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Chevron Phillips MarFlex® 7105D Polyethylene; LLDPE

    • Product Name: Chevron Phillips MarFlex® 7105D Polyethylene; LLDPE
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 250140
    Density 0.918 g/cm³
    Melt Index 1.0 g/10 min
    Melting Point 124 °C
    Vicat Softening Point 93 °C
    Tensile Strength At Yield 10.3 MPa
    Tensile Strength At Break 31.0 MPa
    Elongation At Break 700%
    Flexural Modulus 241 MPa
    Dart Drop Impact 180 g
    Elmendorf Tear Strength Md 250 g
    Elmendorf Tear Strength Td 400 g
    Haze 11%
    Gloss 60%
    Coefficient Of Friction 0.20

    As an accredited Chevron Phillips MarFlex® 7105D Polyethylene; LLDPE factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
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    Application of Chevron Phillips MarFlex® 7105D Polyethylene; LLDPE

    MarFlex 7105D enters downstream converting as a linear low-density polyethylene with nominal melt index 0.5 g/10 min (ASTM D1238, 190 °C, 2.16 kg) and nominal density 0.918 g/cm³ (ASTM D1505). The ethylene-hexene copolymer architecture creates a balance of puncture and tear resistance that is assessed in film by ASTM D1709 and ASTM D1922. The same molecular weight distribution restricts high-speed cast stretch extrusion because melt viscosity remains high at typical cast film temperatures of 240–260 °C. Downstream converting segments are therefore selected where puncture, tear, and seal integrity dominate rather than optical clarity alone.

    In heavy-gauge industrial sack film, 7105D is converted from 100% resin or from an 85/15 wt% blend with a low-melt-index LDPE (density 0.923 g/cm³, melt index 0.25 g/10 min). The LDPE fraction is added when bubble stability on a 250 mm die becomes the limiting constraint. Extrusion is conducted on a 90 mm grooved-feed extruder with a 30:1 L/D barrier screw. Melt temperature is held at 210–225 °C. Die gap is 1.8–2.2 mm. Blow-up ratio is 2.5:1 to 3.0:1. Frost line height is maintained at 12–18 die diameters to balance machine-direction tear and transverse-direction dart impact. Granules stored below 10 °C should be tempered to 20–30 °C before extrusion to avoid surface condensation and melt pressure fluctuation causing gauge bands. Compliance for sift-proof dangerous goods liners is tested under 49 CFR 178.503 and packaging performance under ISO 21898. Mechanical acceptance uses ASTM D1709 dart drop and ASTM D1922 Elmendorf tear. Terminal products include 50 kg resin sacks, industrial liners, lumber wrap, and FIBC inner bladders.

    What Stabilization Package Prevents Premature Film Embrittlement in Silage Bunker Covers?

    Silage bunker covers produced from 7105D require a compounded stabilization package because the film is exposed to ultraviolet radiation, organic acid condensate, and mechanical abrasion for 12–24 months in outdoor service. The formulation is 100 phr 7105D plus 2.5 wt% carbon black masterbatch (50% carbon black in LLDPE carrier), 0.4–0.8 wt% HALS/UV stabilizer masterbatch, and 0.1 wt% fluoropolymer processing aid. Final carbon black concentration is set at 1.0–1.5 wt% to preserve ductility while blocking UV transmission. Organic acid condensate lowers surface pH and attacks unprotected polymer chains; the stabilizer package functions as a sacrificial UV screen and free-radical scavenger rather than as a water barrier. Processing uses a die gap of 1.8 mm, blow-up ratio 2.2:1, and melt temperature capped at 215 °C. Higher temperatures accelerate carbon black dispersion breakdown and generate visible black specks that initiate tear. The film is tested under EN 13206 for agricultural covering films. Tensile properties are measured by ISO 527-3 and tear resistance by ASTM D1922. Terminal products include black/white bunker covers, grain storage clamp films, and temporary stockpile covers.

    When coextruded as a sealant layer in form-fill-seal pouches, 7105D is placed between the product side and the tie layer. The sealant layer thickness is 15–30 µm within an overall laminate of 80–120 µm. The resin is blended at 90/10 wt% with a metallocene plastomer of density 0.902 g/cm³ when lower-temperature seal initiation is required. The coextruded web is produced on a 3-layer blown film line. Die gap is 1.5 mm. Blow-up ratio is 2.3:1. Melt temperature is 215–230 °C. A higher melt temperature improves interlayer adhesion but narrows the hot-tack plateau. Food contact compliance is assessed under FDA 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011. Seal strength is measured by ASTM F88/F88M and hot tack by ASTM F1921. Terminal laminates are converted into stand-up pouches, side-gusseted bags, and frozen-food pillow packs.

    Freezer Film Ductility and Dart Impact Resistance in IQF Packaging

    For individually quick-frozen packaging, blown film is processed from an 80/20 wt% blend of 7105D and a high-pressure LDPE with melt index 0.25–0.45 g/10 min. The LDPE fraction reduces isotropic tear propagation at freezer temperatures of −25 °C to −40 °C. The line configuration uses internal bubble cooling and a die gap of 1.8 mm. Blow-up ratio is held at 2.0:1 to 2.5:1. Melt temperature is 205–215 °C. Poor internal bubble cooling control increases transverse-direction shrink back and lowers dart impact below the inbound specification for IQF vegetable bags. Low-temperature mechanical acceptance uses ASTM D1709 dart drop at −20 °C, ASTM D1922 Elmendorf tear, and ASTM D882 tensile elongation. Food contact compliance follows FDA 21 CFR 177.1520(c). Finished products include IQF vegetable bags, seafood block liners, and subprimal meat packaging.

    Pallet encapsulation via stretch-hood film operates with a mechanical stress pattern that differs from conventional stretch wrap. The film is stretched over a pallet load at ambient temperature and then allowed to recover to generate load-retention force. The resin is formulated at 80/20 wt% with an autoclave LDPE (melt index 0.8 g/10 min, density 0.923 g/cm³). Processing uses a multilayer blown film line with a die gap of 2.3 mm, blow-up ratio 3.2:1 to 3.8:1, and melt temperature 220–230 °C. Layer distribution is controlled to prevent asymmetric shrinkage force. Asymmetric shrinkage causes pallet wrap telescoping on automated hood lines. Puncture resistance is measured by ASTM D5748 and tensile strength by ASTM D882. Published data for 7105D in high-pre-stretch machines above 80% pre-stretch is limited. The high molecular weight fraction increases residual stress and reduces holding force in such configurations. Terminal products include 100–160 µm pallet hoods, machinery export wrap, and heavy equipment covers.

    When Agricultural Chemical Packaging Requires High-Stress Crack Resistance

    Liquid agricultural chemical liners expose 7105D to stress cracking from filled liquids, surfactant contact, and long warehouse storage under load. The formulation is 70/30 wt% 7105D with an LDPE of melt index 0.2–0.3 g/10 min. Additional additives are 2.0 wt% carbon black masterbatch, 0.1 wt% antioxidant, and 0.05 wt% acid scavenger. The blend is designed to raise environmental stress crack resistance measured by ASTM D1693 without dropping dart impact below the liner perforation threshold. Processing uses a die gap of 2.0 mm, blow-up ratio 2.5:1, and melt temperature capped at 200–210 °C. The lower melt temperature protects the additive package from thermal consumption and reduces odorous oxidation by-products. Liner qualification follows 49 CFR 173.24 and drop testing per 49 CFR 178.603. Tensile yield is measured by ASTM D638. Terminal products include bag-in-box liners, drum liners, IBC bladders, and multi-wall chemical bags.

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