Birefringence in Injection-Compression Molding ofAmorphous Polymers: Simulation and Experiment
Nam Hyung Kim, Avraam I. IsayevDepartment of Polymer Engineering, The University of Akron, Akron, Ohio 44325-0301
The influence of the processing variables on the resid-ual birefringence was analyzed for polystyrene and pol-ycarbonate disks obtained by injection-compressionmolding under various processing conditions. Theprocessing variables studied were melt and mold tem-peratures, compression stroke, and switchover time.The modeling of flow-induced residual stresses andbirefringence of amorphous polymers in injection-com-pression molded center-gated disks was carried outusing a numerical scheme based on a hybrid finiteelement/finite difference/control volume method. Anonlinear viscoelastic constitutive equation and stress-optical rule were used to model frozen-in flow stressesin moldings. The filling, compression, packing, andcooling stages were considered. Thermally-inducedresidual birefringence was calculated using the linearviscoelastic and photoviscoelastic constitutive equa-tions combined with the first-order rate equationfor volume relaxation and the master curves for theYoung’s relaxation modulus and strain-optical coeffi-cient functions. The residual birefringence in injection-compression moldings was measured. The effects ofvarious processing conditions on the measured andsimulated birefringence distribution Dn and averagetransverse birefringence <nrr2nhh> were elucidated.Comparison of the birefringence in disks manufacturedby the injection molding and injection-compressionmolding was made. The predicted and measured bire-fringence is found to be in fair agreement. POLYM. ENG.SCI., 53:1786–1808, 2013. ª 2013 Society of Plastics Engineers
INTRODUCTION
Conventional injection molding (CIM) process [1] is
one of the most widely employed polymer processing
operations, being characterized by high degree of automa-
tion, high productivity and good dimensional stability of
moldings. The process can make products with complex
geometries in one production step. Many macro- and
microdevices, such as watches and camera components,
automotive crash and acceleration distance sensors, read/
write heads of hard disks, CD drives, medical sensors,
pump, surgical instruments, and telecommunications com-
ponents, have been successfully molded by CIM. Molded
part defects, such as uneven shrinkage, warpage, sink
marks, residual stresses, and nonuniformity of mechanical
properties, are affected by the entire injection molding
cycle. In molded optical plastic parts, the residual
birefringence, caused by the flow and thermal stresses,
strongly affects their performance. In particular, the bire-
fringence can significantly reduce an optical performance
of electronic devices such as liquid crystal displays,
camera lenses, CD, DVD and other optical products.
A compression molding (CM) is the widely used
process to manufacture various products [1–4]. In this
process, polymer melt is squeezed by the moving platen
to fill the mold. The melt is then continued to be com-
pressed by the pressure exerted from the mold wall of the
core side. This process provides a more uniform pressure
along the cavity wall and requires a low molding pressure
for the postfilling process resulting in less part warpage
and residual stress. However, this operation cannot
achieve high productivity due to the labor-intensive
charge installation. It also has a limitation for molding
large parts of complex shapes.
In recent years, manufacturing of precision plastic opti-
cal products with a strong quest for quality, such as
lenses, disk substrates and other optical components, is
continuously gaining more importance. Though precision
parts usually have simple geometrical shapes such as
disks, plates, or cylinders, their dimensional accuracy and
stability must be strictly satisfied [5]. The optical
performance of these moldings depends on the frozen mo-
lecular orientation, residual stresses and birefringence.
Several special injection molding techniques have been
developed in order to fulfill the rising requirements on the
part quality. Among them, the injection-compression
molding (ICM) is widely used for producing parts with
improved dimensional stability and surface accuracy. By
adding a compression stage after partial melt filling of
the cavity, ICM provides advantages, such as a lower
molding pressure [6] and clamp force (typically 20 to
50% lower) [7], reducing cycle time and residual stress,
minimizing molecular orientation and birefringence, pack-
ing evenly, reducing uneven shrinkage, overcoming sink
Correspondence to: Avraam I. Isayev; e-mail: [email protected]
Contract grant sponsor: NSF Division of Engineering; contract grant
number: DMI-0322920.
DOI 10.1002/pen.23429
Published online in Wiley Online Library (wileyonlinelibrary.com).
VVC 2013 Society of Plastics Engineers
POLYMER ENGINEERING AND SCIENCE—-2013
mark and warpage, reducing density variation and increas-
ing dimensional accuracy [8]. Thus, ICM is a suitable
technique to manufacture high precision optical parts with
improved optical performance [9].
Klepek [10] used the ICM to mold thick optical lenses.
Yang and Lien [11] studied ICM to manufacture high pre-
cision lenses. They compared the quality of polystyrene
(PS) convex lenses made by ICM with that of PS lenses
made by CIM. They found that ICM produced lenses of a
better quality than those produced by CIM at the same
cooling time. They concluded that ICM was a better solu-
tion for molding of high-end plastic optical lenses. Yang
and coworkers [8, 12–14] experimentally investigated the
quality of ICM disks and showed that ICM enhanced the
dimensional accuracy, especially in the direction perpen-
dicular to compression. Shin et al. [15] carried out experi-
mental study on birefringence in optical disks under vari-
ous processing conditions and concluded that the birefrin-
gence was mostly affected by the mold temperature and
cooling time. Michaeli and Wielpuetz [16] investigated
effects of processing parameters of ICM and CIM on the
optical part quality of windscreen for window panes using
a design of experiments. The main parameters influencing
the optical part quality were the injection and compression
velocity in ICM and the injection velocity and the packing
pressure in CIM. Chen and Young [17] studied the effect
of adding the compression stage to CIM for manufacturing
disks and found the significant improvement in their con-
formity to cavity profile and a reduced warpage.
At the present time, the science-based technology for
manufacturing of the ICM optical products has not been
fully established. This is due to the lack of understanding
of viscoelastic mechanical and optical behaviors that
polymers experience during the injection and compression
stages. Numerical analysis of the process including the
viscoelastic effect is quite difficult. Isayev and Hieber
[18] were the first who proposed a theoretical approach to
relate the nonlinear viscoelasticity of polymers to the de-
velopment of frozen-in molecular orientation (birefrin-
gence) in CIM. Also, Isayev and Azari [19] and Isayev
et al. [20] carried out both theoretical and experimental
investigations of squeezing flow of melt using a nonlinear
viscoelastic constitutive equation. They considered the
shear-free flow and the channel flow with moving bound-
ary squeezing the melt similar to that occurring in the
compression stage of ICM. Osswald and Tucker [21] pre-
sented compression molding simulations for nonplanar
parts by combining a finite element (FE) method based
on a control volume for tracking the moving flow front
based on inelastic flow models. Kwon et al. [22, 23] stud-
ied experimentally and numerically the birefringence dis-
tribution in ICM center-gated disk based on a nonlinear
viscoelastic fluid model. Wang [24] used a Hele-Shaw
flow to predict the melt front advancement and the distri-
bution of pressure, temperature, and flow velocity during
the injection, compression and packing stages of ICM.
Park et al. [25] presented a numerical simulation for ICM
of a center-gated disk using finite difference (FD) method
using Leonov compressible viscoelastic model and the
Tait equation of state. Kim et al. [26] and Lee et al. [27]
developed a numerical analysis using FD for the solution
of governing equations of the radial flow and studied the
distribution of birefringence in CIM and ICM center-gated
disk using the Leonov model. Chen et al. developed a nu-
merical algorithm to simulate the filling stage of the
stamping type of ICM using an inelastic [28–30] and
viscoelastic [31] flow. In particular, the effect of the proc-
essing conditions on simulated and measured cavity pres-
sures was studied and a fair agreement between them was
achieved [28]. The simulated results indicated that ICM
significantly reduces shrinkage and improves the uniform-
ity of moldings. Also, they studied effects of various
processing parameters on the average transverse birefrin-
gence without considering the gapwise birefringence dis-
tribution. The results showed that the transverse birefrin-
gence decreases with an increase of the melt temperature
and a decrease of the mold closing velocity, but it is
insignificantly affected by the flow rate and the mold tem-
perature.
Friedrichs et al. [32] used an incompressible viscous
flow model to simulate the birefringence in ICM of the
stamping type. Kim et al. [26, 33] carried out a numerical
analysis to investigate the effects of the compression stage
on the birefringence in ICM of the stamping type using a
viscoelastic model. They found that, in comparison with
CIM, ICM reduced the birefringence and the mold tem-
perature had a significant effect on the density distribution
in comparison with other processing conditions. Fan et al.
[34] developed a code for the simulation of ICM of a
CD-R using a compressible viscous flow model. Young
[35] investigated the residual stresses and shrinkage of
ICM pickup lens having large thickness variations using a
Cross-WLF type equation for description of the viscosity
and a modified Tait equation for the density. The mold
temperature and compression time were found to be the
most important factors affecting the lens shrinkage in the
thickness direction, resulting in surface profile deviation.
Rohde et al. [36] carried out an experimental investigation
on the effect of process parameters on the replication of
various microstructures on a flat disk using micro ICM.
