| HS Code | 143087 |
As an accredited LyondellBasell HDPE RLLP621 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE RLLP621 is supplied in 25 kg polyethylene bags, typically 40 bags per pallet (1,000 kg total). |
| Container Loading (20′ FCL) | 20′ FCL loading: LyondellBasell HDPE RLLP621 in 25 kg bags, palletized, shrink-wrapped, securely stowed, optimizing container payload for safe transport. |
| Shipping | LyondellBasell HDPE RLLP621 is a non-hazardous high-density polyethylene resin. It is not regulated for transport by DOT, IMDG, IATA, or ADR; no UN number, hazard class, or packing group applies. Ship in closed bags or octabins, keep dry, and avoid heat, ignition sources, and dust generation. Transport as general cargo. |
| Storage | Store LyondellBasell HDPE RLLP621 indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep original containers or bags closed to prevent moisture, dust, and contamination. Elevate pallets off floors, rotate stock, and protect from physical damage. Avoid contact with strong oxidizers. Follow the supplier’s SDS and local regulations for safe handling and storage. |
| Shelf Life | Typically 24 months when stored unopened in original packaging, dry, at moderate temperatures, away from direct sunlight and ignition sources. |
For twist-off HDPE closures, LyondellBasell HDPE RLLP621 is processed on high-cavitation injection moulding lines where hot-runner balance and gate freeze-off control the dimensional consistency of the sealing bead. Melt temperature is held between 190 °C and 230 °C; mould temperature is set between 8 °C and 25 °C. Injection speed is adjusted to 80–120 mm/s at the screw tip, with holding pressure between 400 bar and 700 bar and back pressure between 50 bar and 100 bar. A reciprocating screw with an L/D ratio of 20:1 and a compression ratio of 2.5:1 is standard on 32-cavity and 48-cavity closure tools. Mould shrinkage falls between 1.4% and 2.2% in the flow direction and 1.2% to 1.8% transverse, measured after 48 h at 23 °C and 50% relative humidity. The closure compound typically contains 1.5–3.0 wt% colour masterbatch, 0.05–0.15 wt% hindered phenolic antioxidant, and 0.03–0.08 wt% slip/antiblock additive. Regrind at 30 wt% is common in non-food closures; food-contact closures require clean scrap and migration testing. Compliance for beverage closures uses FDA 21 CFR 177.1520(c) 2.1 or 2.2 depending density, EU 10/2011 overall migration below 10 mg/dm², and CONEG heavy metals below 100 ppm. ESCR screening per ASTM D1693-15 Condition B should be run on each regrind lot. Finished parts include still water closures, aseptic beverage caps, and pharmaceutical child-resistant caps. Process bottlenecks on high-cavitation tools include gate blush at the annular gate and dimensional drift after hot-runner nozzle tip wear. The grade is not recommended for carbonated soft drink closure shells unless oxygen permeation and top-load retention are separately validated.
In thin-wall food packaging, the practical cycle time is limited by cooling and ejection rather than melt plasticising. The melt temperature is set at 190–220 °C and the mould at 8–30 °C. Wall sections of 0.45–1.20 mm are filled in 0.3–0.6 s using accumulator-assisted injection. Demoulding is initiated when the part surface temperature falls below 70 °C. A nucleating agent at 0.05–0.2 wt% is added to increase crystallisation temperature and reduce post-mould warpage. Colour masterbatch is used at 1–3 wt%; regrind is limited to 20–50 wt% depending on food-contact status and the presence of in-line metal detection. The supplier datasheet should be consulted for the exact ISO 1133-1:2022 melt flow rate, because high-speed filling requires the MFR value in the upper half of the specified range. Pre-drying is not normally required; if granulate is stored below dew point or exposed to relative humidity above 60%, surface moisture may create silver streaks. Finished parts include dairy cups, tamper-evident lids, and single-use fruit containers.
| Application | Requirement | Standard/Test | Typical Limit |
|---|---|---|---|
| Food contact | Overall migration | EU 10/2011 | 10 mg/dm² |
| Food contact | Resin compliance | FDA 21 CFR 177.1520(c) | Density-specific olefin polymer |
| Heavy metals | Sum of Pb, Hg, Cd, Cr VI | CONEG Model Toxics | 100 ppm |
| REACH SVHC | Candidate list substance | EC 1907/2006 | 0.1 wt% |
When 5 L to 25 L open-head pails are injection moulded from HDPE RLLP621, the design priority is drop-impact retention after cold conditioning. Melt temperature is maintained at 200–240 °C and mould temperature at 15–30 °C. Clamp force on production lines ranges from 5000 kN to 12000 kN for shot weights between 800 g and 2000 g. Wall thickness is held at 1.8–3.2 mm. Carbon black masterbatch at 2.5–4.0 wt% of a 40% carbon black concentrate provides UV screening; 0.1–0.3 wt% hindered amine light stabilizer is added for long-term outdoor stacking. Regrind use is limited to 20–35 wt% because higher levels reduce ESCR and cold-temperature drop impact. Drop impact is measured per ASTM D5276-19 after 24 h at -18 °C. Stacking strength is evaluated per ASTM D4577-19 under constant load at 40 °C for 14 days. For pails certified for dangerous goods, UN 1H2 qualification requires a 1.2 m drop after storage at -18 °C and a 100 kPa hydrostatic pressure test for 30 min. End products include chemical pails, lubricant pails, and food ingredient pails. Processing bottlenecks on production tools are weld-line weakness at handle bosses and inconsistent wall thickness at the top chime.
