| HS Code | 697514 |
| Product Name | Borealis HDPE HE4873 |
| Polymer Type | High-Density Polyethylene (HDPE) |
| Density | 0.948 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.2 g/10 min |
| Melt Flow Rate 190 C 21 6 Kg | 8 g/10 min |
| Tensile Modulus | 1100 MPa |
| Tensile Stress At Yield | 28 MPa |
| Elongation At Break | >600% |
| Charpy Notched Impact Strength 23 C | 12 kJ/m² |
| Charpy Notched Impact Strength 30 C | 6 kJ/m² |
| Vicat Softening Temperature | 76 °C |
| Melting Temperature | 132 °C |
| Shore D Hardness | 60 |
| Environmental Stress Cracking Resistance | >1000 h |
As an accredited Borealis HDPE HE4873 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE HE4873 packaging: 25 kg PE bags, 55 bags per shrink-wrapped pallet, total 1,375 kg. |
| Container Loading (20′ FCL) | 20′ FCL loaded with 25 kg bags of Borealis HDPE HE4873, palletized, stretch-wrapped, and securely stowed for shipment. |
| Shipping | Borealis HDPE HE4873 is shipped as solid thermoplastic pellets in moisture-proof bags or octabins, palletized and stretch-wrapped. It is not classified as dangerous goods for road, rail, sea, or air. Store/transport dry, away from heat, sunlight, and contamination; no special hazard placards required. Keep containers sealed and protected from damage. |
| Storage | Store Borealis HDPE HE4873 in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original bags or octabins sealed and pallets off the floor to prevent moisture and contamination. Avoid prolonged high temperatures and UV exposure. Do not smoke or permit open flames. Maintain clean, labeled containers. Use first-in, first-out stock rotation. |
| Shelf Life | Borealis HDPE HE4873 typically has a two-year shelf life when stored in original packaging, dry, cool, and away from direct sunlight. |
High-speed injection moulding of one-piece HDPE closures for carbonated soft drink beverages using Borealis HE4873 is performed on hot runner stack moulds in which cavity counts of 48–96 are standard and dry-cycle capability is pegged to clamp stroke rather than clamp tonnage. The injection unit uses a reciprocating screw of 35–60 mm diameter, 24:1 L/D ratio, and a screw tip check ring with flight clearance below 0.12 mm to prevent backflow of the low-viscosity melt during holding. Barrel settings from feed throat to nozzle are 180 °C, 210 °C, 225 °C, and 235 °C; the hot runner manifold is held at 220–235 °C, and hot runner valve-gate pressure is limited to 800 bar because higher manifold pressure produces gate-stringing from the small nozzle tip. The closure shell wall is 0.9–1.2 mm, tamper-evident break bridge thickness is 0.15–0.30 mm, and gate diameter on the underside plateau is 0.6–0.9 mm. Mould temperature is maintained at 8–12 °C with turbulent water flow above 2.5 m/s in the cooling channels; injection velocity is set above 300 mm/s to avoid jetting and to fill the thin break bridges before solidification. Switch-over from velocity to pressure control occurs by cavity pressure transduction at 450–550 bar, and holding pressure is 600–800 bar for 1.5–2.5 s. Colour masterbatch with an LLDPE carrier is metered at 1.5–2.5 wt%; erucamide slip agent is added at 400–800 ppm by mass, and the antioxidant package remains as supplied in the base polymer. Food-contact compliance is verified under Commission Regulation (EU) No 10/2011, overall migration is tested according to EN 1186-1:2002 using the assigned food simulant, and olefin polymer status is covered by FDA 21 CFR 177.1520 with conditions of use stated on the supplier certificate. Stress cracking at the tamper-evident bridge is screened by ASTM D1693 in 10% Igepal CO-630 at 50 °C; because published data for HE4873-specific bridge thicknesses are limited, lots are compared against the virgin processing benchmark rather than absolute literature values.
