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Chevron Phillips Marlex® 7308DL Polyethylene; LLDPE

    • Product Name: Chevron Phillips Marlex® 7308DL 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 831833
    Polymer Type Linear Low Density Polyethylene (LLDPE)
    Comonomer 1-Hexene
    Density 0.930 g/cm³
    Melt Index 0.8 g/10 min
    Melting Point 122 °C
    Vicat Softening Point 103 °C
    Tensile Strength At Yield 12 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break 700%
    Flexural Modulus 310 MPa
    Dart Impact Strength 120 g
    Elmendorf Tear Strength Md 200 g
    Elmendorf Tear Strength Td 500 g
    Haze 12%
    Gloss 70%

    As an accredited Chevron Phillips Marlex® 7308DL Polyethylene; LLDPE 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 Marlex® 7308DL Polyethylene; LLDPE

    Cast film extrusion of Chevron Phillips Marlex® 7308DL linear low density polyethylene is performed on a 75 mm 30:1 L/D barrier screw with a 2400 mm coat-hanger die and a 500 mm chill roll for pallet-wrap and stretch-hood films. The resin has a nominal density of 0.918 g/cm³ at 23 °C per ASTM D1505 and a melt index of 0.80 g/10 min at 190 °C/2.16 kg per ASTM D1238. Barrel temperatures are set from 190 °C at the feed throat to 255 °C at the die, with the chill roll held at 22 °C to 28 °C depending on line speed and gauge. At a basis weight of 23 µm, pre-stretch ratios of 200% to 350% are feasible on high-speed pallet wrappers only when machine-direction and transverse-direction elongation at break are measured separately under ISO 527-3, because rapid quenching produces anisotropic orientation that suppresses transverse elongation more than machine-direction elongation. Edge trim generated at 5% to 8% of total throughput is re-pelletized and fed back into the extruder; above 12% trim addition, the lower-molecular-weight fraction may increase gel formation at the die lip and produce visible die lines. A fluoroelastomer processing aid is introduced at 200 ppm to 500 ppm only if melt fracture is observed at the internal die surface. Slip and antiblock concentrates are incorporated at 1.0 wt% to 3.0 wt% when coefficient of friction below 0.30 is required under ASTM D1894. The finished cast stretch film is wound in 500 mm wide rolls for machine wrapping and in 750 mm wide rolls for stretch-hood lines; weld strength at the film’s inner layer is influenced by the quantity of recycled trim and the age of the reclaimed pellet blend. Published data for the specific edge-trim regression rate of this grade in cast film is limited, so converters must monitor die-lip deposit after each 24 h run.

    Why Does a 50 µm Heavy-Duty Liner Sag when the Frost Line Is Kept Below 3 Die Diameters?

    In heavy-duty liner and sack production, blown film dies from 350 mm to 600 mm diameter are operated with blow-up ratios between 2.0:1 and 2.8:1. Marlex 7308DL is blended with 10 wt% to 20 wt% high-pressure LDPE to raise melt tension and stabilize the bubble when the frost line is moved below 3 die diameters to increase quench rate. At a 50 µm gauge, bubble sag and transverse thickness bands appear if internal bubble pressure is not adjusted incrementally with blow-up ratio; layflat width is recorded every 10 min to hold gauge variation within ±5%. Dart impact is measured under ASTM D1709 Method A, and Elmendorf tear is measured under ASTM D1922 in both machine and transverse directions because LLDPE branching produces different tear propagation paths after film orientation. The film is converted into gusseted sacks with bottom seal temperatures from 130 °C to 160 °C and sealing dwell times of 0.8 s to 1.5 s. Seal bar contamination occurs when recycled film contains paper dust or inorganic fillers above 0.5 wt%. The terminal product is used for 25 kg resin bagging, construction aggregate packaging, and textile bale covers, where puncture resistance under ASTM D5748 is more relevant than optical haze. Without a high-molecular-weight HDPE blend, the monolayer liner exhibits higher creep at storage temperatures above 40 °C, so warehouse stacking trials are run before a specification is accepted.

    Where liquid packaging pre-ply and frozen-food cartons require a sealant layer with reduced neck-in, Marlex 7308DL is introduced on extrusion coating lines as a sealant layer in blended form rather than as a neat coating resin. On a 120 mm 30:1 L/D extruder delivering melt through a 2600 mm slot die, melt temperature is maintained at 290 °C to 315 °C and the air gap between die exit and nip is shortened to 100 mm to 150 mm to suppress neck-in. The substitution of a 0.80 g/10 min LLDPE for a 7.5 g/10 min LDPE coating grade raises specific energy input because viscosity at 300 °C remains higher; screw torque limits on existing drives may reduce maximum line speed by 10% to 15% unless barrel temperatures are allowed to rise. The coating weight is typically depressed to 12 g/m² in the sealant layer and to 20 g/m² in the bulk layer; below 12 g/m², melt curtain oscillation and edge polymer degradation at the die deckle produce coating weight variation that cannot be corrected by the back-pressure control loop. Adhesion to paperboard is improved by corona pre-treatment of the board surface to 42 dyn/cm to 46 dyn/cm or by ozone application at the melt curtain; without surface activation, peel adhesion under ASTM D903 falls below practical peel-stop requirements. The finished packaging board is used for liquid carton sealing layers, and compliance is validated under FDA 21 CFR §177.1520 for olefin polymers and under Commission Regulation (EU) No 10/2011 Annex I for overall migration and specific migration of additives. When mineral-filled board scrap is reincorporated into the paperboard furnish, the converter must verify that residual adhesion promoters do not exceed the specific migration limits of the surface coating formulations.

