| HS Code | 260180 |
| Density | 0.918 g/cm³ |
| Melt Flow Index | 0.8 g/10min (190°C, 2.16kg) |
| Melting Point | 123 °C |
| Vicat Softening Point | 100 °C |
| Tensile Strength At Yield | 10 MPa |
| Elongation At Break | 700 % |
| Flexural Modulus | 280 MPa |
| Izod Impact Strength | No break (23°C) |
| Brittleness Temperature | -70 °C |
| Haze | 9% |
| Gloss | 60 |
As an accredited SK LLDPE FN800 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SK LLDPE FN800 is supplied in 25 kg polyethylene-lined woven bags, palletized and stretch-wrapped for safe transport and storage. |
| Container Loading (20′ FCL) | SK LLDPE FN800, 20′ FCL container loading, secure palletized packaging, stable weight distribution, safe transport. |
| Shipping | SK LLDPE FN800 is a linear low-density polyethylene resin in pellet form, shipped in 25 kg bags. It is non-hazardous and not regulated for transport. Keep dry, avoid excessive heat and direct sunlight, and handle with care to prevent bag damage. |
| Storage | Store SK LLDPE FN800 in a cool, dry, well-ventilated area, away from direct sunlight, heat, open flames, and strong oxidizing agents. Keep containers tightly sealed to prevent moisture contamination and dust buildup. Avoid creating airborne dust; use proper grounding to prevent static discharge. Maintain moderate temperatures and follow local regulations. |
| Shelf Life | Shelf life: 12 months from manufacture if stored unopened in dry, cool conditions away from direct sunlight. |
On high-output cast stretch lines reaching 300–600 m/min, SK LLDPE FN800 is introduced as the core or backing layer in 15–25 µm machine roll film. The supplier technical datasheet lists a nominal melt flow rate of 1.0 g/10 min at 190 °C/2.16 kg per ISO 1133-1:2022 and a nominal density of 0.918 g/cm³ per ASTM D1505-18. The extruder is a 90 mm single-screw machine with 30:1 L/D and a Maddock barrier section. Back pressure is maintained at 20–30 MPa through a melt pump and an 80/120/80 mesh screen pack. Screw speed at 350 kg/h typically falls in the range of 70–90 rpm, with melt pump suction pressure kept above 5 MPa to avoid cavitation. The slot die gap is held at 0.5–0.8 mm. Melt temperature at the die is controlled to 235–250 °C; sustained operation above 260 °C increases gel count and reduces elongation at break measured under ASTM D882-18. The cast web is quenched on a chill roll at 18–24 °C. Roll temperatures below 18 °C slow the migration of cling additives, while temperatures above 24 °C raise haze measured under ASTM D1003-21. Polyisobutylene cling masterbatch is fed at 1.0–2.0 wt%, and cling force is measured after 24–72 h at 23 °C using ASTM D5458-12. Neck-in is controlled by maintaining an air gap of 15–25 mm and by reducing the melt draw ratio. Excessive draw produces transverse orientation loss that is confirmed by tensile yield anisotropy under ISO 527-3:2018. Capacitance thickness gauges across a 2,000 mm die should record a transverse thickness variation of not more than ±2%. Thickness profile is further controlled by 90–120 individually heated lip zones; deviation triggers die bolt trim adjustments. Pre-stretch units downstream elongate the web by 150–300%, so machine-direction elongation at break must exceed 300% under ASTM D882-18. If rolled film is stored below 10 °C, cling development is delayed; storage above 40 °C causes blocking. Film-to-film slip is adjusted with erucamide at 500–800 ppm, but slip bloom competes with cling additive surface population. The balance is resolved by separating the cling-rich layer from the slip-rich layer in a two-layer cast construction.
