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Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
Materials Process Design and Control LaboratorySibley School of Mechanical and Aerospace Engineering
169 Frank H. T. Rhodes HallCornell University
Ithaca, NY 14853-3801
Email: [email protected]: http://www.mae.cornell.edu/zabaras
NICHOLAS ZABARASNICHOLAS ZABARAS
A MULTISCALE APPROACH TO A MULTISCALE APPROACH TO MATERIALS USING STOCHASTIC MATERIALS USING STOCHASTIC
AND COMPUTATIONAL STATISTICS AND COMPUTATIONAL STATISTICS TECHNIQUESTECHNIQUES
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
NEED FOR MULTISCALE ANALYSISNEED FOR MULTISCALE ANALYSISFingering in porous media
Water injector
site
Porous bed-rock
• Water displaces the oil layer to the receiving site
• Water accelerates more in areas with high permeability
• Fingering reduces quality of the oil received (polluted with water)
Oil receiver
site • Permeability of bed rock is inherently stochastic
• Statistics like mean permeability, correlation structure are usually constant for a given rock type
• Stationary probability models can be used
• Direct simulation of the effect of uncertainty in permeability on the amount of oil received requires enormous computational power
• Bed rock length scale – typically of order of kms
• Length scale for permeability variation – typically of order of cms
• Requirement – 10000 blocks for a single dimension (1012 blocks overall)
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
NEED FOR MULTISCALE ANALYSISNEED FOR MULTISCALE ANALYSISTransport phenomena in material processes like solidification
Engineering component
Microstructural features
Formation of dendrites, micro-scale flow structure, heat transfer patterns are highly sensitive to perturbations
• Microstructure is dynamic and evolves with the materials process
• Uncertainties at the micro-scale are loosely correlated, however macro-scale features like species concentration, temperature, stresses are highly correlated
• Uncertainty analysis at micro-scale requires considerable computational effort
• Macro-properties dependant on the dendrite patterns and uncertainty propagation at the micro-scales
• Uncertainty interactions are no longer satisfy stationarity assumptions – newer probability models based on image analysis and experimentation needed
Length scale ~ meters
Length scale ~ 10-4 meters
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
STOCHASTIC VARIATIONAL MULTISCALESTOCHASTIC VARIATIONAL MULTISCALE
Physical model
• Statistical variations in properties are significant
• Discontinuities, loosely correlated structures in properties
Large scale system
Micro scale features
• Statistical variations are relatively negligible
• Discontinuities get smoothed out
• Process interactions, properties become correlated
Uncertainties in boundary and initial conditions
• Discrete probability distributions to model properties
• Image analysis to develop the correlation structure
Bayesian data analysis interface
Green’s functions, RFB
type models
Explicit subgrid scale model - FEM
Experimental, Monte Carlo/ MD models
Spectral stochastic/ support-space representation of uncertainty
Discretization method like FEM, Spectral, FDM
Subgrid scale models
Large scale simulation
Averaging out the higher statistical features of
subgrid scale solutions using Karhunen-loeve/
wavelet filtering
Residual
Statistical features
Large scale solutions obtained from the
explicit discretization approach
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
MULTISCALE TRANSPORT SYSTEMSMULTISCALE TRANSPORT SYSTEMS
Flow past an aerofoil Atmospheric flow in Jupiter
Solidification process
Modeling of dendrites at small scale, fluid flow and transport at large scale
Large scale turbulent structures, small scale dissipative eddies, surface irregularities
Astro-physical flows, effects of gravitational and magnetic fields
• Presence of a variety of spatial and time scales - commonality
• Varied applications – Engineering, Geophysical, Materials
• Boundary conditions, material properties, small scale behavior inherently are uncertain
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
IDEA BEHIND VARIATIONAL MULTISCALE IDEA BEHIND VARIATIONAL MULTISCALE -- VMSVMS
Solidification process
Physical model
Micro-constitutive laws from experiments,
theoretical predictions
Subgrid model
Resolved model
• Green’s function• Residual free bubbles• MsFEM “Hou et al.”• TLFEM “Hughes et al.”
• FEM
• FDM
• Spectral
Large scale behavior – explicit
resolution
Small scale behavior –statistical resolution
Large scale
Residual
Subgrid scale
solution
Where does uncertainty fit in
?
