• 제목/요약/키워드: Liquid drop

검색결과 482건 처리시간 0.023초

마이크로핀 관의 기하학적 형상면화에 대한 열전달 특성(II) -증발 열전달- (Heat transfer with geometric shape of micro-fin tubes (II) -Evaporating heat transfer-)

  • 곽경민;장재식;배철호;정모
    • 설비공학논문집
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    • 제11권6호
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    • pp.789-798
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    • 1999
  • The evaporating heat transfer experiments with refrigerant HCFC 22 are performed for performance evaluation using 4 and 6 kinds of microfin tubes with outer diameter of 9.52mm and 7.0mm, respectively. Used microfin tubes have different shape and number of fins with each other, The experimental results are represented with effects of quality, mass flux and EPR. The evaporating heat transfer characteristics are represented by the existence of not only heat transfer area and turbulence promotion effect but also additional other enhancement mechanism, which are the overflow of the refrigerant over the microfin and microfin arrangement. Microfin tubes having a shape which can give much overflow over the microfin show large evaporating heat transfer coefficients. The effect of refrigerant overflow is much severe in evaporation than condensation. The effect of microfin arrangement is related to overflow effect of the refrigerant over the microfin.

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형상이 다른 수평 원형 전열관의 응축 성능에 관한 연구 (A Study on the Condensation Performance for the Horizontal Heat Transfer Tubes with Various Fin Attached)

  • 한규일;박종운
    • 수산해양교육연구
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    • 제4권1호
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    • pp.47-61
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    • 1992
  • An experimental study was carried out to investigate the condensation performance for the horizontal cylindrical heat transfer tube with various fin attached using R-11 vapor. The heat transfer tube used in this study was supplied by SUNG HYUNG METAL CO., LTD. Four different types of heat transfer tubes (plain tube, SH-CYR tube, thermocor tube and thermoexcel tube) were used. Each tube was surrounded by circular acrylate tube, and R-11 gas heated by boiler flows into the acrylate tube. Cooling water counter-flows in heat transfer tubes. Heat transfer coefficient of the plain tube from measured data was compared with those of three other tubes. The results are summarized as follows: 1. As the cooling water temperature decreased, the liquid film of R-11 turned to droplet drop on the top surface of the horizontal tube. 2. Heat transfer coefficient calculated theoretically was higher than that obtained from the experimental data. 3. As far as the condensation concerns the thermocor tube is the highest, the SH-CYR tube is the second, and the thermoexcel tube is the third excluding the plain tube.

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극한지 온도조건에 파이프라인 내부 열유동 영향변수 평가 (Numerical Study about Influence Variables of Permafrost Pipeline by using Thermal Flow Analysis)

  • 조철희;황수진;장춘만;이준호
    • 한국수소및신에너지학회논문집
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    • 제25권4호
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    • pp.443-448
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    • 2014
  • This paper describes thermal flow characteristics in various pipelines: straight pipeline and curved pipeline. In the permafrost area, pipelines are exposed to an extremely low temperature ($-40^{\circ}C$). In this situation, three-dimensional flow analysis should be analyzed to investigate thermal effects such as pressure drop, temperature change, velocity deficit and distribution change of liquid droplet of internal fluid. In this paper, multi-phase and multi-species analysis was introduced to analyze the flow characteristics of permafrost pipelines on the vertical support members above ground.

다단 원심펌프의 공동현상 유동해석 (Cavitating Flow Analysis of Multistage Centrifugal Pump)

  • 라키부자만;서상호;김형호;조민태;신병록
    • 한국유체기계학회 논문집
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    • 제18권1호
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    • pp.65-71
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    • 2015
  • The purpose of this study is to investigate cavitating flow of the multistage centrifugal pump. Cavitation is observed in the impeller leading edge and trailing edge of the suction area. Head coefficients are measured under different flow operating conditions. The Rayleigh-Plesset cavitation model is adapted to predict the occurrence of cavitation in the pump. The two-phase gas-liquid homogeneous CFD method is used to analyze the centrifugal pump performances with two equation transport turbulence model. The simulations are carried out with three different flow coefficients such as 0.103, 0.128 and 0.154. The occurrence of cavitation described according to water vapor volume fraction. The head versus NPSH (Net Positive Suction Head) also measured using different flow coefficients. Development of cavitation in the centrifugal pump impellerI is discussed. It is showed that the simulation represents the head drop about 3%.

이중 매니폴드 가변추력 분사기의 분무 특성에 관한 실험적 연구 (Experimental Study of Spray Characteristics on the Throttleable Dual Manifold Injector)

  • 윤정수;김성혁;윤영빈
    • 한국추진공학회지
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    • 제15권3호
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    • pp.22-30
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    • 2011
  • 추력변화를 위한 방법에는 여러 가지가 있는데, 고압력 강하 시스템, 이중 매니폴드 분사기, 가스 분사, 다중 챔버, 펄스 추력, 움직이는 분사기 구성요소 등이 있다. 이 중에서 이중 매니폴드 분사기의 경우에는 하나의 분사기 구조에 서로 다른 두 개의 매니폴드를 가지는 분사기를 결합하는 방식의 분사기인데, 각 분사기는 각각의 연료 공급시스템을 독립적으로 가지고 있어 각 매니폴드마다 독립적으로 유량을 조절 할 수 있다. 본 논문에서는 이중 매니폴드 분사기를 사용하여 넓은 추력범위에서 연료분사의 안정성을 판단하기 위하여 각 매니폴드의 접선방향 유입구 넓이의 비와 분사압력에 따라 분사 형상을 측정하고, 분사기 오리피스 끝단에서 액막 두께를 측정하였다.

