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UNIT –III


MANUFACTURING OF ADVANCED

COMPOSITES
CONTENTS –MANUFACTURING OF COMPOSITES



 Preparation of moulding compounds
 Prepregs

 Hand lay up method

 Autoclave method

 Filament winding method

 Compression moulding

 Reaction Injection moulding
PREPARATION OF MOULDING COMPOUNDS


   High polymer material is mixed with 4 to 10
    ingredients each of which discharges a useful
    function during moulding or impart some useful
    property to the finished artifact
TYPES OF MOULDING COMPOUNDING
INGREDIENTS

   1.Resin
   2.Plasticizer
   3.Fillers
   4.Lubricants
   5.Catalyst Or Accelerators
   6.Stabilizers
   7.Colouring Materials
TYPES OF MOULDING COMPOUNDING INGREDIENTS-
                          1.RESIN
   It is a binder which holds different constituents together
   Resin in the most specific use of the term is a
    hydrocarbon secretion of many plants, particularly
    coniferous trees.

   Resins are valued for their chemical properties and
    associated uses, such as the production of varnishes,
    adhesives and food glazing agents
1.RESIN
   Synthetic resins are viscous liquids that are
    capable of hardening permanently.

   Otherwise, chemically they are very different from
    the various resinous compounds secreted by
    plants
1.RESIN-EXAMPLES
 Acrylate Resin
 Acrylic
 Acrylic Resin
 Polyethylene
 Phenolic, Phenolic Resin
 Phenoplast
 Epoxy Glue
 Epoxy Resin
 Melamine Resin
 Polyvinyl Resin
 Vinyl Polymer
 Vinyl Resin
1.RESIN


   Some are thermosetting plastics in which the term
    "resin" is loosely applied to the reactant or product,
    or both. "Resin" may be applied to one of two
    monomers in a copolymer (the other being called a
    "hardener", as in epoxy resins).

   For those thermosetting plastics which require only
    one monomer, the monomer compound is the
    "resin.
1.RESIN
TYPES OF MOULDING COMPOUNDING INGREDIENTS
                   2.PLASTICIZERS

 Plasticizers are materials that are added to resins
  to increase their plasticity and flexibility
 They neutralise the part of the intermolecular forces
  of attraction between macromolecules of resins
 They impart a greater freedom of movement
  between the polymeric macro molecules of resin
  there by increasing the flexibility and plasticity of
  the compound material.
2.PLASTICIZERS
                              Phthalate           esters          are
                              plasticizers used in polyvinyl chloride
                              (PVC) to soften the hard PVC by
                              “lubricating” the areas between
                              polymer strands so that it can be
                              used in consumer products like
                              inflatable pools and food packaging.



Almost 90% of the market for plasticizer is for PVC, giving this
material improved flexibility and durability.

Plasticizers work by embedding themselves between the chains of
polymers, spacing them apart (increasing the "free volume"), and
thus significantly lowering the glass transition temperature for the
plastic and making it softer.
2.PLASTICIZERS
   Plasticizers evaporate and tend to concentrate in
    an enclosed space; the "new car smell" is caused
    mostly by plasticizers evaporating from the car
    interior.
3.FILLERS
 Fillers are added to give the final plastic better
  hardness , tensile strength , finish and workability.
 Advantages :
        Reduces cost
        Reduces shrinkage

        Reduces brittleness

   Examples :
        Carborundum,Quartz,Mica to provide extra hardness
        Barium salts to make plastic impervious to X-rays

        Addition of asbestos provides heat and corrosion

         resistance .
4.LUBRICANTS

   Added to make moulding of plastic easier.


   To impart a flawless , glossy finish to the products .


   Prevents plastic material from sticking to the
    fabricating equipment.
   Eg: Waxes , Oils , soaps etc
5.CATALYSTS OR ACCELERATORS
   Are added only in case of thermosetting plastics.

   Accelerates the polymerization of fusible resin
    during moulding operation into crosslinked infusible
    form .

   Eg: Hydrogen peroxide
        Acetyle sulphuric acid
        Benzoyl peroxide
6. STABILIZERS
 Improve thermal stability during processing
 Eg :
       Vinyl chloride


   UV light stabilizers are used frequently in plastics,
    including cosmetics and films.

    The primary function is to protect the substance
    from the long-term degradation effects from light,
    most frequently ultraviolet light.
7.COLOURING MATERIAL
 Used in high polymer artifacts
 Eg: Organic dystuffs

      Opaque inorganic pigments
Carbon fiber epoxy
rein prepreg
PREPREGS

   Prepreg is the industry term for high quality
    reinforced fibers , which are preimpregnated with a
    resin system and partially cured to B-stage.

       B-stage is an intermediate cure stage of a thermosetting
        resin that lies between the completely uncured stage
        and a completely cured stage.


   Ready to mold or cure material in sheet form which
    may be tow , tape , cloth or mat impregnated with
    resin.
ADVANTAGES

   Consistent quality and consistent resin to
    reinforcement ratio
   Few rejections
   Less variance in mechanical properties .
   Finest quality material.
   Reduce the handling damage to dry fibers.
   Increased curing pressure reduces voids and
    improves fiber wetting
PREPREGS
   A prepreg consists of a reinforcement material
    preimpregnated with a resin matrix in controlled
    quantities.

   The resin is partially cured to a B-stage, and in this
    form is supplied to the fabricator, who lays up the
    finished part and completes the cure with heat and
    pressure.

   The required heat and pressure will vary with the
    resin system and the intended application.
PREPREGS
METHODS OF PRODUCING PREPREG

   1.Solvent Solution Pre-impregnation Process or
    Solution Coating

   2.Hot Melt Pre Impregnation Procedure.

     Solution coating saturates the reinforcement with resin
      dissolved in carrier solvent.
     Hot melt coating uses heat and pressure to impregnate
      the fibers with resin.
     The prepreg is typically laid against the paper or
      polyethylene film separator called interleaf so that the
      preperg don’t stick on to itself and is wound around a
      core.
1.SOLVENT SOLUTION PRE-IMPREGNATION
                 PROCESS
 Woven fabric or fiber yarn is passed through a resin
  rich solution .
 Prepreg is then dried to remove the solvent

 Excess resin is then removed via doctor blade or
  metering rolls
 Then the product is staged to the cold stable
  prepreg form (B-Stage )
1.SOLVENT SOLUTION PRE-IMPREGNATION PROCESS
HOT MELT PREIMPREGNATION PROCEDURE
   It   replaces    solvent   method     because   of
    environmental concerns and a need to exert better
    control over the amount of resin on the fiber .

