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High
Performance Mineral Reinforcement Concentrate for
LLDPE & HMW-HDPE Blown Film Extrusion
F.
A. Ruiz
Heritage Plastics, Inc.
1002 Hunt Street
Picayune, MS 39466 USA
Abstract
________________________
LLDPE-based
pelleted calcium carbonate (CaCO3) concentrates
utilizing two different viscosity base resins were
used to add up to 20wt.% fine-ground,
surface-treated mineral to LLDPE and HMW-HDPE
Films. Film was extruded and converted into
institutional can liners on production equipment.
Concentrates based
on higher viscosity resins yielded superior impact
and tensile performance compared to those based on
lower viscosity resins. No problems with
dispersion were noted. Slightly higher melt
pressure and motor current were observed but were
still well within typical extrusion process
conditions for the type of base resins used.
________________________
Introduction
In a previous paper1 the author described the different
modifications of film properties observed
utilizing mineral reinforcement concentrates based
on three different polyolefins. The concentrate
base resin had a major effect on the film
properties obtained with each of four film resin
types. Although certain combinations of film resin
and concentrate produced outstanding film
characteristics, no one concentrate uniformly
delivered a substantial increase in performance.
This paper details
the results obtained by increasing the viscosity
and molecular weight of the carrier resin,
yielding a concentrate of higher viscosity and
lower melt index. Improvements in compounding
technology have allowed the commercial production
of highly loaded mineral concentrates with
moderately viscous carrier resins. In addition, a
calcium carbonate concentrates of 0.5 MI has an I21
of 20. This is close to the typical 1.0 MI film
grade LLDPE resin I21 of 20 – 25, and
above the 8 – 12 typical I21 values
of film grade HMW-HDPE resins. The high-load melt
index, I21, is more representative of
the shear rate experienced by the extrudate during
film processing.
Other papers2,3,4,5
have discussed the mineral factors (particle
morphology, particle size distribution, particle
surface chemistry, and chemical purity) and
polymer factors (molecular weight, molecular
weight distribution, branching type and
distribution, density/crystallinity, and polymer
chemistry, e.g. polar/non-polar) which affect the
processing and product properties with mineral
addition. Proper mixing and dispersion of the
mineral into the polymer matrix is a critical
processing factor in the complete realization of
the benefits of this technology. Commercial film
extrusion equipment in good condition with modern
screw designs has proven satisfactory in achieving
the necessary level of homogenization, even with
concentrates as low as 0.3 MI.
Discussion
Mineral
and Polymer Selection
Two LLDPE resins of 0.920ρ were chosen as
carriers for the preparation of 75% calcium
carbonate concentrates. The first was an LLDPE
chosen to yield a concentrate MI of 3.0. The
second was chosen to yield a concentrate MI of
0.5. These two concentrates are manufactured by
Heritage Plastics and HM10® and HM10HP,
respectively
A
wet-ground calcium carbonate with a 1.0µ mean
particle size (MPS) and 8µ top-cut (maximum
particle size) was selected as the reinforcing
mineral. The calcium carbonate was treated with a
fatty acid by the mineral supplier to form a
hydrophobic coating on the surface of the mineral.
This allows the polyethylene to “wet” the
mineral surface, greatly improving the dispersion
of the mineral into the polymer matrix and
processability of the mineral/PE composite.
A
total of four film trials were conducted, two each
with LLDPE and HMW-HDPE. The details of the
processing conditions employed and results
obtained are detailed below.
LLDPE
Film Extrusion and Conversion
The first LLDPE extrusion run was conducted using
these two concentrates, utilizing a 1.0MI/0.920ρ
ethylene/hexene copolymer as the film resin at 1.0
mil thickness and 1.5:1 BUR. A 114mm (4.5”)
extruder, 406mm (16”) die and in-line bag
machine were used to produce films under the
conditions listed in Table 3. Films were produced
at loadings of both 12% calcium carbonate (CaCO3)(16%
concentrate) and 20% CaCO3 (27%
concentrate).
Table
1 Processing Conditions HBC LD#5, 114mm (4.5”)
24/1 L/D Extruder, 406mm (16”) die
|
Concentrate
Type/MI
|
3.0
|
0.5
|
3.0
|
0.5
|
|
%
CaCO3
|
12
|
12
|
20
|
20
|
|
Melt
Temperature, °C
|
216
|
216
|
216
|
216
|
|
Screw
RPM
|
32
|
32
|
32
|
32
|
|
Head
Pressure, MPa
|
33.4
|
36.4
|
33.0
|
36.1
|
|
Motor
Current
|
192
|
216
|
185
|
212
|
|
Output,
kg/hr
|
144
|
144
|
144
|
144
|
Both
concentrates ran within the normal process
operating parameters of this extrusion line. As
expected, the higher viscosity concentrate
required slightly higher motor current and head
pressure at the same rates.
