• 설비공학논문집
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• 제9권4호
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• pp.527-535
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• 1997

Vapor-liquid equilibrium apparatus is designed and set up. The vapor-liquid equilibrium data of the binary system HFC32/134a are measured in the range between 258.15 and 283.15K at compositions of 0.2, 0.4, 0.6 and 0.8 mole fraction of HFC32. Twenty-two equilibrium data are obtained. Based upon the present data, the binary interaction parameter for Carnahan-Starling-De Santis equation of state is calculated. Temperature range of data is extended to 313.04K using the data in the open literatures. Interaction parameters are determined at nine isotherms.

• Nuclear Engineering and Technology
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• 제52권3호
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• pp.520-529
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• 2020

Experimental investigations were attempted to simultaneously observe the vapor behaviors and critical heat flux under static and rolling conditions. From visualization results, vapor initiated, grew, and detached individually in a vertical direction from the static heated surfaces (at 10, 20, and 30°). While under rolling motion, initiated vapor grew, and interacted with each other, resulting in forming a wider dry spot on the heated surface. Also, it was observed that the vapor drifted upward and stayed on the heated surface longer compared to under static condition. The faster the platform rolls, the longer the vapor stay on the heated surface, significantly decreasing the CHF. On the other hand, as the platform rolls slower (at high rolling period), CHF increases. CHF was decreased with increasing maximum rolling amplitude and inclination angle under both conditions (static and rolling). CHF under rolling conditions was noticed to be lower than under static condition except at maximum rolling amplitude of 10°. The bubble departure frequency at a maximum rolling amplitude of 10° was the highest among all of rolling amplitudes, thereby enhancing the CHF. These results indicate that rolling motion significantly affects vapor behaviors and CHF.

• 설비공학논문집
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• 제11권1호
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• pp.91-99
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• 1999

Vapor-liquid equilibrium apparatus is designed and set up. The equilibrium data of two binary systems, HFC-32/143a and HFC-143a/134a, are measured. Fifteen equilibrium data for HFC-32/143a and HFC-143a/134a systems are measured over the temperature range 263.15~283.15K at 10K interval and the composition range 0.10~0.80, respectively. And vapor-liquid equilibrium data are calculated using equation of state and correlation of activity coefficient and compared with the present data. Equation of state is used CSD and RKS equations and correlation of activity coefficient is used Margules' and Van Ness and Abbott's correlations. Real behavior of HFC-32/143a system has very large deviation with Raoult's rule which is ideal behavior. But real behavior of HFC-143a/134a system is similar to ideal behavior. The calculated data from CSD equation are compared with the data in the open literatures and the calculated data from REFPROP. In the results for REFPROP, the relative deviations of bubble point pressure for HFC-32/143a system are within -2.16~0.84% for CSD equation and within -0.20~1.10% for RKS equation. And the relative deviations of bubble point pressure for HFC-143a/134a system are within -0.45~0.12% and -0.20~2.8% for CSD and RKS equations, respectively.

• 대한기계학회논문집
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• 제14권3호
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• pp.702-715
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• 1990

본 연구에서는 개수로 후래시 증발기 내부를 단순화된 형태로 가정하여 앞서 언급된 운전조건 및 유입되는 기포의 갯수유량(혹은 기공률)에 따라 증발기 내부의 속 도 및 온도분포를 수치적으로 계산해 보고자 한다. 이를 위해 유동을 정상상태의 난 류유동으로 가정하였으며, 구형의 기포에 대해 평균적인 운동 및 성장을 지배하는 방 정식을 세우고 상변화에 의한 증발량을 구하였다. 즉 입구에서 유입된 기포들이 성 장하면서 자유표면을 통해서 빠져나가는 운동 궤적을 추적함으로써 증발기 내부 유동 의 속도 및 온도분포를 구하고 이를 바탕으로 총 증발량 및 증발성능을 예측해 보고자 하는 것이다. 그리고 이렇게 계산된 결과들을 기존의 실험값과 비교하였다.

• Journal of Advanced Marine Engineering and Technology
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• 제17권2호
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• pp.36-43
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• 1993

Real quality and axial void fraction distribution of subcooled refrigerant flow is very important to predict the heat transfer rate and pressure drop in the design of refrigerating system. In the subcooled boiling region, the liquid bulk temperature is still below the corresponding saturation temperature. But beyond the net vapor generation point, bubble detachment is occured actively from the vapor layer formed on the wall. A reliable method to predict the vapor fraction from the liquid bulk temperature is suggested in this paper. And also the actual quality of the subcooled R-113 flow is calculated in the range of 261-1239kg/$m^2$s mass velocity and 10-30K subcooling.

