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  • 8/9/2019 Teddy Ardiansyah - Study on Sodium Cavitation for Fast Reactors (III) Analysis of Cavitation with FLUENT and Erosion Experiment

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    Study onSodium Cavitation

    for Fast Reactors (III)Analysis of Cavitation with FLUENT

    and Erosion Experiment

    Teddy Ardiansyah, Minoru Takahashi, Makoto Asaba,

    Kuniaki MiuraAESJ Annual Meeting

    Ibaraki University, Mito, IbarakiMarch 27, 2010

    E28

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    Background For the development of economic (SFR), reactor

    vessel and components are made compact,which leads to fast flow of a coolant.

    Cavitation is possible to occur due to fast flow

    and low static pressure. Cavitation could lead to a severe damage of the

    inner part of the sodium loop system, neutronic

    and hydrodynamic problems.

    2

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    Purpose

    To analyze cavitation in water and liquid

    sodium using CFD code as well as erosionphenomena caused by cavitation in liquidsodium for 600 hours.

    3

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    Venturi test section

    4

    Cavitation coefficient

    K= cavitation coefficient

    = water/sodium densityP0 = downstream static pressure

    Pv = water/sodium vapor pressure

    V1 = velocity in venturi region

    V0 = velocity in downstream region

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    Experimental conditions

    Sodium

    T: 200-400C

    Pstag: 0.06-0.18 MPa-a

    Water Room temperature

    Pstag: 0.06-0.12 MPa-a

    5

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    6

    Developed cavitation observed by high speed camera (8,000 fps),

    Vinlet: 1.514 m/s, Pds: 0.124 MPa-a, 13o

    C, K: 0.98

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    Numerical calculation of cavitation

    Assumptions

    The working fluid is liquid and gas phase(vapor and non-condensable gas).

    The formation and collapse of bubbles aretaken into account in the model.

    The mass fraction of non-condensable gas isknown in advance.

    7

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    Numerical calculation (1) Equations used in the calculation

    Continuity equation for mixture model

    Momentum equation for mixture model

    ( ) ( ) 0.t

    mmm =+

    8

    ( ) ( )

    +++

    ++=+

    =

    n

    k

    kdrkdrkkm

    T

    mmmmmmmm

    Fg

    pt

    1

    ,,.

    ..

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    Numerical calculation (2) Equations used in the calculation

    Energy equation for mixture model

    ( ) ( )( ) ( ) En

    1k

    eff

    n

    1k

    kkkkkkk STk.pE.E

    t

    +=++

    = =

    9

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    Numerical calculation (3)

    Based on full cavitation model by Singhal,

    et al. Transport equation of vapor mass fraction,

    From generalized Rayleigh-Plesset equation forbubble dynamics with limiting bubble size, Re and

    Rc are derived

    R

    S2

    dt

    dR

    R

    4

    dt

    dR

    2

    3

    dt

    RdR

    )t(p)t(p

    L

    L

    2

    2

    2

    L

    B

    ++

    +=

    ( ) ( ) ( ) cevmm RRffvf

    t+=+

    f

    10

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    Numerical calculation (4)

    When

    When

    empirical coefficient

    vpp ( )

    v

    l

    vvlcc f

    3

    pp2kCR

    =

    ( )( )gv

    l

    vvlee ff1

    3

    pp2kCR

    =

    02.0Ce = 01.0Cc =

    11

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    Calculated condition

    No slip velocity (vl-vg=0)

    Non-condensable gas fraction:

    Sodium: 1, 3, 9 ppm (argon)

    Water: 9, 15 and 45 ppm (air) Boundary condition:

    fixed inlet velocity and fixed outlet pressure

    (based on experimental measurements)

    12

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    13

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    14

    12 13 14 15 16

    0.9

    1

    1.1

    1.2

    1.3

    Venturi velocity (m/s)

    K(-

    )

    Sodium 400CPstag: 0.141 MPa-a (exp)

    No cavitation (experiment)Cavitation (experiment)

    12 13 14 15 16

    0.9

    1

    1.1

    1.2

    1.3

    Venturi velocity (m/s)

    K(-

    )

    Beta: 1 ppmSodium 400C

    No cavitation (calculated)Cavitation (calculated)

    Experiment Calculated

    10 15 200

    1

    2

    3

    Venturi velocity (m/s)

    K(-

    )

    Water 10.8-13.0CPstag: 0.062 MPa-a (exp)

    No cavitation (experiment)Cavitation (experiment)

    10 15 20

    0

    1

    2

    3

    Venturi velocity (m/s)

    K(-

    )

    Beta: 45 ppmWater 10.8-13.0C

    No cavitation (calculated)Cavitation (calculated)

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    15

    Contours of void fraction in sodium for K: 0.92;T: 400C; and 3 ppm of non-condensable gas.

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    Erosion experiment Temperature of sodium: 200C

    Flow rate: 27~28L/min

    Pressure: 0.05~0.1Kg/cm2 (at expansion

    tank) Total: 600 hours

    K: 0.59~0.51 (developed cavitation)

    16

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    17

    X-ray of venturi test section (left) andcutted parts of test section (right).

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    Optical micrograph (up) and SEM of the test section(bottom).

    No.6 x 50 No.7 x 100

    No.6 Outlet No.6 Outlet No.6 Outlet100m 100m 30m

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    Conclusion Onset cavitations are influenced by non-

    condensable gas. Non-condensable gas fraction in liquid

    sodium is lower than in water because ofthe different solubility.

    Erosion occurred at downstream of the

    test section in sodium cavitation for 600 h.

    19

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    Thank You for

    Your Attention.