The dimensions of the microstructures on the inserts card
moldings were measured using a confocal profiler and a
transcription ratio was determined to assess the quality of
the replication. Huang and Chung [37] experimentally
studied the feasibility of CIM and ICM for fabricating
3.5-inch light-guide plates (LGPs) with V-grooves. They
found that the height of the V-grooved microfeatures
replicated by ICM more accurately than those replicated
by CIM. Min and Yoon [38] compared the measured bire-
fringence and extinction angle in CIM and ICM disks and
found more uniform gapwise distributions of these quanti-
ties in the ICM disks. Also, a graphical representation of
the optical refractive indicatrix was suggested. Nagato
et al. [39] carried out experimental investigation of the
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2013 1787
effects of the mold temperature and pattern shape on the
degree of replication of high-aspect-ratio nanostructures
in optical disks and Ni stamper by ICM. A higher mold
temperature resulted in better replication. Ho et al. [40]
performed a three-dimensional (3D) numerical simulation
of flow in ICM and compared the simulated results with
existing experimental data for optical lenses. 3D flow
effects were found to be significant, especially during the
compression stage, and ICM achieved more uniform dis-
tributions of the shear rates and stresses in comparison
with CIM.
In the present study, extensive simulations of the vari-
ous components of the flow birefringence developed dur-
ing the filling, compression, packing, and cooling stages
of the ICM of a center gated disk of polystyrene (PS) and
polycarbonate (PC) is carried out by using hybrid CV/FE/
FD method. The Tait equation [41] is used to describe the
P-V-T relationship. The compressible nonlinear visco-
elastic model [42] is used to calculate the flow stresses.
The flow birefringence was calculated through a linear
stress-optical rule [43]. The linear viscoelasticity was used
to calculate the thermal stresses [44–46]. The thermal
birefringence is calculated from the thermal stresses using
the linear photoviscoelasticity and free volume theory tak-
ing into account the density relaxation [44–46]. Although
the coupling effect between the flow and thermal stresses
is neglected in calculations of the total residual stresses
and birefringence, the present ICM study shows that the
thermal birefringence contribution is significant in the
core of PS disks and throughout the thickness for PC
disks.
MATERIALS AND EXPERIMENTAL PROCEDURES
Two polymers used in the experiments are PS (Styron
615-APR) supplied by Dow Chemical Company and PC
(Lexan 123) supplied by General Electric (GE) Plastics.
The thermophysical properties of polymers are listed in
Table 1 [45–47]. The apparent viscosity, g, of PS melt as
a function of the shear rate, _c, were taken from the refer-
ences [46, 48] at temperatures of 161, 180.5, and
200.58C. The apparent viscosity of PC melt as a function
of the shear rate was measured at temperatures of 260,
273.3, 286.7, and 3008C using an Advanced Capillary
Rheometer (RH7). These viscosity data are depicted in
Fig. 1 for PS (a) and PC (b). These data were fitted using
the two relaxation modes for PS [46] and six relaxation
modes for PC by means of nonlinear regression [49]. The
lines in these figures represent the nonlinear regression fit
of the experimental data to the following equation [18]:
Z ¼ Z0sþXNk¼1
2Zk
1þffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffi1þ 4 gykð Þ2
q (1)
where gk and hk are the temperature-dependent viscosity
and relaxation time of kth relaxation mode according the
WLF equation, s is the parameter lying between 0 and 1.
The parameters obtained from the best fit are listed in
Table 2. The density of polymer melts as a function of
temperature and pressure was presented by the P-V-T
equation of state due Tait [41, 47]. These parameters are
listed in Table 3.
ICM Experiments
Center-gated disks were made by the ICM using Hull
Hydraulic Transfer Molding Press. The schematic diagram
of the apparatus used in ICM experiments is shown in
Fig. 2. The machine is a vertical type ram injection unit
with a clamping system actuated by the hydraulic pres-
sure. The diameter and thickness of the center-gated disks
TABLE 1. Physical properties of polymers.
Properties PS PC
q0 3 103 (kg/m3)a 1.04 [46] 1.16 [47]
q 3 103 (kg/m3)a 0.984 [46] 1.06 [47]
Cp (J/kg K) 1420 [46] 2150 [47]
K (W/m K) 0.17 [46] 0.234 [47]
h (J/s m2 K) 490 [45] 490 [45]
a q0 at T ¼ 258C and q at T ¼ 1808C.
FIG. 1. Measured (symbols) [43] and fitted (curves) viscosity of PS
[47] (a) and PC (b) as a function of shear rate.
1788 POLYMER ENGINEERING AND SCIENCE—-2013 DOI 10.1002/pen
are 12.7 cm and 0.3175 cm, respectively, with the inlet
diameter of 1.36 cm. The schematic mold geometry with
coordinates s, h, z is shown in Fig. 3. The data acquisition
system is used to record the pressure measured by a pres-
sure transducer (Dynisco PT435A) at the center of the
mold and the ram position measured by means of linear
velocity displacement transducer (LVDT).
The ICM experiments were carried out in the follow-
ing manner. PS and PC pellets were dried at 808C and
1058C, respectively, for 4 h under vacuum. The exact
amount of PS and PC required to fill the delivery system
and cavity are used. At first, PS and PC disks of a diame-
ter of 4.445 cm were compression molded at a tempera-
ture of 2008C and 2308C, respectively. Then, the disks
were placed into the cylinder of the machine, and melted.
Finally, the ICM experiments were conducted using dif-
ferent processing conditions by varying the mold and melt
temperatures, compression stroke and switchover time
from injection to compression stage. These processing
conditions for molding of PS and PC disks are shown in
Table 4.
Birefringence Measurements
The measurement of the average transverse birefrin-
gence, < nss � nhh >, in ICM and CIM PS and PC disks
is done on blocks of 1.5 cm in width removed from the
disks, as shown in Fig. 4. To measure the gapwise bire-
fringence distribution, Dn, slices of a thickness of 0.5 mm
and 1 mm were cut parallel to the s� z plane of disks, as
also shown in Fig. 4. A low-speed diamond saw (Iso-
metTM, Buechler) at 120 RPM is used to cut the slices.
The thickness of the slices was measured using a digital
micrometer with a resolution of 0.001 mm. The optical
retardation of the slices was measured using a cross-polar-
ized optical microscope (Leitz laborlux 12 POL, Leitz
Wetzlar) with a four-order tilting compensator for PS and
a thirty-order compensator for PC (1592k, Leitz Wetzlar).
To determine the gapwise position at which the retarda-
tion of the slices is measured, a scale on the microscope
eyepiece and a 403 magnification objective lens are used.
The birefringence measurements are typically started at
about 0.125 mm away from the surface of the disk, since
compensation of the retardation was difficult to achieve at
the position closer to the surface. The average transverse
birefringence, < nss � nhh >, was measured using a Gaert-
ner optical polariscope (model L305) equipped with a
seven-order Babinet compensator (model L-133-A). The
birefringence is calculated from the measured retardation
as Dn ¼ C=d, where C is the optical retardation and d is
the slice thickness.
To determine the sign of the birefringence in PS and
PC disks, the direction of the slow axis in each sample is
compared to the direction of the slow axis shown by the
four-order and 30-order tilting compensators which have
the direction opposite to the slow axis. In particular, the
slow axis of PS sample is perpendicular to the flow
direction due to the presence of the benzene ring. For PS
sample, the direction of the slow axis of the tilting com-
pensators coincides with the direction of the slow axis.
Therefore, the sign of the birefringence of PS is negative.
The direction of the slow axis for the PC sample is per-
pendicular to the direction of the slow axis of the tilting
compensators. Therefore, the sign of the birefringence of
PC is positive.
NUMERICAL ANALYSIS
To reduce computation time in simulation of the mold-
ing process, a quarter of the disk was discretized in plane
by FE triangles. Along the gapwise direction FD meshes
were used. In FE modeling, a finer mesh typically results
in a more accurate solution, however, at the expense of a
significant increase of the computation time. In the cur-
rent simulations the disk mold was divided into 315 ele-
TABLE 3. Material constants in Tait equation.
Tait equation PS [47] PC [47]
b1,l (m3/kg) 970.8 862.8
b2,l (m3/kg K) 0.5788 0.549
b3,l (Pa) 1.555 3 108 1.565 3 108
b4,l (K21) 3.019 3 1023 2.738 3 1023
b1,s (m3/kg) 970.8 862.8
b2,s (m3/kg K) 0.2429 0.2229
b3,s (m3/kg) 2.008 3 108 2.65 3 108
b4,s (K21) 1.38 3 1023 2.78 3 1023
b5 (K) 360.2 422.2
b6 (K/Pa) 3.20 3 1027 5.00 3 1027
TABLE 2. Material constants of PS and PC used in the CIM and ICM
molding simulation.
