pe additives overview
TRANSCRIPT
PE Additives Overview
Polyethylene Film Training Program
Additives for Polyethylene Resins
• What are additives• Selection criteria• Additive types
– Antioxidants & stabilizersPrimary antioxidantsSecondary antioxidantsUV light stabilizers
– Processing aids– Catalyst neutralizers– Slip agents– Antiblocks – Antistatic agents
• Purpose for additives• Additive mechanisms• Typical commercial additives
What Are Additives?
• Materials added to the polymer to– Provide stabilization during processing or end use– Enhance processability– Modify selected physical properties of the final PE film or molded article
• Examples– Antioxidants Reduce Gel Formation During Processing
– Processing Aids Eliminate Melt Fracture in Blown Film
– Slip Reduce COF of Films
– Release/Lubricating Agents Provide Mold Release For IM Resins
Selection Criteria for Additives
• Select the additive that provides the desired performance during processing and/or end-use in the most cost effective manner possible while meeting all safety, handling, regulatory and legal requirements
• Understanding additive mechanism important to – Proper additive selection
– Choosing appropriate concentration
– Minimizing potential interactions w/ other additives
Selection Criteria for Additives
• Additional factors in selection process– Specific customer requirements
– Unique processing conditions, unusual end-use requirements– Performance aspects
– Migration, diffusion, volatility, solubility– Additive form
– Liquid, powder, flake, granule, prill, pastille, pellet, packaging options– Method of addition
– Direct, additive pre-blend, masterblend, masterbatch, hardware requirements– Safety concerns
– Dust generation potential, minimum ignition energy (MIE)– Industrial hygiene
– Personal protective equipment (PPE) requirements, OSHA– Regulatory issues
– Chemical inventories, foodlaw, right-to-know, CONEG (heavy metals), Kosher, endocrine disrupter, BSE (mad cow)
– Legal considerations– FTO, potential patentability
– Cost/performance balance – Total formulation cost vs performance
Antioxidants for Polyolefins
• Principle antioxidant types– Classified by their stabilization chemistry
Primary antioxidants hindered phenolsSecondary antioxidants phosphites
– Other types available for specialized applications
• Why are they needed?– Minimize oxidation of PE and PP during melt processing– Extend lifetime of final product in end use application
provide long term thermal stability (LTTS)
• What do they prevent or minimize?– Excessive polymer crosslinking (MI decrease) or chain scission (MI
increase)– Gel formation– Loss of physical properties– Discoloration (in some cases)
Autoxidation CycleSimplified thermo-oxidative degradation cycle for
Non-stabilized PE
RH (polymer)
ShearHeat
R*
R*+
ROOH
+ RH + Oxygen
+ RH
Cycle 1 ROO*RO* + *OH Cycle 2
Autoxidation CycleSimplified thermo-oxidative degradation cycle for
Non-stabilized PE
RH (polymer)
ShearHeat
R*
R*+
ROOH
+ RH + Oxygen
+ RH
Cycle 1 ROO*RO* + *OH Cycle 2
1 – Polymer is exposed to shearand/or heat, which strips ahydrogen, leaving a radical
Autoxidation CycleSimplified thermo-oxidative degradation cycle for
Non-stabilized PE
RH (polymer)
ShearHeat
R*
R*+
ROOH
+ RH + Oxygen
+ RH
Cycle 1 ROO*RO* + *OH Cycle 2
2 – Polymer radical reactswith oxygen forming a peroxy group
Autoxidation CycleSimplified thermo-oxidative degradation cycle for
Non-stabilized PE
RH (polymer)
ShearHeat
R*
R*+
ROOH
+ RH + Oxygen
+ RH
Cycle 1 ROO*RO* + *OH Cycle 2
3 – Peroxy reacts with another polymermolecule creating another radical aswell as a hydro peroxide
Autoxidation CycleSimplified thermo-oxidative degradation cycle for
Non-stabilized PE
RH (polymer)
ShearHeat
R*
R*+
ROOH
+ RH + Oxygen
+ RH
Cycle 1 ROO*RO* + *OH Cycle 2
4 – By thermal or UV, the hydroperoxide can split apart
Autoxidation CycleSimplified thermo-oxidative degradation cycle for
Non-stabilized PE
RH (polymer)
ShearHeat
R*
R*+
ROOH
+ RH + Oxygen
+ RH
Cycle 1 ROO*RO* + *OH Cycle 2
5 – these species want to take a hydrogen(to make alcohol or water) from anotherpolymer molecule, resulting in another radical
6 – the number of polymer radicals continues to grow through cycle
The Problems with Radicals (R*)
In polyethylene, an R* will react with another R*, thereby making a polymer molecule with increased (almost doubled) molecular weight (“cross-linking”). This will manifest itself as a gel in the bulk film.In polypropylene, the R* will strip away the hydrogen from a tertiary carbon, thereby encouraging the splitting of the polymer backbone at that point (“chain scission”).
