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LyondellBasell HDPE 8750

    • Product Name: LyondellBasell HDPE 8750
    • 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 354286
    Grade LyondellBasell HDPE 8750
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.955 g/cm³
    Melt Index 190 C 2 16 Kg 0.5 g/10 min
    Tensile Strength At Yield 27 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break 600%
    Flexural Modulus 1200 MPa
    Vicat Softening Temperature 127 °C
    Heat Deflection Temperature At 0 45 Mpa 72 °C
    Environmental Stress Crack Resistance F50 >1000 h
    Hardness Shore D 66
    Brittleness Temperature -70 °C
    Melt Temperature 130 °C

    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 & Storage
    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.
    Application of LyondellBasell HDPE 8750

    Thin-Wall Food Packaging and the 0.55 mm Flow-Length Threshold

    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.

    When Mineral Fillers Enter HDPE 8750 Compounding, Where Does Weld-Line Strength Collapse?

    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.

    Industrial Pails, UN Certification, and Stacking Load Retention

    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 Demand Gate Vestige Limits Under ISO 527

    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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    Certification & Compliance
    More Introduction

    LyondellBasell HDPE 8750 is a high molecular weight high-density polyethylene resin positioned for large-part blow moulding, extruded sheet and profile applications where melt strength and environmental stress cracking resistance are critical. The nominal melt flow rate is 0.22 g/10 min at 190 °C under 2.16 kg load, measured in accordance with ASTM D1238-20 or ISO 1133-1:2022. The nominal density is 0.950 g/cm³ by ASTM D1505-18 or ISO 1183-2:2019. These values place the grade in the high molecular weight HDPE class, with a low melt flow rate that increases melt strength and parison hang time relative to medium molecular weight grades. The density remains high enough to provide HDPE modulus and permeation resistance, while controlled comonomer incorporation reduces excessive crystallinity that would otherwise penalize slow crack growth resistance. Typical applications include industrial containers, large closed-head drums, sheet for thermoforming and technical profiles, but the resin is not intended for thin-wall injection moulding because its high molecular weight limits spiral flow length.

    Table 1. Typical published resin properties for LyondellBasell HDPE 8750
    PropertyTest methodNominal value
    Melt flow rate at 190 °C and 2.16 kgISO 1133-1:2022 / ASTM D1238-200.22 g/10 min
    DensityASTM D1505-18 / ISO 1183-2:20190.950 g/cm³
    Tensile stress at yieldASTM D638-14 / ISO 527-2:201224.0 MPa
    Tensile elongation at breakASTM D638-14 / ISO 527-2:2012700 %
    Flexural modulus, 1% secantASTM D790-17890 MPa
    Environmental stress cracking resistance, F50, 100% IgepalASTM D1693-15b>1000 h
    Vicat softening temperature, 10 NASTM D1525-17e1125 °C

    These nominal values are derived from publicly available manufacturer data and are not a complete specification. Lot-specific certificates of analysis should be consulted for production tolerances, because rheology and mechanical properties can shift within the supplier’s release limits.

    Where the Resin Sits in the High Molecular Weight HDPE Spectrum

    The melt flow rate of 0.22 g/10 min is not simply a viscosity index; it is an indirect measure of average molecular weight and chain entanglement density. In high molecular weight HDPE, a lower melt index corresponds to a larger terminal relaxation time and a higher zero-shear viscosity. For the processor, this means the parison or extrudate resists gravitational drawdown longer than a lower molecular weight grade with a melt flow rate in the 0.35–0.60 g/10 min range. The density of 0.950 g/cm³ indicates that the resin is not a low-density or linear low-density polyethylene, but a high-density copolymer with sufficient short-chain branching to reduce lamellar thickness and increase the population of tie molecules that bridge crystalline lamellae. Although absolute molecular weight and comonomer type are not fully disclosed in the public datasheet, the low melt index and moderate density are consistent with a resin designed for slow crack growth resistance rather than for maximum stiffness. In comparison with a high-density homopolymer at 0.960 g/cm³ or above, HDPE 8750 sacrifices some modulus but gains resistance to brittle crack propagation in notched and welded regions.

    What Melt Rheology and Screw Configuration Demands Does Large-Part Extrusion Impose?

    Large-part blow moulding and sheet extrusion operations running HDPE 8750 require screw designs that can convey high-viscosity melt without excessive shear heating. A single-screw extruder with 30:1 to 36:1 L/D is common, typically using a grooved feed throat for positive solids conveying and a barrier screw with a mixing section to homogenize melt temperature. Barrel setpoints are generally maintained between 190 °C and 220 °C, while adapter and die zones are held at 200–230 °C. Melt temperature above 240 °C accelerates oxidative chain scission, which raises melt flow rate, reduces melt strength and can destabilize parison length. Because the resin exhibits shear thinning but retains high extensional viscosity at low strain rates, parison sag is controlled more effectively by melt temperature and parison programming than by screw speed alone. At the die, high shear stress can produce sharkskin melt fracture; HMW-HDPE grades such as HDPE 8750 typically have a lower critical shear rate for melt fracture than lower molecular weight grades. Published critical-shear values for this specific grade are limited, so die shear stress should be validated on the target accumulator head. Streamlined die-lips, chrome-plated surfaces and gradual flow-channel transitions are recommended to reduce localized shear concentrations.

