| HS Code | 260610 |
| Thickness | 76.2 µm |
| Density | 0.920 g/cm³ |
| Yield | 14.3 m²/kg |
| Tensile Strength At Break Md | 26 MPa |
| Tensile Strength At Break Td | 24 MPa |
| Elongation At Break Md | 600% |
| Elongation At Break Td | 700% |
| Tear Strength Md | 200 g |
| Tear Strength Td | 300 g |
| Dart Drop Impact | 120 g |
| Haze | 10% |
| Gloss 45 | 60 |
| Coefficient Of Friction | 0.2 |
| Melting Point | 120 °C |
| Vicat Softening Point | 100 °C |
As an accredited DuPont™ Sclairfilm® LX-3 LLDPE Film, Laminating, 76.2 µm Thickness factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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When a 76.2 µm LLDPE web is positioned as the sealant ply in a laminated food-contact pouch, the converting sequence begins with incoming roll inspection rather than lamination itself. In a duplex or triplex adhesive-laminated construction, the film is unwound at 80–120 N/m tension and passed through a bare-roll corona treater set to a discharge energy density of 2.0–3.0 W·min/m²; wetting tension is checked with formamide–ethylene glycol monomethyl ether solutions per ASTM D2578, and rolls measuring below 38 mN/m are rejected before solventless polyurethane adhesive is applied. On a production-scale five-roll solventless laminator running at 180–250 m/min, adhesive coat weight is maintained between 1.5 g/m² and 1.8 g/m², with transfer roll temperature at 40–45 °C and nip roll pressure at 3–4 bar; a 76.2 µm web is paired with 12 µm BOPET or 20 µm BOPP through the nip, and primary film tension is reduced to 60–80 N/m because LLDPE elongation at yield can exceed 15% under high draw. The laminated reel is then cured at 35–40 °C for 24–48 h until aromatic primary amine migration falls below the limit specified in EU Regulation 10/2011 Annex II; the food-contact surface of the LLDPE layer is supported by FDA 21 CFR 177.1520(c) when the olefin polymer complies with extractables limits for fatty and aqueous simulants. Heat sealing is performed on rotary jaw or bar sealers at 115–135 °C jaw temperature, 0.5–1.0 s dwell, and 0.28–0.41 MPa jaw pressure; a seal strength below 8 N/25 mm tested per ASTM F88/F88M-21 is rejected for stand-up pouch applications because open-pouch failure at the gusset point is frequently traced to insufficient hot tack at 110–130 °C rather than final seal strength. Hot tack is evaluated on a spring-loaded hot-tack tester at 200–250 mm/s peel speed; values under 3 N/25 mm at 110 °C indicate the sealant layer cannot hold a vertical form-fill-seal back seam without delamination. The 76.2 µm film thickness gives a wider sealing window than 50 µm LLDPE, but it also increases thermal demand at the seal bar; controllers must compensate with higher proportional-integral-derivative output or dwell extension of 0.2–0.4 s when solvent retention in a coex thick sealant is suspected.
| Standard or regulation | Test target | Typical condition | Acceptance or action |
|---|---|---|---|
| ASTM D2578 | Wetting tension of lamination face | Formamide/EGME series | Below 38 mN/m rejects roll |
| ASTM F88/F88M-21 | Heat seal strength | 180° peel, 200–300 mm/min | Below 8 N/25 mm rejects pouch |
| EU 10/2011 Annex II | Food-contact migration | Fatty and aqueous simulants | Primary aromatic amine below listed limit |
| FDA 21 CFR 177.1520(c) | Olefin polymer food-contact status | Extractables testing | Must comply with specified end-use extractables |
In terminally sterilized medical device packaging, the Sclairfilm LX-3 web is not normally sealed directly against uncoated Tyvek because the polyolefin lacks sufficient polar adhesion to Tyvek 1073B/2FS; a converter therefore applies a slot-die or gravure coating of an EVA or EMA heat-seal lacquer at 3–6 g/m² dry weight to one surface of the LLDPE. Coating thickness variation exceeding ±0.5 g/m² across the web produces peel strength coefficient of variation above 15% when sealed at 125–140 °C platen temperature, 0.8–1.5 s dwell, and 0.45–0.69 MPa platen pressure on a rotary heat-seal machine. The seal window is bounded on the low-temperature side by incomplete fiber embedment into the EVA/EMA layer, visible as whitening at the seal edge, and on the high-temperature side by film puckering and strike-through when the 76.2 µm LLDPE reaches its crystalline melting region. Peel strength per ASTM F88/F88M-21 is recorded at 180° peel angle and 200–300 mm/min jaw separation; a target of 1.0–2.5 N/15 mm is typical for peelable medical pouches, while higher values can tear the Tyvek. Dye penetration testing per ASTM F1929 uses methylene blue at 0.05% concentration with a 30 s exposure; any dye channel across the seal boundary is a critical defect under ISO 11607-2. The film layer must also survive ethylene oxide sterilization at 50–60 °C and 30–70% relative humidity for 2–4 h, followed by aeration to remove ethylene oxide residues below the limit in ISO 10993-7; published gamma sterilization data for this specific film grade are limited, so dose substantiation per ISO 11137-2 using a 25 kGy reference dose cannot be assumed without testing on the exact adhesive, coating, and Tyvek stack. A production bottleneck occurs when the EVA/EMA coating is not fully cured before lamination; residual solvent above 5 mg/m² can plasticize the seal coat and lower its onset temperature by 4–8 °C, shifting the peel window below validation limits.
