| HS Code | 606090 |
| Density | 0.921 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 3.3 g/10 min |
| Melting Point | 124 °C |
| Vicat Softening Point | 100 °C |
| Tensile Strength At Yield | 10 MPa |
| Tensile Strength At Break | 30 MPa |
| Elongation At Break | 600 % |
| 1 Secant Modulus | 200 MPa |
| Dart Impact | 120 g |
| Haze | 3 % |
| Gloss 45 | 80 |
| Coefficient Of Friction | 0.20 |
| Seal Initiation Temperature | 105 °C |
As an accredited Braskem LH537 LLDPE Cast Film Extrusion Polyethylene factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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On high-speed rotary pallet wrappers equipped with powered pre-stretch heads operating at film feeds of 200–250 m/min, load-containment cast film derived from LH537 is typically extruded at 20–23 µm nominal gauge and slit to 500 mm machine rolls. The formulation places the base resin at 78–85 wt% of the blend, with a C6 or C8 linear low density polyethylene added at 10–15 wt% to raise dart impact and puncture resistance, and LDPE at 5–7 wt% to improve melt curtain stability and reduce neck-in across a 2 800 mm cast die. A polyisobutylene-based cling masterbatch is dosed at 1.2–1.8 wt% total compound, producing one-sided cling forces between 1.5 N and 3.5 N when tested according to ASTM D5458-16. Compliance for European machine-wrap rolls frequently references EN 14932:2018 for thermoplastic stretch films used in logistics and bale wrapping, while tensile properties are measured under ISO 527-3 at 500 mm/min and puncture resistance under ASTM D5748-18. The downstream production sequence on a cast film line uses a barrier screw at 30:1 L/D with a melt temperature of 240–260 °C, a die gap of 0.7–0.9 mm, an air gap of 120–160 mm, and a chill roll held at 18–22 °C to quench the web before downstream treatment. Slit rolls are loaded onto rotary wrappers where the film is pre-stretched at 200–250% before application; retained load after 24 h on a pallet at 23 °C must remain above 80% of initial tension in most distribution network specifications. Terminal products include 23 µm machine pallet wrap, 20 µm hand stretch wrap, and pre-stretched rolls for semi-automatic turntable wrappers; all configurations require edge trimming tolerance below ±0.5 mm to prevent slitter-induced nicks that propagate under high draw.
Slitter operators observe that a chill roll temperature excursion above 25 °C increases cling-layer transfer to the roll face within 30 min, evidenced by web wrap-around on the stripper roll; a drop in line speed below 250 m/min then produces gauge bands at ±2.0 µm. Pre-stretch equipment fitted with load cells records a retained load loss of 10–15% after 72 h creep on a pallet when outer-layer cling force falls below 1.2 N under ASTM D5458-16; above 3.5 N, tail breakage during cut-and-transfer cycles becomes more frequent. These thresholds define the operating envelope for LH537-based formulations on high-speed rotary wrappers and are not transferable to blown-film stretch hood equipment.
For fresh produce overwrap lines running at 60–120 packs/min, cast web at 12–25 µm is produced as a single-layer structure in which LH537 constitutes 92–100 wt% of the polymer phase; the balance is an antiblock masterbatch at 0.5–1.5 wt% and a slip additive at 300–800 ppm active erucamide. The relevant compliance framework for direct food contact in the United States is FDA 21 CFR 177.1520(c) for olefin polymers, with the finished film subject to the overall migration limits of EU 10/2011 when sold into European markets. Processing conditions on the cast line include a melt temperature of 225–245 °C, chill roll temperature of 14–18 °C, and air gap below 100 mm to maintain optical clarity measured at less than 5% haze under ISO 14782. The film is corona-treated online to 38–42 mN/m before slitting to width for use on horizontal form-fill-seal machines where fin-seal jaws operate at 105–125 °C and dwell times of 0.3–0.6 s. Terminal products include bakery tray overwrap, whole-produce flow packs for leafy greens requiring a respiration window in the film, and lightweight bundling films for retail food trays. The lower melt temperature compared with pallet stretch film reduces oxidative degradation in the sealant layer but narrows the die-lip shear window; line operators must maintain die pressure above 80 bar to prevent melt fracture, and with relative humidity above 60% corona-treated film should be converted within 72 h because surface energy decays below 36 mN/m on storage.
