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LyondellBasell HDPE L4912

    • Product Name: LyondellBasell HDPE L4912
    • 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 122088
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.948 g/cm³
    Melt Index 0.25 g/10 min (190 °C/2.16 kg)
    Melting Point 132 °C
    Vicat Softening Temperature 123 °C
    Tensile Strength At Yield 25.5 MPa
    Tensile Strength At Break 33.1 MPa
    Elongation At Break 850%
    Flexural Modulus 1170 MPa
    Environmental Stress Crack Resistance Escr >1000 h
    Hardness Shore D 66
    Brittleness Temperature < -70 °C
    Coefficient Of Linear Thermal Expansion 1.2 × 10⁻⁴ /°C

    As an accredited LyondellBasell HDPE L4912 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell HDPE L4912 is packaged in 25 kg moisture-resistant polyethylene bags, 40 bags per pallet, suitable for industrial storage.
    Container Loading (20′ FCL) 20′ FCL of LyondellBasell HDPE L4912: 25 kg bags, palletized, stretch-wrapped, secured, max payload approx. 18–20 MT net.
    Shipping LyondellBasell HDPE L4912 ships as a non-hazardous high-density polyethylene resin. Typical packaging includes 25 kg bags, bulk bags, or bulk truck/railcar. It is not regulated for transport under DOT, IMDG, or IATA. Store dry, away from heat, ignition, and UV light; avoid contamination.
    Storage LyondellBasell HDPE L4912 should be stored in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original bags or containers closed, palletized, and off the floor to prevent moisture, dust, and contamination. Avoid excessive stacking and prolonged UV exposure. Follow the supplier’s SDS and local regulations.
    Shelf Life LyondellBasell HDPE L4912 typically has a 12-month shelf life when stored in original, unopened packaging under cool, dry conditions away from sunlight.
    Application of LyondellBasell HDPE L4912

    In thin-wall injection molding of LyondellBasell HDPE L4912, the melt temperature band between 190°C and 225°C and the mold surface temperature between 8°C and 15°C govern the balance between flow completion and post-ejection warpage in wall sections from 0.5 mm to 1.2 mm. The material's melt mass-flow rate of 12 g/10 min measured under ISO 1133-1:2022 and density of 0.949 g/cm3 under ISO 1183-1:2019 position it for accumulator-assisted injection in stack molds with 24 to 64 cavities, but the same fluidity narrows the pressure window: cavity pressure below 45 MPa typically produces short shots at flow fronts, while cavity pressure above 75 MPa produces gate blush and intermittent flash at shut-off faces. Production-scale molders observe that cycle-time variation exceeding 0.5 s shifts gate-seal time sufficiently to alter lid-to-tub dimensional interference by 0.10 mm or more, producing intermittent capping failures on downstream filling lines.

    For direct food-contact articles under EU 10/2011 Annex I, the overall migration limit of 10 mg/dm2 and Regulation (EC) No 2023/2006 on good manufacturing practice apply; converters in the United States must demonstrate that food-contact formulations comply with 21 CFR §177.1520(c), and non-food packaging waste obligations fall under 94/62/EC. Formula additions are limited to 1.5 wt% to 2.5 wt% of pigment or mineral-filled nucleating masterbatch to reduce cycle time, and 0.3 wt% to 0.8 wt% of slip/antiblock masterbatch for demolding; regrind is restricted to 10 wt% in direct food-contact articles and 20 wt% in non-food thin-wall packaging unless migration testing validates higher fractions. Terminal product types include injection-molded dairy portion cups, margarine tubs, freezer inserts, tamper-evident deli containers, disposable non-food hygiene packaging, and thin-wall cup bodies where threads or lugs are molded on the same L4912 body.

    What Governs Torque Retention in Single-Piece HDPE Closures Molded from L4912?

