SUPERLINK TM CROSS-LINKABLE ROTOMOULDING RESINS
Transcript of SUPERLINK TM CROSS-LINKABLE ROTOMOULDING RESINS
SUPERLINKTM CROSS-LINKABLE ROTOMOULDING RESINS
Bill Huang
Research Engineer
Ingenia Polymer Corp.
February 2019
Ingenia Polymers In Rotomoulding
• Ingenia is a global supplier to the rotomolding industry with a track record of developing innovative
products
• SuperlinkTM cross-linkable polyethylenes exemplify this commitment to excellence in rotomoulding.
SUPERLINKTM XLPE
• Traditional linear materials do not meet the requirements of high performance
applications including fuel and hydraulic oil tanks:
• High impact and/or low temperature impact
• Improved ESCR
• Improved temperature resistance
• Ingenia SuperlinkTM XLPE can meet these requirements either as a single layer
rotomoulded product or as part of a multilayer solution for applications requiring low
fuel permeation.
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Property ComparisonResin Type Superlink XLPE Typical LLDPE/HDPE
Density 0.943 0.932-0.942
Impact resistance (ARM test, -40 o C) (ft-lbs) >180 80-160
Brittle failure (%) 0 85%-100%
Tensile elongation (%) 800 865-1000
Flexural Modulus (psi) 110,000 88-110,000
ESCR (hrs) >1000 20-400 typical
HDT (°C)
ASTM D648 at 66psi
67 49-57
Chemical Resistance Excellent Fair
Moldability Excellent Good
Impact Strength vs Density
• Linear PE resins show a negative
correlation between impact
strength and increasing density
• SuperlinkTM XLPE shows highly
improved impact strength relative
to density as compared to linear PE
• Besides improvements in impact
strength, crosslink resins offer
improvements in several
properties…0
20
40
60
80
100
120
140
160
180
200
0.93 0.935 0.94 0.945 0.95 0.955 0.96
Im
pa
ct
Str
en
gth
(ft
-lb
s)
Density (g/cc)
Resin Density vs -40C impact Strength
Reactor resin Superlink XLPE Linear (Reactor resin)
Improved impact-
stiffness balance vs.
linear PE
What is Crosslinking?
• Crosslinking is a chemical reaction
• It is initiated by heat or temperature
• Rate is time and temperature dependent.
• It changes the composition of PE from a
collection of linear thermoplastic polymer
chain to a thermoset network chain
structure
Schematic representation of linear PE molecules
Schematic representation of XLPE molecules
Measuring Crosslinking
• Crosslinking of Superlink resins is initiated by
decomposition of peroxide
• A torque rheometer can measure crosslinking
characteristics
• Viscosity and torque will increase as crosslinking proceeds
• The time to reach a percentage (50 or 90%) of maximum torque is indicative
of the rate of cross-linking. Shorter times = higher rates
Rheology Curve
0
5
10
15
20
25
30
35
40
45
50
0 2 4 6 8 10 12 14 16 18 20 22
Time (minutes)
Torq
ue (Lb.IN
)
Measuring Crosslinking via Torque Rheometer
MHF – Plateau Torque
ML – Minimum Torque
t90 – 90% cure time
t50 – 50% cure time
ts2 – time to reach 2 in-lb above ML (Scorch Time)
Rotomolding Process and Crosslinking
• Linear PE
• Loading of powder
• Heating of mold and powder
• Fusion of resin
• Cooling
• Removal of part
• Cross-linkable PE
• Loading of powder
• Heating of mold and powder
• Fusion of resin
• Chemical crosslinking
• Cooling
• Removal of part
Rotomolding process and Crosslinking
INTERNAL AIR TEMPERATURE
TIME
TE
MP
ER
AT
UR
E
Crosslinking
Resin melting
and fusionCooling
LLDPE
XLPE
• XLPE requires a higher
peak internal air
temperature (PIAT) as
compared to linear PEs
during rotomolding
Impact Resistance vs CycleTime
Time
Imp
ac
t
Impact properties vs. cycle time
• Linear PEs are known to degrade if the rotomoulding cycle is extended. The resin ‘overcooks’,
and undergoes thermal and oxidative degradation. Impact properties are severely negatively
affected
• However XLPEs maintain their impact properties if the rotomoulding cycle is extended beyond the
full gel point.
