• 대한기계학회논문집
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• 제12권2호
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• pp.349-358
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• 1988

본 연구에서는 낮은 종횡비의 직각밀폐용기의 경계층흐름영역에 대하여 Lee에 의해 공식적인 수학적 방법으로 얻어진 코어방정식을 기초로 코어흐름 형상을 근사해석으로 구하였으며 그 결과를 다른 연구자들의 결과와 비교, 검토하였다.

• 대한기계학회논문집B
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• 제24권5호
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• pp.699-708
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• 2000

To make compact evaporator, experiments that show characteristics of evaporating heat transfer and pressure drop in the helically coiled small diameter tube were taken in this research. The experiments were performed with HCFC-22 in the helically coiled small diameter tube; inner diameter=1.0(mm), tube length=2.0(m), and curvature diameter=31, 34, 46.2(mm). The experiments were also carried out with the following test conditions; saturation pressure=0.588(MPa), mass velocity=$150{\sim}500(kg/m^2s)$, and heat flux=$1{\sim}5(kW/m^2)$. The experiment results are that the empirical correlation to predict heat transfer coefficient for single phase flow in helically coiled small diameter tube was obtained. It was found that dry-out is occurred at low-quality region for evaporation heat transfer because of breaking of annular liquid film. The friction factor of single phase flow of helically coiled tube was agreed with Prandtl's correlation. Finally, It was proposed for correlation that can precisely predict the friction factor of two phase flow of helically coiled tube.