Table
2. Film Properties at 1.2 mil, 1.5:1 BUR
|
Concentrate
Type/MI
|
3.0
|
0.5
|
3.0
|
0.5
|
|
%
CaCO3
|
12
|
12
|
20
|
20
|
|
Dart,
g
|
435
|
615
|
446
|
>635
|
|
Elmendorf
Tear MD
|
285
|
335
|
335
|
335
|
|
g
TD
|
600
|
630
|
650
|
680
|
|
Tensile
@ Yield, MD |
8.8
|
10.4
|
8.5
|
9.2
|
|
MPa,
TD |
9.5
|
10.2
|
9.3
|
10.1
|
|
Tensile
@ Break, MD |
48.6
|
57.4
|
42.7
|
42.7
|
|
MPa,
TD |
31.4
|
36.5
|
26.8
|
29.6
|
The
films made with the higher viscosity concentrate
yield stronger films at both mineral loadings,
especially in impact performance.
A
second LLDPE extrusion run was conducted using
these two concentrates, this time utilizing a
1.0MI/0.920ρ ethylene/octene copolymer as the
film resin at 1.2 mil thickness and 2.04:1 BUR.
This time an 89mm extruder and in-line bag machine
were used to produce films under the conditions
listed in Table 3. Films were loaded with 9% CaCO3
(12% concentrate) and 15% CaCO3 (20%
concentrate).
Table
3 Processing Conditions HBC LD#7, 89mm (3.5”)
24/1 L/D Extruder, 380mm (15”) die
|
Concentrate
Type/MI
|
3.0
|
0.5
|
3.0
|
0.5
|
|
%
CaCO3
|
9
|
9
|
15
|
15
|
|
Screw
RPM
|
64
|
64
|
64
|
64
|
|
Melt
Temperature, °C
|
205
|
206
|
205
|
205
|
|
Head
Pressure, MPa
|
39.3
|
41.9
|
41.3
|
42.4
|
|
Motor
Current
|
116
|
126
|
122
|
125
|
|
Output,
kg/hr
|
144
|
144
|
144
|
144
|
As
in the first trial, more torque and pressure were
required to process the higher viscosity
concentrates, but all parameters were well within
the normal operating limits of the equipment.
Table
4. Film Properties at 1.2 mil, 1.5:1 BUR
|
Concentrate
Type/MI
|
3.0
|
0.5
|
3.0
|
0.5
|
|
CaCO3
|
9
|
9
|
15
|
15
|
|
Dart,
g
|
320
|
350
|
465
|
630
|
|
Elmendorf
Tear MD
|
435
|
475
|
475
|
470
|
|
g
TD
|
960
|
1050
|
980
|
1030
|
|
Tensile
@ Yield, MD |
7.2
|
7.7
|
7.8
|
8.3
|
|
MPa,
TD |
7.4
|
8.4
|
8.7
|
8.5
|
|
Tensile
@ Break, MD |
41.6
|
45.2
|
40.8
|
42.7
|
|
MPa,
TD |
32.1
|
34.7
|
28.3
|
31.3
|
Film
properties with the lower MI concentrate were
again much improved over the values obtained for
the higher MI version.
HMW-HDPE
Film Extrusion and Conversion
In the first HMW-HDPE trial, 13µ film was
produced at a BUR of 3.27:1 and mineral loadings
of 15% CaCO3 (20% concentrate) and 22%
CaCO3 (30% concentrate) on a 70mm
grooved-feed extruder fitted with twin 175mm dies.
Processing conditions are summarized in Table 5.
Table
5. HMW-HDPE Film Extrusion, 70mm
|
Concentrate
Type/MI
|
3.0
|
0.5
|
3.0
|
0.5
|
|
%
CaCO3
|
15
|
15
|
22
|
22
|
|
Screw
RPM
|
61
|
58
|
61
|
58
|
|
Melt
Temperature, °C
|
224
|
224
|
224
|
224
|
|
Head
Pressure. MPa
|
42.5
|
44.4
|
37.5
|
40.7
|
|
Motor
Current
|
197
|
199
|
188
|
197
|
|
Output,
kg/hr
|
245
|
234
|
252
|
242
|
The
higher viscosity concentrate yielded higher head
pressures and motor load requirements, but all
within typical operating parameters.
