| HS Code | 900542 |
| Polymer Type | High-density polyethylene (HDPE) |
| Density | 959 kg/m³ |
| Melt Flow Rate 190 C 5 0 Kg | 0.25 g/10 min |
| Melt Flow Rate 190 C 2 16 Kg | 0.05 g/10 min |
| Tensile Stress At Yield | 25 MPa |
| Tensile Strain At Yield | 9% |
| Tensile Modulus | 1200 MPa |
| Elongation At Break | >600% |
| Charpy Notched Impact Strength 23 C | 20 kJ/m² |
| Charpy Notched Impact Strength 30 C | 8 kJ/m² |
| Shore D Hardness | 62 |
| Vicat Softening Temperature | 125°C |
| Brittleness Temperature | < -70°C |
| Thermal Conductivity | 0.4 W/m·K |
| Specific Heat | 1900 J/kg·K |
| Coefficient Of Linear Thermal Expansion | 1.5E-4 /°C |
| Water Absorption | <0.01% |
| Dielectric Strength | 45 kV/mm |
| Volume Resistivity | >1E14 ohm·cm |
| Carbon Black Content | 2.5% |
| Oxidation Induction Time 200 C | >20 min |
| Minimum Required Strength Mrs | 10 MPa |
| Uv Stabilization | Yes |
| Color | Black |
As an accredited Borealis HDPE HE2595 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE HE2595 is packaged in 25 kg moisture-resistant polyethylene bags, stacked on pallets, with optional 1000 kg bulk bags. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with 25 kg bags of Borealis HDPE HE2595 resin, palletized, shrink-wrapped, and secured for ocean transport. |
| Shipping | Borealis HDPE HE2595 is normally shipped as non-hazardous polyethylene pellets in 25 kg bags, FIBCs, octabins, or bulk trucks/railcars. It is not classified as dangerous goods for DOT, IMDG, IATA, or ADR transport. Store dry and ventilated, away from heat, sunlight, ignition, moisture, and contamination. |
| Storage | Store Borealis HDPE HE2595 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, moisture, odors, and contaminants. Keep original bags or containers closed and palletized off the floor. Avoid prolonged UV exposure and temperatures above 50 °C. Use first-in, first-out stock rotation and good housekeeping to prevent dust and static buildup. |
| Shelf Life | Borealis HDPE HE2595 shelf life is typically 2 years when stored cool, dry, and away from direct sunlight in original packaging. |
The grade is employed as a single-component pellet in high-cavitation cap moulds, typically 32- to 96-cavity cold-runner tools, where a roundness tolerance of ±0.15 mm on the shell skirt must be held to maintain removal torque below 1.2 N·m after 24 h of capping. Compliance for potable water contact falls under EU Regulation 10/2011, with overall migration into 10% ethanol or 3% acetic acid simulants not exceeding 10 mg/dm², and FDA 21 CFR 177.1520 for olefin polymers under Conditions of Use A through H. Recycled content is not incorporated; if a converter uses rHDPE, EN 15343 traceability and EU 2022/1616 authorisation are required. Formulation remains unmodified except for a titanium dioxide masterbatch at 1.5–2.0 wt% total blend when opaque white caps are required; no slip additive is used, because a coefficient of friction below 0.20 is required at the cap–bottle thread interface. Melt temperature is held at 200–240 °C, mould temperature at 10–20 °C, and injection velocity at 40–80 mm/s to avoid jetting in thin gates; hold pressure is 45–60 MPa for 1.0–1.5 s until gate freeze. Dimensional failure at the gate occurs when hold pressure is released before gate solidification, leaving a sink depth greater than 0.03 mm on the top deck; the gate freeze time is verified by short-shot progression on the production machine rather than assigned as a fixed value.
Batch-to-batch variation in melt viscosity is recorded by in-mould cavity-pressure sensors; when the integral of cavity pressure over time shifts by more than 15% from the qualification lot, the cap top deck begins to show sink or the skirt roundness drifts outside tolerance. This is controlled by adjusting shot size and hold-pressure time within the above limits rather than raising barrel temperature, which accelerates organoleptic degradation. Capping line trials are required before lot approval because the closure must pass a non-destructive vision inspection at 0.01 mm resolution for ovality and a leak test at 20 kPa internal air pressure.
