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LyondellBasell HDPE L5045

    • Product Name: LyondellBasell HDPE L5045
    • 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 741629

    As an accredited LyondellBasell HDPE L5045 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell HDPE L5045 is packaged in 25 kg polyethylene bags, typically palletized and stretch-wrapped for safe industrial transport.
    Container Loading (20′ FCL) LyondellBasell HDPE L5045 is loaded in 20′ FCL containers, typically 20 MT in 25 kg bags, securely stowed for export.
    Shipping LyondellBasell HDPE L5045 is a non-hazardous polyethylene resin shipped as free-flowing pellets. Standard packaging includes 25 kg bags, jumbo bags, octabins, or bulk trucks/railcars. It is not regulated for transport. Store in a cool, dry, ventilated area away from heat, sunlight, moisture, and contamination. Handle palletized, stretch-wrapped units with care.
    Storage Store LyondellBasell HDPE L5045 in original sealed packaging in a cool, dry, well-ventilated area. Protect from direct sunlight, heat, moisture, and contamination. Keep away from ignition sources. Avoid prolonged UV exposure and excessive stacking. Use first-in, first-out rotation. Reseal opened bags; do not store near odorous, incompatible, or strongly oxidizing materials. Maintain clean, dry handling conditions and stable pallet stacking.
    Shelf Life Stable under normal storage conditions; indefinite shelf life when kept dry, cool, sealed, and protected from direct sunlight and contaminants.
    Application of LyondellBasell HDPE L5045

    Thin-walled dairy and deli pots produced from LyondellBasell HDPE L5045 rely on the 45 g/10 min melt flow rate at 190 °C/2.16 kg under ISO 1133-1:2022 to fill side walls of 0.40–0.50 mm without exceeding the injection pressure limit of a 250-tonne electric toggle press. The density of the homopolymer is 0.954 g/cm³ under ISO 1183-1:2019, and the flexural modulus is near 1,240 MPa under ISO 178:2019, which supplies top-load rigidity in shallow tubs. The grade is dry-blended with a white food-contact masterbatch at 2–3 wt% through a gravimetric blender; let-downs above 4 wt% generate pigment streaks because the high-flow narrow molecular weight distribution provides limited dispersive mixing in a 24:1 L/D general-purpose screw. Melt temperature is held at 195–220 °C, mould temperature at 12–20 °C, and screw back pressure below 1.0 MPa to prevent frictional heat from driving stock temperature above 230 °C. The hold-pressure profile uses an initial pack at 55–65 MPa hydraulic pressure for 0.8 s followed by a reduced pack at 35–45 MPa for 1.0–1.5 s; this sequence prevents gate blush at a 0.6 mm valve-gate land while still compensating shrinkage. Mould venting on the cavity perimeter is cut to 0.020 mm depth to remove air from the centre core without allowing flash on a stack mould with 16+16 cavities. Food-contact compliance is established under FDA 21 CFR 177.1520(c)2.1 and under EU Regulation 10/2011 overall migration limit 10 mg/dm² with the assigned food simulant selected by the final dairy product category. Terminal articles are snap-on lid tubs for sour cream, cottage cheese, soft margarine, and portion-service condiment cups. Hot-fill above 70 °C is outside practical operating limits because the deflection temperature under load approaches the Vicat softening range of the homopolymer.

    Why does hold-pressure switchover control the lidding flange more than melt temperature?

    In cold drink cups and flat lids, L5045 is processed at 200–215 °C melt temperature and 10–18 °C mould temperature. The controlling process variable is the switchover from velocity control to pressure control at 95–98% of screw cushion volume. If switchover occurs after the flange freezes, the core remains un-packed and the part warps after the lid is separated from the runner system. A ring gate of 0.9–1.2 mm land depth is specified; a land below 0.8 mm freezes before filling is complete and produces flow hesitation at the flange circumference. An internal release masterbatch is added at 0.5–1.0 wt%; higher loadings reduce print adhesion on the sidewall, and surface wetting tension is checked at 38–42 mN/m following ISO 8296:2003. Cooling time is set so ejection surface temperature is below 45 °C; demoulding above 55 °C creates flange buckle when cups are stacked on high-speed packaging lines. Terminal articles include stadium cups of 300–500 cm³ capacity and flat cold-beverage lids with a 0.35 mm tamper-evident tab. Compliance for aqueous and fatty beverage contact uses FDA 21 CFR 177.1520 and EU Regulation 10/2011; carbonated beverage closures remain outside the supplied application envelope until closure tether retention and stress-crack resistance are validated on the production tool.

