• 제목/요약/키워드: Vertical upward flow

검색결과 88건 처리시간 0.02초

수직상향 기액이상류의 유동특성 (Flow Characteristics of Vertical Upward Gas-Liquid Two-Phase Flow)

  • 최부홍
    • Journal of Advanced Marine Engineering and Technology
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    • 제29권4호
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    • pp.377-383
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    • 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).

T형 수평 및 수직 입구 분지관 내 냉매 2상 유동 특성 (Two-phase Flow Characteristics of Refrigerant in T-branch with Horizontal and Vertical Inlet Tube)

  • 태상진;조금남
    • 설비공학논문집
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    • 제14권9호
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    • pp.741-748
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    • 2002
  • The present study investigated the two-phase flow characteristics of refrigerant R-22 in T-branch with horizontal and vertical inlet tube The key experimental parameters were the orientation of inlet and branch tubes (horizontal and vertical), diameter ratio of branch tube to inlet tube (1 and 0.61), inlet mass flux (200~500 kg/$m^2$s) and inlet quality (0.1~0.4). Predicted pressure profile agreed with the measured data within 25.4%. The flow distribution ratio decreased as the mass flux increased. The flow distribution ratio decreased by 12~25% as the tube diameter ratio decreased from 1 to 0.61, and decreased by 38~47% as the orientation of branch changed from horizontal to vertical upward for horizontal inlet tubes. As the orientation of inlet tube changed from horizontal to vertical upward for horizontal branch, the flow distribution ratio increased by 15~68%, but the quality in the branch tube decreased by 28~92% due to phase separation.

TURBULENCE MODULATION OF THE UPWARD TURBULENT BUBBLY FLOW IN VERTICAL DUCTS

  • ZHANG, HONGNA;YOKOMINE, TAKEHIKO;KUNUGI, TOMOAKI
    • Nuclear Engineering and Technology
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    • 제47권5호
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    • pp.513-522
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    • 2015
  • The present paper aims at improving the modeling of turbulence for the upward turbulent bubbly flow through the use of experimental databases that contain data on small and large vertical ducts. First, the role of bubble-induced turbulence was analyzed, which indicated the dominant role of the bubble-induced turbulence in the duct center for relatively high void fraction cases. Therefore, the turbulence therein was mainly focused on, which indicated that the stronger turbulence could be induced by bubbles in large ducts with similar void fractions as compared to that in small ducts. Next, the turbulence of upward turbulent bubbly flow near the wall is discussed to understand the interaction between the wall-induced and bubble-induced turbulence. It showed that the existence of a wall could suppress the bubble-induced turbulence given the same void fraction, and the existence of bubbles could also suppress the solely wall-induced turbulence as compared to the single-phase turbulent flow, even though the total turbulence is enhanced. The above characteristics indicated that the current turbulence modeling method needs to be modified, especially when the bubble-induced turbulence plays a dominant role.

영상기법을 이용한 수직상향 기포유동에 관한 연구 (A Study on the Vertical upward Bubble Flow using Image Processing Technique)

  • 서동표;오율권
    • Journal of Advanced Marine Engineering and Technology
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    • 제27권5호
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    • pp.617-623
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    • 2003
  • In the present study, the characteristics of upward bubble flow were experimentally investigated in a liquid bath. The velocity of upward bubble flow was calculated for two different experimental conditions:1) bubble flow without kinetic energy 2) bubble flow with kinetic energy. Bubble flow without kinetic energy starts to undergo the effect of buoyancy l0cm away from the nozzle. Whereas. kinetic energy is dominant before 30 cm away from the nozzle in bubble flow but after this point kinetic energy and inertial force are applied on bubble flow at the same time In addition, as the flow rate increases the maximum velocity point moves to the nozzle. The velocity Profiles near free surface is extremely irregular due to surface flow. Gas volume fraction is high near the nozzle due to gas concentration. but decreases with the increasement of axial position. Gas volume fraction does not vary after the axial position, z=60 in spite of the increasement of flow.

통계적 보이드율계측에 의한 수직상향이상류의 유동양식과 보이드분포 분석 (Analyses of the Flow Patterns and Void Distribution in Vertical Upward Two Phase Flow with the Statistical Void Fraction Measurement)

  • 손병진;김인석;이진
    • 대한설비공학회지:설비저널
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    • 제15권3호
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    • pp.283-291
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    • 1986
  • An experimental study has been conducted to investigate characteristics of the flow patterns, its transitions and the mean local void fraction obtained from which the probe was traversed diametrically from center to wall of the test section in the vertical upward air-water flow for isothermal condition using the electrical conductivity probe. It has been shown that the probability density function of the mean local void fraction measured statistically from a Fast Fourier Transform becomes a criterion for the flow patterns and the mean local void fraction profile is a highly function of the flow patterns.

