by s. saeidi contribution from: s. smolentsev, s. malang university of los angeles august, 2009
TRANSCRIPT
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By S. Saeidi
Contribution from: S. Smolentsev, S. Malang
University of Los AngelesAugust, 2009
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IntroductionMotivation/GoalsProblem DefinitionMathematical modelNumerical CodeTest ResultsConclusion and Future Investigation
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Liquid metal, such as PbLi has so many advantages using as heat transfer fluid
Corrosion behavior of ferritic steel exposed to PbLi is not well understood
Maintaining acceptable limits for material loss is an important goal in blanket development
For ferritic steel/PbLi, corrosion is controlled by convection, diffusion and dissolution at the solid-liquid interface
Mass, heat and momentum transfer are coupledThe main purpose is to develop a numerical code
to access corrosion of ferritic steel in PbLi under either experimental or real blanket conditions
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There are no commercial codes available for corrosion analysis under fusion blanket conditions
Experimental data are available on ferritic steel/PbLi corrosion, but no good interpretation exists
We need a code, which would help us to perform some initial corrosion analysis under blanket conditions
We want to help experimentalists to understand the data, and to understand the corrosion phenomenon itself
Use of code for benchmarking with more sophisticated software, which is planned to be developed in future (HIMAG)
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Corrosion is a result of dissolution of wall material, which is then transported by the flow
Transport mechanism are convection and diffusionFlow is either laminar or turbulent. MHD effects should
be includedWe consider only one component (Fe) diffusing into PbLiWe also consider deposition phenomenon, which occurs in
the cold part of the loopHeat, mass and momentum transfer are coupled. The
mathematical model should include energy equation, flow equations (including MHD effects), and mass transfer equation
The boundary condition at the solid-liquid interface assumes saturation concentration at given wall temperature
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Flow
Heat Transfer:
Mass Transfer:
)(111
Bj
y
Uy
yyx
P
y
UV
x
UU
t
Ut
mm
0)(1
Vyyyx
U mm
'''1
qy
Tkky
yyy
TV
x
TU
t
TC t
mmp
y
CtDDmy
ymyy
CV
x
CU
t
C 1
m=0 – plane geometrym=1 – pipe t, kt, Dt=0 – laminar t, kt, Dt>0 – turbulent Turbulence closures are used to calculate t, kt, Dt
MHD effects are included through jxB, P/x, t, kt, Dt
More equationsare used to introduce MHD effects
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•Saturation concentration equation expressed in mole fraction (percentage)
Borgstedt, H.U and Rohrig, H.D:1991, Journal of Nuclear Materials 181-197
Mass diffusion coefficient plotted as a function of the wall temperature
Saturation concentration Csat of iron atoms in PbLi as function of temperature
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MODULE DESCRIPTION STATUS
MAIN Switches between the modules Included
INPUT Reads input data Included
VELO Calculates velocity profile Included
TEMP Solves the energy equation Included
CONC Solves the admixture transport equation Included
OUTPUT Prepares and organizes data output Included
• Velocity distribution can be calculated for both laminar and turbulent flow regimes for simple geometries (pipe, rectangular duct, parallel channel) with or without a magnetic field•Finite-difference computer code•Non-uniform meshes with clustering points near the walls•Implicit method for solving equations (Tri-diagonal solver)
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Flow BC type
Nu (calc.) Nu (theory)
Plane channel, slug flow
Const. T (C)
4.94 4.94
Plane channel, parabolic velocity profile
Const. T (C)
3.77 3.77
Plane channel, parabolic velocity profile
Const. Q 4.12 4.12
Pipe, slug flow Const. T (C)
5.78 5.78
Pipe, parabolic velocity profile
Const. Q 3.66 3.66
Pipe, parabolic velocity profile
Const. Q 4.36 4.36
The comparisons have been made for a laminar flow
Plot of Nusselt number along x direction in Plane channel with parabolic velocity profile
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Flow Length: 2mChannel Width: 20cmTwall= 500 CLaminar flow= U=3 cm/sCwall=0.01 Kg/m3
Concentration profileTemperature profile
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Plot of Sherwood number along the X direction:
Rate of mass transfer along the X direction:
•Sh decreases along the x until the flow become fully developed
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Initials steps towards a mathematical model and numerical code for modeling of corrosion/deposition processes have been performed
We will keep working on the code and use it to analyze the effect of the flow regime, MHD, flow geometry, inlet conditions, etc. on corrosion/deposition of ferritic steel in PbLi under either experimental or real blanket conditions
We will look for experimental data and run the code trying to reproduce the experimental data
In the future, the code will be used for benchmarking with more sophisticated software (HIMAG)