optimizing process condition of resin transfer molding...
TRANSCRIPT
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OPTIMIZING PROCESS CONDITION OF RESIN TRANSFER MOLDING: DETERMINING MATERIAL PROPERTIES FOR NUMERICAL SIMULATION
C-W. Wang 1, C-T. Heng2, L-J. Bin2, S-P. Sun1, C-H. Hsu1, Y. Yao2, and R-Y Chang1
1CoreTech System (Moldex3D) Co., Ltd., Chupei City, Hsinchu, Taiwan 2Department of Chemical Engineering, National Tsing-Hua University, Hsinchu, Taiwan 30043, R.O.C.
Abstract
Herein, we present the recent development in
permeability measurement by an optical visualization
method. We applied this technique to investigate materials
commonly used in wind turbine industry, such as different
types of fiber mats, distribution medium, PVC core
material. Wind turbine industry utilizes predominately
resin transfer molding (RTM) process to manufacture the
components. The traditional-trail-error method in this case
is not practical due to the high cost of producing the
components. To the best of our knowledge, this is the first
example of using an optical method in conjunction with a
simulation tool to obtain out of plane (K33) permeability.
The results demonstrate the promising potential of
permeability measurement by the optical visualization
method, and great relevance to industrially important
processes such as RTM. The measured material properties
are then used in process simulation to obtain optimal
process conditions of RTM.
Introduction Demand for improved part performance has led to
efforts to produce products that are lighter, stronger, and
more efficient. In the last decade or so, FRP (fiber
reinforced plastic) due to their superior mechanical
performance and light weight characteristics have been
widely used in variety of applications ranging from 3C
products, automotives, shipbuilding, aerospace and wind
energy [1-2]. FRP are not a new class of materials, but
recent advancements have dramatically improved them
and given greater range to their properties. Improvements
in the matrix chemistry have allowed composites to move
into harsher environments. For example, some polyimides
can be use up to temperature range of 260-300C [2]. As
well, changes in reinforcement types and configuration
have yielded improved strength and processing
characteristics. Reinforcements in FRP can range from
short/long fibers, mats, directional fabrics, and braided
structures which allow them versatile for different
processes.
The Resin Transfer Molding (RTM) is one of the
most promising technology available today. It belongs to
one of the liquid composites molding (LCM) process. The
RTM process is used in many applications since it is
capable of making large complex three-dimensional part
with high mechanical performance, tight dimensional
tolerance and high surface finish. Furthermore, RTM is
one of the most efficient and economical process due to
its capabilities such as non-expensive process equipment,
closed mold process, low filling pressures, excellent
control on mechanical properties, incorporation of metal
inserts and attachments, possibility of producing large and
complex parts and low labor costs [3-5].
Wind energy has become an indispensable player in
the worldwide energy production and will play an
ever-increasing role in the 21st century energy market.
Vacuum Assisted Resin Transfer Molding (VARTM) has
replaced the traditional Hand layer-up method used in
producing composite wind turbine blades as the more
superior process method as it eliminates process variables
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such as pressure and speed at which the operator applies
the resin. However, there are still challenges facing
VARTM. For example, it is difficult to accurately predict
the resin flow because of locally high fiber volume in
certain regions can drastically change mold fill behavior.
As such, RTM operators cannot accurately anticipate
these effects, nor can they visually verify whether the part
has reached full saturation before injection process is shut
down. If the part is not 100% impregnated, defects such
as dry spots or voids are introduced, and the part must be
discarded and changes made to the injection geometry
until all dry spots are eliminated. Applying this
trial-and-error methodology to the resin transfer molding
of large structures, i.e. utility grade turbine blades, would
be expensive. However, through successful simulation of
RTM flow, it is possible to predict the flow properties in a
complex structure and eliminate the trail-and-error
approach [6-7].
The traditional measurement of permeability is to
measure the filling behavior by using sensor nodes to
detect melt front time and then use this data to fit out the
permeability. However, the presence of sensor nodes
might interfere with the melt front, leading the inaccurate
melt front data. In this study, we build a robust
visualization system which could improve the accuracy of
the measurements of the permeability. We study different
types of fiber mats and core materials that are common in
wind turbine manufacturing. Currently RTM simulation
software is still very rare, with a huge market demand and
potential customer base, including fiber materials
manufacturers, mold manufacturers, and various
industries that uses RTM as a mean to produce their
products [8-9].
Experimental Section
We have carried out experimental investigation on
two different types of fiber mat, distribution medium and
a core material using the visualization system (Figure 1).
Before experiment the material was trimmed to specific
dimensions (120 mm x 300 mm). Using PVC tubing,
the material being tested was connected to a vacuum
pump on one end, while the other end was connected to
the resin reservoir. Vacuum environment was created by
using high performance vacuum bag and clay. Clay was
carefully applied to the edge of vacuum bag with the
material centered under the high speed video camera.
LabVIEW was used for instrument control, process
automation and data acquisition. Industrial motor oil was
used for filling experiment and the viscosity before each
experiment was measured using a viscometer. In order to
calculate the true permeability of the fiber mat, the
porosity of the fiber needs to be measured. The thickness
of fiber mat layer is carefully measured by placing the
stacked fiber mat in between two metal plates and sealed
under vacuum with using high performance vacuum bag
Figure 2). In total, thickness from 6 different areas were
measured and averaged. The density of fiber mat was
measured using a high precision density balance.
