• Journal of Advanced Marine Engineering and Technology
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• 제39권7호
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• pp.696-701
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• 2015

본 연구에서는 깊이 0.2 mm, 폭 0.45 mm, 길이 60mm 그리고 채널의 개수는 15개인 마이크로 채널에서 이상 유동비등에 관한 실험을 수행하였다. 작동유체로는 FC-72가 사용되었으며, 실험은 질량유속과 열유속 각각 $200-400kg/m^2s$, $5-40kW/m^2$ 범위와 증기 건도 0.1-0.9 범위에서 수행되었다. 열전달 계수는 낮은 열유속에서는 급격하게 감소하였으며, 일정 열유속 이상에서는 거의 일정하게 유지되었다. 측정된 열전달 계수로부터 기존의 방법을 이용하여 기포류, 슬러그류, 천류 그리고 파형/환상류의 유동양식으로 분류하였다. 또한 분류한 유동양식의 결과를 파형/환상류 영역으로의 천이 기준과 비교하였다. 하지만 기존의 천이 기준으로는 본 연구의 실험결과를 만족스럽게 예측하지 못하였다.

• 대한기계학회논문집B
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• 제41권1호
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• pp.29-36
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• 2017

본 논문은 환형노즐 이젝터를 이용하여 세정수 공급과 기포생성을 동시에 할 수 있는 세정기술 개발을 위한 기초연구를 목적으로 한다. 환형노즐 이젝터의 피치변화에 따른 구동 및 부유체의 정량적 유동특성과 세정수조에 분출되는 분류의 정성적 가시화 이미지를 분석하였으며, 세정물의 농약 잔류물 성분의 농도를 검증하였다. 피치가 증가하면 구동유량은 증가하는 반면에, 유량비는 감소하였다. 피치가 증가하면 분류는 부력분류나 평형분류 거동을 나타내며, 잔류농약의 농도는 감소 후 증가하였다.

• 한국가시화정보학회지
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• 제10권2호
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• pp.14-19
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• 2012

An optical fiber probe system for measuring the local void fraction in the air-water two-phase flow was developed with a 1550 nm light source. Air was injected through a nozzle placed in the center of the bottom wall of a water-filled cylindrical tank. The optical fiber probe having a diameter of $125{\mu}m$ was sufficiently thin to resolve the air-water interface of the bubbly flows. To verify the performance of the optical fiber probe, the synchronized high speed visualization study using a high speed camera was carried out. Comparison between the optical signals and the instantaneous bubble diffraction images confirms that the optical fiber probe is very accurate to measure the void fraction in two-phase flows. The estimated bubble diameter and the rising velocity by the optical fiber probe have 1% and 5% of accuracy, respectively.

• 대한기계학회논문집B
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• 제31권11호
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• pp.904-911
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• 2007

A measurement technique fur void fraction has been proposed using a time-resolved two-phase PIV system and the bubble dynamics has been investigated in gas-liquid two-phase flows. For the three-dimensional evaluation of the bubble information, both the images from the front and side views are simultaneously recorded into a high speed CCD camera by reflecting the side view image on a $45^{\circ}$ oriented mirror to be juxtaposed with the front view image. Then, a stereo-matching technique is applied to calculate the void fraction, bubble size and shape. To obtain the rising bubble velocities, the 2-frame PTV method was adopted. The present technique is applied to freely rising bubby flows in stagnant liquid. The results show that the increase of bubble flow rate gives rise to the increase of bubble size and rising velocity at first. If it goes over a certain level, the rising velocity becomes constant and the horizontal velocity grows bigger instead due to the obstruction of other bubbles.

• Nuclear Engineering and Technology
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• 제54권12호
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• pp.4776-4797
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• 2022

In the one-dimensional thermal-hydraulic (TH) codes, a subcooled boiling model to predict the void fraction profiles in a vertical channel consists of wall heat flux partitioning, the vapor condensation rate, the bubbly-to-slug flow transition criterion, and drift-flux models. Model performance has been investigated in detail, and necessary refinements have been incorporated into the Safety and Performance Analysis Code (SPACE) developed by the Korean nuclear industry for the safety analysis of pressurized water reactors (PWRs). The necessary refinements to models related to pumping factor, net vapor generation (NVG), vapor condensation, and drift-flux velocity were investigated in this study. In particular, a new NVG empirical correlation was also developed using artificial neural network (ANN) techniques. Simulations of a series of subcooled flow boiling experiments at pressures ranging from 1 to 149.9 bar were performed with the refined SPACE code, and reasonable agreement with the experimental data for the void fraction in the vertical channel was obtained. From the root-mean-square (RMS) error analysis for the predicted void fraction in the subcooled boiling region, the results with the refined SPACE code produce the best predictions for the entire pressure range compared to those using the original SPACE and RELAP5 codes.