Thin-wall injection moulding of dairy cups from HE4873 differs from closure production because the melt must fill a flow length-to-thickness ratio above 200:1 before the gate freezes; cup sidewall thickness is 0.35–0.70 mm, bottom thickness is 0.55–0.85 mm, and draft angle is 1.0–1.5°. The process uses an accumulator-assisted high-speed machine with screw diameter 40–75 mm, injection pressure up to 1,800 bar, and injection velocity 250–400 mm/s. Barrel temperatures from rear to nozzle are 190 °C, 210 °C, 225 °C, and 225 °C; any nozzle zone above 230 °C produces visible gate blush and increases the risk of odour-active volatiles. Mould temperature is 10–15 °C and the cooling pressure drop across the mould is held below 0.8 bar to ensure even temperature distribution. A direct edge gate or hot-tip gate of 0.5–0.8 mm thickness is used; the frozen gate is checked at 0.2–0.4 mm thickness to permit clean automatic degating without puncture. Sidewall flow lines are managed by placing the gate below the cup stacking ring and by using a cold-slug well 6–8 mm deep. Regrind from sprues, start-up scrap, and off-spec cups is added at 15–30 wt% only when the same food-compliant masterbatch is used; post-consumer recycled HDPE is excluded from the food-contact layer. Dairy-contact compliance is assessed under Commission Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm², specific migration is tested in 3% acetic acid for 10 days at 40 °C, and FDA 21 CFR 177.1520 applies for US-market cups. The terminal product is a 125–200 mL single-use dairy cup designed for capping and palletised distribution.
Within the grooming and household detergent packaging sector, Borealis HE4873 is processed into flip-top dispensing closures for liquid soap, shampoo, and surfactant-based household cleaners. The living hinge is moulded at 0.20–0.35 mm thickness, which imposes a processing window not exceeding ±5 °C in the hinge zone; a local mould temperature of 20–25 °C in the hinge insert, while the surrounding cavity runs at 15–20 °C, prevents premature hinge embrittlement. Gate location is placed at the base of the lid opposite the hinge to direct molecular orientation across the hinge line; the cold runner or valve gate has a land length of 1.5–2.0 mm and diameter 1.0–1.2 mm. Melt temperature measured at the nozzle is 215–235 °C, injection velocity is 120–200 mm/s, holding pressure is 450–650 bar, and cooling time is 3–5 s. Formulation includes a polysiloxane processing aid at 0.15–0.30 wt%, a non-amine antistat at 0.05–0.12 wt% to avoid stress-crack acceleration in the hinge, and colour masterbatch at 2–3 wt%; amine-based antistatic additives are excluded because they can accelerate surface microcracking under repeated flexing. Hinge endurance is evaluated by repeated open/close cycling to 500 cycles at 23 °C and 50% relative humidity without visible fracture; notched impact is measured under ISO 179-1/1eA at 23 °C and −30 °C to detect low-temperature hinge failure. Non-food cosmetic packaging is checked for heavy metals under EU Packaging and Packaging Waste Directive 94/62/EC with a combined lead–cadmium–mercury–chromium(VI) limit of 100 mg/kg, and REACH Annex XVII restrictions are screened for phthalates where closures may contact oil-based formulations. The terminal component is a 250–500 mL bottle flip-top closure with a living hinge capable of repeated consumer opening without splitting.
For open-head pails moulded from HE4873 under UN 1H2 design type, regrind practice is dictated by the UN Manual of Tests and Criteria, Part III, and by the commercial requirement that drop-impact retention and stack creep remain within the design qualification range. Post-industrial scrap from the same pail line is added at 15–25 wt%; post-consumer recycled HDPE is limited to 0–15 wt% only where the pail is not used for dangerous goods because lot-to-lot viscosity variation can shift the drop test result. Each regrind blend is verified by ISO 1133-1:2022 method A at 190 °C/2.16 kg and by notched Charpy impact according to ISO 179-1/1eA at −30 °C before reuse. Injection conditions use a single-stage high-torque screw of 60–90 mm diameter, 22:1 L/D ratio, melt temperature 200–240 °C, mould temperature 15–25 °C, and holding pressure 650–850 bar; wall thickness at the pail side is 1.8–2.8 mm and at the top rim is 3.0–4.5 mm. The table below lists the production-level verification matrix for 20–25 L open-head pails used for non-food industrial liquids.
| Verification item | Reference method | Typical production condition | Pass criterion |
|---|---|---|---|
| Drop integrity | UN Manual of Tests and Criteria 6.1.5.3 | Fill to 98% with water, condition at −18 °C for 24 h, drop on weakest point from 1.2 m for Packing Group II | No leak or rupture |
| Leakproofness | UN Manual of Tests and Criteria 6.1.5.4 | Internal air pressure 30 kPa for 30 min | No visible leakage |
| Stacking | ISO 12048:1994 | Load equivalent to 1.5 x maximum gross mass at 40 °C for 28 days | No instability or permanent deformation affecting closure |
For HE4873, the critical limitation is not short-term tensile strength but slow crack growth at the bottom corner radius; pails with a radius below 3.0 mm at the base-to-side transition exhibit elevated drop failure when regrind exceeds 25 wt%. Published data for this specific grade configuration are limited, so filled-pail drop testing on first-off production remains mandatory. The terminal product is a 20–25 L UN 1H2 open-head pail for non-food industrial liquid packaging.