Thin-wall dairy cups and spreadable-fat containers converted at wall stock 0.35–0.80 mm place the highest demand on flow-length-to-wall-thickness ratio, which can exceed 200:1 in 500 mL tubs, and on melt stability. The material is processed without pre-drying at ambient relative humidity below 60%; above this threshold, surface splay on the sidewall becomes visible and requires a 80 °C hopper dryer with a 2 h residence time. Food-contact approval is documented under EU Regulation 10/2011 for simulant A (10% ethanol), B (3% acetic acid), and D1 (50% ethanol), and under FDA 21 CFR 177.1520; a declaration of compliance for the final article must list the masterbatch carrier resin and the migration limits for the chosen simulant. The formulation comprises 100% virgin HE2595 in the first production run and is permitted to include up to 20 wt% clean in-house regrind from the same cups after granulation through a 6 mm screen, provided the melt flow rate of the blend is checked per ISO 1133-1 and does not shift by more than 10% relative to virgin material. Injection moulding uses a 24:1 L/D barrier screw with compression ratio 2.5:1, melt temperature 205–230 °C, and mould temperature 8–20 °C. Hot-runner valve gates are preferred over cold runners for stacking-fit lids, with gate diameter 0.6–1.0 mm; the final cups are tested for stackability at a top load of 150–250 N per 100 mL of capacity and for stress cracking under a 10% nonylphenol ethoxylate solution per ASTM D1693-15 Method B. Published data for the specific HE2595 grade in this dairy-cup configuration is limited, but the material's high-flow HDPE architecture falls within common industrial practice for thin-wall injection moulding.
In interlocking storage crates, stack-line weld strength is governed less by barrel temperature than by the temperature of the melt at the flow front and by the pressure available at the weld line. The grade is dry-blended with a carbon black masterbatch at 2.0–2.5 wt% when outdoor UV resistance is required; for indoor transparent or tinted crates, a phthalocyanine or quinacridone colour masterbatch is used at 0.8–1.5 wt%, but no filler is added because talc above 1.0 wt% reduces weld-line elongation at break below the 8% required for drop impact at -20 °C per ISO 179-1/1eA. The conversion equipment is typically a 20:1 to 24:1 L/D general-purpose screw with a compression ratio of 2.2:1 to 2.8:1; barrel profile from feed to nozzle runs 180–200 °C, 210–220 °C, 220–230 °C, and 230–240 °C. For a 600 mm × 400 mm × 320 mm crate weighing 1.4–1.8 kg, clamp force is set between 8000 and 12000 kN, and injection pressure at the screw tip is 70–100 MPa. The critical weld-line defect is a cold-flow front intersecting at a rib root, producing a V-notch with residual stress that opens during side-load stacking at 40 °C. The mitigation is a two-stage injection profile: first stage fills to 95% at 50–70 mm/s, the second stage packs at 30–45 mm/s until the gate freezes. No post-treatment is used. End products are stackable household crates, storage bins, and garage modules covered by REACH and RoHS compliance for heavy metals, with the final item marked per ISO 11469 for polymer identification.
