a constitutive model for large multiaxial deformations of solid polypropylene at high temperature
TRANSCRIPT
A Constitutive Model for Large Multiaxial Deformationsof Solid Polypropylene at High Temperature
John Sweeney, Robert Spares, Mike WoodheadSchool of Engineering, Design, and Technology/IRC in Polymer Science and Technology, University ofBradford, Bradford BD7 1DP, UK
Experiments on a blow-molding grade of polypropylenehave been performed at 1358C using a biaxial testingmachine. Both simultaneous and sequential equibiaxialtests were performed at strain rates relevant to solidphase processing regimes. A constitutive model hasbeen developed that includes a single Eyring processand two Edwards-Vilgis networks. The effectiveness ofthis model for predicting the observed stress-strainbehavior is explored. Predictions of simultaneousstretching and the first stretch in sequential experi-ments are excellent. The second stretch in sequentialexperiments is less well predicted, but the model’s per-formance is useful overall. The model is incorporatedinto a commercial finite element code and its practical-ity is demonstrated. POLYM. ENG. SCI., 49:1902–1908,2009. ª 2009 Society of Plastics Engineers
INTRODUCTION
There are a number of important polymer processes in
which products are formed by deformation to large strains
at elevated temperatures below melting point. These proc-
esses include thermoforming, blow molding, and stretch
blow molding. There is also an increasing need for effi-
ciency in polymer processing, both in terms of energy
consumption and material usage. This latter factor has led
to a greater interest in process modeling, which in turn
demands a fundamental understanding of large polymer
deformations under the appropriate conditions. At the
heart of this understanding is the material constitutive
equation, which is the subject of this study.
We present both a constitutive model and its experi-
mental verification. For a complex, large deformation
model, uniaxial testing cannot yield sufficient information
to fully define the material parameters, as demonstrated
by Sweeney et al. [1], and this makes a necessity for
biaxial experiments. Furthermore, when deciding what
experiments are required to verify a constitutive theory,
the program of testing should encompass the combina-
tions of strain along the different axes—the strain paths—
that relate to relevant applications. Given the impossibility
of including all possible strain paths, it makes sense to
define the material parameters using those that are partic-
ularly relevant.
In this article, we present a constitutive model that
includes the essential features of the material behavior:
large deformations, strain rate dependence of stress, and
yielding. This theory is applied to a particular grade of
polypropylene. A program of large strain biaxial testing
provides verification at conditions relevant to processing
regimes. Both simultaneous equibiaxial and sequential
biaxial strain paths are modeled. The model is imple-
mented as a user-defined subroutine in the finite element
package ABAQUS.
MATERIALS AND TESTING
A commercial polypropylene material, designed for
injection stretch blow molding (TOTAL Petrochemicals
PPR 7225), supplied in the form of granules was formed
into sheet using a film line that extrudes through a die
onto a chill roll. According to the manufacturer’s data,
this material has a melt temperature of 1468C and is
specially designed for injection stretch blow molding. The
film line incorporated a Betol BK38 extruder connected
to a Davis Standard lab3 Roll ‘‘Hi-Press’’ 3 roll stack.
The four extruder barrel zones were set at 145, 165, 175,
and 1808C respectively with the clamp, adapter, and die
maintained at 1808C. These temperature settings were
arrived at after consideration of the low melting point of
the material in comparison with typical polypropylenes,
and they are each lower by 158C than that which would
be appropriate according to our experience for these more
conventional materials with melting temperature of
around 1658C. The water cooling temperature for the chill
roll was 138C, the extruder screw speed was set at 75
rpm, and the line speed of the stack set to 35 mm/s. By
operating with a die that has a width of 150 mm and gap
of 0.7 mm, the resulting material was 0.65 mm thick.
Correspondence to: J. Sweeney; e-mail: [email protected]
Contract grant sponsor: The European Commission under the Framework
6 Program via the Apt-Pack project.
DOI 10.1002/pen.21426
Published online in Wiley InterScience (www.interscience.wiley.com).
VVC 2009 Society of Plastics Engineers
POLYMER ENGINEERING AND SCIENCE—-2009
Ideally, the product from this process would be iso-
tropic, but a small haul-off force was exerted on the sheet
during processing, inducing some molecular orientation
along the extrusion direction, and this was observable in
the equibiaxial stretching experiments reported below. The
stretching forces along the two experimental axes (corre-
sponding to extrusion and transverse directions) were indis-
tinguishable up to strains of 0.2, but at strains greater than
this became measurably different, with the force along the
extrusion direction exceeding that along the transverse
direction by 12% at strains of 0.5. The results presented
here are for the stress averaged over the two directions.