H H H H H HI I I I I I
— C—–C–—C–—C–—C–—C—I I I I I I
CH3 H CH3 H CH3 H
Hydrogen on tertiary carbon on PP chain
Stabilization with Hindered Phenol A/O’s
• Hindered phenol antioxidants– First line of defense stabilization
Trap alkoxy (RO*) & peroxy radicals (ROO*) Reaction results in hydroperoxide formation (ROOH)
can lead to further degradation unless secondary A/O is present
– Provide stabilization for PEAt melt processing temperaturesDuring end use at lower temperatures (LTTS)
– Can be regenerated in the polymer may react more than once
– Reaction products can cause discoloration (yellowing)
– Use of hindered phenols at low levels in some LDPE resins can cause V-gels
Stabilization Cycle - PhenolsSimplified antioxidant stabilization cycle for PE stabilized with
Hindered Phenol (ArOH) stabilizers
RH (polymer)
ShearHeat
R*
R*+
ROOH
+ RH + Oxygen
+ RH
Cycle 1 ROO*RO* + *OH Cycle 2
ArO* + ROH
+ ArOH
+ ArOH
ArO* + ROOH
Stabilization Cycle - PhenolsSimplified antioxidant stabilization cycle for PE stabilized with
Hindered Phenol (ArOH) stabilizers
RH (polymer)
ShearHeat
R*
R*+
ROOH
+ RH + Oxygen
+ RH
Cycle 1 ROO*RO* + *OH Cycle 2
ArO* + ROH
+ ArOH
+ ArOH
ArO* + ROOH
Phenolic antioxidant interrupt the cycles, preventing the formation of R*.ArO* is a relatively stable species because of its aromatic ring.
Stabilization Cycle - PhenolsSimplified antioxidant stabilization cycle for PE stabilized with
Hindered Phenol (ArOH) stabilizers
RH (polymer)
ShearHeat
R*
R*+
ROOH
+ RH + Oxygen
+ RH
Cycle 1 ROO*RO* + *OH Cycle 2
ArO* + ROH
+ ArOH
+ ArOH
ArO* + ROOH
However, peroxides are still formed
Typical Hindered Phenols Used in PE Resins
HO CH3
C
O
OH CH2CH2 O C18H37
C
O
OOH CH2CH2 CH2
4
C
BHT
Irganox® 1076Anox™ PP18Naugard® 76
Irganox® 1010Anox™ 20Naugard® 10
BHEB HO CH3C2 H5
Stabilization with Secondary AOs
• Typically are Phosphite antioxidants– Second line of defense in stabilization
decompose hydroperoxides
– Provide stabilization only at melt processing temperaturesminimal impact on LTTS
– Normally need hindered phenol antioxidant present to function
– Cannot be regenerated in the polymerneed "active" phosphite to protect polymer
– Can minimize discoloration from hindered phenol reaction products
• Optimum ratio is from 1: 4 to 1: 2 primary:secondary A/O
Stabilization Cycle – with PhosphitesSimplified antioxidant stabilization cycle for PE stabilized with both
Hindered Phenol (ArOH) and Phosphite ((ArO)3 P) Stabilizers
RH (polymer)
ShearHeat
R*
R*+
ROOH
+ RH + Oxygen
+ RH
Cycle 1 ROO*RO* + *OH Cycle 2
ArO* + ROH
+ ArOH
+ ArOH
ArO* + ROOH
+ (ArO)3 P
(ArO)3 P=O + ROH
+ (ArO)3PThe phosphite changes the peroxide to an alcohol, becoming a phosphate in the process
Typical Phosphites Used in POs
O P
3
P P OOO
OO
O
Weston® 399 (TNPP)Doverphos® 4-HRAlkanox™ TNPP
Irgafos® 168Alkanox™ 240Doverphos® S-480
Ultranox® 626Alkanox™ P-24
O ]3-PC9H19[
Effects of Antioxidants on Resin Melt Index
0.0
0.2
0.4
0.6
0.8
1.0
1.2
0 1 3 5
Mel
t Ind
ex (d
g/m
in)
250 ppm IR 1076500/500 IR 1076/Wes 399500/1000 IR 1076/Wes 399
Extrusion Pass # at 260°C (pass #0 -= Compounding at 230°C)
- Higher antioxidant loadings are better at retaining MI during multiple extrusion passes
- Phosphite A/O provides additional protection
UV Inhibitors / Light Stabilizers for PE
• Main UVI types– Classified by their stabilization mechanism
Absorbers benzophenones & benzotriazolesQuenchers organo-nickel compoundsRadical traps hindered amine light stabilizers
• Purpose– Prevent degradation of PE during exposure to UV light– HALS may also function as antioxidants at low / moderate temperatures
enhances LTTS
• Typical applications - anything used outdoors– Heavy duty bags– Agricultural films– Rotomolded parts
Typical UV/LS Used in PE Resins
Tinuvin® 622Lowilite® 62
Chimassorb™ 944Lowilite® 94
