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Chevron Phillips 7105DKT LLDPE Blown Film Resin, Hexene Copolymer

    • Product Name: Chevron Phillips 7105DKT LLDPE Blown Film Resin, Hexene Copolymer
    • 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 124182
    Polymer Type Linear Low Density Polyethylene (LLDPE)
    Comonomer Hexene-1
    Form Pellets
    Processing Method Blown Film Extrusion
    Melt Index 1.0 g/10 min
    Density 0.918 g/cm³
    Melting Point 124 °C
    Vicat Softening Point 104 °C
    Tensile Strength At Yield 11 MPa
    Tensile Strength At Break 26 MPa
    Elongation At Break 700%
    1 Secant Modulus 200 MPa
    Dart Drop Impact 120 g
    Elmendorf Tear Strength Md 300 g
    Elmendorf Tear Strength Td 500 g
    Haze 12%
    Gloss 60%
    Fda Compliance Yes

    As an accredited Chevron Phillips 7105DKT LLDPE Blown Film Resin, Hexene Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

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    Application of Chevron Phillips 7105DKT LLDPE Blown Film Resin, Hexene Copolymer

    On blown-film lines running Chevron Phillips 7105DKT as the primary resin, the practical conversion window differs from butene-copolymer LLDPE of the same nominal density because the hexene side-chain distribution increases bubble stability at blow-up ratios of 2.0–3.0 but raises melt-curtain tension at short frost lines. When the grade is run on a 90 mm grooved-feed extruder with 30:1 L/D and a 350 mm low-pressure die having a 2.0 mm–2.5 mm die gap, the melt temperature at the adapter is held at 204 °C–227 °C. The nominal melt index of 7105DKT is 0.50 g/10 min at 190 °C/2.16 kg under ASTM D1238, and the nominal density is 0.918 g/cm³ under ASTM D1505. A production formulation for 125 µm–200 µm heavy-duty form-fill-seal sacks uses 70 wt% 7105DKT, 20 wt% LDPE extrusion-coating grade, and 10 wt% clean edge-trim regrind, with carbon black masterbatch added at 3 wt%–6 wt% for UV opacity when sacks are stored outdoors. The film is drawn through a dual-lip air ring with internal bubble cooling, and the frost-line height is maintained between 500 mm and 900 mm to avoid excessive orientation in the machine direction. If the frost line drops below 250 mm at outputs above 180 kg/h, the melt curtain freezes before stress relaxation is complete, and the finished sacks show a loss in Elmendorf tear measured by ASTM D1922 after side gussets are folded. Seal-bar temperature on continuous FFS lines is set at 145 °C–165 °C; below this range the LDPE modifier lowers seal initiation, but above 170 °C the heat-seal jaw can draw the film and create wrinkle propagation in the back panel. The sack is filled with polymer pellets, granular fertilizers, or petrochemical prills at fill weights of 15 kg–50 kg. Dart impact resistance per ASTM D1709 is the primary release criterion, and converters monitor film thickness variability at ±5% across the web because thin-spot formation under gusset folds is the dominant field-failure mode. 21 CFR 177.1520(c) covers the polyethylene fraction for food-contact use, but phosphate fertilizer sacks may require a separate migration assessment under EU 10/2011 if exported into food co-transport supply chains.

    Test methodApplication-specific condition for FFS sackPurpose
    ASTM D1709125 µm gusseted film, 23 °Cdart impact at fill-line stresses
    ASTM D1922MD/TD after gusset foldingbrittle tear in thin-spot zones
    ASTM D882500 mm/min jaw separation, 23 °Ctensile yield and break at lay-flat edges
    ASTM F88/F88Mseal bar 145 °C–165 °C, dwell 0.4 scontinuous FFS longitudinal seal
    ASTM D169310% Igepal CO-630, 50 °C, notched stripESCR for stacked chemical sacks

    Layer Distribution and UV Stabilizer Carry-Out in Five-Layer Silage Film

    Five-layer agricultural silage film is one application where 7105DKT is placed in the two outer skins rather than the core. A representative structure comprises an outer skin at 20 wt%, a sub-skin at 25 wt%, a filled core at 20 wt%, another sub-skin at 25 wt%, and an inner skin at 10 wt%. The outer skin is a blend of 85 wt% 7105DKT and 15 wt% UV-stabilizer masterbatch based on a HALS and benzotriazole package; the skin layer carries 8,000 ppm–12,000 ppm of active HALS because the surface must absorb ultraviolet energy before chain scission reaches the load-bearing sub-skins. The sub-skins are modified with a metallocene plastomer to raise dart impact retention after 12 months of field exposure, while the core is filled with TiO₂ or carbon black at 4 wt%–8 wt% for opacity and infrared blocking. Processors running this structure on a five-layer blown-film line maintain a die gap of 2.0 mm, blow-up ratio of 2.0–2.4, melt temperature of 215 °C–225 °C, and frost-line height near 900 mm. The high frost line allows the hexene copolymer chains sufficient relaxation time to reduce machine-direction shrinkage, which is critical when the film is wrapped around round bales at high draw tension. Outdoor exposure data for this grade, as measured by retained elongation at break per ISO 527-3, is the accepted quality gate; published data for this specific 7105DKT formulation is limited, so converters qualify each UV masterbatch lot by accelerated UV testing under ISO 4892-2. The terminal product is bale wrap, clamp film, and silage cover for grass, maize, and lucerne; the film is not recommended for chlorinated-pesticide contact because the antioxidant package can be extracted by chlorinated solvents, causing surface tack and loss of UV protection.

