| HS Code | 354286 |
As an accredited LyondellBasell HDPE 8750 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE 8750 is typically packaged in 25 kg polyethylene bags, palletized for industrial handling and transport. |
| Container Loading (20′ FCL) | 20′ FCL container loading of LyondellBasell HDPE 8750: palletized bags, securely strapped, moisture-protected, labeled, and stowed for safe ocean export. |
| Shipping | LyondellBasell HDPE 8750 is a non-hazardous high-density polyethylene resin. It is shipped as solid pellets in moisture-resistant 25 kg bags, palletized and stretch-wrapped, or in bulk trucks/rail hopper cars. Store dry, away from direct sunlight, heat, and contamination. No special transport placards are required. |
| Storage | Store LyondellBasell HDPE 8750 in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and flames. Keep containers tightly closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and temperatures above recommended limits. Protect from physical damage and incompatible oxidizers. Use appropriate labeled containers. Follow local regulations and the manufacturer’s SDS for safe handling and storage. |
| Shelf Life | Typically, LyondellBasell HDPE 8750 has a 24-month shelf life when stored unopened in cool, dry conditions away from direct sunlight. |
Injection-molded thin-wall containers made from LyondellBasell HDPE 8750 operate within a wall-thickness window of 0.45–0.80 mm, where gate-to-flow length ratio becomes the primary control variable rather than melt temperature alone. Food-contact compliance for these articles is governed by FDA 21 CFR 177.1520(c) for semi-crystalline olefin polymers, EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm², and GB 4806.7-2016 where Chinese food-contact documentation is required. Because the resin is nonpolar, global migration into aqueous and fatty food simulants remains low; however, the molded article must be tested because masterbatch letdown and process lubricants can introduce low-molecular-weight species above organoleptic thresholds. The standard production formulation starts with 100 parts HDPE 8750 and adds 1.5–4.0 phr color masterbatch, 0.1–0.3 phr processing lubricant, and 0.05–0.2 phr antioxidant carrier when post-industrial rework is below 15 wt%.
On high-speed injection molding machines with clamp forces of 250–500 t, screw L/D ratios of 20:1–24:1, and accumulator-assisted injection, the melt temperature is held at 210–235 °C, mold temperature at 10–20 °C, and injection speed at 80–120 mm/s. Holding pressure is set between 40 MPa and 60 MPa, with cooling time of 3.5–7.5 s depending on rim thickness. Edge gates with land lengths of 0.8–1.2 mm and gate thickness of 60–80% of the nominal wall are preferred because center-sprue gates create visible vestiges on the food-contact surface. For stack molds with 32–64 cavities, fill imbalance is corrected by altering gate land length rather than raising melt temperature, because the grade exhibits shear-thinning behavior that makes runner diameter a more effective balancing tool. Cold-runner diameters of 6–8 mm are standard, and venting depths of 0.015–0.020 mm along the parting line prevent gas burn marks at the rim. Terminal product types include dairy cups, delicatessen containers, take-away closures, and single-serve frozen food tubs. Pre-drying is not normally required unless sacks have been stored outdoors at relative humidity above 60%, and melt residence time above 10 minutes should be avoided to suppress oxidative gel formation.
Tamper-evident caps molded from HDPE 8750 fail more often at the tamper ring hinge than at the sealing surface because the break sequence depends on molecular orientation at the gate and the concentration of slip agent that has migrated to the surface during storage. For non-carbonated beverage, dairy, and dry-goods closures, the formulation is 100 parts HDPE 8750, 1.0–3.0 phr color masterbatch, 0.3–1.0 phr erucamide slip concentrate, and 0.05–0.2 phr nucleating masterbatch to control cap ovality. Food-contact compliance for the cap uses FDA 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011; in addition, torque-retention testing on the finished bottle closure is performed after 24 h of conditioning, and organoleptic evaluation under 40 °C aging for 10 days is required when slip-agent addition exceeds 0.8 phr. The production process uses injection molding machines with clamp force of 250–450 t, hot-runner systems with valve gate diameters of 0.6–1.2 mm, melt temperature 215–230 °C, and mold temperature 12–18 °C. A two-stage injection profile is used: the first 1.5 cm³ is injected at high speed to seat the gate, followed by a reduced velocity of 40–60% of maximum to prevent jetting and gate-stringing. Target cycle time is 4.0–6.5 s. Terminal product types are tamper-evident beverage caps, pharmaceutical cap bodies, and dry-goods overcaps. The limiting boundary is that erucamide loadings above 1.2 phr degrade print adhesion and may exceed sensory migration limits in fatty food simulants; carbonated soft-drink closures should not be produced from this formulation unless storage temperature is below 30 °C and creep rupture testing at 0.4 MPa internal pressure is completed.