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
WHY STOCHASTIC MODELING IN VMS ?WHY STOCHASTIC MODELING IN VMS ?Model uncertainty
Material uncertainty Computational uncertainty
• Imprecise knowledge of governing physics
• Models used from experiments
• Uncertain boundary conditions• Inherent initial perturbations• Small scale interactions
Surroundings uncertainty
Solidification microscale features
• Material properties fluctuate – only a statistical description possible
• Uncertainty in codes
• Machine precision errors
Not accounted for in analysis here
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
SOME PROBABILITY THEORYSOME PROBABILITY THEORY
Probability space – A triplet - - Collection of all basic outcomes of the experiment- - Permutation of the basic outcomes- - Probability associated with the permutations
Ω( , , )F PΩFP
: ( )( , , )
W D TW x t ω
× ×Ω →
Sample space Real interval
Ω
ξ ω( )Random variable –a function
Stochastic process – a random function at each space and time point
Notations:
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
SPECTRAL STOCHASTIC EXPANSIONSSPECTRAL STOCHASTIC EXPANSIONS
1( , , ) ( , ) ( , ) ( )i i
iW x t W x t W x tω ξ ω
∞
=
= +∑
• Covariance kernel required – known only for inputs• Best possible representation in mean-square sense
• Series representation of stochastic processes with finite second moments
( , )W x t( , )iW x t
( )iξ ω
- Mean of the stochastic process
- Coefficient dependant on the eigen-pairs of the covariance kernel of the stochastic process
- Orthogonal random variables
Karhunen-Loeve expansion
Generalized polynomial chaos
expansion 0( , , ) ( , ) (ξ( ))i i
iW x t W x tω ψ ω
∞
=
=∑( , )(ξ( ))
i
i
W x tψ ω
- Coefficients dependant on chaos-polynomials chosen
- Chaos polynomials chosen from Askey-series (Legendre –uniform, Jacobi – beta)
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
SUPPORTSUPPORT--SPACE/STOCHASTIC GALERKINSPACE/STOCHASTIC GALERKIN( ( ))f ξ ω - Joint probability density function of the inputs
{ ( ) : ( ( )) 0}A fξ ω ξ ω= > - The input support-space denotes the regions where input joint PDF is strictly positive
Triangulation of the support-space
Any function can be represented as a piecewise polynomial on the triangulated support-space
- Function to be approximated( ( ))X ξ ω
( ( ))hX ξ ω - Piecewise polynomial approximation over support-space
( ( ))hX ξ ω
L2 convergence – (mean-square)2 1( ( ( )) ( ( ))) ( ( ))dh q
A
X X f Chξ ω ξ ω ξ ω ξ +− ≤∫h = mesh diameter for the support-space discretization
q = Order of interpolation
Error in approximation is penalized severely in high input joint PDF regions. We use importance based refinement of
grid to avoid this
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
BOUSSINESQ NATURAL CONVECTIONBOUSSINESQ NATURAL CONVECTION
g
2
0
( ) Pr( ) e
2 Pr( ) ( )1( ) [ ( ) ]2
T
vv v v Rat
vt
pI v
v v v
ω ω θ σ
θ θ θ
σ ω ε
ε
∇ =∂
+ ∇ = − +∇∂
∂+ ∇ = ∇
∂= − +
= ∇ + ∇
i
i i
i
hmΓ
gmΓ
gtΓ
htΓ
gv v=
gθ θ=
0.n qθ∇ =
.n hσ∇ =
• Temperature gradients are small
• Constant fluid properties except in the force term
• viscous dissipation negligible
Momentum equation boundary conditions
Energy equation boundary conditions
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
DEFINITION OF FUNCTION SPACESDEFINITION OF FUNCTION SPACES
1 2 2
22
22
1
( ) { : ( ( ) )d }
( ) { : d }
( ) { : d }
( ) { : d }
D
D
T
T
H D v v v x
L D v v x
L T w w t
L T w w t
= + ∇ < ∞
= < ∞
= < ∞
= < ∞
∫
∫
∫
∫DT
- Spatial domain
- Time interval of simulation [0,tmax]
Function spaces for deterministic quantities
Function spaces for stochastic quantities
22 ( ) { : dP }L ξ ξ
Ω
Ω = < ∞∫
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
DERIVED FUNCTION SPACESDERIVED FUNCTION SPACES
1 d2 2
1 d0 2
2 1 2
0 2 21
2 2
10 2
{ : [ ( ) ( ) ( )] , }
{ : [ ( ) ( )] , 0 }
{ : ( ) ( ) ( )}{ : ( ) ( )}
{ : ( ) ( ) ( ), }
{ : ( ) ( ), 0 }
g gm
gm