Material constants PS PC
WLF equation
C1 8.285 7.23
C2 (K) 131.5 163.4
Tr (K) 474.15 533.15
Leonov model
s 0.0048 0.0001
g1 (Pa s) 2228 30.1
g2 (Pa s) 446.8 9.11
g3 (Pa s) — 392
g4 (Pa s) — 766
g5 (Pa s) — 50.8
g6 (Pa s) — 18.4
y1 (s) 0.1466 2.1
y2 (s) 0.00489 0.104
y3 (s) — 0.011
y4 (s) — 0.00115
y5 (s) — 0.00012
y6 (s) — 0.000016
Stress-optical coefficient and
volume relaxation time
Cflr (Pa21) 25.2 3 1029 [45] 5.6 3 1029 [45]
sr (s) 0.04 [45] 0.3 [45]
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2013 1789
ments and 184 nodes in the plane based on the previous
work [46] where the initial trial showed that the computa-
tion time is significantly increased with an increase in
number of elements and nodes. With these meshes, the
CPU time to carry out calculations for one processing
condition was 4 to 6 h on Pentium IV 3 GHz PC.
For numerical simulation in the filling, compression,
packing and cooling stages, a nonlinear viscoelastic model
is used [42]. The resulting set of nonlinear algebraic equa-
tions was solved with a globally convergent Newton’s
method [50, 51].
Governing Equations of ICM Process
Mold filling during the ICM process is comprised of
two stages: injection mold filling of a melt into a partially
open mold and subsequent compression mold filling by
closing the mold. Inelastic [52–54] and viscoelastic [46,
50, 54–57] simulations of the CIM have been already
developed based on the control volume approach [54].
The governing equations for flow of the viscoelastic melt
under nonisothermal conditions during the compression
stage are presented earlier [57]. This article has also pro-
vided the solution for the melt front advancement during
injection and compression stages. In particular, the volu-
metric flow rate during the compression stage is equal to
the rate at which the mold is closed displacing a volume
of the melt injected. For control volumes located on the
flow front, the filling parameter is calculated from the
occupied volume fraction and the additional volume frac-
tion due to compression flow at a given time [57]. It
should be noted that the study [57] has not considered the
packing and cooling stages of the ICM in the develop-
ment of the flow birefringence and also the contribution
of the thermal birefringence into the total birefringence.
In the ICM simulation, the density q T;Pð Þ is assumed to
follow the Tait equation [41, 47].
The parameters gk and hk of kth mode are temperature-
dependent quantities based on the WLF-type temperature
dependence [57, 58].
FIG. 2. Schematic diagram of ICM apparatus used in experiments.[Color figure can be viewed in the online
issue, which is available at wileyonlinelibrary.com.]
1790 POLYMER ENGINEERING AND SCIENCE—-2013 DOI 10.1002/pen
The governing equation for the viscoelastic flow during
injection and compression stages of ICM are given in
Refs. 50, 55–58, respectively.
Numerical Implementation
On the basis of the formulations described earlier [50,
55–58], a numerical scheme using CV/FE/FD for a two-
dimensional viscoelastic flow in a center-gated disk is
developed. To solve the equations, a set of appropriate
boundary conditions is given first. The CV/FE [54] with
FIG. 3. Geometry of a center-gated disk with coordinate system.
TABLE 4. Processing conditions for manufacturing of ICM and CIM PS and PC disks.
Run no. Melt temp. Mold temp. Volume flow rate (cm3/s) Compression stroke (cm) Compression speed (cm/s) Switch over time (s)
PS
1 230 40 13 0.15 0.4 1.1
2 230 60 13 0.15 0.4 1.1
3 230 80 14 0.15 0.4 1.1
4 190 60 14 0.15 0.4 1.1
5 210 60 14 0.15 0.4 1.1
6 230 60 15 0.1 0.4 1.0
7 230 60 16 0.2 0.4 1.08 210 60 15 0 0 0
PC
1 260 40 23 0.15 0.4 1.12
2 260 60 23 0.15 0.4 1.0
3 260 80 26 0.15 0.4 1.12
4 240 60 22 0.15 0.4 1.0
5 280 60 24 0.15 0.4 0.86
6 260 60 23 0.1 0.4 1.2
7 260 60 22 0.2 0.4 1.0
8 260 60 23 0 0 0
FIG. 4. Cutting procedure used for preparing a specimen from an injec-
tion-compression molded disk, to measure average transverse birefrin-
gence < nss � nhh > (a), and birefringence Dn (b).
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2013 1791
triangular elements and linear shape functions is used.
The boundary conditions in the injection, compression
and packing stages are different. In the injection stage,
the volume flow rates at the entrance nodes were speci-
fied, and the pressures at the melt front nodes were
assumed to be zero with the pressure at the entrance
nodes and flow rates at the melt front nodes to be solved.
In the packing stage, the entrance pressure was speci-
fied as an imposed packing pressure, with flow rates at
the entrance nodes to be determined. Besides, in the
impermeable boundary region, the melt is in contact with
the boundary of the mold, and the normal velocity com-
ponents vanish. In addition, symmetric boundary condi-
tions at the centerline and no slip at the solid wall of the
cavity were assumed. The additional boundary conditions
for the compression stage in ICM were specified [57]. In
ICM, the temperature at the entrance nodes is assumed to
be uniform and equal to the inlet melt temperature, T0.To solve the pressure equations, a quarter of the disk
cavity is discretized by a series of three-node triangular ele-
ments in the x-y plane. Only one control volume is associ-
ated with each node. For each node of a triangular element,
by connecting the centroid of each element to the midpoints
of the three corresponding sides, the region enclosed by a
contour in the counter-clockwise direction around each ver-
tex node of a triangular element is specified as the subcon-
trol volume for this node. The polygonal control volume
that surrounds each vertex node is defined by the summa-
tion of sub-control volumes, which contains node N [54].
Pressure Development. After introducing linear inter-
polation functions as well as a FD representation for the
time derivative and applying the Galerkin weighted-resid-
ual procedure [59–61] and mass conservation using a con-
trol-volume approach [62], and the governing equation for
pressure [57] in the whole cavity domain is obtained.
Elastic Strain Tensor. To calculate the flow-induced
stresses during the filling and packing stages, the elastic
strain tensor, Cij;k, for all relaxation modes of the Leonov
model has to be calculated at each time step. Therefore,
the governing equations for the elastic strain tensor along
the streamwise coordinate are discretized using a FD
approach. The time derivatives are discretized using for-
ward difference and space derivatives were discretized
using backward difference [63].
To determine the components of Cij;k tensor, the Glob-
ally Convergent Method for Nonlinear Systems of Equa-
tions [51] that is closely related to the quasi-Newton method
of minimization was implemented for the discretized sys-
tem of governing equations for the elastic strain tensor. This
method is powerful but the numerical computation of the Ja-
cobian matrix represents a disadvantage [51]. However, for
this case the Jacobian matrix is available analytically. In this
work, the subroutine ‘‘fdjac’’ which calculates the Jacobian
matrix numerically, was replaced by the function that pro-
vides the Jacobian matrix calculated analytically.
Temperature Distribution. For the solution of the energy
equation, the implicit FD method is used for the conduction
and time derivative terms. To calculate the convective term
in the energy equation during the filling and compression
stages, the temperature distribution in the flow direction, is
linearly interpolated within each element. The heat convec-
tive terms at a node were evaluated by taking the area
average of the values calculated at the center of the upstream
elements of the node under consideration [55, 56, 64].
Numerical Algorithm and Convergence
At each new time step, the velocity field and pressure field
are first solved with the elastic strain tensor. During the solu-
tion process, the temperature obtained in the time step is used
to calculate the various physical quantities. After obtaining
the velocity and pressure fields, the energy equation, with the
fixed pressure and velocity fields, is solved to obtain the tem-
perature field, and then the next time step is ensured.
The under-relaxation iteration method [55] was used to
solve the pressure and temperature at each time step. Dur-
ing iteration, new values of the pressure and temperature
are obtained. When the solution converges, the old and
updated values are almost same. Iterations terminate when
the absolute change in the each property is less than a
specified value. In particular, the successive under-relaxa-
tion method is also used for calculation of the pressure
and temperature profile due to numerical stability.
Residual Stresses and Birefringence in ICM Parts
Flow Stresses and Birefringence. In the cooling stage,
the shear rate, velocity and pressure are taken to be zero.
Accordingly, the convection, dissipation, and pressure
terms in the energy equation are omitted. The shear
stresses and normal stress differences are calculated
according to the Leonov constitutive equation [42]. The
residual flow birefringence for amorphous polymers can
be calculated by the stress-optical rule during the noniso-
thermal flow and the subsequent relaxation. The flow
birefringence in s� z plane, Dnfl, is given as
Dnfl ¼ Cs Tð Þ � Ds s; z; tð Þ (2)
where,
Ds s; z; tð Þ ¼ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiN21 s; z; tð Þ þ 4t2sz s; z; tð Þ
q(3)
and Cr is the temperature dependent stress-optical coeffi-
cient of polymer in the melt state [43].
Similarly, the birefringence in the s� h plane is given by
nflss � nflyy ¼ CsðTÞ � ðsss � syyÞ (4)
where the superscript fl indicates flow-induced birefrin-
gence components, Dn and nss � nhh are the birefringence
1792 POLYMER ENGINEERING AND SCIENCE—-2013 DOI 10.1002/pen
component in the planes s� z and s� h, respectively.
rii(i ¼ s; h) are the normal stresses in the s and h direc-
tions, respectively, and ssz is the shear stress in the s� zplane.