   Issues with Solvent method :
     Stringent Air emission control regulations and liabilities .
     High cost of maintaining solution ovens .
HOT MELT PREIMPREGNATION PROCEDURE



   In this process woven fabric or fiber yarn is passed
    over a series of rollers .

   The molten polymeric resin wets the fibers and then
    the resin impregnated sheet of fibers is compacted
    over a sheet of release paper and subsequently
    wrapped on rolls for storage .
HOT MELT PREIMPREGNATION PROCEDURE
HOT MELT PREIMPREGNATION PROCEDURE
HOT MELT PREIMPREGNATION PROCEDURE
   At the hot melting machine , the fibers go through a
    metered comb to maintain their parallel integrity for even
    spreading , and are laid on a release film containing a
    controlled amount of resin .

   Another role of release film , either dry or film coated , is
    positioned above the fibers.

   The fibers sandwiched between the films are pulled along
    the tape line with pull rollers as pressure is applied from
    sets of heated compaction rolls metered to the prepreg
    thickness
HOT MELT PREIMPREGNATION PROCEDURE
   The compaction ensures that the fibers are evenly spread
    apart and wet out .

   Once through the heated compaction area , the sandwich
    typically passes through cooling rolls before the carrier
    paper is removed.

   Great care is taken to control the temperature

   Trimming is done at both sides of the prepreg to exact
    width is down just before rewinding

   At the end of the tapeline , windup rolls remove one layer
    of carrier film and reroll it for disposal.
PREPREG CLASSIFICATION
   1.Bleed System

   2.No Bleed or Net Resin Content System
BLEED SYSTEM

   The bleed system Prepregs are those, which
    contain excess matrix that is bled off during the
    cure cycle by the use of BLEEDER PILES.

       Bleeder piles are the layers of fiber glass cloth or other
        highly absorbent material
NO BLEED SYSTEM
   Curing of prepreg takes place under heat and
    pressure

   Bleeder piles are generally not required for no
    bleeding system
DISADVANTAGES OF          PREPREGS


   Shelf Life
        Since the epoxy is in a B-stage, it is required to be
        stored either refrigerated or frozen prior to use.

       Additionally, the overall shelf life can be low.
DISADVANTAGES OF            PREPREGS

   Cost Prohibitive
      When manufacturing composites through a process
      such as vacuum infusion, the raw fiber and resin are
      combined on site.
     However, when using prepregs, the raw material must
      first be prepregged. This is most often done off-site at a
      specialized company that focuses on prepregs. This
      added step in the manufacturing chain can add
      increased cost, and in some instances close to double
      the material cost.
3.HAND LAYUP METHOD
WET/HAND LAY UP METHOD
   Hand Lay-Up is well suited for low volume
    production of product.

   This method can be used for both corrosion barrier
    and the structural portion.
WET/HAND LAY UP METHOD
WET/HAND LAY UP METHOD
   A mold must be used for hand lay-up parts unless
    the composite is to be joined directly to another
    structure.

   The mold can be as simple as a flat sheet or have
    infinite curves and edges.

    For some shapes, molds must be joined in
    sections so they can be taken apart for part
    removal after curing.
WET/HAND LAY UP METHOD
   Reinforcement fibers can be cut and laid in the
    mold.
       It is up to the designer to organize the type, amount and
        direction of the fibers being used.
 Resin must then be catalyzed and added to the
  fibers.
 A brush or roller can be used to impregnate the
  fibers with the resin.
       The lay-up technician is responsible for controlling the
        amount of resin and the quality of saturation.
MATERIALS USED FOR HAND LAYUP
 Resins:
       Any, e.g. epoxy, polyester, vinylester,
        phenolic.


   Fibres:
       Any, although heavy aramid fabrics can
        be hard to wet-out by hand.
HAND   LAY UP METHOD ADVANTAGES
 Advantages:
 i) Widely used for many years.



   ii) Simple principles to teach.

   iii) Low cost tooling, if room-temperature cure resins
    are used.

   iv) Wide choice of suppliers and material types.

    v) Higher fibre contents, and longer fibers than with
    spray lay-up.
Hand Lay-Up Method




Figure 15.4 Hand lay-up : (1) mold is treated with mold release agent; (2) thin gel coat
   (resin) is applied, to the outside surface of molding; (3) when gel coat has partially
   set, layers of resin and fiber are applied, the fiber is in the form of mat or cloth;
   each layer is rolled to impregnate the fiber with resin and remove air; (4) part is
   cured; (5) fully hardened part is removed from mold.
HAND LAY-UP METHOD
HAND LAYUP METHOD - DISADVANTAGES
   Resin mixing, laminate resin contents, and laminate
    quality are very Dependent On The Skills of laminators.
    Low resin content laminates cannot usually be achieved
    without the incorporation of excessive quantities of
    voids.

    ii) Health and safety considerations of resins. The lower
    molecular weights of hand lay-up resins generally
    means that they have the potential to be more harmful
    than higher molecular weight products. The lower
    viscosity of the resins also means that they have an
    increased tendency to penetrate clothing etc.

