optimizing process condition of resin transfer molding...

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OPTIMIZING PROCESS CONDITION OF RESIN TRANSFER MOLDING: DETERMINING MATERIAL PROPERTIES FOR NUMERICAL SIMULATION C-W. Wang 1 , C-T. Heng 2 , L-J. Bin 2 , S-P. Sun 1 , C-H. Hsu 1 , Y. Yao 2 , and R-Y Chang 1 1 CoreTech System (Moldex3D) Co., Ltd., Chupei City, Hsinchu, Taiwan 2 Department 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 (K 33 ) 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 260-300°C [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 21 st 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 SPE ANTEC ® Anaheim 2017 / 750

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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

    SPE ANTEC Anaheim 2017 / 750

  • 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.

    SPE ANTEC Anaheim 2017 / 751

  • 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

    SPE ANTEC Anaheim 2017 / 752

  • 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.

    References 1. P. Ferland, L. J Lee, Polymer Composites, 17,

    149 (1996)

    2. S. Laurenzi, M. Marchetti, Composites and Their

    Properties, Chapter 10 (2012).

    3. W.D. Brouwer , Composites: Part A 34 (2003).

    4. Koefoed, Michael Schlarth,Lund, Erik,Sol, H.

    Degrieck, J, 2002

    5. V. R. Voller*, S. Peng and F. Chen, International

    Journal for Numerical Methods in Engineering,

    2889-2906,(1998)

    6. Q. Liu , R. S. Parnas, H. S. Giffard, Composites:

    Part A, 38, 954(2007).

    7. R.-Y. Chang and W.-H. Yang, Int. J. Numer. Meth.

    Fluids, 37, 125 (2001).

    8. W. B. Young, K. Han. L. H. Fong, and L. J Lee,

    POLYMER COMPOSITES, 12, 391 (1991)

    9. Shojaei, A., S.R. Ghaffarian, and S.M.H. Karimian,

    Composites Science and Technology, (2002).

    SPE ANTEC Anaheim 2017 / 753

  • 10. J. Ni, Y. Zhao, L. J, James, S. Nakamura, Polymer

    Composites, 18, 2, 254 (1997)

    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

    SPE ANTEC Anaheim 2017 / 754

  • Figure 7. In plane filling data for PVC core material

    Table 1. Summary of the permeability data for different

    materials

    SPE ANTEC Anaheim 2017 / 755