Square samples of 55 3 55 mm were stretched in
tension using a biaxial testing machine in air at a temper-
ature of 1358C. This corresponds to an appropriate tem-
perature for solid phase processing of the material. The
specimens were held by six pneumatic grips per side, with
force transducers incorporated into two of the grips as
shown in Fig. 1. The biaxial testing machine was manu-
factured originally by T M Long, and as a result of recent
modifications, it is fitted with PC-based displacement,
temperature control, and data capture. Software was writ-
ten using National Instruments Labview 8.0 to interface
with two NI PCI-6221 cards housed in a single PC. One
card is responsible for monitoring the position of the
hydraulic pistons and set the required speed via two
Parker VRD350 hydraulic motion controllers. The loads
are also monitored to prevent overload and damage to the
machine. Draw rates, ratios, and starting time of each pis-
ton can be controlled independently of one another. The
second card monitors the load and position, with the data
captured in block mode to ensure precise time increments
of the data for subsequent analysis.
The modes of stretching were simultaneous equibiaxial
and sequential equibiaxial. The latter comprises two pla-
nar extension (constant width) steps, the first always along
the sheet extrusion direction, followed immediately by a
second perpendicular stretch, to achieve a final equibiaxial
stretch. Tests were performed at two constant speeds, cor-
responding to initial strain rates of 0.37 and 2.3 s21 up to
extension ratios of 4.75 (true strains of 1.56). Loads were
monitored at a sampling rate of 400 Hz. The specimens
were observed to deform uniformly.
The higher value of strain rate is the greatest practicable
rate for the present stretching apparatus. In industrial proc-
essing, strain rates are often much higher. However, even
if the much higher strain rates were achievable experimen-
tally, the problems of anisothermal conditions associated
with adiabatic heating would further complicate the experi-
mental interpretation. We believe that this experimental re-
gime can establish the principles of the constitutive behav-
ior that should be applicable at higher strain rates.
Strains were calculated from the grip displacements dand the gauge length L, the distance between opposite
grips. The extension ratios k are thus given by
l ¼ 1þ dL
(1)
and the true strains e by
e ¼ lnðlÞ (2)
The stresses were calculated by assuming that the total
force on each specimen side was equal to six times the
force measured in one of the six transducers. The validity
of this procedure is explored below by modeling. For the
calculation of true stresses, the material is assumed to be
incompressible, with the true stress s calculated as
s ¼ lF=a (3)
where F is the total force on the specimen side, and a the
initial cross-sectional area.
The results presented are averages of three tests.
THEORY
Time and rate dependence are included in the constitu-
tive model by means of an Eyring process in which the
scalar plastic strain rate ep is given by
ep ¼ A expðVpsÞ sinhðVstÞ (4)
where A is a temperature dependent term that includes
activation enthalpy, and Vp and Vs are material constants
being (at constant temperature) proportional to pressure
and shear activation volumes respectively (following, for
example, Buckley and Jones [2] or Spathis and Kontou
[3]). The process is driven by the mean stress s and the
octahedral shear stress t, to be defined below.
The other major component in the model represents
large elastic deformations. Edwards and Vilgis [4] derivedFIG. 1. Arrangement of grips and transducers around biaxial specimen.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2009 1903
the following expression for the change in strain energy
per unit volume W, as a result of principal extension
rations kI, kII, and kIII
W
kT¼ 1
2Nc
ð1� a2ÞI11� a2I1
þ lnð1� a2I1Þ� �
þ 1
2Ns
Xi
ð1þ ZÞð1� a2Þl2ið1þ Zl2i Þð1� a2I1Þ
þ lnð1þ Zl2i Þ8>>>:
9>>>;"
þ lnð1� a2I1Þ#
ði¼ I; II; IIIÞ ð5Þ
Here, k is Boltzmann’s constant and T, the absolute tem-
perature. Nc and Ns are crosslink and sliplink densities
respectively, and Z is a ‘slipperiness factor’ that charac-
terizes the degree of mobility of the sliplink; Z ‡ 0 where
Z ¼ 0 corresponds to no mobility. The model includes
the phenomenon of finite strain extensibility, which is char-
acterized by the parameter a and corresponds to a
singularity in the strain energy as the denominator 1 2 a2I1approaches zero. I1 is the first strain invariant, equal to
I1 ¼ l2I þ l2II þ l2III (6)
The material is assumed incompressible with lIlIIlIII ¼1. As a result, principal stresses are derived from Eq. 5 by
si ¼ liqWqli
� p ði ¼ I; II; IIIÞ (7)
where p is an unknown hydrostatic pressure. In the present
analysis, we assume plane stress conditions with zero stress
along the III direction, so that on elimination of p the
stresses in the I-II plane are
si ¼ liqWqli
� lIIIqWqlIII
ði ¼ I; IIÞ (8)
The model consists of two ‘arms’ arranged in parallel.