HAND LAYUP METHOD - DISADVANTAGES

    iii) Resins need to be low in viscosity to be
    workable by hand. This generally compromises
    their mechanical/thermal properties due to the need
    for high diluents levels.
TYPICAL APPLICATIONS
 Standard wind-turbine blades
 Production boats,

 Architectural moldings
PRODUCTS MADE BY HAND LAY-UP
 Generally large in size but low in production
  quantity - not economical for high production
 Applications:

    Boat hulls
    Swimming pools
    Large container tanks
    Movie and stage props
    Other formed sheets
 The largest molding ever made was ship hulls for
  the British Royal Navy: 85 m (280 ft) long
FILAMENT WINDING PROCESS
Filament winding process


Filament winding is automated processes for
creating   parts of   simple   geometry     wherein
continuous resin impregnated fibres are wound
over a rotating male tool called mandrel.
FILAMENT WINDING
 Resin impregnated continuous fibers are wrapped around a
  rotating mandrel that has the internal shape of the desired
  FRP product; the resin is then cured and the mandrel
  removed.
 The fiber rovings are pulled through a resin bath
  immediately before being wound in a helical pattern onto
  the mandrel.
 The operation is repeated to form additional layers, each
  having a criss-cross pattern with the previous, until the
  desired part thickness has been obtained.
Filament Winding




      Figure 15.8 Filament winding.
FILAMENT WINDING PROCESS
TYPES OF FILAMENT WINDING PROCESS

 (i) The Polar Or Planer Method


   (ii) The High Helical Pattern Winding.
THE POLAR OR PLANER METHOD

 A winding in which the filament path passes tangent
  to the polar opening at one end of the chamber and
  tangent to the opposite side of the polar opening at
  the other end.
 The polar or planer method of winding utilizes a
  fixed mandrel and a shuttle that revolves around
  the longitudinal axis of the part to form longitudinal
  winding patterns.

   This type of winding is used if the longitudinal fibres
    are required with angle less than 25° to the mandrel
    axis.
THE POLAR OR PLANER METHOD
HELICAL WINDING PROCESS
   A winding in which the filament or band advances
    along a helical path, not necessarily at a constant
    angle except in the case of a cylindrical article.In
    the high helical pattern winding, the mandrel rotates
    while the shuttle transverses back and forth. Both
    the mandrel rotation and shuttle movement are in
    the horizontal plane. By controlling the mandrel
    rotation and shuttle speed, the fibre angle can be
    controlled.




   .
HELICAL WINDING PROCESS




Angles of 25°-85° to the mandrel rotation axis are
possible
HELICAL WINDING PROCESS
HELICAL WINDING PROCESS
   After completion of the winding, the filament wound
    structure is cured at room temperature or in an
    oven.

   The mandrel is removed after the curing. The
    mandrel, which determines accurate internal
    geometry for the component, is generally the only
    major tool.
FILAMENT WINDING PROCESS
   Low cost mandrel materials such as cardboard or
    wood can be used for winding low cost routine
    parts. For critical parts requiring close tolerances,
    expensive mandrels designed for long term use
    may be required.

    For high temperature cure 315°C (600°F), graphite
    mandrels with low thermal expansion may be
    advantageous. However, attention should be paid
    for potential difficulties for mandrel removal.
TYPES OF MANDRELS
   Mandrels are either REMOVABLE or NON-
    REMOVABLE.

    Removable mandrels are classified according to
    the removal techniques as:
     • Entirely removed.
     • Collapsible.
     • Breakable or soluble.
THE SELECTION OF MANDREL
1.   Part size and complexity
2.    Size of openings
3.    Resin system and its curing
4.   The number of components to be
     fabricated.
THE REQUIREMENTS FOR A MANDREL


 It   must be stiff and strong enough to support
    its own weight and the weight of the applied
    composite while resisting the fibre tension
    pressure from winding and curing.

    It must be dimensionally stable and should
    have thermal coefficient of expansion greater
    than the transverse coefficient of the
    composite structure.
MATERIALS USED FOR CONSTRUCTION OF
MANDREL.

  Low melting temperature alloys used for small
  diameter applications.
 Sand, soluble plaster and eutectic salts used for
  irregular shapes.
 Inflatable   material used in applications where
  sometimes the mandrel remains a part of the structure.
 Segmented metal used for high production rates, and
  where the mandrel can be withdrawn through a small
  hole in the part.
   This process utilises large tonnage presses wherein
    the part is cured between two matched steel dies
    under pressure and high temperature. The moving
    platen is heated either by steam or electricity to
    promote thermal curing.
   Curing of the part is affected by the following
    factors:

       Size of platen, which determines the length and width of
        the part, which can be cured.

       Total tonnage of the press, which determines the
        pressure to be exerted on the projected surface area of
        the part.
   After placing the laminate to be cured called the
    'charge' in the core of the mold, the cavity is then
    closed at a rate of usually 4-12 mm/sec.

   In most cases the mold is heated to 150°C (302°F),
    which causes the charge viscosity to be reduced.

   With increasing mold pressure as the mold is
    closed, the charge flows towards the cavity
    extremities, forcing air out of the cavity.
   The molding pressure based on projected part area
    ranges from 0.7 to 9 MPa (100 to 1200 psi).

   Higher molding pressure causes sink marks, while
    lower pressure cause scumming of the mold and
    porosity.
 The curing time is usually between 25
 sec to 3 minutes depending on several
 factors including
   resin-initiator-inhibitor reactivity
    part thickness

    component complexity

   mold temperature.
ADVANTAGE OF THE COMPRESSION MOLDING

 The primary advantage of the compression molding
  is its ability of producing large number of parts with
  little dimensional variations
 A wide variety of shapes, sizes and complexity can
  be produced by compression molding.
DRAWBACKS
 High tooling cost
 Need for large heated presses.



   Thus, this method is not practical for low volume
    production.
TYPES OF COMPRESSION MOULDING
                    PROCESSES


          1.Sheet Moulding Compound. (SMC)
           2.Bulk Moulding Compound. (BMC)
          3.Wet system Compression Moulding.
   4.Reinforced Thermoplastic Sheet Compression
                       Moulding.
   Sheet moulding compound (SMC) or sheet
    moulding composite is a ready to mould fibre-
    reinforced polyester material primarily used in
    compression moulding.

   The sheet is provided in rolls weighing up to
    1000 kg.
SHEET MOULDING COMPOUND(SMC)
   It refers to both material and process for producing
    glass fiber reinforced polyester resin items .

   SMC is a totally integrated compound in sheet form
    that incorporates all reinforcements resin , chemical
    thickness , fillers , mould release agents and other
    ingredients .