g gt
gt
V v v H D L T L v v on
V w w H D L w on
Q p p L D L T LQ q q L D L
E H D L T L on
E w w H D L w on
θ θ θ θ
= ∈ × × Ω = Γ
= ∈ × Ω = Γ
= ∈ × × Ω= ∈ × Ω
= ∈ × × Ω = Γ
= ∈ × Ω = Γ
Velocity function spaces
• Uncertainty is incorporated in the function space definition
• Solution velocity, temperature and pressure are in general multiscale quantities (as Rayleigh number increases) the computational grid capture less and less information
Pressure function spaces
Temperature function spaces
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
WEAK FORMULATION WEAK FORMULATION –– BOUSSINESQ EQNSBOUSSINESQ EQNS
v 0( , ) ( . , ) ( , ) ( , ) htt w v w w q wθ θ θ Γ∂ + ∇ + ∇ ∇ =
v g( , ) ( . , ) ( , ( )) ( , ) ( ( ) Pr( ) e , )
( , ) 0hmt
v w v v w v h w Ra w
v q
σ ε ω ω θΓ∂ + ∇ + = −
∇ =i
Eθ ∈ 0w E∈Find such that for all , the following holds
[ , ] [ , ]v p V Q∈ 0 0[ , ] [ , ]w q V Q∈Find such that for all , the following holds
Energy equation – weak form
Momentum and continuity equations – weak form
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
VARIATIONAL MULTISCALE DECOMPOSITIONVARIATIONAL MULTISCALE DECOMPOSITION
0 0 0
0 0 0 0 0 0
', ', '
', ', '
V V V V V V Q Q Q
Q Q Q E E E E E E
= ⊕ = ⊕ = ⊕
= ⊕ = ⊕ = ⊕
', ', 'v v v p p p θ θ θ= + = + = +
• Bar denotes large scale/resolved quantity• Prime denotes subgrid scale/ unresolved quantity
Induced multiscale decomposition for function spaces
Interpretation• Large scale function spaces correspond to finite element spaces – piecewise polynomial and hence are finite dimensional
• Small scale function spaces are infinite dimensional
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
SCALE DESOMPOSED WEAK FORM SCALE DESOMPOSED WEAK FORM -- ENERGYENERGY
v 0
v 0
( ', ) ( . . ', ) ( ', ) ( , )
( ', ') ( . . ', ') ( ', ') ( , ')ht
ht
t t
t t
w v v w w q w
w v v w w q w
θ θ θ θ θ θ
θ θ θ θ θ θΓ
Γ
∂ + ∂ + ∇ + ∇ + ∇ +∇ ∇ =
∂ + ∂ + ∇ + ∇ + ∇ +∇ ∇ =
Find and such that for all and , the following holds
' 'Eθ ∈Eθ ∈ 0w E∈ 0' 'w E∈
Small scale strong form of equations
2 2' . ' ' ( . )t tv v Rθ θ θ θ θ θ∂ + ∇ −∇ = − ∂ + ∇ −∇ =2( ) : .L vθ θ θ= ∇ −∇
1 11 ( ), (1 )t n n n n n nf f f f f ft γ
γ γδ + + +
∂ = − = + −Time discretization rule
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
ELEMENT FOURIER TRANSFORMELEMENT FOURIER TRANSFORM
DSpatial domain
( )eD
( )
ˆ ˆexp( ) ( , )d ( , ) ( , )e
j jj
D
k kg k xn i g x i g k i g kx h h h
ω ω ω∂ = − Γ + ≈∂ ∫
i
( )
ˆ ( , ) exp( ) ( , )deD
k xg k i g x xh
ω ω= −∫i
Subgrid scale solution denotes unresolved part of the solution, hence dominated by large wave number modes!!
Spatial derivative approximation
• Other techniques to solve for an approximate subgrid solution include:
- Residual-free bubbles, Green’s function approach
- Two-level finite element method – explicit evaluation
- Multiscale FEM – Incorporates subgrid features in large scale weighting function
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
ALGEBRAIC SUBGRID SCALE MODELALGEBRAIC SUBGRID SCALE MODEL2 2' . ' ' ( . )t tv v Rθ θ θ θ θ θ∂ + ∇ −∇ = − ∂ + ∇ −∇ =
' '( )t n n nL Rγ γθ θ + +∂ + =
2' '
2
1 1ˆ ˆˆn n n
kv ki Rt h h tγ γ
θ θγδ γδ+ + + + = +
i
122 2
' '1 22
1 1 1,n t n n tv
R c ct h t hγ γ
θ τ θ τγδ γδ
−
+ +
≈ + = + +
Time discretization
Element Fourier transform
Parseval’s theorem
Mean value theorem
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
STABILIZED FINITE ELEMENT EQUATIONSSTABILIZED FINITE ELEMENT EQUATIONSStrong regularity conditions
v 0
2 2
1
' 2
1
( , ) ( , ) ( , ) ( , )
( , ( )
( , /( ) ) ) 0
htt n n n
Nel
t n n n te
Nel
n t te
w v w w q w
v w v w w
w t v w w w
γ γ
γ γ
θ θ θ
θ θ θ τ
θ τ γδ τ
+ + Γ
+ +=
=
∂ + ∇ + ∇ ∇ −
+ ∂ + ∇ −∇ − + ∇ +∇
+ − ∇ −∇ − =
∑
∑
i
i i
i
2v v( ', ) ( ', ), ( ', ) ( ', )v w v w w wθ θ θ θ∇ = − ∇ ∇ ∇ = − ∇i i
Stabilized weak formulation
/( )w w tγδ=where
Time integration has a role to play in the stabilization (Codina et al.)