Table
6. Film Properties at 13µ (0.5 mil) & 3.27:1
BUR
|
Concentrate
Type/MI
|
3.0
|
0.5
|
3.0
|
0.5
|
|
%
CaCO3
|
15
|
15
|
22
|
22
|
|
Dart,
g
|
310
|
440
|
280
|
340
|
|
Tensile
@ Yield, MD |
24.6
|
28.4
|
24.2
|
27.0
|
|
MPa,
TD |
24.9
|
25.2
|
23.0
|
24.0
|
|
Tensile
@ Break, MD |
61.7
|
70.4
|
55.7
|
68.0
|
|
MPa,
TD |
55.2
|
65.6
|
44.9
|
62.7
|
The
higher viscosity concentrate yielded higher impact
and tensile strength at both mineral loadings.
A
second HMW-HDPE trial was conducted on an
identical line (70mm grooved-feed extruder fitted
with twin 175mm dies) at a target gauge of 14µ
and 3.6:1 BUR. This time a no-mineral control was
run for comparison, and all concentrates were run
at 20% addition (15% CaCO3).
Table
7. HMW-HDPE Film Extrusion, 70mm
|
Concentrate
Type/MI
|
None
|
3.0
|
0.5
|
|
%
CaCO3
|
0
|
15
|
15
|
|
Screw
RPM
|
54
|
54
|
54
|
|
Melt
Temperature, °C
|
223
|
223
|
223
|
|
Head
Pressure. MPa
|
52.0
|
45.6
|
45.4
|
|
Motor
Current
|
203
|
191
|
196
|
|
Output,
kg/hr
|
201
|
224
|
214
|
Both
concentrates reduced extruder head pressures and
motor load requirements, while increasing process
output. As expected, the improvements were not as
marked with the higher viscosity concentrate.
Table
8. Film Properties at 13µ (0.5 mil) & 3.27:1
BUR
|
Concentrate
Type/MI
|
None
|
3.0
|
0.5
|
|
%
CaCO3
|
0
|
15
|
15
|
|
Dart,
g
|
280
|
320
|
380
|
|
Tensile
@ Yield, MD |
30.0
|
19.3
|
30.0
|
|
MPa,
TD |
28.5
|
20.2
|
26.1
|
|
Tensile
@ Break, MD |
76.6
|
52.0
|
72.3
|
|
MPa,
TD |
74.4
|
47.8
|
61.7
|
While
addition of either concentrate improves the dart
impact of the film, the higher viscosity
concentrate yielded greater impact strength gain.
Of great importance is that tensile properties
remained much higher with the higher viscosity
concentrate. These properties are critical in
typical thin-gauge HDPE film applications such as
T-shirt bags and institutional can liners.
Conclusions
Calcium
carbonate mineral reinforcement improves the
ductile performance of LLDPE and HMW-HDPE films.
Increasing the viscosity/molecular weight of the
concentrate carrier resin can improve dramatically
the response of film impact and tensile properties
to mineral reinforcement. Modern film extrusion
equipment in proper operating condition has been
shown to be able to mix and disperse concentrates
of the rheological properties studied without
difficulty.
References
-
Ruiz,
F.A., “Optimizing The Benefits Of Film
Mineral Reinforcement: Interactions Of Film
And Concentrate Base Resins” TAPPI 1996
Polymers, Laminations, and Coatings Conference
Proceedings, TAPPI Press, p 344
-
Z.
Bartczak, A.S. Argon, R.E. Cohen, M. Weinberg,
“Toughness Mechanism in Semi-Crystalline
Polymer Blends: II. High Density Polyethylene
Toughened with Calcium Carbonate Filler
Particles,” Polymer, 40, pp 2347-2365
(1999)
-
Ruiz,
F.A., “Mineral Reinforcement of LLDPE Film,
Bags, and Liners,” TAPPI Journal, 76
(1) 174 (1993).
-
Ruiz,
F. A. and Allen, C.F., TAPPI 1987 Polymers,
Laminations, and Coatings Conference
Proceedings, TAPPI Press, p.365.
-
Arina,
M., and Honkanen, A., “Mineral Fillers in
Low-Density Polyethylene Films” Polymer
Engineering and Science, Vol. 19, No. 1,
30-39 (1979)
Acknowledgements
The
author wishes to acknowledge Mrs. Myra Classen and
the production personnel of Heritage Bag Company
for conducting all the extrusion trials, and staff
of Heritage Laboratories for the testing of film
properties.
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