Cold pressure-sensitive adhesive lamination over UV-cured digital prints places the 76.2 µm LLDPE film on the exterior surface of signage and point-of-sale graphics where abrasion resistance and curl control are evaluated. The top surface is corona-treated to 40–42 mN/m per ASTM D2578 before a solvent acrylic pressure-sensitive adhesive is transfer-coated at 15–25 g/m² dry weight. On a wide-web cold laminator, nip pressure is held at 4–6 N/mm across a 1.6 m width; film tension below 40 N/m prevents neck-in and gauge-band distortion that causes adhesive strikethrough. Peel adhesion after 24 h dwell on printed vinyl or BOPP is measured per ASTM D3330/D3330M Test Method A at 180° angle and 300 mm/min; values below 5 N/25 mm are rejected because edge lifting begins on curves with radius less than 25 mm. The LLDPE film improves tear initiation resistance relative to a 25 µm BOPP overlaminate, but it will not provide long-term outdoor UV protection unless a hindered amine light stabilizer and a UV absorber are present in an adjacent ink or adhesive layer; without these, surface chalking and gloss loss occur under modified ISO 4892-3 QUV cycling within 500–800 h for unstabilized LLDPE, although published data for LX-3 in this configuration is limited. The dominant process failure is silvering caused by insufficient wet-out over high-density ink deposits; this is resolved by raising the laminator roll temperature to 25–35 °C and reducing line speed below 15 m/min when ink film thickness exceeds 12 µm. Curl after lamination must be kept below 10 mm over a 500 mm flat sheet; a moisture-resistant backside coating is often required if the graphic is installed in a high-humidity environment above 60% RH.
In foil sachets for nutraceutical powders and oleic liquid doses, the 76.2 µm LLDPE film functions as the inner sealant ply over a 9–12 µm aluminium foil that is adhesive-laminated with a retort-grade polyester exterior film. The duplex or triplex structure is run on a vertical form-fill-seal machine with flat or crimped jaws at 135–160 °C jaw temperature, 0.6–1.2 s dwell, and 0.34–0.55 MPa pressure; because the 76.2 µm web retards heat transfer to the foil interface, the outer jaw temperature is set 8–12 °C higher than would be used with 50 µm LLDPE. Seal integrity is tested per ASTM F88/F88M-21 in both tensile peel and burst modes, with burst values below 20 kPa per ASTM F2054 typically rejected for liquid fills. Powder fill lines generate dust that deposits in the seal zone; a waxy magnesium stearate or medium-chain triglyceride residue above 2 g/m² reduces hot tack by occupying polar sites on the LLDPE surface, and the seal-through-contamination performance can only be recovered by raising jaw temperature 5–10 °C or by using a sealant layer with an EVA-rich skin. Pinholing in the aluminium foil is measured by light-table inspection with a limit of 0 pores per 0.01 m² for liquid pharmaceutical sachets; if foil below 9 µm is flex-cracked during form-fill-seal, the LLDPE layer can mask water vapor leaks temporarily while oxygen ingress remains high. Drop testing per ASTM D5276 at 1 m drop height onto a rigid steel surface is used after sealing to detect flex cracks at the bottom gusset; a leak is defined by peel failure at the point of maximum strain. This construction is not retortable beyond 100 °C because the LLDPE sealant begins to flow under back pressure, and the foil/polymer interlayer may delaminate if the structure is heated above 95 °C for more than 30 min.