Threaded closures for agrochemical bottles are run from HE4873 on unscrewing-core tools with thread start counts of 2–4 and closure diameters of 38–63 mm. The application imposes continuous contact with ester solvents, xylene, and surfactant adjuvants; environmental stress cracking is therefore the dominant failure mode rather than hinge fatigue. Pre-production compatibility is evaluated by storing closure samples in contact with the actual formulation at 40 °C for 21 days and then measuring retained sealing torque and visual crack formation; ASTM D1693 provides comparative screening but does not replace filled-package immersion testing. Melt temperature is 200–230 °C, mould temperature 15–20 °C, injection velocity 100–180 mm/s, and cooling time 8–12 s because thread roots 0.8–1.2 mm thick require stable demoulding. Cold-runner degating is preferred over hot tips to avoid degraded resin stagnation in the manifold during colour-change campaigns; the runner diameter is 4–6 mm and gate land is 1.0–1.5 mm. Titanium dioxide or carbon-black masterbatch is added at 4–6 wt% for opacity and UV shielding; slip agent loading is kept below 300 ppm to prevent torque loosening after capping machine tightening at 1.8–2.2 N·m. Compliance references Regulation (EC) No 1107/2009 for plant protection product packaging where applicable, and UN 3H1 packaging certification applies when the entire package is submitted as a dangerous goods combination. The terminal component is a tamper-evident or child-resistant agrochemical bottle closure for 1–5 L containers.
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Borealis HDPE HE4873 is a bimodal high-density polyethylene produced by the Borstar multistage polymerisation process. The resin is supplied as pellets for extrusion blow moulding; it is not formulated for injection moulding or cast film. Density under ISO 1183-1:2019 is 0.950 g/cm³; melt flow rate at 190 °C/2.16 kg under ISO 1133-1:2022 is 0.8 g/10 min. These figures are typical release values, not maximum or minimum specification limits. The bimodal molecular weight distribution is the central variable controlling the product’s difference from conventional unimodal HDPE.
The low-molecular-weight fraction lowers shear viscosity under die-lip shear rates, while the high-molecular-weight fraction increases extensional viscosity at the low strain rates relevant to parison sag. This combination reduces parison drawdown in continuous shuttle and wheel-type blow moulding compared with unimodal HDPE grades of identical melt flow rate. In practice, a 10 °C increase in melt temperature can produce a greater sag change than replacing a 0.8 g/10 min resin with a 1.2 g/10 min resin. Published data for this specific configuration is limited; die-swell and sag measurements should therefore be generated on the target tooling rather than extrapolated from capillary rheometry alone.
| Property | Test method | Typical value | Unit |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 0.950 | g/cm³ |
| Melt flow rate, 190 °C/2.16 kg | ISO 1133-1:2022 | 0.8 | g/10 min |
| Tensile modulus | ISO 527-2 | 950 | MPa |
| Tensile stress at yield | ISO 527-2 | 24 | MPa |
| Elongation at break | ISO 527-2 | >600 | % |
| Notched Charpy impact, 23 °C | ISO 179-1 | 15 | kJ/m² |
| Vicat softening temperature, A50 | ISO 306 | 126 | °C |
| Environmental stress crack resistance | ASTM D1693, condition B, 50 °C | >300 | h |
Extrusion blow moulding trials on single-screw machines with L/D ratios between 24:1 and 30:1 indicate that a reverse-temperature profile is normally required. Barrel zones from feed to metering are set from 170 °C to 210 °C, while the die head is held at 190–220 °C. Tooling with a diverging die gap of 0.8–1.2 mm and a mandrel angle of 15–20° provides stable parison swell. Blow-up ratios above 3.0:1 reduce wall-thickness uniformity in oval containers; when ovality exceeds ±0.2 mm, parison programming should be adjusted rather than increasing melt temperature. Mould temperatures of 10–30 °C are typical for fast cooling. Pre-drying is not normally required when pellets are stored in sealed silos below 60 % relative humidity. Condensation on cold pellets transferred from outdoor storage into a warm production hall can create surface moisture; in such cases a dehumidifying hopper dryer at 80 °C for 2–4 h removes film moisture without oxidative yellowing. Regrind from trimmed flash and rejected bottles can be added up to 30 wt% in non-food applications; for food contact packaging, the use of post-industrial regrind must comply with the converter’s quality assurance plan and the relevant food-contact regulation.
