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<strong>New</strong> <strong>Stabilization</strong> <strong>Package</strong> <strong>for</strong> <strong>Controlled</strong><br />

<strong>Rheology</strong> <strong>Polypropylene</strong> Fibers<br />

(Benchmarked against Phenol & Phenol-free Systems)<br />

J. Mara 1 , H.-J. Kwon 2 , J.-D. Kim 2 , J. Bayer 3 & K. Keck 2<br />

1 Songwon International Americas; USA<br />

2 Songwon Industrial, South Korea<br />

3 Songwon International, Switzerland<br />

SPE International Polyolefins Conference 2012


• Introduction to Auto-oxidation of Polyolefins<br />

• Degradation of <strong>Polypropylene</strong> (PP)<br />

• Classification of PP Fibers (by Songwon)<br />

� <strong>Stabilization</strong> Requirements <strong>for</strong> PP Fibers<br />

� <strong>Stabilization</strong> Strategies <strong>for</strong> PP Fibers<br />

� Technical Benchmarking vs. Phenol-containing & Phenol-free Systems<br />

� Summary<br />

Contents<br />

SPE International Polyolefins Conference 2012


Introduction<br />

Simplified Auto-Oxidation Cycle of Polyolefins<br />

Polymer<br />

OH<br />

Oxygen<br />

Heat<br />

Shear<br />

UV<br />

Metal Ion (Mn + )<br />

O 2<br />

H2O None Radicalic Products<br />

*<br />

Alkyl Radical<br />

Polymer<br />

OO*<br />

Peroxy Radical<br />

O*<br />

Alkoxy Radical<br />

HO *<br />

Hydroxy Radical<br />

SPE International Polyolefins Conference 2012<br />

OOH<br />

Hydroperoxide<br />

Heat<br />

UV<br />

Polymer


Introduction<br />

Concepts to Counter Auto-Oxidation of Polyolefins<br />

Free Radical<br />

Scavenging<br />

Peroxide<br />

Decomposition<br />

Phenolic<br />

Antioxidant + → +<br />

Aminic<br />

N<br />

*<br />

R<br />

Antioxidant + → N R +<br />

Phosphite<br />

Antioxidant P + → RO P OR +<br />

Thioester<br />

Antioxidant<br />

A<br />

RO<br />

R<br />

R<br />

OH<br />

C<br />

H<br />

OR<br />

B<br />

OR<br />

S R<br />

O<br />

S<br />

R<br />

OO*<br />

OO*<br />

OOH<br />

O*<br />

+ → +<br />

OOH<br />

+ → +<br />

SPE International Polyolefins Conference<br />

A<br />

R<br />

R<br />

C<br />

OOH<br />

O<br />

OR<br />

O<br />

S<br />

O<br />

B<br />

R<br />

S R<br />

O<br />

OOH<br />

OOH<br />

OH<br />

OH<br />

OH


Introduction<br />

Polymer<br />

Radical Scavenging<br />

OH<br />

H 2O<br />

Oxygen<br />

Heat<br />

Shear<br />

UV<br />

Metal Ion (Mn + )<br />

HALS, Amine ?<br />

O 2<br />

Radical Scavenging<br />

HALS, Amine, AO<br />

Auto-Oxidation Mechanism<br />

Thermo-Oxidation<br />

*<br />

Alkyl Radical<br />

Polymer<br />

OO*<br />

Peroxy Radical<br />

O*<br />

Alkoxy Radical<br />

HO *<br />

Hydroxy Radical<br />

SPE International Polyolefins Conference 2012<br />

Radical Scavenging<br />

HALS, Amine, AO<br />

OOH<br />

Hydroperoxide<br />

Heat<br />

UV<br />

Polymer<br />

Peroxide<br />

Decomposition<br />

Phosphite, Thioester


Degradation of <strong>Polypropylene</strong><br />

• PP is an unstable substrate<br />

• Industrially unsuitable w/o stabilizers<br />

• Undergoes uncontrolled thermo-oxidative degradation w/o stabilizers<br />

• Polymerization, processing, & service life conditions can vary …<br />

SPE International Polyolefins Conference 2012