    Single-piece beverage and dairy closures produced in L4912 require a controlled balance of thread-form rigidity and enough melt fluidity to fill tamper-evident band undercuts with wall thickness of 0.6 mm to 1.0 mm; the 12 g/10 min MFR allows filling of 24 to 48 cavities, yet melt temperature above 235°C oxidizes the polymer and reduces torque retention after simulated shelf loading. Compliance for food-contact closures is assessed under EU 10/2011 Annex II and FDA 21 CFR §177.1520(c); for pharmaceutical closures, USP 661.1 and USP 661.2 plastic packaging suitability tests apply, with migration and biological reactivity data governing formulation choices. In formulation terms, closures requiring thread-off torque of 1.5 N·m to 2.5 N·m under ASTM D2063 use 0.5 wt% to 1.2 wt% erucamide or silicone-based slip masterbatch, 2.0 wt% to 3.0 wt% color concentrate, and 0.1 wt% to 0.3 wt% antioxidant stabilizer; regrind addition is held below 15 wt% because higher levels broaden the molecular weight distribution and increase torque variability. The downstream process is a reciprocating-screw injection molding machine with screw L/D of 20:1 to 24:1, clamp force from 1200 kN to 2500 kN, valve-gated hot runner drops with gate diameters of 0.8 mm to 1.2 mm, holding pressure from 55 MPa to 75 MPa, and cooling time of 6 s to 9 s. Terminal products include one-piece tamper-evident beverage closures, dairy cap bodies, personal care flip-top hinge closures, and child-resistant bottle caps where thread geometry is molded directly without liner insertion.

    Stacking Load Distribution in Industrial Pail Sidewalls

    Open-top pails and lids molded from L4912 for non-dangerous and regulated liquid transport operate with nominal sidewall thickness between 2.0 mm and 3.5 mm; thicker sections generate sink marks at the intersection of sidewall ribs and handle anchors unless packing pressure is profiled to compensate for volumetric shrinkage of 1.5% to 2.5% under ISO 294-4:2018 measurement conditions. Compliance for dangerous goods packaging depends on UN certification as 1H2 open-head plastics drums or pails, with drop-test and leakproofness evaluations carried out according to ADR/RID packing group requirements; filled pails carrying liquids above flash points must be tested with water densities equivalent to the intended product class. Formulation additions for exterior durability include 2.0 wt% to 3.0 wt% carbon black or UV-stabilizer masterbatch, 0.2 wt% to 0.5 wt% antioxidant/anti-UV additive, and 0.2 wt% to 0.5 wt% release aid; controlled regrind from the same production stream is normally kept below 20 wt% because higher regrind fractions reduce the margin against UN drop-test failure on ribbed bases. The downstream process requires a single- or two-cavity pail mold on a clamp force of 8000 kN to 12000 kN, melt temperature from 200°C to 230°C, mold temperature from 12°C to 25°C, hold pressure from 40 MPa to 70 MPa for 18 s to 30 s, and total cycle time of 25 s to 40 s depending on wall thickness. Terminal product types include 5 L, 10 L, and 20 L open-top pails, tamper-evident lids, in-mold labeled containers, and integrally molded bail handles for industrial adhesives, coatings, lubricants, and non-hazardous chemical concentrates.

    Where returnable transport crates and distribution trays are molded from L4912, the main process constraint is anisotropic shrinkage across flow lengths of 800 mm to 1200 mm, not short-shot filling, because high-flow HDPE solidifies with frozen skin layers that differ in orientation between gate-to-edge and transverse directions. The injection cell requires sequential valve gating with 4 to 8 hot drops, melt temperature from 200°C to 220°C, mold temperature from 15°C to 30°C, clamp force from 12000 kN to 16000 kN, and cooling-dominated cycle times of 35 s to 60 s. Weld lines generated at the meeting points of sequential valve gates exhibit reduced impact strength unless injection-speed profiling maintains melt front temperature above 195°C at the flow-front boundary.

    Compliance for logistics packaging is governed by ISO 8611-1:2021 for flat pallet testing where applicable, ASTM D642-20 for compression resistance of filled crates, and REACH Regulation (EC) No 1907/2006 Annex XVII for restricted substances; returnable food distribution crates must also satisfy EU 10/2011 if the crates are in direct contact with unpackaged food. Formulation additions are adjusted for outdoor exposure and cold-store impact: 1.5 wt% to 2.5 wt% UV-stabilizer masterbatch, 1.0 wt% to 2.0 wt% antistatic masterbatch, and optionally 3 wt% to 5 wt% POE impact modifier for use below -20°C; regrind from rejected crate bodies is routinely blended at 25 wt% to 35 wt% when the final article does not require tight part-mass consistency. Terminal products include rigid beverage crate shells, bakery tray stacks, produce distribution trays, returnable roll cages, pallet corner blocks, and collapsible supermarket logistics boxes with integrally molded hinges and interlocking feet.

