• 한국지반공학회논문집
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• 제30권7호
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• pp.55-61
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• 2014

최근 들어 경제적이고 친환경적인 에너지 활용을 위하여 지열에너지 필요성이 증대되고 있다. 수평형 지중 열교환기는 설치 비용이 저렴하여 비용 대비 효율면에서 우수하다. 수평형 지중 열교환기의 타입에는 여러 가지가 있으나 이 중 슬링키형과 코일형이 우수한 것으로 알려져 있다. 따라서 본 논문에서는 $5m{\times}1m{\times}1m$ 크기의 모형 토조내에 수평 슬링키형과 코일형 지중 열교환기를 각각 설치한 후 열교환율을 실험적으로 측정하였다. 모형 토조 내에는 건조 상태의 주문진 모래가 조성되었으며 수평 슬링키형과 코일형의 피치 간격에 따라 열교환율을 측정하기 위해 30시간 동안 연속으로 열응답 시험을 실시하였다. 실험 결과 코일형 지중 열교환기 이용시 수평 슬링키형 보다 약 30, 40% 정도의 높은 파이프 단위 길이당 열교환율을 보였다. 또한 수평 슬링키형과 코일형 이용시 피치 간격이 넓을 때(피치/직경 = 1)가 좁을 때(피치/직경 = 0.2)보다 약 200, 250% 정도의 높은 파이프 단위 길이당 열교환율을 나타냈다.

• 태양에너지
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• 제15권3호
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• pp.3-14
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• 1995

태양열 이용 축열식 직접접촉 열교환기의 실제 적용을 위한 작동조건도출 및 열교환기내 열전달 특성 규명을 위하여 작동유체를 물보다 가벼운 경우(Texaterm)와 무거운 경우 두가지를 실제 태양열 집열회로상에서 실험하였다. 작동유체가 물보다 가벼운 경우와 무거운 경우에 대해 실제 태양열 집열회로상에서 작동하여 최적 열전달을 위한 작동유체드럽형성과 유동을 도출하였고, 작동유체가 무거운 경우가 가벼운 경우보다 열손실계수가 높음을 알 수 있었다. 작동유체가 축열유체보다 가벼운 경우와 무거운 경우에 대해 실제 태양열 직열회로에서 실험한 결과, 작동유체가 가벼운 경우 체적 열전달계수는 $1.848{\times}10^{-3}w/cm^3^{\circ}C$, 효율은 73%이고 무거운 경우는 $0.128{\times}10^{-2}w/cm^3^{\circ}C$, 효율은 82%로 작동유체가 무거운 경우가 보다 좋은 것으로 나타났다.

• 한국자동차공학회논문집
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• 제12권2호
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• pp.91-100
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• 2004

Plate heat exchangers (PHE) have been widely used in different industrial applications, because of high heat transfer efficiency per unit volume. Basic study is performed for PHE to the application of intercooler in automobile. In order to understand the flow phenomena in the plate heat exchanger, a channel which was formed by the upper and lower plate in single plate was considered as calculation domains. Because chevrons attached on the upper plate are brazed with chevrons attached on the lower plate, the flow channel has very complex configuration. This complex geometry was analyzed by Fluent. In order to validate this methodology the proper experimental and theoretical data are collected and compared with numerical results. Finally, due to the lack of experimental values for PHE to the application of intercooler, various chevron angles and air velocities at inlet were tested in terms of physical phenomena. From this point of view, results of velocity vector, path lines, static pressure, heat flux, heat transfer coefficient, and Nusselt number are physically reasonable and accepted for the solutions. From these results, the correlations for pressure drop and Nusselt number with respect to chevron angle and Reynolds number in specific PHE are obtained for the design purpose. Thus, the methodology of the flow analysis in the full geometry of the channel was established for the predictions of performance in plate heat exchanger.

• 설비공학논문집
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• 제9권2호
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• pp.153-162
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• 1997

In this study, the wet surface heat transfer coefficients and friction factors of the heat exchanger with slit-wavy fin were measured. Four sample cores of two or three row with fins of 12 fpi or 16 fpi were tested. Tests were conducted in a closed loop wind tunnel, where the heat exchanger was mounted at 45 degree inclination angle. The wet surface heat transfer coefficient was reduced following the procedure given in ARI 420-81. During the course, new definitions of the $\varepsilon$-NTU applicable to enthalpy driving system were introduced. The wet surface heat transfer coefficients were approximately equal to the dry surface values. However, the friction factors were approximately 120% to 170% higher than those of the dry surface. Both the heat transfer coefficient and the friction factor of the wet surface increased as the relative humidity increased, fin pitch decreased, and the number of row decreased, although the difference was not large.