Degradation of <strong>Polypropylene</strong><br />

PP will undergo different Degradation Mechanisms:<br />

• Processing/Conversion:<br />

• Concentration [ROO*] < Concentration [R*]<br />

• MW decreases; [Mw/Mn] narrows<br />

• Disproportioning of Alkyl Radicals (<strong>for</strong>mation of c=c)<br />

• Storage/Service Life:<br />

• Concentration [ROO*] >> Concentration [R*]<br />

• MW decreases; [Mw/Mn] broadens<br />

• Formation of Carbonyl Groups<br />

• Different & Contradicting Stabilizer Reqirements<br />

SPE International Polyolefins Conference 2012


Classification of <strong>Polypropylene</strong> Fiber<br />

Monofilament<br />

Slit Tape<br />

Staple Fiber<br />

Continuous Filament<br />

Spunbond<br />

Meltblown<br />

Reactor grade<br />

Normal<br />

Can be cracked<br />

Normal to broad<br />

Normal<br />

Normal to narrow<br />

Narrow<br />

0 10 20 30 40 50 60 70 80<br />

Melt Flow MFI 230°C/2.16<br />

Typically cracked<br />

1-Step CR 2-Step CR<br />

• PP fiber grades are supplied over a range of MW’s depending upon processing &<br />

conversion characteristics as well as required properties of the application.<br />

• Songwon classifies PP fiber grades by the conversion technology & by the presence<br />

(or absence) of peroxides <strong>for</strong> controlled degradation (<strong>Controlled</strong> <strong>Rheology</strong>).<br />

• Monofilament & Tape grades have low MFI’s which need to be maintained during<br />

compounding & conversion.<br />

• Meltblown & Spunbond grades have MFI’s that must be tailored in a post reactor<br />

operation via the use of peroxides (CR grades).<br />

• Bulk continuous filament & Staple grades are available as either reactor grades or CR<br />

grades.<br />

SPE International Polyolefins Conference 2012<br />

Narrow<br />

- 1500


Classification of <strong>Polypropylene</strong> Fibers<br />

Monofilament<br />

Slit Tape<br />

Staple Fiber<br />

Continuous Filament<br />

Spunbond<br />

Reactor grade<br />

Normal<br />

Normal to broad<br />

Normal<br />

Normal to narrow<br />

Narrow<br />

Meltblown Narrow - 1500<br />

0 10 20 30 40 50 60 70 80<br />

Melt Flow MFI 230°C/2.16<br />

Reference: E.P. Moore; <strong>Polypropylene</strong> Handbook; Hanser Publishers (1996)<br />

SPE International Polyolefins Conference 2012


Classification of <strong>Polypropylene</strong> Fibers<br />

Monofilament<br />

Slit Tape<br />

Staple Fiber<br />

Continuous Filament<br />

Spunbond<br />

Reactor grade<br />

Normal<br />

Can be cracked<br />

Normal to broad<br />

Normal<br />

Normal to narrow<br />

Narrow<br />

Meltblown Narrow - 1500<br />

0 10 20 30 40 50 60 70 80<br />

Melt Flow MFI 230°C/2.16<br />

Reference: E.P. Moore; <strong>Polypropylene</strong> Handbook; Hanser Publishers (1996)<br />

SPE International Polyolefins Conference 2012


Classification of <strong>Polypropylene</strong> Fibers<br />

Monofilament<br />

Slit Tape<br />

Staple Fiber<br />

Continuous Filament<br />

Spunbond<br />

Meltblown<br />

Reactor grade<br />

Normal<br />

Can be cracked<br />

Normal to broad<br />

Normal<br />

Normal to narrow<br />

Narrow<br />

0 10 20 30 40 50 60 70 80<br />

Melt Flow MFI 230°C/2.16<br />

Reference: E.P. Moore; <strong>Polypropylene</strong> Handbook; Hanser Publishers (1996)<br />