Furthermore, we also carried out experimental
investigation on flow information in the thickness
direction. The melt front data is obtained using radial flow
method where the melt is injected in the center, and
spreads in a circular or elliptical pattern. The melt front
data is recorded on both sides of the fiber mats using high
speed camera, one on the top and one at the bottom.
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Results and Discussion Fluid flow in porous medium can be described by
Darcys Law (Eq1)
LPKVDD
=
1
where P is pressure difference and in this case 1atm
(1.013 x 105 Pa), V is the fluid velocity, L is the distance
that the fluid travel in unit time, and is fluid viscosity.
Thus the permeability K can be obtained using equation 1.
Before we can begin to process the data, one must
understand the difference between Seepage Velocity and
Darcian Velocity. The flow in fiber mat is through porous
medium, and therefore the effective area (A) is much
smaller than the cross-sectional area (A) and can be
described by the equation 2.
fAA = 2
If A is incorporated into Darcys Law, we can define a
new velocity Seepage Velocity, and Q the volumetric
flow rate from Equation 3 can be written into Equation 4.
PAKQ -=
! 3
PAKQ -=f'!
4
The Darcian (V) and seepage velocity (V)can be obtain
from equation 5 and 6
PkAQV -=-=
f'
!!
5
fV
AQV
!!!
=-='
6
What is observed in experiment (Figure 3) is not the
velocity term (V ) described in the Darcys Law, but
rather is the seepage velocity (V). The porosity is less
than 1, and therefore A< A. From Mass balance, Q =VA
=VA, one can see that V> V. In order to bring the
observed melt front into Darcys Law for calculation, we
need to convert the Seepage Velocity to Darcian Velocity,
and can be described by the following equation (7)
PKVVd -
==
f'!!
7
Equation 7 can be further simplified to give 1D scalar
form (Equation 8)
LPKVVd
D-==
f'!!
8
After replacing the velocity term by dL/dT, and
integration on both sides, we obtain Equation 9.
tPKL
fD
=22
9
The flow front data L is recorded as a function of time.
After plugining P (pressure difference), (viscosity)
and (the porosity of medium), the permeability can be
obtained.
From the permeability data obtained for biaxial
(-45/+45), we note that the average K11 and K22 are
within 5% difference, indicating that there is no
preferential flow directional for this type of fiber mat. For
large structure such as wind turbine where fiber mat
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layers can go up to 20-30 layers in certain area, flow
information in the thickness direction is critical, and
therefore we carried out experimental investigation on
permeability in the out of plane direction (K33). Out of
plane data from both the top and bottom surface was fitted
simultaneously using Moldex3D RTM module to derive
the out of plane permeability (K33 = 2.20E-13 m2). Most
experimental investigations on K33 relies on using sensors
of some sort, which could potentially interfere the melt
front as the melt travels in the thickness direction. In this
study, we present an alternate method to derive the
permeability data in the thickness direction without any
interference. We further carried out investigations on the
permeability behavior of different systems, including
uni-axial fiber mat, distribution medium and PVC core
material. The results are summarized in table 1. We note
that the filling behavior for uni-axial shows strong
directionality along the fiber direction as is the case with
distribution medium along principal filling direction.
Permeability and porosity result is summarized in table 1.
Since PVC core material is a closed cell foam material,
fluids only travels through the pre-opened channels. The
out of plane permeability data (K33 = 4.95 E-10 m2) is
derived using empirical formula assuming the
fully-developed average velocity in a channel resembles
the Darcy equation [10].
In this study, we use the Moldex3D RTM to simulate
the filling behavior of the core material. The simulation
geometry shows in Figure 6, and the dimension of the
cavity is 30cm in length, 15 cm in width, and 3cm in
thickness. The material parameters are set according to
the Table 1. The PVC core material is anisotropic with a
porosity = 0.002 and in-plane permeability of K11 = K22
=4.95 E-13 m2, out of plane permeability K33 = 4.95 E-10 m2.
In this experiment we used constant viscosity oil h=0.157 Pa s to fill the core under a constant inlet pressure
P = 1 atm. The experimental data for PVC core material
and simulation flow front time results is shown in Figure
7. The filling behavior of the simulation is in good
agreement with the experiment.
Conclusions In this paper, we carried out experimental
investigations into material properties that is required for
accurate RTM simulation. We built a robust visualization
system to improve the accuracy of permeability
measurements. Different types of fiber mats, distribution
medium and core materials, common in wind turbine
manufacturing, are thoroughly analyzed. We believed that
the methodology presented here could in term improve the
accuracy of RTM prediction and benefit the related
industry.
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Figure 1. Schematic of flow visualization system (redraw)
Figure 2. Fiber mat thickness measurement setup
Figure 3. Difference between Darcian and Sleepage
velocity
Figure 4. In plane permeability data for biaxial
(+45/-45) fabrics with surface density (808g/cm2)
Figure 5. Out of plane melt front data for biaxial
(+45/-45) fabrics with surface density (808g/cm2). The
out of plane permeability is calculated to be K33 = 2.20E-13
m2
Figure 6. Geometry of the core material
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Figure 7. In plane filling data for PVC core material
Table 1. Summary of the permeability data for different
materials
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