| HS Code | 153267 |
| Grade | BB2581 |
| Polymertype | High Density Polyethylene (HDPE) |
| Density | 958 kg/m³ |
| Meltflowrate | 0.2 g/10 min at 190°C/2.16 kg |
| Tensilemodulus | 1100 MPa |
| Tensilestressatyield | 26 MPa |
| Elongationatbreak | >600% |
| Charpynotchedimpactstrengthat23c | 20 kJ/m² |
| Charpynotchedimpactstrengthatminus30c | 8 kJ/m² |
| Vicatsofteningtemperature | 125 °C |
| Meltingtemperature | 130 °C |
| Environmentalstresscrackingresistance | >1000 h |
| Hardnessshored | 60 |
| Carbonblackcontent | 2.0% |
As an accredited Borealis HDPE BOREALIS BB2581 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Typically, Borealis HDPE BB2581 comes in 25 kg polyethylene bags, palletized and shrink-wrapped; each pallet holds 1000 kg. |
| Container Loading (20′ FCL) | 20′ FCL loading for Borealis HDPE BB2581: 25 kg bags, palletized, approximately 20–22 metric tons per container, dependent on packaging. |
| Shipping | Borealis HDPE BB2581 is shipped as non-hazardous polyethylene pellets in 25 kg bags, octabins, or bulk trucks/railcars. No UN number or dangerous-goods class applies. Keep containers dry, closed, and away from ignition sources; avoid prolonged direct sunlight and extreme heat. Standard industrial handling applies. |
| Storage | Store Borealis HDPE BB2581 in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and ignition sources. Keep original bags sealed and palletized off the floor to prevent moisture and contamination. Avoid prolonged UV exposure and excessive stacking. Maintain clean, compatible storage separate from oxidizing agents, oils, and strong chemicals. Store at ambient temperature. Follow supplier SDS and local regulations. |
| Shelf Life | Shelf life is typically 24 months when stored in unopened original packaging, dry, below 30°C, away from direct sunlight. |
Oxidizing and alkaline household cleaning formulations—sodium hypochlorite solutions within 2.0–6.0 wt% available chlorine, quaternary ammonium disinfectant concentrates, and formulated detergent blends with pH above 11.0—impose environmental stress-cracking loads on monolayer extrusion blow-moulded HDPE containers. Borealis BB2581 is processed in this segment as a natural or masterbatched high-density polyethylene with a density of approximately 0.958 g/cm³ measured in accordance with ISO 1183-1:2019 and a melt mass-flow rate of 0.3 g/10 min at 190°C/2.16 kg under ISO 1133-1:2022. The packaging compliance framework typically references EU Detergent Regulation (EC) No 648/2004 for product labelling, REACH Regulation (EC) No 1907/2006 for substance restrictions, and ADR/RID/IMDG dangerous goods provisions when the filled container exceeds transport thresholds; mechanical qualification is anchored to ASTM D2463-15 for drop impact resistance of blow-moulded thermoplastic containers and ASTM D2561-17 for environmental stress-crack resistance of blow-moulded polyethylene containers. Formulation addition is limited to white or blue masterbatch at 1.0–2.5 wt%, processing aid at 0.2–0.5 wt%, and external regrind up to 30 wt%; the operational boundary is set because pigment loadings above 3.0 wt% can reduce ESCR by creating stress concentration sites at pigment agglomerates, and regrind above 30 wt% produces measurable batch-to-batch viscosity drift. Downstream processing uses single-screw extrusion blow-moulding machines with grooved feed sections and barrier screws of L/D 24:1–30:1; barrel zone temperatures are profiled from 175°C near the feed throat to 210°C at the metering section, the die head is held at 190–210°C, and the parison is inflated at 0.6–1.0 MPa into aluminium or beryllium-copper mould blocks conditioned to 8–18°C. Cycle times for 1–5 L containers fall between 15 s and 45 s, with parison weight control maintained within ±0.5 g to prevent wall thickness drift below 0.8 mm at shoulder and pinch-off zones. Finished product types include 500 mL, 750 mL, 1 L, and 5 L household bleach and detergent bottles, industrial disinfectant canisters with handleware geometry, and trigger-spray refill containers with 28 mm or 38 mm finish diameters.