Stochastic intrinsic time scale (subgrid scale solution has a stochastic model)
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
CONSIDERATIONS FOR MOMENTUM EQUATIONCONSIDERATIONS FOR MOMENTUM EQUATIONPicard’s linearization 'v v v v v v∇ ≈ ∇ + ∇i i iFairly accurate for laminar up to transition (moderate Reynolds number flows)
For high Reynolds number flows, the term assumes importance since small scales act as momentum dissipaters
' 'v v∇i
Small scale strong form of equations
g' ' ( ', ') ( ) Pr( ) e ( , )
't tv v v v p Ra v v v v p
v v
σ ω ω θ σ∂ + ∇ −∇ = − −∂ − ∇ +∇
∇ = −∇
i i i ii i
g( ) Pr( ) e ( , )mom t n n n nR Ra v v v v pγ γ γω ω θ σ+ + += − − ∂ − ∇ +∇i i
con nR v γ+= −∇i
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
SUBGRID VELOICTY AND PRESSURESUBGRID VELOICTY AND PRESSURE2
' ' '2
'
1 1ˆˆ ˆ ˆPr( )
ˆ ˆ
n n mom n
ncon
k v k ki v i p R vt h h h t
k vi R
h
γ γ
γ
ωγδ γδ+ +
+
+ + + = +
=
i
i
Element Fourier transform
Simultaneous solve
Parseval’s theorem
Mean-value theorem1
22 222'
1 1
' 2'
1
, Pr( )
,
n c con c
nn m mom m
c
c v hhp Rc t c
v hv Rt c
γ
γ
τ τ ωγδ
τ τγδ τ
+
+
≈ = + +
≈ + =
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
STABILIZED FINITE ELEMENT EQUATIONSSTABILIZED FINITE ELEMENT EQUATIONSStrong regularity conditions
v v( ', ) ( ', ), (Pr( ) ( '), ( )) ( ', Pr( ) ( ))v v w v v w v w v wω ε ε ω ε∇ = − ∇ = − ∇i i i
Stabilized weak formulation
/( )w w tγδ=where
( )'
g1
'
( , ) ( , ) (2 Pr( ) ( ), ( )) ( , )
( ) Pr( ) e ( , ) , Pr( ) ( )
( , ) ( , ) 0
hmt n n n n
Neln
t n n n n me
n n c
v v v w p w v w h w
vRa v v v v p w v w wt
v w v w
γ γ γ
γ γ γ
γ
ω ε ε
ω ω θ σ τ ω εγδ
τ
+ + + Γ
+ + +=
+
∂ + ∇ − ∇ + −
+ − −∂ − ∇ + − + ∇ + ∇
− + ∇ ∇ =
∑
i i
i i i
i i
'
g1
( , ) ( ( ) Pr( ) e ( , ) , 0Nel
nn t n n n n m
e
vv q Ra v v v v p qtγ γ γ γ
ω ω θ σ τγδ+ + + +=
∇ + − −∂ − ∇ + − ∇ =
∑i i
Momentum equation
Continuity equation
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
IMPLEMENTATION ISSUES IMPLEMENTATION ISSUES -- GPCEGPCE
DSpatial domain
( )eD
nbf
1
( , ) ( ) ( )f x f N xα αα
ω ω=
=∑
Generic function
Random coefficient
Galerkin shape
function
GPCE expansion for random coefficients
0
( ) (ξ( ))P
i ii
f fα αω ψ ω=
=∑
Random coefficient
Askey polynomial
• Each node has P+1 degrees of freedom for each scalar stochastic process
• Interpolation is accomplished by tensor-product basis functions
• (P+1) times larger than deterministic problems
• Assume the inputs have been represented in Karhunen-Loeve expansion such that the input uncertainty is summarized by few random variables
1 nξ( ) {ξ ( ), ,ξ ( )}ω ω ω= …
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
IMPLEMENTATION ISSUES IMPLEMENTATION ISSUES –– SUPPORT SPACESUPPORT SPACE
DSpatial domain
A stochastic process can be interpreted as a random variable at each spatial point
( , , )W x t ω
Two-level grid approach
Spatial grid
Support-space grid
• Mesh dense in regions of high input joint PDF
( )eD
Element
( , )x ω
A
( ')eA
nbf nbf ' nbf'
1 1 1( , ) ( ) ( ) ( ) ( )i i i j j i
i j if x f N x f N N xω ω ω
= = =
= =∑ ∑∑
• There is finite element interpolation at both spatial and random levels
• Each spatial location handles an underlying support-space grid
• Highly OOP structure
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
NUMERICAL EXAMPLESNUMERICAL EXAMPLES• Flow past a circular cylinder with uncertain inlet velocity – Transient behavior
• RB convection in square cavity with adiabatic body at the center – uncertainty in the hot wall temperature (simulation away from critical points)
- Transient behavior- Simulation using GPCE, validation using deterministic simulation
• RB convection in square cavity – uncertainty in Rayleigh number (simulation about a critical point)
- Failure of the GPCE approach- Analysis support-space method - Comparison of prediction by support-space method with deterministic simulations