SPE International Polyolefins Conference 2012<br />

Typically cracked<br />

1-Step CR 2-Step CR<br />

Narrow<br />

- 1500


Standard Post Reactor Extrusion<br />

Storage<br />

tank<br />

Peroxide<br />

(mainly liquid)<br />

Pump<br />

P<br />

Stabiliser & Peroxide Addition <strong>for</strong> CR-PP<br />

Stabiliser<br />

Single Additive, OPS<br />

or masterfluff<br />

Loss-in-weight<br />

feeder<br />

W W<br />

(Individual) additive streams<br />

High shear extruder<br />

Silo or<br />

discharge hopper<br />

Polymer main stream<br />

SPE International Polyolefins Conference 2012<br />

Polyolefin<br />

bulk feed<br />

Pelletizing & Storage


Separate Addition during Extrusion<br />

Storage<br />

tank<br />

Peroxide<br />

(mainly liquid)<br />

Pump<br />

P<br />

Stabiliser & Peroxide Addition <strong>for</strong> CR-PP<br />

Stabiliser<br />

Single Additive, OPS<br />

or masterfluff<br />

Loss-in-weight<br />

feeder<br />

W W<br />

High shear extruder<br />

Silo or<br />

discharge hopper<br />

Peroxide stream (first)<br />

SPE International Polyolefins Conference 2012<br />

Stabiliser stream (later)<br />

Polymer main stream<br />

Polyolefin<br />

bulk feed<br />

Pelletizing & Storage


<strong>Stabilization</strong> Requirements of PP Fibers<br />

• Excellent MW protection during compounding & conversion<br />

– Principle reason <strong>for</strong> addition of processing stabilizer<br />

• No interaction with peroxides (CR grades)<br />

– Peroxide interaction leads to strong antagonism w/processing stabilizer<br />

• Low initial color following compounding<br />

• Low color development following conversion<br />

• Low gas fade during conversion & storage<br />

– Potentially negatively affected by primary AO<br />

• Adequate storage stability (optional)<br />

• Outdoor UV stability (optional)<br />

– Easily adjustable by choice of HAS<br />

• Other (registrations, cost, industrial availability)<br />

SPE International Polyolefins Conference 2012


<strong>Stabilization</strong> Requirements of PP Fibers<br />

• Per<strong>for</strong>mance requirements <strong>for</strong> PP fiber stabilization packages vary<br />

with the conversion technology & the need <strong>for</strong> CR grades.<br />

• An overview of the importance of the various requirements <strong>for</strong> the<br />

different PP fiber grades is given below:<br />

Compounding<br />

Conversion<br />

Service Life<br />

Monofilament<br />

Tape<br />

Staple (Reactor)<br />

(B) CF (Reactor)<br />

Excellent MW Preservation P P � � � � � � �<br />

Low Peroxide Interaction P P � � � �<br />

Low Initial Colour P P � � � � � � � �<br />

Low Colour Development P P P � � � � � � � �<br />

Low Gas Fading P � � � � � �<br />

Low Smoke & Fume P � �<br />

Good MW Protection- LTTS P � � � � � � � �<br />

Good MW Protection - UV P � � � � � � � �<br />

� Very important<br />

� Suitable; usually required<br />

� Required or not depending on end application<br />

Staple - CR<br />

(B) CF-CR<br />

SPE International Polyolefins Conference 2012<br />

Spunbond-CR<br />

Meltblown-CR<br />

Remark<br />

Only colour critical applications<br />

Depending on end application


<strong>Stabilization</strong> Strategies <strong>for</strong> PP Fibers<br />

February 26 th - February 29 th , 2012<br />

3 Alternatives <strong>for</strong> PP Fibers<br />

Grade Compounding Fiber Conversion <strong>Stabilization</strong> Strategy<br />

Reactor MW Preservation MW Preservation Excellent Processing<br />

Stability<br />

1 Step CR <strong>Controlled</strong> MW Decrease MW Preservation Optimum Balance of<br />

Good Processing Stability<br />

vs. Low Peroxide Interaction<br />

2 Step CR <strong>Controlled</strong> MW Decrease <strong>Controlled</strong> MW Decrease No or Minimal<br />

Processing Stability<br />

SPE International Polyolefins Conference 2012


Selection Guide <strong>for</strong> PP Fiber Grades<br />

• Recommendations are grouped around the conversion technology & corresponding<br />