Solvent-borne emulsifiable concentrates and suspension concentrates containing xylene, cyclohexanone, or N-methyl-2-pyrrolidone require packaging that limits mass loss by permeation and maintains stack integrity under burst-pressure conditions. In such applications, BB2581 forms the structural layers of multi-layer coextruded jerricans, while the barrier function is supplied by a discrete core layer. Compliance for the filled packaging is governed by UN Model Regulations Chapter 6.1 for dangerous goods packagings, with the specific design type tested under ADR/RID/IMDG and marked with a UN packaging code such as 3H1/Y1.9/100/… after passing drop, leakproofness, hydrostatic pressure, and stack tests. Material-level ESCR comparison is performed in accordance with ASTM D1693-21 or ISO 16770:2019, while finished container evaluation uses ASTM D2561-17 for stress-crack resistance and ASTM D2463-15 for drop impact. Barrier layer addition in six-layer coextrusion typically comprises EVOH at 2.0–5.0 wt% or polyamide at 3.0–6.0 wt%, maleated tie resins at 1.0–2.0 wt% per adhesive layer, and BB2581 outer and inner structural layers totalling 92–97 wt%; carbon black masterbatch in the outer layer is added at 0.5–1.5 wt% for UV stabilization, and a UV stabilizer masterbatch at 0.2–0.5 wt% is incorporated where outdoor storage is expected. Processing is carried out on six-layer coextrusion blow-moulding systems with separate extruders for structural and barrier resins; the EVOH extruder maintains melt temperature at 205–220°C after pre-drying to moisture content below 0.10%, while BB2581 structural layers are processed at 190–215°C. Die head temperature is maintained at 200–215°C, parison die gap is profiled between 0.8 mm and 2.5 mm, and the multi-layer parison is protected from moisture-induced delamination by keeping regrind concentration below 20 wt% and by using triple-layer die sequencing to encapsulate the regrind layer. Finished product types include 1 L, 5 L, 10 L, and 20 L narrow-neck jerricans with UN-certified screw closures, child-resistant caps meeting ISO 8317:2015, and gasketed induction seals compatible with solvent-based agricultural actives.
| Test category | Standard designation | Applied to |
|---|---|---|
| Drop impact resistance | ASTM D2463-15 | Filled container, closure in place |
| Environmental stress-crack resistance | ASTM D2561-17 | Blow-moulded container body |
| Material-level ESCR | ASTM D1693-21 | HDPE structural layer |
| Full notch creep | ISO 16770:2019 | Structural resin comparison |
| Child-resistant closure | ISO 8317:2015 | Closure and container system |
Monolayer containers for hydrocarbon-based lubricants, hydraulic oils, and windshield wash concentrates are produced from BB2581 without barrier layers because the non-polar service fluids have low aqueous activity but can plasticize the polymer matrix after prolonged contact. Commercial motor oil packaging in 1 qt and 5 qt containers requires resistance to swelling, creep under top-load, and closure torque retention after hot-fill operations. The packaging qualification matrix includes ASTM D543-21 for chemical resistance of plastics, ASTM D2463-15 for drop impact, and ASTM D2659-16 for column crush properties of blown thermoplastic containers; engine oil classification itself is separate and governed by SAE J300. Formulation addition is controlled as follows: colour masterbatch at 0.5–2.0 wt%, antistatic masterbatch at 1.0–3.0 wt% to reduce dust adhesion on filled bottle surfaces, slip or antiblock additive at 0.05–0.15 wt%, and regrind at 0–25 wt%. Downstream processing uses extrusion blow-moulding with melt temperature maintained at 190–220°C; hot-fill and closure application are limited to product temperatures not exceeding 60°C because closure torque retention degrades at elevated fill temperatures due to relaxation of the neck finish. Wall thickness at the base and handle is maintained above 1.0 mm to resist top-load buckling, and the offset-neck design requires parison programming with die gap adjustment of 0.6–2.0 mm to compensate for parison sag. Finished product types include 1 L and 5 L motor oil bottles with offset necks, handled oil jugs for 5 qt service fills, and windshield wash fluid containers with 38 mm closures.