For open-head pails in the 5–25 L range, the cooling-time requirement is not linear with wall thickness because the volumetric shrinkage of semi-crystalline HDPE must be compensated before gate freeze. Moulded wall sections between 1.8 mm and 3.5 mm require packing profiles that compensate for volumetric shrinkage of 2.0–3.0%; otherwise top-chime ovality exceeds 0.8 mm and the lid gasket loses sealing compression. The material is processed as 100% virgin HE2595 when the pail is certified for dangerous goods under ADR/RID and UN 6.1.5.3; if industrial non-hazardous pails are produced, up to 15 wt% clean regrind from post-industrial pail scrap is introduced after melt filtration through a 100-mesh screen pack. Vacuum venting is applied at -0.06 MPa to remove volatiles from recycled content, and an organoleptic test per EN 1622:2006 is carried out when the pail will contact foodstuffs. Injection is performed on a 25:1 L/D barrier screw with check ring, melt temperature 190–220 °C, and mould temperature 10–25 °C; the hold pressure is 60–80 MPa, with hold time scaled at 0.4–0.6 s/mm of nominal wall. For a 10 L pail, the cycle time is controlled by the gate area because the central sprue gate remains molten longer than the wall; solidification time in the gate region is estimated from the square of the effective thickness, so the gate is designed as a 2.5–3.0 mm diameter hot-sprue channel to extend packing without extending the cycle. Stacking-compression tests at 40 °C and 75% relative humidity for 28 days per UN 6.1.5.3 are used to verify the pail shoulder does not crack when filled to 95% nominal capacity and loaded with 1.5 times the static stacking mass. The final article is labelled with the UN packaging code and the specific gravity under ISO 1183-1.
When carbonated soft-drink closures in 28/25 mm and 38 mm sizes are produced, a stress-cracking failure mode associated with the thread root under internal pressure and torque controls the process window. The grade is moulded with a neat formulation of 100% virgin HE2595; no post-consumer recyclate is added because the organoleptic requirements and CO₂ retention boundary are not met above 5 wt% recyclate without vacuum devolatilization. A slip additive is generally avoided because the shell must retain a removal torque of 1.0–1.4 N·m after 24 h at 22 °C; instead, surface lubrication is achieved by mould-side plasma or fluorination where dictated by capping line efficiency. Injection-compression moulding, rather than conventional injection, is specified when the top deck thickness falls below 0.8 mm and the thread root radius is below 0.2 mm, because conventional packing cannot transmit pressure through such thin sections without excessive gate stress. Melt temperature is 200–235 °C; mould temperature is 8–15 °C. The press closes to a gap 0.1–0.2 mm above final part thickness during injection, then compresses at 0.3–0.5 MPa surface pressure for 0.5–1.0 s. This reduces molecular orientation at the gate and lowers the incidence of radial cracks under drop impact from 1.5 m per ASTM D2463-15. The final closures are tested for CO₂ retention at 40 °C and 85% relative humidity for 28 days, with a maximum weight-loss threshold of 0.5% of gross bottle weight, and for stress-cracking resistance under ASTM D1693-15 Condition B. The relevant food-contact instruments remain EU Regulation 10/2011 and FDA 21 CFR 177.1520.
A living hinge in flip-top caps for personal-care viscous products requires a minimum flexural fatigue life defined by the cap geometry rather than by polymer grade alone. The grade is dry-blended with a silicone masterbatch at 0.8–1.2 wt% to lower hinge friction and with a UV absorber at 0.15–0.25 wt% where translucent colour retention is specified. Compliance is assessed under EU Regulation 1223/2009 for cosmetic packaging and under REACH Annex XVII entries relating to phthalates and heavy metals; food-contact testing is not required unless the same cap is used on a dual-use toiletries line. The living hinge is filled from a subgate located on the top deck, with gate diameter 0.6–0.8 mm and melt temperature 200–230 °C. A critical process boundary exists at mould temperatures below 10 °C: rapid freezing of the hinge mid-thickness produces a frozen-in skin that fails by flexural fatigue before 100 open-close cycles, whereas mould temperatures of 15–30 °C extend fatigue life beyond 500 cycles when measured by a motorized hinge-flex test at 0.5 Hz. The final cap is assessed for hinge performance by the same motorized test after conditioning at -10 °C, 23 °C, and 45 °C for 48 h; tensile elongation at break of the hinge material is benchmarked per ISO 527-2, with values below 50% after accelerated weathering rejected. Published data for the specific HE2595 grade in flip-top hinge configurations is limited, so converter-specific hinge-fatigue studies are made before lot approval.