Blown film for heavy-duty sacks and industrial liners uses FN800 at 70–85 wt% blended with high-density polyethylene for creep resistance. The primary process limit is bubble stability, not melt temperature. A die diameter of 250–350 mm with a die gap of 1.8–2.5 mm and a blow-up ratio of 2.0–2.8 is operated with a frost line height of 6–9 die diameters. External and internal bubble cooling on 90–120 mm extruders with 30:1 L/D enables throughput above 350 kg/h. The short-chain branching introduced by butene comonomer reduces melt extensional viscosity under high strain, which improves draw-down but lowers bubble tension and raises sensitivity to air turbulence. Processors stabilise the bubble by raising the frost line 10–15%, not by increasing melt temperature. Melt temperature is capped at 210 °C. At 230 °C oxidative coupling raises gel count and machine-direction Elmendorf tear measured under ASTM D1922-15 declines. Diameter fluctuation above ±3% at 100 µm translates to downstream gauge variation and lower dart impact. The high-density polyethylene component is selected with a high load melt index of 5–10 g/10 min to increase melt elasticity and reduce bubble sway. Calcium carbonate masterbatch at 5–15 wt% may be added for heavy-duty liner film, but impact drops rapidly above 15 wt%. Puncture resistance of 100 µm industrial liners is measured under ASTM D5748-19 or ISO 7765-1:1988. For outdoor sacks, 2.0–3.0 wt% carbon black masterbatch is added for UV protection. On form-fill-seal bag lines, the seal initiation temperature is validated at 105–115 °C with ASTM F88/F88M-21. The machine-direction tear and transverse-direction tear imbalance is controlled by maintaining blow-up ratio below 2.8. A blow-up ratio above 3.0 overbalances transverse orientation and lowers machine-direction tear. Published FN800-specific data for this multilayer configuration is limited; therefore the processing window above must be confirmed on the target line.
Extrusion lamination with FN800 as the sealant web begins at a slot die melt temperature of 305–320 °C, which is 70–90 °C above the resin’s normal film extrusion range. The elevated temperature is specific to oxidative modification of the polyethylene melt, which increases carbonyl content at the substrate interface and raises primerless peel adhesion to aluminium foil. The die gap is set at 0.5–0.7 mm; the air gap from die lip to chill roll nip is held at 150–250 mm. The web is drawn to 15–30 µm between PET or BOPP and a chill roll at 15–20 °C. Chill roll surface finish controls haze and blocking; haze is measured under ASTM D1003-21. Peel strength is measured after 24 h on 15 mm strips using ASTM F88/F88M-21 for heat-seal testing or ASTM D1876-08 for metal-to-film bonds. A melt temperature below 290 °C creates a sharp adhesion decrease, with a process cliff-edge of less than 10 °C before sealant delamination. Butene branches allow lower coating weight than LDPE and resist draw resonance; however, primerless adhesion to aluminium foil is lower. A dilute primer is applied at 0.02–0.05 g/m² when metal peel strength must exceed 4 N/15 mm. Neck-in is quantified by the difference between die width and actual lamination width. For a 2,000 mm die, neck-in above 8–12% indicates excessive draw or low melt strength. Edge bead formation is trimmed and recycled, but recycled material from oxidised melt edges can contain gel particles that later reduce optical quality. The substrate path is tension-controlled; BOPP and PET webs are preheated by a corona treater and a back-up roll at 70–90 °C before the nip. Adhesion failure is classified as cohesive or adhesive by peel examination. Under ASTM D1876-08, a peel strength of 2–4 N/15 mm is typical for printed PET sealant webs; values below 1 N/15 mm require revalidation of melt temperature or primer deposition. The chill roll surface is cleaned to avoid polyethylene oligomer deposit; haze rises when roll build-up reaches 0.05–0.10 g/m².
White/black or white/green agricultural silage film at 150–200 µm uses a high blow-up ratio of 2.8–3.2 and a die gap of 2.0–2.5 mm. EVA is excluded in certain high-bacterial-load ensiling conditions because acetic acid generation and oxygen permeability conflict with oxygen barrier targets. FN800 is used as the core layer at 60–80 wt%, blended with an octene metallocene LLDPE at 20–40 wt% to raise dart impact and low-temperature tear resistance. The melt temperature is limited to 190–210 °C to preserve UV stabiliser activity. A HALS-based stabiliser masterbatch is added at 3–5 wt%; in black film, 2.0–3.0 wt% carbon black masterbatch is used. Outdoor durability is evaluated by retaining at least 50% of tensile elongation after 2,000 h of exposure in UV-A-340 lamps under ASTM G154-23 or ISO 4892-2:2022. The film is produced on dual-lip air ring blown film lines with internal bubble cooling to limit transverse gauge variation below ±8%. Low thickness variation is critical because silage film is stretched during wrapping. Edge tear propagation is measured under ASTM D1922-15; a blend with 20 wt% octene mLLDPE raises machine-direction tear above the butene-only baseline. The outer white layer is pigmented with titanium dioxide at 2–4 wt% to reflect radiation and reduce photodegradation; the black layer contains carbon black. The interface between layers must remain continuous; delamination is tested by peel under ASTM D1876-08. Puncture resistance after field exposure is measured by the film purchaser’s slow puncture protocol or by ISO 7765-1:1988. Bubble oscillation at ±5% diameter variation is considered unacceptable for 150 µm film because it creates thin spots during bale wrapping. Blown film collapsing frames are set at a low-angle configuration to reduce wrinkles; a web guide with ±1 mm lateral accuracy is required for winding. Published FN800-specific outdoor ageing data is limited; the stabiliser dosage and UV retention protocol must be validated on the exact film structure because additive migration under silage acid contact changes surface slip and thermal ageing.