One arm consists of an Edwards-Vilgis network in series
with an Eyring process (the X arm), and the other entirely
of an Edwards-Vilgis network (the Y arm), the general
arrangement being shown in Fig. 2. There are many prece-
dents for this configuration, perhaps the earliest being due
to Haward and Thackray [5]. The formulation is suitable
for implementation as a user-defined ‘UMAT’ subroutine
within the finite element package ABAQUS. The total
strain is the same as the strain in each arm and is defined
by the deformation gradient G. G is split into pure defor-
mation D and rigid body rotation R (via the use of the
Cauchy-Green strain measure) to give
G ¼ DR (9)
In the X arm, the strain is split into elastic and plastic
components, DeX and Dp, associated with stress-strain laws
Eqs. 4, 5, respectively:
G ¼ DeXDpR (10)
The principal values of DeX, leXI, and leXII, define the
stress in the X arm via Eq. 8, with parameters NXc , N
Xs , Z
X
and aX. An incremental approach is employed, with the
current plastic stretch related to the plastic strain Dp0 at the
end of the previous time increment and the increment of
plastic strain DDp, developed during the current increment,
related by
G ¼ DeXDDpDp0R (11)
For a given total deformation, G, DeX, and DDp in
Eq. 11 are derived via an iterative process, involving
Eqs. 4, 5, to impose the condition that the stresses in
the network and the Eyring process are equal. The rela-
tive proportions of the components of DDp are fixed
by the use of a Levy-Mises flow rule, defined in the
relation (Eq. 18) below. The resulting true stress is
then transformed to global directions to give the stress
tensor SX.
The Y arm consists of an Edwards-Vilgis network with
parameters NYc , N
Ys , g
Y and aY. The principal extension
ratios are those of D, and Eq. 8 defines the stress. From
this, we derive the stress tensor in global axes SY. The
total stress S is then given by
� ¼ �X þ�Y (12)
The stress quantities driving the Eyring process of Eq.4 relate to the stress SX. The stress deviator t is given by
t ¼ �X � sI (13)
where the mean stress is given by
s ¼ 1
3tr �X� �
(14)
The scalar octahedral shear stress t used in (Eq. 4) is
then given in terms of the stress deviator tensor s by
t ¼ffiffiffiffiffiffiffiffiffiffiffiffi1
3s : s
r(15)
where the colon denotes the double contraction.
FIG. 2. Schematic arrangement of constitutive model.
1904 POLYMER ENGINEERING AND SCIENCE—-2009 DOI 10.1002/pen
At each time increment, any rigid body rotations are
stripped from the plastic strain tensor using the Cauchy-
Green process and polar decomposition, to give a pure
stretch Dp with zero associated plastic spin. The scalar
strain rate used in (Eq. 4) is derived from the rate of plas-
tic deformation Qp
Qp ¼ DpDp�1 (16)
by the relation
ep ¼ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffi1
3Qp : Qp
r(17)
The Levy-Mises flow rule can then be expressed as
Qp
ep¼ s
t(18)
The above analysis has been programmed as a user-
defined ‘UMAT’ subroutine in the finite element package
ABAQUS. For convenience, the calculations of stress for
the polymer matrix in uniform states of strain, as used in
Figs. 3–6, and are obtained by runs of four-element
square models in ABAQUS.
