| HS Code | 883075 |
| Productname | LyondellBasell HDPE M6580WC |
| Polymertype | High Density Polyethylene (HDPE) |
| Density | 0.958 g/cm³ |
| Meltflowrate | 0.8 g/10 min (190°C/2.16 kg) |
| Tensilemodulus | 1100 MPa |
| Tensilestressatyield | 26 MPa |
| Tensilestrainatyield | 9% |
| Tensilestrainatbreak | >600% |
| Flexuralmodulus | 1200 MPa |
| Charpynotchedimpactstrengthat23c | 15 kJ/m² |
| Charpynotchedimpactstrengthatminus30c | 8 kJ/m² |
| Vicatsofteningtemperature | 125 °C |
| Heatdeflectiontemperatureat0 45mpa | 70 °C |
| Meltingtemperature | 130 °C |
| Environmentalstresscrackresistance | >1000 h |
| Carbonblackcontent | 2.5% |
| Hardnessshored | 60 |
| Waterabsorption | <0.01% |
As an accredited LyondellBasell HDPE M6580WC factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg polyethylene bags, 55 bags per pallet, shrink-wrapped; total 1,375 kg per pallet. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL) – LyondellBasell HDPE M6580WC supplied in 25 kg bags, palletized, stretch-wrapped, and securely loaded for sea freight. |
| Shipping | LyondellBasell HDPE M6580WC is shipped as non-hazardous resin pellets in 25 kg polyethylene bags, 1,000 kg bulk bags, or bulk trucks/railcars. Store in a cool, dry area away from ignition sources, moisture, and direct sunlight. Follow local transport and handling regulations. |
| Storage | Store LyondellBasell HDPE M6580WC in original closed bags on pallets within a cool, dry, well-ventilated warehouse. Protect from direct sunlight, moisture, heat, ignition sources, and contamination. Keep away from strong oxidizers, acids, bases, and solvents. Avoid excessive stacking, minimize dust, and follow first-in, first-out stock rotation. Inspect packaging regularly for damage or leaks. |
| Shelf Life | Store in a cool, dry, well-ventilated area away from sunlight; typical shelf life is 12 months in unopened original packaging. |
In high-cavitation thin-wall dairy packaging lines operating at 1,200–1,600 containers per hour per stack mould, LyondellBasell HDPE M6580WC is processed at melt temperatures of 210–240 °C and injection velocities of 200–400 mm/s through valve-gated hot runner systems with 8–16 drops per face. The grade's narrow molecular weight distribution controls shear-thinning behaviour at apparent shear rates above 1,000 s⁻¹, reducing flow-front freeze-off in wall sections of 0.35–0.80 mm. Compliance for food-contact use is anchored to FDA 21 CFR 177.1520(c) for olefin polymers in contact with aqueous, acidic, and low-alcohol foods, to EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm², and to GB 4806.7-2016 with a total migration limit of 10 mg/dm² and a potassium permanganate consumption limit of 10 mg/kg. Formulation addition ratios are set at 100 wt% virgin resin for direct food contact, with 2–3 wt% titanium dioxide white masterbatch added for opacity and up to 10 wt% clean in-house regrind permitted only where the converter has validated that the regrind stream remains from the same food-grade lot and free from cross-contamination under EU 10/2011 Article 4 recycling provisions. Downstream production uses accumulator-assisted injection units that generate filling times below 0.4 s per cavity, with a hold pressure of 40–80 MPa applied through the hot runner gate to prevent sink marks on rim sealing surfaces; mould temperature is held at 10–30 °C and total cycle time at 3.5–6.0 s, with mould-open time kept below 0.8 s to minimize ambient moisture pick-up on the cold runnerless gate area. Published data for this specific stack mould configuration is limited; converters should confirm lot-specific melt flow rate under ISO 1133-1:2022 and density under ISO 1183-1:2022 before releasing the mould window to production. Terminal products include 125–500 mL yogurt cups, dairy dessert tubs, sour cream containers, delicatessen cups, and thin-wall lids with tamper-evident rim geometries.
