• 제목/요약/키워드: Liquid Slug

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PREDICT10N OF THE ONSET OF SLUG FLOW IN NEARLY HORIZONTAL AIR-WATER COUNTERCURRENT FLOW

  • Yu, Seon-Oh;Chun, Moon-Hyun;Kim, Yang-Seok
    • 한국원자력학회:학술대회논문집
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    • 한국원자력학회 1997년도 춘계학술발표회논문집(1)
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    • pp.368-373
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    • 1997
  • The transition from a statified wavy to a slug flow has been analyzed considering the mechanistic forces acting on the wave crest in a nearly horizontal air-water countercurrent flow. To verify the results of the analysis, a series of experiments have been performed changing the inclination angle of the test section. Comparisons of the theoretical predictions with experimental data show a good agreement and the results show that the present model gives similar results of Taitel and Dukler's in the case of inclined pipes. However, at high superficial liquid velocity, the results of present work agree more closely with data than that of Taitel and Dukler's. Also, predictions of the present model gives a very close agreement with the experimental data for various tube sizes obtained by others.

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소형 공기 양수 펌프의 불규칙한 가스-액체 흐름의 CFD 모델링 (CFD Modeling of Unsteady Gas-Liquid Flow in a Small Scale Air-Lift Pump)

  • 이설송;정효민;정한식
    • 동력기계공학회지
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    • 제16권1호
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    • pp.30-37
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    • 2012
  • 공기 양수 펌프는 재생 에너지 분야, 부식 및 마모 특성의 유체의 활용 등 높은 신뢰성과 낮은 유지보수 비용을 필요로 하는 분야에서 그 사용이 증대되고 있다. 본 연구에서는 소형 공기 양수 펌프의 성능 평가 및 기초 데이터를 얻기 위한 연구로, D=0.012~0.019m, L=0.933m인 배관의 침수 깊이(${\beta}$=0.55,0.60,0.65,0.70)에 따른 수치해석을 수행하였다. 수치 해석 및 실험 결과는 유사성을 뛰었으며, 펌프의 사양과 효율은 공기의 질량 유속 비, 침수 깊이 비와 양수 배관의 길이에 관한 함수로 나타났다. 그리고 최대 물과 공기 질량 유속의 비는 각 배관에서 서로 다른 침수 깊이의 비로 나타났으며, 공기 양수 펌프의 최대 효율이 발생되는 운전조건은 슬러그(slug)와 슬러그 교반 정도(slug-churn flow regime)에 따라 나타남을 알 수 있었다.

Bubbly, Slug, and Annular Two-Phase Flow in Tight-Lattice Subchannels

  • Prasser, Horst-Michael;Bolesch, Christian;Cramer, Kerstin;Ito, Daisuke;Papadopoulos, Petros;Saxena, Abhishek;Zboray, Robert
    • Nuclear Engineering and Technology
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    • 제48권4호
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    • pp.847-858
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    • 2016
  • An overview is given on the work of the Laboratory of Nuclear Energy Systems at ETH, Zurich (ETHZ) and of the Laboratory of Thermal Hydraulics at Paul Scherrer Institute (PSI), Switzerland on tight-lattice bundles. Two-phase flow in subchannels of a tight triangular lattice was studied experimentally and by computational fluid dynamics simulations. Two adiabatic facilities were used: (1) a vertical channel modeling a pair of neighboring sub-channels; and (2) an arrangement of four subchannels with one subchannel in the center. The first geometry was equipped with two electrical film sensors placed on opposing rod surfaces forming the subchannel gap. They recorded 2D liquid film thickness distributions on a domain of $16{\times}64$ measuring points each, with a time resolution of 10 kHz. In the bubbly and slug flow regime, information on the bubble size, shape, and velocity and the residual liquid film thickness underneath the bubbles were obtained. The second channel was investigated using cold neutron tomography, which allowed the measurement of average liquid film profiles showing the effect of spacer grids with vanes. The results were reproduced by large eddy simulation + volume of fluid. In the outlook, a novel nonadiabatic subchannel experiment is introduced that can be driven to steady-state dryout. A refrigerant is heated by a heavy water circuit, which allows the application of cold neutron tomography.

