특성을 분석 고찰 하였으며, 콘크리트에 사용된 분체에 대한 미소수화열량을 측정하여 얻은 분체의 열특성값, 간이단열온도실험을 실시하여 얻은 콘크리트의 열특성값 및 콘크리트에 사용된 재료의 일반적인 열특성값을 간편한 방법의 추정식을 이용하여 콘크리트 단열온도를 추정하였다. 또한, 온도해석에 의하여 얻어진 수화열 및 단열온도 특성값을 MIDAS CIVIL 06 프로그램을 이용하여 3차원 온도응력 해석을 실시하여 고유동 자기충전 콘크리트의 수화발열 특성 및 수화열에 의한 온도응력을 분석 고찰하였다.

• Ocean and Polar Research
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• 제38권2호
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• pp.89-102
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• 2016

In this study, we evaluated the model performance with respect to Sea Surface Temperature (SST) and Net Heat Flux (NHF) by considering the characteristics of seasonal temperature variation and contributing factors and by analyzing heat budget terms in the Northwestern Pacific and East Asian Marginal Seas ($110^{\circ}E-160^{\circ}E$, $15^{\circ}N-60^{\circ}N$) using the HadGEM2-AO historical run. Annual mean SST of the HadGEM2-AO is about $0.065^{\circ}C$ higher than observations (EN3_v2a) from 1950 to 2000. Since 1960, the model has simulated well the long-term variation of SST and the increasing rate of SST in the model ($0.014^{\circ}C/year$) is comparable with observations ($0.013^{\circ}C/year$). Heat loss from the ocean to the atmosphere was simulated slightly higher in the HadGEM2-AO than that in the reanalysis data on the East Asian Marginal Seas and the Kuroshio region. We investigated the causes of temperature variation by calculating the heat budget equation in the two representative regions. In the central part of the Kuroshio axis ($125^{\circ}E-130^{\circ}E$, $25^{\circ}N-30^{\circ}N$: Region A), both heat loss in the upper mixed layer by surface heat flux and vertical heat advection mainly cause the decrease of heat storage in autumn and winter. Release of latent heat flux through the heat convergence brought about by the Kuroshio contributes to the large surface net heat flux. Positive heat storage rate is mainly determined by horizontal heat advection from March to April and surface net heat flux from May to July. In the central part of the subtropical gyre ($155^{\circ}E-160^{\circ}E$, $22^{\circ}N-27^{\circ}N$: Region B), unlike Region A, vertical heat advection predominantly causes the decrease of heat storage in autumn and winter. In spring and summer, surface heat flux contributes to the increase of heat storage in Region B and the period is two times longer than the period for Region A. In this season, shoaling of the mixed layer depth plays an important role in the increase of SST.

• Journal of Welding and Joining
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• 제26권1호
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• pp.63-68
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• 2008

This paper has aimed to prevent excessive heat input by controlling arc distribution and heat input capacity with pulse GTAW in order to improve weld quality in 0.08mm pressure gauge diaphragm and flange welding parts. A design of experiment was designed using Box-Behnken method to optimize a welding process. The pulse GTAW parameters such as pulse current, base current, pulse duty, frequency and welding speed were set to input variables while hydraulic pressure that represents welding characteristics in diaphragm and flange joint were set to output variables. Based on the test result, a second regression equation was obtained between input and output variables and turned out significant. Besides, an influence of parameters has been confirmed through response surface analysis using the second-order regression equation and optimum welding condition was obtained through a grid-search method. The optimum welding condition was set to pulse current 84.4(A), base current 29.6(A), pulse duty 58.8(%), frequency 10(%), and welding speed 596(mm/min). Then, decent bead shape was acquired with no excessive heat input under the $2.3kgf/cm^2$ of hydrostatic pressure.

• 콘크리트학회지
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• 제7권6호
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• pp.186-196
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• 1995

본 연구에서는 국내에서 생산되는 시멘트의 발열상태에 대한 정량화를 목적으로 A시멘트사에서 생산되는 보통포틀란드시멘트를 그 대상으로 하여 단위시멘트량 및 타설온도를 주요변수로 한 단열온도 상승시험을 실시하여 각 변수가 콘크리트의 단열온도 상승량 및 발열속도에 미치는 영향을 검토하였고, 현재 시방서에 제시되어 있는 단열온도 상승시험 결과에 대하여 재검토를 하였다. 또한 이러한 시험결과가수치해석법에서 어떠한 영향을 미치는 가를 검토하였다. 검토결과 보통포틀란드시멘트에 대해서 시방서에 제시되어 잇는 단열온도상승량은 실제보다 과대평가하고 있으며, 시방서에 제시되어 있는 2-parameter 식 형태는 발열상태를 과대평가하고 있으며 이 식보다는 3- parameter식이 시멘트의 발열상태를 더 잘 근사하고 있음을 알았다. 또한 단열온도상승시험을 통해 얻어진 결과와 시방서에 제시된 값을 사용한 경우를 각각 수치해석법으로 해석한 결과, 온도는 큰 차이가 없었으나 온도응력은 외부구속이 강한 경우에는 약 20%정도가 큰 안전측의 해석결과를 나타내 시공계획 수립시에는 주의하지 않으면 안된다는 것을 알았다.