Compression of the processing window occurs most severely when the tamper-evident band's breakaway bridges are thinned below 0.25 mm and the edge-gate vestige length is reduced under 0.5 mm; at these dimensions, melt face velocity must be sustained above 120 mm/s to avoid premature solidification across a 96-cavity hot runner system. The grade is processed at melt temperatures of 200–230 °C, mould temperatures of 10–25 °C, and cycle times of 4.0–6.5 s for closures on 28 mm PCO 1881 and 30/25 mm neck finishes. The closing torque requirement of 1.8–2.5 N·m for carbonated soft drink applications requires a minimum bridge thickness that preserves breakaway force without causing handle leakage. Regulatory compliance is anchored to FDA 21 CFR 177.1520(c) for room-temperature beverage contact, EU Regulation (EU) No 10/2011 for overall migration below 10 mg/dm², and USP <661.1>/USP <661.2> for plastic packaging materials in pharmaceutical closures. Sensory performance is assessed under EN 1622 for odour and flavour of water, with a threshold odour number not greater than 2. Formulation addition comprises 1.5–2.5 wt% of a slip-agent masterbatch containing erucamide or oleamide at 5–10% active concentration in a polyethylene carrier, reducing the closure coefficient of friction below 0.20 on high-speed capping lines running at 1,000–2,200 caps/min; colour masterbatch is added at 1–2 wt%, and regrind is limited to 5 wt% where child-resistant torque retention is a release criterion. Downstream production uses electric and servo-hydraulic injection machines with clamp forces of 350–600 t, hot runner tips with individual thermocouple control, and a melt residence time below 5 min to limit slip additive degradation. Post-mould inspection includes dimensional control of closure major diameter within ± 0.10 mm and removal torque verification on a calibrated torque stand with 0.01 N·m resolution. Terminal products include single-piece HDPE caps for still water and carbonated soft drinks, tamper-evident sports closures, and pharmaceutical syrup closures with child-resistant mechanisms.
| Jurisdiction | Standard | Test/Designation | Requirement |
|---|---|---|---|
| United States | FDA 21 CFR 177.1520(c) | Olefin polymer food contact | Extraction limits per condition of use |
| European Union | EU 10/2011 | OM2 total migration | 10 mg/dm² |
| United States Pharmacopeia | USP <661.1>/USP <661.2> | Plastic materials of construction | Physicochemical test panel |
| Sensory | EN 1622 | Odour and flavour of water | TON < 2 |
On 800–1,200 t hydraulic clamp machines producing UN-certified 1H2 removable-head plastics pails, injected wall sections of 1.8–3.5 mm are held dimensionally stable through a cycle time of 18–35 s, with melt temperature at 215–240 °C and mould temperature at 10–25 °C. Compliance for dangerous goods packaging is defined by UN Model Regulations Chapter 6.1 design types 1H1 and 1H2; performance tests include drop tests from 1.8 m, 1.2 m, and 0.8 m for packing groups I, II, and III respectively, a stacking test at 40 °C for 28 days, and a hydraulic pressure test of 250 kPa gauge for 30 min. Transport-specific references include ADR 6.1.5, RID 6.1.5, IMDG Code Part 6, and 49 CFR §178.504. Formulation addition permits 10–30 wt% certified in-house regrind from the same UN-approved line, conditioned by checking melt flow rate under ISO 1133-1:2022 so that the shift does not exceed ± 1.0 g/10 min from nominal; 2–3 wt% colour masterbatch and 0.5–1.0 wt% hindered amine light stabilizer are added for exterior exposure, while slip additives are excluded to preserve lid friction. Production uses accumulator-assisted injection with sequential valve gating from the base centre outward to relocate weld lines away from the handle eye and lid-gasket contact zone; packing pressure is held at 35–60 MPa for 6–10 s to compensate for volumetric shrinkage of 1.5–2.0% at the sidewall-to-base junction. Terminal products include 5 L, 10 L, 20 L, and 25 L open-top pails for paints, coatings, construction chemicals, food ingredient concentrates, and pharmaceutical intermediates, with UN markings embossed in the base.
