| HS Code | 788557 |
| Polymertype | High Density Polyethylene (HDPE) |
| Density | 0.953 g/cm³ |
| Meltflowrate | 0.30 g/10 min (190°C/2.16 kg) |
| Tensilestressatyield | 27 MPa |
| Tensilestrainatyield | 9 % |
| Tensilestressatbreak | 30 MPa |
| Tensilestrainatbreak | >600 % |
| Tensilemodulus | 1200 MPa |
| Flexuralmodulus | 1200 MPa |
| Charpynotchedimpactstrength23c | 20 kJ/m² |
| Charpynotchedimpactstrengthminus30c | 8 kJ/m² |
| Shoredhardness | 64 |
| Vicatsofteningtemperature | 126 °C |
| Brittlenesstemperature | < -70 °C |
| Environmentalstresscrackresistance | >1000 h |
| Meltingtemperature | 130 °C |
| Thermalconductivity | 0.4 W/(m·K) |
| Volumeresistivity | >1E15 Ω·cm |
| Dielectricconstant | 2.3 |
| Dissipationfactor | 0.0002 |
As an accredited LyondellBasell HDPE 5331H factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE 5331H is supplied as pellets in 25 kg polyethylene bags, available palletized or in 1,000 kg bulk bags. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with LyondellBasell HDPE 5331H in 25 kg bags, palletized, shrink-wrapped, and securely stowed for transport. |
| Shipping | LyondellBasell HDPE 5331H is a non-hazardous high-density polyethylene resin, shipped as pellets in 25 kg bags, bulk bags, or bulk trucks/railcars. It is not DOT/IMDG/IATA regulated, with no UN number or hazard class. Store dry, away from heat and moisture. |
| Storage | Store LyondellBasell HDPE 5331H in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original containers or bags closed, clean, and palletized off the floor. Avoid moisture, dust, and contamination. Protect from prolonged UV exposure and excessive temperatures. Store separately from incompatible materials and follow the manufacturer’s safety data sheet. |
| Shelf Life | No established shelf life; indefinite when stored properly in original packaging, cool, dry conditions, away from direct sunlight and contaminants. |
LyondellBasell HDPE 5331H is processed on accumulator-head continuous-shuttle extrusion blow molding lines for rigid intermediate bulk chemical packaging. The compliance set for UN 1H2 packagings includes UN Model Regulations Chapter 6.1 drop, hydraulic internal pressure, and stack testing as referenced in ADR/RID/IMDG periodic type approvals; resin-specific food-contact status under FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011 with migration testing per EN 1186-1 applies only where direct food contact is validated in the final monolayer structure. In virgin-regrind formulations, 100 parts of HDPE 5331H are combined with 15 to 20 parts of clean, dry, non-contaminated post-industrial trim regrind, 2.0 to 2.5 parts of carbon black masterbatch, and 1.5 to 2.0 parts of hindered amine light stabilizer masterbatch; reclaimed material above 25 parts by weight is avoided because melt fracture onset at die exit shifts upward and parison sag becomes difficult to control within the mold open time. Extrusion is conducted through a 24:1 L/D barrier screw with a grooved feed section, melt temperature 190 to 215 °C, die head temperature 180 to 200 °C, and parison programmer gap from 2.5 to 3.5 mm; blow pressure is 0.8 to 1.2 MPa, mold temperature 8 to 20 °C, and blow-up ratio 2.0 to 2.8:1. Terminal articles are 10 to 60 L rectangular and cylindrical jerrycans with UN 1H2 certification, used for liquid detergents, agrochemical concentrates, and corrosive cleaning chemicals with closure torque retention exceeding 2.0 N·m after conditioning at 40 °C for 48 h.
