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Simulation of Polymer Processing

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Simulation of Polymer Processing David O. Kazmer, P.E., Ph.D. March 26, 2005 Progress in Polymer Process Simulation! General Electric 1988 Vax 8800 cluster E&S 3D ... – PowerPoint PPT presentation

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Title: Simulation of Polymer Processing


1
Simulation ofPolymer Processing
  • David O. Kazmer, P.E., Ph.D.
  • March 26, 2005

2
Progress in Polymer Process Simulation!
  • General Electric 1988
  • Vax 8800 cluster
  • ES 3D vector graphics
  • UML 2005
  • PC

3
Simulation of Polymer ProcessingAgenda
  • Modeling Overview
  • Governing Equations
  • Constitutive Models
  • Numerical Solution
  • Capabilities
  • Challenges

4
MotivationUnderstand Process
  • Polymer processing is a nasty black box
  • Dynamic process
  • Multivariate process
  • Spatially distributed process
  • Complex 3D geometry
  • Thermoviscoelastic materials
  • Multiple quality requirements
  • Expensive mold tooling changes

5
MotivationVirtual Development
  • Model and understand the process
  • Perform virtual development
  • What-if analyses
  • System-level optimization

6
MotivationPost-Mortem Analysis
  • Modeling of existing processes
  • Inspection of internal polymer states
  • Pressure, temperature, flow rate, shear stress,
    shear rate,
  • Development of corrective strategies
  • Change process conditions
  • Assess material changes
  • Recommend mold tooling changes

Simulation provides the means for trying the
impossibleat negligible cost.
7
Agenda
  • Motivation
  • Governing Equations
  • Constitutive Models
  • Numerical Solution
  • Capabilities
  • Challenges

8
Governing EquationsNavier Stokes Equations
  • For laminar (or time-averaged turbulent) flow
  • Net pressure force is the gradient of the
    pressure
  • Net viscous force is the Laplacian of the velocity

N-S assumes that all macroscopic length and time
scales are considerably larger than the largest
molecular length and time scales.
9
Polymer Processing SimulationTypical Assumptions
  • Viscous flow
  • Negligible inertia
  • Negligible viscoelasticity
  • Known boundary conditions
  • No slip at mold wall
  • Constant inlet resin temperature
  • Flow travels in a plane
  • No out of plane flow
  • 2D simplification

10
Governing EquationsMass Equation
  • Conservation of mass
  • What goes in must come out
  • Or stay in there
  • Change in density with non-steady velocity

IN
OUT
?r
11
Governing EquationsMomentum Equation
  • Conservation of momentum
  • Change in pressure in the flow direction is due
    to shear stress of flowing viscous melt

12
Governing EquationsHeat Equation
  • Conservation of energy
  • Change in temperature balances heat convection,
    heat conduction, and shear heating (and others)

13
Agenda
  • Motivation
  • Governing Equations
  • Constitutive Models
  • Numerical Solution
  • Capabilities
  • Challenges

14
Constitutive ModelsOverview
  • Constitutive model describes the behavior of the
    material as a function of polymer state
  • Viscosity, density,
  • Trade-offs between
  • Model form and complexity
  • Number of model parameters
  • Data redundancy in model fitting
  • Computational efficiency stability
  • Everything should be made as simple as possible
    -but no simpler! - Einstein

15
Constitutive ModelsViscosity
  • Most polymers are shear thinning
  • Cross model
  • WLF temperaturedependence

16
Constitutive ModelsViscoelasticity
  • Polymers exhibit melt elasticity
  • Memory effect
  • 5 orders of magnitude!
  • Extremely data andCPU intensive
  • Need to store andcompute on current andall past
    process states!

