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Hongjie Zhang
Purge gas flow impact on tritium permeation
Integrated simulation on tritium permeation in the solid breeder unit
FNST, August 18-20, 2009
FNST 2009
Issues Tritium behavior in blanket is a complicated phenomenon which
consist of tritium generation, tritium permeation, purge gas thermo-fluid and nuclear heating
No single integrated program of theory, computer modeling to simulate tritium behavior in blanket units.
Handling of 3D complicated large scale geometry Objective
Develop a predictive capability of tritium and hydrogen permeation from breeding zones to the coolant in the helium cooled pebble-bed blanket.
Construct 3-D convection-diffusion models Integrated with thermal-fluid analysis in TBM unit
Take into account the tritium generation rate distribution and nuclear heating rate distribution.
Provide predictive capabilities, and Assist solid breeder design
Motivations and Objectives
FNST 2009
COMSOL model Set-up Convection-diffusion model with imported velocity and
temperature profiles Apply Law-boundary conditions at gas-metal interface. Works on 2-D or 3-D small scale geometry Memory issue for large-scale geometry
Sctetra model Extend CFD code for tritium permeation assessment in TBM unit Add multi-species permeation / Isotope permeation Support Law-dependent boundary condition or Rate-dependent
boundary condition at gas-metal interface Support 3-D complex geometry at large scale
Previous work and Recent advancement
Two multi-physics models based on different codes were developed
FNST 2009
Ωbreeder
Model Domain Ωstructure
Ωcoolant
Methodology Develop a 3-D multi-species convection-diffusion permeation model Integrated with
thermal-fluid analysis in porous media to account for the effects of purge stream convection and the accompanying velocity and temperature profile
Model domain: 1.the purge flow region 2.the structure3.the coolant.
•H2, T2, and HT are transported by diffusion and convection in the two fluid phase•diffusion is the only transport mechanism in the structure phase
c1t
uc1 D12c1Qc
c2
tD2
2c2
c3
t Uc3 D3
2c3
B.C.s at the gas-structure interface should ensure • The flux continuity• The concentration discontinuities
c2 SP11/2
2211 cDcD
C1
C3
Solid
c2 c2
T2
Diffusion across a film
T
T2
FNST 2009
Reflects the variations of porosity and transport in the bed near the wall regions
Governing equations
**11
121
11 Kp
t
uuuu
u
]}/)2/(exp[1{* 111*
pdywNC
*K
qTTCt
TCp
p
1
21111
111
u
To obtain the convective part of the flux, velocity distributions can be introduced by solving the N-S equation based on Brinkman model of a flow in a packed bed. Considering the wall effect, which reflects the variations of porosity and tritium transport in the bed near the wall regions, the calculation uses the following governing equations:
Momentum conservation equation
Energy conservation equation
*
]}/)2/(exp[1{* 122*
pdywNCKK
2Cp2
T2
t2
2T2
3Cp3
T3
t3Cp3UT3 3
2T3
c1t
uc1 D12c1Qc
c2
tD2
2c2
c3
t Uc3 D3
2c3
Diffusive species conservation equation
FNST 2009 Experiments: Permeation of deuterium through a palladium membrane, which was accompanied by co-permeation of hydrogen were performed.
Two cases were compared: Permeation of D2 only through Pd membrane (0.025mm, 825K, 865K) Co-permeation of H2 D2 through Pd membrane(0.025mm, 825K)
Calculated permeation flux agree well with the experimental results for both cases
Modal Validation - Co-permeation of deuterium and hydrogen
through Pd, K. Kizu, A. Pisarev, T. Tanabe, J. of Nuclear Materials, 289(2001) 291-302
1E-4 1E-3 0.01 0.1 1 101E-8
1E-7
1E-6
1E-5
1E-4
1E-3
J(D2
)/m
ol m-2
s-1
P(D2) (Pa)
Calculated 825K Measured 825K Calculated 865K Measured 865K
1E-3 0.01 0.1 11E-8
1E-7
1E-6
1E-5
1E-4
1E-3
Su
rfa
ce f
lux
/ m
ol m
-2
s-1
Effective deuterium pressure (Pa)
Calculated H2 flux
Calculated D2 flux
Calculated HD flux Measured H
2 flux
Measured D2 flux
Measured HD flux
Case 1
D2 permeation flux as a function of upstream deuterium pressure
HD H2 D2 permeation flux in co-permeation measurements as a function of effective deuterium pressure PD=P(D2)+P(HD)/2 and at a fixed value of effective H2 pressure PH=P(H2)+P(HD)/2=0.063Pa.
Case 2
H2 D2 partial pressures from
P_H2 : 0.06 ~ 0.0035
P_D2 : 0.0001 ~ 1
FNST 2009
Model Application - multi-physics simulation in a TBM unit As a part of integrated multi-physics
modeling capability, able to Evaluate temperature profile, velocity profile,
chemical composition Calculate Tritium Concentration, Tritium
permeation flux, and other parameters of interest
Handle any 3-D large scale geometry Multi-physics simulation in a TBM unit
-0.05 0.00 0.05 0.10 0.15 0.20 0.25 0.30 0.35 0.40
0
1x106
2x106
3x106
4x106
5x106
6x106
7x106
8x106
He
at r
ate
dis
trib
utio
n (
W/m
3 )
Distance from FW(m)
-0.05 0.00 0.05 0.10 0.15 0.20 0.25 0.30 0.35 0.40
0.0
2.0x10-6
4.0x10-6
6.0x10-6
8.0x10-6
1.0x10-5
1.2x10-5
1.4x10-5
1.6x10-5
1.8x10-5
2.0x10-5
Tri
tium
pro
duct
ion
rat
e d
istr
ibu
tion
(m
ol/m
3 s)
Distance from FW(m)
Tritium production rate distribution in the radial direction
Heating rate distribution in the radial direction
TBM unit
Purge gas inlet
Purge gas outlet
Coolant channels
FNST 2009
0.00 0.02 0.04 0.06 0.08 0.100.00
0.02
0.04
0.06
0.08
0.10
0.12
0.14
Per
me
atio
n f
lux
to c
oo
lan
t/P
rod
uct
ion
Average purge flow velocity (m/s)
Model Application - multi-physics simulation in a TBM unit
Purge gas streamline
Tritium concentration in breeder
Temperature
Low velocity field will appear in the Left-Bottom corner and Right-Top corner, which will affect tritium concentration slightly.
Tritium permeation over the production decreases quickly as the average purge gas velocity increases
Tritium concentration is impacted by production rate, Velocity and Temperature profiles
FNST 2009
Conclusion
3-D multi-species convection-diffusion permeation model Integrated with thermal-fluid analysis in porous media are assessed to provide predictive capabilities and assist solid breeder design
Benchmark cases agree well with experimental results, and more benchmark with available data can be done
As a part of integrated multi-physics modeling capability, able to Evaluate temperature profile, velocity profile, chemical composition Calculate Tritium Concentration, Tritium permeation flux, and other parameters of interest Handle 3-D large scale geometry
Simulation in a TBM unit show that parameters such as temperature distribution and purge gas flow can strongly affect tritium transport. Under reasonable purge velocity profile, increasing the inlet velocity is an effective method to reduce tritium permeation to the coolant.
FNST 2009
Thank you