Blown film lines running HDPE 5331H for industrial liners and heavy-duty packaging require high-stalk bubble configuration because the resin’s melt strength counteracts extension thinning at frost line heights of 5 to 8 die diameters. Material conformity is evaluated under FDA 21 CFR 177.1520, EU Regulation (EU) No 10/2011, and when exported to North American food packaging, the specific end-use condition of use under 21 CFR 176.170(c) may be required; mechanical film characterisation follows ASTM D882 for tensile and elongation, ASTM D1709 for dart drop, and ASTM D1922 for Elmendorf tear. A typical outer-layer formulation comprises 100 parts HDPE 5331H, 20 to 30 parts C8-LLDPE with density 0.918 to 0.920 g/cm³ to reduce machine-direction tear, 2 to 5 parts high-slip masterbatch, and 1 to 3 parts antiblock masterbatch; blending below 20 phr LLDPE may produce unstable bubble edges, while above 30 phr the dart drop impact gain is offset by reduced film stiffness. Processing on a 30:1 L/D extruder at melt temperature 190 to 220 °C, die gap 1.2 to 2.0 mm, blow-up ratio 3.0 to 4.0:1, and internal bubble cooling air temperature 15 to 25 °C produces film thickness 12 to 120 µm. Terminal types include refuse sacks, construction vapour barriers, and hazardous-waste liners where tear propagation resistance is the limiting specification.
Corrugated polyolefin drainage pipe and conduit manufactured from HDPE 5331H is formed on vacuum-corrugation machines with a segmented mold tunnel, where the resin’s slow strain rate response must satisfy ring stiffness and creep ratio requirements in buried gravity-flow applications. Compliance frameworks include EN 13476-1:2018 for non-pressure underground drainage and sewerage, ASTM F2306 for corrugated HDPE pipe, ISO 9969 for ring stiffness, and ASTM D3350 for polyethylene pipe materials code classification; UV-stabilised compound formulations for outdoor storage require 2.0 to 2.5 wt% carbon black masterbatch to achieve dispersion above the minimum level in ISO 4427 or comparable outdoor exposure requirements. The compound is fed as 100 parts HDPE 5331H with 2.0 to 2.5 parts carbon black and 0.3 to 0.8 parts antioxidant masterbatch; regrind from trimmings is restricted to 10 to 15 wt% because higher fractions increase melt flow instability and inside-surface roughness. Extrusion uses a 30:1 L/D single-stage screw with melt temperature 200 to 230 °C, die temperature 180 to 210 °C, corrugator vacuum 0.06 to 0.09 MPa, and cooling water inlet 15 to 30 °C; output per line width is typically limited by vacuum mold release. Terminal products are 50 to 600 mm external diameter double-wall corrugated land drainage pipes and cable conduits for civil engineering. Data for HDPE 5331H in buried pressure pipe under PE100 MRS classification is limited; suitability must be explicitly validated against ISO 9080 long-term hydrostatic strength before pressure service.
Thermoformed dunnage and technical trays produced from HDPE 5331H begin on a flat-die sheet line where melt temperature, roll gap, and line speed determine forming window thickness uniformity. Material compliance for non-food industrial applications is evaluated under REACH substance restrictions and, when exported, RoHS Directive 2011/65/EU; for food-contact trays the substance migration provisions of EU Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520 apply. The material formulation includes 100 parts HDPE 5331H, 20 to 40 parts closed-loop regrind from trim skeleton, 2 to 4 parts color masterbatch, and 1 to 2 parts antistatic masterbatch; regrind above 40 parts produces sheet edge curl and non-uniform sag in the heater tunnel. Sheet extrusion is run with a 30:1 L/D extruder, flexible-lip die gap 2.0 to 6.0 mm, three-roll stack temperatures 70 to 95 °C, and line speed adjusted for sheet thickness 0.5 to 6.0 mm. Thermoforming uses plug-assisted molds, sheet surface temperature 145 to 160 °C, forming pressure 0.4 to 0.7 MPa, and mold temperature 5 to 15 °C. Terminal products are reusable pallet covers, automotive interior panel blanks, and material-handling dunnage trays with dimensional recovery below 2 % after 30 cycles at 60 °C.
Exposed geomembrane applications evaluate HDPE 5331H against stress crack resistance, carbon black dispersion, and oxidative induction time because failure in service is driven by slow crack growth under constant tensile load. The applicable material specification is usually GRI-GM13 for HDPE geomembranes, with oxidative induction time tested to ASTM D3895, single-point notched constant tensile load to ASTM D5397, tensile properties to ASTM D638, and density to ASTM D1505; regulatory liner certifications may additionally require ISO 9001 batch traceability. The geomembrane compound is produced with 100 parts HDPE 5331H, 2.0 to 3.0 parts carbon black masterbatch, and 0.5 to 1.0 parts antioxidant masterbatch; carbon black concentration below 2.0 wt% leads to low ultraviolet ageing resistance, while above 3.0 wt% compromises melt flow and surface finish. Flat-die extrusion at melt temperature 200 to 230 °C, die temperature 180 to 210 °C, and polished chill rolls at 70 to 100 °C produces sheet thickness 1.0, 1.5, 2.0, and 2.5 mm with beta-gauge thickness control. Terminal products include landfill capping, pond liners, and mining heap leach pad barriers. Published data for HDPE 5331H under long-term ASTM D5397 in this specific geomembrane configuration is limited; qualification must be completed on the production line before specification commitment.