   Also includes pigments and shrink control agents
SHEET MOULDING COMPOUND(SMC
SHEET MOULDING COMPOUND(SMC

   A SMC processing machine produces molding
    compound in sheet form.
   The glass fibre is added to a resin mixture that is
    carried onto a plastic carrier film.
   After partial cure, the carrier films are removed.
   The sheet molding material is cut into lengths and
    placed onto matched metal dies under heat and
    pressure
SHEET MOULDING COMPOUND(SMC
ADVANTAGES OF        SMC MOLDING PROCESS
 High volume production.
 Excellent part reproducibility.

 Minimum material scrap.

 Excellent design flexibility.

 Parts consolidation.
   BMC is a combination of chopped glass strands and Resin
    in the form of a bulk pre-preg.

   BMC is suitable for either compression or injection
    molding.

   Injection molding of BMC is used to produce complex
    components such as electrical equipment, car
    components, housings for electrical appliances and tools,
    in large industrial volumes.
BULK MOULDING COMPOUND
BULK MOULDING COMPOUND
   Unlike SMC, it is not necessary to include a
    maturation stage. Consequently, BMC pre-preg
    formulations contain higher filler contents.

 The chopped glass strands vary in length
  depending on the level of performance required.
  Reinforcement content generally ranges between
  15 and 20 percent; however, it may reach 25
  percent for the highest performance.
 BMC uses a lower reinforcement content than SMC
  and permits higher filler loadings with lower costs.
APPLICATIONS OF BULK MOLDING COMPOUND
 Pump housing
 A/C components

 Circuit Breakers

 Computer components

 Power Tools

 Gear cases

 Electrical insulators
WET SYSTEM COMPRESSION MOULDING


   Matrix ( Liquid Resin ) is pumped to dry
    reinforcement in press mounted and heated
    matched metal moulds

   Hydraulic pressure forces the liquid resin to flow
    through the reinforcement and hold the material in
    place until cure is completed at the cure
    temperature of 120C to 180C
WET SYSTEM COMPRESSION MOULDING


   The equipment used for WCM is same as the BMC.


   Matrix material is thermosetting polyester vinylester
    and epoxy , resins filled with inert materials such as
    clay , calcium carbonate and alumina , catalyst and
    pigment to form a complete liquid system which
    require only the addition of heat for curing

   Reinforcement is chopped strand mats and
    continuous strand mats
REINFORCED THERMOPLASTIC SHEET
            COMPRESSION MOULDING

 Utilizes precombined sheet of thermoplastic resin
  and glass fiber reinforcement
 These sheets are cut into blanks which are
  preheated to a specified temperature and loded into
  matched metal compression mould.
 Under pressure , heat softened blanks flow and fill
  the mould.
 The mould is maintained at a temperature which
  causes the sheet to solidify and allows demoulding
  of the part
REINFORCED THERMOPLASTIC SHEET
                 COMPRESSION MOULDING

   Matrix :
        Thermoplastic Resin , Polypropylene ,
        thermoplastic polyester , polycarbonate and
        nylon.

   Reinfrocement :
       Continous glass fiber mats
REINFORCED THERMOPLASTIC SHEET
            COMPRESSION MOULDING


   ADVANTAGES

 Maximum design flexibility
 Low capital cost

 Tooling cost is low

 Minimum material scrap

 High volume production
REINFORCED THERMOPLASTIC SHEET
DISADVANTAGES
          COMPRESSION MOULDING
   DISADVANTAGES



 Operater skill dependent
 Lower impact resistance

 Only one molded surface is obtained

 Longer curig times required
APLICATION
 Helmets
 Automotive bumper

 Radiator supports

 Battery trays
INJECTION MOULDING
INJECTION MOULDING
   Injection molding is a manufacturing process for
    producing parts from both thermoplastic and
    thermosetting plastic materials.
INJECTION MOULDING

 Material is fed into a heated barrel,
 mixed, and forced into a mold cavity
 where it cools and hardens to the
 configuration of the cavity.
INJECTION MOULDING
CLAMPING - the moving and
fixed platens of the injection
moulding machine holds the           DWELLING - after the molten
mould tool together under            plastic has been injected into the
pressure.                            mould pressure is applied to
                                     ensure all cavities are filled.
INJECTION - the molten plastic       COOLING - the plastic parts are
that has been melted from pellet     then allowed to solidify in the
form in the barrel of the moulding   mould.
machine is injected under
pressure into the mould.
OPENING - the moving platen moves away from the fixed platen separating
the mould tool.

EJECTION - rods, a plate or air blast then aids ejection of the completed
plastic moulding from the injection mould tool.

The length of time from closing the mould to ejecting the finished plastic
moulding is the cycle
PROCESS CHARACTERISTICS

   Utilizes a ram or screw-type plunger to force molten
    plastic material into a mold cavity .

   Produces a solid or open-ended shape that has
    conformed to the contour of the mold.

   It is ideal for producing high volumes of the same
    object
INJECTION MOULDING
 wire spools, packaging, bottle caps,
 automotive dashboards,

 pocket combs,

 , one-piece chairs and small tables,

 storage containers,

 mechanical parts (including gears),

 and most other plastic products available today.



   Injection molding is the most common method of
    part manufacturing..[4].
ADVANTAGES OF INJECTION MOLDING


 high production rates
 repeatable high tolerances

 the ability to use a wide range of materials

 low labor cost

 minimal scrap losses

 little need to finish parts after molding
DISADVANTAGES


 expensive equipment investment
 potentially high running costs

 the need to design moldable parts.
REACTION INJECTION MOLDING

   It is similar to injection moulding except thermosetting
    polymers which requires a curing reaction to occur
    within the mold.


   The RIM Process involves a chemical reaction between
    the two liquid components. Initially, the liquids are held
    in separate, temperature-controlled feed tanks. The
    chemicals are fed through supply lines to metering units
    that precisely meter both chemicals, at high pressure, to
    a mixhead device.
Reaction injection molding
   RIM parts are created through a process that
    begins when two liquid reactants - an Isocyanate
    component and a Polyol resin mixture - are held in
    separate tanks at an elevated temperature with
    agitators.

