| HS Code | 516845 |
As an accredited LyondellBasell HDPE L5485 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE L5485 is packaged in 25 kg polyethylene bags or 1,000 kg bulk bags for transport and storage. |
| Container Loading (20′ FCL) | 20′ FCL loading of LyondellBasell L5485 HDPE: 25 kg bags on pallets, stretch-wrapped, secured in container for safe ocean transport. |
| Shipping | LyondellBasell HDPE L5485 is typically shipped as non-hazardous polyethylene pellets in 25 kg bags, jumbo bags, or bulk trucks/railcars. Keep packaging sealed and dry, away from heat, sunlight, and ignition sources. Not classified as dangerous goods; follow local transport regulations and avoid contamination. |
| Storage | Store LyondellBasell HDPE L5485 in a cool, dry, well-ventilated area in closed original containers. Protect from direct sunlight, moisture, dust, and contaminants. Keep away from heat, sparks, flames, and strong oxidizers. Avoid prolonged UV exposure. Store at ambient temperature, preferably below 50°C. Use first-in, first-out rotation, clean handling, and keep containers sealed and pallets off the floor. |
| Shelf Life | Store dry, cool, well-ventilated, away from sunlight; LyondellBasell HDPE L5485 has a recommended shelf life of 12 months from delivery. |
In direct food-contact rigid packaging, LyondellBasell HDPE L5485 is specified on the basis of a nominal density of 0.954 g/cm³ (ASTM D1505) and a melt flow rate of 5.2 g/10 min at 190 °C/2.16 kg (ASTM D1238-23a). Compliance under FDA 21 CFR 177.1520(c) 3.2 covers olefin polymers used with aqueous, acidic, and fatty foods. Under Regulation (EU) No 10/2011 Annex I, the overall migration limit is 10 mg/dm², while specific migration limits for additives remain controlling. The following matrix consolidates the compliance boundary before formulation and processing parameters are introduced.
| United States | 21 CFR 177.1520(c) 3.2 | High-density olefin polymers for aqueous, acidic, and fatty food-contact use |
| European Union | Regulation (EU) No 10/2011 Annex I | Overall migration limit 10 mg/dm²; specific migration limits for positive-list additives |
| European Union | Regulation (EC) No 2023/2006 | Good manufacturing practice for food-contact materials |
| United States | 21 CFR 178.3297 | Colorants for polymers used in food-contact applications |
Formulation addition levels within the food-contact boundary are set by carrier resin compatibility and additive migration behavior. FDA-compliant color concentrate is introduced at 0.5–1.5 wt% for tub wall thicknesses below 1.0 mm and at 1.0–2.0 wt% for pail sidewalls above 1.8 mm. A slip and antiblock masterbatch containing 10 wt% erucamide is dosed at 0.2–0.5 wt%, yielding an active erucamide level of 0.02–0.05 wt% in the final melt. Active erucamide above 0.08 wt% lowers lid seal friction below assembly torque requirements and promotes core plate-out on extended production runs. Post-industrial regrind from the same food-contact compound may be reintroduced up to 30 wt% when the melt flow rate shift measured by ASTM D1238-23a remains within 0.5 g/10 min of virgin lots.
Processing on reciprocating-screw injection molding machines with screw L/D of 20:1 to 24:1 and compression ratio of 2.2:1 to 2.5:1 uses rear-zone temperatures of 180 °C, center zones of 195–205 °C, front zones of 210–220 °C, and nozzle settings of 200–220 °C. Mold temperature is held at 10–30 °C with turbulent cooling channels to limit warpage in thin-walled tubs. Hold pressure below 45 MPa on thick pail bosses creates visible sink marks, while melt temperatures above 230 °C increase odor generation and yellowing in fatty-food pails. Injection velocity is set at 80–120 mm/s for flow lengths up to 150 mm at wall thickness 0.6 mm to prevent short shots on high-speed multi-cavity lines cycling above 12 shots/min. Terminal products include 1–5 L sauce and dairy pails, 150–500 mL snap-lid tubs, deli container bodies, and tamper-evident lid systems used in chilled distribution.