importance of stabilizer requirements as captured in previous slide.<br />

Classification<br />

Monofilament<br />

& Tape<br />

Staple - Reactor<br />

Continuous<br />

Filament (CF) -<br />

Reactor<br />

Staple - CR<br />

Continuous<br />

Filament (CF) - CR<br />

Spundbond<br />

Meltblown<br />

Songwon Product<br />

(ppm)<br />

Songnox 21B<br />

(1500 ~ 2000)<br />

Songnox 1790 + Songnox<br />

6260 [33:67](1000~1500)<br />

Songnox 21B<br />

(1500 ~ 2000)<br />

Songnox 331B<br />

(1500 ~ 2000)<br />

Songnox 3016 GR<br />

(1000 ~ 2000)<br />

Songnox 331B<br />

(1500 ~ 2000)<br />

Songnox 3016 GR<br />

(500 ~ 1500)<br />

Songnox 331B<br />

(1000 ~ 2000)<br />

Songnox 3016 GR<br />

(500 ~ 1500)<br />

Songnox 3016 GR<br />

[1:1] (300 ~ 600)<br />

Excellent MW preservation<br />

Low peroxide interaction<br />

Low initial color<br />

Low color development<br />

Criteria<br />

Low gas fading<br />

Low Fume & Smoke<br />

SPE International Polyolefins Conference 2012<br />

Good MW protection-LTTS<br />

● ○ ○ ○<br />

Good MW protection-MI<br />

Remarks<br />

Not suitable <strong>for</strong> color sensitive<br />

applications<br />

● ○ ● Severe processing condition<br />

● ○ ○ ○<br />

Not suitable <strong>for</strong> color sensitive<br />

applications<br />

● ○ ● ○ ○ ○ Offers improved color<br />

● ○ ● ● ● ● ●<br />

Offers best color<br />

● ○ ● ○ ○ ○ Offers improved color<br />

● ○ ● ● ● ● ●<br />

Best color, Excellent balance<br />

MW preservation & Low peroxide<br />

interaction<br />

● ○ ● ○ ○ ○ Offers improved color<br />

● ○ ● ● ● ● ●<br />

● ● ● ● ● ○ ○<br />

Best color, Excellent balance<br />

MW preservation & Low peroxide<br />

interaction<br />

No peroxide interaction<br />

Very good color & gasfading<br />

Low Fume & Smoke<br />

● Recommended / Fulfills criterion completely / ○ Can be used<br />

[Green: very important / critical (in general), Yellow: very important / critical (selected end application) Gray: important / useful]


Songnox 3016 Characteristics<br />

• <strong>New</strong> AO package <strong>for</strong> color critical applications, including:<br />

– PP Fiber (Bulk Continuous Filament – Reactor & CR; Staple – Reactor & CR; & Spunbond<br />

applications)<br />

– Polyolefin Film applications (Not covered today)<br />

– Polyolefin Tape applications (Not covered today)<br />

– Thin Walled Injection Molding (TWIM) applications (Not covered today)<br />

• Provides an excellent balance between Processing Stability & Low Peroxide<br />

interaction.<br />

• The interaction with peroxide is significantly reduced compared to Phenol<br />

containing systems (i.e., Songnox 321B) & Phenol-free systems, including:<br />

– Irgastab FS 533 (Composition: FS042 + I-168 + C-2020) [1:10:3]<br />

– Irgastab FS 102 (Composition: FS042 + I-168 + T-622) [1:2:1]<br />

– Irgastab FS 410 (Composition: FS042 + C-944) [1:1]<br />

• Per<strong>for</strong>mance data in PP homopolymer (gas phase) / MFI (230 C/2.16 kg) ~4 to 6<br />

[dg/min] follows…<br />

SPE International Polyolefins Conference 2012


Stabilizer Interaction with Peroxide in CR-PP<br />

No additive<br />

Songnox 3016 GR<br />

Songnox 321B<br />

Irgastab FS 533<br />

Irgastab FS 102<br />

Irgastab FS 410<br />

Substrate: PP homopolymer (gasphase)<br />

MFI 230/2.16 ~ 4 to 6 [dg/min]<br />

Compounding: N 2, 190 – 215 o C, TS<br />

Criterion: MFI after compounding<br />

4 8 12 16 20 24 28 32<br />

MFI (g/10min) 2.16kg/230 o C<br />

SPE International Polyolefins Conference 2012<br />

Stabilisation: 500 ppm Ca-stearate + 1000 ppm stabiliser<br />

Additivation: 490 ppm PO-4<br />

[2,5-Bis(t.-butylperoxy)-2,5-dimethylhexane]