   These liquids are fed through supply lines at high
    pressure to the mixhead.
 When the injection begins, valves open in the
  mixhead and the liquids enter a chamber in the
  mixhead at high pressures (usually between 1,500
  and 3,000 psi) and high speeds.
 Here    they     are    mixed   by    high-velocity
  impingement.
 From the mix chamber, the mixed liquid flows into
  the mold at atmospheric pressure and undergoes
  an exothermic chemical reaction, forming a polymer
  in                    the                    mold.
   Reaction time is usually expressed in seconds. For
    extremely large parts the reaction time can be
    extended to allow for proper filling of the mold.
ADVANTAGES
   strong, flexible, lightweight parts which can easily
    be painted.

   The bi-component mixture injected into the mold
    has a much lower viscosity than molten
    thermoplastic polymers, therefore large, light-
    weight, and thin-walled items can be successfully
    RIM processed.

   This thinner mixture also requires less clamping
    forces, which leads to smaller equipment and
    ultimately lower capital expenditures.
   The disadvantages are slow cycle times, compared
    to injection molding, and expensive raw materials.

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Unit –iii manufac of adv comp

  • 1. UNIT –III MANUFACTURING OF ADVANCED COMPOSITES
  • 2. CONTENTS –MANUFACTURING OF COMPOSITES  Preparation of moulding compounds  Prepregs  Hand lay up method  Autoclave method  Filament winding method  Compression moulding  Reaction Injection moulding
  • 3. PREPARATION OF MOULDING COMPOUNDS  High polymer material is mixed with 4 to 10 ingredients each of which discharges a useful function during moulding or impart some useful property to the finished artifact
  • 4. TYPES OF MOULDING COMPOUNDING INGREDIENTS  1.Resin  2.Plasticizer  3.Fillers  4.Lubricants  5.Catalyst Or Accelerators  6.Stabilizers  7.Colouring Materials
  • 5. TYPES OF MOULDING COMPOUNDING INGREDIENTS- 1.RESIN  It is a binder which holds different constituents together  Resin in the most specific use of the term is a hydrocarbon secretion of many plants, particularly coniferous trees.  Resins are valued for their chemical properties and associated uses, such as the production of varnishes, adhesives and food glazing agents
  • 6. 1.RESIN  Synthetic resins are viscous liquids that are capable of hardening permanently.  Otherwise, chemically they are very different from the various resinous compounds secreted by plants
  • 7. 1.RESIN-EXAMPLES  Acrylate Resin  Acrylic  Acrylic Resin  Polyethylene  Phenolic, Phenolic Resin  Phenoplast  Epoxy Glue  Epoxy Resin  Melamine Resin  Polyvinyl Resin  Vinyl Polymer  Vinyl Resin
  • 8. 1.RESIN  Some are thermosetting plastics in which the term "resin" is loosely applied to the reactant or product, or both. "Resin" may be applied to one of two monomers in a copolymer (the other being called a "hardener", as in epoxy resins).  For those thermosetting plastics which require only one monomer, the monomer compound is the "resin.
  • 10. TYPES OF MOULDING COMPOUNDING INGREDIENTS 2.PLASTICIZERS  Plasticizers are materials that are added to resins to increase their plasticity and flexibility  They neutralise the part of the intermolecular forces of attraction between macromolecules of resins  They impart a greater freedom of movement between the polymeric macro molecules of resin there by increasing the flexibility and plasticity of the compound material.
  • 11. 2.PLASTICIZERS Phthalate esters are plasticizers used in polyvinyl chloride (PVC) to soften the hard PVC by “lubricating” the areas between polymer strands so that it can be used in consumer products like inflatable pools and food packaging. Almost 90% of the market for plasticizer is for PVC, giving this material improved flexibility and durability. Plasticizers work by embedding themselves between the chains of polymers, spacing them apart (increasing the "free volume"), and thus significantly lowering the glass transition temperature for the plastic and making it softer.
  • 12. 2.PLASTICIZERS  Plasticizers evaporate and tend to concentrate in an enclosed space; the "new car smell" is caused mostly by plasticizers evaporating from the car interior.
  • 13. 3.FILLERS  Fillers are added to give the final plastic better hardness , tensile strength , finish and workability.  Advantages :  Reduces cost  Reduces shrinkage  Reduces brittleness  Examples :  Carborundum,Quartz,Mica to provide extra hardness  Barium salts to make plastic impervious to X-rays  Addition of asbestos provides heat and corrosion resistance .
  • 14. 4.LUBRICANTS  Added to make moulding of plastic easier.  To impart a flawless , glossy finish to the products .  Prevents plastic material from sticking to the fabricating equipment.  Eg: Waxes , Oils , soaps etc
  • 15. 5.CATALYSTS OR ACCELERATORS  Are added only in case of thermosetting plastics.  Accelerates the polymerization of fusible resin during moulding operation into crosslinked infusible form .  Eg: Hydrogen peroxide Acetyle sulphuric acid Benzoyl peroxide
  • 16. 6. STABILIZERS  Improve thermal stability during processing  Eg :  Vinyl chloride  UV light stabilizers are used frequently in plastics, including cosmetics and films.  The primary function is to protect the substance from the long-term degradation effects from light, most frequently ultraviolet light.
  • 17. 7.COLOURING MATERIAL  Used in high polymer artifacts  Eg: Organic dystuffs Opaque inorganic pigments
  • 18.
  • 20. PREPREGS  Prepreg is the industry term for high quality reinforced fibers , which are preimpregnated with a resin system and partially cured to B-stage.  B-stage is an intermediate cure stage of a thermosetting resin that lies between the completely uncured stage and a completely cured stage.  Ready to mold or cure material in sheet form which may be tow , tape , cloth or mat impregnated with resin.
  • 21. ADVANTAGES  Consistent quality and consistent resin to reinforcement ratio  Few rejections  Less variance in mechanical properties .  Finest quality material.  Reduce the handling damage to dry fibers.  Increased curing pressure reduces voids and improves fiber wetting
  • 22. PREPREGS  A prepreg consists of a reinforcement material preimpregnated with a resin matrix in controlled quantities.  The resin is partially cured to a B-stage, and in this form is supplied to the fabricator, who lays up the finished part and completes the cure with heat and pressure.  The required heat and pressure will vary with the resin system and the intended application.