| Test | Packing Group I | Packing Group II | Packing Group III | Reference |
|---|---|---|---|---|
| Drop height | 1.8 m | 1.2 m | 0.8 m | UN 6.1.5.3 |
| Stacking load | 40 °C, 28 days | 40 °C, 28 days | 40 °C, 28 days | UN 6.1.5.6 |
| Internal pressure | 250 kPa, 30 min | 250 kPa, 30 min | 250 kPa, 30 min | UN 6.1.5.5 |
For large flat sidewalls and bases in modular storage bins where the gate vestige creates a stress-concentrating feature, the filling pattern is altered to position the gate in a low-stress, non-appearance zone and to maintain wall thickness above 1.5 mm so that a brittle failure at the gate remnant does not propagate across the base. The grade is processed at a melt temperature of 205–225 °C, a mould temperature of 15–30 °C, and a clamp force of 500–1,200 t depending on the projected area; hold pressure of 30–50 MPa is applied for 5–8 s to suppress sink marks at rib-to-wall junctions. Compliance for general housewares rests on REACH Annex XVII restricted substances verification; where the article can be accessed by children, EN 71-3:2019 migration limits for 19 elements apply, with lead not exceeding 2.0 mg/kg, cadmium 1.3 mg/kg, and chromium VI 0.02 mg/kg in the dried toy-material extract. For food storage containers, EU Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520(c) apply. Formulation addition includes 2–4 wt% custom colour masterbatch; outdoor storage compounds incorporate 0.3–0.8 wt% of a polymeric hindered amine light stabilizer and 0.1–0.3 wt% of a phosphite antioxidant. Regrind of 5–15 wt% may be used only in non-food and non-toy articles. Production on electric toggle machines with 25–40 s cycle time uses multi-stage injection profiles—slow-to-fast filling to avoid gas traps at rib intersections—and beryllium-copper inserts in handle regions for accelerated cooling. Terminal products include modular storage bins, under-bed storage boxes, garage shelving components, dustbin bodies up to 20 L, and houseware baskets.
The ISO 23907-1:2019 puncture test for sharps containers requires that a free-falling steel penetration probe does not create leakage or compromise the one-way lid mechanism, placing constraints on wall thickness uniformity and weld line placement. This grade is moulded at a melt temperature of 210–230 °C, a mould temperature of 10–20 °C, wall sections of 1.5–2.5 mm, and cycle times of 20–35 s. Cavity filling uses a two-stage injection profile with a slow initial velocity to avoid jetting around the lid-locking lugs. Regulatory alignment is maintained under ISO 23907-1:2019, WHO guidelines on safe injection waste management, and UN 3291 provisions for clinical waste packs where the filled container is transported. Resin suitability for healthcare contact is referenced to FDA 21 CFR 177.1520(c) and, where cytotoxicity documentation is required, ISO 10993-5. Formulation addition is 100 wt% virgin resin; 2–3 wt% red or yellow masterbatch is added according to WHO colour coding, and 0.5–1.0 wt% HALS is used for outdoor collection stations. Regrind is excluded to prevent local weak zones caused by degraded or cross-contaminated particles. Production requires validated cavity pressure monitoring, with the packing phase held at 40–60 MPa for 4–6 s to eliminate internal voids that could become leak paths. Post-mould assembly joins the hinged lid and locking mechanism, and each production lot is sampled for leakproofness and puncture resistance according to ISO 23907-1:2019. Terminal products include 1 L, 5 L, and 10 L sharps disposal containers, rotating lid designs, and chemotherapy sharps containers with colour-coded lids.
For injection-moulded cosmetic jars in the 15–200 mL range, high-gloss outer surfaces are achieved by moulding at a melt temperature of 215–235 °C and a mould temperature of 20–40 °C, at which a gloss-enriched skin layer forms; cycle time remains 30–50 s. Wall sections of 2.0–4.0 mm demand a multi-stage packing ramp from 60 MPa down to 20 MPa over 3–5 s to compensate for shrinkage around the threaded neck without overpacking the base and causing stress cracking at the gate. Compliance for cosmetic packaging is referenced to EU Regulation (EC) No 1223/2009 for the packaging safety information required in the cosmetic product safety report, to FDA 21 CFR 177.1520(c) for indirect food and drug contact where applicable, and to REACH Annex XVII for restricted substances. In China, the packaging must satisfy the safety and technical standards for cosmetic contact materials under the Cosmetics Supervision and Administration Regulation, which requires supplier declaration of restricted heavy metals and phthalates. Formulation addition is 100 wt% virgin resin; 2–3 wt% opaque white masterbatch is used for jars intended to protect light-sensitive actives, and 0.1–0.5 wt% UV absorber is incorporated only when the closure is transparent or lightly pigmented. Regrind is excluded from exterior cosmetic surfaces where flow marks and gloss reduction from gel particles would be visible. Production on 150–350 t electric injection machines uses direct sprue or hot-tip gating positioned at the jar base centre to minimize gate blush on the visible sidewall, with cooling channels placed no more than 10 mm from the cavity surface to maintain thermal uniformity. Terminal products include cream jars, hair wax containers, lip scrub pots, body butter jars, and personal care formulation containers.
