Modeling of bubble coalescence and disintegration in confined upward two-phase flow

Xiaodong Sun, Seungjin Kim, Mamoru Ishii, Stephen G. Beus

    Research output: Contribution to journalConference article

    116 Citations (Scopus)

    Abstract

    This paper presents the modeling of bubble interaction mechanisms in the two-group interfacial area transport equation (IATE) for confined gas-liquid two-phase flow. The transport equation is applicable to bubbly, cap-turbulent, and churn-turbulent flow regimes. In the two-group IATE, bubbles are categorized into two groups: spherical/distorted bubbles as Group 1 and cap/slug/churn-turbulent bubbles as Group 2. Thus, two sets of equations are used to describe the generation and destruction rates of bubble number density, void fraction, and interfacial area concentration for the two groups of bubbles due to bubble expansion and compression, coalescence and disintegration, and phase change. Five major bubble interaction mechanisms are identified for the gas-liquid two-phase flow of interest, and are analytically modeled as the source/sink terms for the transport equation in the confined flow. These models include both intra-group and inter-group bubble interactions.

    Original languageEnglish (US)
    Pages (from-to)3-26
    Number of pages24
    JournalNuclear Engineering and Design
    Volume230
    Issue number1-3
    DOIs
    StatePublished - May 1 2004
    Event11th International Conference on Nuclear Energy - Tokyo, Japan
    Duration: Apr 20 2003Apr 23 2003

    Fingerprint

    Disintegration
    two phase flow
    disintegration
    coalescence
    Bubbles (in fluids)
    Coalescence
    Two phase flow
    coalescing
    bubble
    bubbles
    Gases
    Confined flow
    Void fraction
    Liquids
    Turbulent flow
    modeling
    caps
    liquid
    slug
    interactions

    All Science Journal Classification (ASJC) codes

    • Nuclear and High Energy Physics
    • Nuclear Energy and Engineering
    • Materials Science(all)
    • Safety, Risk, Reliability and Quality
    • Waste Management and Disposal
    • Mechanical Engineering

    Cite this

    Sun, Xiaodong ; Kim, Seungjin ; Ishii, Mamoru ; Beus, Stephen G. / Modeling of bubble coalescence and disintegration in confined upward two-phase flow. In: Nuclear Engineering and Design. 2004 ; Vol. 230, No. 1-3. pp. 3-26.
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    abstract = "This paper presents the modeling of bubble interaction mechanisms in the two-group interfacial area transport equation (IATE) for confined gas-liquid two-phase flow. The transport equation is applicable to bubbly, cap-turbulent, and churn-turbulent flow regimes. In the two-group IATE, bubbles are categorized into two groups: spherical/distorted bubbles as Group 1 and cap/slug/churn-turbulent bubbles as Group 2. Thus, two sets of equations are used to describe the generation and destruction rates of bubble number density, void fraction, and interfacial area concentration for the two groups of bubbles due to bubble expansion and compression, coalescence and disintegration, and phase change. Five major bubble interaction mechanisms are identified for the gas-liquid two-phase flow of interest, and are analytically modeled as the source/sink terms for the transport equation in the confined flow. These models include both intra-group and inter-group bubble interactions.",
    author = "Xiaodong Sun and Seungjin Kim and Mamoru Ishii and Beus, {Stephen G.}",
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    Modeling of bubble coalescence and disintegration in confined upward two-phase flow. / Sun, Xiaodong; Kim, Seungjin; Ishii, Mamoru; Beus, Stephen G.

    In: Nuclear Engineering and Design, Vol. 230, No. 1-3, 01.05.2004, p. 3-26.

    Research output: Contribution to journalConference article

    TY - JOUR

    T1 - Modeling of bubble coalescence and disintegration in confined upward two-phase flow

    AU - Sun, Xiaodong

    AU - Kim, Seungjin

    AU - Ishii, Mamoru

    AU - Beus, Stephen G.

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    N2 - This paper presents the modeling of bubble interaction mechanisms in the two-group interfacial area transport equation (IATE) for confined gas-liquid two-phase flow. The transport equation is applicable to bubbly, cap-turbulent, and churn-turbulent flow regimes. In the two-group IATE, bubbles are categorized into two groups: spherical/distorted bubbles as Group 1 and cap/slug/churn-turbulent bubbles as Group 2. Thus, two sets of equations are used to describe the generation and destruction rates of bubble number density, void fraction, and interfacial area concentration for the two groups of bubbles due to bubble expansion and compression, coalescence and disintegration, and phase change. Five major bubble interaction mechanisms are identified for the gas-liquid two-phase flow of interest, and are analytically modeled as the source/sink terms for the transport equation in the confined flow. These models include both intra-group and inter-group bubble interactions.

    AB - This paper presents the modeling of bubble interaction mechanisms in the two-group interfacial area transport equation (IATE) for confined gas-liquid two-phase flow. The transport equation is applicable to bubbly, cap-turbulent, and churn-turbulent flow regimes. In the two-group IATE, bubbles are categorized into two groups: spherical/distorted bubbles as Group 1 and cap/slug/churn-turbulent bubbles as Group 2. Thus, two sets of equations are used to describe the generation and destruction rates of bubble number density, void fraction, and interfacial area concentration for the two groups of bubbles due to bubble expansion and compression, coalescence and disintegration, and phase change. Five major bubble interaction mechanisms are identified for the gas-liquid two-phase flow of interest, and are analytically modeled as the source/sink terms for the transport equation in the confined flow. These models include both intra-group and inter-group bubble interactions.

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