| HS Code | 387523 |
| Productname | LyondellBasell HDPE M6080 |
| Polymertype | High Density Polyethylene (HDPE) |
| Density | 0.960 g/cm³ |
| Meltflowrate 190c 5kg | 0.8 g/10 min |
| Tensilemodulus | 1400 MPa |
| Tensilestressatyield | 30 MPa |
| Tensilestressatbreak | 35 MPa |
| Elongationatbreak | >600% |
| Flexuralmodulus | 1400 MPa |
| Charpynotchedimpactstrength 23c | 15 kJ/m² |
| Charpynotchedimpactstrength Minus30c | 5 kJ/m² |
| Vicatsofteningtemperature | 128 °C |
| Heatdeflectiontemperature 0 45mpa | 75 °C |
| Shoredhardness | 65 |
| Meltingtemperature | 135 °C |
| Waterabsorption | <0.01% |
| Environmentalstresscrackresistance | >1000 h |
As an accredited LyondellBasell HDPE M6080 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE M6080 is typically packaged in 25 kg polyethylene bags, 1,000 kg octabins, or bulk trucks/railcars for safe handling. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with LyondellBasell HDPE M6080 in 25 kg bags, palletized, stretch-wrapped, and secured for safe ocean transport. |
| Shipping | LyondellBasell HDPE M6080 is a non-hazardous solid polyethylene resin, typically shipped in 25 kg bags, octabins, or bulk trucks/railcars. Not classified as dangerous goods. Store in a dry, cool, well-ventilated area away from direct sunlight, heat, and ignition sources. Avoid moisture, dust, and prolonged UV exposure. |
| Storage | Store LyondellBasell HDPE M6080 in a cool, dry, well-ventilated area. Keep containers closed and palletized in original packaging, off the ground, away from direct sunlight, moisture, heat, and ignition sources. Protect from contamination and strong oxidizers. Avoid prolonged UV exposure and extreme temperatures. Clean spilled pellets promptly because they can be slippery. Follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Typically 24 months when stored unopened in original packaging in a cool, dry area, away from direct sunlight and moisture. |
Open-head pails in the 10 L to 25 L range are molded from LyondellBasell HDPE M6080 at melt temperatures of 210 °C to 235 °C and mold coolant temperatures of 12 °C to 24 °C. The grade’s nominal melt index of 8.0 g/10 min under ASTM D1238-20 at 190 °C and 2.16 kg permits thin rim sections to fill without short shots on 2,500 kN to 4,000 kN toggle clamps. Fill times of 1.6 s to 2.8 s at peak cavity pressures of 70 MPa to 95 MPa are typical for a 20 L pail weighing 980 g with a 2.0 mm sidewall. A direct sprue gate into the bottom center or a film gate into the rim is used; gate land thickness is held at or above 1.5 mm so that freeze-off does not occur before hold pressure compensates crystallization-induced shrinkage. The pail is subjected to stack testing at 40 °C with a 250 kg static top load for 28 days under ISTA 2A procedures, with rim-diameter dimensional change maintained below 2.0 %. Compliance for food-contact pails is governed by FDA 21 CFR §177.1520 for olefin polymers, and the EU declaration is conditional on overall migration below 10 mg/dm² under EU Regulation (EU) No 10/2011. For industrial pails carrying mild detergent concentrates, unmodified homopolymer ESCR must be verified against each formulation under ASTM D1693 Condition B, because HDPE M6080 is not an ESCR-modified hexene or butene copolymer. Pail lids with load-bearing living hinges are excluded from this grade; flexural fatigue after 5,000 cycles can initiate stress whitening and crack propagation at the hinge root.
Returnable bottle crates with 24 × 0.33 L cells depend on balancing short-cycle rigidity against low-temperature impact. M6080 is processed on a 6,500 kN clamp injection machine with a 22:1 L/D general-purpose screw and a compression ratio of 3.2:1; back pressure is maintained at 0.6 MPa. Melt temperature is held at 220 °C to 245 °C. If residence time exceeds 8 min, chain branching and gel formation can appear as black specks at gate regions and should trigger reduced screw rotation or shot-size adjustment. Mold temperature is controlled asymmetrically: 18 °C on the core to reduce cooling time and 28 °C on the cavity to preserve surface gloss and reduce notch sensitivity at the cell corner radii. Fill time is set at 2.5 s to 3.2 s, with hold pressure of 50 MPa to 65 MPa applied for 6 s. Premature hold release causes gate sink and center-core voiding in the divider walls; gate plugs are sectioned after startup to confirm voids do not exceed 0.5 mm. Drop impact performance of filled crates at 2 °C is evaluated under ASTM D2463-15, with gate areas and divider weld lines recorded as primary failure locations. Flame-retardant additive packages based on brominated epoxy and antimony trioxide above 5 wt% are not used with this grade in bottle crates, because acidic species generated at high melt temperature can accelerate autocatalytic oxidation. Phosphite stabilizer is typically added at 0.10 % to 0.20 % during compounding to protect the melt during extended cycles.