Cyasorb™ UV3346
Product Lifetimes with use of UV Stabilization
0
1000
2000
3000
4000
5000
6000
7000
0 10 20 30 40 50
Square Root [HALS Concentration (ppm)]
Tinuvin 622Chimassorb 944Tinuvin 783Tinuvin 111Chimassorb 119CGL 116Chimassorb 2020Pr
edic
ted
Life
time
(Xe
WO
M, h
rs)
- Performance ≈
square root of HALS concentration- Based on % elongation in 5 mil thick clear mLLDPE films
Discoloration of Polyethylene Products
Antioxidant interactions sometimes result in discoloration– Oxidative yellowing
• Auto-oxidation of hindered phenol A/Os can generate chromophores• Aggravated by high melt temp and air exposure during processing
– Pigment interactions• TiO2 pigments can react directly/induce oxidation of hindered phenols • Can minimize by using high quality coated TiO2 pigments
– Gas fading• NOx vapors can react with hindered phenols to create discoloration• Aggravated by the presence of basic additives such as HALS
– Cardboard yellowing• Oxidation of phenol-like materials that have migrated from cardboard
boxes • Use of PE liner will eliminate problem
Proper use of phosphite A/Os and catalyst neutralizers can minimize color formation
Gas Fade Mechanism for BHT Discoloration
CH3
hO
+ NO2 + HONO
NO2
H2 O R.T.
+ HONO
Slightly Yellow| |CH2
O⏐⏐
O⏐⏐
CH3
O⏐⏐
CH3 NO2
Conjugated Dimer
Intensely Yellow
HO
CH3
h
NOx Gas Fade Exposure Discoloration
0
2
4
6
8
10
0 25 50 75 100NOx Exposure Time (hrs)
Yello
wne
ss In
dex
NOx exposure should be minimized during polymer processing, storage & transport
Possible NOx sources include exhaust from
– Corona discharge treaters– Furnaces and gas burners– Propane-powered fork-lifts– Gasoline or diesel engines
Can reduce NOx discoloration by use of appropriate antioxidant type & level
Standard A/O package (hind. phen. + phosphite)
Standard A/O package + additional phosphite
Gas fade resistance hindered phenol + additional phosphite
Auto-oxidation of Hindered Phenol A/O
-8-6-4-202468
1012
Extrusion Pass
Yello
wne
ss In
dex
Melt processing at high temp in air can lead to auto-oxidation of hindered phenol A/O
Oxidized form of hindered phenol is more susceptible to NOx gas fading
High levels of regrind or reprocessed materials can intensify discoloration
If reprocessed materials are necessary, consider use of additional phosphite A/O
0 1 3 5
Pass 0 - Compounding @ 450°F in N2
@ 550°F in air
Polymer Processing Aids
• Purpose– Reduce / eliminate melt fracture– Increase processability
Lower melt temperatureReduce melt pressure / motor load / torque
– May reduce die buildup (blown & cast film applications)
• Function– Polymeric process aids (PPA’s) form a thin layer on film die surfaces– Coating allows molten polymer to exit die more uniformly / quickly– Slightly reduces apparent shear stress/viscosity of resin improved processability– PPA performance can be affected by
PE base resin (MI, MWD, A/O stabilization level)Concentration and degree of dispersion of the processing aid in the resin Interfering additives (antiblocks, HALS, TiO2 pigments, antistats, fillers)
Polymer Processing Aid Effect on PE Rheology
PPA reduces shear stress resulting in less melt fracture
1
10
1 10log Shear Rate
(Output)
log
Shea
r Str
ess
(Gat
e Pr
essu
re)
Smoo
th Mat
te Shar
kski
n
CM
F
“Slip
”
No PPA
w/ PPA
Typical PPAs Used in PE Resins
• Typical PPA’s used in PE resins– Fluorine based polymers like poly (vinylidene fluoride/hexafluoro propylene)
– Poly (vinylidene fluoride/hexafluoro propylene)– Dynamar® FX9613– Dupont-Dow Viton® Free Flow™ 23
– Poly (vinylidene fluoride/hexafluoro propylene) + synergist– Dynamar® FX5920A– Dupont-Dow Viton® Free Flow™ RC
– Poly (vinylidene fluoride)
– Kynar®
F
F H
H
CF3
F
F
Fn
m
Functionality of PPAs
Reference: S. Woods*, R. King**, J. Kunde; Proceeding from Polyolefin XI Conference; Houston; 1999; p. 591-610.