In the last example, temperature contours do not convey useful information and hence are ignored
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
FLOW PAST A CIRCULAR CYLINDERFLOW PAST A CIRCULAR CYLINDER
X
Y
0 5 10 15 200
2
4
6
8
• Computational details – 2000 bilinear elements for spatial grid, third order Legendre chaos expansion for velocity and pressure, preconditioned parallel GMRES solver
• Time of simulation – 180 non-dimensional units
• Inlet velocity –Uniform random variable between 0.9 and 1.1
• Kinematic viscosity 0.01
• Time stepping –0.03 non-dimensional units
Inlet
Traction free outlet
( )U ω
No-slip
No-slip
Investigations
• Onset of vortex shedding
• Shedding near wake regions, flow statistics
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
ONSET OF VORTEX SHEDDINGONSET OF VORTEX SHEDDING
X
Y
0 2 4 6 8 10 12 14 16 18 200
2
4
6
8
-0.50 -0.42 -0.34 -0.26 -0.18 -0.10 -0.02 0.06 0.14 0.22 0.30 0.39 0.47 0.55 0.63
X
Y
0 2 4 6 8 10 12 14 16 18 200
2
4
6
8
-0.14 -0.12 -0.10 -0.08 -0.06 -0.04 -0.03 -0.01 0.01 0.03 0.05 0.07 0.09 0.10 0.12
Mean pressure at t = 79.2
• Vortex shedding is just initiated
• Not in the periodic shedding mode
First order term in Legendre chaos expansion of pressure at t = 79.2
• Vortex shedding is predominant
• Periodic shedding behavior noticed
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
FULLY DEVELOPED VORTEX SHEDDINGFULLY DEVELOPED VORTEX SHEDDING
Mean pressure contours
First order term in LCE of pressure contours
Second order term in LCE of pressure contours
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
VORTEX SHEDDING VORTEX SHEDDING -- CONTDCONTD
Frequency
Ampl
itude
0.1 0.2 0.3 0.4 0.50
0.03
0.06
0.09
0.12
0.15
• The FFT of the mean velocity shows a broad spectrum with peak at frequency 0.162
• The spectrum is broad in comparison to deterministic results wherein a sharp shedding frequency is obtained
• Mean velocity has superimposed frequencies
• Mean velocity has comparatively lower magnitude than the deterministic velocity (Y-velocities compared at near wake region)
X
V
5 8 11 14 17 20-0.6
-0.4
-0.2
0
0.2
0.4
0.6
DeterministicMean
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
RB CONVECTION RB CONVECTION -- CENTRAL ADIABATIC BODYCENTRAL ADIABATIC BODY• Computational details – 2048 bilinear elements for spatial grid, third order Legendre chaos expansion for velocity, pressure and temperature, preconditioned parallel GMRES solver
• Time of simulation –1.5 non-dimensional units
• Rayleigh number - 104
• Prandtl number – 0.7
• Time stepping – 0.002 non-dimensional units
• Transient behavior of temperature statistics ( Flow results in paper )
X
Y
0 0.25 0.5 0.75 10
0.25
0.5
0.75
1Cold wall
Hot wall
Insulated InsulatedAdiabatic
body
0cθ =
[0.95,1.05]h Uθ =
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
TRANSIENT BEHAVIOR TRANSIENT BEHAVIOR –– TEMPERATURETEMPERATURE
• Mean temperature contours
• Steady conduction like state not reached
• Second order term in the Legendre chaos expansion of temperature
• First order term in the Legendre chaos expansion of temperature
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
CAPTURING UNSTABLE EQUILIBRIUMCAPTURING UNSTABLE EQUILIBRIUM• Computational details – 1600 bilinear elements for spatial grid
• Time of simulation – 1.5 non-dimensional units
• Rayleigh number – uniformly distributed random variable between 1530 and 1870 (10% fluctuation about 1700)
• Prandtl number – 6.95
• Time stepping – 0.002 non-dimensional units
• Support-space grid – One-dimensional with ten linear elements
• Simulation about the critical Rayleigh number – conduction below, convection above
• Both GPCE and support-space methods are used separately for addressing the problem
• Failure of Generalized polynomial chaos approach
• Support-space method – evaluation and results against a deterministic simulation
Cold wall
Hot wall
Insulated Insulated
0cθ =
1hθ =X
Y
0 0.25 0.5 0.75 10