    Pail wall thickness reduction trials in 5 L open-top containers for water-based coatings

    Moulders running L5045 in small open-head pails for water-based coatings add a calcium carbonate masterbatch at 5–15 wt% to reduce cycle time and increase side-wall stiffness at a nominal wall of 1.6 mm. The filler addition lowers tensile yield under ISO 527-2:2012 by 10–15%, so the handle is gated with a fan gate of 1.5 mm depth and the weld-line strength at the core pin is specified to reach at least 80% of the non-welded tensile yield. Melt temperature is kept at 190–210 °C; higher melt temperatures with filler masterbatch can produce a 5–8% variation in hot-runner manifold viscosity. Core and cavity cooling are set differentially at 10 °C and 25 °C to shift shrinkage away from the visible outer wall. Demoulding before the side wall reaches 35 °C causes the handle to tear at the mould pin. A lid gasket groove depth of 1.0–1.3 mm compresses an EVA foam gasket to 30–40% of its free thickness. Containers for water-based latex primers, adhesives, and non-aggressive detergent concentrates are not automatically qualified for dangerous goods; full performance testing under UN 6.1.5 is required if the pail is to carry UN-classified filling materials. Exposure to aromatic solvents at 23 °C is a known stress-cracking risk for this homopolymer class, and a compatibility screen under ISO 175:2010 is required before solvent-borne filling is considered.

    Storage totes, tool trays and drawer organisers are a shallow application zone for L5045; the controlling material input is not melt flow but long-term flexural creep of the unreinforced homopolymer under top loading at 40 °C. The grade is run unfilled, and regrind is held below 15 wt% because higher addition levels produce flow lines on low-gloss side walls. Published data for this specific configuration is limited, so component validation follows ISO 899-2:2003 with a maximum continuous edgewise compressive stress of 4 MPa at 23 °C for non-load-bearing dividers.

    When alcohol-free cosmetic jars are switched from PETG to high-flow HDPE

    Injection-moulded cosmetic jars and dispensing overcaps in alcohol-free formulations use L5045 at melt temperatures of 200–220 °C and mould temperatures of 10–20 °C. The essential process selection is a valve-gated hot runner with tip orifices of 0.6–0.9 mm; smaller tips create shear heating above 230 °C, which produces gate stringing and occasional black specks after 4–6 h of continuous running. A slip/antiblock masterbatch is added at 1–2 wt% where the jar requires automated label sleeves; surface coefficient of friction is measured following ISO 8295:1995 on plaques moulded from the same melt, and label-sleeve insertion jams occur if the value remains above 0.30. Chemical compatibility is the binding constraint. Published grade-specific solubility data for L5045 is limited, but homologous high-flow HDPE data show a sharp decline in environmental stress crack resistance above 20% ethanol and 5% isopropyl alcohol; producers therefore screen filled jars under ISO 175:2010 and ASTM D1693 with the exact emulsion before release. Migration is controlled under EU Regulation 10/2011 and cosmetics GMP under ISO 22716:2007. Terminal articles are alcohol-free cream jars, loose-powder bodies, and dispensing overcaps. Hot filling above 60 °C is not permissible because the distortion temperature of the resin is too close to the fill temperature.

    At -18 °C, weld-line placement overrides notched Izod data in frozen meal tray release criteria

    At -18 °C, frozen meal trays moulded from L5045 fail primarily at compartment weld lines rather than through uniform side-wall yielding. The gate is placed in the floor of each compartment at 20–30 mm from the flange; additional gates are added only when the distance between weld lines exceeds 25 mm, because every added gate creates a cold flow boundary that can fracture at freezer temperature. Melt temperature is run at 215–230 °C to improve weld strength, while total residence time above 230 °C is limited to 6 min to limit molecular weight loss. Regrind up to 20 wt% is allowed if the flake is ground to 5–8 mm and melt-filtered through a 60-mesh screen pack before dry blending; higher regrind raises melt flow by 5–10% and shifts the hold-pressure window. Filled-tray drop testing follows ASTM D2463-15 procedure B from 1.0 m at -18 °C, with failure defined as any side-wall crack visible after 24 h at freezer temperature. Notched Izod under ISO 180:2019 at 23 °C is not a release criterion because it does not capture flange sharp corners and compartment weld lines. Compliance is checked under FDA 21 CFR 177.1520 and EU Regulation 10/2011. Terminal articles are multi-compartment frozen meal trays and single-serve freezer containers. If wall thickness falls below 0.8 mm, the pack time is extended by 0.3–0.5 s; otherwise flange distortion after freezing exceeds 1.5% of the diameter.

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