• 한국추진공학회지
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• 제24권5호
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• pp.1-12
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• 2020

본 논문에서는 재생냉각 연소기에서 냉각제 및 연료로 사용되는 Jet A-1의 열전달 특성에 대해 실험적으로 연구하였다. 냉각채널 가열을 위한 인가 전류, 모사 시편 지름, 시편 후단 압력, Jet A-1 유속을 변화시키며, 시편에서의 벽면 온도 및 시편 전/후단에서의 Jet A-1 온도를 측정하였다. 시편 지름과 유속이 열전달 특성에 중요한 인자임을 알 수 있었으며, 시편의 후단 압력은 열전달 성능에 영향을 주지 않음을 확인할 수 있었다. 열전달 실험결과는 기존 Nu수 경험식들과 비교하였으며, 최종적으로 새로운 Nu수 경험식을 도출하였다.

• 설비공학논문집
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• 제12권4호
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• pp.398-403
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• 2000

Numerical analysis was conducted to investigate flow and heat transfer characteristics in louver fin exchanger, which were influenced by louver pitch, fin pitch, louver angle and inlet velocity. Standard $k-\varepsilon$ turbulent modelling was used in this study, and compared with laminar modelling. As a result of this study, Nusselt number became smaller as louver pitch or fin pitch was greater. Drag coefficient became smaller as louver pitch or fin pitch was greater, but it was little affected by inlet velocity.

• Journal of Advanced Marine Engineering and Technology
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• 제22권2호
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• pp.200-209
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• 1998

Experiments have been conducted to determine heat transfer characteristics for a two-dimen-sional turbulent wall attaching offset jet at different oblique angles to a flat surface. The local Nusselt number distributions were measured using liquid crystal as a temperature sensor. Wall static pressure coefficient profiles were measured at the Reynolds number Re 53200(based on the nozzle width, D) the offset ratio H/D from 2.5 to 10 and the oblique angle a from $0^{\circ}$, to $40^{\circ}$ It is observed that the maximum Nusselt number point occurs slightly upstream of time-averaged reattachment point for all oblique angles. The correlations between the maximum Nusselt number and Reynolds number offset ration and oblique angle are presented.

• 대한기계학회논문집B
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• 제30권4호
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• pp.337-342
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• 2006

Natural convection flows in a cubical air-filled cavity that has one pair of opposing faces isothermal at different temperatures, $T_h\;and\;T_c$, respectively, the remaining four faces having a linear variation from $T_c\;to\;T_h$ are numerically simulated by a solution code(PowerCFD) using unstructured cell-centered method. Special attention is paid to three-dimensional flow and thermal characteristics according to the variation of inclination angle $\theta$ of the isothermal faces from horizontal: namely $\theta=0^{\circ},\;15^{\circ},\;30^{\circ},\;45^{\circ},\;50^{\circ},\;60^{\circ},\;75^{\circ}\;and\;90^{\circ}$. Comparisons of the average Nusselt number at the cold face are made with experimental benchmark results found in the literature. It is demonstrated that the average Nusselt number at the cold face has a maximum value around the inclination angle of $50^{\circ}$. It is also found that the code is capable of producing accurately the nature of the laminar convection in a cubical air-filled cavity with differentially heated walls.

• 설비공학논문집
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• 제8권1호
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• pp.120-139
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• 1996

Experiment was performed to study the heat transfer characteristics in 27 kinds of 15 : 1 scale models of multi-louverred fin heat exchangers with a wide range of variables(R $e_{Lp}$ =100~1, 800, $L_p$/F$p$=0.3~0.9, $\theta$=20$^{\circ}$~40$^{\circ}$). Thermofoil heaters were used to heat the louver fins and the local average Nusselt number for each louver in the louver array was obtained at constant wall temperature conditions. Correlations are developed to predict the heat transfer characteristics and drag coefficients. Generally, the heat transfer characteristics in the multi-louvered fins is shown to be similar to those of the laminar heat transfer on a flat plate. As the Reynolds number, the louver pitch to fin pitch ratio$L_p$/F$p$and the louver angle($\theta$) increase respectively, the average Nusselt number increases, but the variation of average Nusselt number as a function of the louver angle is smaller than that as a function of the louver pitch to fin pitch ratio. In case of$L_p$/F$p$ <0.5, the average Nusselt number of the 3rd louver is especially lower than the others, it is expected that it is due to the flow structure such as a recirculation flow and a flow separation.

• 설비공학논문집
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• 제23권8호
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• pp.535-542
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• 2011

The performance of a plate heat exchanger for using liquid solution in the absorption chiller-heater was analyzed. The model was developed by using the various performance prediction correlations. The performance characteristics of the plate heat exchanger with the mass flow rate ratio was verified by using experimental data. To investigate performance of plate heat exchanger with geometry variables, the chevron angle, corrugated wave length, and corrugation depth were changed. As a result, the capacity of Kim and Martin correlation models was similar with the experimental data, and the capacity difference was less than 2%. Besides, the pressure drop of Marin correlation model showed a similar variation with experimental data, and the difference of pressure drop was less than 1.5 kPa.