Closure skirts produced from HDPE L5485 are typically molded in 38 mm and 43 mm tamper-evident configurations for non-carbonated dairy, juice, and spoonable dressing systems. The compliance framework is FDA 21 CFR 177.1520(c) 3.2 and Regulation (EU) No 10/2011, supplemented by Regulation (EC) No 1935/2004 for overall food-contact safety. ISO 8317:2015 applies only when the closure is marketed as child-resistant; for standard beverage closures it does not govern. Supplier declarations of compliance must cover the slip additive, color concentrate, and any processing aid introduced in the mold.
Slip addition in closure molding is controlled within a narrow band. A 10 wt% erucamide masterbatch is dosed at 0.2–0.5 wt%, equivalent to 0.02–0.05 wt% active erucamide. At active erucamide above 0.08 wt%, removal torque on 38 mm skirts falls below 1.0 N·m, and the migrated slip film on core surfaces causes ejection friction and tamper-band deformation. Color concentrate is introduced at 0.4–1.2 wt%. Formulations that omit slip entirely produce removal torque above 3.5 N·m and stress-whitening at the tamper band. This grade is not recommended for carbonated soft-drink closures because top-load and pressure-retaining sealing requirements are outside the specification envelope of the material.
Production-scale closure tools with 32 to 64 cavities require valve-gated hot runners or direct-gated cold runners with melt temperature held at 204–215 °C. Mold temperature is set at 8–15 °C to reduce cycle time to 5–8 s for closures weighing 2.0–3.5 g. Injection pressure at transfer is 70–90 MPa, hold pressure 40–60 MPa, and injection velocity 80–120 mm/s. Velocity reductions below 40 mm/s during filling of the tamper-band hinge cause short shots and inconsistent band elongation. If melt temperature exceeds 220 °C, longitudinal molecular orientation in the hinge region is reduced and the tamper-evident band fails during capping. Terminal products include 38 mm dairy cap shells, 43 mm sauce and dressing caps, overcaps for dry food canisters, dispensing flip-top caps, and measuring cup closures for liquid household chemicals.
When an open-top industrial pail is certified for dangerous goods transport, the resin must demonstrate sufficient environmental stress crack resistance after passing UN 3H2 performance tests, including stack loading at 40 °C for 28 days and drop impact after conditioning. The compliance chain includes UN Model Regulations Chapter 6.1, ADR/RID Chapter 6.1, and IMDG Code Chapter 6.1 for open-top plastic jerricans. A packaging group II test program is frequently referenced for chemical fillings up to 1.5 kg/L relative density.
Formulation for industrial pails differs from food-grade pail molding because external weathering and chemical exposure dominate. UV-stabilized color masterbatch is added at 0.6–1.2 wt%, carbon black masterbatch at 2.0–2.5 wt% for outdoor or abrasive chemical service, and antioxidant masterbatch at 0.2–0.5 wt%. Slip additives are omitted or held below 0.1 wt% because lid engagement and gasket sealing under stack load are more critical than surface slip. Post-industrial regrind is limited to 25 wt%; higher regrind levels introduce label adhesive, oil contamination, and low-molecular-weight fractions that produce pinholing near pail handles.
On production lines using 1,200–1,500 t clamp force machines, open-top pails of 20 L shot weight 1.2–2.5 kg are molded with barrel rear-zone temperature 180 °C, mid-zone 195–205 °C, front-zone 210–220 °C, and nozzle 220 °C. Mold temperature is held at 10–25 °C, hold pressure at 50–70 MPa, injection pressure at 90–110 MPa, and cooling time at 20–35 s. If surface moisture is present on regrind stored at RH above 60%, a pre-drying step at 70 °C for 1–2 h is required to prevent splay on the pail sidewall. Screw speed is limited to 50–80 rpm to avoid excessive shear heating that raises melt temperature above 230 °C and creates yellowing near the sprue. Terminal products include 5 L, 10 L, 20 L, and 25 L open-top pails for water-based coatings, adhesives, inks, textile dyes, pool chemicals, and concentrated detergent intermediates.
