Polyolefin cast film sealant webs are coextruded and quenched as an integral step in flexible packaging lines where horizontal form-fill-seal mandrels and vertical fill-seal jaws convert rollstock at speeds above 40 cycles/min. Heat seal strength is measured according to ASTM F88/F88-21 with a 25.4 mm wide specimen, a jaw dwell time of 0.5 s to 1.0 s, a sealing pressure of 0.275 MPa to 0.55 MPa, and a peel rate of 200 mm/min to 300 mm/min. The same film must simultaneously meet optical specifications expressed as haze percentage per ASTM D1003-21 and 60° gloss per ASTM D2457-13. In conventional Ziegler-Natta linear low-density polyethylene, the broad interchain comonomer distribution produces a heterogeneous crystallite population that raises seal initiation temperature and contributes extractable low-molecular-weight oligomers that can bloom to the film surface and increase haze after sealing. Metallocene-catalyzed linear low-density polyethylene, synthesized with a constrained geometry catalyst and narrow comonomer distribution, alters this trade-off because the uniform incorporation of hexene or octene into the polyethylene backbone creates a narrower melting endotherm and reduces the concentration of highly branched, low-molecular-weight extractables. On a cast film line, the molten polymer exits a flat die, contacts a polished chill roll, and is quenched rapidly enough to suppress spherulitic light scattering; this is the principal mechanism by which mLLDPE can retain optical clarity while the sealant layer still reaches plateau peel forces of 12 N/25 mm to 18 N/25 mm at sealing temperatures 10°C to 20°C below a comparable Ziegler-Natta grade. The processing difficulty is not the resin chemistry alone but the interaction of the narrow melting peak, rapid quench, additive migration, and sealing jaw dwell time on a production machine.
Differential scanning calorimetry of a 0.918 g/cm³ metallocene ethylene-octene copolymer with a melt index of 2.0 g/10 min at 190°C/2.16 kg per ASTM D1238-13 typically shows a second-heat peak melting temperature near 118°C when scanned at 10°C/min according to ASTM D3418-15. Seal initiation temperature, defined here as the jaw setpoint at which peel force reaches 4.4 N/25 mm, can fall to 95°C or lower for a 50 µm cast sealant film. This creates a process window narrower than that observed with LDPE-rich sealants because the seal strength curve steeply rises from near-zero at 90°C to plateau at 105°C. A temperature deviation of ±5°C on a vertical form-fill-seal jaw can shift seal strength from 8 N/25 mm to below 3 N/25 mm if the setpoint is positioned on the lower inflection of the curve. The same film may have a hot tack peak of 6 N/25 mm to 9 N/25 mm at 110°C to 130°C when tested under ASTM F1921/F1921-18 with a 0.5 s dwell and 0.275 MPa pressure, but the hot tack window is also compressed because the melt remains cohesive over a smaller temperature range before the seal separates under peel force. Production-scale cast film lines running these resins typically use a 75 mm primary extruder with a 30:1 L/D barrier screw, a 0.6 mm to 1.0 mm die gap, and an air gap of 10 mm to 40 mm before the chill roll. The narrow molecular weight distribution of metallocene polyethylene, often with a polydispersity index of 2.0 to 2.5, reduces shear thinning relative to Ziegler-Natta materials; capillary rheometry per ASTM D3835-16 can show shear viscosity at 1000 s⁻¹ that is 10% to 30% higher than a Ziegler-Natta LLDPE of similar melt index. This elevates melt pressure and can induce flow marks on the chill roll surface if die-lip shear stress exceeds the critical value for melt fracture. A fluoropolymer processing aid is added at 200 ppm to 1000 ppm to suppress melt fracture without a measurable increase in haze for films below 100 µm, but too high a level can form surface residues that reduce wetting tension and degrade adhesion in laminated structures. The practical operating boundary is therefore a compromise: the cast film line should be run at a melt temperature 10°C to 20°C lower than a conventional Ziegler-Natta LLDPE to stabilize the curtain against edge neck-in, while the sealant layer must still receive sufficient thermal input to destroy all prior crystallographic memory before quenching.
