Adhesion in Extrusion Coating & Laminating - the Importance of Machine Variables. Bruce Foster Mica Corporation

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Transcription:

Adhesion in Extrusion Coating & Laminating - the Importance of Machine Variables Bruce Foster Mica Corporation

Outline Identify key factors that affect adhesion Examine Machine Variables that affect these factors

The Extrusion Coating System: Surface modifier (corona, flame, chemical primer) Secondary substrate (if extrusion lamination) ++++++++++++++++++++++++++++++++++++++++++ Extrudate (LDPE, copolymer, ionomer = adhesive) ++++++++++++++++++++++++++++++++++++++++++ Primary Substrate (paper, film, foil, fabric, etc)

Two Key Components for Adhesion 1. Intimate contact between adhesive & substrate, which permits: 2. Chemical bonding between adhesive & substrate

Factors Influencing Intimate Contact Adhesive Thickness (thicker = more easily deformed, longer solidification time) Adhesive mobility/ deformability (viscosity, modulus, solidification temp., wet-out) Substrate morphology (rough surface = less intimate contact) Substrate wettability (poor wetting = less intimate contact)

Machine Factors That Can Improve Extrudate thickness Intimate Contact Nip conditions (pressure & length) Melt temperature

Factors Influencing Chemical Bonding Degree of intimate contact Substrate surface chemistry Adhesive surface chemistry Migratory chemicals (in adhesive or substrate) Environmental stresses

Machine Factors That Can Improve Chemical Bonding Substrate treatment conditions (corona or flame power level, or primer application variables) Choice of extrudate type Extrudate thickness Air-gap distance Melt temperature of extrudate Extruder back-pressure Ozone assist

Intimate contact + Chemical bonding = Durable Adhesion

Now, Examine Each Machine Factor in More Detail

Machine Factors That Can Improve Intimate Contact 1. Extrudate thickness 2. Nip conditions (pressure & length) 3. Melt temperature

Extrudate Thickness Single most important variable in achieving good adhesion* Thicker is almost always better *(Assumption: Other extrusion conditions are in normal ranges)

Fig. 1 - Typical Adhesion Response to Coating Thickness 500 450 400 Max Peel, g/25mm 350 300 250 200 150 100 50 0 5 10 15 20 25 30 35 40 Coating Weight, gsm Ref. 1 - Foster, Bruce ; Baker, Mike, Effect of Extrusion Parameters on Adhesion of Polyester A Line Study, 2001 TAPPI Polymers, Laminations, Coatings Conference Proceedings, TAPPI PRESS, Atlanta, paper 17-2

Why Thickness is Important Transfer of thermal mass to insure intimate contact Thermal mass aids in surface oxidation of the extrudate Thicker = more compressible, important for non-smooth substrates

Why Thickness is Important Substrate >>> Extrudate Nip die Air gap Chill Roll Objective: Transfer thermal energy from die to nip

Fig. 2 - Transfer of Thermal Energy Nip Roll Position in Nip apex Chill Roll Nip impression (deformation of rubber) 0 Nip pressure max Time in Nip, msec = 60 x Nip length, mm Line speed, mpm

Transfer of Thermal Energy Solidification Model Gives Insight. 1-dimensional unsteady-state state heat conduction equation:* Model predicts solidification of polymer in the nip *Ref. 2 - Trouilhet, Yves; Morris, Barry A, Prediction of Temperature Profiles Across Coating and Substrate in the Nip, 1999 TAPPI Polymers, Laminations, Coatings Conference Proceedings, TAPPI PRESS, Atlanta, p. 457.