Cast coextruded surface protection film uses a three-layer A/B/C structure with an FN800-based backing layer of 30–60 µm. The backing layer is extruded on a 90 mm main extruder at 210–240 °C; the adhesive layer is coextruded on a 65 mm satellite extruder at 200–230 °C with 5–15 wt% olefinic plastomer or ethylene-vinyl acetate copolymer. Adhesion to stainless steel is adjusted to 0.10–0.50 N/25 mm and measured at 300 mm/min peel speed under ASTM D3330-04. Backing tensile modulus is tested under ISO 527-3:2018; a machine-direction secant modulus above 200 MPa is generally required to prevent distortion during application. Elmendorf tear at 50 µm must exceed 2 N in machine direction under ASTM D1922-15. A high-resolution optical gel counter at 10 µm resolution is used after 48 h at 80 °C to detect gel formation. Chill roll temperature above 28 °C increases surface roughness and reduces adhesive wet-out. The film is corona-treated inline to 40–44 mN/m; treatment decay over 6 months is checked by wetting tension measured under ASTM D2578-17. Slip additive overdose above 800 ppm in the backing layer migrates to the adhesive interface over 14–28 days and lowers peel force by 0.05–0.15 N/25 mm. Accelerated ageing is conducted at 60 °C for 7 days under vertical rack storage; peel force change should remain within ±0.05 N/25 mm. The adhesive layer is corona-treated before lamination to a wetting tension of 38–42 mN/m measured under ASTM D2578-17. Backing film stiffness is adjusted by adding high-density polyethylene at 5–10 wt%, but this raises haze. The protection film must be free of gel particles above 150 µm because they cause point loads on polished metal or glass surfaces. The backing layer must be free of slip additives that migrate to the adhesive interface and reduce peel force below the target.
A three-layer blown sealant web uses FN800 as the heat-seal layer at 12–20 µm in a total structure of 45–70 µm. The die gap is 0.8–1.2 mm; the blow-up ratio is 2.0–2.5. Seal initiation is measured on 25 mm strips at 0.275 MPa seal bar pressure and 0.5 s dwell using ASTM F88/F88M-21. Hot tack is measured separately under ASTM F1921-20 at the same pressure. A slip additive such as erucamide at 500–1,000 ppm reduces film-to-film coefficient of friction below 0.2 measured under ASTM D1894-11; however, surface bloom raises seal initiation by 3–6 °C because the amide layer must melt or dissipate before full interdiffusion. This slip–seal trade-off is the main formulation conflict. The sealant layer is therefore designed with asymmetric additive placement: slip is confined to the skin layer and antiblock is kept below 1,000 ppm in the sealant layer. Amine-based antistatic agents are avoided in the sealant layer because their migration can lower surface tension and interfere with film-to-film seal initiation. Differential scanning calorimetry under ISO 11357-3:2018 shows a primary melting peak near 118–124 °C; seal initiation is reached when the seal bar temperature exceeds the crystalline melting onset. A dwell time of 0.3 s requires a seal bar temperature of 10–15 °C above the DSC melting peak. Blocking resistance is tested by placing two film layers under 0.5 kPa at 50 °C for 24 h; blocking force should remain below 0.1 N/25 mm. For direct food contact, the structure must comply with FDA 21 CFR 177.1520(c) olefin polymer specifications and Commission Regulation (EU) No 10/2011 Annex I Table 1, with overall migration below 10 mg/dm² under Article 12. Low-seal initiation is critical because dwell time on high-speed form-fill-seal equipment is below 0.3 s; any shift above 115 °C reduces leak-proof seal frequency below target. The coextruded structure can be further tuned by placing a metallocene LLDPE skin layer outside the FN800 sealant layer to maintain low seal initiation while improving optics.
