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Effect Of Time, Temperature, And Draw Down On Interlayer ...DDR DDR v L t f f ln 1 ... Temperature...

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1 2009 TAPPI Flexible Packaging – Trends and Technology Developments Symposium Effect Of Time, Temperature, And Draw Down On Interlayer Peel Strength During Coextrusion Coating, Film Casting and Film Blowing Presented by: Hariharan.K Technical Specialist, Packaging & Industrial Polymers, E I DuPont India Pvt. Ltd.
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  • 12009 TAPPI Flexible Packaging –Trends and Technology

    Developments Symposium

    Effect Of Time, Temperature, And Draw Down On Interlayer Peel Strength During Coextrusion Coating, Film Casting and Film Blowing

    Presented by:Hariharan.KTechnical Specialist, Packaging & Industrial Polymers, E I DuPont India Pvt. Ltd.

  • 2

    OutlineBackground

    Experimental

    Results

    Discussion

    Time

    Temperature

    Area Creation

    Practical Implications

    Conclusions

  • 3

    Coextrusion• Combination of resins in the melt

    • Cost effect technique to make functional articles

    Nip Roll Chill Roll

    Die

    Line Speed

    Air gap

    Substrate

    Not drawn to scale

  • 4

    Many factors influence adhesion• Compatibility of polymers and their ability to interdiffuse

    • Presence of functional groups to promote chemical bonding at the interface

    • Contact time and temperature

    • Thickness and physical properties of the layers

    • Stress imparted by drawing and other means

    • The environment the article is subjected in its end use (RH, temperature, chemicals, etc.)

  • 5

    Effect of Time in the Air Gap on Foil Adhesion

    25 μm Coatings onto Al Foil

    0

    200

    400

    600

    800

    1000

    1200

    0 50 100 150 200TIAG, ms

    Peel

    Str

    engt

    h,

    g/25

    mm

    Time in Air Gap Known to Effect Adhesion to Solid Substrates

    Antonov and Soutar (1991)

    Little attention given to affect on interlayer adhesion in coextrusion.

    EMAA

    LDPE

  • 6

    Blown FilmMorris (1996)

    Blown Film Results(HDPE-Adh-EVOH)

    0

    200

    400

    600

    800

    1000

    1200

    1400

    1600

    0 2 4 6 8 10 12 14

    EVOH Process time (sec)

    Peel

    Str

    engt

    h (g

    /25m

    m)

    ADH1

    ADH2

    ADH3

    ADH3

    ADH1

    ADH2

  • 7

    Coextrusion tie resin technology

    PE Tie EVOH

    Tie resin is polyethylene or ethylene copolymer based to promote diffusion at PE/Tie interface

    Tie has anhydride groups for chemical interaction at Tie/EVOHinterface

    Tie may contain modifiers such as rubber that enhance peel strength

  • 8

    Blown Film

    • Tie resins• ADH1: LLDPE,

    low anhydride• ADH2: LLDPE,

    high anhydride• ADH3: rubber

    modified LLDPE, medium anhydride

    • Stress believed to be involved

    Blown Film Results(HDPE-Adh-EVOH)

    0

    200

    400

    600

    800

    1000

    1200

    1400

    1600

    0 2 4 6 8 10 12 14

    EVOH Process time (sec)

    Peel

    Str

    engt

    h (g

    /25m

    m)

    ADH1

    ADH2

    ADH3

    ADH3

    ADH1

    ADH2

    Morris, 1996 SPE ANTEC

  • 9

    Current StudyPurpose: Look at the effect of process time on interlayer adhesion in coextrusion coating/cast film

    What is the appropriate process time?

    Constant velocitytf = TIAG = L/vf

    Linear model

    ( )DDRDDR

    DDRvLt

    ff ln1

    ⎟⎠⎞

    ⎜⎝⎛

    −=

    Newtonian Model

    .)ln(1⎟⎟⎠

    ⎞⎜⎜⎝

    ⎛ −=

    DDRDDR

    vLt

    ff

    Velocity Profile in Air Gap

    0

    0.1

    0.2

    0.3

    0.4

    0.5

    0.6

    0.7

    0.8

    0.9

    1

    0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1

    z/L

    (V-V

    o)/(V

    f-Vo)

    Constant Velocity

    Linear ModelCanning and Co, 1999, DDR=7.27

    Newtonian Model

  • 10

    ExperimentalStructure: Kraft Paper/LDPE//(tie-EVOH-tie-LDPE)

    19 5 6.3 5 25 micronsResins:

    Variables:• Die gap: 0.5 mm, DDR 18

    • Air gap: 13 - 25 cm (5 – 10 in)

    • Line speed: 61 – 183 m/min (200 – 600 fpm)

    • Process time: 0.22 – 1.3 s

    Resin Description LDPE Standard coating grade EVOH 44 mol % ethylene Tie 1 LLDPE with low anhydride Tie 2 LLDPE with high anhydride Tie 3 Rubber modified LDPE with intermediate anhydride

  • 11

    ExperimentalStructure: Al/(EAA-LDPE)

    50 5 25 micronsResins:

    • EAA: 9% AA, 10 MI

    • LDPE: 0.923 g/cc, 4.5 MI

    Variables:• Die gap: 0.5 mm, DDR: 20

    • Air gap: 11.4 – 22.9 cm (4.5 – 9 in)

    • Line speed: 61 – 183 m/min (200 – 600 fpm)

    • Process time: 0.21 – 0.42 s

  • 12

    ResultsCoextrusion Coating Results

    Paper/LDPE//(tie/EVOH/tie/LDPE)