Compounding HDPE 8750 with lamellar talc for automotive washer reservoirs, HVAC ducts, and appliance brackets introduces a conflict between stiffness gain and weld-line fusion, particularly when filler loadings exceed 18 wt%. The formulation starts with 100 parts HDPE 8750, 10–25 wt% talc with median particle size 1.5–3.0 µm, 0.5–1.5 wt% maleic anhydride grafted polyethylene coupling agent, and 0.2–0.6 wt% antioxidant masterbatch. Regulatory compliance for European automotive components is based on REACH Regulation (EC) No 1907/2006 for SVHC declarations and RoHS Directive 2011/65/EU Annex II for restricted heavy metal content; mechanical acceptance uses ISO 179-1:2010 Charpy impact and ISO 527-2:2012 tensile yield stress. The compounding process is performed on a corotating twin-screw extruder with an L/D of 40:1, screw speed 250–450 rpm, barrel set points 170–225 °C, and die-plate melt temperature 190–220 °C. Vacuum devolatilization at −0.08 MPa is applied before the dispersion zone to strip moisture from the talc. The strand-pelletized compound is then injection molded with mold temperature raised to 25–40 °C, and gate location moved away from weld zones to restore fusion. Below 18 wt% talc, a standard three-zone screw may be sufficient; above 22 wt%, mixing elements in the plastication zone and a check ring gap of 1.5–2.5 mm are required to prevent streaks and delamination at the weld line. Terminal product types are automotive HVAC air-duct sections, washer fluid reservoirs, battery protective covers, and under-hood clips. The main operational boundary is that high-aspect-ratio talc reduces weld-line strength nonlinearly with increasing filler content; published data for this specific configuration is limited, so production trials on the planned twin-screw equipment are required before scale-up.
Open-head and tight-head industrial pails molded from HDPE 8750 for dangerous goods are governed less by short-term tensile strength than by drop-impact and stacking performance required under UN Model Regulations Chapter 6.1 and, in the United States, 49 CFR Part 178 Subpart L for non-bulk performance-oriented packagings. The typical formulation for black or blue pails uses 100 parts HDPE 8750, 1.5–4.0 phr carbon black masterbatch for UV stabilization, 0.3–0.6 phr primary/secondary antioxidant, and 0.5–1.0 phr fluoroelastomer processing aid when melt fracture appears near the gate. Production is performed on injection molding machines with clamp force of 800–1200 t, melt temperature 200–230 °C, mold temperature 15–25 °C, and cool-down time adjusted to local wall thickness of 1.5–3.0 mm. Post-mold cooling fixtures are mandatory to prevent lid-seat distortion below 0.15 mm. Gate design normally uses a diaphragm gate or three-point pin gate to balance hoop stresses; a center-sprue gate is avoided because it creates molecular orientation along the sidewall that reduces stacking creep resistance. Cold-region pails require drop testing at −18 °C after conditioning for 24 h, typically from 0.8 m to 1.8 m depending on Packing Group. Terminal products are UN-rated pails from 5 L to 25 L for solvent, adhesive, and powdered chemical packaging. The critical boundary is that carbon black loadings above 4.0 phr can overload the melt pump and reduce weld-line impact; insufficient venting cannot be compensated by higher injection pressure without increasing flash at the parting line.
Creep modulus, not Charpy impact, controls sackable distribution crates molded from HDPE 8750 when loaded at 45 °C for warehouse storage exceeding 30 days. The formulation consists of 100 parts HDPE 8750, 1.5–4.0 phr color masterbatch, 0.3–0.8 phr hindered amine light stabilizer for outdoor deployment, and optionally 2.0–5.0 phr polyolefin elastomer as a low-temperature impact modifier when cold-store racking below −20 °C is specified. Performance validation follows ISO 8611-1:2011 for flat pallet load-deflection and ASTM D2990-17 for compressive creep; structural crates are additionally tested to ISO 178:2019 flexural modulus and ISO 179-1:2010 Charpy impact. The downstream process is structural foam injection molding on 1200–2000 t clamp force machines, with 0.1–0.3 wt% nitrogen chemical foaming agent, gas counter pressure in the mold, and melt temperature 195–220 °C. Cycle time is dictated by foam skin formation and is normally 60–120 s for pallets in the 20–35 kg range. Terminal products are nestable distribution crates, rackable pallets, and collapsible agricultural crates. The known boundary is that foaming agent dosing above 0.3 wt% produces visible gas swirl marks and unpredictable cavity-to-cavity fill variation when mold temperature exceeds 25 °C.
Household storage boxes and multi-compartment organizers molded from HDPE 8750 accumulate quality claims at the hot-runner gate vestige because visible gate protrusion interacts with stack loading and stress concentration at the sidewall. The formulation is 100 parts HDPE 8750, 2.0–5.0 phr color masterbatch, 0.5–1.5 phr slip agent, and 0.1–0.4 phr antistatic masterbatch for dust-resistant storage. Regulatory references include FDA 21 CFR 177.1520(c) when the container is marketed for dry food storage and EU Regulation (EU) No 10/2011 for overall migration below 10 mg/dm²; mechanical acceptance uses ISO 527-2:2012 tensile yield stress for the lid hinge and ASTM D648-18 heat deflection temperature at 0.455 MPa. Production is performed on multi-cavity hot-runner injection molding machines with valve gate diameters of 0.8–1.5 mm, melt temperature 210–230 °C, mold temperature 15–20 °C, and holding pressure 35–55 MPa; gate vestige height is controlled to below 0.05 mm by adjusting nozzle retraction time rather than reducing holding time. Terminal products are stackable household storage totes, pantry canisters, and office organizers. The main operational boundary is that antistatic masterbatch loadings above 0.4 phr reduce weld-line strength in the handle area and should not be specified for containers with living hinges.
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