RESULTS AND MODELING
In Fig. 7, we plot yield stress in the form of octahedral
stress (defined in Eq. 15) against the natural logarithm of
octahedral strain rate (defined in Eq. 17) for both simulta-
neous and sequential stretching. Yield is observed at
strains of 0.1–0.2, and is taken as the stress corresponding
to when the gradient in the stress-strain curve stops
decreasing (this is observable in Figs. 3–6). If we envis-
age the action of the two-arm model, this stress would
correspond to the stress in the X-arm becoming constant
(Fig. 2). At this point, the rate of strain in the Eyring
model matches that of the total applied strain, and the
network in the X-arm ceases to stretch. Conventionally
[6], the rate dependence of the Eyring process is derived
by approximating the hyperbolic sine function of Eq. 4
with an exponential, which then becomes
ep ¼ A expðVpsþ VstÞ (19)
Typically, Vp � Vs and the first term in the argument
of the exponential may be neglected. Then (Eq. 19) can
be rearranged to give
t ¼ 1
Vs
lnepA
8>: 9>; (20)
which implies that the gradient of the plot in Fig. 7 is
equal to 1/Vs. On this basis, the gradient of the line fitted
through all the results in Fig. 7 corresponds to Vs ¼ 6.9
MPa1. The results presented in Fig. 7 suggest that the rate
dependence of the planar extension (sequential biaxial)
results differs from that obtained for the simultaneous
equibiaxial results. However, we shall proceed on the
assumption that there is one average rate dependence for
the two stretching modes in accordance with the theory
presented above, and accept that this may introduce an
approximation.
With the value of Vs determined, the value of the pres-
sure activation parameter Vp is then derived on the basis
that it is a fixed proportion of Vp ¼ 0.06 Vs, in line with
the conclusions of other workers on polymers [7–9]. With
the activation volumes established, the Eyring constant A
FIG. 3. Simultaneous equibiaxial drawing for strain rate 0.37 s21.
FIG. 4. Sequential drawing for strain rate 0.37 s21. Axial strain
increases from 0 to 1.56, and is then constant. Transverse strain is zero
until axial strain reaches 1.56, and then is increased to 1.56.
FIG. 5. Simultaneous equibiaxial drawing for strain rate 2.3 s21.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2009 1905
determines the stress at yield, and is fixed on that basis
with respect to the experimental curves of Figs. 3–6.
There remain two Edwards-Vilgis networks to be
defined. The X-arm network ceases to extend, once the
Eyring process begins to flow, so is subject only to strains
up to around 0.1. The chief aspects of this network model
are not invoked, and therefore, we include only the cross-
link term (the first term involving Nc in Eq. 5) with no
finite strain extensibility, so that we are assuming a Gaus-
sian network. This is defined by the single parameter NXc
which is derived from the initial slopes of the stress-strain
curves. The other network is defined by shape of the
stress-strain curve up to maximum strain. The parameters
for this network are determined by trial and error, using
both kinds of experiment and, in the case of sequential
experiments, both axial and transverse stresses. The set of
parameters for the whole model is given in Table 1.
The quality of the model predictions at the two strain
rates is apparent from Figs. 3–6. For the simultaneous
stretches of Figs. 3 and 5, the initial yielding behavior is
well modeled. At higher strains, there is negligible error
up to a strain of 1.0 at the lower speed in Fig. 3, with the
maximum error around 10% as the maximum strain is
approached. At the higher speed in Fig. 5, the maximum
error is around 7%. For the sequential tests of Figs. 4 and
6, the predictions of the first stretches are of a quality
similar to those of the simultaneous experiments. For the
second stretches, there are significant errors. For the axial
stresses at both testing speeds, there is a sharp drop in the
observed stress after the end of the first stretch that is not
well captured. The rate of stress relaxation observed is
much higher than that associated with the single Eyring
process of the model, the parameters of which are deter-
mined by the observed stress levels and strain rate de-
pendence. We must conclude that there are in reality
other flow processes in operation at shorter time scales
that are not featured in this simple model. The other
major discrepancy is in the underprediction of the trans-
verse stress during the second stretch, which is apparently
an inherent feature of the Edwards-Vilgis network model;
this issue is developed in the discussion below.
A finite element model of the experimental specimen
has been made, using the mesh shown in Fig. 8a. A quar-
ter model is used, stretched simultaneously along its two
perpendicular axes at an overall strain rate of 2.3 s21 to a
state of true strain of 1.4 3 1.4, as shown in Fig. 8b. The
circular unstrained regions near the outer boundaries rep-
resent the grips, which are in the form of cylindrical
pneumatic pistons. We calculate the stress with the
method used to interpret the experiments, using only the
reaction force at the grips nearest the centre of the speci-
men sides (corresponding to two circular regions in Fig.
