| HS Code | 332890 |
| Materialtype | High-Density Polyethylene (HDPE) |
| Density | 0.952 g/cm³ |
| Meltflowrate | 1.5 g/10 min (190°C/2.16 kg) |
| Tensilestressatyield | 26 MPa |
| Tensilemodulus | 1100 MPa |
| Tensilestrainatbreak | >600% |
| Flexuralmodulus | 1200 MPa |
| Charpynotchedimpactstrength23c | 10 kJ/m² |
| Charpynotchedimpactstrengthminus30c | 4 kJ/m² |
| Vicatsofteningtemperature | 120°C |
| Meltingtemperature | 130°C |
| Hardnessshored | 60 |
| Waterabsorption | <0.01% |
| Thermalconductivity | 0.4 W/m·K |
| Coefficientoflinearthermalexpansion | 1.2E-4 /°C |
| Dielectricstrength | 20 kV/mm |
| Volumeresistivity | 1E16 ohm·cm |
| Moldingshrinkage | 1.5-2.0% |
| Processingtemperature | 190-210°C |
As an accredited Borealis HDPE BS2581 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE BS2581 is packaged in 25 kg polyethylene bags, palletized and securely wrapped for industrial storage and transport. |
| Container Loading (20′ FCL) | Borealis HDPE BS2581 loads 18 pallets per 20′ FCL, each 55 x 25 kg bags, totaling 24.75 MT net, double-stacked. |
| Shipping | Borealis HDPE BS2581 is shipped as a non-hazardous solid polymer in pellet form, usually in 25 kg PE bags or octabins on pallets. It is not classified as dangerous goods for transport (ADR/RID/IMDG/IATA). Keep packaging dry, sealed, and protected from heat, ignition, moisture, and UV exposure. |
| Storage | Store Borealis HDPE BS2581 in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and moisture. Keep pellets in original sealed packaging, palletized off the ground, to prevent contamination and dust. Avoid prolonged UV exposure and extreme temperatures. Use first-in, first-out stock rotation. Maintain clean handling equipment and minimize open-air storage. Follow local regulations and supplier guidance. |
| Shelf Life | Borealis HDPE BS2581 has a two-year shelf life when stored dry, unopened, below 50°C, and protected from direct sunlight and UV. |
On shuttle-type extrusion blow moulding machines equipped with 50–80 mm, 24:1 to 30:1 L/D single-flight barrier screws, Borealis HDPE BS2581 is processed as a monolayer parison for bleach, quaternary ammonium disinfectant, and surfactant-based cleaner containers ranging from 500 mL to 5 L. The barrel temperature profile is typically established from 170°C at the feed throat to 190–195°C at the metering section, with the adapter and die head held at 195–205°C to balance parison hang strength against oxidative volatiles. A die gap of 1.5–2.5 mm is used, and parison sag over a 200 mm free hang should not exceed 10–15 mm before mould closure; greater sag produces thin sidewalls below the pinch-off and reduces top-load reserve. Compatibility with hypochlorite-containing formulations is evaluated through environmental stress-cracking resistance under ASTM D1693-15 Condition A at 50°C; common release thresholds for aggressive oxidising household liquids are an F50 value above 48 h, while lot-specific certificates should be checked against the exact formulation. Top-load behaviour is measured by ASTM D2659-16 at 23±2°C using a 10 mm/min crosshead speed, with failure typically defined as panel buckling or visible crease initiation. Drop impact is screened on filled and capped bottles under ASTM D2463-15 at 23°C and, where cold-climate transport is required, at -20°C after 24 h conditioning. Pellets do not require mandatory drying, but material stored at ambient relative humidity above 70% should be hopper-dried for 1–2 h at 70–80°C; surface moisture on pellets has been observed to produce splay and microvoids in the parison skin that later become stress-cracking initiation sites at the bottle shoulder.
In tall narrow-neck bottles with a length-to-body-diameter ratio above 4:1, the wall thickness distribution is controlled less by the extruder output than by the parison programmer and the annular swell behaviour after the die land. A Hall-effect thickness gauge is used to section bottles at 10 measurement points from the neck inset to the base corner; a wall thickness range tighter than 0.15 mm across the body is required when capping torque exceeds 1.5 N·m. Parison weight variation should be held within ±0.5 g on a 40 g parison because a 1 g shift can reduce the minimum sidewall below 0.6 mm and create a low-top-load failure under ASTM D2659-16. The pinch-off zone is a critical discontinuity: after the flash is trimmed, the weld line at the base should taper from 0.3 mm to 0.5 mm without entrapped air bubbles, since incomplete pinch-off leaves a notch-like crack path when exposed to wetting agents. On machinery without a proportional hydraulic programmer, a stepped die gap profile is used: a smaller gap of 1.2–1.8 mm for the neck region, a larger gap of 2.0–2.8 mm for the body, and an intermediate gap for the base pinch-off. Die swell at the bushing exit typically increases with lower melt temperature and shorter land length; a land length below 10 mm can generate melt fracture lines on the parison surface, while a land length above 25 mm raises die head pressure and lowers output on 60 mm extruders by approximately 8–12%.