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LyondellBasell HDPE M6580WC is a high-density polyethylene resin supplied in pellet form for extrusion and blow molding operations. The public datasheet identifies a nominal density of 0.958 g/cm³ (ASTM D1505) and a melt flow rate of 0.80 g/10 min at 190 °C/2.16 kg load (ASTM D1238, ISO 1133-1). The grade is positioned for large-part blow molding, sheet extrusion, and profile extrusion where the balance of stiffness, melt strength, and environmental stress-crack resistance controls part performance. It is not classified as a thin-wall injection molding grade, and published data for multicavity injection molding of this specific configuration is limited.
The molecular weight distribution is broader than that of a conventional monomodal HDPE of the same density; this feature is inferred from processing behavior and ESCR response, but the complete distribution is not disclosed in public literature. The polymer is often converted on equipment with grooved-barrel extruders because the higher melt viscosity at low shear rates requires stable feed pressure.
Melt temperature control is the principal variable in extrusion blow molding. Barrel profiles are set to produce a melt temperature of 190–230 °C; the lower boundary is constrained by insufficient homogenization and the upper boundary by oxidative chain scission. Accumulator-head machines with grooved-barrel extruders of 30:1 to 36:1 L/D are used for large-part production. Screw speed is adjusted to limit melt temperature overshoot; when melt temperature exceeds 240 °C, environmental stress-crack resistance can decline without visible discoloration. Melt pressure fluctuations at the die should be below ±1.0% to avoid thickness variation in the parison.
The melt flow rate of 0.80 g/10 min is a single-point viscosity measurement and does not capture the low-shear-rate viscosity relevant to parison sag. Capillary rheometry at 190–230 °C with shear rates from 10 s⁻¹ to 1000 s⁻¹ is recommended to establish die pressure and melt fracture limits. The Carreau viscosity parameters for this grade are not published. A representative sheet extrusion barrel profile is feed 170 °C, compression 190 °C, metering 200 °C, and die 200 °C, with final setpoints adjusted to measured melt temperature.
Polyethylene is not hygroscopic, and predrying is not routinely required. Surface condensation from outdoor storage can be removed by a heated hopper air supply at 70–80 °C for 1–2 h. Residual moisture on pellet surfaces creates steam during plastication and can introduce pinholes in thin sections. The use of a melt pump is recommended for sheet and profile lines to reduce pressure variation and temperature gradients.
Regrind addition influences slow crack growth resistance. Clean in-house regrind is typically limited by the processor’s ESCR validation, not by melt flow stability alone. The effect of regrind on ESCR must be measured under ASTM D1693 on the finished part; adding regrind without validation can mask a loss of slow crack growth performance.
Large-part blow molding on accumulator-head equipment uses programmed parison wall thickness to counteract sag. The grade’s melt strength is sufficient for containers in the 10–20 L range; however, published hang-time data for this specific configuration is limited. Mold temperature is maintained at 15–40 °C to control shrinkage and warpage. Mold shrinkage in HDPE of this density typically falls between 1.5% and 4.0%, depending on part thickness, cooling rate, and mold configuration. Blow pins are configured to provide preblow and final blow pressures of 0.6–0.8 MPa and 0.8–1.0 MPa, respectively, depending on part geometry. Compared with a 0.952 g/cm³ HDPE blow molding grade, M6580WC provides higher top-load strength due to the density differential, but the processing window at low melt temperatures is narrower. Production defects observed on accumulator-head lines include parison sag, shark-skin melt fracture, and pinch-off thinning; reducing melt temperature and increasing die gap often mitigate these faults.
Sheet produced from M6580WC is processed with roll stack temperatures between 80 °C and 100 °C. Higher roll temperatures reduce residual stress but can increase gloss variation. Plug-assisted thermoforming requires sheet surface temperatures of 160–180 °C; mold temperatures are held between 40 °C and 60 °C to improve dimensional stability. Draw ratios above 3:1 are possible only with uniform sheet temperature; localized thinning is controlled by plug material, plug temperature, and preheat profiling. Cooling jigs should maintain contact pressure until the sheet drops below 80 °C to prevent warpage.
| Property | Test Method | Value |
|---|---|---|
| Density | ASTM D1505 | 0.958 g/cm³ |
| Melt flow rate (190 °C/2.16 kg) | ASTM D1238 | 0.80 g/10 min |
| Tensile strength at yield | ASTM D638 | 28.0 MPa |
| Elongation at break | ASTM D638 | >600% |
| Flexural modulus, 1% secant | ASTM D790 | 1,280 MPa |
| Environmental stress-crack resistance, 100% Igepal CO-630 | ASTM D1693, Condition B | >1,000 h |
| Vicat softening temperature | ASTM D1525 | 126 °C |
| Brittleness temperature | ASTM D746 | <-76 °C |
These values are representative of laboratory-molded or extruded specimens and do not constitute batch-release specifications. Lot-to-lot variation, test specimen preparation, and conditioning affect results.