  • 24. METHODS OF PRODUCING PREPREG  1.Solvent Solution Pre-impregnation Process or Solution Coating  2.Hot Melt Pre Impregnation Procedure.  Solution coating saturates the reinforcement with resin dissolved in carrier solvent.  Hot melt coating uses heat and pressure to impregnate the fibers with resin.  The prepreg is typically laid against the paper or polyethylene film separator called interleaf so that the preperg don’t stick on to itself and is wound around a core.
  • 25. 1.SOLVENT SOLUTION PRE-IMPREGNATION PROCESS  Woven fabric or fiber yarn is passed through a resin rich solution .  Prepreg is then dried to remove the solvent  Excess resin is then removed via doctor blade or metering rolls  Then the product is staged to the cold stable prepreg form (B-Stage )
  • 27. HOT MELT PREIMPREGNATION PROCEDURE  It replaces solvent method because of environmental concerns and a need to exert better control over the amount of resin on the fiber .  Issues with Solvent method :  Stringent Air emission control regulations and liabilities .  High cost of maintaining solution ovens .
  • 28. HOT MELT PREIMPREGNATION PROCEDURE  In this process woven fabric or fiber yarn is passed over a series of rollers .  The molten polymeric resin wets the fibers and then the resin impregnated sheet of fibers is compacted over a sheet of release paper and subsequently wrapped on rolls for storage .
  • 31. HOT MELT PREIMPREGNATION PROCEDURE  At the hot melting machine , the fibers go through a metered comb to maintain their parallel integrity for even spreading , and are laid on a release film containing a controlled amount of resin .  Another role of release film , either dry or film coated , is positioned above the fibers.  The fibers sandwiched between the films are pulled along the tape line with pull rollers as pressure is applied from sets of heated compaction rolls metered to the prepreg thickness
  • 32. HOT MELT PREIMPREGNATION PROCEDURE  The compaction ensures that the fibers are evenly spread apart and wet out .  Once through the heated compaction area , the sandwich typically passes through cooling rolls before the carrier paper is removed.  Great care is taken to control the temperature  Trimming is done at both sides of the prepreg to exact width is down just before rewinding  At the end of the tapeline , windup rolls remove one layer of carrier film and reroll it for disposal.
  • 33. PREPREG CLASSIFICATION  1.Bleed System  2.No Bleed or Net Resin Content System
  • 34. BLEED SYSTEM  The bleed system Prepregs are those, which contain excess matrix that is bled off during the cure cycle by the use of BLEEDER PILES.  Bleeder piles are the layers of fiber glass cloth or other highly absorbent material
  • 35. NO BLEED SYSTEM  Curing of prepreg takes place under heat and pressure  Bleeder piles are generally not required for no bleeding system
  • 36. DISADVANTAGES OF PREPREGS  Shelf Life  Since the epoxy is in a B-stage, it is required to be stored either refrigerated or frozen prior to use.  Additionally, the overall shelf life can be low.
  • 37. DISADVANTAGES OF PREPREGS  Cost Prohibitive  When manufacturing composites through a process such as vacuum infusion, the raw fiber and resin are combined on site.  However, when using prepregs, the raw material must first be prepregged. This is most often done off-site at a specialized company that focuses on prepregs. This added step in the manufacturing chain can add increased cost, and in some instances close to double the material cost.
  • 39. WET/HAND LAY UP METHOD  Hand Lay-Up is well suited for low volume production of product.  This method can be used for both corrosion barrier and the structural portion.
  • 40. WET/HAND LAY UP METHOD
  • 41. WET/HAND LAY UP METHOD  A mold must be used for hand lay-up parts unless the composite is to be joined directly to another structure.  The mold can be as simple as a flat sheet or have infinite curves and edges.  For some shapes, molds must be joined in sections so they can be taken apart for part removal after curing.
  • 42. WET/HAND LAY UP METHOD  Reinforcement fibers can be cut and laid in the mold.  It is up to the designer to organize the type, amount and direction of the fibers being used.  Resin must then be catalyzed and added to the fibers.  A brush or roller can be used to impregnate the fibers with the resin.  The lay-up technician is responsible for controlling the amount of resin and the quality of saturation.
  • 43. MATERIALS USED FOR HAND LAYUP  Resins:  Any, e.g. epoxy, polyester, vinylester, phenolic.  Fibres:  Any, although heavy aramid fabrics can be hard to wet-out by hand.
  • 44. HAND LAY UP METHOD ADVANTAGES  Advantages:  i) Widely used for many years.   ii) Simple principles to teach.  iii) Low cost tooling, if room-temperature cure resins are used.  iv) Wide choice of suppliers and material types.  v) Higher fibre contents, and longer fibers than with spray lay-up.
  • 45. Hand Lay-Up Method Figure 15.4 Hand lay-up : (1) mold is treated with mold release agent; (2) thin gel coat (resin) is applied, to the outside surface of molding; (3) when gel coat has partially set, layers of resin and fiber are applied, the fiber is in the form of mat or cloth; each layer is rolled to impregnate the fiber with resin and remove air; (4) part is cured; (5) fully hardened part is removed from mold.
  • 47. HAND LAYUP METHOD - DISADVANTAGES  Resin mixing, laminate resin contents, and laminate quality are very Dependent On The Skills of laminators. Low resin content laminates cannot usually be achieved without the incorporation of excessive quantities of voids.  ii) Health and safety considerations of resins. The lower molecular weights of hand lay-up resins generally means that they have the potential to be more harmful than higher molecular weight products. The lower viscosity of the resins also means that they have an increased tendency to penetrate clothing etc. 
  • 48. HAND LAYUP METHOD - DISADVANTAGES  iii) Resins need to be low in viscosity to be workable by hand. This generally compromises their mechanical/thermal properties due to the need for high diluents levels.
  • 49. TYPICAL APPLICATIONS  Standard wind-turbine blades  Production boats,  Architectural moldings
  • 50. PRODUCTS MADE BY HAND LAY-UP  Generally large in size but low in production quantity - not economical for high production  Applications:  Boat hulls  Swimming pools  Large container tanks  Movie and stage props  Other formed sheets  The largest molding ever made was ship hulls for the British Royal Navy: 85 m (280 ft) long
  • 52. Filament winding process Filament winding is automated processes for creating parts of simple geometry wherein continuous resin impregnated fibres are wound over a rotating male tool called mandrel.