Rectangular 2 L containers for concentrated detergents and fabric conditioners are filled on high-speed lines where capping heads apply axial loads between 150 N and 250 N, and the pallet load may superimpose an additional static force during storage. Top-load testing under ASTM D2659-16 is therefore performed both immediately after moulding and after 48 h of load recovery at 23°C to detect post-mould shrinkage effects. The rectangular geometry concentrates stress at the sidewall corners and at the label panel transitions; containers with a 28–34 g weight and a sidewall thickness of 0.7–1.0 mm commonly fail by corner buckling rather than by vertical sidewall crushing. To stabilise the panel geometry, the mould temperature is held between 10°C and 20°C because a higher mould temperature delays crystallisation and increases shrinkage after ejection, while an excessively low mould temperature below 8°C can produce surface stresses that reduce environmental stress-cracking resistance under ASTM D1693-15. The base corner radius should not be reduced below 3 mm without re-qualifying top-load capacity; a sharp corner transitions from compressive yield to local buckling at lower force. When olefinic mineral oil or silicone-based lubricants are used on the mould surface, transfer levels must be below 0.1 mg/dm², because higher residues interfere with label adhesion and can act as environmental stress-cracking agents on the finished container sidewall.
| Application Attribute | Normative Reference | Measured Parameter | Typical Acceptance Range |
|---|---|---|---|
| Environmental stress-cracking resistance | ASTM D1693-15 | F50 failure time, Condition A | Above 48 h at 50°C |
| Top-load rigidity | ASTM D2659-16 | Peak force at 10 mm/min | 180–250 N for 500 mL, 28–32 g |
| Drop impact | ASTM D2463-15 | Failure height, filled containers | Above 1.2 m at 23°C |
| Melt flow rate | ISO 1133-1:2022 | MFR 190°C/2.16 kg | 0.25–0.50 g/10 min |
| Polymer density | ISO 1183-1:2019 | Gradient column density | 0.955–0.960 g/cm³ |
| UN stacking integrity | UN Manual of Tests and Criteria, 6.1.5.3 | Equivalent stack load | 24 h at 3 m stack height without rupture |
A 25 L jerry can blow-moulded from Borealis HDPE BS2581 and filled with a Packing Group III liquid is qualified under the UN Manual of Tests and Criteria, Part III, with drop testing at 0.8 m for PG III and 1.2 m for PG II, followed by leakproofness verification after each drop. The can is dropped on its handle seam, base corner, side seam, and top closure, because the handle bridge and pinch-off are the most frequent fracture origins. Stacking qualification under 6.1.5.3 applies a load equal to the total weight of equivalent packages in a 3 m stack for 24 h; after load removal, the container must not leak or show deformation that compromises closure security. Wall thickness design for a 1.6 kg jerry can typically ranges from 1.1 mm on the side panels to 2.5–3.5 mm at the handle and top shoulder, with the base pinch-off kept above 2.0 mm because the hydraulic impact during drop testing concentrates at the base weld. Process control must include shot weight verification at intervals not exceeding 30 min; shot weight drift greater than 10 g on a 1.6 kg article changes sidewall distribution and can move the failure mode from ductile yielding to brittle weld splitting. The accumulator head is normally held at 190–200°C and the mould at 12–18°C; mould temperatures above 20°C extend cooling time and increase the risk of handle sink marks, while temperatures below 10°C can reduce weld-line strength at the top insert. Frozen-condition transport requires additional cold drop testing at -18°C after chemical conditioning with the intended filling liquid, because residual stress in the handle pinch-off can produce brittle fracture even when room-temperature qualification has passed.
Diameter swell and weight swell after the die bushing are routinely measured by cutting a static parison at a known length and weighing the segment on an analytical balance; weight swell is expressed as the ratio of measured parison mass per millimetre to the theoretical extrudate mass per millimetre. For a die bushing with a land length of 12–20 mm and a gap of 1.8–2.4 mm, diameter swell is often observed in the range 1.15–1.35 for high-molecular-weight blow-moulding HDPE, but published data for Borealis HDPE BS2581 in square and rectangular bushing geometries is limited and should be generated on the target tool. Swell directly controls the pinch-off thickness: excessive swell floods the mould parting line and thickens flash beyond the 0.3–0.5 mm target, while low swell produces a thin weld line that fails under side-impact testing. On accumulator-head machines, the shot size is set 5–10% above the finished article weight to cover flash and neck calibration scrap; a parison length sensor should trigger when the parison extends beyond 700 mm on large jerry can tools to prevent fold-over at mould close. Melt temperature at the die exit is checked with an insertion probe and should be controlled within ±3°C across the circumference; a temperature spread wider than 5°C around the annular gap has been correlated with helical thickness variation in the moulded sidewall. The parison surface skin can cool to approximately 120°C during its free hang, which increases melt strength but raises ejection-time variability if the mould is not closed within the programmed cycle window.
