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LyondellBasell HDPE 5121B

    • Product Name: LyondellBasell HDPE 5121B
    • 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 158962

    As an accredited LyondellBasell HDPE 5121B factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell HDPE 5121B comes in 25 kg polyethylene bags, typically palletized at 1,000 kg per pallet.
    Container Loading (20′ FCL) Container Loading (20' FCL): LyondellBasell HDPE 5121B in 25 kg bags on pallets, approximately 18–20 metric tons per 20' container.
    Shipping LyondellBasell HDPE 5121B is a non-hazardous polyethylene resin. It typically ships as pellets in 25 kg bags on pallets, jumbo bags, or bulk trucks/railcars. Transport in dry, clean containers at ambient temperature, away from heat, sunlight, and moisture. No UN number or dangerous goods classification.
    Storage Store LyondellBasell HDPE 5121B in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep original packaging sealed to prevent moisture, dust, and contamination. Use pallets, avoid excessive stacking, and rotate stock. Maintain ambient temperature, protect from UV, and follow local regulations and supplier safety data sheet. Do not store near strong oxidizers or odorous materials.
    Shelf Life Shelf life is typically indefinite when stored in sealed containers, cool, dry, away from direct sunlight, moisture, and contaminants.
    Application of LyondellBasell HDPE 5121B

    LyondellBasell HDPE 5121B is applied in cold-fill dairy and delicatessen containers in the 200–1,000 mL range because the melt flow rate of 12 g/10 min at 190°C/2.16 kg under ISO 1133-1:2022 permits a flow length-to-wall thickness ratio above 150:1 in high-speed injection moulds. The specified density of 0.952 g/cm³ under ISO 1183-1:2019 provides sidewall stiffness at a nominal wall thickness of 0.6–0.9 mm without excessive flex. In production the material is processed with a reciprocating screw having 20:1–24:1 L/D and a compression ratio of 2.5:1–3.0:1; melt temperature is held at 210–230°C, and water-cooled mould cavities are kept at 15–25°C. Injection speed is set from 300 mm/s to 450 mm/s to prevent premature freeze-off at the gate, with pack pressure at 40–60 MPa for 0.8–1.5 s. Hold time is intentionally short because the thin wall freezes rapidly; extending hold pressure beyond 2 s does not increase part weight and may only increase residual gate stress. Mould vents on the parting line are cut to 0.02–0.04 mm to allow gas escape; blocked vents cause burn marks at the rim. For direct food contact, articles must satisfy FDA 21 CFR 177.1520 for olefin polymers and EU 10/2011 overall migration requirements; the overall migration limit is 10 mg/dm² when assessed with food simulant D1 under 40°C/10 days or equivalent conditions from EN 1186-1. Production also requires compliance with Regulation (EC) 2023/2006 on good manufacturing practice for food contact materials. The material is not recommended for hot-fill above 60°C, microwave reheating, or retort because the article may distort and the lid seal may fail. Terminal articles are dairy tubs, deli containers, and snap-on lids for cold-fill distribution.

    When Ejection Speed Creates Tamper-Band Tearing in High-Cavitation Closure Moulds

    In high-cavitation closure moulding, the 12 g/10 min flow characteristic is not the limiting factor; instead the ejection sequence dominates defect formation. Closures for still water, juice, and dairy products are moulded as closed-top cylinders with a tamper-evident band connected by bridges to the cap skirt. Stripper-plate ejection at speeds above 250–300 mm/s is observed to tear the bridges, particularly on 48-cavity systems with 180–250 t clamp force. Ejection speeds below 120 mm/s avoid tearing but increase cycle time and may impose ejection marks on the sidewall. The practical operating window is therefore set at 150–220 mm/s stripper speed. Melt temperature is held at 215–235°C, while core temperature is kept below 35°C to reduce part shrinkage onto the core. Packing pressure is maintained at 30–50 MPa for 1.0–1.8 s; pressures above 60 MPa can enlarge the band inside diameter and produce ovality. For cold-runner tools, submarine gates are sized at 0.8–1.2 mm; for hot-runner tools, valve-gate diameters are typically 0.6–1.0 mm. Vent grooves are cut to 0.02–0.03 mm to avoid flash while venting the upper crown. The HDPE closure must comply with FDA 21 CFR 177.1520, EU 10/2011, and Regulation (EC) 2023/2006 for food contact; organoleptic testing may be performed following EN 1230-1. The grade is not suitable for sustained CO₂ pressure retention without a liner or barrier layer because of creep in HDPE. Terminal articles include tamper-evident caps for non-carbonated beverages, snap-on dairy caps, and dry powder closures.

    What Limits Packing Pressure in 25 L UN-Certified Open-Head Pails?

