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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
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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

  1. 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

  2. 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)

  3. Ruiz, F.A., “Mineral Reinforcement of LLDPE Film, Bags, and Liners,” TAPPI Journal, 76 (1) 174 (1993).

  4. Ruiz, F. A. and Allen, C.F., TAPPI 1987 Polymers, Laminations, and Coatings Conference Proceedings, TAPPI Press, p.365.

  5. 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.

  

Heritage Plastics, Inc.
1002 Hunt Street
Picayune, MS 39466 USA
Toll Free: 1-800-245-4623
Fax: 1-601-798-1946

1-800-245-4623

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