기포유동층 고분자 중합 반응기에서의 슬러그 특성 (Slug Characteristics in a Bubbling Fluidized Bed Reactor for Polymerization Reaction)

  • 고은솔;강서영;서수빈;김형우;이시훈
    • Korean Chemical Engineering Research
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    • 제58권4호
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    • pp.651-657
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    • 2020
  • 고체 입자들이 유체처럼 움직이는 유동층 공정은 에너지 전환 공정뿐만 아니라 범용 고분자 수지의 생산 공정에도 이용되고 있다. 범용 고분자 수지 중의 하나인 LLDPE(Linear low density polyethylene)도 기포 유동층 공정을 통해 전세계에서 생산되고 있다. 입자 크기에 비해 밀도가 낮은 LLDPE 입자들은 고분자 중합 반응을 위해 공급되는 수소에 의해서 유동화된다. 그러나 LLDPE 생산 공정은 기포유동층 공정임에도 불구하고 발생한 슬러그로 인하여 반응에 영향을 끼쳐 공정의 효율 저하를 불러올 수 있다. 이에 본 연구에서는 상용 고분자 반응기를 모사한 pilot 규모의 고분자 합성 반응기(0.38 m l.D., 4.4 m High)와 동일한 시뮬레이션 모델을 구축하여 LLDPE 입자의 유동화 상태를 고찰하였다. 특히 기체 유속(0.45-1.2 m/s), 고체 입자 밀도(900-1900 kg/㎥), 입자 구형도(0.5-1.0), 입자 크기(120-1230 ㎛)의 변화에 따른 슬러그 특성을 세밀하게 고찰하기 위하여 전산입자유체해석(Computational particle-fluid dynamics, CPFD)을 이용하였다. CPFD를 통해서 일부 실험자들만 고찰할 수 있었던 flat slug의 발생을 시각적으로 구현하였으며 밀도, 구형도, 크기 등의 고체의 물리적 특성을 변화시킴에 따라 슬러그 발생을 저감시킬 수 있음을 확인하였다.

Liquid phase hydrogen peroxide decomposition for micro-propulsion applications

  • McDevitt, M. Ryan;Hitt, Darren L.
    • Advances in aircraft and spacecraft science
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    • 제4권1호
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    • pp.21-35
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    • 2017
  • Hydrogen peroxide is being considered as a monopropellant in micropropulsion systems for the next generation of miniaturized satellites ('nanosats') due to its high energy density, modest specific impulse and green characteristics. Efforts at the University of Vermont have focused on the development of a MEMS-based microthruster that uses a novel slug flow monopropellant injection scheme to generate thrust and impulse-bits commensurate with the intended micropropulsion application. The present study is a computational effort to investigate the initial decomposition of the monopropellant as it enters the catalytic chamber, and to compare the impact of the monopropellant injection scheme on decomposition performance. Two-dimensional numerical studies of the monopropellant in microchannel geometries have been developed and used to characterize the performance of the monopropellant before vaporization occurs. The results of these studies show that monopropellant in the lamellar flow regime, which lacks a non-diffusive mixing mechanism, does not decompose at a rate that is suitable for the microthruster dimensions. In contrast, monopropellant in the slug flow regime decomposes 57% faster than lamellar flow for a given length, indicating that the monopropellant injection scheme has potential benefits for the performance of the microthruster.

2중판 오리피스를 이용한 기액 2상유량계의 개발 (Development of a 9as-liquid two-phase flowmeter using double orifice plates)

  • 이상천;이상무;남상철
    • 설비공학논문집
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    • 제10권5호
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    • pp.619-629
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    • 1998
  • An experimental work was conducted to investigate a feasibility of simultaneous measurement of gas-liquid two-phase flowrates with double orifice plates using air and water. The tests were carried out under the atmospheric pressure and at the ambient temperature using two different tube sizes. Qualities of an air-water flow in the present study have values less than 0.1 and thus the mixed flow showed bubbly, plug, slug flow regimes. The probability density function (PDF) and the power spectral density function (PSDF) of the instantaneous pressure drop traces for the flow regimes were obtained. It is found that some distinctive features exist in the distribution of these functions, depending upon the two-phase flow pattern. The time-averaged value of the instantaneous pressure drop increases with increasing gas and liquid flowrates, showing a single-valued function for the total mass flowrate and the quality. It is also found that the two-phase discharge coefficient exhibits a consistent trend for variation of dimensionless parameters such as the superficial velocity ratio and the gas Reynolds number. The results indicate that simultaneous measurement of two-phase flowrate may be possible based upon a statistical analysis of the instantaneous pressure drop curves monitored using double orifice plates.