Thermal Stresses and Birefringence. The residual ther-
mal stresses and birefringence in ICM disks are treated
as those for freely quenched polymer plates and are
calculated based on the linear viscoelasticity and
photoviscoelasticity with the volume relaxation effects
included [45, 65]. As a first approximation, we treated the
residual thermal stresses and birefringence in ICM parts
as those developed in freely quenched plates [45]. Based
on the varying temperature fields, the changes in visco-
elastic properties are determined and utilized to calculate
the thermal stresses until the polymer reaches thermal
equilibrium with the molding system. For this case, the
thermal stress tensor is
sth ¼sthss 0 0
0 sthyy 0
0 0 0
24
35 (5)
where rthss ¼ rthhh.The refraction index tensor due cooling alone is:
nth ¼nthss 0 0
0 nthyy 0
0 0 nthzz
24
35 (6)
Total Stresses and Birefringence. To the best of our
knowledge, no single nonlinear constitutive equation is
available to describe the rheological behavior of a poly-
mer in the glassy and melt states and in the transition
region between them. Moreover, in the injection, com-
pression and cooling stages, the dominant terms in the
dynamic equations are different. Therefore, a further sim-
plifying assumption was made that the coupling effects
between the flow and thermal stresses are negligible, such
that they can be evaluated independently. The constitutive
equation used to calculate the flow and thermal stresses
are different, as mentioned earlier. Thus, the total residual
stresses are:
sres
¼ sflres
þ sthres
(7)
Similarly, the total refraction index tensor is,
n ¼ n0dþ nth þ nflnth ¼n0 þ nrrthþnflrr
0 nflrz
0 n0 þ nthyy þ nflyy 0
nflrz 0 n0 þ nthzz þ nflzz
264
375 ð8Þ
where subscripts res and superscripts fl and th stand for
residual, flow, and thermal, respectively.
The birefringence measured in the rz plane is then
Dn ¼ Dnrz ¼ Dnflrz� �2þ Dnthrz
� �2þ2 nflrr � nflzz� �
Dnthrz� �h i1=2
(9)
with the flow birefringence, Dnflrz, and the thermal bire-
fringence, Dnthrz, being
Dnfl ¼ Dnflrz ¼ Cfls sflrr � sflzz� �2þ4 sflrz
� �2h i1=2(10)
Dnthrz ¼ nthrr � nthzz (11)
In free quenching nthrr ¼ nthhh, the birefringence in the rhplane becomes
Dnry ¼ nthrr � nthyy� �
þ nflrr � nflyy� �
¼ nflrr � nflyy (12)
RESULTS AND DISCUSSION
Pressure Profile
The experimental (symbols) and simulated (solid line)
pressure traces and a ram displacement for the ICM PS
run 1 in Table 4 are given in Fig. 5. The measured pres-
sure trace was obtained directly from the pressure trans-
ducer located under the sprue at the center of cavity, as
shown in Fig. 2. The simulated pressure trace during the
filling, compression and at the beginning of the packing
stage is in a good agreement with the experimental data.
It can be seen that the pressure increases monotonically
during the filling stage. Also, it is noted that the pressure
drops during the switchover time of 1.1 s from the filling
to compression stage. During this time the plunger does
not move and stress relaxation occurs. Accordingly, this
FIG. 5. Measured (symbols) and simulated (solid line) pressure at the
center of the disk and displacement of plunger (dashed line) as a func-
tion of time for run 1 of PS: melt temperature ¼ 2308C, mold tempera-
ture ¼ 408C, volume flow rate ¼ 13 cm3/s, compression stroke ¼ 0.15
cm, compression speed ¼ 0.4 cm/s and switchover time ¼ 1.1 s.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2013 1793
was the only mechanism governing the behavior of the
pressure history during the switchover time. When the
compression stage starts, the pressure sharply increases
followed by the overshoot at the beginning of the packing
stage and then the packing pressure is maintained. The
measured pressure trace is taken as the pressure for the
packing simulation. As seen from Fig. 5, the time at the
end of injection stage was 2.874 s and the switchover
time is 1.1 s. The compression stage ends at time of
4.254 s and then the packing stage starts. In the cooling
stage which starts right after end of the packing stage, the
pressure decreases due to the release of the packing pres-
sure and further cooling.
Velocity and Shear Rate Profiles
Figure 6 shows the predicted gapwise velocity (a, b)
and shear rate (c, d) profiles at the end of the injection (a,
c) and compression (b, d) stages of ICM PS disk in run 2.
As expected, during the injection stage the velocity
decreases with radial position and the melt flow dimin-
ishes in the wall layer around z=h ¼ 0.8 due to cooling
from the mold wall, as seen from Fig. 6a. In contrast to
the injection stage, the velocity at the end of the compres-
sion stage during ICM increases with the radius, as shown
in Fig. 6b. Similar velocity profiles are also obtained by
Kim et al. [26], Chen et al. [31], and Lee and Isayev
[57]. The velocity behavior can be explained by consider-
ing the mass balance. Since the volumetric flow rate of
the melt through the surface increases with the radius, the
velocity through the section at a position far from the
inlet is greater than that near the inlet. The 150% reduc-
tion of the centerline velocity between r¼ 2.948 cm and
r¼ 4.46 cm occurs at the end of the injection stage (Fig.
6a), whereas the only 45% increase occurs at the end of
the compression stage (Fig. 6b). This is an indication that
the squeezing flow during the compression stage causes
the pressure distribution in the mold cavity to become
more uniform, resulting in a reduction of the velocity var-
iation with radial position.
Figure 6c and d show the predicted gapwise shear rate
profiles at the end of the injection and compression stage,
respectively. Similar to the velocity behavior, the shear rate
at the end of the injection stage decreases with increasing
radial positions from the gate. However, the shear rate at
the end of compression stage increases with the radius.
Birefringence in PS
In this section the influence of the processing conditions
on the simulated and measured birefringence, Dn, and aver-
age transverse birefringence, < nss � nhh >, for ICM PS
disks is presented. The total birefringence is comprised of
both flow- and thermally-induced birefringence. The simu-
lated results are compared with measurements.
FIG. 6. Predicted gapwise distribution of velocity vs(a, b) and shear rate (c, d) at various radial positions for
run 2 of PS at the end of injection (a, c) (t ¼ 2.64 s) and compression stages (b, d) (t ¼ 4.16 s) during ICM.
1794 POLYMER ENGINEERING AND SCIENCE—-2013 DOI 10.1002/pen
Simulation of Transient Birefringence. The flow-
induced birefringence is determined by the thermome-
chanical history that the polymer experiences during the
polymer processing [18]. The build-up and relaxation of
the shear and normal stresses taking place during molding
process lead to a transient birefringence history. Figure 7
shows the evolution of the predicted gapwise flow-
induced birefringence, Dnfl, distribution at various radial
positions at the end of the injection stage corresponding
to t ¼ 2.64 s (a) and during the compression stage at t ¼3.8 s (b), and t ¼ 4.11 s (c) and at the end of the com-
pression stage corresponding to t ¼ 4.16 s (d) for the
ICM PS disk in run 2. The maximum birefringence at the
end of the injection stage occurred at about z=b ¼ 0.7–0.8
due to the dominant effect of the first normal stress differ-
ence during the injection stage. The maximum decreases
in the magnitude with the radial position. During the
switchover time, the stresses relaxation occurs due to the
absence of flow, but it is retarded due to cooling. After
the switchover time, the predicted transient gapwise bire-
fringence distribution during the compression stage
increases with time (Fig. 7b and c). The birefringence
maximum also increases. However, in contrast to the
results obtained during the injection stage, the birefrin-
gence behavior during the compression stage is different.
The simulated transient birefringence, Dn, at the end of
the injection stage and after the switchover time, changes
significantly. In particular, the magnitude of Dn signifi-
cantly decreases at the radius over r ¼ 4.46 cm. This is
due to the fact that after the switchover time the tempera-
ture is decreased along the gapwise direction at the loca-
tion close to the melt front. The latter causes an increase
in the shear and normal stresses during the compression
stage due to the increase of viscosity and relaxation time
of the polymer melt upon cooling. The minimum and
maximum of the birefringence appear near the wall
region. This is caused by the change of the shear rate due
to narrowing of the flow channel by the solidification
leading to freezing of the chain orientation in the filling
and compression stages and a slow relaxation in the cool-
ing stage. At the end of the compression stage (Fig. 7d),
a maximum and minimum of the birefringence can be
seen with their magnitude determined by the shear and
normal stresses present at the time of melt solidification.