The substitution of M6580WC for a monomodal 0.958 g/cm³ HDPE often requires higher melt temperature set points. The resin’s molecular weight distribution is broader than that of a monomodal grade, which increases melt strength and ESCR but also raises die pressure at low shear rates. Processors should perform capillary rheometry rather than rely on melt index alone; the melt flow ratio between 21.6 kg and 2.16 kg loads, if available, gives an indication of molecular weight distribution but does not replace a shear-viscosity curve.
Compared with lower melt index blow molding grades such as 0.21–0.40 g/10 min HDPE, M6580WC has a higher melt flow rate and therefore shorter parison hang time but may allow lower melt temperature and faster cycle time in smaller parts. Compared with higher-flow injection molding HDPE grades, M6580WC is formulated for slower crystallization and higher melt strength, making it unsuitable for fast-cycle thin-wall molding where demolding stiffness controls cycle time.
| Attribute | M6580WC | Conventional monomodal blow molding HDPE | Thin-wall injection molding HDPE |
|---|---|---|---|
| Density | 0.958 g/cm³ | 0.958 g/cm³ | 0.960 g/cm³ |
| Melt flow rate (190 °C/2.16 kg) | 0.80 g/10 min | 0.30–0.70 g/10 min | 4–20 g/10 min |
| Parison hang time | Moderate | Longer | Not applicable |
| Primary conversion route | Blow molding, sheet, profile | Blow molding | Injection molding |
| ESCR | >1,000 h (ASTM D1693 B) | Often 100–500 h | Not typically specified |
Published data for side-by-side container or pipe testing of this specific configuration is limited.
Compliance verification for food-contact uses must be performed on the specific lot and finished article. High-density polyethylene of this class may be formulated to meet FDA 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011, but migration testing under EN 1186 or equivalent is required for final compliance. REACH obligations under Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU apply to the finished article, not only the resin. Prolonged contact with oxidizing acids, aromatic hydrocarbons, and chlorinated solvents at temperatures above 60 °C reduces ESCR and tensile strength. Continuous service under sustained internal pressure is not recommended above 80 °C without derating and specific long-term hydrostatic testing.
Outdoor service requires UV stabilization. Natural HDPE is susceptible to photo-oxidation; carbon black at 2–3% is used in pipe-grade formulations. Dispersion quality is assessed by ASTM D5596; poor carbon black dispersion creates large agglomerates that reduce ESCR and impact resistance. Published formulation details for M6580WC are not disclosed.
Environmental stress-crack resistance is measured with a bent strip immersed in 100% Igepal CO-630 at 50 °C under ASTM D1693. The test provides a comparative ranking but does not directly predict slow crack growth in notched pipe or structural parts. For pressure-pipe applications, notched pipe testing under ISO 13479 or full-notch creep testing under ASTM F1473 is required. Published data for M6580WC under ASTM F1473 is limited; therefore, the grade should not be inferred to possess PE100 or PE4710 slow crack growth resistance without additional validation.
Slow crack growth in high-density polyethylene is governed by tie-molecule density, lamellar orientation, and residual stress. Rapid quenching increases crystallite nucleation density and can reduce ESCR compared with slower cooling because tie-molecule formation is suppressed. Processing temperature, mold cooling rate, and post-mold annealing all influence the failure mode. Additives that alter nucleation or interfacial energy can shift slow crack growth performance; any additive change must be validated by ESCR testing under ASTM D1693 or fracture mechanics testing rather than inferred from melt flow stability.
In extrusion and blow molding, the upper melt temperature limit is set by chain scission rather than visible yellowing. A melt temperature excursion above 240 °C can reduce slow crack growth resistance even if the part appears acceptable. The same principle applies to regrind history: multiple heat histories can shorten the time to brittle failure under constant load.
For profile and sheet extrusion, melt temperatures of 200–220 °C are used with a barrel profile that avoids a temperature peak in the compression zone. High-shear mixers are not required; distributive mixing is sufficient for color concentrate letdown. Color concentrate is added at 2–4% by gravimetric feeder, and poor dispersion produces surface streaking. Extrusion welding of fabricated parts requires a melt temperature of 200–230 °C at the weld zone; the melt must be protected from oxidation to maintain ESCR at the weld line.