    L4912 Exhibits a Shrinkage Window of 1.5% to 2.0% in Deep-Draw Houseware Molds

    Deep-draw domestic storage boxes and drawer organizers molded from L4912 demand core-cavity dimensioning that accounts for post-mold shrinkage of 1.5% to 2.0% under ISO 294-4:2018; this range forces tooling tolerances of ±0.05 mm on snap-fit lid ledges and ±0.10 mm on base stacking ledges to preserve consistent lid assembly. Regulatory oversight for non-food housewares is anchored in REACH Annex XVII and EN 71-3:2019 for articles that could be used in children's storage or toy storage, with migration limits for soluble elements evaluated from the finished article. Formula additions are focused on surface properties and electrostatic dust attraction: 1.0 wt% to 2.0 wt% antistatic masterbatch, 1.5 wt% to 3.0 wt% pigment masterbatch, 0.3 wt% to 0.8 wt% slip/anti-scratch concentrate, and 15 wt% to 25 wt% internal regrind when color consistency allows. The downstream process uses conventional hydraulic injection molding machines with clamp force from 2500 kN to 5000 kN, screw L/D of 20:1, mold temperature from 15°C to 25°C, and profiled injection speed from 80 mm/s to 180 mm/s to avoid jetting in deep-draw flow paths. Terminal product types include household storage boxes, under-bed organizers, drawer dividers, stackable shelf bins, clothes hangers, and modular wardrobe accessories with integrally molded hinge lines and side locks.

    When Red Bag Waste Containment Requires Puncture Resistance and Autoclave Thermal Cycling

    Sharps disposal and clinical waste containers molded from L4912 are expected to survive gravity-displacement autoclave cycles at 121°C for 30 min while stacked under load; published Vicat softening temperature data for L4912 under ISO 306 is limited, so validation on the finished article under ISO 23907-1:2019 is required rather than relying on pellet-data thermal limits. Regulatory compliance combines UN 3291 for regulated medical waste packaging, ADR/RID packaging instructions for infectious substances, and ISO 23907-1:2019 requirements for sharps injury protection, particularly closure security and puncture resistance after conditioning. Formulation additions are deliberately conservative to avoid compromising sidewall toughness: 2.0 wt% to 3.0 wt% pigment masterbatch for red or yellow identification, 0.2 wt% to 0.5 wt% antioxidant/processing stabilizer, and regrind limited to 10 wt% to 15 wt% because recycled HDPE from sharps containers has uncertain thermal history and can reduce puncture resistance after autoclave exposure. The downstream process is injection molding on clamp force from 1000 kN to 2500 kN, wall thickness of 1.5 mm to 2.5 mm, melt temperature from 200°C to 215°C, mold temperature from 15°C to 25°C, and cycle time from 25 s to 35 s; hot-runner sequential gating is avoided in some configurations because gate vestiges can create puncture paths. Terminal products include single-use sharps bins, clinical waste containers, pharmaceutical disposal jars, and laboratory waste vessels with hinged tamper-evident final closure lids.

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    Certification & Compliance
    More Introduction

    LyondellBasell HDPE L4912 is a pelletized high-density polyethylene copolymer grade positioned for injection moulding of closures, thin-wall containers, and general-purpose rigid packaging. The grade is specified by a nominal melt flow rate of 12 g/10 min measured at 190 °C with 2.16 kg load under ISO 1133-1:2022 and a nominal density of 0.954 g/cm³ under ISO 1183-1:2019. Typical short-term mechanical values reported for natural pellet are tensile yield stress of 22 MPa under ISO 527-2:2012, flexural modulus of 950 MPa under ISO 178:2019, notched Izod impact strength of 2.4 kJ/m² at 23 °C under ISO 180/A:2019, Vicat softening temperature of 126 °C under ISO 306:2022, and Shore D hardness of 62 under ISO 868:2003. These values are single-point laboratory data and are not design limits. The resin is supplied as natural pellet with an antioxidant stabilization package; colour, slip, antistat, and UV additives are not part of the base specification and must be added by the converter if required. Pellet bulk density is approximately 0.55–0.60 g/cm³ under ISO 60:1977, while melt density at processing temperature is approximately 0.75–0.80 g/cm³ and should be used for shot-size calculation rather than solid density.