• 대한기계학회논문집A
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• 제28권6호
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• pp.774-782
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• 2004

This article presents a numerical and experimental investigation for the single-phase forced laminar convective heat transfer through arrays of micro-channels in micro heat exchangers to be used for cooling power-intensive semiconductor packages, especially the stacked multi-chip modules. In the numerical analysis, a parametric study was carried out for the parameters affecting the efficiency of heat transfer in the flow of coolants through parallel rectangular micro-channels. In the experimental study, the cooling performance of the micro heat exchanger was tested on prototypes of stacked multi-chip modules with difference channel dimensions. The simulation results and the experiment data were acceptably accordant within a wide range of design variations, suggesting the numerical procedure as a useful method for designing the cooling mechanism in stacked multi-chip packages and similar electronic applications.

• 설비공학논문집
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• 제18권9호
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• pp.729-737
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• 2006

Air-side forced convective heat transfer of a plate fin-tube heat exchanger is investigated by experimental measurement and numerical computation. The heat exchanger consists of staggered arrangement of refrigerant pipes of 10.2 m diameter and the pitch of fins is 3.5 m. In the experimental study, the forced convective heat transfer is measured at Reynolds number of 1082, 1397, 1486, 1591 and 1649 based on diameter of refrigerant piping and mean velocity. Average Nusselt number for the convective heat transfer coefficient is also computed for the same Reynolds number by commercial software of STAR-CD with standard $k-{\varepsilon}$ turbulent model. It is found that the relative errors of average Nusselt numbers between experimental and numerical data are less than 6 percentage in Reynolds number of $1082{\sim}1649$. The errors between experiment and other correlations are ranged from 7% to 32.4%. But the correlation of Kim at al is closest to the experimental data within 7% of the relative error.

• Journal of Advanced Marine Engineering and Technology
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• 제36권8호
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• pp.1003-1009
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• 2012

열교환기는 에너지전달을 필요로 하는 산업분야에 널리 사용되고 있으며 효율이 좋은 판형 열교환기의 비중이 크게 증가되고 있다. 본 연구는 판형열교환기의 최적설계를 위하여 주요설계인자를 분석하고 방정식을 유도하였으며 상용코드와 비교 분석하였다. 판의 쉐브론각에 따른 열전달계수와 압력강하 설계식을 도입하였으며 각각의 설계식은 레이놀즈 수의 함수로 표현되었다. 이 설계식을 이용해 쉐브론 각이 동일한 판을 사용하였을 경우와 쉐브론각이 다른 두 판을 교차한 경우에 대하여 성능 해석하였으며 상용프로그램의 결과와 비교분석하였다. 성능해석을 한 결과 대류열전달계수는 8%이내, 압력강하는 5%이내의 오차로 만족할 만한 결과를 나타냈다.

• 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.

• 설비공학논문집
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• 제11권4호
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• pp.472-483
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• 1999

The evaporation heat transfer and pressure drop characteristics for HFC-l34a in flat plate type heat exchangers with enhanced beads were experimentally investigated. Three plate type evaporators with different geometric condition of U-turn area were tested. Mass fluxes were tested over the range of 83kg/$m^2$s to 166kg/$m^2$s, and heat fluxes were varied from 4㎾/$m^2$ to 12㎾/$m^2$. Evaporation temperature was 5$^{\circ}C$ with inlet qualities of 0.1 to 1.0. There was no notable difference in the heat transfer coefficient by geometric variation of U-turn area, but the third plate with cross-ribbed channel at U-turn area was better than others in the evaluation using volume goodness factor comparison. Also, the mixtures of HFC-l34a and PAG oil was tested to determine oil effects on heat transfer and pressure drop. As oil concentration was increased, heat transfer coefficient was increased by 22~48% up to the 3wt.%, but decreased by 14~22% at the 4wt.%. The pressure drop was increased by the maximum of 100% as oil concentration was increased.

• 동력기계공학회지
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• 제17권2호
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• pp.87-94
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• 2013

Applicability of organic Rankine cycle for a passenger car with 3.5 L gasoline engine to convert low grade waste heat to useful shaft power has been numerically studied. Working fluid is R134a, and the Rankine cycle is composed of boiler for recovering engine cooling water heat, super heater for recovering exhaust gas heat, scroll expander for converting waste heat to shaft power, condenser for heat emission, internal heat exchanger, and feed pump. Assuming efficiencies of 90% for the heat exchangers, 75% for the scroll expander, and 80% for the feed pump, the Rankine cycle efficiency of 5.53% was calculated at the vehicle speed of 120 km/hr. Net expander shaft output after subtracting the power required to run the pump was 3.22 kW, which was equivalent to 12.1% improvement in fuel consumption. About the same level of improvement in the fuel consumption was obtained over the vehicle speed range of 60 km/hr~120 km/hr.