• 한국초전도저온공학회:학술대회논문집
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• 한국초전도저온공학회 2003년도 학술대회 논문집
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• pp.228-231
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• 2003

Experimental investigations of AC breakdown characteristics of liquid nitrogen in the environment to restrain boil bubbles are presented in this paper. The environment to restrain vapor bubble in the liquid nitrogen is both increasing pressure and decreasing temperature. Measurements of the breakdown voltage of liquid nitrogen in the environment to restrain vapor bubbles are investigated under AC high voltage in a quasi-uniform and non-uniform electrical field for pressures and temperatures ranging from 0 to 0.5 MPa and 77 K to 65 K respectively.

• Journal of Advanced Marine Engineering and Technology
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• 제39권8호
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• pp.801-806
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• 2015

The experimental analysis of a crevice-type vapor chamber heat pipe (CVCHP) is investigated. The heat source of the CVCHP is a high-power light-emitting diode (LED). The CVCHP, which exhibits a bubble pumping effect, is used for heat dissipation in a high-heat-flux system. The working fluid is R-141b, and its charging ratio was set at 60 vol.% of the vapor chamber in a heat pipe. The total thermal conductivity of the falling-liquid-film-type model, which was a modified model, was 24% larger than that of the conventional model in the LED package. Flow visualization results indicated that bubbles grew larger as they combined. These combined bubbles pushed the working fluid to the top, partially wetting the heat-transfer area. The thermal resistance between the vapor chamber and tube in the modified design decreased by approximately 32%. The overall results demonstrated the better heat dissipation upon cooling of the high-power LED package.

• 한국가스학회지
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• 제14권5호
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• pp.32-37
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• 2010

본 연구에서는 이산화탄소와 에탄 이성분계에 대해서 여러 등온 조건하에서 기액 상평형을 PRO/II with PROVISION (PRO/II) 전산 모사기에 내장되어 있는 Peng-Robinson (PR) 상태방정식의 이성분계 상호작용 매개변수를 이용하여 추산하였다. 또한, 이산화탄소와 에탄 이성분계의 각각의 등온 기액 상평형에 대해서 기포점 압력의 편차의 제곱에 대한 합산값을 목적함수로 하여 PR 상태방정식의 이성분계 상호작용 매개변수를 회귀분석을 통하여 새로 결정하였다. 기존의 PRO/II에 내장되어 있는 이성분계 상호작용 매개변수를 사용한 것과 새로 결정한 매개변수를 사용하여 기포점 압력의 편차의 절대값에 대한 평균값을 각각 비교하였다. 본 연구에서 새로 결정한 매개변수를 이용하여 추산한 결과가 기존의 PRO/II에 내장되어 있는 매개변수를 이용하여 추산한 결과보다 우수함을 알 수 있었다.

• 한국진공학회:학술대회논문집
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• 한국진공학회 2014년도 제46회 동계 정기학술대회 초록집
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• pp.258-258
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• 2014

Spark discharge in water generates shockwaves which have been utilized to generate mechanical actuation for potential use in pumping application. Discharge pulses of several microseconds generate shockwaves and vapor bubbles which subsequently displace the water for a period of milliseconds. Through the use of a sealed discharge chamber and metal bellow spring, the fluid motion can be used create an oscillating linear actuator. Continuous actuation of the bellow has been demonstrated through the use of high frequency spark discharge. Discharge in water forms a region of high electric field around the electrode tip which leads to the creation of a thermal plasma channel. This process produces fast thermal expansion, vapor and bubble generation, and a subsequent shockwave in the water which creates physical displacement of the water [1]. Previous work was been conducted to utilize the shockwave effect of spark discharge in water for the inactivation of bacteria, removal of mineral fouling, and the formation of sheet metal [2-4]. Pulses ranging from 25 to 40 kV and 600 to 900 A are generated inside of the chamber and the bellow motion is captured using a slow motion video camera. The maximum displacements measured are from 0.7 to 1.2 mm and show that there is a correlation between discharge energy input to the water and the displacement that is generated. Subsequent oscillations of the bellow are created by the spring force of the bellow and vapor in the chamber. Using microsecond shutter speed ICCD imaging, the development of the discharge bubble and spark can be observed and measured.

• 대한기계학회논문집B
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• 제35권10호
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• pp.1089-1095
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• 2011

열전달 향상을 위한 방법으로 많이 사용되고 있는 마이크로 핀을 포함한 표면 위에서의 핵비등을 액상과 기상에서 질량 및 운동량, 에너지에 대한 지배 방정식을 풀어 수치해석을 수행하였다. 핵비등에서의 기포거동을 계산하기 위해 sharp-interface 레벨셋(level-set) 방법을 상변화 효과와 핀과 캐비티와 같은 잠긴 고체에서의 점착 조건 및 접촉각, 마이크로 액체층에서의 증발 열유속을 포함하도록 수정하였다. 핀과 캐비티를 포함한 표면에서의 기포 생성, 성장, 이탈에 대한 해석을 통하여 핀-캐비티 배열, 핀-핀 간격이 핵비등에서의 기포거동에 중요한 역할을 하는 것을 확인하였다.