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      KCI등재

      수평관 기포유동 실험 데이터를 이용한 3차원 2상유동 해석코드 CUPID 평가

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      https://www.riss.kr/link?id=A105243931

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      다국어 초록 (Multilingual Abstract)

      Bubbly flows may occur in horizontal pipes during an accident in a nuclear power plant. Horizontal bubbly flows are characterized by asymmetric distribution of main parameters, such as void fraction and velocity, and slip ratio less than 1. Thus, three-dimensional simulation capability is needed for horizontal bubbly flows. In this study, horizontal bubbly flows were simulated using the CUPID code. The model evaluation results showed that the particle based 2-fluid momentum equation simulated more physically reasonable slip ratio than standard 2-fluid momentum equation and the turbulent dispersion force was the most important factor in the prediction of void fraction. In the quantitative assessments, it was shown that the CUPID code predicted well the axial pressure drop within the error range of 10%. Also, the code estimated well axial development process of void fraction. However, it was found that the code can not simulate asymmetric distribution of flow parameters and phenomena which gas phase moves slower than liquid phase. To improve the prediction ability, the modification of turbulence model such as turbulent shear stress, bubble induced turbulence, and so on, or the additional term in momentum equation are needed.
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      Bubbly flows may occur in horizontal pipes during an accident in a nuclear power plant. Horizontal bubbly flows are characterized by asymmetric distribution of main parameters, such as void fraction and velocity, and slip ratio less than 1. Thus, thre...

      Bubbly flows may occur in horizontal pipes during an accident in a nuclear power plant. Horizontal bubbly flows are characterized by asymmetric distribution of main parameters, such as void fraction and velocity, and slip ratio less than 1. Thus, three-dimensional simulation capability is needed for horizontal bubbly flows. In this study, horizontal bubbly flows were simulated using the CUPID code. The model evaluation results showed that the particle based 2-fluid momentum equation simulated more physically reasonable slip ratio than standard 2-fluid momentum equation and the turbulent dispersion force was the most important factor in the prediction of void fraction. In the quantitative assessments, it was shown that the CUPID code predicted well the axial pressure drop within the error range of 10%. Also, the code estimated well axial development process of void fraction. However, it was found that the code can not simulate asymmetric distribution of flow parameters and phenomena which gas phase moves slower than liquid phase. To improve the prediction ability, the modification of turbulence model such as turbulent shear stress, bubble induced turbulence, and so on, or the additional term in momentum equation are needed.

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      참고문헌 (Reference)

      1 Schiller, L., "Uber die grundlegenden Berecgnnungen bei der Schwerkraftaufbereitung" 77 (77): 318-320, 1933

      2 Tomiyama, A., "Transverse migration of single bubbles in simple shear flows" 57 : 1849-1858, 2002

      3 Yang, J., "Quasi 3-D measurements of turbulence structure in horizontal air-water bubbly flow" 227 : 301-312, 2004

      4 Lahey, R.T., "Phase distribution in complex geometry conduits" 141 : 177-201, 1993

      5 Yeoh, G.H., "On the prediction of the phase distribution of bubbly flow in a horizontal pipe" 90 : 40-51, 2012

      6 D. BESTION, "On the Modelling of Two-phase Flow in Horizontal Legs of a PWR" 한국원자력학회 44 (44): 871-888, 2012

      7 Han Young Yoon, "Multi-Scale Thermal-Hydraulic Analysis of PWRs using the CUPID Code" 한국원자력학회 44 (44): 831-846, 2012

      8 Sato, Y., "Momentum and heat transfer in two-phase bubble flow-I" 7 : 167-177, 1981

      9 Iskandrani, A., "Local void fraction and velocity field description in horizontal bubbly flow" 204 : 117-128, 2001

      10 Kocamustafaogullari, G., "Kocamustafaogullari, G. and Huang, W.D., "Internal structure and interfacial velocity development for bubbly two-phase flow" 151 : 79-101, 1994

