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  • 7/30/2019 Patrics Hand-out 3

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    Polymer Blends

    - Homogeneous blends

    - miscible on molecular scale,

    mobility is averaged, consequently glass transition

    temperatures are averaged

    - Heterogeneous blends

    p. 295

    - not miscible but phase separated,

    mobility of original phases present, consequently glass

    transition temperatures of original phases are present

    Miscibility and modulus

    M

    Purecomponents

    Tg1 Tg2

    Tg12

    M

    Miscibleblend

    Tg1 Tg2

    M

    T

    Immiscibleblend

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    Phase Behaviour of Blends

    Change of Gibbs free energy Gm should be negative and second derivativewith respect to volume fraction must be larger than zero for complete

    Gm = Hm - TSm

    .

    - Complete miscibility seldom in highmolecular systems because of entropyeffects (Sm 0) favourable interactionsare necessary (0 > Hm)

    p. 297

    - Heterogeneous blends common

    Phase Behaviour of Blends

    Example: Polystyrene Polycarbonate blends shows LCST behaviour

    Decreasing molecular

    Lower Critical

    Solution Temperature

    weight of PS

    p. 299

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    Commercial Miscible Polymer Blends

    p. 303

    Glass Transition and Crystallisation in PVDF/PMMA

    Poly(vinylidene fluoride) can crystallisedepending on composition andtemperature. PMMA serves like a diluent

    and lowers the meltin tem erature.

    p. 303

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    Properties of Blends

    p. 304

    Toughened Plastics and Phase Separated Blends

    Example: high-impact Polystyrene (HIPS)

    Promotion ofextensive shearyielding or crazeformation

    p. 306

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    Interpenetrating Networks

    Example: IPN of poly(ethyl acrylate) and polystyrene

    p. 307

    Properties of Fibers

    p. 290

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    Properties of Matrices

    p. 309

    Mechanical Properties

    Modulus : in the fiber direction in uniaxial reinforced composite

    EL = (1-f) Em + f Ef

    Strength :

    L = (1-f) m + f f

    p. 310

    Reinforcement in perpendicular direction much lower and dependent oninterfacial adhesion between fiber and matrix.

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    Interfacial Adhesion and Coupling Agents

    p. 312

    Nanocomposites

    p. 316

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    Nanocomposites properties

    p. 315

    Nanocomposite Structure

    Exfoliated nanoclay in a polymer matrix

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    Polysulfone Nanocomposites

    p. 317

    Composite Processing: Filament Winding

    Products: pipes,tanks, flagpoles

    p. 318

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    Composite Processing: Pultrusion

    Continuous moulding process for profiles utilizing glassor other fibrous reinforcement in a polyester or otherresin matrix

    p. 319

    Polymer Processing and Rheology

    Basic steps for processing thermoplastics and elastomers:

    heating of material

    Rheology is science of flow of materials

    p. 427

    transport of hot melt

    shape realization

    fixation of shape

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    Extrusion Process

    - Extrusion is a continuous process to produce:tubes, profiles, cables, plates, foils, fibers, bottles

    tratt

    silpaket

    skruv

    vrmeelement termoelement gngamatar-ficka

    p. 429

    matarzonkompressionszonskjuvzon

    munstycke

    mantel

    Extrusion Process

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    Molding Processes

    Moldin : discontinuous rocess

    - injection molding

    - reaction injection molding

    - compression molding

    - transfer molding

    - thermoforming termoformning, vacuumformning

    formpressning

    reaktiv formsprutning

    formsprutning

    sprutpressning

    p. 429

    - blow molding

    - rotational molding

    formblsning

    rotationsgjutning

    Injection Molding

    un yc e

    p. 432

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    Injection Molding

    Injection Molding

    p. 433

    inlopp frdelningskanal

    formrumskanal

    formrum

    frgreningskanal

    kallplugg

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    Reaction Injection Molding

    RIM process with two separate tanks for polymerisation reagents

    Polyamides

    Epoxies

    Polyurethanes

    p. 434

    Compression Molding Process

    A. View of open mold withmolding material in place

    B. Closed mold showing formed partand flash formed from excess resin

    p. 430

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    Transfer Molding

    A. Transfer potis loaded whilemold is in closed position

    .into mold form

    C. Mold opens and ejector pins pushout molded part

    p. 431

    Thermoforming

    Also called vacuumforming

    p. 435

    A. Flat sheet is heated

    B. Softened sheet is forcedto fit the mold contour byevacuating the spacebetween the sheet and themold

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    Blow Molding

    Extrusion blow-molding process in the production of plastic bottles

    p. 436

    PET preforms forinjection blow molding

    Calendering

    Production of plastic sheet of PVC, PVC blends and copolymers of PVC

    Simplified representation ofa calendering process,usually several cylindersinvolved

    p. 437

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    Coating

    A. Roll coating

    B. Blade coating

    p. 437

    C. Curtain coating

    Polymer Rheology

    Shear stress is proportional to shear rate

    The viscosit is

    p. 440

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    Viscosity of Polymer Melts

    Typical behaviour of a polymeric melt

    Zero-shear viscosity

    -avarage molecular mass

    p. 442

    Rheometry

    Measurement techniques:

    Capillary rheometer

    Couette rheometer

    p. 461

    Cone-and Plate rheometer

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    Capillary Rheometer

    Range : shear rates from 1 105 s-1

    By measuring pressure drop over thecapillary and volumetric flow rate theshear stress and shear strain rate can becalculated and thus the viscosity.

    p. 462

    Couette Rheometer

    The shear stress is determinedby measuring the torque, theshear rate is determined by theangular velocity and dimensions ofthe system.

    p. 465

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    Cone-and Plate Rheometer

    Why using a cone ? Cone angle is very small, 1-3 degrees

    Shear rate is independent on R !

    p. 467

    ear ra e

    Shear stress is proportional to torque

    Viscosity measurements

    Polymer melts at 200 oC

    HDPE

    PP

    PSPMMA

    LDPE

    p. 468

    Cone-and-plate