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LyondellBasell HDPE 5331H is supplied as a black bimodal high-density polyethylene compound intended for pressure-pipe extrusion. The grade is classified under ISO 12162 as PE100, with a minimum required strength of 10.0 MPa at 20 °C for 50 years. Published representative data list a density of 0.959 g/cm³ when measured according to ISO 1183-1 and a melt flow rate of 0.3 g/10 min under a 5.0 kg load at 190 °C using ISO 1133-1:2022. The numerical suffix 5331H identifies a specific balance of molecular weight, comonomer distribution, and carbon black package within the Hostalen ACP product family. The material is not a general-purpose injection-moulding resin; its rheological signature is engineered for thick-wall pipe and industrial profile extrusion.
The defining structural feature is the bimodal molecular weight distribution produced in a cascade slurry polymerisation process. A low molecular weight fraction contributes controlled shear-thinning and processability, while a high molecular weight fraction with greater comonomer incorporation raises tie-molecule density in the semi-crystalline network. That architecture increases slow crack growth resistance relative to unimodal high-density polyethylene of equivalent density and melt flow rate. The high molecular weight fraction is not merely a broadened single-reactor distribution; it preserves extrudability at commercial line speeds without sacrificing long-term hydrostatic performance.
Unlike a unimodal HDPE with similar density, 5331H resists slow crack propagation along crystalline lamellae by increasing the number of tie molecules that bridge adjacent lamellae. This property is evaluated in pipe form by notched pipe tests under ISO 13479, where a longitudinally notched specimen is subjected to hydrostatic pressure at 80 °C and 4.6 MPa. Published data for this exact grade under full-scale ISO 13479 protocols are not always itemised in public summaries; however, comparable PE100 bimodal grades commonly exceed 500 h to failure. The classification difference is also direct: ISO 12162 assigns a minimum required strength of 10.0 MPa for PE100 and 8.0 MPa for PE80. Pipe wall thickness at equal pressure rating may therefore be reduced when installation codes permit substitution, but actual reduction depends on soil loading, traffic load, surge pressure, and joining practice.
Table 1 lists representative mechanical and thermal values published for 5331H. These data are not batch certificates and should not be used as specification limits; lot-to-lot variance occurs within the manufacturer's release tolerances.
| Property | Test method | Representative value |
|---|---|---|
| Density | ISO 1183-1 | 0.959 g/cm³ |
| Melt flow rate at 190 °C, 5.0 kg | ISO 1133-1:2022 | 0.3 g/10 min |
| Tensile modulus | ISO 527-2 | 1100 MPa |
| Tensile stress at yield | ISO 527-2 | 25 MPa |
| Tensile strain at break | ISO 527-2 | >600% |
| Charpy notched impact strength at 23 °C | ISO 179-1/1eA | 35 kJ/m² |
| Oxidation induction time at 210 °C | ISO 11357-6 | >20 min |
| Carbon black content | ISO 6964 | 2.0–2.5 wt% |
For pressure-pipe service, the controlling material property is long-term hydrostatic strength rather than short-term tensile yield. Design stress is derived from ISO 9080 regression of pipe burst data generated under ISO 1167 at multiple temperatures, typically 20 °C, 40 °C, and 60 °C. The PE100 classification indicates that the predicted lower confidence limit at 50 years does not fall below 10.0 MPa at 20 °C. The grade is intended for water and wastewater lines conforming to ISO 4427 and EN 12201. Gas-distribution suitability must be verified under ISO 4437 because rapid crack propagation resistance and gas-specific fusion protocols are additional qualification barriers; published data for this specific configuration under gas full-scale testing is limited in public literature.