Fig. 3 Modeling Polymer Solidification 5 Time vs. Thickness 4.5 4 Solidification Time, msec 3.5 3 2.5 2 1.5 1 2 - Assumed Solidification Temperatures (Ts): Ts = 80 o C Ts = 100 o C 0.5 0 0 5 10 15 20 25 Chill-Roll Chill-roll side Thickness, um Substrate side

Fig. 4 Solidification Time vs. Melt Temperature msec to Solidify 5 4.5 4 3.5 3 2.5 2 1.5 1 0.5 0 300 305 310 315 320 325 330 Melt Temperature, deg C

Fig. 5 Solidification Time vs. Chill Roll Temperature msec to Solidify 5 4.5 4 3.5 3 2.5 2 1.5 1 0.5 0 25 35 45 55 65 75 85 Chill Roll Temperature, deg C

Machine Factors That Can Improve Intimate Contact 1. Extrudate thickness 2. Nip conditions (pressure & length) 3. Melt temperature

Fig. 6 Nip Conditions Nip Roll Position in Nip apex Chill Roll Nip impression (deformation of rubber) 0 Nip pressure max Time in Nip, msec = 60 x Nip length, mm Line speed, mpm

Fig. 7 Effect of Nip Length & Line Speed 12 Nip Time, msec 10 8 6 4 2 Nip Impression, mm: 20 10 5 0 100 150 200 250 300 Line Speed, mpm

Fig. 3 Solidification Time vs. Thickness 5 4.5 4 Solidification Time, msec 3.5 3 2.5 2 1.5 1 2 - Assumed Solidification Temperatures (Ts): Ts = 80 o C Ts = 100 o C 0.5 0 0 5 10 15 20 25 Chill-Roll Chill-roll side Thickness, um Substrate side

Guidelines for Nip Length & Pressure Softer Polymers (e.g.: LDPE, EVA, EMA) Longer impression, lower pressure (softer nip roll) Harder Polymers (e.g.: HDPE, PP, PET) Shorter impression, higher pressure (harder nip roll)

Machine Factors That Can Improve Intimate Contact 1. Extrudate thickness 2. Nip conditions (pressure & length) 3. Melt temperature

Melt Temperature (T) & Intimate Contact T Lower Viscosity.Yes! T Improve intimate contact?.no! Well maybe

Fig. 4 Solidification Time vs. Melt Temperature msec to Solidify 5 4.5 4 3.5 3 2.5 2 1.5 1 0.5 0 300 305 310 315 320 325 330 Melt Temperature, deg C

Melt Temperature (T) & Intimate Contact T More surface oxidation Surface oxidation Better wetting of substrate

Machine Factors That Can Improve Intimate Contact 1. Extrudate thickness 2. Nip conditions (pressure & length) 3. Melt temperature

Intimate contact + Chemical bonding = Durable Adhesion

Machine Factors That Can Improve Chemical Bonding Substrate treatment conditions (corona or flame power level, or primer application variables) Choice of extrudate type Extrudate thickness Air-gap distance Melt temperature of extrudate Extruder back-pressure Ozone assist

Substrate Treatment Treatment adds reactive sites to substrate Consult the supplier for PROPER treatment levels for your substrates Avoid over-treatment

Substrate Treatment ++++++++++++++++++++++++++++++++++++++++++ Substrate (after proper treatment) Reactive sites Corona, flame, plasma, priming + + + + + + + + + + Substrate (as received)

Substrate fracture Avoid Over-Treatment! ++++++++++++++++++++++++++++++++++++++++++ + + + + + + + + + + + + + + + + Substrate (after over-treatment) Reactive sites Excess Corona, flame, plasma, priming + + + + + + + + + + Substrate (as received)

Corona Treatment of Films Use Proper Watt-Density Watt-Density = Power / area / time Metric Units: W/m 2 /minute [KW setting x1000] / [Line Speed (m/min) x width (m)] Example: Treater is 3.0kW, line speed is 130mpm, and the treater width is 1400mm (1.4m), then the watt-density is: (3.0 x 1000) / (130 x 1.4) = 16.5 W/m 2 /min Important: You must determine optimum watt-density for each film and each set of running conditions. Some starting suggestions: BOPP films: 30 40 WD OPET films: 15 20 WD BON films: 5 15 WD

Other Treatment Methods Flame proper air/gas ratio & manifold position Chemical priming primer choice, proper amount & complete drying Plasma ask the experts!