    What processing advantages result from a 12 g/10 min melt flow rate in thin-wall tooling?

    From a melt-rheology standpoint, the 12 g/10 min melt flow rate places L4912 among higher-flow injection moulding HDPE grades. At capillary shear rates between 10³ s⁻¹ and 10⁴ s⁻¹, high-flow HDPE undergoes shear thinning that lowers apparent viscosity relative to low-flow grades with MFR in the 0.3–1.5 g/10 min range. This viscosity reduction supports lower hydraulic injection pressure, faster cavity filling, and more uniform pressure distribution across multi-cavity closure tools. Single-point MFR data alone do not define processability; capillary rheometry under ISO 11443:2021 is required to obtain the shear-viscosity curve used in mold-filling simulation. A narrow molecular weight distribution in high-flow HDPE reduces melt elasticity and die swell, which improves dimensional repeatability in lids and caps but also limits parison sag resistance in extrusion blow moulding.

    Processors should not expect cycle time to decline linearly with MFR. In thin-wall closures with wall thickness below 0.8 mm, cooling time is governed by part thickness, mould temperature, and HDPE crystallization rate, not solely by fill speed. Production-scale experience indicates that changing from a 4 g/10 min HDPE to L4912 can reduce injection pressure by 15–25% in the same tool, but overall cycle reduction is typically controlled by gate freeze and ejection temperature requirements. Published data for this specific tool-to-tool comparison are limited; in-plant capability studies remain necessary before cycle-time commitments are made.

    On a reciprocating screw injection moulding machine with screw L/D 20:1–24:1 and compression ratio 2.0:1–3.0:1, melt temperature is maintained at 200–240 °C. Mould wall temperature is set at 10–35 °C for fast cycle operation; mould temperatures up to 50 °C improve dimensional stability in closures with tight internal diameters. Back pressure of 0.5–1.5 MPa and screw surface speed of 0.1–0.3 m/s are typical. Gate freeze time controls the cycle in most thin-wall tools; at a 0.8 mm side wall and 30 °C mould, gate freeze may occur within 2–5 s. Clamp force is estimated from projected area and a cavity-pressure assumption of 35–55 MPa in thin sections. Pre-drying is not routinely required for natural pellet, but material exposed to relative humidity above 60% or condensation should be dried for 2 h at 80 °C using desiccant air. Melt temperature above 260 °C or residence time longer than 5 min increases the risk of chain scission, yellowing, and plate-out on vents. Frequent in-plant checks of MFR per ISO 1133-1:2022 and density per ISO 1183-1:2019 are advisable because batch-to-batch variation can shift injection pressure by 5–10% in high-cavitation tools.

    Hot-runner manifold and nozzle zones should be controlled below 240 °C; stagnant zones in valve-gate systems can generate gelled particles if residence time exceeds 5 min. Purging with general-purpose HDPE or a commercial purging compound is recommended during colour changes. Venting depth should be maintained at 0.01–0.03 mm to prevent gas burn without causing flash. Screw-back settings typically include decompression of 2–5 mm and cushion of 3–6 mm to provide consistent shot volume and limit nozzle drool. On high-speed closure tools, cycle times of 6–12 s are common for wall sections below 0.8 mm, depending on part weight and cooling layout.

    Linear mould shrinkage of L4912 is typically in the range 1.5–2.0% in the flow direction and 1.8–2.4% transverse, measured after 48 h conditioning at 23 °C and 50% relative humidity under ISO 294-4:2018. Shrinkage anisotropy is strongly influenced by packing pressure and gate freeze; insufficient packing causes sink marks and loss of circularity in snap-fit closures. Warpage in flat lids is controlled by balanced cooling, avoidance of melt temperature above 240 °C, and uniform ejection. Dimensional inspection should therefore be performed after conditioning, not immediately after ejection.

    Differential scanning calorimetry under ISO 11357-3:2018 at 10 °C/min cooling typically records a crystallization peak near 116–120 °C for high-flow HDPE. The corresponding peak melting endotherm under ISO 11357-3:2018 is near 130–133 °C. These thermal transitions explain short cooling time in thin sections and show why melt temperature should remain above 200 °C to avoid premature freeze-off in thin-wall cavities. Crystallinity and shrinkage are also influenced by pack pressure; under low pack pressure, thicker sections can develop voiding and post-mould dimensional change.