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수직 동심 환형관 내의 난류혼합대류 현상에 관한 직접수치모사 (Direct Numerical Simulation of Turbulent Mixed Convection in Heated Vertical Annulus)

  • 전용준;배중헌;유정열
    • 대한기계학회논문집B
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    • 제33권9호
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    • pp.674-681
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    • 2009
  • Turbulent mixed convection in heated vertical annulus is investigated using Direct Numerical Simulation (DNS) technique. The objective of this study is to find out the effect of buoyancy on turbulent mixed convection in heated vertical annulus. Downward and upward flows with bulk Reynolds number 8500, based on hydraulic diameter and mean velocity, have been simulated to investigate turbulent mixed convection by gradually increasing the effect of buoyancy. With increased heat flux, heat transfer coefficient first decreases and then increases in the upward flow due to the effect of buoyancy, but it gradually increases in downward flow. The mean velocity and temperature profiles can not be explained by the wall log laws due to the effect of buoyancy, too. All simulation results are in good quantitative agreement with existing numerical results and in good qualitative agreement with existing experimental results.

수직 동심 환형관 내의 난류혼합대류 현상에 관한 직접수치모사 (Direct numerical simulation of turbulent mixed convection in heated vertical annulus)

  • 전용준;배중헌;유정열
    • 대한기계학회:학술대회논문집
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    • 대한기계학회 2008년도 추계학술대회B
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    • pp.2759-2764
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    • 2008
  • Turbulent mixed convection in heated vertical annulus is investigated using Direct Numerical Simulation (DNS) technique. The objective of this study is to find out the effect of buoyancy on turbulent mixed convection in heated vertical annulus. Downward and upward flows with bulk Reynolds number 8500, based on hydraulic diameter and mean velocity, have been simulated to investigate turbulent mixed convection by gradually increasing the effect of buoyancy. With increased heat flux, heat transfer coefficient first decreases and then increases in the upward flow due to the effect of buoyancy, but it gradually increases in downward flow. The mean velocity and temperature profiles can not be explained by the wall log laws due to the effect of buoyancy, too. All simulation results are in good quantitative agreement with existing numerical results and in good qualitative agreement with existing experimental results.

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Critical Heat Flux and Flow Pattern for Water Flow in Annular Geometry

  • Park, Jae-Wook;Baek, Won-Pil;Chang, Soon-Heung
    • 한국원자력학회:학술대회논문집
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    • 한국원자력학회 1996년도 추계학술발표회논문집(1)
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    • pp.224-229
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    • 1996
  • An experimental study on critical heat flux (CHF) and two-phase flow visualization has been performed for water flow in internally-heated, vertical, concentric annuli under near atmospheric pressure. Tests have been done under stable forced- circulation, upward and downward flow conditions with three test sections of relatively large gap widths (heated length = 0.6 m. inner diameter = 19 mm, outer diameter = 29, 35 and 51 mm). The outer wall of the test section was made up of the transparent Pyrex tube to allow the observation of flow patterns near the CHF occurrence. The CHF mechanism was changed in the order of flooding, chum-to-annular flow transition, and local dryout under a large bubble in churn flow as the flow rate was increased from zero to higher values. Observed parametric trends are consistent with the previous understanding except that the CHF for downward flow is considerably lower than that for upward flow.

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인공용승구조물 설치에 의한 유동변화 ( I ) (The Variation of Current by the Building of Artificial Upwelling Structure ( I ))

  • 김동선;황석범
    • 해양환경안전학회지
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    • 제12권4호
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    • pp.301-306
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    • 2006
  • 인공용승구조물 설치해역의 구조물에 의한 유동분포를 파악하기 위하여 ADCP(Acoustic Doppler Current Profiler)를 이용한 정선관측을 2006년 5월 4일(소조기) 및 5월 30일(대조기)에 실시하였다. 동서-남북(un-component) 유동성분의 분석결과, 조시에 따른 흐름이 전반적으로 남동류가 우세하게 나타났으며 구조물 주변역의 표층에서 수심 $30\sim40m$까지의 유동과 이심에서의 유동이 서로 다르게 나타났다. 연직유동성분(w-component)은 소조기시 구조물 주변해역과 서쪽역에서는 상승류의 흐름이 나타났고 남쪽역, 북쪽역 및 동쪽역에서는 하강류의 흐름이 나타났다. 대조기 W-W line의 낙조시에는 동쪽과 서쪽해역에서 상승류의 흐름이 나타났으며 구조물 중심 동쪽 부근에서 상승류의 흐름이 나타났고 구조물에서 멀어질수록 하강류의 흐름이 나타났다. 대조기시의 분포는 창조시 S-N line에서 상승류의 분포가 전반적으로 나타났다. 또한 구조물 구축 주번해역에서의 단위면적당 상승류의 유량은 대 소조기 창 낙조시에 하강류에 대한 유량보다 크게 나타났다. 소조기에는 창조시보다 낙조시에 더 강하였으며, 대조기에는 창조시가 낙조시보다 큰 유량을 나타내고 있다.

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