0.25
0.5
0.75
1
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
FAILURE OF THE GPCEFAILURE OF THE GPCE
X
Y
0 0.25 0.5 0.75 10
0.25
0.5
0.75
19.2E-07 5.7E-06 1.0E-05 1.5E-05 2.0E-05 2.5E-05 3.0E-05 3.4E-05
X
Y
0 0.25 0.5 0.75 10
0.25
0.5
0.75
1-6.4E-08 4.3E-07 9.3E-07 1.4E-06 1.9E-06 2.4E-06 2.9E-06 3.4E-0
X
Y
0 0.25 0.5 0.75 10
0.25
0.5
0.75
1-5.0E-03 -3.6E-03 -2.1E-03 -7.1E-04 7.1E-04 2.1E-03 3.6E-03 5.0E-03
XY
0 0.25 0.5 0.75 10
0.25
0.5
0.75
1-3.2E-03 -2.0E-03 -8.0E-04 3.9E-04 1.6E-03 2.8E-03 4.0E-03 5.2E-03
X-vel
X-vel
Y-vel
Y-vel
Mean X- and Y-velocities determined by GPCE yields extremely low values !! (Gibbs effect)
X- and Y-velocities obtained from a deterministic simulation with Ra = 1870 (the upper limit)
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
PREDICTION BY SUPPORTPREDICTION BY SUPPORT--SPACE METHODSPACE METHOD
X
Y
0 0.25 0.5 0.75 10
0.25
0.5
0.75
1-5.0E-03 -3.6E-03 -2.1E-03 -7.1E-04 7.1E-04 2.1E-03 3.6E-03 5.0E-03
XY
0 0.25 0.5 0.75 10
0.25
0.5
0.75
1-3.2E-03 -2.0E-03 -8.0E-04 3.9E-04 1.6E-03 2.8E-03 4.0E-03 5.2E-03
X-vel
X-vel
Y-vel
Y-vel
Mean X- and Y-velocities determined by support-space method at a realization Ra=1870
X- and Y-velocities obtained from a deterministic simulation with Ra = 1870 (the upper limit)
X
Y
0 0.25 0.5 0.75 10
0.25
0.5
0.75
1-5.0E-03 -3.6E-03 -2.1E-03 -7.1E-04 7.1E-04 2.1E-03 3.6E-03 5.0E-03
X
Y
0 0.25 0.5 0.75 10
0.25
0.5
0.75
1-3.2E-03 -2.0E-03 -7.4E-04 4.9E-04 1.7E-03 2.9E-03 4.2E-03 5.4E-03
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
MICROSTRUCTURE RECONSTRUCTION MICROSTRUCTURE RECONSTRUCTION & CLASSIFICATION WITH & CLASSIFICATION WITH
APPLICATIONS IN APPLICATIONS IN MATERIALSMATERIALS--BYBY--DESIGNDESIGN
Materials Process Design and Control LaboratorySibley School of Mechanical and Aerospace Engineering
188 Frank H. T. Rhodes HallCornell University
Ithaca, NY 14853-3801
Email: [email protected]: http://www.mae.cornell.edu/zabaras/
Veeraraghavan Sundararaghavan and Nicholas Zabaras
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
MATERIALS DESIGN FRAMEWORK
Machine learning schemes
Microstructure Information library
Accelerated Insertion of new
materials
Optimization of existing
materials
Tailored application specific material
properties
Virtual process simulations to
evaluate alternate designs
Computational process design
simulator
Virtual materials design
framework
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
DESIGNING MATERIALS WITH TAILORED PROPERTIES
Micro problem driven by the velocity gradient L
Macro problem driven by the macro-design
variable βBn+1
Ω = Ω (r, t; L)~Polycrystal
plasticityx = x(X, t; β)L = L (X, t; β)
ODF: 1 2 3 4 5 6 7
L = velocity gradient
Fn+1
B0
Reduced Order Modeling
Data mining techniques
Database
Multi-scale Computation
Design variables (β) are macrodesign variables Processing sequence/parameters
Design objectives are micro-scaleaveraged material/process
properties
Process Process parameters Values ..Tension Strain rate, time, velocity gradient 0.56Forging Forging velocity ,Initial Temperature 2.13
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
DATABASE FOR POLYCRYSTAL MATERIALS
Meso-scale database for polycrystalline materials Machine Learning
Database
Feature Extraction
Data Organization
Reduced order basisgeneration
You
ngsM
odul
us
RD TD
Multi-scale microstructure
evolution models
Process design for desired properties
RD
R-v
alue
0.9850.99
0.9951
1.0051.01
1.0151.02
1.0251.03
1.035
0 10 20 30 40 50 60 70 80 90
Angle from rolling direction
InitialIntermediateOptimalDesired
TD
ODF
Pole Figures
0 20 40 60 80144
144.1
144.2
144.3
144.4
144.5
144.6
144.7
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
MOTIVATIONMOTIVATION1. Creation of 3D microstructure models for property analysis from
2D images
2. 3D imaging requires time and effort. Need to address real–time methodologies for generating 3D realizations.
