Hong Kong MPR -09
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Transcript of Hong Kong MPR -09
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The experimental validation of numerical simulation for precise polymer melt processing
by
Malcolm Mackley, David Hassell* Tim Lord and Lino Scelsi.
Department of Chemical Engineering and Biotechnology. University of Cambridge. UK
*School of Chemical and Environmental Engineering. University of Nottingham.Selanger, Darul Ehsan, Malaysia
Hong Kong 2009
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Mission
• Carry out precise polymer processing experiments that can be compared with simulation.
• Characterise rheology of polymer and select constitutive equation.
• Numerically simulate viscoelastic flow and match result with experiment.
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The Cambridge Multipass Rheometer (MPR)
Rheo Optic slit flow mode Cross-slot flow mode
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The Cambridge Multipass Rheometer (MPR)
Top section
Test section
Bottom section
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Test section geometries
• Slit
Depth =10, 7 and 1.5 mm
1.4 mm
1.5 mm
1.5 mm
1.5 mm
10 mm
0.75 mm
• Cross-Slot
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Depth =10, 7, and 1.5 mm
R = 0.375 mm
Z ~ 1.4 mm
10 mm
The Geometries: Contraction Expansion Slit
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An example of Rheo optic slit flow for LDPE
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Visit MPR Slit Flow movie
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The Cross-Slot
• Generates a hyperbolic pure shear flow pattern as shown.• Near centre. Essentially uniform extensional flow with residence time, which
is equivalent to strain, inversely dependant on distance from the exit symmetry axis
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MPR Cross-Slot Flow
• The MPR action modified for cross-slot flow
• Pistons force polymer melt through a cross-slot geometry
Kris Coventry and Collaborative project with Leeds University; Tom Mcleish et al
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Typical Result
-Dow PS680E
-Piston velocity of 0.5 mm/s (maximum extension rate =4.3/s).
-Inlet slit width=1.5mm
-Section depth=10mm
- T=180°C.
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Visit MPR Cross Slot Flow movie
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Rheology and Characterisation
• Linear viscoelasticity
Obtain spectrum of relaxation times• Non Linear response.
Sentmanat Extensional Rheometry fixtures (SER)• Constitutive equations
Pom Pom or Rolie Poly• Simulation
Leeds 2D Flowsolve or 3D EUsolve
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Simulation
For linear polymer melts, “Rolie-Poly” theory is used
Constitutive equation;
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Multimode Pom-Pom model
Viscoelastic stress:
Backbone orientation:
Stretch:
Time scales:
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16dP = 3.32 bar dP = 3.76 bar
3D simulation2D simulation
Vp = 0.44 mms-1
2D FlowsolveAnd3D EUsolve
Polystyrene (PS2)
10mm depth
Pom Pom
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17dP = 3.96 bardP = 3.76 bar
Vp = 0.44 mms-1
3D simulation Experiment
3D EUsolve
Polystyrene (PS2)
10mm depth
LHS Pom Pom
RHS Experiment
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3D EUsolve
Polystyrene (PS2)
7 mm depth
LHS Pom Pom
RHS Experiment
dP = 5.46 bar dP = 5.18 bar
Vp = 0.44 mms-1
3D simulation Experiment
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3D EUsolve
Polystyrene (PS2)
1.5 mm depth
LHS Pom Pom
RHS Experiment
dP=9.66bardP=17.24bar
Vp = 0.07 mms-1
3D simulation Experiment
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t= 0.1 s t= 10 s t= 18.9 ss
t = 0.1 s t = 8 s t = 12 s
PomPom
RoliePoly
Pom Pom vs Rolie Poly, 3D EUsolve
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Vp = 0.04 mms-1 Vp = 0.09 mms-1
MPR experiment3D simulation MPR experiment3D simulation
Cross Slot Pom Pom 3D EUsolve
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Vp = 0.07 mms
Cross Slot 1.5mm depth. Pom Pom 3D EUsolve
Simulation Experiment
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t = .1 s t = 8.5 s t = 37 s
t = 0.1 s t =17 s t =37 s
Cross Slot Pom Pom vs Rolie poly 3D EUsolve
PomPom
RoliePoly
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24EPSRC Microscale Polymer Processing project
Tim Lord, David Hassell and Dietmar Auhl 2008
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10-1 100 101 102 103
103
104
105
106
LDPET = 150°C 10
5
2
10.5
0.10.010.001
shear
visc
osi
ty (
t), P
as
elo
ngatio
nal v
isco
sity
(t)
, P
as
time t, s
10
3
10.3
0.001
0.003
0.010.030.1.0 [s-1]
.0 [s-1]
Stagnation Point flows as rheometersDr Dietmar Auhl et al, Leeds University 2008
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ststyyxxstE /)(,
pistonst VxA
22 4 xyyyxxSOCn X-4 -2 0 2 4
steady-state elongational viscosity at the stagnation point
=
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Dr Dietmar Auhl et al , Leeds University
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Conclusions
• MPR experiments provide precise processing data.
• Both Rolie Poly and Pom Pom models can be simulated to give good experimental matching.
• Simulation can be sensitive to both constitutive equations,
relaxation spectra and non linear fit.
Acknowledgements. Tom Mcleish for masterminding Microscale Polymer Processing project and EPSRC for providing most of the funds