Environmental stress crack resistance is measured under ASTM D1693, condition B, at 50 °C in 100 % Igepal CO-630. The typical value exceeds 300 h, but this is a geometry-dependent index; the result does not directly predict field performance with aggressive formulations containing esters, ketones, or nonylphenol ethoxylates. Drop impact at −20 °C is evaluated on finished containers according to ASTM D2463; failure mode analysis shows that the transition from ductile yielding to brittle fracture depends on cooling rate, wall-thickness distribution, and mould surface replication. Pinch-off weld strength, a frequent bottleneck in small detergent bottles, is improved by the high-molecular-weight fraction, but weld-line notches deeper than 0.3 mm should be avoided by maintaining tail flash compression at the parting line.
Compared with a conventional unimodal HDPE with the same 0.950 g/cm³ density, HE4873 typically exhibits lower die-head pressure at constant screw speed and higher melt strength. This permits a reduction in melt temperature of 10–15 °C without sacrificing surface gloss. The lower processing temperature reduces cooling time and shortens dry-cycle time in shuttle machines with clamp forces between 50 kN and 250 kN. Against a low-melt-flow HDPE such as a 0.3 g/10 min blow moulding resin, HE4873 gives faster plastication and lower torque, but it is less suited to very large drums where parison sag is the dominant constraint. Against a high-flow HDPE injection moulding grade of 4–6 g/10 min, HE4873 retains higher melt elasticity and is not intended for injection moulding of thin-wall closures.
Regulatory status is supported by compliance statements referencing FDA 21 CFR 177.1520 for olefin polymers and EU 10/2011 as amended; specific migration limits must be verified on the finished article under the intended food simulant and time-temperature conditions. The resin does not contain substances of very high concern in concentrations above the reporting threshold under REACH and meets the restricted substance requirements of RoHS Directive 2011/65/EU where applicable to packaging. For pharmaceutical or medical device packaging, converters should request a drug master file letter or change-control agreement from the manufacturer; published data for this specific configuration is limited.
| Regulatory reference | Scope | Condition relevant to HE4873 |
|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymers for food contact | Compliance verified on finished article under intended temperature and food type |
| EU 10/2011 | Plastics for food contact | Overall migration limit 10 mg/dm²; simulant selection required |
| REACH | Registration, evaluation, authorisation of chemicals | SVHC below 0.1 wt% |
| RoHS 2011/65/EU | Restriction of hazardous substances | Pb, Hg, Cd, Cr VI, PBB, PBDE not intentionally added |
Assessment of the rheological fingerprint across production lots provides a practical quality indicator beyond single-point melt flow rate. Capillary rheometry at 190 °C shows shear thinning with a power-law index between 0.35 and 0.45 over shear rates from 100 s⁻¹ to 1000 s⁻¹. Batch-to-batch variation in melt flow rate is typically controlled within ±0.1 g/10 min; density variation is controlled within ±0.002 g/cm³. Pellet size distribution after underwater pelletising is monitored by sieve analysis; fines below 0.5 mm are kept below 0.1 wt% to avoid screw slippage in gravimetric feeders. Excessive fines accumulation in the hopper can cause bridging and feed interruption in extruders with L/D above 30:1.
The resin is used in extrusion blow moulding of containers from 250 mL to 5 L for household detergents, personal care products, edible oil, and certain industrial chemical packaging. In detergent bottle trials, the neck finish must be calibrated for compression moulded or injection blow moulded closures with a dimensional tolerance of ±0.15 mm. Bottles intended for hot-fill above 60 °C require a post-mould annealing step or a thicker preform because the Vicat softening temperature of 126 °C does not imply dimensional stability under hot-fill load. The material is not recommended for continuous exposure to strong oxidising agents, aromatic solvents, or post-consumer recyclate blends above 25 wt% without validation of stress crack resistance.