| Measurement | Standard method | Application relevance |
|---|---|---|
| Melt flow rate | ISO 1133-1:2022 | Extruder output and melt temperature verification |
| Density | ASTM D1505-18 / ISO 1183-1:2019 | Sealant crystallinity and barrier baseline |
| Tensile modulus and elongation | ISO 527-3:2018 / ASTM D882-18 | Cast and blown film mechanical release |
| Elmendorf tear resistance | ASTM D1922-15 | Protective film and silage film edge tear |
| Dart impact | ASTM D1709-22 | Heavy-duty sack puncture resistance |
| Haze | ASTM D1003-21 | Stretch film and lamination clarity |
| Seal strength | ASTM F88/F88M-21 | Form-fill-seal and lamination bond verification |
| Food contact compliance | FDA 21 CFR 177.1520(c) / EU 10/2011 | Direct and indirect food packaging |
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SK LLDPE FN800 is a butene-copolymerized linear low-density polyethylene resin manufactured by SK Geo Centric for blown film extrusion operations in agricultural, industrial packaging, and lamination segments. The product designation belongs to the FN-series film resin family, in which the numeric block "800" denotes a melt index decade of 0.8 g/10 min and a density cluster near 0.919 g/cm³. Melt mass-flow rate is determined under ISO 1133-1:2022 at 190°C with a 2.16 kg piston load, while density is measured by ISO 1183-1 or ASTM D1505 using gradient column or pycnometer methodology. These primary specifications position FN800 in the intermediate melt strength band of LLDPE film grades: melt strength is sufficient to sustain stable bubble expansion on single-screw extruders with L/D ratios between 24:1 and 30:1, while the melt index remains low enough to permit drawdown to gauges below 25 µm on lines equipped with high-output barrier screws. Precise comonomer distribution, molecular weight distribution, and antioxidant neutralizer package are controlled by the manufacturer's proprietary specification; independent grade-specific datasets in the open literature are limited, so film property ranges should be confirmed on production-scale equipment rather than extrapolated from pellet-level metrics alone.
Butene-1 incorporation along the polyethylene backbone of FN800 generates ethyl short-chain branches that suppress lamellar thickness during quiescent crystallization and fix the density within the 0.918 g/cm³ to 0.920 g/cm³ band. For Ziegler-Natta-catalyzed butene-LLDPEs at this density, weight-average molecular weight generally falls between 80,000 g/mol and 120,000 g/mol by gel permeation chromatography using polystyrene calibration, with polydispersity index in the 3.5 to 4.5 range; however, grade-specific GPC curves for FN800 have not been published in open technical literature and should be requested from the manufacturer's technical service network. The breadth of the molecular weight distribution controls extruder backpressure and film optical properties: narrower distributions reduce haze but diminish bubble rigidity under variable ambient conditions, while broader distributions improve melt strength at the cost of gel dispersion and surface smoothness. Industrial extrusion observations on 55 mm to 90 mm single-screw blown film lines suggest that FN800 processes most consistently when melt temperature is maintained between 190°C and 220°C, with the upper boundary reduced to 205°C when post-industrial recycled content exceeds 20 wt% of the feed. The additive package used in commercial FN800 compounds typically includes a primary hindered phenolic antioxidant and an acid neutralizer; exact loading levels are not standardized across converter formulations and depend on the intended film service life.