Figure 8 shows the predicted gapwise distribution of
the flow birefringence at the various radial positions at
the end of the packing (a) and cooling (b) stages for ICM
PS disk in run 2. It should be noted that, due to the me-
chanical limitation of the ICM machine used in the pres-
ent study, it was difficult to precisely control the high
packing pressure required to compensate the melt shrink-
age during cooling. Therefore, the packing stage in this
FIG. 7. Predicted transient flow-induced birefringence (Dnfl) distributions in the gapwise direction at various
radial positions at the end of the injection stage at t ¼ 2.64 s (a), during the compression stage at t ¼ 3.8 s
(b) and t ¼ 4.11 s (c) and at the end of the compression stage t ¼ 4.16 s (d) for the ICM PS run 2.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2013 1795
study does not play a major role in development of the
flow-induced birefringence. It is seen from Fig. 8 that the
birefringence near the wall does not change and becomes
frozen during the packing stage since the temperature near
the mold wall is below the glass transition temperature,
Tg. However, outside this region the temperature is still
high and the stress and, therefore, birefringence relaxation
is significant. This figure shows that the predicted flow
birefringence in the core is very low due to the fast relax-
ation of chain orientation immediately after completion of
the compression stage. At the end of the cooling stage
(Fig. 8b), the temperature in an extensive wall region is
below Tg, therefore, the distribution of the birefringence
is similar to that at the end of the packing stage (Fig. 8a).
Since the shear and normal stresses cannot relax anymore
below Tg, the residual flow stresses are frozen during the
cooling stage. However, the residual flow birefringence in
the core is zero, due the complete relaxation of the chain
orientation upon completion of the packing stage, since
the temperature is still high in this region. A shoulder in
the birefringence profile that appears during the packing
stage is absent after cooling due to the stress relaxation in
this region.
The Effect of Mold Temperature. The predicted and
measured residual gapwise distribution of the flow bire-
fringence Dnfl at various radial positions for ICM PS
disks in runs 1 and 3 are shown in Fig. 9 at mold temper-
atures of 408C (a) and 808C (b) and a melt temperature of
2308C. As the mold temperature increases the overall
flow-induced birefringence and the thickness of solidified
layer decreases due to a slower rate of cooling leading to
faster stress relaxation at the higher mold temperature.
The predicted and measured birefringence is seen to
decrease with increasing the radial location due to a lower
shear rate during the injection stage, as shown in Fig. 6c.
The development of the gapwise distribution of the bire-
fringence is determined by the combination of effects of
the shear rate variation and the temperature history. The
former is caused by the flow during the filling and com-
pression stages followed by the packing stage. The tem-
perature history of the melt is affected by the switchover
time. During the injection stage, the velocity and shear
rate decrease near the mold wall because of cooling lead-
ing to the solidification. In addition, during the switchover
time, the further cooling takes place, but without the melt
flow, causing the stress relaxation. During the compres-
sion stage, the gapwise shear rate distribution shows a
peak just outside the solidified region. As a result, at the
FIG. 8. Predicted transient flow-induced birefringence (Dnfl) distribu-
tions in the gapwise direction at various radial positions at the end of the
packing (a) and cooling (b) stages for the ICM PS run 2.
FIG. 9. Measured (symbols) and predicted (lines) residual flow-induced
birefringence Dnfl distribution in the gapwise direction at various radial
positions at the end of the cooling stage for the ICM disks obtained in
runs 1 and 3 corresponding to mold temperature of 408C (a) and 808C(b). The contribution of the thermal birefringence was not included in
the predicted birefringence.
1796 POLYMER ENGINEERING AND SCIENCE—-2013 DOI 10.1002/pen
end of the compression stage, a maximum and a mini-
mum in the birefringence profile is developed due to the
shear and normal stresses. It seems that the packing stage
does not significantly affect the flow-induced birefrin-
gence because the packing pressure used is low and not
sufficient to compensate the shrinkage.
In contrast to the measured birefringence showing a
nonzero value in the core, the predicted residual birefrin-
gence in the core is zero (Fig. 9). As will be shown
later, the thermally-induced birefringence dominates in
the core region. The linear viscoelasticity and photovis-
coelasticity with the volume relaxation effects are used
to calculate the residual thermal stresses and birefrin-
gence [45]. In calculating the thermal birefringence, the
relaxation modulus and strain-optical coefficient func-
tions reported earlier [65] are used. As the first approxi-
mation, it is assumed that the residual thermal stresses
and birefringence in CIM and ICM disks developed sim-
ilarly as in freely quenched slabs. The predicted residual
thermal birefringence distributions along the gapwise
direction of PS slabs quenched from an initial tempera-
ture of 2308C to different quenching temperatures are
shown in Fig. 10. An increase in the quenching tempera-
ture leads to a decrease in the thermally-induced bire-
fringence. As seen from comparison of Figs. 9 and 10
the thermally-induced birefringence, Dnth, near the wall
is significantly lower than the flow-induced birefrin-
gence, Dnfl. Also, in this region, the flow-induced bire-
fringence in ICM PS disks is negative, while the ther-
mally-induced birefringence is positive. However, in the
core of ICM disks the magnitude of the flow-induced
birefringence is zero since the flow-induced birefringence
completely relaxed. The total residual birefringence was
obtained by summation of the calculated residual ther-
mally induced and flow-induced birefringence. Figure 11
shows the measured and simulated total birefringence,
Dn in the ICM PS disks in runs 1 and 3 at various ra-
dial positions. It is seen that when the thermally-induced
birefringence is added to the flow-induced birefringence,
the simulated total birefringence provided a better
description of the measured birefringence in ICM PS
disks. Simulations show that the total birefringence near
the wall is mainly caused by the flow, since the ther-
mally-induced birefringence at this location is low. How-
ever, the birefringence in the core is caused by thermal
stresses developed during rapid cooling. Both the pre-
dicted and measured birefringence shows slightly con-
cave shape in the core with a maximum near the mold
surface and a maximum at a location of about z=b =
0.70–0.75. The location of the birefringence maximum
at a mold temperature of 808C is shifted toward the sur-
face, because of the smaller thickness of the solidified
layer developed at the higher mold temperature.
Some differences in the simulated and measured bire-
fringence are evident in the region between the location
of a maximum of Dn and the core. Generally, the simu-
lated results underestimate the measured gapwise birefrin-
gence because in simulations of the present study, the
flow in the delivery system is neglected. It is known that
the contraction and expansion flow provides an additional
contribution to the birefringence [1].
FIG. 10. Predicted residual thermal birefringence Dnth of PS plates
freely quenched from a melt temperature of 2308C to different quench-
ing temperatures of Ti.
FIG. 11. Measured (symbols) and predicted (lines) total residual bire-
fringence Dn distribution in the gapwise direction at various radial posi-
tions at the end of the cooling stage for the ICM disks obtained in run 1
and 3 corresponding to a mold temperature 408C (a) and 808C (b). The
contribution of thermal birefringence is included in the predicted bire-
fringence.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2013 1797
The Effect of Melt Temperature. Figure 12 shows the
predicted and measured gapwise distribution of the flow
birefringence Dnfl at various radial positions at the end of
cooling stage for ICM PS disks in runs 4 and 5 corre-
sponding to melt temperatures of 1908C (a) and 2108C(b) at a mold temperature 608C. It is seen that the distri-
bution of birefringence is very sensitive to the melt tem-
perature. Higher peak values of the birefringence are
obtained at a lower melt temperature. The outer peak is
due to the flow during the injection and compression
stages leading to the frozen-in orientation near the surface
and the subsequent relaxation of the molecular orientation
in the intermediate region. This flow-induced birefrin-
gence peak near the wall reduces in value at the higher
melt temperature. This is because a faster stress relaxation
at the higher temperature lowers shear and normal stresses
developed during flow at the given volumetric flow rate
during the filling and compression stages. Accordingly,
the simulation shows that the maxima of the flow-induced
birefringence Dnfl at the wall and near the wall signifi-
cantly decrease when the melt temperature is increased.
The predicted flow-induced birefringence Dnfl in the core
is zero due to the fast relaxation of the chain orientation
right after filling, since the temperature is still high in this
region. However, the measured birefringence is nonzero
in the core region due to the presence of the thermally-
induced birefringence. Thus, to obtain a better prediction,
the total residual birefringence was calculated by summa-
tion of the calculated residual thermal and flow birefrin-
gence, as mentioned earlier. These results are given in
Fig. 13a and b. Compared with a melt temperature of
1908C, the birefringence in the core does not change sig-
nificantly as the melt temperature is increased to 2108C.This is due to the fact that these melt temperatures are
much higher than Tg of PS such that the effect of the melt
temperature on the thermal birefringence becomes insig-
nificant [45, 66]. It is clearly seen from Fig. 13 that the
calculated total birefringence is in a better agreement with
the measured one.
The average transverse birefringence < nss � nhh > is
directly obtained by measuring the retardation of the nor-
mal incident laser beam. The predicted average transverse
birefringence was calculated by the integration of the
in-plane birefringence over the thickness of the disk. The
average transverse birefringence as a function of radial
location for melt temperatures of 1908C, 2108C, and
2308C at a mold temperature of 608C corresponding to
FIG. 12. Measured (symbols) and predicted (lines) residual flow-
induced birefringence Dnfl distribution in the gapwise direction at various
radial positions at the end of the cooling stage for the ICM PS disks
obtained in runs 4 and 5 corresponding to a melt temperature of 1908C(a) and 2108C (b). The contribution of thermal birefringence is not
included in the predicted birefringence.