  • 53. FILAMENT WINDING  Resin impregnated continuous fibers are wrapped around a rotating mandrel that has the internal shape of the desired FRP product; the resin is then cured and the mandrel removed.  The fiber rovings are pulled through a resin bath immediately before being wound in a helical pattern onto the mandrel.  The operation is repeated to form additional layers, each having a criss-cross pattern with the previous, until the desired part thickness has been obtained.
  • 54. Filament Winding Figure 15.8 Filament winding.
  • 56. TYPES OF FILAMENT WINDING PROCESS  (i) The Polar Or Planer Method  (ii) The High Helical Pattern Winding.
  • 57. THE POLAR OR PLANER METHOD  A winding in which the filament path passes tangent to the polar opening at one end of the chamber and tangent to the opposite side of the polar opening at the other end.  The polar or planer method of winding utilizes a fixed mandrel and a shuttle that revolves around the longitudinal axis of the part to form longitudinal winding patterns.  This type of winding is used if the longitudinal fibres are required with angle less than 25° to the mandrel axis.
  • 58. THE POLAR OR PLANER METHOD
  • 59. HELICAL WINDING PROCESS  A winding in which the filament or band advances along a helical path, not necessarily at a constant angle except in the case of a cylindrical article.In the high helical pattern winding, the mandrel rotates while the shuttle transverses back and forth. Both the mandrel rotation and shuttle movement are in the horizontal plane. By controlling the mandrel rotation and shuttle speed, the fibre angle can be controlled.  .
  • 60. HELICAL WINDING PROCESS Angles of 25°-85° to the mandrel rotation axis are possible
  • 62. HELICAL WINDING PROCESS  After completion of the winding, the filament wound structure is cured at room temperature or in an oven.  The mandrel is removed after the curing. The mandrel, which determines accurate internal geometry for the component, is generally the only major tool.
  • 63. FILAMENT WINDING PROCESS  Low cost mandrel materials such as cardboard or wood can be used for winding low cost routine parts. For critical parts requiring close tolerances, expensive mandrels designed for long term use may be required.  For high temperature cure 315°C (600°F), graphite mandrels with low thermal expansion may be advantageous. However, attention should be paid for potential difficulties for mandrel removal.
  • 64. TYPES OF MANDRELS  Mandrels are either REMOVABLE or NON- REMOVABLE.  Removable mandrels are classified according to the removal techniques as:  • Entirely removed.  • Collapsible.  • Breakable or soluble.
  • 65. THE SELECTION OF MANDREL 1. Part size and complexity 2. Size of openings 3. Resin system and its curing 4. The number of components to be fabricated.
  • 66. THE REQUIREMENTS FOR A MANDREL  It must be stiff and strong enough to support its own weight and the weight of the applied composite while resisting the fibre tension pressure from winding and curing.  It must be dimensionally stable and should have thermal coefficient of expansion greater than the transverse coefficient of the composite structure.
  • 67. MATERIALS USED FOR CONSTRUCTION OF MANDREL.  Low melting temperature alloys used for small diameter applications.  Sand, soluble plaster and eutectic salts used for irregular shapes.  Inflatable material used in applications where sometimes the mandrel remains a part of the structure.  Segmented metal used for high production rates, and where the mandrel can be withdrawn through a small hole in the part.
  • 68.
  • 69.
  • 70.
  • 71.
  • 72. This process utilises large tonnage presses wherein the part is cured between two matched steel dies under pressure and high temperature. The moving platen is heated either by steam or electricity to promote thermal curing.
  • 73. Curing of the part is affected by the following factors:  Size of platen, which determines the length and width of the part, which can be cured.  Total tonnage of the press, which determines the pressure to be exerted on the projected surface area of the part.
  • 74. After placing the laminate to be cured called the 'charge' in the core of the mold, the cavity is then closed at a rate of usually 4-12 mm/sec.  In most cases the mold is heated to 150°C (302°F), which causes the charge viscosity to be reduced.  With increasing mold pressure as the mold is closed, the charge flows towards the cavity extremities, forcing air out of the cavity.
  • 75. The molding pressure based on projected part area ranges from 0.7 to 9 MPa (100 to 1200 psi).  Higher molding pressure causes sink marks, while lower pressure cause scumming of the mold and porosity.
  • 76.  The curing time is usually between 25 sec to 3 minutes depending on several factors including resin-initiator-inhibitor reactivity  part thickness  component complexity mold temperature.
  • 77. ADVANTAGE OF THE COMPRESSION MOLDING  The primary advantage of the compression molding is its ability of producing large number of parts with little dimensional variations  A wide variety of shapes, sizes and complexity can be produced by compression molding.
  • 78.
  • 79. DRAWBACKS  High tooling cost  Need for large heated presses.  Thus, this method is not practical for low volume production.
  • 80. TYPES OF COMPRESSION MOULDING PROCESSES  1.Sheet Moulding Compound. (SMC)  2.Bulk Moulding Compound. (BMC)  3.Wet system Compression Moulding.  4.Reinforced Thermoplastic Sheet Compression Moulding.
  • 81. Sheet moulding compound (SMC) or sheet moulding composite is a ready to mould fibre- reinforced polyester material primarily used in compression moulding.  The sheet is provided in rolls weighing up to 1000 kg.
  • 82.
  • 83. SHEET MOULDING COMPOUND(SMC)  It refers to both material and process for producing glass fiber reinforced polyester resin items .  SMC is a totally integrated compound in sheet form that incorporates all reinforcements resin , chemical thickness , fillers , mould release agents and other ingredients .  Also includes pigments and shrink control agents
  • 85. SHEET MOULDING COMPOUND(SMC  A SMC processing machine produces molding compound in sheet form.  The glass fibre is added to a resin mixture that is carried onto a plastic carrier film.  After partial cure, the carrier films are removed.  The sheet molding material is cut into lengths and placed onto matched metal dies under heat and pressure
  • 87. ADVANTAGES OF SMC MOLDING PROCESS  High volume production.  Excellent part reproducibility.  Minimum material scrap.  Excellent design flexibility.  Parts consolidation.