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Borealis HDPE HE2595 is a high-molecular-weight, high-density polyethylene extrusion blow-moulding grade intended for rigid packaging in the 1–10 L range. It is commonly specified for detergent, cosmetic, and industrial chemical containers in which environmental stress crack resistance, top-load strength, and water-vapour barrier are simultaneously required. Under ISO 1183-1:2019, the nominal density is 959 kg/m³; under ISO 1133-1:2022 at 190 °C and 2.16 kg, the melt mass-flow rate is 0.30 g/10 min. The low flow index places HE2595 in the high-molecular-weight segment of HDPE blow-moulding resins, separating it from injection-moulding HDPE grades with MFR2 values of 4–20 g/10 min and from general-purpose bottle grades with MFR2 values above 1.0 g/10 min. The grade is supplied as natural pellets and is typically processed without pre-drying unless the pellets have been stored under conditions that allow surface condensation.
The practical consequence of a 0.30 g/10 min MFR2 is high melt viscosity at low shear rates, which controls parison sag between die exit and mould closing. In production-scale shuttle blow moulding machines, die swell and parison ovalisation are the principal variables limiting bottle weight consistency. HE2595 tends to produce a higher die-swell ratio than lower-viscosity HDPE grades, requiring wider parison programming allowances and more conservative die pin movement. A typical 60 mm grooved-barrel extruder with a 24:1 L/D ratio can be expected to run at head pressures of 280–340 bar at a die temperature of 200 °C, with screw speed adjusted to maintain 30–60 rpm. The observed pressure is a function of both molecular weight and shear-thinning; the ratio of MFR2 to MFR5 is approximately 0.27, indicating significant non-Newtonian behaviour. That rheological character supports stable parison formation but means any increase in regrind particle-size distribution, melt-temperature drift above 220 °C, or die-gap narrowing can shift die swell abruptly. Production records from continuous shuttle lines show bottle-weight variation below ±2% only when the melt temperature is held within a 190–210 °C band and the parison length is actively controlled by calibrated photocells.
Because the grade has high density, cooling-induced crystallisation is rapid. Blow moulds maintained at 15–25 °C are required to prevent post-mould shrinkage and warpage in flat panel sections; mould temperatures below 10 °C can cause surface haze and chill marks. Pre-drying is normally unnecessary, but pellets exposed to high humidity should be passed through a desiccant hopper or hot-air dryer at 60–80 °C for 2–4 h only if surface moisture is visible. Blowing air pressure for technical containers is typically 6–10 bar, and blow time is controlled to achieve uniform wall thickness at corners. Regrind levels of post-industrial trims are commonly limited to 20 wt% in ESCR-critical applications; higher levels reduce stress-crack resistance and shift the odour profile of the final container. When the grade is used on a blow line previously optimised for a lower-viscosity HDPE, extruder torque and melt pressure rise. Operators should not compensate by increasing barrel temperatures above 220 °C because chain scission and the formation of low-molecular-weight oxidised species lower environmental stress crack resistance in the finished container.
Environmental stress crack resistance is the central property for detergent, surfactant, and diluted agrochemical packaging. Slow crack growth in HDPE proceeds through tie-molecule rupture ahead of a craze-like damage zone under external stress. In ASTM D1693-21, condition A, HE2595 typically exhibits F50 beyond 1000 h in 10% Igepal CO-630 at 50 °C. Published data for this specific configuration is limited at test temperatures above 60 °C or for surfactant systems with high linear-alkylbenzene sulfonate content. The high density of 959 kg/m³ reduces equilibrium moisture uptake and water-vapour transmission rate compared with typical LDPE or LLDPE, but it does not make the material suitable for aromatic or halogenated solvents. Containers produced from HE2595 should be limited to aqueous detergent systems, diluted acids, and alkalis at ambient or mildly elevated temperatures. Continuous contact with strong oxidizing acids, aromatic hydrocarbons, or chlorinated solvents above 40 °C is outside the grade’s operational boundary. Post-consumer recyclate with unknown surfactant history should be validated before use by ASTM D1693-21 or ISO 22088-2:2021 notched constant tensile load methods. The grade may also be pigmented with carbon black or coloured masterbatches, but high loadings of calcium carbonate or talc should be avoided because plate-like fillers initiate stress concentrations that negate the ESCR advantage.
