) 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.