• PPAs function by hydrogen bonding to die surface• Oxidized PE and other additives can interfere reducing
effectiveness performance improves with clean die
OOO OOO O.. .. .. .. .. .. .. .. .. .. .. .. .. ..
: :.... .. .... .. .... OO O OOO O O O OO
H H HH H H HH
..
..
Phenol
NH
..
Hindered Amine
OP
O
ORO
HH P OR
OROR
..
Phosphite (Hydrolysis)
H2O
Fluoropolymer
OH :..
. .
: :..
F
F H
H
F
FF F
F
F
: :..: :..
..: :..: :
..: :
..: : ..: :
..
H :O:
HMoisture
H:O:
:O::O:
:O::O:
Polyethylene OxideH
:O:
:O:
Metal Stearate / Stearic Acid
Oxidized PolymerH
:O::O: :O:H
O
:O:H
MxOy (H2O)z(Partially Hydrated
Metal Oxide Surface)
MxOy (Metal OxideSub-Surface)
M (MetalSub-Surface)
Polymer Melt
Impact of A/B & TiO2 on PPA Effectiveness
• Addition of antiblock and/or TiO2 pigments often reduce the effectiveness of PPAs may require higher PPA use level
Effect of Antiblock & TiO2 on Elimination of Melt Fracture in PE Blown Films
0
20
40
60
80
100
0 20 40 60 80 100 120
Extrusion Time (min)
800 ppm PPA800 ppm PPA + 5000 ppm A/B1200 ppm PPA + 5000 ppm A/B + 3.5% TiO2
Catalyst Neutralizers• Purpose
– Neutralize trace level acidic compounds due to catalyst residues in PE Minimizes corrosion on processing equipmentImproves PE colorMinimizes side reactions between A/O’s and catalyst residues
– Mold release agents for PE injection molding and blow molding grades
• Function by neutralizing HCl resulting from catalyst residue– Ziegler catalyzed PE should contain acid neutralizer
LLDPE, MDPE & HDPE– Catalyst neutralizer not necessary for
Metallocene PE Free radical based PE (LDPE, EVA, EMA, etc)
• Typical catalyst neutralizers used PE resins– Metal stearates Calcium, Zinc– Metal oxides Zinc– Dihydrotalcites DHT-4A, L55RII
Catalyst Neutralizer Effects on Resin Color
0.0
2.0
4.0
6.0
8.0
10.0
12.0
14.0
16.0
18.0
w/o Zinc Stearate w/ 500 ppm Zinc StearateAdditive Formulation
(Base Stabilization = 500 / 1000 ppm Irganox 1076 / Irgafos 168)
1st Pass
5 th Pass
Yello
wne
ss In
dex
- Addition of neutralizer greatly helps reduce discoloration
Slip Additives
• Purpose– Reduces the coefficient of friction (COF) of blown film surfaces– May also function as an antiblock (reducing film reblock) although excessive levels may
actually cause blocking
• Function– Incompatible slip additive begins migration to surface as film is extruded– Slip molecules form crystallized layer on surfaces of extruded film– Solidified layer results in smoother/firmer film surface thereby reducing COF
• Typical slip additives– Fatty amides with alkyl chain length ranging from C18 to C22– May be totally saturated or contain 1 or more unsaturation groups (C=C)– Best overall slip additive is erucamide (C22:1)
Typical Slip Additives Used in PE Resins
NH2
O
O
NH2
O
NH2
Stearamide (C18:0)Kemamide® S, Crodamide® SR
Oleamide (C18:1)Kemamide® U, Crodamide® OR
Erucamide (C22:1)Kemamide® E Ultra, Crodamide® ER,
Armoslip® E
Functionality of Slip Additives
Schematic of slip migration mechanism
Additive in molten polymer
Migrationafter solidification
Equilibriumafter time
COF Measurement
Measured by sled test
Test reference: ASTM D-1894A lower numerical value of COF is called “low COF”but represents the “high slip” film
Diagram from ASTM procedure
COF Development with Time and Type
0.00
0.20
0.40
0.60
0.80
0.1 1.0 10.0 100.0 1000.0
Elapsed Time (hrs)
CO
F
StearamideOleamideErucamide
Slip agents bloom (migrate to the surface) with time
Saturated amides (such as Stearamide)yield higher COFs than unsaturatedamides (such as Oleamide)