    When frozen-food film is specified for abuse resistance below -10 °C, the choice of dart impact method and seal-jaw temperature becomes the selection tool. 7105DKT is converted on small to medium blown-film dies at melt temperatures of 180 °C–200 °C, with finished thickness from 40 µm to 80 µm and a frost line held below 300 mm. For a 60 µm monolayer pack for individually quick-frozen vegetables, the resin is run with 700 ppm erucamide slip and 1,200 ppm synthetic silica anti-block; the masterbatch let-down ratio is calculated from the carrier polymer melt index rather than total film thickness because overdosing the anti-block will raise haze above the threshold needed for in-store display. Film for frozen seafood is produced at 70 µm and tested for dart impact at -20 °C by ASTM D1709 and for low-temperature seal strength by ASTM F88/F88M after filling with brine. The sealing layer operates at 120 °C–135 °C on vertical form-fill-seal equipment; higher temperatures cause film shrinking at the jaw and curl on the longitudinal seal. Compliance is normally certified under 21 CFR 177.1520(c) for food contact and EU 10/2011 with an overall migration limit of 10 mg/dm². Terminal products include bags for IQF vegetables, frozen seafood, ice cubes, and frozen dough portions, where the key resin contribution is resistance to impact-induced puncture at temperatures below -10 °C during transport.

    What Limits Seal Strength Retention in a 30 µm Coextruded Lidding Sealant Web?

    Three-layer coextruded lidding films for modified-atmosphere trays use 7105DKT as the sealant skin because its hexene comonomer distribution produces a broader hot-tack window than an EVA-based sealant layer. The sealant skin is typically 25 wt%–35 wt% of the total structure and is blended with 15 wt%–20 wt% LDPE to bring seal initiation down to 115 °C–125 °C on high-speed tray sealing machines. Below 115 °C, the dwell time must be longer than 1.0 s to reach interfacial fusion; above 125 °C, the sealant layer becomes prone to stringing at the knife cut-off. Seal strength is measured by ASTM F88/F88M at 250 mm/min jaw separation, but production audits at 500 mm/min reveal a transition from peel mode to film tear once the sealant skin exceeds 25 µm. The limiting parameter after warehouse ageing is not the resin melting point; anti-block particles from the adjacent core layer migrate to the seal surface when the film is stored at 40 °C for 8 weeks, increasing seal initiation by 10 °C–15 °C. A monolayer drop-in replacement with the same sealant formulation but no coextrusion fails the same aged-seal protocol because there is no core layer to act as a reservoir for the silica. The lidding structure is tested for overall migration under EU 10/2011 and for the polyethylene fraction under 21 CFR 177.1520(c); oxygen transmission rate of the composite is governed by the outer PET or polyamide layer and is characterized by ASTM F1249, not by the sealant skin. Terminal products are MAP lidding for leafy greens, dairy snack trays, and case-ready meat or poultry trays where the sealant must survive case-rigid base deformation without splitting.

    In 200-litre steel and fibre drum liner production, environmental stress-crack resistance governs shelf-level packaging performance far beyond the ambient tensile properties measured on lay-flat tubing. 7105DKT is converted into 200 µm–300 µm tubular film at a blow-up ratio below 2.0, melt temperature of 210 °C–225 °C, and die gap of 2.0 mm; the low BUR reduces hoop orientation and prevents the liner from failing along the weld line when the drum is dropped at -18 °C under UN 1H2 and UN 1H1 testing. The formulation includes 3 wt% carbon black masterbatch for UV opacity and electrostatic dissipation; dispersion is checked by a Hegman grind gauge, and agglomerates larger than 20 µm are rejected because carbon agglomerates act as stress concentrators at the interface with the hexene copolymer matrix. ESCR performance is assessed by ASTM D1693 with 10% Igepal CO-630 at 50 °C, and for drum-liner grades the time to 50% failure in notched bent-strip specimens is the accepted predictor of stacking endurance in warm chemical warehouses. The liner is used for aromatic solvents, agricultural emulsifiable concentrates, printing inks, and viscous resins; strong oxidizers and chlorinated solvents require pre-qualification because chemical attack can shift the failure mechanism from brittleness to oxidative embrittlement at the fill line. Terminal product is a sealed drum liner for 200-litre steel drums, 120-litre open-top drums, and hazardous solid/liquid combinations moving under ADR/RID transport.

    When Mandrel Pre-Stretch Approaches 45% in 80 µm Stretch Hood Film

    Stretch hood packaging lines pre-stretch the film by 40%–55% before the hood is pulled over a palletised load, so the film must retain puncture resistance at corner edges after molecular orientation has already consumed part of the elastic limit. A formulation for 70 µm–100 µm stretch hood film uses 85 wt% 7105DKT, 10 wt% LDPE, and 5 wt% polyisobutylene-based cling masterbatch; the cling additive is kept below 7 wt% to avoid blocking the roll after high-tension winding. The film is run at a blow-up ratio of 2.2–2.6, with frost-line height of 600 mm and melt temperature of 210 °C–220 °C. Tight frost-line control is required because a frost line that shifts upward by 150 mm during the run reduces MD tear resistance at the corner of the pallet, which is the primary cause of hood burst on rectangular loads. Tensile properties are tested by ASTM D882 in both machine and transverse directions, and puncture resistance by ASTM D5748, with the load cell set to capture the first corner penetration rather than film rupture at the top. 7105DKT-based hoods are used for palletised cement bags, PET resin sacks, beverage crates, and machinery crates where a dust-tight, waterproof layer must survive fork-lift handling and outdoor storage. For export loads stored under direct sunlight, UV-stabilizer masterbatch is added at 4 wt%–6 wt%, and the resulting film is qualified for simple transit packaging under the applicable national road and rail transport standards.

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