Tooling built for lower-density HDPE grades with density 945–950 kg/m³ may require modification when HE2595 is introduced. The higher density increases orientation-induced shrinkage in the amorphous fraction and raises mould ejection forces on deep-textured surfaces. Pinch-off flash thickness in extrusion blow moulding depends on melt temperature, mould closing speed, and parison wall geometry. If the same parison programming is used, the higher low-shear viscosity of HE2595 can generate thicker pinch-off scars and higher downstream trimming force. In practice, the parison programmer profile is split into wall-thickness zones, and the die gap is adjusted from a starting range of 1.5–3.5 mm depending on container volume and target wall thickness. Top-load strength under ASTM D2659-16 is improved by the higher density and wall-thickness consistency, but operators should not assume that down-gauging by more than 10–15% is possible without finite-element verification of column strength and drop impact. Drop impact resistance at -20 °C should be evaluated according to ASTM D2463-15 or ISO 6272-2. The higher crystallinity of HE2595 can reduce low-temperature impact energy relative to lower-density HDPE grades, so cold-climate distribution trials are necessary before commercial conversion.
The typical property matrix below is compiled from publicly available data sheets and should not be read as a contractual specification for individual lots.
| Property | Test standard | Typical value |
|---|---|---|
| Density | ISO 1183-1:2019 | 959 kg/m³ |
| Melt mass-flow rate, 190 °C/2.16 kg | ISO 1133-1:2022 | 0.30 g/10 min |
| Melt mass-flow rate, 190 °C/5.0 kg | ISO 1133-1:2022 | 1.1 g/10 min |
| Tensile modulus | ISO 527-2:2012 | 1150 MPa |
| Tensile stress at yield | ISO 527-2:2012 | 27 MPa |
| Tensile strain at yield | ISO 527-2:2012 | 8% |
| Charpy notched impact strength, 23 °C | ISO 179-1:2023 | 22 kJ/m² |
| Charpy notched impact strength, -30 °C | ISO 179-1:2023 | 6 kJ/m² |
| Vicat softening temperature, A50 | ISO 306:2022 | 127 °C |
| Shore D hardness | ISO 868 | 64 |
| Environmental stress crack resistance, F50 | ASTM D1693-21, condition A | >1000 h |
Processing parameters are machine-dependent. The following start-up window is typical for a shuttle blow moulder using a 60 mm grooved-barrel extruder with a 24:1 L/D ratio.
| Parameter | Start-up range |
|---|---|
| Barrel profile | 170–200 °C |
| Die head temperature | 195–205 °C |
| Melt temperature at die exit | 190–210 °C |
| Blow mould temperature | 15–25 °C |
| Blowing air pressure | 6–10 bar |
| Screw speed, 60 mm extruder | 30–60 rpm |
| Head pressure | 280–340 bar |
| Pre-drying | Not normally required; if condensation visible, 60–80 °C for 2–4 h |
| Regrind addition | Up to 20 wt% for non-critical; ESCR-critical applications require validation |
For food-contact packaging, the final article must be evaluated under EU Regulation 10/2011 and US FDA 21 CFR 177.1520 for olefin polymers. The base resin alone does not establish migration compliance for the final container; additives, masterbatches, and processing aids must be assessed in the finished article. Under RoHS Directive 2011/65/EU, unpigmented high-density polyethylene is not typically subject to restricted substance limits for the six priority substances, but suppliers should provide REACH Article 33 declarations for substances of very high concern. Users should confirm that the grade as supplied does not contain intentionally added perfluorinated compounds or phthalates when those substances are excluded by brand-specific packaging standards. The grade is not considered suitable for rotational moulding or thin-wall injection moulding because its molecular architecture is optimised for extrusion blow moulding; attempts to use it in cast film or thin-wall injection moulding typically produce high melt pressure and poor draw-down.