• 대한기계학회논문집B
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• 제38권2호
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• pp.139-146
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• 2014

수소화붕소나트륨은 수소 에너지를 저장 및 공급할 수 있는 안정된 금속 물질이다. 본 논문에서는 탈수소 화학반응기 유로 설계를 위해 수력학적 직경 $461{\mu}m$를 가지는 마이크로채널에서 수소화붕소나트륨 수용액의 탈수소 화학반응이 일어날 때 수용액과 수소 기체 간의 이상유동 계면마찰에 대하여 실험연구를 수행하였다. 화학반응기 마이크로채널은 직사각 단면으로 높이 $300{\mu}m$, 너비 1 mm, 길이 50 mm 로 실리콘 웨이퍼에 공정되었으며, 가수분해 촉진을 위해 루테늄을 촉매로서 100 nm 두께로 채널 표면에 증착하였다. 가시화 결과 Re 수 30 이하에서 기포유동 양상이 관측되었다. 이상마찰승수는 기포율에 선형적으로 비례하며, 탈수소 화학반응기를 설계할 때 계면마찰에 영향을 미치는 수용액의 초기농도, 촉매 화학반응률, 체류시간을 고려해야 된다.

• 대한기계학회논문집
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• 제10권3호
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• pp.335-342
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• 1986

본 연구에서는 이러한 가능성을 알아 보기 위하여 오리피스판을 통하여 기액 2상흐름이 있을 때 각 상의 유량변화레 따른 순간압력강하치를 분석하고자 한다. 우선 평균압력강하치를 측정하여 식 (1)과 비교 분석하며, 교란치의 평균진폭과 교란 강도를 구하여 기공율의 변화에 따른 이러한 통계치들의 경향을 고찰한다. 그리고 순간압력강하 곡선에 대한 통계함수들, 확률밀도함수(probability density function) 와 자기상관함수(auto-correlation function)을 구하여 이 들의 통계적 성질을 구명 하고 2상 유동량의 결정에 대한 교란치의 할동도를 토의한다.

• Journal of Korean Society for Atmospheric Environment
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• 제15권E호
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• pp.17-28
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• 1999

Gas-liquid contact tests above a perforated-plate were conducted with air and water at flooding gas-flow conditions in order to study two-phase flow characteristics in a limestone-gypsum SO2 absorber. Gas layers were in the form of air pockets and confined to the limited areas around each duct pipe, while the remaining tary area were in the wet condition. The liquid above the tray was always in the flooded and even fluidized conditions at gas flows over the range studied, although vigorous bubbly or churn-turbulent two-phase regime was only observed in the immediate vicinity of the gas hole exit at low gas loads. The froth zone was extremely active to provide intimate contact between gas and liquid so that the necessary mass transfer operation can take place, which is the primary purpose of high-performance SO2 absorbers. Howefer, the absorber $\Delta$P was 250mmH2O for the initial water level at 150mm, which is an important issue to be resolved for economical operation of the SO2 absorber. It was seen in the liquid level-and gas flow-transient tests that changes in the absorber liquid inventory were much more pronounced for intimate gas-liquid contact than changes in the gas flow. Based on the 4- and 8-duct pipe test results, grouping the duct pipes near the center of the test tray seemed to promote better recirulation of liquid from gas-liquid contact zone back to the reaction tank so that the absorbed SO2 can be neutralized.

• 한국해양공학회지
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• 제30권1호
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• pp.44-50
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• 2016

An experimental study was performed to investigate the behavior of green water on a structure with a rectangular cross section under wave conditions, along with the flow characteristics in bubbly water flow. An experiment was conducted in a two-dimensional wave flume using an acrylic model (1/125) of FPSO BW Pioneer operating in the Gulf of Mexico under its design wave condition. The occurrence of green water, including its development, in front of the model was captured using a high-speed Charge Coupled Device (CCD) camera with the shadowgraph technique. Using consecutive images, the generation procedure for green water on the model was divided into five phases: flip through, air entrapment, wave run-up, wave overturning, and water shipping. In addition, the distinct water elevations of the green water were defined as the height of flip through, height of splashing jet, and height of freeboard exceedance, and showed a linear relationship with the incoming wave height.

• 한국가시화정보학회지
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• 제15권2호
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• pp.59-67
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• 2017

To verify floatability of ABB (Air bubble barrier), we compared bubble swarm behavior with and without the air-driven ejector. Experiment was conducted using the fabricated air-driven ejector with 5 mm nozzle on the bottom of 1 m3 water tank. Reynolds number of air in the nozzle was ranged 1766-13248. We analyzed data with statistical method using image processing, particle mage velocimetry (PIV) and proper orthogonal decomposition (POD) analysis. As a result of POD analysis, there was no significant eigenmode in bubbly flow generated from the ejector. It means that more complex turbulent flows were formed by the ejector, thereby (1) making bubbles finer, (2) promoting three-dimensional energy transfer between bubble and water, and (3) making evenly distributed velocity profile of water. It is concluded that the air-driven ejector could enhance the performance of ABB.