Songnox 3016 GR<br />

Songnox 321B<br />

Irgastab FS 533<br />

Irgastab FS 102<br />

Irgastab FS 410<br />

Low Gas Fading in CR-PP<br />

Substrate: PP homopolymer (gasphase)<br />

MFI 230/2.16 ~ 4 to 6 [dg/min]<br />

Compounding: N 2, 190 – 215 o C, TS<br />

Exposure: 5hr at 60 o C under 5% NO x gas<br />

(KS K 0454)<br />

0 5 10 15 20 25 30<br />

Delta Yellowness Index<br />

SPE International Polyolefins Conference 2012<br />

Stabilisation: 500 ppm Ca-stearate + 1000 ppm stabiliser<br />

Additivation: 490 ppm PO-4<br />

[2,5-Bis(t.-butylperoxy)-2,5-dimethylhexane]<br />

Criterion: Delta YI


Songnox 3016 GR<br />

Songnox 321B<br />

Irgastab FS 533<br />

Irgastab FS 102<br />

Irgastab FS 410<br />

Substrate: PP homopolymer (gasphase)<br />

MFI 230/2.16 ~ 4 to 6 [dg/min]<br />

Compounding: N 2, 190 – 215 o C, TS<br />

Low Initial Color in CR-PP<br />

-4.0 -3.8 -3.6 -3.4 -3.2 -3.0<br />

Yellowness Index E 313<br />

SPE International Polyolefins Conference 2012<br />

Stabilisation: 500 ppm Ca-stearate + 1000 ppm stabiliser<br />

Additivation: 490 ppm PO-4<br />

[2,5-Bis(t.-butylperoxy)-2,5-dimethylhexane]<br />

Criterion: YI after compounding


Low Color Development during Processing<br />

Songnox 3016 GR<br />

Songnox 321B<br />

Irgastab FS 533<br />

Irgastab FS 102<br />

Irgastab FS 410<br />

Substrate: PP homopolymer (gasphase)<br />

MFI 230/2.16 ~ 4 to 6 [dg/min]<br />

Compounding: N 2, 190 – 215 o C, TS<br />

-3.0 -2.0 -1.0 0.0 1.0 2.0 3.0<br />

Yellowness Index E 313<br />

SPE International Polyolefins Conference 2012<br />

Pass 5<br />

Pass 3<br />

Pass 1<br />

Stabilisation: 500 ppm Ca-stearate + 1000 ppm stabiliser<br />

Additivation: 490 ppm PO-4<br />

[2,5-Bis(t.-butylperoxy)-2,5-dimethylhexane]<br />

Criterion: YI after multiple extursion Pass 1 ~ 5


Stabilisation of <strong>Controlled</strong> <strong>Rheology</strong> <strong>Polypropylene</strong><br />

Methodology<br />

� Radar chart<br />

� Relative scale: 5 Best (outside)<br />

4<br />

3 Intermediate<br />

2<br />

1 Worst (inside, center)<br />

SPE International Polyolefins Conference 2012


Stabilisation of <strong>Controlled</strong> <strong>Rheology</strong> <strong>Polypropylene</strong><br />

Easy Adjustment LTTS / UV<br />

Low Gas fading<br />

Excellent Processing Stability<br />

5<br />

4<br />

3<br />

2<br />

1<br />

Low Colour Development (Processing)<br />

SPE International Polyolefins Conference 2012<br />

Low Peroxide Interaction<br />

Low Initial Colour


Stabilisation of <strong>Controlled</strong> <strong>Rheology</strong> <strong>Polypropylene</strong><br />

Unstabilised <strong>Controlled</strong> <strong>Rheology</strong> PP<br />

Easy Adjustment LTTS / UV<br />

Low Gas fading<br />

Excellent Processing Stability<br />

5<br />

4<br />

3<br />

2<br />

1<br />

Low Colour Development (Processing)<br />

SPE International Polyolefins Conference 2012<br />

Low Peroxide Interaction<br />

Low Initial Colour


� Formulation:<br />

� Stabilisation Strategy:<br />

� Positioning:<br />

General Phenol Stabilizer System A<br />

� A [Songnox 317B]<br />

Composition: 3 parts SN1680 + 1 part SN1076<br />

� [Phenolic AO + Phosphite] synergism<br />

� Standard phenolic AO<br />

� Standard phosphite<br />

� Partially optimised composition & ratio<br />

� Standard AO package from IM or extrusion<br />

SPE International Polyolefins Conference 2012


Stabilisation of <strong>Controlled</strong> <strong>Rheology</strong> <strong>Polypropylene</strong><br />