  • 88. BMC is a combination of chopped glass strands and Resin in the form of a bulk pre-preg.  BMC is suitable for either compression or injection molding.  Injection molding of BMC is used to produce complex components such as electrical equipment, car components, housings for electrical appliances and tools, in large industrial volumes.
  • 90. BULK MOULDING COMPOUND  Unlike SMC, it is not necessary to include a maturation stage. Consequently, BMC pre-preg formulations contain higher filler contents.  The chopped glass strands vary in length depending on the level of performance required. Reinforcement content generally ranges between 15 and 20 percent; however, it may reach 25 percent for the highest performance.  BMC uses a lower reinforcement content than SMC and permits higher filler loadings with lower costs.
  • 91.
  • 92. APPLICATIONS OF BULK MOLDING COMPOUND  Pump housing  A/C components  Circuit Breakers  Computer components  Power Tools  Gear cases  Electrical insulators
  • 93. WET SYSTEM COMPRESSION MOULDING  Matrix ( Liquid Resin ) is pumped to dry reinforcement in press mounted and heated matched metal moulds  Hydraulic pressure forces the liquid resin to flow through the reinforcement and hold the material in place until cure is completed at the cure temperature of 120C to 180C
  • 94. WET SYSTEM COMPRESSION MOULDING  The equipment used for WCM is same as the BMC.   Matrix material is thermosetting polyester vinylester and epoxy , resins filled with inert materials such as clay , calcium carbonate and alumina , catalyst and pigment to form a complete liquid system which require only the addition of heat for curing  Reinforcement is chopped strand mats and continuous strand mats
  • 95. REINFORCED THERMOPLASTIC SHEET COMPRESSION MOULDING  Utilizes precombined sheet of thermoplastic resin and glass fiber reinforcement  These sheets are cut into blanks which are preheated to a specified temperature and loded into matched metal compression mould.  Under pressure , heat softened blanks flow and fill the mould.  The mould is maintained at a temperature which causes the sheet to solidify and allows demoulding of the part
  • 96. REINFORCED THERMOPLASTIC SHEET COMPRESSION MOULDING  Matrix : Thermoplastic Resin , Polypropylene , thermoplastic polyester , polycarbonate and nylon.  Reinfrocement :  Continous glass fiber mats
  • 97. REINFORCED THERMOPLASTIC SHEET COMPRESSION MOULDING  ADVANTAGES  Maximum design flexibility  Low capital cost  Tooling cost is low  Minimum material scrap  High volume production
  • 98. REINFORCED THERMOPLASTIC SHEET DISADVANTAGES COMPRESSION MOULDING  DISADVANTAGES  Operater skill dependent  Lower impact resistance  Only one molded surface is obtained  Longer curig times required
  • 99. APLICATION  Helmets  Automotive bumper  Radiator supports  Battery trays
  • 101. INJECTION MOULDING  Injection molding is a manufacturing process for producing parts from both thermoplastic and thermosetting plastic materials.
  • 102. INJECTION MOULDING  Material is fed into a heated barrel, mixed, and forced into a mold cavity where it cools and hardens to the configuration of the cavity.
  • 104.
  • 105. CLAMPING - the moving and fixed platens of the injection moulding machine holds the DWELLING - after the molten mould tool together under plastic has been injected into the pressure. mould pressure is applied to ensure all cavities are filled. INJECTION - the molten plastic COOLING - the plastic parts are that has been melted from pellet then allowed to solidify in the form in the barrel of the moulding mould. machine is injected under pressure into the mould.
  • 106. OPENING - the moving platen moves away from the fixed platen separating the mould tool. EJECTION - rods, a plate or air blast then aids ejection of the completed plastic moulding from the injection mould tool. The length of time from closing the mould to ejecting the finished plastic moulding is the cycle
  • 107. PROCESS CHARACTERISTICS  Utilizes a ram or screw-type plunger to force molten plastic material into a mold cavity .  Produces a solid or open-ended shape that has conformed to the contour of the mold.  It is ideal for producing high volumes of the same object
  • 108. INJECTION MOULDING  wire spools, packaging, bottle caps,  automotive dashboards,  pocket combs,  , one-piece chairs and small tables,  storage containers,  mechanical parts (including gears),  and most other plastic products available today.  Injection molding is the most common method of part manufacturing..[4].
  • 109. ADVANTAGES OF INJECTION MOLDING  high production rates  repeatable high tolerances  the ability to use a wide range of materials  low labor cost  minimal scrap losses  little need to finish parts after molding
  • 110. DISADVANTAGES  expensive equipment investment  potentially high running costs  the need to design moldable parts.
  • 111. REACTION INJECTION MOLDING  It is similar to injection moulding except thermosetting polymers which requires a curing reaction to occur within the mold.  The RIM Process involves a chemical reaction between the two liquid components. Initially, the liquids are held in separate, temperature-controlled feed tanks. The chemicals are fed through supply lines to metering units that precisely meter both chemicals, at high pressure, to a mixhead device.
  • 113. RIM parts are created through a process that begins when two liquid reactants - an Isocyanate component and a Polyol resin mixture - are held in separate tanks at an elevated temperature with agitators.  These liquids are fed through supply lines at high pressure to the mixhead.
  • 114.  When the injection begins, valves open in the mixhead and the liquids enter a chamber in the mixhead at high pressures (usually between 1,500 and 3,000 psi) and high speeds.  Here they are mixed by high-velocity impingement.  From the mix chamber, the mixed liquid flows into the mold at atmospheric pressure and undergoes an exothermic chemical reaction, forming a polymer in the mold.
  • 115. Reaction time is usually expressed in seconds. For extremely large parts the reaction time can be extended to allow for proper filling of the mold.
  • 116. ADVANTAGES  strong, flexible, lightweight parts which can easily be painted.  The bi-component mixture injected into the mold has a much lower viscosity than molten thermoplastic polymers, therefore large, light- weight, and thin-walled items can be successfully RIM processed.  This thinner mixture also requires less clamping forces, which leads to smaller equipment and ultimately lower capital expenditures.
  • 117. The disadvantages are slow cycle times, compared to injection molding, and expensive raw materials.