Returnable transport packaging exposes the material to both sub-zero impact and repeated sanitization cycles. The compliance baseline is REACH Regulation (EC) No 1907/2006 Annex XVII, RoHS Directive 2011/65/EU where electronic waste handling is involved, and the CONEG heavy-metal limit of 100 ppm total lead, mercury, cadmium, and hexavalent chromium for packaging. For direct food-contact bakery trays and dairy crates, FDA 21 CFR 177.1520(c) 3.2 and Regulation (EU) No 10/2011 apply.
Color-coded crate production uses 0.5–2.0 wt% color concentrate, 0.5–1.0 wt% HALS and UV stabilizer masterbatch, and 0.2–0.5 wt% antioxidant masterbatch. Regrind is introduced at 20–40 wt%, but the high-flow character of L5485 requires lot-specific melt flow rate comparison against virgin resin. If melt flow rate increases more than 0.8 g/10 min, impact strength in corner gussets falls below the threshold for drop impact at -20 °C. Foaming agents and gas-assisted molding are avoided because the melt strength of this grade is insufficient for uniform cell structure.
Conventional injection molding for crates uses wall thicknesses of 2.5–4.0 mm, melt temperature 200–215 °C, mold temperature 15–25 °C, hold pressure 40–60 MPa, and cooling time 25–40 s. Sequential valve gating on hot runners controls weld lines around corner ribs; linear injection velocity is 60–100 mm/s. In high-cavity stack molds, clamp force requirements range from 8,000 kN to 12,000 kN. When regrind exceeds 40 wt%, the processing window narrows because reduced molecular weight lowers melt viscosity and promotes flash at the parting line. Quantitative drop-impact data for L5485 at 40 wt% regrind in thin-wall ventilation ribs are limited in public datasheets; processor qualification should therefore include notched Izod and multi-axial impact tests on production-representative plaques. Terminal products include nestable dairy crates, beverage distribution trays, collapsible pallet boxes, ventilated agricultural harvest crates, and bakery stacking trays for automated warehouse systems.
Child-resistant pharmaceutical closures and dosing cups require additive selection that permits the closure to pass ISO 8317:2015 senior-adult and child-resistant panel tests while remaining compliant with FDA 21 CFR 177.1520 and USP <661.1> for plastic packaging systems used with oral dosage forms. The European pharmacopoeial framework for polyolefin packaging, including Ph. Eur. monograph 3.1.5, is applied where the closure is part of a drug product dossier.
Color concentrate is limited to 0.2–0.8 wt% and must be PE-carrier based to avoid affecting torque retention. Slip additives are either omitted or added at 0.05–0.1 wt% final active concentration. Higher slip levels compromise child-resistant push-turn or squeeze-turn mechanisms by reducing the coefficient of friction below the design assumption. Organic peroxide processing aids and silicone-based additives are not introduced where they might alter USP <661.1> extractables.
Closure tooling uses 16 to 48 cavities, valve-gated hot runners, and melt temperatures of 195–215 °C. Mold temperature is 10–20 °C. For a 1.5–2.5 g closure, injection velocity is set at 60–100 mm/s, hold pressure at 50–70 MPa, and cooling time at 6–10 s. Long flow paths across the child-resistant engagement teeth require packing pressure maintained for 2–3 s after velocity-to-pressure transfer. If packing is removed too early, the teeth shrink unevenly and removal torque falls outside the 1.5–3.0 N·m specification window after accelerated aging at 40 °C/75% RH for 6 months. Terminal products include 28 mm and 33 mm child-resistant caps for solid oral dose bottles, graduated dosing cups of 10–30 mL, and closure shells for pediatric liquid formulations.
Housewares and appliance interior parts formed from L5485 are governed by REACH Regulation (EC) No 1907/2006 Annex XVII and, for children’s storage items marketed as toys, EN 71-3 migration limits for specific elements; food-contact kitchenware falls under Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520. Color concentrate is added at 0.5–1.5 wt%, antistatic masterbatch at 0.5–1.0 wt% for dust-sensitive appliance housings, and antioxidant masterbatch at 0.2–0.4 wt%. Production uses melt temperatures of 190–210 °C, mold temperatures of 15–25 °C, hold pressures of 35–55 MPa, and wall thicknesses of 1.2–2.5 mm; terminal products include storage bins, waste containers, refrigerator shelf brackets, detergent dispenser housings, and appliance kick plates.
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