Surface haze in mLLDPE cast film is not governed solely by bulk crystallinity; it is also a function of the topography imparted by the chill roll and the surface-additive package. The polished chill roll can confer a surface roughness below Ra 0.05 µm, which minimizes front-surface scattering, but this same smoothness raises the static and kinetic coefficients of friction to 0.6 or higher when measured according to ISO 8295:1995. To bring static coefficient of friction into the typical packaging range of 0.2 to 0.4, formulators add erucamide or oleamide at 500 ppm to 2000 ppm and a synthetic silica anti-block at 1000 ppm to 5000 ppm. The migration of slip additive to the surface follows a diffusion-controlled process through the amorphous phase; at 23°C, the coefficient of friction may require 24 h to 72 h to stabilize after winding, and this migration can temporarily increase near-surface haze by creating a low-refractive-index boundary layer. Silica anti-block agglomerates larger than 2 µm become scattering centers under ASTM D1003-21 and are a frequent source of haze loss in otherwise clear mLLDPE films. In mLLDPE sealants, the lower level of high-molecular-weight gels and low-molecular-weight extractable species often permits a reduction in anti-block loading relative to Ziegler-Natta LLDPE because die-lip oxidation residues are lower on the chill roll. However, the operational limitation is that slip bloom is slower in high-density crystalline regions and can be arrested entirely if the film is stored below 10°C; converter trials on slitting and bag-making equipment show that blocking events increase when freshly slit mLLDPE rolls are immediately processed without a post-wind maturation step. The incompatibility of certain amide-based slip additives with upstream process aids is also a known failure mode: localized pitting on the cast roll can occur when slip-agent decomposition products volatilize at melt temperatures above 260°C, leaving deposits that transfer to the film as haze bands. Therefore, the additive package is not a minor post-formulation adjustment but a direct control variable for the observed haze after sealing.
Blending mLLDPE with Ziegler-Natta LLDPE or LDPE is frequently attempted to reduce melt viscosity, improve web stability, or lower raw-material cost. The optical penalty arises from a mismatch in both melt elasticity and comonomer distribution. Ziegler-Natta LLDPE contains a high-molecular-weight, low-comonomer fraction that crystallizes rapidly upon contact with the chill roll, creating surface protrusions and internal lamellar stacks that scatter light. LDPE introduces long-chain branching that reduces the crystallization rate and improves chill-roll gap stability, but the branched architecture broadens the seal melting range and decreases hot tack at short dwell times. The following table compiles representative directional responses for 50 µm cast sealant films; exact values vary with catalyst type, comonomer identity, additive package, and line configuration.
| Formulation | Seal initiation temperature (°C) | Plateau seal strength (N/25 mm) | Haze (%) | Hot tack peak (N/25 mm) | Static coefficient of friction |
|---|---|---|---|---|---|
| 100% mLLDPE (0.918 g/cm³, MI 2.0 g/10 min) | 95–105 | 14–18 | 2.0–3.5 | 6–9 | 0.4–0.7 |
| 80/20 mLLDPE/LDPE (0.919 g/cm³, LDPE MI 4.0 g/10 min) | 95–110 | 12–16 | 3.5–5.0 | 4–6 | 0.2–0.4 |
| 70/30 mLLDPE/Ziegler-Natta LLDPE (0.918 g/cm³, MI 1.0 g/10 min) | 105–115 | 13–17 | 5–8 | 5–7 | 0.4–0.7 |
At LDPE loadings above 30 wt%, the seal initiation temperature can broaden enough to tolerate ±10°C jaw temperature variation, but the plateau hot tack typically declines to 4 N/25 mm or lower because the long-chain branching reduces melt cohesion during the seal-opening cycle. At Ziegler-Natta LLDPE loadings above 50 wt%, haze frequently increases by more than 2 percentage points at 50 µm and the seal initiation temperature shifts upward by 10°C to 15°C, negating the mLLDPE advantage. These are property cliff-edges rather than linear responses: optical haze is relatively insensitive to Ziegler-Natta addition up to about 20 wt%, after which the coarse crystalline domains become optically dominant. Published data for this specific configuration is limited for industrial three-layer structures because proprietary masterbatch and processing-aid interactions often dominate the measured haze.