Oleamide (C18) blooms faster thanerucamide (C22) due to its lower molecular wt but eventually results in a higher COF(on an equal weight basis)
COF Development with Additive Level
Increasing the slip agent levelwill generally reduce COF
Too much slip additive can also make the film surface tacky and start toincrease the COF. This typically does not happen with the levels present inresin but can occur if a film producer adds additional slip agent.
0.00
0.20
0.40
0.60
0.1 1.0 10.0 100.0 1000.0
Elapsed Time (hrs)
CO
F
500 ppm Oleamide
1000 ppm Oleamide
500 ppm Erucamide
1000 ppm Erucamide
Slip Requirements for Various Film Gauges
0.0
0.2
0.4
0.6
0.8
1.0
0 20 40
Film Gauge (micron)
CO
F
For given amount of slip additive in resin, COF generally decreases with increased film thickness
– decreasing surface/volume ratio– more slip additive available for
migration to film surface
At certain film thickness, surface will be entirely covered with slip agent and there will be no further reduction in COF
- Base resin 2 MI, 0.922 LDPE- 500 ppm slip
Slip Agents in Coextruded Films
Generally, slip agents are used in the skin layers of a coextruded film and migrate from there to coat the film’s surface.To the first order, COF of the film is based on the thickness and slip agent level of the skin layer, not the overall structure.It is possible to make films with a low COF on one side and a high COF on the other, by including the slip agent only in the skin layer of the low COF side.Although, the slip agent wants to migrate out of the PE, it willoccasionally have low level migration to an adjacent layer whichdoesn’t have slip. This is called “Scalping”. It can be addressed by adding a low level (~100 ppm) of slip to that layer or by using a higher density resin in that layer.
Common Problems with Slip AdditivesSome common problems seen with the use of slip additives
– Slip concentration too high• Poor ink adhesion• Film blocking• Build-up on processing equipment• Color formation• Poor hot tack strength/sealing
– Slip concentration too low• High COF
– High film drag (sticking) during converting– Films sticking in end use
• Film blocking
Antiblock Additives
• Purpose– Reduce the blocking force needed to separate two films (blocking and reblock)– May also reduce film COF
• Function– Traditional antiblocks are non-migratory and function by roughening film surface with
numerous discrete particles (~1- 20 µm) – Organic antiblocks (saturated slip additives) function by forming layer on outer surface
reducing film to film adhesion
• Typical antiblock additives– Minerals of various types which are mined and classified by size. Some are surface
treated– Saturated fatty amides (stearamide & behenamide)– Organic non-migratory antiblocks based upon silicone or methacrylate specialty
polymers
Typical Antiblocks Used in PE Resins
• Antiblocks used in PE resins– Diatomaceous Earth (Silica A/B) Superfloss®, Micro-Ken™– Talc ABT2500, Clear-Bloc® 80– Treated Talc Optibloc®, Polybloc®– Kaolin (China clay) Polestar®– Nepheline Syenite Minex®– Fumed Silica Sylobloc®
• Selection is based upon – Film properties (blocking, COF, optics, physical properties)– Dispersability– Abrasiveness– Physical handling characteristics– Industrial hygiene
Antiblock Size and Shape
The antiblock size and shape is determined by the mineral type as well as grinding / classification process
Talc is a ‘platy’ mineral so it yields a flat antiblock particle, while diatomaceous earth shows range of diatom particle morphologies.