Machine Factors That Can Improve Chemical Bonding Substrate treatment conditions (corona or flame power level, or primer application variables) Choice of extrudate type Extrudate thickness Air-gap distance Melt temperature of extrudate Extruder back-pressure Ozone assist

Choice of Extrudate (General General Rules of Thumb ) LDPE for paper, primed plastics & primed foils Acid copolymers for metal substrates & primed films Ionomers for metal & primed substrates Acrylate copolymers for PP & PET films, & primed surfaces

Machine Factors That Can Improve Chemical Bonding Substrate treatment conditions (corona or flame power level, or primer application variables) Choice of extrudate type Extrudate thickness Air-gap distance Melt temperature of extrudate Extruder back-pressure Ozone assist

Thickness, Air-Gap, Melt Temp Substrate >>> Extrudate Nip die Air gap Chill Roll

4 References: Ref. 3 - W.J. Ristey and R.N. Schroff; ; The Degradation and Surface Oxidation of Polyethylene During the Extrusion Coating Process, 1978 TAPPI Paper Synthetics Proceedings, TAPPI PRESS, Atlanta, p.267 Ref. 4 - V. Antonov and A.M. Soutar; ; Foil Adhesion With Copolymers: Time in the Air Gap, 1991 TAPPI Polymers, Laminations, and Coatings Conference Proceedings, TAPPI PRESS, Atlanta, p.553 Ref. 5 - B.A. Morris & N. Suzuki; ; The Case Against Oxidation as a Primary Factor for Bonding Acid Copolymers to Aluminum Foil, 2000 TAPPI Polymers, Laminations, and Coatings Conference Proceedings, TAPPI PRESS, AtlantaA Ref. 6 B. Foster; ; Effect of Extrusion Coating Parameters on Activation of a Primed Film, 2002 TAPPI PLACE Proceedings, TAPPI PRESS, Atlanta Paper 14-2.

Ristey & Schroff - 1978 Studied Effects of: Air-Gap Melt Temperature Thickness On These Properties: Molecular Weight Changes Surface Oxidation

Ristey & Schroff - 1978 Most Significant Conclusion: 25mm air-gap = 5.5 o C melt temp For LDPE surface oxidation between 321 338 o C

4 References: Ref. 3 - W.J. Ristey and R.N. Schroff; ; The Degradation and Surface Oxidation of Polyethylene During the Extrusion Coating Process, 1978 TAPPI Paper Synthetics Proceedings, TAPPI PRESS, Atlanta, p.267 Ref. 4 - V. Antonov and A.M. Soutar; ; Foil Adhesion With Copolymers: Time in the Air Gap, 1991 TAPPI Polymers, Laminations, and Coatings Conference Proceedings, TAPPI PRESS, Atlanta, p.553 Ref. 5 - B.A. Morris & N. Suzuki; ; The Case Against Oxidation as a Primary Factor for Bonding Acid Copolymers to Aluminum Foil, 2000 TAPPI Polymers, Laminations, and Coatings Conference Proceedings, TAPPI PRESS, AtlantaA Ref. 6 B. Foster; ; Effect of Extrusion Coating Parameters on Activation of a Primed Film, 2002 TAPPI PLACE Proceedings, TAPPI PRESS, Atlanta Paper 14-2.

Antonov & Soutar - 1991 Introduced the concept of: Time In the Air-Gap (TIAG) Simplifying Assumption: Extrudate Speed = Line Speed Then, TIAG (msec) = ~ Air-Gap (mm) x 60 Line Speed (mpm)

Antonov & Soutar - 1991 Most Significant Conclusion: Air-gap time of ca. 80 120 msec To allow oxidation of EAA & thereby get good adhesion to aluminium foil Subsequently found to be a good rule of thumb for LDPE resins

Time In the Air-Gap Has been & continues to be a useful tool for troubleshooting adhesion problems in extrusion coating & laminating processes But...