    On 20–25 L open-head pails, the moulded wall thickness of 1.8–2.5 mm is thicker than in packaging, so the limiting factor is not flow length but the ability to pack the bottom and handle bosses without sink marks. Melt temperature is set at 220–240°C; injection fill time is 1.5–2.5 s. Holding pressure is raised from 50 MPa to 80 MPa for 6–10 s, but above 80 MPa the projected area of a two-cavity pail mould requires clamp force beyond 450–600 t, and flashing occurs at the parting line if clamp pressure per projected area drops below 10–12 kN/cm². Tooling uses 0.03 mm circumferential vents and a heated sprue bushing. Because high-flow HDPE has relatively fast crystallisation, the mould is kept at 25–35°C to avoid post-ejection residual stress that distorts the lid seat. For industrial chemical pails requiring UN certification under UN 1H2, the finished article is submitted to drop testing, stacking load testing, and hydraulic pressure testing under the UN Model Regulations, Chapter 6.1. The design and mould label must account for the density of the packaged liquid and the specific gravity of the HDPE article. Terminal articles are open-head pails for water-based latex, food ingredients, and non-hazardous industrial powders.

    Returnable transit crates and perforated agricultural lug boxes are produced at wall thicknesses of 3.0–4.5 mm so that the long cooling time dominates cycle economics. The flow length of HDPE 5121B permits rib-to-wall intersections and side bosses without gas traps when vents are machined at 0.03 mm. Melt temperature is set at 205–225°C and mould temperature at 20–30°C; holding pressure of 30–50 MPa is held for 4–8 s. The filling phase is completed in 2.5–4.0 s, and the total cycle is 25–40 s. Corner gussets and bottom ribs are dimensioned to provide stack load transfer rather than increasing wall thickness. The crates are assessed for compressive resistance under ASTM D642-20 and for free-fall drop under ASTM D5276-19; outdoor grades incorporate UV stabilisation because HDPE is sensitive to long-term ultraviolet exposure. Under EU 94/62/EC Article 11, the sum of lead, cadmium, mercury, and hexavalent chromium in the packaging material must not exceed 100 mg/kg. Terminal articles are returnable beverage crates, bread trays, vented produce lug boxes, and modular logistics containers.

    Stacking Lug and Draft Angle Conflicts in Two-Plate Storage Crate Tooling

    Storage totes, drawer organisers, and closet accessories use polished cores and draft angles of 1.25–1.75° per side; ejector pins are placed on rib intersections rather than on exterior surfaces to avoid visible marks. The high-flow HDPE fills rib-to-wall ratios up to 3:1 without sink marks, but a ratio above 4:1 produces visible shrinkage at the junction because the mass of the rib exceeds the cooling capacity of the adjacent wall. Mould temperature is held at 25–30°C and packing pressure is limited to 20–40 MPa because structural stiffness comes from geometric ribbing rather than high packing density. Terminal articles are stackable storage totes, drawer organisers, and closet accessories.

    When HDPE 5121B is used for toy components, the main process boundary is set by safety compliance rather than fill capability. Building blocks, wheel hubs, and ride-on toy structural parts are injection-moulded at melt temperatures of 190–220°C and mould temperatures of 20–30°C. Since the material does not require phthalate plasticisers, the restrictions under REACH Annex XVII entries 51 and 52 are not triggered by formulation. Migration of elements is tested under EN 71-3:2019+A1:2021, and toy mechanical and physical properties are assessed under ISO 8124-1:2022 or ASTM F963-17 depending on destination market. The part must also meet the dimensional and small-part hazard limitations applicable to the intended age grade. Terminal articles are toy blocks, storage bins sold as toy accessories, and ride-on toy wheels and structural panels.

    Downstream segmentStandard or regulationRelevant test or clauseCritical requirement
    Direct food contact containers and closuresFDA 21 CFR 177.1520Olefin polymer provisionsCompliance for intended food types and conditions of use
    Direct food contact articles in EUEU 10/2011Overall migration via EN 1186-110 mg/dm² overall migration limit
    Food contact manufacturing practiceRegulation (EC) 2023/2006GMP requirementsDocumented process control and traceability
    Industrial pails and packaging liquidsUN Model Regulations, Chapter 6.1UN 1H2 designationDrop, stacking, and hydraulic pressure test
    Packaging heavy-metal limitsEU 94/62/EC Article 11Total heavy-metal concentrationSum of Pb, Cd, Hg, Cr(VI) below 100 mg/kg
    Toy components in EUEN 71-3:2019+A1:2021Element migrationCategory-specific migration limits
    Toy components in North AmericaASTM F963-17Soluble heavy-metal limitsSubstrate and surface-coating limits apply
    Material identification and processingISO 1133-1:2022190°C/2.16 kg12 g/10 min melt flow rate
    Material densityISO 1183-1:2019Immersion method at 23°C0.952 g/cm³
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