Greenhouse and tunnel cover conversion uses the film as one ply in a scrim-reinforced laminate; in many lines the 76.2 µm LLDPE web is extrusion-laminated to a high-density polyethylene woven scrim with an LDPE tie layer at 315–330 °C melt temperature and 20–30 g/m² coat weight. The LLDPE ply contributes tear resistance in the machine direction, but the scrim-dominated composite has anisotropic tensile strength per ASTM D882; MD values are typically 1.5–2.0× the transverse direction values, and laminators adjust wind-up tension below 50 N/m to prevent transverse draw-down. The film should contain a hindered-amine light stabilizer package if the laminate is intended for 24-month outdoor service; unstabilized LLDPE develops carbonyl index increases under ISO 4892-2 artificial weathering within 500 h, causing interply delamination. Process conflict arises from the heat-shrinkage of LLDPE as it approaches the extruder die; edge cooling is maintained at 10–15 °C with web stabilizer bars, and shrinkage after lamination per ASTM D1204 at 100 °C is limited to 1–2% MD and 0.5–1% TD. A major failure mode in the field is separation initiated at pinholes from insect abrasion; field repairs with adhesive tapes perform poorly on corona-treated surfaces that have aged beyond 6 months because wetting tension falls below 34 mN/m. This application is classed as industrial film; compliance is normally tested against REACH and RoHS rather than FDA food-contact, and the laminator must not use recycled feedstock in the 76.2 µm web if the final film is specified for nursery soil-contact use because extractable additives may inhibit seedling development.
Building envelope facings for insulation batts and rigid foam boards use a lamination of aluminium foil, glass-reinforced paper, or metallized PET to the 76.2 µm LLDPE film as a water vapor barrier and scuff-resistant interior surface. Water vapor transmission rate is determined per ASTM E96/E96M Procedure B wet cup at 23 °C and 50% RH; for a foil-facing laminate, the LLDPE layer contributes puncture resistance but the foil controls the vapor permeance, and the measured value is typically below 0.1 perm when the foil remains free of pinholes. The film is melt-bonded to the facing with a hot-melt or extrusion lamination process; extrusion lamination uses an LDPE-type extrudate at 300–320 °C and 20–25 g/m² coat weight, while a hot-melt line uses a slot-die coater with a polyolefin-based adhesive at 150–170 °C application temperature. Bond strength is measured per ASTM D1876 T-peel; interfacial failure below 250 N/m is rejected for utility-knife edge wrapping. Field handling exposes the LLDPE exterior to tears from staples and stud friction; Elmendorf tear per ASTM D1922 is specified at ≥8 N in the machine direction for building wrap. The use of unmodified LLDPE without flame retardants means the laminate must be positioned away from open-flame construction activities; if code requires a Class A surface, a separate mineral-filled facing is required because the LLDPE layer alone does not meet ASTM E84 Class A unless compounded with halogen-free intumescent additives. This application has no direct food-contact restriction, but the material must conform to REACH SVHC restrictions for any residual slip additives and to EU Construction Products Regulation for formaldehyde and heavy metal emissions where installed in interior conditioned spaces.
Thermal laminating pouch conversion uses a 76.2 µm LLDPE layer as a low-melt adhesive component between polyester or polypropylene oversheets and a paper document core. The pouch is activated on a heated-shoe laminator at 100–130 °C surface temperature and 0.4–0.8 m/min feed rate; uniform melting of the LLDPE layer is confirmed by haze testing per ASTM D1003, with delaminated microvoids increasing haze above 10%. The operation relies on the difference between the melting range of LLDPE and the thermally stable polyester oversheet; overshoe temperatures above 140 °C cause adhesive exudation at the sheet edges, producing adhesive contamination on downstream rollers. This pouch application is limited to non-critical graphic finishing; published data for LX-3 specifically in thermal pouch grades is limited, and converters must confirm melt-viscosity compatibility with the heated-shoe dwell time. A short dwell above 2 s does not allow complete wet-out of absorbent paper; wet-out below 85% of the paper surface produces a speckled appearance under transmitted light. Measurement of laminate bond strength is typically not required, but a peel force above 2 N/20 mm is regarded as sufficient for document preservation. The final structure is not suitable for archival preservation if the LLDPE contains octadecamide slip additives above 600 mg/kg because these may migrate to the document surface and alter ink gloss; extraction testing can quantify amide and siloxane species before conversion.
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