Surfactant-rich personal care formulations—sodium laureth sulfate, cocamidopropyl betaine, and cationic conditioning agents—create stress-cracking environments comparable to or more severe than detergent systems. BB2581 is used for bottles where high-density polyethylene provides sufficient stiffness for thin-wall lightweighting while maintaining resistance to crazing and environmental stress cracking. Compliance for packaging components is assessed under EU Cosmetic Regulation (EC) No 1223/2009 for the finished cosmetic product safety boundary, while pack-and-fill operations follow ISO 22716:2007; mechanical qualification uses ASTM D2561-17 for stress-crack resistance, ASTM D2463-15 for drop impact, and ASTM D2659-16 for top-load resistance. Formulation addition includes pearlescent or opaque masterbatch at 1.0–3.0 wt%, slip additive at 0.05–0.15 wt%, processing aid at 0.2–0.5 wt%, and colour concentrate matched to brand specifications; excessive masterbatch above 4.0 wt% is avoided because it can reduce stress-crack resistance in thin-wall sections. Downstream processing is performed on extrusion blow-moulding machines with parison programming to maintain wall thickness at 0.5–1.0 mm in cylindrical and oval profiles; blow mould temperatures are held at 10–15°C to increase surface gloss and reduce cycle time, melt temperature is maintained at 190–210°C, and neck calibration diameters are held at 24 mm or 28 mm to retain closure torque after filling. Surface polarity for label adhesion is achieved by inline corona or flame treatment, but treated surfaces retain limited shelf life before labelling and require verification of dyne level after storage. Finished product types include 200 mL, 250 mL, 500 mL, and 1000 mL bottles for shampoos, body wash, conditioners, and pump-dispenser formats.
Transport of corrosive liquid industrial intermediates—acetic acid up to 10%, sodium hydroxide solution up to 50%, sulfuric acid up to 30%, and hydrogen peroxide up to 35%—uses HDPE large-format jerricans with thick walls and UN certification. BB2581 is selected for this segment because its high molecular weight and broad molecular weight distribution provide melt strength needed for thick-walled accumulator-head processing. The compliance matrix includes UN Model Regulations Chapter 6.1, ADR/RID/IMDG, and the design type testing under UN provisions for plastics jerricans: drop, leakproofness, hydrostatic pressure, and stack tests. Mechanical qualification adds ASTM D2561-17 for ESCR, ASTM D543-21 for chemical resistance, ASTM D2659-16 for top-load, and ISO 16770:2019 for full notch creep comparison. Formulation addition includes UV stabilizer masterbatch at 0.2–0.8 wt% for outdoor storage, antistatic masterbatch at 0.5–1.5 wt%, colourant masterbatch at 0.5–2.0 wt%, and regrind limited to 0–20 wt%; the regrind boundary is set because thick-wall sections magnify gel and unmelt defects originating from recycled material. Downstream processing is performed on accumulator-head extrusion blow-moulding machines with L/D 30:1, melt temperature maintained at 200–220°C, and mould cooling water at 8–18°C; post-cooling fixtures are required to control shrinkage deformation in 20–30 L containers with wall thickness from 1.5 mm to 3.0 mm. Finished product types include 20 L, 25 L, and 30 L UN-certified jerricans for corrosive industrial intermediates, with screw closures and tamper-evident seal systems.
| Compliance item | Standard designation | Typical acceptance boundary |
|---|---|---|
| UN drop test | UN Model Regulations Chapter 6.1 | No leakage or rupture after specified drop height |
| Leakproofness | ADR/RID/IMDG | No leakage under specified internal pressure |
| Hydrostatic pressure | UN Model Regulations Chapter 6.1 | No failure at prescribed test pressure |
| Stress-crack resistance | ASTM D2561-17 | No container failure in accelerated ESCR medium |
| Chemical resistance | ASTM D543-21 | No mass loss or surface attack beyond specification |
| Top-load resistance | ASTM D2659-16 | No column crush below filled-container stacking load |
Water-based polymer emulsions, dispersion adhesives, and low-VOC architectural coating intermediates are filled into HDPE wide-mouth containers where chemical inertness and moisture vapour transmission stability are required. The packaging must withstand mild alkaline pH and freeze-thaw exposure from the product without stress cracking at the pinch-off seam. BB2581 is processed in this segment for extrusion blow-moulded 2–20 L pails and wide-mouth containers. The compliance framework references ASTM D543-21 for chemical resistance, ASTM D2463-15 for drop impact, and ASTM D1693-21 for material-level ESCR; for non-food industrial packaging, REACH substance restrictions under Regulation (EC) No 1907/2006 apply to the supplied resin and masterbatch system. Formulation addition includes colourant masterbatch at 1.0–2.0 wt%, UV stabilizer masterbatch at 0.1–0.4 wt%, processing aid at 0.2–0.5 wt%, and recycled HDPE at 0–30 wt% where end-market specifications permit; regrind percentages at the upper limit require continuous melt pressure monitoring to detect viscosity drift. Downstream processing uses single-station shuttle blow-moulding machines with L/D 24:1, melt temperature at 190–215°C, mould temperature at 10–20°C, and parison programming for handleware and bottom pinch-off integrity. Wall thickness is held between 1.0 mm and 2.0 mm to maintain pail rigidity and ensure closure seating under stacking. Finished product types include 2.5 L, 5 L, 10 L, and 20 L wide-mouth pails for water-based adhesives, sealants, construction polymer dispersions, and pigment paste intermediates.