| Parameter | Reference method | Nominal value or boundary |
|---|---|---|
| Melt flow index | ASTM D1238-20, 190 °C / 2.16 kg | 8.0 g/10 min |
| Density | ASTM D1505-18 | 0.960 g/cm³ |
| Tensile yield strength | ASTM D638-14, Type IV specimen, 50 mm/min | 28 MPa |
| Flexural modulus | ASTM D790-17, 1% secant | 1,100 MPa |
| Shore D hardness | ASTM D2240-15 | 68 |
| Vicat softening temperature | ASTM D1525-17, Method A50 | 127 °C |
| Mold shrinkage | Internal tool cutting practice, flow/transverse | 1.5 % to 2.2 % |
| Food-contact status | FDA 21 CFR §177.1520; EU Regulation (EU) No 10/2011 | Conditional on end-use additive package and specific migration testing |
Thin-walled dairy spread tubs with 0.55 mm nominal sidewall and 250 mL capacity are filled in 0.38 s to 0.50 s on a 32-cavity cold-runner stack mold. Nozzle melt temperature is held at 225 °C to 235 °C. Injection velocity is profiled so that the flow front reaches 300 mm/s in the first 10 mm of fill, then decelerates to 120 mm/s through the top rim to prevent jetting marks. Peak cavity pressure is 90 MPa to 110 MPa. M6080 provides a nominal density of 0.960 g/cm³ under ASTM D1505-18 and flexural modulus of 1,100 MPa under ASTM D790-17, which supplies stacking stiffness at thin wall without additional sidewall ribs. Tool cooling is run at 8 °C to 12 °C with a 30 % ethylene glycol-water mixture. Sink over the bottom stacking ring is held below 0.4 % scrap when packing pressure is raised to 75 MPa for 0.2 s after velocity-pressure switchover. Food-contact compliance is restricted to conditions of use A through H in FDA 21 CFR §177.1520, and the EU declaration is governed by Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm². Fatty filling temperatures above 60 °C are excluded because the homopolymer can develop surface stress cracking in the presence of free fatty acids and high-temperature oils. Recycled content in the molded article must not exceed 25 % unless the recovered polymer is produced under a closed-loop feedstock program with contaminant testing under Regulation (EU) 2022/1616.
Overcap molding on a 48-cavity hot-runner system with valve gates uses HDPE M6080 at melt temperature 210 °C to 225 °C. The skirt wall thickness is 0.9 mm, the top panel is 0.7 mm, and the shot weight is 3.2 g. To maintain inner-bead concentricity of ±0.10 mm, the valve gate must open before the pressure ramp reaches 55 MPa; delayed gate opening creates an eccentric flow front that freezes into dimensional bias. Clamping force is set at 1,200 kN, and injection velocity is profiled in three steps of 85 mm/s, 140 mm/s, and 40 mm/s over a total fill time of 0.13 s. Mold temperature is 10 °C to 15 °C to suppress post-mold ovality. The component is used as an overcap on metal-ended composite canisters for dried infant formula and must comply with FDA 21 CFR §177.1520 olefin polymer requirements. Sensory panel testing under EU Regulation (EU) No 10/2011 Annex V is typically performed to confirm low off-odor transfer into the dry product. The cap is evaluated for removal torque after 2 weeks of storage at 50 °C, with acceptance between 1.2 N·m and 2.2 N·m measured on a torque tester; published data for this specific overcap configuration is limited, and end-use torque retention must be validated for each rib and knurl design. Continuous contact with alcohol above 8 % is outside the operational boundary because stress cracks can initiate at the knurl root.
Logistics totes of 45 L capacity with sidewall ribs are molded at 4.2 mm nominal wall from M6080 using a 6,000 kN hydraulic clamp and a 120 mm diameter screw. The density of 0.960 g/cm³ yields a molded part mass of 2,650 g. Fill time is 4.5 s at 60 MPa hydraulic pressure, with screw cushion control set at 4 mm to 8 mm to maintain shot consistency. Cooling time is 32 s with mold temperature at 22 °C. Side ribs of 0.8 mm base thickness are spaced at 22 mm centers to prevent visible sink; rib-to-wall ratio is kept below 0.6, because higher ratios create warpage as the high-density melt crystallizes rapidly. Corner posts are evaluated for compressive loading under ASTM D642-20. Exposure to quaternary ammonium disinfectants at 50 °C for 7 days requires prototype validation under ASTM D1693 Condition B, since molded-in stress at the floor-junction corner can initiate environmental stress cracking in unmodified homopolymer. Color masterbatch at 2 wt% on a high-density polyethylene carrier is typical for dark grey and black totes; pre-blending in a mechanical tumbler for 20 min before hopper loading reduces shade variation.
