• 대한기계학회논문집B
• /
• 제32권8호
• /
• pp.621-628
• /
• 2008

A numerical study for the flow, heat and mass transfer characteristics of the evaporating tube with the films flowing down on both the inside and outside tube walls has been carried out. The condensation occurs along the outside wall while the evaporation occurs at the free surface of the inside film. The transport equations for momentum and energy are parabolized by the boundary-layer approximation and solved by using the marching technique. The calculation domain of 2 film flow regions (evaporating and condensation films at the inside and outside tube wall respectively) and tube wall is solved simultaneously. The coupling technique for the problem with the 3 different regions and the 2 interfaces of them has been developed to calculate the temperature field. The velocity and temperature fields and the amount of the condensed and evaporated mass as well as the position where the evaporating film is completely dried out are successfully predicted for various inside pressures and inside film inlet flow rates.

• Journal of Advanced Marine Engineering and Technology
• /
• 제29권4호
• /
• pp.377-383
• /
• 2005

This paper deals with the flow characteristics of air-water two-phase flow in a vertical tube of 10mm I.D. and 600mm in length at an adiabatic condition. The obtained experimental data were covered with the liquid superficial velocity ranging from 0.095m/s to 2.56m/s. and the gas superficial velocity ranging from 0.032m/s to 21.08m/s. The effects of the gas and liquid superficial velocity on the flow pattern transitions, frictional pressure drop, and film thickness and gas-liquid interface roughness were also examined. It was found that the film thickness increased and the liquid film wave length was more longer with the liquid superficial velocity $j_L$ increasing at $j_G$ constant. It was also showed that the frictional pressure drops were experienced in three regions. namely increasing region(bubbly flow), decreasing region (Taylor bubble and slug flows) and re-increasing region (annular flow).

• 에너지공학
• /
• 제14권3호
• /
• pp.194-202
• /
• 2005

본 연구는 다양한 수직 액막형 흡수기에서 열 및 물질전달 과정에 따른 흡수 특성 예측을 이론 및 실험적으로 수행하였다. 열 및 물질전달 향상은 해석적으로 조사되었으며, 흡수 성능에 대한 유동 형태, 삽입기구 및 주름에 의한 형상 변수의 영향 등을 조사하였다. 특히, 최대 흡수 성능에 대한 동적 변수(수용액 유량, 유동형태)와 흡수기 형상(ID=22.8mm, L=1150m)의 최적값을 수치 해석적으로 예측하였다 수치 해석 및 실험에서 최대 흡수 성능은 삽입기구(스프링)에 의한 파동 유동에서 나타났다.

• 설비공학논문집
• /
• 제25권5호
• /
• pp.246-254
• /
• 2013

Some characteristics of nitrogen-water slug flow were optically measured, in vertical acrylic tubes of 2, 5 and 8 mm diameter. Bubble velocity, bubble and unit cell lengths were measured, by analyzing the light intensity signals from two sets of dot laser-infrared sensor modules mounted along the transparent tubes. Optical images of the bubbles were also taken and analyzed, to measure bubble shapes and liquid film thickness. It was found that the measured bubble velocities were in good agreement with the empirical models in the literature, except for those measured under high superficial velocity condition in the 2 mm tube. Bubble length was found to be the longest in the 2 mm tube, being 4 to 5 times those of the other tubes. Liquid film was found to have developed early in the 2 mm tube, which made the blunt shape of the bubble head. Liquid film thickness in the 8 mm tube was measured at almost twice those of the other tubes.

• 한국산학기술학회논문지
• /
• 제16권5호
• /
• pp.3022-3029
• /
• 2015

본 연구에서는 물과 비 혼합 비 공비 물질을 작동 유체로 사용하는 가시화 실험 장치를 제작하여 열유속을 증가시키며 시간에 따른 벽면온도 특성과 내부 유동를 카메라로 연속 촬영하며 2유체 열사이폰의 내부의 유동 및 열전달 특성에 대하여 가시적 방법으로 실험을 수행하여 실험 결과로부터 다음과 같은 결론을 얻을 수 있었다. 물과 FC40을 사용한 비 혼합 2유체 열사이폰은 열유속의 크기에 따라 자연대류, 펄스비등, 연속비등의 세가지 영역으로 구분 되었으며 비등은 증기압이 낮은 물에서 발생하였다. 자연대류에서는 액체 풀에서 물의 증발과 대류 액막 유동이 발생하였다. 액체 풀에서 비등이 발생할 때에는 강한 비등에 의하여 FC40과 물의 혼합된 상태로 전 영역에 걸쳐 기-액 이상 유동이 발생하였다.