A [Songnox 317B] 1000 ppm<br />

SPE International Polyolefins Conference 2012


� Formulation:<br />

� Stabilisation Strategy:<br />

� Positioning:<br />

General Phenol Stabilizer System B<br />

� B [Songnox-321B]<br />

Composition: 2 parts SN1680 + 1 part SN3114<br />

� [Phenolic AO + Phosphite] synergism<br />

� Phenolic AO with reduced color <strong>for</strong>mation<br />

� Partially optimised composition & ratio<br />

� Improved processing stability<br />

SPE International Polyolefins Conference 2012


Stabilisation of <strong>Controlled</strong> <strong>Rheology</strong> <strong>Polypropylene</strong><br />

A [Songnox 317B] 1000 ppm<br />

B [Songnox 321B] 1000 ppm<br />

SPE International Polyolefins Conference 2012


� Formulation:<br />

� Stabilisation Strategy:<br />

� Positioning:<br />

Phenol-Free Stabiliser System C<br />

� C [Hydroxylamine + HAS / FS 410]<br />

� Elimination of phenolic AO (color source)<br />

� Processing stability based only on hydroxylamine<br />

� No synergistic effect<br />

� Conversion independant of service life<br />

� Hyperactive processing stabiliser<br />

SPE International Polyolefins Conference 2012


Stabilisation of <strong>Controlled</strong> <strong>Rheology</strong> <strong>Polypropylene</strong><br />

A [Songnox 317B] 1000 ppm<br />

B [Songnox 321B] 1000 ppm<br />

C [FS 410] 1000 ppm<br />

SPE International Polyolefins Conference 2012


� Formulation:<br />

� Stabilisation Strategy:<br />

� Positioning:<br />

Phenol-Free Stabiliser System D,E<br />

� D [Hydroxylamine + Phosphite + HAS / FS 102]<br />

� E [Low hydroxylamine + Phosphite + HAS / FS 533]<br />

� Elimination of phenolic AO (colour source)<br />

� ‘‘Kinetic’’ balance Processing vs. Peroxide<br />

� Synergistic effect<br />

� Conversion independant of Service Life<br />

� C System <strong>for</strong>mulated with low level of hyperactive<br />

processing stabiliser<br />

SPE International Polyolefins Conference 2012


Stabilisation of <strong>Controlled</strong> <strong>Rheology</strong> <strong>Polypropylene</strong><br />

A [Songnox 317B] 1000 ppm<br />

B [Songnox 321B] 1000 ppm<br />

C [FS 410] 1000 ppm<br />

D [FS 102] 1000 ppm<br />

E [FS 533] 1000 ppm<br />

SPE International Polyolefins Conference 2012


� Formulation:<br />

� Stabilisation Strategy:<br />

� Positioning:<br />

<strong>New</strong> Color Critical Stabiliser System<br />

� F [Songnox 3016 GR]<br />

� Elimination of phenolic AO (colour source)<br />

� ‘‘Kinetic’’ balance Processing vs. Peroxide<br />

� Synergistic effect<br />

� Conversion independant of Service Life<br />

� No hyperactive processing stabiliser<br />

SPE International Polyolefins Conference 2012


Stabilisation of <strong>Controlled</strong> <strong>Rheology</strong> <strong>Polypropylene</strong><br />

A [Songnox 317B] 1000 ppm<br />

B [Songnox 321B] 1000 ppm<br />

C [FS 410] 1000 ppm<br />

D [FS 102] 1000 ppm<br />

E [FS 533] 1000 ppm<br />

F [Songnox 3016] 1000 ppm<br />

SPE International Polyolefins Conference 2012


Summary<br />

• PP in general must be stabilized during compounding, processing,<br />

storage, and service life.<br />

• The stabilization of CR-PP during compounding and conversion is<br />

rather complex.<br />

• While efficient protection of the PP is easily achievable via<br />

stabilizers with high molar activity & reaction kinetics, peroxides may<br />

also be added in order to degrade the PP in a controlled manner,<br />

yielding grades with lower MW & narrower MWD’s.<br />

• In this work, we introduced a powerful new AO package <strong>for</strong> CR-PP<br />

that provides excellent balance between processing stability, color<br />

suppression, and low peroxide interaction.<br />

• While the scope of today’s presentation was limited to CR-PP fiber<br />

applications, the technology is also applicable to other applications<br />

such as TWIM where low peroxide interaction and low color<br />

development are critical.<br />

SPE International Polyolefins Conference 2012


SPE International Polyolefins Conference 2012

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