teddy ardiansyah - study on sodium cavitation for fast reactors (iii) analysis of cavitation with...
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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.
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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.
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Venturi test section
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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
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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.
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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
+=++
= =
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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
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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 =
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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)
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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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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)
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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.
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Thank You for
Your Attention.