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An Experimental Study of The Effects of The Mixing Vane on Air-water Mixed Flow

  • Kim, Soo-Hyung;Baek, Won-Pil;Chang, Soon-Heung
    • 한국원자력학회:학술대회논문집
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    • 한국원자력학회 1996년도 춘계학술발표회논문집(2)
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    • pp.331-336
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    • 1996
  • The effects of a mixing vane on air-water mixed flow have been experimentally studied in this work, to investigate the basic mechanisms that the mixing vane affects critical heat flux (CHF). Experiment was performed for various flow rates focusing on bubbly flow and annular flow patterns. Acrylic tube (1.7m long, 11 mm I.D.) and the split vane type mixing vane were used, and ring-type conductance probes were used to measure the liquid film thickness in annular flow. Experimental results show that, (a) bubbly-to slug flow transition and churn-to-annular flow transition occur respectively near the mixing vane compared to the tests without mixing vane, (b) in bubbly flow region, the mixing vane breaks the bubbles into smaller ones and forwards bubbles to the center region of the tube by the centrifugal force, (c) the liquid film thickness in annular flow is decreased near the mixing vane for mass fluxes.

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Review on Gas-Voiding Models for HCDA(Hypothetical Core Disruptive Accident) Initiating Phase in LMR Analysis (I)

  • Chang, W.P.;Kwon, Y.M.;Hahn, D.H.;Suk, S.D.
    • Nuclear Engineering and Technology
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    • 제31권6호
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    • pp.51-65
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    • 1999
  • The present review report introduces the existing analysis codes and physical modeling of two-phase flow associated with initiating event of HCDA in Liquid Metal Reactors for the effective study in the future, because the related research has not been systematically carried out in Korea compared with other areas. The description in this report is specifically addressed to the results yielded from careful review of the technical concepts on the two-phase flow modeling in the SAS2A code which was developed in ANL. The report is prepared in 2 parts based on the definite physical phenomena. The liquid slug and gas behavior models are main representations in the part (I) and (II), respectively. In this regard, it is expected that this report provide a fundamental knowledge on the two-phase flow model in LMR and, thus, contribute to establishment of the necessary HCDA analysis technology concerned with the LMR development in Korea.

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수직관에서 상승하는 Taylor 기포의 수치해석 (Numerical Simulation of a Taylor Bubble Rising in a Vertical Tube)

  • 손기헌
    • 대한기계학회논문집B
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    • 제25권3호
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    • pp.373-380
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    • 2001
  • In this study, a single Taylor bubble and a train of Taylor bubbles rising in a vertical tube were simulated numerically. A finite difference method was used to solve the mass and momentum equations for the liquid-gas region. The liquid-gas interface was captured by a level set function which is defined a signed distance from the interface. For a train of Taylor bubbles repeated periodically in space, the periodic conditions were imposed at the boundaries normal to the gravitational direction and the pressure boundary conditions were iteratively determined so that the computed flow rate should be equal to a given flow rate. Based on the numerical simulation, the calculated shape and rise velocity of a Taylor bubble were found to be in good agreement with the experimental data reported in the literature.

Development of Sodium Voiding Model for the KALIMER Analysis

  • Chang, Won-Pyo;Dohee Hahn
    • Nuclear Engineering and Technology
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    • 제34권4호
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    • pp.286-300
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    • 2002
  • An algorithm for the sodium boiling model has been developed for calculation of the void reactivity feedback as well as the fuel and cladding temperatures in the KALIMER core after onset of sodium boiling. Modeling of sodium boiling in liquid metal reactors using sodium as a coolant is necessary because of phenomenon difference comparing with that observed generally in light water reactor systems. The applied model to the algorithm is the multiple-bubble slug ejection model. It allows a finite number of bubbles in a channel at any time. Voiding is assumed to result from formation of bubbies that (ill the whole cross section of the coolant channel except for the liquid film left on the cladding surface. The vapor pressure, currently, is assumed to be uniform within a bubble The present study is focused on not only demonstration of the vapor bubble behavior predicted by the developed model, but also confirmation of a qualitative acceptance for the model. As a result, the model can represent important phenomena in the sodium boiling, but it is found that further effort is also needed for its completition.