• 대한기계학회논문집B
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• 제21권10호
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• pp.1314-1325
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• 1997

Experiments have been conducted to determine the flow and heat transfer characteristics for a two-dimensional turbulent wall attaching offset jet at different oblique angles to a flat surface. The distributions of the wall static pressure coefficient and time-averaged reattachment position for various offset ratios and oblique angles have been measured. The local Nusselt number distributions on the plate surface were also measured using liquid crystal as a temperature indicator. The new hue-capturing technique utilizing a true color image processing system was used to accurately determine the temperature of the liquid crystal. The experiments were carried out at Reynolds number, Re (based on D) of from 7300 to 21,300 with offset ratio, H/D from 2.5 to 10, and oblique angle, .alpha. from 0 deg. to 400 deg..

• 태양에너지
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• 제13권2_3호
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• pp.91-106
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• 1993

유동층을 열교환기에 응용하기 위한 시도로 알루미나 입자를 유동입자로 하는 수직 이중관식 유동층형 열교환기에서 내관으로 평활관과 핀관(종형핀)을 사용하는 경우에 각각의 열전달효과를 비교, 검토하였다. 본 실험에서는 평균직경이 $0.41{\sim}0.77mm$ 범위의 4종의 알루미나 입자를 사용하였으며, 초기충진높이는 50mm($H_o/H=0.083$)에서 250mm($H_o/H=0.417$)의 범위로 하였다. 입자의 크기와 초기 충진높이 및 유동화속도가 열전달계수에 미치는 영향을 검토하고, 단상강제대류형 열교환기와 열전달효과를 비교한 결과, 평활관을 사용하는 경우에는 7.8배, 핀관을 사용하는 경우에는 12.9배의 전열증진효과가 있었다. 또 유동층에서는 유동화속도가 증가함에 따라 열전달계수는 최대값을 보인후 다시 감소하는데, 이때의 Nu수 및 Re수와 Ar수의 무차원 관계식을 구하였다.

• 한국전산유체공학회지
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• 제16권3호
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• pp.66-74
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• 2011

A fluid in an enclosure can be heated by electric heating, chemical reaction, or fission heat. In order to remove the volumetric heat of the fluid, the walls surrounding the enclosure must be cooled. In this case, a natural convection occurs in the pool of the fluid, and it has a dominant role in heat transfer to the surrounding walls. It can augment the heat transfer rates tens to hundreds times larger than conductive heat transfer. The heat transfer by a natural convection in a regular shape such as a square cavity or semi-circular pool has been studied experimentally and numerically for many years. A pool of an inverted triangular shape with 10 degree inclined bottom walls has a good cooling performance because of enhanced boiling critical heat flux (CHF) compared to horizontal downward surface. The coolability of the pool is determined by comparing the thermal load from the pool and the maximum heat flux removable by cooling mechanism such as radiative or boiling heat transfer on the pool boundaries. In order to evaluate the pool coolability, it is important to correctly expect the thermal load by a natural convection heat transfer of the pool. In this study, turbulence models with modifications for buoyancy effect were validated for unsteady natural convections by volumetric heating. And natural convection in the triangular pool was evaluated by using the models.

• 태양에너지
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• 제18권2호
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• pp.145-152
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• 1998

본 연구는 furan 주물사의 재생시 냉각효율을 크게 높이며 폐열의 회수를 증진하는 데 활용할 수 있는 자료들을 얻기 위하여, 재생된 Furan foundry sand를 유동입자로 사용한 유동층에서 평활관(smooth tube), 나선관(spiral tube) 및 핀관(finned tube)을 수평으로 설치하여, 유동층 내 온도를 $50{\sim}200^{\circ}C$로 유지하면서 전열 관에 대한 열 전달계수를 실험적으로 구하였다. 유동층의 내경은 210mm이고, 전열관의 외경은 모두 12.7mm인 동관을 각각 사용하였다. 본 실험은 관내 냉각수의 Reynolds수 $4,000{\sim}18,000$범위이고, 유동층내 유동입자 Reynolds수 $0.8{\sim}7.5$의 범위에서 수행하여 다음과 같은 결과들을 얻었다. 1. 유동층내 온도가 높으면 모든 전열관에서 열 전달계수는 커진다. 2. 최대 열 전달계수는 평활관에서는 $Re_p$수 $3.5{\sim}5.5$, 나선관에서는 $Re_p$수 $4.4{\sim}5.2$, 핀관에서는 $Re_p$수 $3.5{\sim}4.8$의 범위에서 각각 얻을 수 있다. 3. 유동층내의 온도에 따라 약간 다르지만 평활관, 나선관 및 핀관에서의 최대 Nu수들은 각각 대략 1:1.5:3.0의 비를 얻는다.