The peel force required to remove a temporary cast protective film from an anodised aluminium profile is controlled by the viscoelastic behaviour of the coextruded skin layer rather than by the bulk density of the base resin. In this structure LH537 is used at 70–80 wt% of the total extrudate as the core layer for tensile strength and puncture resistance, while the skin layer contains a metallocene plastomer at 20–30 wt% of the skin formula to produce pressure-sensitive adhesion without a separate coating step. The downstream process is a three-layer cast coextrusion line with feedblock distribution and a die width of 2 200 mm; the chill roll is run at 25–35 °C with a matte finish to control unwinding and provide a 60–90% surface contact area. Industry compliance is anchored to ASTM D3330/D3330M-04 for 180° peel adhesion from stainless steel, ISO 2409:2013 for coating/substrate interface cleanliness after removal, and ASTM D882 for tensile elongation at break. Peel forces are normally maintained between 0.8 N/25 mm and 3.0 N/25 mm depending on the substrate surface energy; values below 0.5 N/25 mm produce edge-lift on outdoor profiles, while values above 4.0 N/25 mm cause deformation of thin masking sections during high-speed application. Terminal product configurations include 60–80 µm films for anodised aluminium profiles, 40–60 µm films for stainless steel panels, and 25–35 µm films for polycarbonate sheet; each is supplied in 1 000 mm machine rolls with an application temperature range of 10–35 °C. A known operational boundary is that LH537-based protective films should not be applied to freshly painted coil coatings unless the paint supplier confirms that the cling layer does not contain low-molecular-weight species that can migrate into the coating within 72 h.
Silage bale wrap extruded from LH537 is formulated at 85–92 wt% base resin, 5–10 wt% LDPE or C8 linear density modifier, 2–4 wt% carbon black masterbatch, and 0.3–0.6 wt% hindered amine light stabiliser/UV package. The carbon black loading is not cosmetic; it maintains film integrity under ultraviolet exposure by limiting accelerated oxidative chain scission during 12-month outdoor bale storage. The material is extruded at 25 µm nominal thickness on a cast film line with a die width of 2 400 mm, an air gap of 150–200 mm, and a chill roll at 30–40 °C to reduce blocking before slitting to 750 mm bale-wrap rolls. Compliance is tested under EN 14932:2018 for thermoplastic stretch films used in agricultural baling, with tensile stress at break measured under ISO 527-3 and UV exposure under ASTM G154 cycle 1 for 500 h. Downstream bale wrappers apply the film at 55–70% pre-stretch and 4–6 film layers per bale, producing an anaerobic silage environment that limits aerobic yeast and mould proliferation. Terminal products include round bale silage wrap, haylage wrap, and tube-wrap film for silage compaction. The main processing limitation is that carbon black masterbatch at the upper end of the stated range lowers melt drawing stability; line operators should reduce line speed by 10–15% when running at 3 wt% carbon black to avoid draw resonance.
Because the cast web is intended as the heat-seal layer inside a three-component laminated pouch, seal initiation temperature and hot-tack strength are the controlling parameters for converter acceptance. LH537 is compounded at 65–80 wt% of the sealant film, with a metallocene polyethylene at 20–35 wt% to lower seal initiation to 95–105 °C and to extend hot-tack strength above 2 N/25 mm at 110 °C under ASTM F1921-24. The cast film is extruded at 20–30 µm, corona-treated to 42–46 mN/m, and adhesive-laminated to a reverse-printed polyester or metallised polyester outer web; the finished laminate must pass ASTM F88/F88M seal strength testing with values above 10 N/15 mm at 130 °C jaw temperature. Regulatory compliance for dry food pouches uses FDA 21 CFR 177.1520(c) and EU 10/2011 with fatty-food simulant D2 migration protocol where applicable, while packaging converters frequently add internal specification limits for residual solvents below 5 mg/m² under DIN 55664. Terminal product types include stand-up pouches for dry cereal, detergent refill pouches, and medical device overwrap where the sealant layer must not contaminate the sealed product. The critical processing limitation is that excessive corona dose above 50 mN/m can oxidise the surface and reduce interlayer adhesion against solvent-based adhesives by creating weak boundary layers.
In controlled-environment hygiene film converting, cast extrusion from LH537 replaces blown LDPE when the downstream operation demands gauge uniformity below ±3% across a 1 800 mm web and a low-gloss matte surface for automated diaper line feeding. The cast film formulation contains 70–85 wt% LH537, 8–15 wt% titanium dioxide white masterbatch, 1–3 wt% slip/antiblock masterbatch, and 0.05–0.10 wt% fluoropolymer processing aid to suppress die-lip build-up. The production process runs through a cast die at a melt temperature of 235–255 °C and an embossed chill roll at 22–28 °C, followed by inline slitting to 10–20 µm film and adhesive lamination to a polypropylene spunbond nonwoven. Compliance for absorbent hygiene laminates supplied in the EU relies on REACH Annex XVII substance restrictions and component testing under ISO 13934-1:2013 for tensile strength and EDANA NWSP 110.4.R0 for thickness and basis weight, rather than food-contact standards. Terminal products include non-breathable backsheet films for adult incontinence products, feminine hygiene pads, and infant diaper outer layers; the LH537 cast film is not marketed as a breathable monolithic grade, so water vapour transmission rates remain below 15 g/m²·24 h under ISO 15106-3 unless the film is microperforated downstream. The relevant processing boundary is that at line speeds below 80 m/min, the low melt tension of LH537 can cause draw resonance on a polished chill roll; an embossed roll and an air gap below 120 mm mitigate this condition.
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