FIG. 13. Measured (symbols) and predicted (lines) total residual bire-
fringence Dn distribution in the gapwise direction at various radial posi-
tions at the end of the cooling stage for the ICM PS disks obtained in
runs 4 and 5 corresponding to melt temperatures of 1908C (a) and 2108C(b). The contribution of thermal birefringence is included in the pre-
dicted birefringence.
1798 POLYMER ENGINEERING AND SCIENCE—-2013 DOI 10.1002/pen
ICM PS disks in runs 4, 2, and 5 is shown in Fig. 14. As
the mold temperature increases from 1908C to 2308C, avalue of < nss � nhh > decreases significantly due to a
faster stress relaxation at higher melt temperatures. In
agreement with experimental data reported earlier [15,
67], the birefringence < nss � nhh > decreases in the ra-
dial direction However, the theoretical and experimental
data on < nss � nhh > of the present study are in contrast
with experimental data reported by Chen et al. [31] indi-
cating the presence of the birefringence minimum at some
radial location. Finally, it should be noted that the simu-
lated and experimental results on < nss � nhh > at all ra-
dial locations at various melt temperatures are in a fair
agreement.
The Effect of Compression Stroke. In comparison with
CIM, the ICM introduces new processing parameters
including the compression stroke and speed and switch-
over time. Therefore, it is of great importance to deter-
mine the effect of the compression stage on the total bire-
fringence in disks. During the injection stage, the melt is
injected into a partially open cavity with a thickness being
greater than the final thickness from 1.0 mm to 2.0 mm.
Figure 15 shows the predicted total and measured gapwise
birefringence, Dn, distribution at various radial positions
at the end of cooling stage in ICM PS disks in runs 6 and
7 corresponding to compression strokes of 1 mm (a) and
2 mm (b). As the compression stroke increases from 1
mm to 2 mm, the birefringence decreases and shows a
lower maximum. At the higher compression stroke the
melt experiences a less resistance during the compression
flow leading to a lower pressure and therefore, lower
stresses, and birefringence.
The Effect of Switchover Time. The switchover from
the injection to compression stage is not instantaneous
leading to a time lag defined as the switchover time. To
identify the effect of the switchover time in ICM, calcula-
tions of the birefringence are carried out at zero and non-
zero switchover times. Figure 16 shows the simulated
gapwise residual flow-induced birefringence, Dn, distribu-tion at various radial positions at the end of cooling stage
in ICM PS disks in run 2, but at zero switchover time.
Results of the simulated birefringence at a switchover
FIG. 14. Measured (filled symbols) and predicted (open symbols) aver-
age transverse birefringence, –< nss � nhh > as a function of the radial
position for ICM PS disks in runs 2, 6, and 7.
FIG. 15. Measured (symbols) and predicted (lines) total residual bire-
fringence Dn distribution in the gapwise direction at various radial posi-
tions at the end of the cooling stage for the ICM PS disks obtained in
runs 6 and 7 corresponding to a compression stroke of 1 mm (a) and 2
mm (b). The contribution of thermal birefringence is included in the pre-
dicted birefringence.
FIG. 16. Predicted residual flow-induced birefringence, Dnfl, distribu-
tion in the gapwise direction at various radial positions at the end of the
cooling stage for the ICM PS disks in run 2 without switchover time.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2013 1799
time of 1.1 s in ICM PS disk in run 2 are shown earlier
in Fig. 8b. In the presence of the switchover time, there
are two competing effects. One is the stress relaxation
during switchover time when cooling takes place in the
absence of flow. The other is the development of higher
stresses due to flow of colder and therefore, more viscous
melt in the compression stage. Obviously, the dominating
effect is determined by the duration of the switchover
time. At a shorter switchover time a less time is available
for the stress relaxation and cooling. At a longer switch-
over time the cooling may be significant and therefore,
the second effect becomes more important in determining
the final birefringence distribution. The simulated birefrin-
gence with and without the switchover time suggests that
the switchover time is a relatively important parameter
affecting the birefringence. The simulated results in Fig.
16 show a minimum and a maximum of the birefringence
at the switchover time of 0 s with their magnitudes deter-
mined by the stress evolution when the melt solidifies at
a gapwise position. However, when the switchover time is
employed, the maximum of the birefringence increases. In
addition, the gapwise position corresponding to this maxi-
mum of Dn is shifted further away from the surface, as
seen from comparison of data depicted in Figs. 8b
and 16.
Comparison between CIM and ICM. It is of great im-
portance to find the effect of the compression stage on
the birefringence in the molded parts. For this purpose,
simulations are carried out without imposing the packing
pressure for CIM and for ICM with the zero switchover
time. Figure 17 shows the simulated gapwise flow-
induced birefringence, Dnfl, distribution along the radial
direction for ICM (a) and CIM (b) PS disks at the end of
the cooling stage. It is seen that the birefringence in the
ICM disk is dramatically decreased in comparison with
that of the CIM one, especially near the mold surface.
From these results, it is clear that the ICM certainly
reduces the flow-induced birefringence level most notably
near the wall region. It is expected that a more drastic
decrease of the birefringence can be obtained if the injec-
tion stage is applied at a wider cavity opening such that
the compression stage becomes more dominant over the
injection stage. Therefore, the simulation shows that the
ICM is indeed more suitable process for manufacturing of
precision products of good optical quality than the CIM.
It is also interesting to find the difference in the average
transverse birefringence in the ICM and CIM moldings.
The predicted and measured average transverse birefrin-
gence, < nss � nhh >, as a function of the radial direction
is compared in Fig. 18 for both CIM and ICM disks at the
end of the cooling. This birefringence decreases with the
radial direction as earlier reported [15, 67]. It can be seen
that the average transverse birefringence along the radial
direction decreases with distance from the gate. The aver-
age transverse birefringence in the CIM disk is approxi-
mately twice larger than that in the ICM one. Regardless,
the overall predicted values of < nss � nhh > are in a quali-
tative agreement with the experimental results.
Birefringence in PC Disks
The following sections present the influence of the
processing conditions on the simulated total residual bire-
FIG. 17. Predicted residual flow-induced birefringence, Dnfl, distribu-
tion in the gapwise direction at various radial positions at the end of the
cooling stage in ICM (a) and CIM (b) PS disks for run 2 without switch-
over time and packing stage.
FIG. 18. Measured (filled symbols) and predicted (open symbols) aver-
age transverse birefringence as a function of the radial position of PS
disks for run 5 (ICM) and run 8 (CIM).
1800 POLYMER ENGINEERING AND SCIENCE—-2013 DOI 10.1002/pen
fringence, Dn, and the average transverse birefringence,
< nss � nhh >, in PC ICM disks. The total birefringence
is comprised of both flow- and thermally-induced birefrin-
gence. The simulated and measured results are compared
and the similarities and differences in the birefringence of
ICM PS and PC disks are discussed.
Numerical Simulation of Transient Birefringence. Fig-
ure 19 shows the predicted gapwise flow birefringence,
Dnfl, distribution at the end of the compression (a), packing
(b), and cooling (c) stages at various radial positions for
ICM PC disk in run 2. Similar to the PS disk, in the PC
disk at the end of the compression stage, a maximum and a
minimum of the birefringence near the wall is observed.
These are caused by the shift of the shear rate maximum
toward the core due to solidification. It is noted from Fig.
19a that at a radius of above r ¼ 4.46 cm, the magnitude of
Dn decreased tremendously. It is due to the fact that, after
the switchover time, the melt is cooled along the gapwise
direction away from the melt front leading to an increase
of the shear and normal stresses during the compression
stage. At the same time after the switchover time, since the
temperature along the gapwise direction in the region close
to the melt front is still high, a decrease of the stresses
takes place during the compression stage in that region.
The predicted gapwise distribution of the flow birefrin-
gence at the various radial positions at the end of the
packing stage is presented in Fig. 19b. As noted earlier,
in the present study the packing stage does not play a
major role in the development of the flow-induced bire-
fringence because the packing pressure is too low to com-
pensate the shrinkage of the melt caused by cooling. It
may be noted that the birefringence near the wall does
not change and frozen during the packing stage since the
temperature near the wall is below Tg. However, in the
core, the stress relaxation is significant since the tempera-
ture is still high and the birefringence is completely
FIG. 19. Predicted flow-induced birefringence (Dnfl) distributions in the
gapwise direction at various radial positions at the end of the compres-
sion (a), packing (b), and cooling (c) stages for the ICM PC disks for
run 2.
FIG. 20. Measured (symbols) and predicted (lines) residual flow-
induced birefringence Dnfl distribution in the gapwise direction at various
radial positions at the end of the cooling stage for the ICM PC disks in
runs 1 and 2 corresponding to mold temperatures of 408C (a) and 608C(b). The contribution of the thermal birefringence is not included in the
predicted birefringence.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2013 1801
relaxed. During the cooling stage, as shown in Fig. 19c,
the birefringence in the core relaxed completely before
the melt temperature reaches Tg in that region. Away
from the core the birefringence remains almost the same
as that at the end of the packing stage because the
stresses do not relax anymore and become residual since
the melt temperature is already below Tg.