3. Make intelligent use of available information from computational models and experiments.
vision
Database
Pattern recognition
MicrostructureAnalysis
2D Imaging techniques
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
PATTERN RECOGNITION (PR) STEPSPATTERN RECOGNITION (PR) STEPS
DATABASE CREATION
FEATURE EXTRACTION
TRAINING
PREDICTION
Datasets: microstructures from experiments or physical models
Extraction of statistical features from the databaseCreation of a microstructure class hierarchy: Classification methodsPrediction of 3D reconstruction, process paths, etc.
PATTERN RECOGNITION : A DATA-DRIVEN OPTIMIZATION TOOL•Feature matching for reconstruction of 3D microstructures•Microstructure representation•Texture(ODF) classification for process path selection Real-time
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
3D MICROSTRUCTURE RECOGNITION: A TWO3D MICROSTRUCTURE RECOGNITION: A TWO--CLASS PROBLEMCLASS PROBLEM
Training Features
36.5236.5214.0814.0852.1552.1524.0224.02--11
9.529.5220.0120.01160.12160.1221.3021.3011
11.3011.3025.3025.30158.20158.2020.1020.1011
2.522.5223.0123.01154.12154.1223.3223.3211
Feature Vector (x) Feature Vector (x) –– single feature type (Grain size feature)single feature type (Grain size feature)Class(y)Class(y)
Match lower order features using PR
New Feature (From a 2D image) – To which 3D class does this belong?2.312.3124.1024.10153.14153.1421.4521.45
Heyn intercept histogram of a 2D cross-section
Feature Extraction
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
MULTIPLE CLASSESMULTIPLE CLASSES
Class-AClass-B
Class-CA
CB
AB
C
Given a new planar microstructure with its ‘s’ features given by
find the class of 3D microstructure (y ) to which it is most likely to belong.
[1,2,3,..., ]p∈1 2
1 1 1 2 2 21 1 2 2 1 2 1 2{ , , ...., }, { , , ...., }, ..., { , , ...., }sT T T s s s
m m s mx x x x x x x x x x x x= = =
p = 3One Against One Method:
• Step 1: Pair-wise classification, for a p class problem
• Step 2: Given a data point, select class with maximum votes out of ( 1)
2p p −
( 1)2
p p −
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
TWO PHASE MICROSTRUCTURE: CLASS HIERARCHYTWO PHASE MICROSTRUCTURE: CLASS HIERARCHY
Class - 1
3D MicrostructuresFeature vector : Three point probability
function
3D Microstructures
Class - 2
Feature:Autocorrelation
function
LEVEL - 1 LEVEL - 2
r µm
γ
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
STATISTICAL CORRELATION MEASURESSTATISTICAL CORRELATION MEASURES
MC Sampling: Computing the three point probability function of a 3D microstructure(40x40x40 mic)
S3(r,s,t), r = s = t = 2, 5000 initial points, 4 samples at each initial point.
Rotationally invariant probability functions (SiN ) can be interpreted as the probability of finding the N vertices of a polyhedron separated by relative distances x1, x2,..,xN in phase i when tossed, without regard to orientation, in the microstructure.
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
3D RECONSTRUCTION3D RECONSTRUCTION
Ag-W composite (Umekawa 1969) A reconstructed 3D microstructure
3 point probability function
Autocorrelation function
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
ELASTIC PROPERTIES: YOUNGS MODULUSELASTIC PROPERTIES: YOUNGS MODULUS
170
190
210
230
250
270
290
310
0 200 400 600 800 1000Temperature (deg-C)
You
ngs
Mod
ulus
(GP
a)
HS boundsBMMP boundsExperimentalFEM
3D image derived through pattern
recognition Experimental image
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
MICROSTRUCTURE REPRESENTATION USING SVM & PCAMICROSTRUCTURE REPRESENTATION USING SVM & PCA
COMMON-BASIS FOR MICROSTRUCTURE REPRESENTATION
Does not decay to zero
A DYNAMIC LIBRARY APPROACH
•Classify microstructures based on lower order descriptors.
•Create a common basis for representing images in each class at the last level in the class hierarchy.
•Represent 3D microstructures as coefficients over a reduced basis in the base classes.
•Dynamically update the basis and the representation for new microstructures
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
PCA MICROSTRUCTURE RECONSTRUCTIONPCA MICROSTRUCTURE RECONSTRUCTION
Pixel value round-off
Basis Components
X 5.89
X 14.86
+
Project
onto basis
Reconstruct using two basis components
Representation using just 2 coefficients (5.89,14.86)
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
ORIENTATION FIBERS: LOWER ORDER FEATURES OF AN ODF
1 (1 .
r h y+ (h+y))h y
λ= ×+
Points (r) of a (h,y) fiber in the fundamental region
angle
Crystal Axis = h
Sample Axis = y
φ φ
Rotation (R) required to align h with y
(invariant to , )φ φ
Fibers: h{1,2,3}, y || [1,0,1]
{1,2,3} Pole FigurePoint y (1,0,1)
0 0
h ||y
R .h=h , h||y1P (h,y) = (P (h,y)+P (-h,y))21P (h,y) =
2Adθ
π ∫
Integration is performed over all fibers corresponding to crystal direction h and sample direction y
For a particular (h), the pole figure takes values P(h,y) at locations y on a unit sphere.