8a and b, one at lowest right and the other at highest left)
to calculate the total force, and making use of Eqs. 1–3 to
calculate the stress-strain curve. This is compared with
the stress-strain curve at the position corresponding to the
specimen center (the 3 3 3 array of elements at the lower
left corner of the model). The comparison is shown in
Fig. 9. This plot suggests that the simple method of calcu-
lating specimen stress-strain data produces little error.
DISCUSSION
There have been some previous studies of polypropyl-
ene under conditions that, like those used here, are rele-
vant to the solid phase processing regime. Briatico-
Vangosa et al. [10] performed high temperature tests at
rates of 0.5–2 s21 under uniaxial tensile conditions, and
modeled their results using elastic theories. Capt et al.
[11] performed high temperature stretches at strain rates
in the range 0.24–1.43 s21 in simultaneous equibiaxial,
planar, and uniaxial modes. Their observed strain rate de-
pendence of yield stress, reported for simultaneous equi-FIG. 7. Rate dependence of yield stress.
FIG. 6. Sequential drawing for strain rate 2.3 s21. Axial strain
increases from 0 to 1.56, and is then constant. Transverse strain is zero
until axial strain reaches 1.56, and then is increased to 1.56.
TABLE 1. Parameters used for the constitutive model.
NXc /
MPa
NXs /
MPa gX aXNYc /
MPa
NYs /
MPa gY aYVs/
MPa21
Vp/
MPa21
103
A/s21
4.37 0 – 0 0.36 0.085 0.2 0.08 6.9 0.4 8.0
1906 POLYMER ENGINEERING AND SCIENCE—-2009 DOI 10.1002/pen
biaxial stretching at 1508C (148C below the melting
point), which is of a similar magnitude to that reported
here (at 118C below the melting point). There have also
been observations of inhomogeneous multiaxial stretching
of polypropylene, modeled using an elastic theory [1].
This work advances the field in two ways: the inclu-
sion of strain rate dependence into the constitutive model;
and the use of both simultaneous and sequential biaxial
stretching experiments to verify the model. The first issue
is important because the strain rate sensitivity of a mate-
rial determines whether or not strain inhomogeneities,
such as necks, will form. When used in a process model,
it is highly desirable that the constitutive model be capa-
ble of predicting the consequences of this, such as local-
ized wall thinning. The second issue also applies to pro-
cess modeling. Any constitutive equation will provide at
best an approximation to the real material behavior, and
will represent some strain states better than others. It is
therefore desirable to examine its performance for strain
paths that are relevant to processing. Sequential biaxial
drawing is a strain path that is particularly relevant to
stretch blow molding and representative of the complexity
that can be encountered in practice. Examination of a
model’s performance under these conditions provides a
more realistic assessment of its practical value. For the
present model, we may conclude that the quality of its
predictions are good to excellent for the simultaneous
stretching and the first stretch in the sequential stretching
and less good but still useful for the second sequential
stretch.
In these experiments, it is clear that, once a significant
strain has been realized and the Eyring process activated,
the greater part of the stress is due to the network in the
Y arm of the model. On the basis of this model, the dis-
crepancy in the predictions of stress for the second stretch
in the sequential experiments must to a large extent be
accounted for in the response of the Edwards-Vilgis net-
work. In particular, the stress predicted for the transverse
direction during the second stretch is consistently low.
This could reflect some increase in crystallinity or net-
work entanglements during the first stretch.
The Eyring parameter Vs can be interpreted as an acti-
vation volume v, via the relation
v ¼ VskT (21)
where k is a Boltzmann’s constant and T, the absolute
temperature. For the testing temperature 1358C, the cur-
rent value of 6.9 MPa–1 corresponds to v ¼ 39 nm3. This
can be compared with values obtained by others for poly-
propylene, invariably obtained at lower test temperatures.
Working on the oriented polypropylene fibers at room
temperature, Duxbury and Ward [12] identified two acti-
vation volumes, with the larger one in the range 0.5–0.6
nm3. Teoh et al. [13], working in tension at room temper-
ature on a commercial isotropic polypropylene, identified
a single Eyring process with an activation volume of
6.13 nm3. Seguela et al. [14] made measurements in
tension on both quenched and annealed polypropylene at
various temperatures, and found for quenched material
(conditions similar to the production of our sheet) an acti-
FIG. 9. Comparison of model stresses deduced from stretching force
with those calculated for specimen center.