Peroxide decomposition and crosslinking process
• Measuring gel content of finished product confirms
complete crosslinking
• The gel content is measured by dissolving the PE in
recirculating hot xylene. Linear PEs will completely
dissolve. XLPE will have a content of undissolvable ‘gel’
• A typical gel content of 70-84% indicates full cross-linking
and fully developed physical properties.
• Increased toughness
• Increased stress crack resistance
• Increased notch crack resistance
• Increased abrasion resistance
Gel test apparatus
GEL Analysis
Outside Surface
(mold)
Inside Surface
84%
79.8%
71.8%
• Due to the nature of the rotomoulding process – where heat is applied from the
outside – the part thickness has a gradient in heat history and corresponding gel
level. the gel content will be higher on the outside wall.
Property Comparison
• Superlink has been tested extensively and has a proven track record of 20+ years
• Superlink XLPE outperforms linear materials
• Superlink has also been evaluated against industry competitive XLPEs and
demonstrates superior processability and properties
• Differences between XLPE resins can be attributed to differences in:
• Base resin
• Crosslinking system (peroxide type, concentration and use of co-additives)
• Antioxidant system
• UV additives
• Pigments
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Comparison of Industry XLPEs
• Ingenia regularly benchmarks its SuperlinkTM XLPE versus industry competitors
Property Comparison
Resin Type SL110NA Competitive 1 SL110CA
Lot# 113218 (Natural) Natural 112376 (Black)
Density 0.942 0.941 0.942
Impact resistance (ARM test, -40 o C, ¼“) (ft-
lbs)
183 181 186
Tensile Strength at Yield (psi) 2921 2806 2935
Tensile Strength at Break (psi) 899 904 860
Flexural Modulus (psi) 113,000 101,200 111,800
ESCR (hrs)
100% Igepal
10% Igepal
>1000
>1000
>1000*
>1000*
>1000
>1000
HDT (°F)
ASTM D648 at 66 psi
264 psi
152
104
141*
98*
*from datasheet. All other properties measured
Comparison of Industry XLPEs
Crosslink Time (t50)
0
5
10
15
20
25
30
35
40
300 320 340 360 380 400 420
Temperature (F)
Tim
e (
min
)
Superlink 110 Competitive 1
• Rheological studies show that Ingenia
Superlink has a longer crosslinking time (t50
and t90) at lower temperatures and a similar
crosslinking time at higher temperatures to
competitive XLPE
• A lower reactivity at low temperatures allows
Superlink to fully fill the mold, fill out detail,
and fully fuse without entrapped air bubbles,
before crosslinking
• A higher reactivity at higher temperatures
allows Superlink to fully crosslink without
extended heating cycles
REACTIVITY OF CROSSLINKABLE RESINS
INCREASING TEMPERATURE
RE
AC
TIV
ITY
Superlink 110 Competitive
Crosslinking curing temperatures
Fusion and melting
temperatures
Comparison of Industry XLPEs
• Crosslinking time is inversely
proportional to reactivity.
• Superlink is less reactive at lower
temperatures and has increased
reactivity at higher temperatures
• This provides good moldability
• Good fill and detail
• Complete melting and fusion prior to
crosslinking
• Efficient molding times
Comparison of Industry XLPEs
Maximum Torque (Crosslink Density)
vs. Temperature
0
10
20
30
40
50
300 320 340 360 380 400 420
Temperature (F)
To
rqu
e (
in.l
b)
Superlink 110 Competitive 1
• Rheological studies show that
Superlink has a higher maximum
torque than industry competitive
XLPE
• Maximum torque is an indication
of crosslink density and gel
content
Comparison of Industry XLPEs
%Elongation vs QUV Exposure Time
0
100
200
300
400
500
600
700
800
900
1000
0 200 400 600 800 1000
QUV Time (hrs)
Ten
sile S
train
(%
)
SL110:113218 Competitive 1
• Ingenia has carried out extensive
long term testing of Superlink and
competitive XLPE
• Ingenia Superlink has superior
QUV resistance to industry
competitive XLPE
• All XLPEs have comparatively low UV
resistance compared to well stabilized
linear resins.