For pharmaceutical dry dosage packaging, extrusion blow moulded containers produced from Borealis HDPE BS2581 may be evaluated under USP <661.1> for extractable metal ions, pH shift, and UV absorbance, provided the finished component is not subject to a mono-material barrier claim. The processing window is shifted downward compared with industrial chemical containers: adapter temperature is limited to 175–190°C to reduce oxidative degradation products, and the hopper residence time should not exceed 30 min. Wall thickness for tablet packs is typically 0.5–0.8 mm, and closure retention torque is verified at 0.4–0.8 N·m after 24 h ageing at 40°C/75% RH. Where food-contact or pharmaceutical declarations are required, the supplier’s grade-specific documentation must be confirmed against EU No 10/2011, 21 CFR 177.1520, and the final container’s migration testing schedule; the base olefin polymer is only one element of the finished article compliance chain.
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Borealis HDPE BS2581 is a black bimodal high-density polyethylene compound supplied in pellet form for solid-wall pressure pipe extrusion. The material is classified as PE 100 under ISO 12162:2009, with a minimum required strength of 10.0 MPa at 20 °C for 50 years, derived from the hydrostatic stress regression methodology of ISO 9080:2012. The grade is specified for potable water distribution and industrial pressure piping within the system standards EN 12201-1:2011+A1:2017 and ISO 4427-1:2019. Carbon black content of 2.0–2.5 % measured under ISO 6964:2019 provides ultraviolet screening for open-air storage and above-ground pipe sections; the same loading does not confer chemical resistance to strong oxidising media.
| Property | Test method | Typical value |
|---|---|---|
| Density at 23 °C | ISO 1183-1:2019 | 0.959 g/cm³ |
| Melt flow rate at 190 °C / 5 kg | ISO 1133-1:2022 | 0.3 g/10 min |
| Carbon black content | ISO 6964:2019 | 2.0–2.5 % |
| Tensile yield stress | ISO 527-2:2012 | 25 MPa |
| Elongation at break | ISO 527-2:2012 | >600 % |
| Oxidation induction time at 210 °C | ISO 11357-6:2018 | >20 min |
Manufacturer-published typical values place the density at 0.959 g/cm³ at 23 °C under ISO 1183-1:2019. The melt flow rate at 190 °C and 5 kg load is 0.3 g/10 min under ISO 1133-1:2022. Tensile yield stress measured on compression-moulded plaques is 25 MPa under ISO 527-2:2012, and elongation at break exceeds 600 %. The oxidation induction time at 210 °C is greater than 20 min under ISO 11357-6:2018. The profile is that of a high-molecular-weight extrusion compound: the low melt flow rate suppresses sag in thick-walled pipe, while the same viscosity excludes use in thin-wall injection moulding or rotational moulding.
Because the product is a black compound, carbon black dispersion is a manufacturing control point. Agglomerates above the threshold defined by ISO 18553:2002 act as local stress concentrations and reduce slow crack growth resistance. Routine dispersion checks on extruded pipe are used because melt filtration alone does not reliably detect sub-millimetre carbon black gels that can initiate brittle fracture under sustained hoop stress.
Borealis HDPE BS2581 relies on a bimodal molar mass distribution produced by the Borstar process. This distribution consists of a low-molecular-weight fraction that reduces melt viscosity and a high-molecular-weight fraction that increases tie-molecule density and slow crack growth resistance. The result is a polymer with a broader rheological spectrum than a conventional unimodal PE100 of equivalent melt flow rate. In extrusion, the high-molecular-weight fraction contributes melt elasticity, which reduces gravity-driven sag after the die. In long-term pressure service, the same fraction increases resistance to crack propagation through the amorphous tie-molecule network.