4 References: Ref. 3 - W.J. Ristey and R.N. Schroff; ; The Degradation and Surface Oxidation of Polyethylene During the Extrusion Coating Process, 1978 TAPPI Paper Synthetics Proceedings, TAPPI PRESS, Atlanta, p.267 Ref. 4 - V. Antonov and A.M. Soutar; ; Foil Adhesion With Copolymers: Time in the Air Gap, 1991 TAPPI Polymers, Laminations, and Coatings Conference Proceedings, TAPPI PRESS, Atlanta, p.553 Ref. 5 - B.A. Morris & N. Suzuki; ; The Case Against Oxidation as a Primary Factor for Bonding Acid Copolymers to Aluminum Foil, 2000 TAPPI Polymers, Laminations, and Coatings Conference Proceedings, TAPPI PRESS, AtlantaA Ref. 6 B. Foster; ; Effect of Extrusion Coating Parameters on Activation of a Primed Film, 2002 TAPPI PLACE Proceedings, TAPPI PRESS, Atlanta Paper 14-2.

Morris & Suzuki - 2000 Most significant conclusion: Oxidation is not the mechanism for EAA* adhesion to aluminium foil, but Time in the air-gap does influence the adhesion * For Nucrel grades of 9% & 12% acid

Morris & Suzuki - 2000 Another conclusion: For LDPE & low-acid EAA copolymers, Oxidation is a key mechanism for adhesion

4 References: Ref. 3 - W.J. Ristey and R.N. Schroff; ; The Degradation and Surface Oxidation of Polyethylene During the Extrusion Coating Process, 1978 TAPPI Paper Synthetics Proceedings, TAPPI PRESS, Atlanta, p.267 Ref. 4 - V. Antonov and A.M. Soutar; ; Foil Adhesion With Copolymers: Time in the Air Gap, 1991 TAPPI Polymers, Laminations, and Coatings Conference Proceedings, TAPPI PRESS, Atlanta, p.553 Ref. 5 - B.A. Morris & N. Suzuki; ; The Case Against Oxidation as a Primary Factor for Bonding Acid Copolymers to Aluminum Foil, 2000 TAPPI Polymers, Laminations, and Coatings Conference Proceedings, TAPPI PRESS, AtlantaA Ref. 6 B. Foster; ; Effect of Extrusion Coating Parameters on Activation of a Primed Film, 2002 TAPPI PLACE Proceedings, TAPPI PRESS, Atlanta Paper 14-2.

Experiment Set #1 Feb 02 Experimental Design - Modified Box-Benkin (center and edge-centers) Variables: Melt temp, Acid#, Coat Wt, Offset Fixed Line-Speed @26mpm (85fpm) & Air-Gap at 44mm (100msec) Point # Melt Temp Acid # Coat Wt Offset Adhesion Comments deg C (deg F) gsm (#/rm) (0, -0.5) (g/25mm) 1 271 (520) 0 20 (12) 0 & -0.5 0 2 271 (520) 3 10 (6) -0.5 FT @300 3 271 (520) 3 30 (18) - 4 271 (520) 9 20 (12) 0 FT @2000 5 293 (560) 0 10 (6) 0 & -0.5 FT @300 6 293 (560) 0 30 (18) 0 & -0.5 FT @900 7 293 (560) 3 20 (12) - 8 293 (560) 9 10 (6) - Degraded melt 9 293 (560) 9 30 (18) - 10 315 (600) 0 20 (12) - 11 315 (600) 3 10 (6) - 12 315 (600) 3 30 (18) - 13 315 (600) 9 20 (12) - Max T= 302 (575) - not tested