    0

    200

    400

    600

    800

    1000

    1200

    0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4

    Process Time, s

    Peel

    Str

    engt

    h to

    EVO

    H, g

    /25m

    m

    Tie3

    Tie2

    Tie1

  • 13

    ResultsCoextrusion Coating

    50-μm Al//(5-μm EAA - 25μm LDPE)

    500

    520

    540

    560

    580

    600

    620

    640

    660

    680

    0.15 0.2 0.25 0.3 0.35 0.4 0.45

    Process Time, s

    Peel

    Stre

    ngth

    to L

    DPE

    , g/2

    5mm

  • 14

    Comparison of EC and BF Results

    Coextrusion Coating ResultsPaper/LDPE//(tie/EVOH/tie/LDPE)

    0

    200

    400

    600

    800

    1000

    1200

    0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4

    Process Time, s

    Peel

    Str

    engt

    h to

    EVO

    H, g

    /25m

    m

    Tie3

    Tie2

    Tie1

    Blown Film Results(HDPE-Adh-EVOH)

    0

    200

    400

    600

    800

    1000

    1200

    1400

    1600

    0 2 4 6 8 10 12 14

    EVOH Process time (sec)

    Peel

    Str

    engt

    h (g

    /25m

    m)

    ADH1

    ADH2

    ADH3

    ADH3

    ADH1

    ADH2

    Extrusion Coating results suggest kinetic effect

  • 15

    Slope Differences

    Ga = Wb(1 + Φ(R, T))where Ga = fracture energy

    Wb = work of adhesion or bonding

    Φ = local viscoelastic energy dissipation

    R = rate

    T = temperature.

    Multiplying effect• Rubber modification increases Φ

    • If Wb = constant, adding rubber shifts curve upward (blown film)

    • If Wb increases with process time (kinetics), slope also increases

  • 16

    Differences between blown and cast film

    Time scales• Process time

    • Blown film: 5-10 s

    • Cast film/EC: 0.2-1.0 s

    • Crystallization time

    • Blown film: 2-5 s

    • Cast film/EC: 2-10 ms

    Temperature during drawing

    Interfacial area creation

  • 17

    Time Scales: Blown Film50 μm HDPE

    80

    90

    100

    110

    120

    130

    140

    150

    160

    0 10 20 30 40 50

    z, cm

    Tem

    pera

    ture

    , ºC

    CLH

    FLH

    FZH

    Temperature measurements of outside of film using IR thermometer

    CLHFLH

    FZHz

  • 18

    Crystallization time: Blown Film

    Plateau of Bubble Temperature

    00.5

    11.5

    22.5

    33.5

    44.5

    5

    0 5 10 15

    Process Time (sec)

    Plat

    eau

    Wid

    th (s

    ec)

    Morris, 1998

  • 19

    Time Scales: Cast Film/ECModel Prediction of Temperature at EVOH-

    Tie InterfacePaper/LDPE//(tie-EVOH-tie-LDPE)

    123 m/min, 13-cm air gap

    20

    70

    120

    170

    220

    270

    320

    0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4

    Time Since Die Exit, s

    Tem

    pera

    ture

    , C

    WebChill Roll

    Contact with Chill Roll

    Die

    Chill Roll

  • 20

    Time Scales: Cast Film/EC

    Results using heat conduction model

    Cooling in NipPaper/LDPE//(tie-EVOH-tie-LDPE)

    123 m/min, 13-cm air gap

    0

    50

    100

    150

    200

    250

    300

    0 2 4 6 8 10 12

    Time since contact with chill roll, ms

    Tem

    pera

    ture

    of E

    VOH

    -tie

    Inte

    rface

    , C EVOH freezing

    LDPE, tie freezing

  • 21

    Interfacial Area Creation

    Blown film• A/Ao = (BUR)*(DDR)

    Cast film and EC• A/Ao = DDR

    A/Ao = go/g

  • 22

    Interaction of area creation and temperature in blown film

    Data from Morris, 1998 SPE ANTEC

    (45-mm HDPE - 23-mm EVOH) Blown FilmBUR = 2.2, DDR = 6, FLH (EVOH) = 20 cm

    0

    2

    4

    6

    8

    10

    12

    14

    0 0.5 1 1.5 2

    z/L

    V/V

    o, D

    /Do,

    A/A

    o

    100

    110

    120

    130

    140

    150

    160

    170

    180

    Tem

    pera

    ture

    of H

    DP

    E, C

    D/Do

    V/Vo

    A/Ao

    Temperature

  • 23

    Interaction of area creation and temperature in cast film/EC

    0

    2

    4

    6

    8

    10

    12

    14

    16

    0 0.2 0.4 0.6 0.8 1z/L

    A/A

    o

    240

    250

    260

    270

    Tem

    pera

    ture

    , C

    A/Ao

    Temperature

  • 24

    Summary

    Blown film• Rapid increase in interfacial area near frostline

    • Time available for bonding and relaxation after area creation has ceased is several orders of magnitude greater than for cast film

    Cast film• High temperatures in air gap

    • Exponential increase in interfacial area

    • Very rapid freezing – little time for reaction and relaxation after interfacial area creation has ceased.

  • 25

    Practical Implications

    Effect of Output on Peel Strength

    0

    200

    400

    600

    800

    1000

    1200

    Output (at constant air gap)

    Peel

    Str

    engt

    h, g

    /25m

    m

    Tie3

    Tie2

    Tie1

  • 26

    ConclusionsInterlayer adhesion generally increases with increasing process time

    Character of curves differ between cast film/EC and blown film

    • Cast film/EC appears to be kinetic effect; BF stress effect

    • Related to differences in

    • Time scales

    • Temperature

    • Area creation

  • 27

    Thank YouPRESENTED BYHariharan.KTechnical Specialist, Packaging & Industrial Polymers, E I DuPont India Pvt. Ltd.

    Please remember to turn in your evaluation sheet...


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