      1 Schiller, L., "Uber die grundlegenden Berecgnnungen bei der Schwerkraftaufbereitung" 77 (77): 318-320, 1933

      2 Tomiyama, A., "Transverse migration of single bubbles in simple shear flows" 57 : 1849-1858, 2002

      3 Yang, J., "Quasi 3-D measurements of turbulence structure in horizontal air-water bubbly flow" 227 : 301-312, 2004

      4 Lahey, R.T., "Phase distribution in complex geometry conduits" 141 : 177-201, 1993

      5 Yeoh, G.H., "On the prediction of the phase distribution of bubbly flow in a horizontal pipe" 90 : 40-51, 2012

      6 D. BESTION, "On the Modelling of Two-phase Flow in Horizontal Legs of a PWR" 한국원자력학회 44 (44): 871-888, 2012

      7 Han Young Yoon, "Multi-Scale Thermal-Hydraulic Analysis of PWRs using the CUPID Code" 한국원자력학회 44 (44): 831-846, 2012

      8 Sato, Y., "Momentum and heat transfer in two-phase bubble flow-I" 7 : 167-177, 1981

      9 Iskandrani, A., "Local void fraction and velocity field description in horizontal bubbly flow" 204 : 117-128, 2001

      10 Kocamustafaogullari, G., "Kocamustafaogullari, G. and Huang, W.D., "Internal structure and interfacial velocity development for bubbly two-phase flow" 151 : 79-101, 1994

      11 Lee, S.J., "Improvement of the two-fluid momentum equation using a modified Reynolds stress model for horizontal turbulent bubbly flows" 173 : 208-217, 2017

      12 Bottin, M., "Experimental investigation of a developing two-phase bubbly flow in horizontal pipe" 60 : 161-179, 2014

      13 Yoon, H.Y., "Current status of CUPID 2.1" 2017

      14 이승준, "Comparative study of the two-fluid momentum equations for multi-dimensional bubbly flows: Modification of Reynolds stress" 대한기계학회 31 (31): 207-214, 2017

      15 Talley, J.D., "Characterization of horizontal air-water two-phase flow in a round pipe part II: Measurement of local two-phase parameters in bubbly flow" 76 : 767-785, 2015

      16 Talley, J.D., "Characterization of horizontal air-water two-phase flow in a round pipe part I: Flow visualization" 76 : 212-222, 2015

      17 Kong, R., "Characterization of horizontal air-water two-phase flow" 312 : 266-276, 2017

      18 Ekambara, K., "CFD simulation of bubbly two-phase flow in horizontal pipes" 144 : 277-288, 2008

      19 Ekambara, K., "CFD Modeling of gas-liquid bubbly flow in horizontal pipes: influence of bubble coalescence and breakup" 2012 : 2012

      20 Antal, S.P., "Analysis of phase distribution in fully developed laminar bubbly two-phase flow" 17 (17): 635-652, 1991

      21 Kocamustafaogullari, G., "An experimental study on local interfacial parameters in a horizontal bubbly two-phase flow" 17 (17): 553-572, 1991

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      학술지 이력

      학술지 이력
      연월일 이력구분 이력상세 등재구분
      2027 평가예정 재인증평가 신청대상 (재인증)
      2021-01-01 평가 등재학술지 유지 (재인증) KCI등재
      2018-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2015-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2011-01-01 평가 등재 1차 FAIL (등재유지) KCI등재
      2009-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2006-01-01 평가 등재학술지 선정 (등재후보2차) KCI등재
      2005-06-16 학술지명변경 외국어명 : Jpurnal of Computatuonal Fluids Engineering -> Korean Society of Computatuonal Fluids Engineering KCI등재후보
      2005-01-01 평가 등재후보 1차 PASS (등재후보1차) KCI등재후보
      2004-01-01 평가 등재후보 1차 FAIL (등재후보1차) KCI등재후보
      2002-07-01 평가 등재후보학술지 선정 (신규평가) KCI등재후보
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      기준연도 WOS-KCI 통합IF(2년) KCIF(2년) KCIF(3년)
      2016 0.2 0.2 0.19
      KCIF(4년) KCIF(5년) 중심성지수(3년) 즉시성지수
      0.16 0.15 0.405 0.05
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