Experiment Set#2 May 02 Following are designed to vary air-gap distance & TIAG, all with LDPE only: (and the primed stock is now 4 months old!) Pt. # Melt Temp Line Speed Coat Wt Air-Gap Air Gap, Adhesion Failure deg C (F) mpm(fpm) gsm (#/rm) mm (inch) msec (g/25mm) Mode 1 293 (560) 15 (50) 10 (6) 25 (1.0) 100 40 2 293 (560) 26 (85) 10 (6) 44 (1.7) 103 35 3 293 (560) 15 (50) 10 (6) 89 (3.5) 350 300 FT 4 293 (560) 15 (50) 20 (12) 25 (1.0) 100 50 5 293 (560) 26 (85) 20 (12) 44 (1.7) 103 500 FT 6 293 (560) 26 (85) 20 (12) 64 (2.5) 147 500 FT 7 293 (560) 26 (85) 20 (12) 89 (3.5) 206 500 FT 8 293 (560) 15 (50) 20 (12) 89 (3.5) 350 500 FT 9 282 (540) 15 (50) 10 (6) 25 (1.0) 100 6 10 282 (540) 26 (85) 10 (6) 44 (1.7) 100 7 11 282 (540) 26 (85) 10 (6) 89 (3.5) 206 70 12 282 (540) 15 (50) 10 (6) 89 (3.5) 350 70 13 282 (540) 15 (50) 20 (12) 25 (1.0) 100 6 14 282 (540) 26 (85) 20 (12) 44 (1.7) 100 9 15 282 (540) 26 (85) 20 (12) 89 (3.5) 206 500 FT 16 282 (540) 15 (50) 20 (12) 89 (3.5) 350 500 FT 17 282 (540) 26 (85) 30 (18) 44 (1.7) 100 12

Carbony l Absorbance 1.4 1.2 1 0.8 0.6 0.4 Oxidation -vs- Air Gap Time 1978 Data of Ristey & Schroff 321 C (610 F) 329 C (625 F) 338 C (640 F) Power (321 C (610 F)) Power (329 C (625 F)) Power (338 C (640 F)) y = 0.0002x 1.6735 R 2 = 0.9107 y = 0.0001x 1.9016 R 2 = 0.965 y = 9E-05x 1.7915 R 2 = 0.9649 0.2 0 20 40 60 80 100 120 140 Air Gap, msec

Foster -2002 Most Significant Conclusion: (For oxidation of LDPE in air gap): Air-gap time > thickness > melt temp

Scale-Up Differences.. Parameter Line speed: Air-gap: Pilot-Line Conditions 26m/min (85ft/min) 44mm (1.75 inches) Typical Production Conditions 100-400m/min (~300-1300ft/min) 150-300mm (6-12 inches) Die shear rate: 190sec -1 500-2500sec -1

Foster 2002 Q Is die shear rate an important factor?

Recent Experiment Jan 05 Surface Oxidation -vs- Die Shear Rate 0.018 0.016 0.014 Carbonyl Absorbance 0.012 0.01 0.008 0.006 600 800 1000 1200 1400 1600 1800 Die Shear Rate, 1/s

Q Is die shear rate an important factor? A Maybe! More work needed

Machine Factors That Can Improve Chemical Bonding Substrate treatment conditions (corona or flame power level, or primer application variables) Choice of extrudate type Extrudate thickness Air-gap distance Melt temperature of extrudate Extruder back-pressure Ozone assist

Extruder Back Pressure Back Pressure: Creates more shear More polymer chain ends More oxidation More degradation! (possible heat-seal & bond aging problems)

Machine Factors That Can Improve Chemical Bonding Substrate treatment conditions (corona or flame power level, or primer application variables) Choice of extrudate type Extrudate thickness Air-gap distance Melt temperature of extrudate Extruder back-pressure Ozone assist

Ozone Assist: Ozone die Substrate >>> Nip Air gap Chill Roll

Ozone Assist Aids surface oxidation Lower melt temps and/or thinner coat weights may be possible Many References available

Conclusions Many factors affect adhesion More research needed to better understand the oxidation / mechanical process in the air-gap.