Blown film conversion of FN800 on annular dies ranging from 150 mm to 400 mm in diameter requires disciplined management of blow-up ratio, frost line height, and air ring temperature. The low melt index supports a blow-up ratio window of 2.0:1 to 3.5:1 on dual-lip air rings with chilled process air between 8°C and 15°C; operation above 3.5:1 has been associated with bubble flutter and asymmetric frost line migration on lines lacking internal bubble stabilization cages. Die gap settings between 1.2 mm and 2.0 mm are selected for FN800 because wider gaps diminish machine-direction orientation and degrade MD tear strength, while narrower gaps elevate backpressure above 350 bar and suppress throughput at constant screw speed. Field data from Southeast Asian heavy-duty sack converters using FN800 indicate optimal frost line positioning at 6 to 10 die diameters above the air ring; lower frost lines increase the MD-to-TD tensile ratio, whereas higher frost lines reduce bubble carrying capacity and promote blocking on the collapsing frame. Tensile measurements on 50 µm film specimens per ASTM D882 at a crosshead speed of 500 mm/min yield machine-direction tensile strength at break in the 25 MPa to 35 MPa band, while transverse-direction Elmendorf tear values per ASTM D1922 generally fall between 400 g and 600 g. Converter-specific slip and antiblock loadings shift these values by up to 15 percent; published data for unmodified FN800 film is therefore insufficient for final product specification without line trials.
In agricultural film conversion, a substantial fraction of FN800 production capacity is consumed on mono-layer lines with fixed-lip dies, where gauge variation below ±5 percent across a 1,200 mm lay-flat width is reported when a static mixer is installed between the extruder gate and the die entry and when die temperature is held within ±3°C of the adapter setpoint. Greenhouse covering film produced from FN800 requires downstream compounding with hindered amine light stabilizers at loadings between 0.3 wt% and 0.8 wt%, because the base resin does not contain a UV stabilization system sufficient for multi-season exposure. Accelerated weathering per ISO 4892-2 in a xenon arc chamber at 60 W/m² irradiance in the 300 nm to 400 nm band and black panel temperature of 65°C has been used by converters to benchmark relative elongation retention; unstabilized FN800 film exhibits 50 percent loss of elongation after approximately 1,500 h of exposure, while HALS-stabilized formulations retain over 70 percent elongation beyond 3,000 h. Silage wrap producers selecting FN800 for its puncture propagation resistance typically target 25 mm probe resistance values above 3.5 N/µm using a modified ASTM D5748 protocol, though exact testing modifications vary by agricultural film converter.
FN800 serves as a skin or sub-skin layer in three- and five-layer coextruded films where EVOH or polyamide forms the core barrier. In such configurations, viscosity matching between FN800 at 0.8 g/10 min and EVOH grades at 1.6 g/10 min to 3.2 g/10 min is achieved by running the EVOH at 220°C to 235°C while holding FN800 between 195°C and 210°C. Interfacial instability presenting as wavy layer geometry develops when the skin-to-tie-layer viscosity ratio exceeds approximately 3:1; maleic anhydride-grafted LLDPE tie layers with melt indices of 0.9 g/10 min to 1.2 g/10 min are therefore preferred. Adhesion testing per ASTM F904 on corona-treated FN800 skin surfaces exceeding 40 mN/m surface energy produces peel force values above 3.5 N/15 mm, while untreated FN800 film measures 31 mN/m to 33 mN/m and is insufficient for water-based adhesive lamination or flexographic ink wetting. Production-scale coextrusion lines running FN800 in the skin layer typically employ skin-layer extruder torque capacities of 40 Nm to 60 Nm per 1,000 kg/h of throughput; undersized skin-layer extruders exhibit screw speed surging and interfacial thickness variability when the extruder operates below 40 rpm.
The comparative positioning of FN800 against adjacent LLDPE families is summarized in the table below. Values represent broadly documented industry datasets for film-grade resins and are not intended as FN800-specific certification figures; direct comparison against the manufacturer's current datasheet revision is required for contractual specification.
| Property | FN800 (C4-LLDPE) | C6-LLDPE (equivalent MFI) | LDPE film grade | Metallocene C6-LLDPE |
|---|---|---|---|---|
| MFI (g/10 min) per ASTM D1238 | 0.8 | 0.8–1.0 | 0.7–0.9 | 0.9–1.1 |
| Density (g/cm³) per ASTM D1505 | 0.918–0.920 | 0.918–0.920 | 0.922–0.924 | 0.918–0.920 |
| MD Tensile at Break (MPa) per ASTM D882, 50 µm film | 25–35 | 30–36 | 18–24 | 32–38 |
| TD Elmendorf Tear (g) per ASTM D1922 | 400–600 | 450–650 | 150–250 | 500–700 |
| Dart Impact (g) per ASTM D1709, Method A | 110–160 | 130–190 | 80–110 | 200–300 |
| Copolymer Type | Butene-1 | Hexene-1 | None (long-chain branched homopolymer) | Hexene-1 |
FN800 in pellet form is assessed for United States food contact under FDA 21 CFR §177.1520 for olefin polymers, provided the n-hexane extractable fraction at 50°C does not exceed 5.5 percent and the density conforms to the designated category for polyethylene copolymers. European Union food contact conformity is evaluated under Commission Regulation (EU) No 10/2011, with overall migration limited to 10 mg/dm² per Annex I and specific migration limits applied according to the intended food simulant. REACH registration under EC No 1907/2006 for polyethylene substances is completed through established polymer consortia; downstream importers must retain the upstream supplier's substance registration confirmation. The RoHS Directive 2011/65/EU restricts lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE in electrical equipment; FN800 in unmodified form contains none of these substances as intentional additions, but cadmium-based pigments or lead-containing heat stabilizers must never be introduced during downstream compounding where electrical and electronic market compliance is mandated. The regulatory matrix below consolidates the principal frameworks governing FN800 supply and conversion.