• Korean Chemical Engineering Research
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• 제44권3호
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• pp.277-283
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• 2006

화력발전소에서 배출되는 배연가스에서의 $CO_2$가스 흡수를 목적으로 sodium glycinate계 흡수제를 개발하기 위하여 sodium glycinate의 순수 및 수용액의 물성인 용해도, 증기압과 비점, 열전도 및 증발 잠열을 측정 또는 추산하였다. 용매인 $H_2O$ 25 g에 대한 sodium glycinate의 온도별 용해도는 y = 0.3471x + 20.993의 1차 함수 관계로 증가하였다. Sodium glycinate 10 wt％, 20 wt％, 30 wt％, 40 wt％, 50 wt％, 60 wt％ 수용액의 증기압과 비점을 측정하고, Antoine 상수를 구하였으며 Clausius- Clapeyron 식을 이용하여 증기압 측정값으로 증발 잠열을 구하였다. Sodium glycinate 분체의 열전도도 측정은 분체를 disk판으로 성형한 후, 고체 열전도도 측정 장치로 측정하였으며 그 값은 $1.0933kcal/m{\cdot}hr{\cdot}^{\circ}C$이었다.

• 전기전자학회논문지
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• 제6권2호
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• pp.136-145
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• 2002

정상상태에서 소자 내부의 격자온도 분포를 해석할 수 있는 시뮬레이터를 개발하였다. Slotboom 변수를 사용하여 열흐름 방정식을 이산화하였고, 요소내에서 열전도율의 적분값을 해석적으로 구할 수 있는 방법을 제안하였다. 제안된 방법의 타당성을 검증하기 위해 $N^+P$ 접합 다이오드와 BJT에 대해 모의실험을 수행하였고 DAVINCI와 MEDICI의 결과와 비교하였다. $N^+P$ 접합 다이오드에서 순방향 인가전압이 1.4[V]일 때 격자 온도분포는 DAVINCI의 결과와 2%의 상대오차를 보였으며 BJT에서 컬렉터 전압이 5.0[V]이고 베이스 전압이 0.5[V]일 때 격자 온도분포는 MEDICI의 결과와 3%의 상대오차를 보였다. BANDIS에서 제안된 열전도율의 적분방법을 사용하는 경우 수렴을 위해 평균 3.45회의 행렬 연산이 필요하나 DAVINCI에서는 평균 5.1회의 행렬 연산이 필요하였고 MEDICI는 평균 4.3회 행렬연산이 필요하였다.

• 한국결정성장학회:학술대회논문집
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• 한국결정성장학회 1999년도 PROCEEDINGS OF 99 INTERNATIONAL CONFERENCE OF THE KACG AND 6TH KOREA·JAPAN EMG SYMPOSIUM (ELECTRONIC MATERIALS GROWTH SYMPOSIUM), HANYANG UNIVERSITY, SEOUL, 06월 09일 JUNE 1999
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• pp.187-207
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• 1999

The thermal distributions near the growth interface of 150mm CZ crystals were measured by three thermocouples installed at the center, middle (half radius) and edge (10m from surface) of the crystals. The results show that larger growth rates produced smaller thermal gradients. This contradicts the widely used heat flux balance equation. Using this fact, it si confirmed in CZ crystals that the type of point defects created is determined by the value of the thermal gradient (G) near the interface during growth, as already reported for FZ crystals. Although depending on the growth systems the effective lengths of the thermal gradient for defect generation are varied, were defined the effective length as 10mm from the interface in this experiment. If the G is roughly smaller than 20C/cm, vacancy rich CZ crystals are produced. If G is larger than 25C/cm, the species of point defects changes dramatically from vacancies to interstitial. The experimental results which FZ and CZ crystals are detached from the melt show that growth interfaces are filled with vacancy. We propose that large G produces shrunk lattice spacing and in order to relax such lattice excess interstitial are necessary. Such interstitial recombine with vacancies which were generated at the growth interface, next occupy interstitial sites and residuals aggregate themselves to make stacking faults and dislocation loops during cooling. The shape of the growth interface is also determined by the distributions of G across the interface. That is, the small G and the large G in the center induce concave and convex interfaces to the melt, respectively.