FIG. 8. (a) Mesh for quarter model of biaxial specimen. (b) Deformed
model, stretched to true strains of 1.4 3 1.4.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE—-2009 1907
vation volume of around 3.0 nm3 at 258C and for annealed
material around 7.7 nm3 at 608C. Dasari et al. [15] haveused room temperature testing of polypropylene to deter-
mine an activation volume of 2.77 nm3. The general indi-
cation is that, for polypropylene up to 608C, there is an
activation volume of 3–8 nm3, with a trend of increasing
activation volume with temperature. When viewed in this
context, our value is of a reasonable order of magnitude.
CONCLUSION
When operating at large strains, biaxial experiments
are an essential tool for the determination of the material
parameters that define complex constitutive equations. It
is desirable that the strain paths used in the experiments
reflect those that occur in the applications for which the
constitutive equation is to be used.
A constitutive equation, in which yielding and strain
rate dependence are controlled by an Eyring process and
large strain behavior by an Edwards-Vilgis network, has
been shown to give an effective representation of the
multiaxial stretching of a blow-molding grade of polypro-
pylene at 1358C, at true strains of up to 1.56. Both simul-
taneous and sequential equibiaxial strain paths were used
in the experiments. The latter provided a severe test of
the constitutive model, particularly in the case of the sec-
ond stretch. For the simultaneous stretching and for the
first stretch in the sequential experiment, i.e., in planar
extension, the model provided excellent predictions.
NOMENCLATURE
A Pre-exponential factor in Eyring
equation
a Cross-sectional area
D Pure stretch tensor
DD Stretch increment tensor
ep Scalar plastic strain rate
Superscript e elastic
F Force
G Deformation gradient tensor
I1 First strain invariant
k Boltzmann’s constant
L Gauge length
Nc Crosslink density
Ns Sliplink density
p Hydrostatic pressure
Superscript p plastic
Qp Rate of plastic strain tensor
R Rotation tensor
T Absolute temperature
v Activation volume
Vp Parameter proportional to pressure
activation volume
Vs Parameter proportional to shear
activation volume
w Strain energy density
Superscript X X-arm of model
Superscript Y Y-arm of model
Greek Symbols
a Finite strain extensibility factor
d Grip displacement
g Sliplink slipperiness factor
k Extension ratio
r Component of normal stress
r Mean stress
s Scalar octahedral shear stress
s Stress deviator tensor
S Stress tensor
REFERENCES
1. J. Sweeney, T.L.D. Collins, P.D. Coates, and I.M. Ward,
Polymer, 38, 5991 (1997).
2. C.P. Buckley and D.C. Jones, Polymer, 36, 3301 (1995).
3. G. Spathis and E. Kontou, Polym. Eng. Sci., 41, 1337
(2001).
4. S.F. Edwards and T.A. Vilgis, Polymer, 27, 483 (1986).
5. R.N. Haward and G. Thackray, Proc. Roy. Soc A., 302, 453(1968).
6. I.M. Ward and J. Sweeney, An Introduction to the Mechani-cal Properties of Solid Polymers, John Wiley & Sons Ltd,
Chichester, UK, 233 (2004).
7. S. Nazarenko, S. Bensason, A. Hiltner, and E. Baer, Poly-mer, 35, 3883 (1994).
8. C. Bauwens-Crowet and J.-C. Bauwens, J. Mater. Sci., 7,176 (1972).
9. L.E. Govaert, P.H.M. Timmermans, and W.A.M. Brekel-
mans, J. Eng. Mater. Technol., 122, 177 (2000).
10. F. Briatico-Vangosa, M. Rink, F. D’Oria, and A. Verzelli,
Polym. Eng. Sci., 40, 1553 (2000).
11. L. Capt, S. Rettenberger, H. Munstedt, and M.R. Kamal,
Polym. Eng. Sci., 43, 1428 (2003).
12. J. Duxbury and I.M. Ward, J. Mater. Sci., 22, 1215 (1987).
13. S.H. Teoh, A.N. Poo, and G.B. Ong, J. Mater. Sci., 29,4918 (1994).
14. R. Seguela, E. Staniek, B. Escaig, and B. Fillon, J. Appl.Polym. Sci., 71, 1873 (1999).
15. A. Dasari, S. Sarang, and R.D.K. Misra, Mater. Sci. Eng.,A368, 191 (2004).
1908 POLYMER ENGINEERING AND SCIENCE—-2009 DOI 10.1002/pen