    Greenhouse Side-Wall Films Above 150 µm Require a Stabilizer Package That the Base Resin Does Not Provide

    For greenhouse side-wall films specified at 150 µm to 200 µm, Marlex 7308DL is processed in monolayer and three-layer blown film lines with die sizes from 250 mm to 500 mm and blow-up ratios between 2.0:1 and 3.0:1. A UV stabilization masterbatch is added at 3.0 wt% to 5.0 wt% because the unmodified polymer lacks hindered amine light stabilizers and will undergo photo-oxidative embrittlement under polyethylene film exposure. Anti-fog agents are added at 1.0 wt% to 2.0 wt% when inner surface condensation control is required for light transmission in protected cropping; the anti-fog incorporation must be completed at low screw temperatures below 200 °C to avoid thermal degradation of the surfactant. Mulch film is run at 15 µm to 25 µm with carbon black masterbatch at 2.0 wt% to 4.0 wt% for photoperiod control and weed suppression. Film tensile properties are measured under ISO 527-3; impact resistance under ASTM D1709; and tear resistance under ASTM D1922 or ASTM D1004. For silage wrap and bale netting replacement, puncture resistance is evaluated under ASTM D5748 because repeated handling causes localized stress concentrations that can exceed the resin’s intrinsic craze resistance at low outdoor temperatures below 5 °C. Outdoor exposure validation is carried out by the converter in accordance with ISO 4892-2 or regional agricultural film standards such as EN 13206; the base resin pellet itself is not a UV-stabilized product and cannot be placed on a greenhouse roof or side wall without the stabilizer masterbatch.

    When 7308DL Is Blended into Frozen-Food Packaging, Seal Temperature Rather Than Gauge Defines the Converter’s Window

    Flexible food packaging lines that run frozen vegetable, seafood, and bakery overwrap use three-layer coextruded blown film with Marlex 7308DL in the sealant skin and a core layer containing in-process edge trim. Sealant layer thickness is held between 8 µm and 15 µm, while the total film gauge is 35 µm to 60 µm. Because the seal initiation temperature of an LLDPE-rich skin is higher than that of an LDPE-rich formulation, the converter must re-map the sealing jaw temperature profile whenever the 7308DL content exceeds 20 wt% of the sealant layer; otherwise the crimp jaw at 130 °C can produce a weak seal that fails under ASTM F88 peel testing. A production-scale validation typically records heat seal strength above 4 N per 15 mm after a 0.5 s dwell at 135 °C on a hydraulic laboratory sealer, but jaw geometry and film backing stock require on-site confirmation. Slip and antiblock concentrates are added to the skin at 1.0 wt% to 2.0 wt% to achieve a coefficient of friction below 0.30 under ASTM D1894; higher antiblock levels above 3.0 wt% reduce seal strength and increase haze in the frozen-food pack. Compliance for direct contact with all food types under the applicable cold-temperature use condition is assessed under FDA 21 CFR §177.1520 and Commission Regulation (EU) No 10/2011, with attention to the specific migration of slip additives and the authorized monomer status of the base polyethylene. The terminal pack is a pillow pouch or flow-wrap with a hermetically sealed longitudinal fin seam and transverse crimp seals; the converter must reject rolls that show blocking after 48 h warehouse storage at 35 °C because the absence of sufficient antiblock in the core layer accelerates blocking during warm shipment.

    Regulation/standardRelevant clause/testValidation parameter
    FDA 21 CFR §177.1520Olefin polymersFood-type end tests and extractable fraction limits
    Commission Regulation (EU) No 10/2011Annex I, Article 11Overall migration below 10 mg/dm²
    ASTM F88Seal strengthTarget above 4 N per 15 mm on frozen pack closures
    ASTM D1894Kinetic coefficient of frictionBelow 0.30 on skin surface

    When 1.0 mm to 2.5 mm geomembrane is run on flat-die sheet equipment, a 110 mm 30:1 L/D vented extruder with a 2000 mm flexible-lip die and a three-roll polish stack is operated with die temperatures from 240 °C to 260 °C and roll temperatures from 50 °C to 70 °C to control surface gloss and shrinkage. For temporary landfill covers and secondary containment liners, carbon black or titanium dioxide masterbatch is added at 2.0 wt% to 5.0 wt% to achieve the required weathering resistance and to reduce ultraviolet penetration into the polymer matrix. Hot-wedge welding is used to join panels at 350 °C to 400 °C with a 0.5 m/s to 1.5 m/s travel speed; lap-shear strength after welding is evaluated under ASTM D6392 and shear elongation is measured under ASTM D638 or ISO 527-3. Stress-crack resistance is assessed under ASTM D1693 Condition B after the sheet has been exposed to a 10% Igepal CO-630 solution at 50 °C; the converter should not assume a single pass/fail value without comparing sheet thickness and carbon black dispersion because the stress-crack response is influenced by extrusion orientation and residual stress at the sheet edges. Published data for the specific stress-crack performance of this grade in geomembrane thickness is limited, so plant-level validation must include both weld peel and shear tests after panel roll-up at 10 °C overnight. This LLDPE is not a direct substitute for HDPE geomembrane grades in municipal solid waste landfill primary liner specifications that require GRI-GM13 compliance; its use is confined to short-term cover systems, pond liners, and secondary containment where the applicable design standard accepts LLDPE sheet with the measured elongation at break and low-temperature brittleness data from ASTM D746.

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