17
Constitutive ModelsSpecific Volume
  • Polymers exhibit thermal expansion and
    compressibility
  • Double domainTait Equation

18
Constitutive ModelsSpecific Heat
  • Specific heat Cp

19
Constitutive ModelsThermal Conductivity
  • Thermal conductivity k

20
Agenda
  • Motivation
  • Governing Equations
  • Constitutive Models
  • Numerical Solution
  • Capabilities
  • Challenges

21
Numerical MethodsGeometric Modeling
  • Polymer domain decomposed into elements
  • 2D elements across flow domain
  • Plastics parts are often thin so nice assumption
  • Each element has defined thickness
  • 3D elements for entire domain
  • Need many, many elements of higher order shape
    functions

22
Numerical MethodsSolution
  • Iterative solution method
  • Flow field
  • Temperature field

23
Numerical MethodsFinite Element Solution of Flow
4
4
6
1
1
2
2
3
3
5
k35
24
Numerical MethodsFinite Difference Solution of
Heat
HeatConvection
ViscousHeating
Changein Temp
HeatConduction
AdiabaticCompression
5
25
Agenda
  • Motivation
  • Governing Equations
  • Constitutive Models
  • Numerical Methods
  • Capabilities
  • Challenges

26
CapabilitiesOptical Media Molding
  • Optical media CDs DVDs
  • Injection-compression molding (coining)

27
Numerical AlgorithmCoining Process
  • Coining Process
  • Partly open mold
  • Inject polymer
  • Profile clamp force
  • Simulation

Force
28
Coining Process ValidationDisplacement Profiles
Effect of melt temperature experiment vs.
simulation
29
Birefringence Models
  • Constitutive model for flow induced stress
    (Wagner, M. H. et al)

30
Birefringence Models (Cont.)
  • Shear stress
  • First normal stress difference
  • Integral stress-optical rule
  • (birefringence constitutive model)
  • Path difference (retardation)

31
Numerical Algorithm
  • Incremental formulation for the integral
    equations
  • Solved by FDM in time domain

32
In-plane Birefringence Validation
Validation experiment vs. simulation
33
Vertical Birefringence Prediction
Effect of mold temperature (low-high) simulation
34
Simulation of Internal Stressand Post-Molding
Deformation
  • Thermal stress/warpage
  • In-mold FDM (Baaijens, F. P. T. et al)
  • Out-of-mold FEA (plate bending)

35
Finite Element Discretization
  • Kirchhoff thin-plate elements

36
Finite Element Formulation
  • Strain-displacement relationship
  • Stress-strain relationship
  • Element stiffness matrix and element
    right-hand-side vector

37
Relaxation ModelingTruncated WLF Equation
  • WLF Fit by data at 150-280oC
  • Truncated at at 140, 135, 130, 125oC

38
Effect of the Truncation
  • Warpage at different truncation temperatures
  • Could fudge any desired result!

39
Proposed Function for Relaxation Model, aT
  • For TltTref
  • For TgtTref

40
Results for ImplementedRelaxation Function, aT
  • Model fit performance in simulation

41
Optical Molding SimulationResults Summary
  • Optical media simulation used for
  • Process development and optimization
  • Development of new polymeric materials
  • Higher data density lower costs

42
Agenda
  • Motivation
  • Governing Equations
  • Constitutive Models
  • Numerical Solution
  • Capabilities
  • Challenges

43
ChallengesProcess Controllability
  • What are the boundary conditions foranalysis?
  • Is melt temperature constant?
  • What is the mold wall heat transfer?
  • Is a no-slip condition at mold wall valid?

44
ChallengesConstitutive Models
  • N-S assumes a continuum
  • Is a continuum approach valid on the nano-level?
    If not
  • What are the governing equations?
  • What are the constitutive models?
  • How to apply thermodynamics statistics?

45
ChallengesNumerical Methods
  • Modeling on the atomic scale?
  • Sandia Labs Atomic weapons
  • Crystal-level modeling of metals
  • Protein folding

46
Final ThoughtsModeling Principles
  • Pritskers Modeling Principles, from Handbook of
    Simulation, edited by Jerry Banks for Wiley
    Interscience, 1998
  • Model development requires system knowledge,
    engineering judgment, and model-building tools.
  • The modeling process is evolutionary because the
    act of modeling reveals important information
    piecemeal.
  • The secret to being a good modeler is the ability
    to remodel.
  • A model should be evaluated according to its
    usefulness.
  • From an absolute perspective, a model is neither
    good or bad, nor is it neutral.
  • All truths are easy to understand once they are
    discovered the point is to discover them.
  • Galileo
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