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Borealis HDPE BOREALIS BB2581 is a high-density polyethylene grade supplied as natural-colour pellets for extrusion blow moulding of rigid containers. The published density is 958 kg/m³ when measured to ISO 1183-1:2019, and the melt mass-flow rate is 0.30 g/10 min at 190 °C under a 2.16 kg load according to ISO 1133-1:2022. These two properties define the grade’s basic stiffness-processing balance: the 0.30 g/10 min melt flow rate reflects a high-molecular-weight fraction that supports parison stability, while the 958 kg/m³ density reflects a crystalline fraction sufficient for load-bearing sidewalls. The material is positioned for single-station and double-station shuttle blow moulding of containers up to approximately 5 L in volume, where the combined demands are drop-impact survival, top-load rigidity, and environmental stress cracking resistance.
The melt rheology of BB2581 is controlled by its high melt strength and shear-thinning behaviour during screw plastication. At the low shear rates encountered during parison formation, the resin retains sufficient viscosity to limit sag. At the higher shear rates generated in the die land, viscosity reduction enables practical throughput on shuttle machines. The melt mass-flow rate of 0.30 g/10 min determined to ISO 1133-1:2022 is only a single-point indicator; it does not describe the full molecular weight distribution or extensional viscosity response. In production-scale evaluations on shuttle blow moulding lines, melt temperatures between 180 °C and 220 °C are commonly used. Die temperatures are normally held between 180 °C and 210 °C. Excessively high melt temperatures reduce molecular orientation and can depress top-load strength in the finished container, while excessively low settings raise head pressure and can produce melt fracture at elevated output. The shear rate at a typical die gap of 2 mm may fall between 100 s⁻¹ and 500 s⁻¹ depending on extruder output and die geometry. In this range, high-density polyethylene grades of comparable melt flow rate typically display pseudoplastic flow with a power-law index of approximately 0.4 to 0.6. Published die swell versus shear rate data for this specific configuration is limited, so tooling dimensions should be validated on the target production line using parison weight, die gap, and container wall-thickness distribution measurements.
On extrusion blow moulding lines using 20:1 to 30:1 L/D screws and grooved feed sections, BB2581 is normally processed without pre-drying under controlled indoor storage conditions. If pellets are stored in unheated silos and ambient relative humidity exceeds 60%, surface condensation can create feed-zone surging and should be mitigated by bringing the resin above the dew point before hopper loading. Mould temperatures of 10 °C to 40 °C are commonly applied; the lower end of this range reduces cycle time but can introduce frozen-in stress in thick wall sections. Blow pressure is typically 0.6 MPa to 1.0 MPa, with clamp force determined by projected mould area. Cooling time is approximately proportional to the square of wall thickness. For a 1.5 mm wall section in a 10 °C mould, closed-mould time on shuttle equipment often falls between 15 s and 25 s, but the exact value is tooling-dependent and should be established by thermal imaging or part-weight stability trials.