The Effect of Mold Temperature. Figure 20 shows the
measured and predicted gapwise birefringence at the end of
cooling stage at various radial locations at mold tempera-
tures of 408C (a) and 608C (b) and a melt temperature of
2608C for ICM PC disks in runs 1 and 2. It is seen from this
figure that an increase in the mold temperature from 408C to
608C leads to a decrease in the magnitude of the flow bire-
fringence along the gapwise direction. The difference of the
predicted flow birefringence between the mold temperatures
of 408C and 608C becomes significant near the wall.
Comparison of the measured and predicted flow-
induced birefringence distribution shown in Fig. 20 indi-
cates that the measured birefringence significantly differ-
ent in the skin and core regions of ICM PC disk. These
differences are evidently due to neglect the thermally-
induced stress and birefringence. In particular, the tensile
stresses in the core and the compressive stresses in the
skin, evidently contribute significantly to the birefrin-
gence. In order to prove this the residual thermal stresses
and birefringence are calculated based on the linear vis-
coelasticity and photoviscoelasticity with volume relaxa-
tion and free quenching assumption [45, 66]. In calculat-
ing the thermal birefringence relaxation modulus and
strain-optical coefficient functions, reported in Ref. 65,
are used. The predicted thermal birefringence distributions
along the gapwise direction of PC slabs freely quenched
from an initial temperature of 2608C to different quench-
ing temperatures are shown in Fig. 21. It is seen that an
increase of the cooling temperature reduces the thermal
birefringence. In the case of ICM PC disks, the simulated
results in Fig. 21 show that the thermal birefringence,
Dnth, near the wall is lower than the flow birefringence,
Dnfl, shown in Fig. 20. In this region, the flow birefrin-
gence is positive, while the thermal birefringence is nega-
tive. However, in the core, the magnitude of the flow
birefringence is negligible (Fig. 20). In this case the ther-
mal birefringence is positive and much higher than that in
the quenched PS slabs. When the simulated thermal and
flow birefringence is added, the measured and simulated
total birefringence is in much better agreement, as indi-
cated in Fig. 22. It is clear that the contribution of the
thermal birefringence to the total birefringence in ICM
PC disks is higher than that in ICM PS disks. The pre-
dicted and measured birefringence is seen to have a con-
cave shape in the core. The predicted birefringence maxi-
mum appears near the surface at a location of about z=b¼ 0.75–0.90 with its value being slightly higher at a
lower mold temperature. The location of this maximum at
a higher mold temperature is shifted toward the surface.
Some differences between the measured and predicted
birefringence are evident in the region between the loca-
tion of maximum of Dn and the core as seen from Fig.
22. The latter is evidently due to neglect in the present
simulation of the contribution of contraction and expan-
sion flow in a delivery system [1].
FIG. 21. Predicted residual thermal birefringence Dnth of PC plates
quenched from 2608C to different quenching temperatures Ti.
FIG. 22. Measured (symbols) and predicted (lines) total residual
birefringence Dn distribution in the gapwise direction at various radial
positions at the end of the cooling stage for the ICM PC disks in runs 1
and 2 corresponding to mold temperature of 408C (a) and 608C (b). The
contribution of thermal birefringence is included in the predicted
birefringence.
1802 POLYMER ENGINEERING AND SCIENCE—-2013 DOI 10.1002/pen
The predicted average transverse birefringence,
< nss � nhh >, is calculated by the integration of the in-
plane birefringence over the thickness of the PC disk. The
average transverse birefringence as a function of radial
location at mold temperatures of 408C, 608C, and 808Cand a melt temperature of 2608C in ICM PC disks corre-
sponding to runs 1, 2, and 3 is shown in Fig. 23. Again,
as in the case of ICM PS disks, as the mold temperature
increases from 408C to 808C, the average transverse bire-
fringence decreases due to a faster stress relaxation at the
higher mold temperature. As in the case of PS disks, the
birefringence in PC disks also decreases in the radial
direction [15, 67]. The simulated results are in a qualita-
tive agreement with the experimental data. However, sim-
ilar to ICM PS disks, the simulated and experimental bire-
fringence < nss � nhh > in ICM PC disks of the present
study are in contrast with experimental data reported by
Chen et al. [31] indicating a minimum birefringence at
some radial location.
The Effect of Melt Temperature. The measured and
predicted gapwise birefringence distribution at various radial
positions at the end of cooling stage in PC ICM disks in runs
4, 2, and 5 are shown in Figs. 24a, 20b and 24b, correspond-
ing to a melt temperature of 2408C, 2608C, and 2808C,respectively. It is seen that the distribution of birefringence
is very sensitive to the melt temperature. Both the simulated
and experimental results indicate that the maximum of the
birefringence is significantly higher at a lower melt tempera-
ture due to a slower stress relaxation after the injection and
compression stages. The measured birefringence in the core
is little affected by the melt temperature since it is due to
the thermal birefringence, as shown below. The contribution
of the thermal birefringence in ICM PC disks is relatively
high in comparison with little contribution in ICM PS disks,
as discussed earlier.
By adding the simulated thermal and flow birefrin-
gence, the better prediction of the measured residual bire-
fringence profiles at various radial positions is obtained.
These results are shown in Figs. 25a, 22b, and 25b for
melt temperatures of 2408C, 2608C, and 2808C, respec-
tively. It can be seen that increasing the melt temperature
leads to a decrease of the birefringence. It should be
noted that compared with the effect of the mold tempera-
ture the change of the melt temperature has a larger effect
on the values of the residual birefringence.
In general, the simulation tends to underestimate the
gapwise distribution of measured residual birefringence.
In particular, it is found that some differences between
experimental and predicted birefringence are evident in
the region between the location of maximum of Dn and
the core. Regardless, the predicted overall total values of
Dn are in a qualitative agreement with experimental
results.
The average transverse birefringence, < nrr � nhh >, as
a function of radius at melt temperatures of 2408C,2608C, and 2808C and a mold temperature of 608C in
ICM PC disks in runs 4, 2, and 5 is shown in Fig. 26. As
the melt temperature increases from 2408C to 2808C, thebirefringence < nrr � nhh > decreases significantly due to
FIG. 23. Measured (filled symbols) and predicted (open symbols) aver-
age transverse birefringence < nss � nhh > as a function of the radial
position for ICM PC disks in runs 1, 2, and 3 corresponding to mold
temperatures of 408C, 608C, and 808C.
FIG. 24. Measured (symbols) and predicted (lines) residual flow-
induced birefringence Dnfl distribution in the gapwise direction at various
radial positions at the end of the cooling stage for the ICM PC disks in
runs 4 and 5 corresponding to melt temperatures of 2408C (a) and 2808C(b). The contribution of thermal birefringence is not included in the pre-
dicted birefringence.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2013 1803
a more stress relaxation at the higher melt temperature.
This birefringence also decreases in the radial direction
[15, 67]. The behavior of the predicted and measured
birefringence < nss � nhh > of the present study is in con-
trast with experimental data reported by Chen et al. [31]
indicating a minimum birefringence at some radial dis-
tance. Generally, the simulated and experimental results
on the average transverse birefringence at various melt
temperatures are in good agreement. However, some devi-
ation between them is seen at radial positions close to the
gate. It is attributed to the neglect of a contribution to the
birefringence due to flow in a delivery system consisting
of contraction and expansion region [1].
The Effect of Compression Stroke. Figure 27a and b
shows the predicted and measured gapwise distributions
of the total birefringence, Dn, at a mold temperature 608Cat various radial positions at the end of cooling stage for
ICM PC disks in runs 6 and 7 corresponding to at com-
pression strokes of 1 mm and 2 mm, respectively. As a
compression stroke increases the birefringence decreases
because the resistance of melt to flow under large com-
pression stroke is less resulting in a low pressure and
stresses. In particular, the compression stroke of 1 mm
showed a higher maximum of the birefringence than that
of 2 mm.
FIG. 25. Measured (symbols) and predicted (lines) total residual bire-
fringence Dn distribution in the gapwise direction at various radial posi-
tions at the end of the cooling stage for the ICM PC disks obtained in
runs 4 and 5 corresponding to melt temperature of 2408C (a) and 2808C(b). The contribution of thermal birefringence was included in the pre-
dicted birefringence.
FIG. 26. Measured (filled symbols) and predicted (open symbols) aver-
age transverse birefringence < nss � nhh > as a function of the radial
position for ICM PC disk in runs 4, 2, and 5 corresponding to melt tem-
perature of 2408C, 2608C, and 2808C.
FIG. 27. Measured (symbols) and predicted (lines) total residual bire-
fringence Dn distribution in the gapwise direction at various radial posi-
tions at the end of the cooling stage for the PC ICM disks in runs 6 and
7 corresponding to the compression stroke of 1 mm (a) and 2 mm (b).
The contribution of thermal birefringence is included in the predicted
birefringence.