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
LIBRARY FOR TEXTURES
[100] pole figure
[110] pole figure
Parameter Feature Vector DATABASE OF ODFs
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
SUPERVISED CLASSIFICATION USING SUPPORT VECTOR MACHINES
Given ODF/texture
Tension (T)
Stage 1
LEVEL – 2 CLASSIFICATIONPlane strain compression
T+P
LEVEL – I CLASSIFICATIONTension identified
Stag
e 2
Stage 3
Multi-stage classification with each class affiliated with a unique process
Identifies a unique processing sequence:
Fails to capture the non-uniqueness in the
solution
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
UNSUPERVISED CLASSIFICATION
Find the cluster centers {C1,C2,…,Ck} such that the sum of the 2-norm distance squared between each feature xi , i = 1,..,n and its nearest cluster center Ch is minimized.
21 2
21,..,1
1( , ,.., ) ( )2min
nk h
ih ki
J c c c x C==
= −∑
Identify clusters
Clusters
DATABASE OF ODFs
Feature Space
Cost function Each class is affiliated with multiple processes
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
PROCESS PARAMETERS LEADING TO DESIRED PROPERTIESY
oung
’s M
odul
us (G
Pa)
Angle from rolling direction
CLASSIFICATION BASED ON PROPERTIES
Class - 1 Class - 2
Class - 3Class - 4 0.5 0.25 00.25 -1.25 0
0 0 0.75
0.5 0 00 0.75 00 0 -1.25
Velocity Gradient
Different processes, Similar properties
Database for ODFs
Property Extraction
ODF Classification
Identify multiple solutions
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
A TWOA TWO--STAGE PROBLEMSTAGE PROBLEM
Process – 2 Plane strain compression α = 0.3515
Process – 1 Tension α = 0.9539Initial Conditions:
Stage 1
Sensitivity of material property
Initial Conditions- stage 2
DATABASE Reduced Basis
φ(1) φ(2)
Direct problem
Sensitivity problem
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
MULTIPLE PROCESS ROUTESMULTIPLE PROCESS ROUTES
0 10 20 30 40 50 60 70 80 90144
144.5
145
145.5
Angle from the rolling direction
You
ngs
Mod
ulus
(GP
a)
Desired Young’s Modulus distribution
Magnetic hysteresis loss distribution
0 10 20 30 40 50 60 70 80 901.205
1.21
1.215
1.22
1.225
1.23
1.235
1.24
Mag
netic
hys
tere
sis
loss
(W/k
g) Stage: 1 Shear-1 α = 0.9580
Stage: 2 Plane strain compression (α = -0.1597 )
Stage: 1 Shear -1 α = 0.9454
Stage: 2 Rotation-1
(α = -0.2748)
Stage 1: Tension α = 0.9495
Stage 2: Shear-1 α = 0.3384
Stage 1: Tension α = 0.9699
Stage 2: Rotation-1 α = -0.2408
Classification
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
DESIGN FOR DESIRED ODF: A MULTI STAGE PROBLEMDESIGN FOR DESIRED ODF: A MULTI STAGE PROBLEM
0 5 10 15 20 250
0.2
0.4
0.6
0.8
1
Iteration Index
Nor
mal
ized
obj
ectiv
e fu
nctio
nInitial guess, α1 = 0.65,
α2 = -0.1
Desired ODF Optimal- Reduced order control
Full order ODF based on reduced order control parameters
Stage: 1 Plane strain compression (α1 = 0.9472)
Stage: 2 Compression (α2 = -0.2847)
Materials Process Design and Control LaboratoryMaterials Process Design and Control LaboratoryCCOORRNNEELLLL U N I V E R S I T Y CCOORRNNEELLLL U N I V E R S I T Y
DESIGN FOR DESIRED MAGNETIC PROPERTYDESIGN FOR DESIRED MAGNETIC PROPERTY
I te ra t io n I n d e x
Nor
mal
ized
obj
ectiv
e fu
nctio
n
5 1 0 1 50
0 .2
0 .4
0 .6
0 .8
1
h
Crystal direction.
Easy direction of
magnetization – zero power
loss
External magnetization direction
0 20 40 60 80
1.21
1.215
1.22
1.225
1.23
1.235
Angle from the rolling direction
Mag
netic
hys
tere
sis
loss
(W/K
g)
Desired property distributionOptimal (reduced)Initial
Stage: 1 Shear – 1 (α1 = 0.9745)
Stage: 2 Tension
(α2 = 0.4821)