The table below consolidates principal characterisation methods and typical published values for BB2581. The values are drawn from Borealis technical literature and represent typical values, not guaranteed release limits. Product release limits are governed by the supplier’s certificate of analysis and the relevant grade specification.
| Property | Standard designation | Typical published value | Unit |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 958 | kg/m³ |
| Melt mass-flow rate, 190 °C/2.16 kg | ISO 1133-1:2022 | 0.30 | g/10 min |
| Tensile modulus, 1 mm/min | ISO 527-2:2012 | 1100 | MPa |
| Tensile stress at yield | ISO 527-2:2012 | 26 | MPa |
| Tensile strain at yield | ISO 527-2:2012 | 9 | % |
| Charpy notched impact strength, 23 °C | ISO 179-1:2010 | 10 | kJ/m² |
| Vicat softening temperature, A50 | ISO 306:2013 | 127 | °C |
| Shore D hardness | ISO 868:2003 | 63 | — |
Environmental stress cracking resistance is evaluated to ASTM D1693-15 using 10% Igepal CO-630 at 50 °C. Published F50 values for BB2581 are condition-dependent because residual stress, moulding temperature, cooling rate, and specimen thickness all change the failure time. Comparative rankings should therefore use identical specimen preparation and stress cracking agent concentration. The Charpy notched impact value of 10 kJ/m² at 23 °C to ISO 179-1:2010 provides a ductile-failure reference only when the specimen preparation protocol is fixed. The Vicat A50 value of 127 °C to ISO 306:2013 indicates the temperature at which a defined indenter penetration occurs under a 10 N load; it is not a continuous service temperature limit.
For household chemical and personal care containers, the combination of the 0.30 g/10 min melt flow rate and the 958 kg/m³ density supports a practical balance between top-load strength and drop-impact survival. On production-scale shuttle machines, wall-thickness distribution in the neck and pinch-off zones is sensitive to parison programming. The die gap should be set so that the parison length at mould contact compensates for sag without creating excessive pinch-off flash. Containers moulded with BB2581 can be coloured by masterbatch addition at typical let-down ratios of 1% to 4%, provided the carrier polymer is HDPE-compatible and the extruder temperature profile remains above 180 °C to avoid dispersion defects. Top-load performance can be measured by compression testing of the finished container; sidewall stiffness and yield behaviour should be reported with test speed and support conditions because container geometry influences the result at least as strongly as resin modulus.
When BB2581 replaces a conventional unimodal HDPE blow moulding grade of similar density and melt flow rate, the principal difference is the balance between stiffness and environmental stress cracking resistance. Unimodal grades often require a reduction in density or an increase in comonomer content to raise ESCR, which can reduce top-load strength. BB2581 is part of the Borealis Borstar HDPE blow moulding portfolio, in which the molecular weight distribution and comonomer placement are adjusted so that sidewall stiffness and stress crack resistance are not coupled in the same way as in a unimodal structure. In production, this can allow the same mould to be run with thinner pinch-off wall sections while maintaining drop-impact survival, but the downgauging magnitude must be confirmed by instrumented drop tests to ASTM D2463-15 or equivalent container-specific impact methods. Published data for direct downgauging comparisons on BB2581 is limited; side-by-side moulding trials on the target tool are required.
Against polypropylene, BB2581 exhibits a different failure envelope. High-density polyethylene of this density class generally retains ductile failure at lower temperatures than typical propylene homopolymer, which is why HDPE blow moulding grades are often specified for containers that must survive sub-zero drop events. However, polypropylene may offer higher upper service temperature and different chemical resistance. Direct comparison between BB2581 and polypropylene in instrumented puncture or drop testing is limited in publicly available literature; selection should be based on side-by-side moulding trials with the intended closure, thread, and filling line.
Food-contact compliance for BB2581 must be verified against the current Borealis product statement. Where the final article is intended for food packaging, the converter must confirm that the finished container meets Regulation (EC) No 1935/2004, Regulation (EU) No 10/2011, and, where applicable, FDA 21 CFR 177.1520. The resin data sheet alone does not convey food-contact approval for the final article. The base grade is not recommended for continuous service above 80 °C without mechanical support because creep and stress relaxation become significant. Outdoor exposure requires additional UV stabilisation, and long-term weathering performance should be assessed by ISO 4892-2:2013 or ASTM G154-23. Aggressive surfactant systems, including certain quaternary ammonium compounds, can accelerate environmental stress cracking in high-density polyethylene; ESCR testing should therefore be repeated on the actual container formulation and geometry when the intended fill contains stress cracking agents.