    On a roll-stack sheet line, a gear pump is frequently installed between the extruder and die to damp screw-induced pressure pulsation and control thickness variation. Closed-loop gauge control can hold sheet thickness within ±2% of target when the gear pump inlet pressure is stable. Moisture condensation on pellet surfaces becomes a processing risk when hopper residence exceeds 8 h at relative humidity above 60%; the resulting steam can generate pinholes in sheet below 1.0 mm thickness. Pre-drying at 80 °C for 2–4 h is a standard corrective measure when ambient dew point rises above silo temperature. In the grooved feed section of the extruder, HMW-HDPE granules generate high specific torque before melting, making feed-zone screw and barrel wear a practical failure mode. Gradual throughput loss at constant screw speed, increasing melt-pressure variation and poor melt-temperature uniformity are field indicators of feed-zone wear or feed-bridge blockage.

    Environmental Stress Cracking Resistance Under ASTM D1693 and Field Failure Modes

    Environmental stress cracking resistance data for HDPE 8750 are commonly reported as >1000 h to F50 failure in 100% Igepal at 50 °C under ASTM D1693-15b. The method applies a notched bent strip under a controlled surface-active environment; time to 50% failure is a comparative indicator of slow crack growth resistance. Slow crack growth in HDPE proceeds through a craze-like zone ahead of the notch, followed by rupture of fibrils. Tie molecules bridging adjacent lamellae are the principal resistance mechanism, and higher molecular weight plus moderate density increases the likelihood that a given chain participates in more than one crystalline region. This laboratory result is relevant to blow moulded containers with pinch-off seams, weld lines and sharp base corners, where frozen-in orientation and thickness transitions create triaxial stress states. In actual service, crack initiation is frequently observed at the base pinch-off junction or at threaded closure transitions. However, ESCR is processing-dependent: rapid cooling from the melt increases localized orientation and can reduce failure time in the same geometry. Part-level top-load, drop-impact and weld-line testing on production mouldings should therefore supplement datasheet ESCR values.

    Chemical exposure boundaries require immersion testing rather than inference from ESCR alone. Polar detergent solutions, emulsifiable concentrates and aromatic solvents can plasticize or stress-crack HDPE at elevated temperatures. Published data for HDPE 8750 in specific aggressive media is limited; compatibility testing per ASTM D543 is required when the service environment contains surfactants above 10% concentration or imposes continuous exposure above 50 °C. Continuous exposure to strong oxidizing acids at temperatures above 40 °C should be avoided unless supported by long-term testing, because oxidative chain scission can degrade surface integrity. For geomembrane and outdoor sheet applications, carbon black dispersion is critical: a loading of 2.0–3.0 wt% angular carbon black with aggregate size below 20 μm is standard for UV stabilization, and oxidative-induction time per ISO 11357-6 should be verified on the compounded product.

    When Substitution for Unimodal Blow Moulding Grades Is Evaluated

    When HDPE 8750 is substituted for a lower molecular weight unimodal blow moulding grade with a melt flow rate near 0.45 g/10 min, the first processing response is an increase in extruder head pressure at constant screw speed. This follows from the higher molecular weight and longer relaxation time. Die swell and parison swell also change; the lower melt flow rate generally increases extrudate swell, so annular die gaps may need adjustment to maintain the same parison wall thickness. The compensating advantage is greater hang strength: longer parison drop lengths and larger container diameters can be formed before drawdown failure. Compared with a high-flow injection moulding HDPE having a melt flow rate above 8 g/10 min, HDPE 8750 is unsuitable for thin-wall injection moulding because spiral flow length is low and required clamp pressures are disproportionate. The grade is therefore positioned between medium molecular weight blow moulding resins and very high molecular weight sheet resins. Selection should consider accumulator capacity, part mass, target wall-thickness distribution, post-cooling cycle time and actual weld-line performance, rather than melt flow rate alone. Published machine-specific throughput comparisons for HDPE 8750 are limited; head-pressure data should be generated on the intended production extruder before product transfer.

    Regulatory status must be confirmed with the supplier for the final article. HDPE 8750 is typically evaluated for compliance with FDA 21 CFR 177.1520 for olefin polymers in food-contact applications and with EU Regulation No 10/2011 for plastic materials intended to come into contact with food. The resin is not inherently flame retardant; if used in electrical enclosures, the compounded part must meet IEC 60695-11-10 flammability requirements. For RoHS-covered articles, the supplier should be requested to confirm the absence of restricted substances listed in Directive 2011/65/EU Annex II above threshold concentrations. Downstream converters must verify lot-specific certificates, migration compliance for the final article and weld or seam performance on production tooling before release.

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