The optical and thermal history of a cast mLLDPE sealant layer is set in the first 0.1 s to 0.5 s of contact with the chill roll. For a 50 µm film exiting a die at 220°C and contacting a chill roll held at 15°C, the average cooling rate can exceed 10³ K/s when sufficient electrostatic pinning or vacuum box pressure maintains full contact. This rapid quench suppresses the growth of optically active lamellar stacks and freezes in a lower-density amorphous phase that contributes to a lower seal initiation temperature. Higher chill roll temperatures, above 30°C, reduce the quench rate and permit secondary crystallization during winding, which can increase haze by 0.5% to 1.5% in the days following production. Conversely, chill roll temperatures below 10°C can cause condensation of ambient moisture on the roll surface, producing surface defects that scatter light and create variability in seal strength. The air gap between the die lip and the chill roll must be kept between 10 mm and 40 mm to minimize curtain oscillation, because a vibrating melt curtain creates transverse thickness bands that are visible as haze lines. On coextrusion cast film lines with a 3-layer feedblock and a 1500 mm wide die, edge encapsulation of the mLLDPE sealant with a thin LDPE layer is sometimes used to stabilize the melt curtain, but the encapsulating layer can increase the surface haze of the sealant if its thickness exceeds 5 µm. The chill roll surface finish is another independent variable: a mirror-polished roll with Ra 0.02 µm to Ra 0.04 µm minimizes haze, while a matte finish roll with Ra 0.2 µm to Ra 0.4 µm reduces blocking but increases surface scattering. The selected finish therefore must be paired with anti-block loading to maintain a stable coefficient of friction without exceeding a specified haze ceiling.
Food-contact compliance for mLLDPE cast sealant films is governed by the base olefin polymer regulation rather than by a single film specification. Under FDA 21 CFR 177.1520, olefin polymers are cleared for use in contact with food when the density is between 0.85 g/cm³ and 1.00 g/cm³ and the maximum extractable fraction, where specified, meets the designated end-test condition for the intended food type. The European Union framework under Regulation (EU) 10/2011 imposes an overall migration limit of 10 mg/dm² for food-contact plastics and, for specific simulants, the result may be expressed as 60 mg/kg for foods intended for infants and young children. A cast film sealant layer based on metallocene polyethylene can demonstrate lower hexane extractables than a conventional Ziegler-Natta grade because the narrow molecular weight distribution limits the concentration of low-molecular-weight oligomers, but the converter must still validate the final laminated structure because the adhesive, printing inks, and outer substrate may contribute migrating species. The following checklist summarizes the standards and criteria used to evaluate mLLDPE cast sealant webs.
| Property | Test method | Typical criterion or reporting unit |
|---|---|---|
| Heat seal strength | ASTM F88/F88-21 | N/25 mm, minimum of 5 specimens per setpoint |
| Hot tack | ASTM F1921/F1921-18 | N/25 mm at 0.5 s dwell and 0.275 MPa |
| Haze | ASTM D1003-21 | % per thickness, typically 50 µm |
| Specular gloss | ASTM D2457-13 | 60° incidence |
| Melt flow rate | ASTM D1238-13 | g/10 min at 190°C/2.16 kg |
| Melting temperature | ASTM D3418-15 | °C, second heat at 10°C/min |
| Density | ASTM D1505-18 or ISO 1183-1:2019 | g/cm³ |
| Coefficient of friction | ISO 8295:1995 | Dimensionless static/kinetic values |
| Food contact | FDA 21 CFR 177.1520; Regulation (EU) 10/2011 | Overall migration 10 mg/dm² or 60 mg/kg as applicable |
Operational boundaries are equally important. The mLLDPE sealant layer should not be processed with amine-based antifog or antistatic concentrates that induce acid-base reactions with residual catalyst activators, because the resulting salts can migrate to the seal surface and cause haze or seal failure. Pre-drying of the resin is generally unnecessary below 0.02% moisture, but storage in unheated warehouses above 60% relative humidity can introduce surface moisture that produces bubbles in the cast film if the material is not protected by a sealed hopper with dry-air purging at −40°C dew point. In horizontal form-fill-seal converters, the seal jaw release time must be lengthened when sealing mLLDPE at temperatures below 100°C because the residual heat is lower and the seal is more sensitive to peel force immediately after jaw opening. The same film, when laminated to a metallized polyester outer web, may require a different sealant density because the heat sink of the lamination shifts the apparent seal initiation temperature by as much as 5°C to 8°C. These limitations define the practical envelope in which metallocene polyethylene delivers seal strength without haze loss: a cast film line must be operated with controlled quench, minimal additive overconcentration, and a sealing jaw temperature profile that remains inside the narrow, high-slope region of the material's seal strength curve.