Crate and pallet tools originally balanced for polypropylene require rebalanced gating when HDPE RLLP621 is substituted because the shrinkage range differs. HDPE mould shrinkage in logistics parts is 1.2–2.0%, while PP typically shrinks 1.0–1.8% depending wall thickness. Melt temperature is set at 200–230 °C, mould temperature at 15–30 °C, and injection speed is reduced to avoid jetting in thick ribs. Back pressure of 30–60 bar and screw rotation speed of 60–100 rpm improve additive dispersion. Unfilled HDPE flexural modulus is lower than PP; the addition of 10–25 wt% talc or calcium carbonate increases the flexural modulus from the unfilled range of 900–1300 MPa to 1800–2600 MPa when tested per ASTM D790-17. A maleic anhydride-grafted polyolefin coupling agent at 1.0–2.0 wt% may be used to improve filler-matrix adhesion. Post-consumer recycled HDPE can be incorporated at 25–50 wt%, but impact strength under ASTM D256 may fall by 15–30% depending the recycled fraction. Compliance for export is maintained under RoHS 2011/65/EU and REACH SVHC thresholds. End products include beverage crates, distribution pallets, and collapsible storage boxes. Process bottlenecks include sink marks over thick bosses and warpage caused by differential shrinkage between flow and transverse directions.
HDPE RLLP621 can be injection moulded into PE100 water network fittings when the final part passes hydrostatic strength testing under ISO 4427-3:2019. Melt temperature is held between 190 °C and 220 °C; mould temperature between 15 °C and 30 °C. Hot-runner balancing is more critical in fittings than in solid-walled pipe because weld lines at the intersection of the bore and outlet can reduce burst pressure. Injection speed is reduced to 40–70 mm/s at the screw tip, and holding pressure is maintained at 500–800 bar for 8–15 s. Shrinkage ranges from 1.5% to 2.5%, requiring core-pin retraction to avoid microcracking at the sealing surface. The compound should contain 0.1–0.2 wt% thermal stabilizer and 0.05–0.15 wt% processing aid. Regrind is generally excluded from pressure-bearing fitting bodies because hydrostatic strength loss may exceed acceptable limits. Potable water contact requires NSF/ANSI 61 or AS/NZS 4020; European potable water fittings typically conform to EN 12201-3 and ISO 4427-3. End products include compression fittings, tapping tees, and valve bodies for PE100 distribution systems. ESCR testing per ASTM D1693-15 Condition C is used as a screening tool, but the controlling qualification is the 20 °C, 100 h, 12.4 MPa hoop stress requirement for PE100. Not all injection-moulding HDPE grades meet PE100 hydrostatic classification; material-specific hydrostatic testing is mandatory before this application is qualified.
Storage containers, buckets, and appliance housings made from HDPE RLLP621 are moulded at melt temperatures of 190–230 °C and mould temperatures of 10–30 °C. Injection pressure is set between 600 bar and 1000 bar, with clamp force from 1500 kN to 5000 kN depending projected area. Colour masterbatch is used at 1–2 wt% for opaque shades. Antistatic additives are incorporated at 0.05–0.2 wt% to reduce dust attraction; published data for specific static decay times in this precise compound is limited. Antioxidant levels of 0.05–0.15 wt% are common for long-term thermal stability during processing. Mould shrinkage is 1.4–2.2%; dimensional checks after 24 h at 23 °C and 50% relative humidity are required before release to production. This application is governed by REACH SVHC 0.1 wt% limits and RoHS 2011/65/EU for electrical and electronic appliance housings. End products include storage boxes, buckets, vacuum cleaner housings, and white appliance internal panels. Processing bottlenecks are weld lines at handle bosses and sink marks opposite ribs; these are controlled by gas counterpressure or by reducing rib thickness to 50–60% of the nominal wall. Post-mould annealing is not normally required, but parts with thick bosses may require 2–4 h at 80 °C to stabilise dimensions before assembly.
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