Housewares articles such as waste bins with snap-on rims and storage boxes with textured surfaces are produced from M6080 at melt temperatures of 205 °C to 220 °C and injection speeds of 120 mm/s to 180 mm/s. The density of 0.960 g/cm³ produces a hard surface with Shore D hardness of 68 under ASTM D2240-15, but shear rates above 1,500 s⁻¹ at thin entry points can induce sharkskin melt fracture. Gate cross-section is therefore oversized by 20 % relative to the adjacent wall, and the nozzle tip is held at a flat 225 °C to stabilize the melt front. Anti-static additive masterbatch is incorporated at 1.5 wt% to 2.0 wt% for items used in electronic assembly areas; surface resistivity is tested under IEC 61340-2-3, with acceptance at or below 1 × 10¹² Ω. Regrind content is limited to 20 %, because higher fractions reduce melt strength and produce a measurable shift in Vicat softening temperature from 127 °C under ASTM D1525-17 to below 124 °C by chain scission. Mold temperature is set at 20 °C to 30 °C, and cooling lines are placed within 12 mm of the cavity surface. Tool cutting uses mold shrinkage of 1.8 % to 2.2 % in the flow direction and 1.5 % to 1.9 % transverse to flow; differential shrinkage above 0.3 % causes bowing in flat storage boxes. This grade is not intended for high-gloss appearance panels because rapid crystallization at the mold wall produces a matte surface and visible weld lines. Chemical blowing agent at 0.5 wt% is used only in thick handles to improve edge rigidity and is excluded from thin-wall visible panels.
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LyondellBasell HDPE M6080 is a pelletized high-density polyethylene resin specified for extrusion-grade blown film. Supplier technical documentation positions the product as a high-molecular-weight grade for thin-gauge packaging, including refuse sacks, retail bag film, and industrial liners. The product is defined by a nominal melt mass-flow rate of 0.8 g/10 min at 190 °C under a 2.16 kg load and a nominal density of 0.959 g/cm³ at 23 °C, measured respectively under ISO 1133-1:2022 and ISO 1183-1:2019. The grade is supplied as pellets and is handled in conventional polyolefin silo and hopper systems. Because the resin is semi-crystalline, its melt rheology, solidification rate, and density dominate downstream film properties. The values cited here are typical supplier literature values, not batch release limits; final material acceptance must be based on the lot-specific certificate of analysis and safety data sheet.
Table 1 consolidates the property ranges commonly associated with this product in commercial datasheets. Specimens are conditioned according to ISO 291:2008 class 2 at 23 °C ± 2 °C and 50 % ± 10 % relative humidity unless otherwise stated. The ranges are not release limits unless the certificate of analysis identifies them as such.
| Property | Typical range | Method |
|---|---|---|
| Melt mass-flow rate (190 °C, 2.16 kg) | 0.75–0.90 g/10 min | ISO 1133-1:2022 |
| Density (23 °C) | 0.958–0.962 g/cm³ | ISO 1183-1:2019 |
| Tensile stress at yield | 26–30 MPa | ISO 527-2:2012, 50 mm/min, type 1A |
| Elongation at break | 600–900 % | ISO 527-2:2012 |
| Flexural modulus | 1,000–1,250 MPa | ISO 178:2019, 2 mm/min |
| Vicat softening temperature | 124–130 °C | ISO 306:2013, method A50 |
The comparatively high density is a primary differentiating parameter against low-density polyethylene and linear-low-density polyethylene. It raises film modulus but reduces low-speed puncture and tear resistance unless the product is blended. The melt flow rate is intermediate within high-molecular-weight HDPE film grades, low enough to retain extrudate strength and high enough to control melt pressure in grooved-feed extruders. The density range can also be used to estimate crystalline volume fraction. Using the two-phase density model with crystalline polyethylene density of 1.000 g/cm³ and amorphous polyethylene density of 0.855 g/cm³, a density of 0.959 g/cm³ gives a crystalline fraction near 0.72. Exact crystallinity determined by differential scanning calorimetry depends on cooling rate, measurement method, and thermal history.
Bubble stability in this product is governed by molecular weight distribution, extensional strain hardening, and melt relaxation time. The polymer exits a spiral mandrel or side-fed annular die and is subjected to biaxial orientation. A high-molecular-weight fraction increases the melt relaxation time and supports the bubble between the die and frost line. On blown-film lines with die gaps from 1.2 mm to 2.0 mm, blow-up ratios from 3:1 to 5:1, and melt temperatures from 200 °C to 225 °C, gauge below 12 µm can be maintained. At melt temperatures above 230 °C, oxidative degradation may lower viscosity and induce bubble oscillation. At temperatures below 190 °C, sharkskin melt fracture may appear at the die lip because the critical shear stress is exceeded. These limits are not absolute, since die design, air-ring configuration, and output rate shift the practical operating window.