    Mechanical and thermal benchmarks that separate L4912 from bimodal HDPE

    Representative natural-grade property values are tabulated below. The data are laboratory single-point results, not design allowables.

    Property Test standard Nominal value Measurement condition
    Melt flow rate ISO 1133-1:2022 12 g/10 min 190 °C, 2.16 kg
    Density ISO 1183-1:2019 0.954 g/cm³ 23 °C
    Tensile yield stress ISO 527-2:2012 22 MPa 50 mm/min
    Flexural modulus ISO 178:2019 950 MPa 2 mm/min
    Notched Izod impact strength ISO 180/A:2019 2.4 kJ/m² 23 °C
    Vicat softening temperature ISO 306:2022 126 °C Method A50
    Shore D hardness ISO 868:2003 62 15 s
    Heat deflection temperature ISO 75-2:2013 70 °C 0.45 MPa

    In comparison with bimodal HDPE pipe grades, which commonly exhibit MFR values below 0.3 g/10 min and densities of 0.958–0.960 g/cm³, L4912 trades creep resistance and slow crack growth resistance for injection moulding economy. The notched Izod value of 2.4 kJ/m² at 23 °C supports closure impact requirements but is not a replacement for ISO 16770:2019 notched creep testing used to qualify PE100 pipe grades. The flexural modulus of 950 MPa provides stacking strength in rigid packaging; continuous load-bearing service above 50 °C should be validated using tensile creep data under ISO 899-2:2021. Extrusion blow moulding grades with MFR 0.5–1.2 g/10 min retain parison shape during sag; L4912 does not possess that melt strength and is not interchangeable in bottle production.

    When Environmental Stress Crack Resistance Governs Grade Selection

    High-flow HDPE grades such as L4912 generally have lower environmental stress crack resistance than bimodal HDPE pipe grades because of lower molecular weight and reduced tie-chain density in the crystallized state. Published ESCR data for this specific grade are limited; selection for detergent, surfactant, or aggressive liquid packaging should be confirmed by testing under ASTM D1693-16 Condition B or ISO 16770:2019 notched constant tensile load. Service is generally tolerated with dilute acids, alkalis, and aqueous solutions at temperatures below 40 °C, but stress concentration at weld lines, sharp internal corners, and gate remnants must be minimized. Strong oxidizing acids, aromatic hydrocarbons, and chlorinated solvents can cause swelling, cracking, or property loss at elevated temperatures. Long-term contact with aggressive fluids should be evaluated on the final moulded part, not inferred from resin melt flow rate alone.

    Food-contact status of L4912 must be confirmed against the manufacturer’s current certificate. When the grade and additive package comply with FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011, the polymer may be considered for food-contact components provided conversion contamination is controlled. EU overall migration limits of 10 mg/dm² or 60 mg/kg apply depending on article geometry and food simulant. Specific migration tests under Regulation (EU) No 10/2011 are performed on the final article, not on resin pellets alone. Converting lines that use regrind must ensure that the regrind source is controlled and does not introduce foreign polymer or contaminants. REACH and RoHS declarations for heavy metals are typically supplied in the product regulatory documentation. Regrind from clean sprues and runners can be incorporated at levels up to 20% without substantial short-term tensile yield loss, but repeated processing beyond two cycles can reduce notched Izod impact and require revalidation per ISO 180/A:2019. The polymer is not intended for continuous service above its Vicat softening temperature or for use with strong oxidizers.

    Comparative positioning within rigid packaging polyethylene families

    Within the LyondellBasell high-density polyethylene portfolio, L4912 is designated for injection moulding applications rather than blown film, sheet, pipe, or large-part blow moulding. The 12 g/10 min MFR permits filling of wall sections below 0.6 mm in multi-cavity closures without excessive injection pressure. Film-grade HDPE with MFR 0.7–1.2 g/10 min offers better bubble stability and dart impact in blown film; L4912 is not optimized for tubular film orientation. Specialized closure grades may contain tailored slip, antistat, or UV packages, whereas L4912 is supplied as natural pellet with a general-purpose stabilization package. Processors requiring coefficient of friction control, colour, weathering, or antistatic properties must add masterbatch at the throat and verify dispersion and property retention. The grade is not intended for pressure piping, gas distribution, or structural load-bearing parts where hydrostatic strength under ISO 9080 and slow crack growth resistance are design drivers.

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