Rapid crack propagation is a separate failure mode from slow crack growth. Bimodal PE100 grades may show improved resistance to rapid crack propagation in small-scale S4 testing according to ISO 13477, but full-scale data for this specific grade is limited. Gas and high-pressure water projects should not rely on short-term Charpy values as a proxy for rapid crack propagation resistance.
Chemical compatibility for industrial pipe service should be evaluated using ISO/TR 10358 or project-specific immersion testing. The grade is resistant to many aqueous salt solutions and dilute acids at ambient temperature, but organic solvents and strong oxidisers require case-by-case assessment. Published data for 5331H in concentrated acid service is limited.
Extrusion lines with a grooved feed section and forced cooling in the feed zone are preferred because the high molecular weight fraction generates substantial shear heat. Screw geometries with an L/D ratio between 30:1 and 33:1 and a barrier or double-flight mixing section provide stable melt temperature control. Production-scale settings reported for similar Hostalen ACP PE100 grades place the barrel temperature profile from 180 °C at the feed throat to 220 °C at the metering zone, with die head zones held between 200 °C and 210 °C. Melt temperature should not be allowed to exceed 240 °C for prolonged residence periods because carbon black and stabiliser package depletion accelerates. Published processing guidelines for 5331H specifically are limited; start-up trials should be conducted against these mechanical-rheological boundaries rather than against generic HDPE settings.
Moisture uptake is negligible; bagged material does not require pre-drying unless surface condensation has formed after outdoor storage at high relative humidity. If condensation is present, a heated-air drying step at 80 °C for 4 h may be applied. Vacuum venting is not normally required for this grade, but a plugged vent port or excessive screw speed can raise volatiles burden and produce microvoids in thick pipe walls.
Wall-thickness control for pipe above 110 mm outer diameter requires ultrasonic scanning immediately after cooling; excursions beyond the wall-thickness tolerance specified in the pipe standard reduce hydrostatic design life at elevated hoop stress. No additional compounding or blending is required before extrusion.
On production-scale lines, batch-to-batch variance in carbon black dispersion is controlled by the resin supplier, but pipe manufacturers should verify dispersion by ISO 18553 or microtome inspection. Poor dispersion appears as agglomerates in the pipe wall and can initiate brittle fracture under cyclic pressure. The black compound should not be mixed with unpigmented HDPE or recycled regrind without prior qualification, because dilution of the carbon black and bimodal molecular weight distribution may compromise slow crack growth resistance and pressure-rating classification.
Under hydrostatic design practice, the allowable design stress for water service is the minimum required strength divided by the service coefficient. ISO 4427 applies a service coefficient of 1.25 for polyethylene, yielding 8.0 MPa for PE100 and 6.3 MPa for PE80 at 20 °C. This numerical gap, rather than short-term tensile value, is the reason 5331H can substitute for a PE80 grade in pressure-pipe systems with a thinner wall when project standards allow the material-class upgrade.
| Parameter | 5331H | Conventional PE80 |
|---|---|---|
| Classification under ISO 12162 | PE100 | PE80 |
| Minimum required strength | 10.0 MPa | 8.0 MPa |
| Design stress for water at 20 °C | 8.0 MPa | 6.3 MPa |
Jointing by butt fusion or electrofusion follows ISO 21307 and ISO 12176-1. The fusion window for 5331H is controlled by melt-flow behaviour; excessive heating can form a wide bead with incomplete interfacial mixing, while cold fusion produces brittle failure under slow crack growth. Production welding trials should qualify the grade on the specific fusion machine, because the black compound's heat absorption profile differs from unpigmented test sleeves used for calibration.
The grade is not suitable for injection moulding, blow moulding, or thin-wall packaging because the melt flow rate of 0.3 g/10 min under 5.0 kg is too low for those tools. Similarly, it is not designed for rotational moulding or film extrusion; those processes require lower-viscosity grades.
Outdoor storage of black HDPE pipe compound is governed by carbon black content. The 2.0–2.5 wt% loading provides ultraviolet stabilisation, but unwrapped pipe should still be covered during prolonged open-yard storage to limit oxidative skin formation. Service temperatures above 20 °C require pressure derating; continuous operation above 60 °C is outside the normal design envelope for PE100 pressure pipe without detailed engineering review. If North American specifications require an ASTM D3350 cell classification, published data for this grade under the ASTM dataset is limited; the ISO-based datasheet should not be converted by equivalence without direct testing.