고점도 용액 정밀토출을 위한 노즐 직경 및 표면젖음성 특성 연구 (Study of the Geometry and Wettability of Nozzles for Precise Ejection of High Viscous Liquids)

  • 이상현;배재현;이상민
    • 한국기계가공학회지
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    • 제20권12호
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    • pp.123-128
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    • 2021
  • Liquid dispensing systems are extensively used in various industries such as display, semiconductor, and battery manufacturing. Of the many types of dispensers, drop-on-demand piezoelectric jetting systems are widely used in semiconductor industries because of their ability to dispense minute volumes with high precision. However, due to the problems of nozzle clogging and undesirable dispensing behavior in these dispensers, which often result in device failure, the use of highly viscous fluids is limited. Accordingly, we studied the behaviors of droplet formation based on changes in viscosity. The effects of surface energy and the inner diameters of needle-type nozzles were also studied. Results showed that nozzles with lower surface energies reduced the ejection volume of droplets when a smaller nozzle diameter (0.21 mm in this study) was applied. These results indicate that the hydrophobic treatment of nozzle surfaces and the use of smaller nozzle diameters are critical factors enabling the use of highly viscous fluids in precision dispensing applications.

소수성 미니채널 내 움직이는 접촉선을 가진 액체슬러그의 압력 강하에 대한 수치해석 (Numerical study on pressure drop with moving contact lines of dry slug flow in a hydrophobic minichannel)

  • 전준호;박수청;유동인;김태훈;이연원
    • 한국가시화정보학회지
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    • 제18권3호
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    • pp.116-121
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    • 2020
  • In this study, a single-phase analysis of droplet slug with different contact angles was performed based on the visualization of experimental results. Droplet slug - flowing between gases in a hydrophobic mini channel - moves with a triple contact line without a gas liquid film on the wall. The results show that the rotational flow inside the droplet occurred; this was compared and verified with the results of two-phase analysis. The pressure field shows pressure rise at the front and rear ends. The effective length - the section that satisfies the laminar flow condition - became shorter as the droplet velocity increased. The Choi's correlation for the effective length agrees with this analysis results with a slight difference. This difference is judged as the difference in the contact angle of the slug model.

Wave plate 습분제거기의 형상 변경을 통한 성능 개선 (Performance improvement of wave plate mist eliminator through geometry modification)

  • 노정훈;조민철;이승종
    • 한국입자에어로졸학회지
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    • 제18권4호
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    • pp.97-107
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    • 2022
  • The geometry of popular wave plate type mist eliminator for the wet flue gas desulfurization process was improved, fabricated, and experimentally evaluated. A Mist eliminator is a type of inertial particle collector which collection efficiency is proportional to the velocity of the gas phase. However, as the amount of re-entrainment is also proportional to the gas phase velocity, there is a limitation for the gas phase flow rate. Re-entrainment is one of the most important issues in a mist eliminator and is likely to occur as the input of the liquid phase and flow rate of the gas phase increase. In order to resolve this problem, the projection angle of the improved mist eliminator is set to 30° from the conventional one while maintaining the cross-section. With low flow rate conditions, the modified mist eliminator showed a similar pressure drop and overall collection efficiency. However, with conditions in which re-entrainment is obviously occurring, the modified mist eliminator showed better performance in draining droplets than the conventional one. As a result, the modified mist eliminator showed higher overall collection efficiency.

쿨링 포그 시스템의 저압 안개 노즐 분무특성에 대한 실험적 연구 (Experimental Study on the Spray Characteristics of Low Pressure Fog Nozzles in Cooling Fog System)

  • 김지엽;정철;강원중;김정웅;홍정구
    • 한국분무공학회지
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    • 제27권4호
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    • pp.173-180
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    • 2022
  • Cooling fog is being used in various parts of society such as fine dust reduction, cleanliness, and temperature drop. Cooling fog has the advantage of low flow rate and ease of use compared to other spray systems. In the case of cooling fog, it was confirmed that the injection angle increased as the pressure increased and the nozzle diameter increased. In this study, the minimum injection angle was 33.61 degrees and the maximum injection angle was 107.38 degrees. It was confirmed that the larger the nozzle diameter and the smaller the pressure, the larger the droplet size. In addition, it was confirmed that the Sauter Mean Diameter (SMD) increased along the X and Y axis directions. It was confirmed that the size of the droplet decreases as it approaches the nozzle tip due to the characteristics of the nozzle design factor.

Plant-scale experiments of an air inflow accident under sub-atmospheric pressure by pipe break in an open-pool type research reactor

  • Donkoan Hwang;Nakjun Choi;WooHyun Jung;Taeil Kim;Yohan Lee;HangJin Jo
    • Nuclear Engineering and Technology
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    • 제55권5호
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    • pp.1604-1615
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    • 2023
  • In an open-pool type research reactor with a downward forced flow in the core, pipes can be under sub-atmospheric pressure because of the large pressure drop at the reactor core in the atmospheric pool. Sub-atmospheric pressure can result in air inflow into the pipe from the pressure difference between the atmosphere and the inside of the pipe, which in a postulated pipe break scenario can lead to the breakdown of the cooling pump. In this study, a plant-scale experiment was conducted to study air inflow in large piping systems by considering the actual operational conditions of an advanced research reactor. The air inflow rate was measured, and the entrained air was visualized to investigate the behavior of air inflow and flow regime depending on the pipe break size. In addition, the developed drift-flux model for a large vertical pipe with a diameter of 600 mm was compared with other correlations. The flow regime transition in a large vertical pipe under downward flow was also studied using the newly developed drift-flux model. Consequently, the characteristics of two-phase flow in a large vertical pipe were found to differ from those in small vertical pipes where liquid recirculation was not dominant.