1804 POLYMER ENGINEERING AND SCIENCE—-2013 DOI 10.1002/pen
The average transverse birefringence, < nss � nhh >, as
a function of radial location in ICM PC disks at compres-
sion strokes of 1 mm, 1.5 mm, and 2 mm, a melt temper-
ature of 2608C and a mold temperature of 608C corre-
sponding to runs 6, 2, and 7 is shown in Fig. 28. Again
as the compression stroke increases from 1 mm to 2 mm,
the average transverse birefringence, < nss � nhh >,
decreases significantly because during the injection and
compression stages less stresses are developed in the melt
at a higher compression stroke. This birefringence also
decreases in the radial direction [15, 67] in contrast to the
experimental data reported by Chen et al. [31], indicating
a minimum birefringence at some radial distances. The
simulated and experimental results of the average trans-
verse birefringence at all radial positions with compres-
sion stroke of 1 mm, 1.5 mm, and 2 mm are in a qualita-
tive agreement. Again, some discrepancies between the
experimental and simulated results may be attributed to
the neglect of a contribution to the birefringence due to
the flow in the delivery system consisting of contraction
and expansion region especially near the gate [1].
The Effect of Switchover Time. The switchover time
in ICM process also of greatly affects the flow-induced
birefringence. Due to the limitation of control system, the
switchover time in this work was varied from 0.9 to 1.1 s
only. Figure 19c shows the predicted gapwise residual
flow birefringence Dn distribution at various radial posi-
tions for ICM PC disks in run 2 corresponding to the
switchover time of 1 s. This data can be directly com-
pared with Fig. 29 showing the calculated results for a
hypothetical case of the ICM PC disk in run 2 corre-
sponding to zero switchover time with other processing
conditions being similar to run 2. As stated earlier, during
the switchover time, two competing effects occur cooling
and stress relaxation in the absence of flow. Dominating
effect during the switchover time depends on the duration
of the switchover time. At the short switchover time, the
relaxation effect is dominating factor over the cooling.
Also, at the short switchover time the pressure is lower
and stress relaxation is less. On the other hand, at a long
switchover time used in this work, the cooling is dominat-
ing factor. Due to the cooling effect, the flow-induced
birefringence near the mold surface becomes higher due
to higher stresses at the given compression speed and
slower stress relaxation during the compression stage.
The simulated results in this work suggest that the
switchover time is an important parameter affecting the
birefringence of ICM PC disks. The simulated results
shown in Fig. 29 indicate the presence of a minimum and
a maximum of the birefringence at the switchover time of
0. When the switchover time was employed, more cooling
and higher shear rate at the given compression speed
occur resulting in higher stresses with the maximum of
Dn increasing and shifting further away from the wall as
seen from comparison of Fig. 19c.
The Comparison between CIM and ICM. In contrast
to ICM, in CIM compression stage is absent. It is impor-
tant to find effects of the compression stroke on the bire-
fringence distribution, Dn, and average transverse birefrin-
gence, < nss � nhh >, in ICM PC disks. In this regard,
calculations are carried out at zero switchover time. Fig-
ure 30 shows the predicted gapwise residual flow birefrin-
gence, Dn, distribution at various radial positions at the
end of cooling stage of CIM (a) and ICM (b) without
inclusion of the packing stage. As seen from comparison
of Fig. 30a and b, the birefringence is dramatically
decreased in ICM PC disk, especially near the mold sur-
face in comparison with CIM PC disk. In particular, the
birefringence of ICM PC disk increases and then decrease
slightly with the radial position, whereas that of CIM PC
disk continues to decrease significantly with the radial
position. This trend in ICM and CIM disks is explained
in detail [26, 57]. A reduction of birefringence in ICM
PC disk at a radial position of 2.948 cm compared with
that at a radial position of 3.704 cm is due to the fact that
FIG. 28. Measured (filled symbols) and predicted (open symbols) aver-
age transverse birefringence < nss � nhh > as a function of the radial
position for ICM PC disks in runs 6, 2, and 7 corresponding to the com-
pression stroke of 1 mm, 1.5 mm, and 2 mm.
FIG. 29. Predicted residual flow-induced birefringence Dnfl distribution
in the gapwise direction at various radial positions at the end of the cool-
ing stage for the ICM PC disks without switchover time for run 2.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2013 1805
the velocity and shear rate increase with the radial posi-
tion during the compression stage. In contrast in CIM PC
disk, the velocity and shear rate decrease with the radial
position. From these results, one can conclude that the
compression stage in the ICM certainly reduces the mag-
nitude of the flow birefringence, most notably near the
mold wall.
It is also interesting to find the difference in the average
transverse birefringence < nss � nhh > in ICM and CIM
disks. The predicted and measured average transverse bire-
fringence, < nss � nhh > as a function of the radial location
for CIM and ICM PC disks at the end of cooling is com-
pared in Fig. 31. In both cases this birefringence decreases
in the radial direction [15, 67]. It can be seen that the value
of < nss � nhh > along the radial direction decreases with
distance from the gate with its value in CIM disk being
approximately twice larger than that in ICM disk. Regard-
less, the overall predicted and measured values of
< nss � nhh > are in a qualitative agreement.
CONCLUSIONS
Simulations of a two-dimensional flow in the ICM PS
and PC center-gated disk are carried to predict the flow
and thermal gapwise birefringence distribution and the av-
erage transverse birefringence. The CV/FE/FD numerical
method is employed using a nonlinear viscoelastic model
for flow and the linear viscoelastic and photoviscoelastic
models for the thermal stresses and birefringence. The re-
sidual flow birefringence in the molded disk is calculated
by considering the filling, compression, packing, and
cooling stages of ICM by using a compressible nonlinear
viscoelastic constitutive equation [42]. To take into
account the compressibility of polymeric melts, the Tait
equation is used. The thermal birefringence in ICM disks
was calculated using the viscoelastic and photoviscoelas-
tic models [45, 66] based on the free quenching approxi-
mation. Then, the total birefringence is calculated as a
sum of the flow and thermal birefringence. Effects of
various processing conditions on the birefringence are still
elucidated.
From the extensive simulation of the flow birefrin-
gence for ICM PS and PC disks, processing conditions
affecting significantly the birefringence are identified. The
melt temperature, compression stroke and switchover time
are the processing parameters that have a strong influence
on the birefringence Dn and average transverse birefrin-
gence < nss � nhh >. With an increase of the melt tem-
perature and compression stroke the flow residual birefrin-
gence and average transverse birefringence significantly
decrease. At zero switchover time, the maximum in the
gapwise birefringence distribution in ICM disks is signifi-
cantly reduced compared to that in CIM disks. When the
switchover time is employed, the flow birefringence and
average transverse birefringence are higher compared with
those of ICM disks without a switchover time, but they
are still lower compared to the CIM disks.
The thermal birefringence in ICM disks is treated as
that developed in freely quenched slabs but with the tem-
perature evolution taken from simulation of ICM disks. It
is shown that the thermal birefringence in ICM disks is
mostly influenced by the mold temperature. The effect of
the melt temperature on the residual thermal birefringence
is comparatively less than that of the mold temperature
due to the fact that molding is typically carried out at the
FIG. 30. Predicted residual flow-induced birefringence Dnfl distribution
in the gapwise direction at various radial positions at the end of the cool-
ing stage for PC disks made by the CIM in run 8 (a) and ICM in run 2
without switchover time (b).
FIG. 31. Measured (filled symbols) and predicted (open symbols) aver-
age transverse birefringence as a function of the radial position for PC
disks made CIM in runs 8 and by ICM in run 2.
1806 POLYMER ENGINEERING AND SCIENCE—-2013 DOI 10.1002/pen
melt temperature significantly above Tg. At the same melt
and mold temperatures, the compression stroke does not
show much effect on the thermal residual birefringence.
The presence of the compression stage in the ICM
decreases the overall birefringence, but not the thermal
birefringence. Therefore, one may conclude that ICM is
more suitable for manufacturing of high quality optical
parts than the CIM.
It was found that the measured residual birefringence
distribution showed a maximum near the mold wall and
significant birefringence in the core. The simulated results
capture the essential features of the gapwise flow birefrin-
gence, Dn, and average transverse birefringence,
< nss � nhh >, distributions.
The simulation showed that for ICM PS disks, the bire-
fringence caused by the thermal stresses was negligible
compared with the flow birefringence because the stress-
optical coefficient of PS in the glassy state is much lower
than that in the melt state. For ICM PC disks, the thermal
birefringence is of similar magnitude as the flow birefrin-
gence. The simulation showed that the gapwise residual
flow birefringence is zero at the core due to a fast relaxa-
tion of stresses at high temperatures. A peak near the
mold surface appears as a result of the combination of
frozen-in chain orientation in the injection and compres-
sion stages and slow relaxation in the cooling stage. The
nonzero concave shape of the residual birefringence in
the core predicted and measured in ICM disks is due to
the residual thermal birefringence. The magnitude of the
average transverse birefringence in CIM disks is twice
higher than that of ICM disks. To the best of our knowl-
edge, the present study is the first extensive experimental
and simulation investigations of the frozen-in thermal and
flow birefringence in ICM disks. Although the simulations
do not fully describe the experimental observations, the
present study is a significant step toward understanding
complicated phenomena.
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