• 설비공학논문집
• /
• 제13권4호
• /
• pp.225-232
• /
• 2001

An experimental study is carried out to investigate the characteristics of heat transfer of outside helical tubes. The main heat exchanger consists of twelve curved columns with each 300mm diameter and the total length of 1.2m copper tube having an outer diameter of 19.05mm with 1.5mm thickness. Water flows down the outside of helical tube, where flow patterns are the vertical film falling flow, immerged flow, and mixed-flow which is the combination of film falling flow and immerged flow. Refrigerant 11 flow the inside of the tube countercurrently. The experimental range of inside flow rate is 1.7~3.2$\ell$/min and outside flow rate is 21-33$\ell$/min. The results are presented as Nusselt number with corresponding Reynolds number for variety of outside and inside flow rates. The heat transfer rates of the mixed flow are 8 to 56% higher than those of film falling flow or immerged flow only. Interpretation of the results is given on the basis of physical reasoning and the correlation equations.

• 한국분무공학회지
• /
• 제7권4호
• /
• pp.32-41
• /
• 2002

The breakup characteristics of liquid sheets formed by like-doublet injector were investigated in the cold-flow and atmospheric ambient pressure condition. The sheet breakup wavelength, which induces the sheet to be broken into ligaments, as well as the sheet breakup length, which is important for the flame location, was measured using a stroboscopic light. The liquid ligaments are formed intermittently after the breakup of sheet, and the wavelength of ligaments has been believed to have a relation to the combustion instability of liquid rocket engine. Therefore, the wavelength of ligaments and the breakup length of ligaments into fine drops were also measured. Since these spray characteristics are affected by the flow characteristics of two liquid jets before they impinge on each other, we focused on the effects of orifice internal flow such as the cavitation phenomenon that occurs inside the sharp-edged orifice. From the experimental results, we found that the liquid jet turbulence delays the sheet breakup and makes shorter wavelengths for both sheets and ligaments. Since the turbulent strength of sharp-edged orifice is stronger than that of round-edged orifice, the shape of orifice entrance results in large differences in the spray characteristics. Using these results, we proposed empirical models on the spray characteristics of the like-doublet injector, and these models are believed to provide some useful and actual data for designing liquid rocket combustors.

• 에너지공학
• /
• 제22권4호
• /
• pp.362-369
• /
• 2013

이상유동은 원자력 발전소 내 노심과 석유 수송 등 여러 산업 분야에서 빈번히 관찰된다. 이상유동영역은 두 상의 성질과 유량의 차이, 그리고 유로의 구조에 따라 결정된다. 유동영역의 판별은 시스템 설계 및 안전 해석에 있어 중요하기 때문에 많은 이론과 실험 연구들이 수행되었다. 본 연구는 파이프 내의 이상유동장에서 각 이상유동영역 및 천이경계에서의 특징 파악을 위한 기초 연구로서, 30 mm의 내경을 갖는 수직관의 수직상향류 공기-물 이상유동영역을 고속카메라와 Wire-mesh sensor(WMS)를 이용하여 판별하였다. 또한 유동양식을 정량적으로 판별하기 위해 액막 두께를 적용하였다. 판별한 실험 데이터를 Taitel 외와 Mishima와 Ishii의 유동양식선도와 비교하였다. 실험을 통해 판별한 유동영역은 기존의 유동양식선도와 전체적으로 잘 일치함을 보였다.

• 한국추진공학회:학술대회논문집
• /
• 한국추진공학회 2009년도 춘계학술대회 논문집
• /
• pp.267-274
• /
• 2009

아음속 영역의 대류에 평행하게 압력형 스월 제트를 분사시켜 액막 분열 및 액적 크기와 분포를 실험적으로 측정하였다. 대류로 인한 거시적과 미시적인 분무 특성의 영향을 제트 $We_{\iota}$수와 기상에 대한 액상의 운동량 비를 사용하여 광학적인 방법으로 측정하였다. 낮은 제트 $We_{\iota}$수일 때는 제트의 원심력 부족으로 인해 액막을 형성하지 못하고 Rayleigh 제트 분열을 하게 된다. 높은 $We_{\iota}$수에서는 거시적인 분무 특성은 대류의 영향을 거의 받지 않지만 미시적인 분무 특성은 운동량 비가 높을수록 2차 미립화 과정을 통해 대류의 영향을 많이 받았다. 대류는 제트의 분열을 촉진시키고 스월 제트의 분무 특성을 향상하는 것으로 관찰되었다.

• 한국마린엔지니어링학회:학술대회논문집
• /
• 한국마린엔지니어링학회 2002년도 춘계학술대회논문집
• /
• pp.83-88
• /
• 2002

This study is to provide the experimental information and basic data on heat transfer characteristics of horizontal liquid film driven by hot wind. Heat transfer characteristics of the liquid film in the rectangular duct was observed and the change of film temperature was measured. The experiments were carried out for a variety of parameter, such as feed water rate and velocity and temperature of feed air. From the observation and the measurement the general understanding of heat transfer characteristics for liquid film driven by hot wind was provided.