| Standard / Regulation | Scope | Typical FN800 Position |
|---|---|---|
| FDA 21 CFR §177.1520 | Olefin polymers – food contact articles | Conforms when hexane extractable fraction at 50°C ≤ 5.5% |
| EU No 10/2011 | Plastic food contact materials | Overall migration ≤ 10 mg/dm²; specific migration per Annex I |
| REACH EC 1907/2006 | Chemical registration | Polyethylene substance registered by consortia |
| RoHS 2011/65/EU | Hazardous substances in EEE | No restricted substances as intentional additions |
| ISO 1133-1:2022 | Melt mass-flow rate determination | Method used: 190°C, 2.16 kg |
| ASTM D1505 | Density by gradient column | Reported in g/cm³ |
| ISO 1183-1 | Density by gradient column or pycnometer | Reported in g/cm³ |
| ASTM D882 | Tensile properties of thin plastic sheeting | Type IV specimens, 500 mm/min crosshead speed |
Pre-drying of FN800 is generally unnecessary for blown film extrusion when pellet storage is maintained below 60 percent relative humidity, but moisture accumulation on pellets held in unheated silos during humid winter months has been correlated with surface defects and intermittent bubble instability. Under those conditions, hopper drying at 70°C to 80°C for 1 h to 2 h is recommended before processing. The resin is incompatible with amine-based slip additives because free amines catalyze ester hydrolysis in the presence of polar contaminants and generate fatty acid blooms on the film surface. Unneutralized acid-containing adhesion promoters are similarly incompatible in coextrusion, because protonation at the tie-layer interface reduces interlayer peel force and promotes delamination after repeated folding. Post-industrial recycled film scrap may be incorporated at addition levels up to 30 wt% without statistically significant reduction in transverse-direction tear resistance, provided the scrap is free of label adhesives and has not been UV-exposed for more than 6 months. Above 30 wt% recycled content, melt filtration through 100 µm to 150 µm screen packs is required, and output rates on 65 mm single-screw extruders decline by approximately 5 percent per 10 wt% recycled increment due to elevated melt viscosity.
For form-fill-seal machinery, heat seal initiation temperature of FN800-based blown film is a critical specification. Laboratory heat sealing at 0.5 MPa jaw pressure and 1 s dwell defines the seal initiation threshold as the temperature at which peel force reaches 2 N/15 mm per ASTM F88; for 40 µm FN800 film this threshold lies between 105°C and 115°C. This band is approximately 10°C to 15°C higher than metallocene C6-LLDPE films of equivalent density, an outcome attributable to the broader molecular weight distribution produced by the Ziegler-Natta catalyst system. High-speed vertical form-fill-seal equipment operating at dwell times as low as 0.3 s requires verification of seal bar temperature settings against this range; antiblock silica and slip agents can shift the initiation temperature upward by an additional 3°C to 5°C. Hot tack strength measured per ASTM F1921 across 110°C to 130°C for FN800 is reported by converter technical summaries to be 15 percent to 20 percent lower than C6-mLLDPE at equivalent seal temperatures, which constrains deployment on ultra-high-speed packaging lines exceeding 60 packages/min. For bag-in-box and heavy-duty sack applications operating at seal jaw temperatures of 145°C to 155°C, the seal plateau strength of 5 N/15 mm to 7 N/15 mm is reached across all LLDPE film types, eliminating this differential.