Rheological characterization should be performed by capillary rheometry under ISO 11443:2014 at 190 °C, 200 °C, and 220 °C over apparent shear rates from 100 s⁻¹ to 1,000 s⁻¹. Bagley and Rabinowitsch corrections are required for true viscosity data. The supplier’s condensed data sheet for M6080 does not typically publish a complete viscosity curve, so line-specific rheology testing is preferred for optimizing screw speed, melt temperature, and die pressure. Melt pressure before the screen changer on a 30:1 L/D single-screw extruder is commonly observed in the range of 250–350 bar, but actual pressure depends on die size, output, melt temperature, and screw condition.
When the resin is processed on a 65 mm grooved-feed single-screw extruder with an L/D ratio of 30:1, barrel temperature settings are usually ramped from 160 °C at the feed zone to 190 °C at the metering zone, with adapter and die zones at 195 °C to 210 °C. Melt temperature should be checked with an insertion pyrometer because barrel setpoints alone under-report actual melt temperature. Internal bubble cooling with air at 8 °C to 15 °C and external air-ring velocities of 20 m/s to 40 m/s are used to stabilize the frost line. Frost line height is normally held at 4 to 8 die diameters. Shorter frost line settings reduce orientation but can produce blocking and gauge variation. Longer settings increase machine-direction splitting tendency and can narrow the transverse-direction tear window.
M6080 differs from a typical C8-LLDPE of density 0.918 g/cm³ in that its density is approximately 0.04 g/cm³ higher. The film modulus therefore increases, while dart drop impact and Elmendorf tear resistance are generally lower. Converters address this by blending 10 wt% to 30 wt% LLDPE, using the HDPE phase to supply stiffness and thin-gauge economics and the LLDPE phase to improve dart drop impact and tear propagation resistance. Film property measurements follow ISO 7765-1 for dart drop and ISO 6383-2 for Elmendorf tear. Absolute values are line- and gauge-dependent and should be established on the actual film tower rather than quoted from pellet datasheets.
The melt flow rate of M6080 is approximately three times that of a nominal 0.25 g/10 min blow-molding HDPE. This makes M6080 more fluid during extrusion but unsuitable for large-part extrusion blow molding, where high parison melt strength and hang time are required. Compared with a PE100 pressure-pipe HDPE, M6080 is not formulated to meet the hydrostatic strength and slow crack growth requirements of ISO 4427 and ISO 12162; therefore it must not be used for pressure-pipe service. The molecular structure is reported to have a broad molecular weight distribution, which is not equivalent to the bimodal-copolymer architecture commonly employed for PE100 pipe resins. Published data for this specific configuration is limited, but practical processing differences are observable in bubble stability and film stiffness.
In high-speed refuse-sack conversion, seal jaws typically operate at 120 °C to 140 °C with dwell times between 0.3 s and 0.7 s. The film must produce consistent seal strength at fast cycle times while resisting blocking on wound rolls. Monitoring of film gauge at 10 to 20 circumferential points across the bubble, with a tolerance band of ±5 % on nominal gauge, is necessary to prevent bag gusset failures and seal-jaw sticking. The performance of M6080 in this application is influenced more by die alignment, air-ring uniformity, and take-off tension control than by pellet properties alone. High-shear dispersion is not required for polyethylene blends; simple tumble blending of M6080 and LLDPE pellets is sufficient if the extruder screw has a mixing section. Concentrate masterbatches are added at 1 wt% to 3 wt%, with the carrier resin selected to minimize viscosity mismatch.
Food-contact and regulatory status depends on the final formulation and conversion conditions. M6080 can be assessed for compliance with U.S. FDA 21 CFR 177.1520(c), item 2.1 or 3.1, for olefin polymers in contact with food, and with European Plastics Regulation EU 10/2011 for overall migration and specific migration limits. Compliance with RoHS Directive 2011/65/EU is contingent on the absence of intentional addition of restricted substances. Under REACH Regulation (EC) No 1907/2006, the substance is registered, and substances of very high concern should be verified as below the 0.1 wt% threshold.
Polyethylene has low water absorption, typically below 0.01 % by weight after 24 h immersion under ISO 62:2008. Pre-drying is therefore generally unnecessary under dry warehouse conditions. Condensation can occur when cold pellets are introduced into a warm, humid production hall. If surface moisture is visible, drying at 65 °C for 2 h is recommended. Storage should avoid prolonged direct sunlight and ambient temperatures above 50 °C, because ultraviolet radiation can initiate chain scission and yellowing. The product should not be combined with strong oxidizing agents or stored in contact with solvents that swell polyethylene.