Comparison of Industry XLPEs
Tensile Elongation vs Xenon Arc Exposure Time
0
200
400
600
800
1000
0 1000 2000 3000 4000
Exposure (hrs)
Elo
ng
ati
on
(%
)
SL110NA Competitive 1
• The UV performance of
Superlink was confirmed by
Xenon Arc Weatherometer,
which is considered more
representative to real world
conditions than QUV
Comparison of Industry XLPEs
• Materials have also been
evaluated for resistance to
thermal aging
Comparison of Industry XLPEs
Different Formulation XLPE Thermal Aging
Performance at 80C
0
200
400
600
800
1000
0 5 10 15 20 25
Thermal Aging Time (Weeks)
Te
ns
ile
Elo
ng
ati
on
(%
)
SL110NA Competitive 1
• SuperlinkTM shows
equivalent performance to
industry competitive XLPE in
thermal aging tests
Long Term Testing of SuperlinkTM
• HYDROSTATIC PRESSURE TESTING (ASTM D1998/D2837)
• LTHS: LONG TERM HYDROSTATIC STRENGTH
• Samples are exposed to pressurized high temperature water for an extended
period of time
• Property that resists stress in the hoop direction generally due to hydrostatic forces
in applications such as pipe, pressure vessels or upright storage tanks
• LTHS improves as MW increases (this is why pipe is extruded from high to very high
MW resins)
• Roto XLPE is generally 30% higher LTHS vs LLDPE of similar density
• Critical for large tanks (i.e. wall thickness/material usage, process window for thick
walled parts)
Long Term Hydrostatic Testing
• Preparation of samples for LTHS
• Samples are tested until failure
Ingenia 4" PEX at 73F
y = -0.0268x + 3.3578
y = -0.031x + 3.3578
R2 = 0.8856
3.12
3.16
3.20
3.24
3.28
3.32
3.36
3.40
-1 0 1 2 3 4 5 6 7 8
Log Time (Hrs)
Log S
tress (
psi)
Predicted
(SIM slope + Burst intercept)
Burst 100,000
1674 psi
1595 psi
Long Term Hydrostatic Testing
• Testing at different pressure and temperature allows extrapolation to extended times
at lower temperatures
Ingenia 4" PEX at 150F
y = -0.0329x + 3.0986
R2 = 0.9791
2.94
2.96
2.98
3.00
3.02
3.04
3.06
3.08
3.10
0.00 0.50 1.00 1.50 2.00 2.50 3.00 3.50 4.00
Log Time (Hrs)
Log
Str
ess (
psi)
WHAT DOES ALL OF THIS MEAN TO THE MOLDERS?
• Superlink offers improved properties over linear materials for high performance
applications including large chemical tanks and fuel tanks
• Performance has been demonstrated in extensive laboratory and field testing and
supported by industry certifications:
• UNECE-R34 TUV certificate for wheel vehicle part application;
• UL94 HB burning test certificate,
• Open fire resistance testing certificate per ABYC H24 specification for marine fuel tank application
(provided on request)
• Processability and performance are improved versus industry competitive XLPE.
Molders observations
• Lower scrap rate
• Faster cycle time
• Fewer defects and rejects (Pinholes, Voids, Blemishes)
XLPE applications
• Fuel tanks for gasoline and diesel
• (single layer or part of a multilayer solution depending on local fuel permeability requirements)
• Large chemical tanks
• Road barriers
• Waste bin covers
• Go-cart bodies
• High impact doors
XLPE Grades
SL110 Series: High performance XLPE resin with wide processing window.
SL120 Series: ‘Low odor’ product
SL114 Series: High flow, high productivity grade for molding challenging product
design at very high oven temperatures, short oven times with
moderated gel content.
SL230 series: High adhesion grade for bonding to metal. Used for lining metal tanks
in order to provide excellent chemical resistance.
• Oven temperature ~510F—600F (265C to 315C)
• PIAT target: SL110 series----195C to 210C
SL120 series----195C to 205C
SL114 series----205C to 215C
SL230 series----195C to 210C
• We suggest the use of AXEL WB 4606 mold release for all SuperlinkTM resins
• 2” vent opening.
• Cycle time: ~18 to 28 minutes depending on part thickness and design, mold
specifics and oven temperature.
Processing Guidelines for SUPERLINKTM
Benefits of SuperlinkTM
Greatly improved stiffness - toughness balance as compared with LLDPE and HDPE:
Improved temperature resistance
Improved abrasion resistance
Improved stress crack resistance
propagation failure
SuperlinkTM was developed to meet the demanding requirements for applications
requiring outstanding durability, improved abrasion and scratch resistance and
improved ESCR.
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