The difference appears most directly in slow crack growth testing. Under ISO 13479:2009, notched pipe specimens of BS2581-type bimodal PE100 grades exhibit longer failure times than unimodal PE100 at equivalent hoop stress and test temperature. The improved performance is not a matter of higher density alone; density remains close to 0.959 g/cm³. The structural variable is the content of high-molecular-weight material and the continuity of the crystalline network, which can be assessed indirectly through strain-hardening modulus under ISO 18488:2015. Published data for the exact BS2581 strain-hardening modulus is limited; however, PE100 pipe-grade formulations in this class typically exceed 50 MPa.
| Differentiation parameter | BS2581 | Conventional unimodal PE100 | PE80 |
|---|---|---|---|
| Classification | PE 100 | PE 100 | PE 80 |
| Minimum required strength at 20 °C / 50 years | 10.0 MPa | 10.0 MPa | 8.0 MPa |
| Molar mass distribution | bimodal | unimodal | unimodal |
| Melt flow rate at 190 °C / 5 kg | 0.3 g/10 min | typically 0.4–0.7 g/10 min | typically 0.6–0.9 g/10 min |
| Slow crack growth resistance | higher | moderate | lower |
| Extrusion sag tendency | lower | higher | moderate |
Compared with PE 80, the minimum required strength of 10.0 MPa under ISO 12162:2009 permits a higher design stress at the same service life. For a given internal pressure, wall thickness may be reduced relative to PE 80 under the applicable design coefficient in ISO 4427-1:2019. The numerical difference in minimum required strength, 10.0 MPa versus 8.0 MPa, does not translate directly into a proportional thickness reduction because installation, surge pressure, and system inspection requirements also govern. The practical advantage is a higher safety factor at the same wall thickness or a smaller outer diameter for the same hydraulic capacity in pressure mains.
On single-screw grooved-barrel extruders with length-to-diameter ratios from 30:1 to 36:1, the compound is processed with barrel temperature profiles from 190 °C to 220 °C. Melt temperature at the die entry is maintained below 230 °C because prolonged residence above that threshold accelerates depletion of the phenolic and phosphite stabiliser package. Below 190 °C, melt viscosity increases to the point where screw torque rises and melt fracture appears on the pipe surface. Production experience on grooved-barrel lines shows that die-head pressure for large-diameter thick-wall pipe can exceed 250 bar; extrusion lines without high-thrust gearboxes and melt pumps may therefore be limited in throughput. The melt pump inlet pressure is controlled to avoid cavitation and pressure pulsation, which otherwise produce wall-thickness variation along the pipe axis.
Thick-wall pipe of SDR 11 and SDR 9 dimensions requires graduated cooling rather than a single high-rate quench. Rapid surface cooling lowers the outer layer temperature before the core has solidified, creating residual stresses that reduce long-term pressure resistance. Multi-stage cooling baths with water temperatures between 20 °C and 40 °C are common, with additional internal air cooling used for diameters above 630 mm. Wall-thickness measurement by ultrasonic or gravimetric systems is required at the downstream end; the low melt flow rate of the compound makes the wall more sensitive to die swell, which must be corrected through draw-down ratio and calibration sleeve pressure rather than through a simple increase in line speed.
Moisture on pellet surfaces is not a typical processing limitation for HDPE; however, pellets stored outdoors under relative humidity above 60 % can carry surface moisture into the feed throat and generate surface defects in high-speed thin-wall pipe. The use of hopper dryers at 70–80 °C for 2 h is applied when visual surface quality is critical, though such drying is not required for the prevention of hydrolysis. Open-flame or direct-contact heating of pellets is avoided because it can cause local oxidation at the feed zone.
In potable water service, the limiting long-term degradation mechanisms are slow crack growth and antioxidant depletion caused by residual chlorine and chlorine dioxide. The design basis of ISO 9080:2012 does not itself cover continuous exposure to high oxidant concentrations; system owners therefore apply additional safety factors or specify accelerated testing according to ASTM F2263 or ISO 13479:2009 when water quality departs from neutral potable-water assumptions. Field data from pressure mains indicate that failure origins are often located at butt-fusion welds or electrofusion fittings rather than in the pipe body. Welding parameters for BS2581 are selected within the ranges specified in ISO 21307:2017 and DVS 2207-1; excessive interfacial pressure or insufficient bead size produces brittle fusion defects that lower the entire system's hydrostatic strength.
The compound is not intended for continuous immersion in strong oxidizing acids, aromatic hydrocarbons, or high-temperature organic solvents. At temperatures above 40 °C, the maximum allowable operating pressure must be reduced by the service derating factors in ISO 4427-1:2019. For applications involving abrasive slurries or chlorinated water, pipe liners and wall-thickness allowances are calculated separately from the pressure rating. Published data for BS2581 in chlorinated water at residual concentrations above 1 mg/L at 60 °C is limited; accelerated testing on the final pipe system is therefore required before service.
The product differs from black PE80 pipe compounds by its higher pressure rating and improved slow crack growth resistance. It differs from orange or blue single-layer utility compounds by its carbon black content, which is designed for UV stability rather than colour coding. It differs from natural or coloured PE100 grades in that carbon black dispersion must be verified by ISO 18553:2002 or an equivalent dispersion protocol to prevent agglomerates that act as local stress raisers in high-pressure pipe walls.