Superfloss (DE)ABT-2500 (untreated talc)
Antiblock Size
Antiblock suppliers specify an average or median particle size as well as a top size.
Too large a particle can cause gels, film breaks, screen pack pluggage and may be optically unappealing.Too small a particle will be ineffective for blocking resistance.
ABT-2500 particle size distribution
Typically, the median particle size of antiblocks is 2-5 μm, with a top sizeof 20-30 μm.
Functionality of Antiblock Additives
Polyethylene films with smooth surfaces tend to stick together, or “block”
Antiblocks disrupt the film surface to prevent blocking
Antiblocks Roughen Film Surfaces
Antiblock additives roughen the surface of an otherwise smooth plastic film
The rougher film surface also shows up as a lowered gloss for the sample
LL1002KW Film with kaolin antiblock
Effect of Antiblock Type & Level on Blocking
- Base resin 1 MI, 0.917 Exceed mLLDPE, 0.9 mil films
0
20
40
60
80
100
120
0 1000 2000 3000 4000 5000 6000 7000 8000
Antiblock Concentration (ppm)
TalcTreated TalcNo A/B Line
Effect of Antiblock Type & Level on Haze
- Base resin 1 MI, 0.917 Exceed mLLDPE, 0.9 mil films
2
4
6
8
10
12
0 1000 2000 3000 4000 5000 6000 7000 8000
Antiblock Concentration (ppm)
Talc
Treated Talc
No A/B Line
Combined Effects of Slip and Antiblock
0.0
0.2
0.4
0.6
0.8
1.0
0 500 1000Slip Level (ppm)
CO
F
0
100
200
0 2000 4000Antiblock Level (ppm)
Reb
lock
(g)
No antiblock1000 ppm antiblock
No slip500 ppm slip
Antistatic Agents
• Purpose– Dissipate static charge which may accumulate on PE films or molded articles
Minimizes dust accumulation on final articleUsed more frequently in injection or blow molded PE resins
– At low levels, may be used as catalyst neutralizer
• Function– Traditional antistats function by migrating to surface of PE film or molded article and
forming thin layer– Hygroscopic nature of antistat attracts moisture from the air which dissipates static
charge requires certain humidity level to function effectively– Non-hygroscopic antistats are available for specialty applications
• Potential problems– If antistat agent concentration is too high may cause problems
– Tacky (blocky) films– Printing issues (ink adhesion)
Typical Antistatic Agents Used in PE Resins
• Types of antistats– Ethoxylated amines Atmer® AS974, Armostat® 310
Atmer® AS990, Armostat® 1800
– Polyethylene glycols Carbowax® PEG
– Glycerol derivatives Dimodan, Atmer® 122
• Selection is based upon – Static dissipation performance
– Foodlaw (FDA) restrictions
Additives Found in End-use Applications• Fillers
– Usually finely divided inorganic solids used to improve polymer properties or reduce costs
– Examples - calcium carbonate, kaolin, talc
• Pigments– Used to add color to polymer product and may also provide UV protection– Examples - titanium dioxide, carbon black, chromium oxide, iron oxide
• Antifog agents– Used in packaging and greenhouse films to impart hydrophilicity to film
surface and promote the formation of a continuous,less opaque film of water
– Examples - fatty acid esters (e.g. polyoxyethylene sorbitan ester, Atmer® 112, POE sorbitan derivatives)
Summary
• Many different additive types needed for different polyethylene end-uses– Antioxidants, primary and secondary
Prevent polymer degradation during processing and long term– UV light stabilizers
Prevent degradation during long term exposure to sunlight– Processing aids
Minimize melt fracture during processing– Catalyst neutralizers
Prevent corrosion, discoloration– Slip agents
Control COF for more efficient converting– Antiblocks
Prevent films from sticking to themselves– Antistatic agents
Eliminate static, prevent dust accumulation• Key reasons for selecting an additive
– Selection based upon polymer requirementsProvide stabilization during processing or end useEnhance processabilityModify selected physical properties of the final film or article
Summary
• Numerous additional factors in selection process– Specific customer requirements– Performance aspects – Additive form– Method of addition– Safety concerns– Industrial hygiene– Regulatory issues– Legal considerations– Cost/performance balance
• Overall goal is to provide the desired performance in the most cost effective manner possible while meeting all safety, handling, regulatory and legal requirements