| HS Code | 673854 |
| Density | 0.946 g/cm³ |
| Melt Flow Rate 190 C 5 Kg | 0.6 g/10 min |
| Tensile Modulus | 900 MPa |
| Tensile Stress At Yield | 22 MPa |
| Tensile Strain At Break | >600% |
| Charpy Notched Impact Strength 23 C | 20 kJ/m² |
| Charpy Notched Impact Strength 20 C | 10 kJ/m² |
| Vicat Softening Temperature | 75°C |
| Oxidation Induction Time 200 C | >20 min |
| Carbon Black Content | 2.0-2.5% |
| Moisture Content | <0.1% |
| Thermal Conductivity | 0.4 W/m·K |
| Coefficient Of Linear Thermal Expansion | 2 x 10^-4 1/°C |
| Specific Heat Capacity | 1900 J/kg·K |
| Volume Resistivity | >10^14 Ω·cm |
| Dielectric Constant | 2.3 |
| Hardness Shore D | 60 |
As an accredited Borealis HDPE HE3466-RT factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE HE3466-RT is typically supplied in 25 kg polyethylene bags, 40 bags per 1,000 kg pallet, or bulk containers. |
| Container Loading (20′ FCL) | Borealis HDPE HE3466-RT in 25 kg bags, palletized and shrink-wrapped, securely loaded into a 20-foot FCL container for ocean shipment. |
| Shipping | Borealis HDPE HE3466-RT is a non-hazardous polyethylene resin, not classified as dangerous goods for transport. It is shipped in 25 kg bags, FIBCs, or octabins on pallets, in dry trucks or containers. Keep dry, clean, and away from excessive heat, sunlight, and contamination. Observe normal industrial hygiene. |
| Storage | Store Borealis HDPE HE3466-RT in a cool, dry, well-ventilated area at ambient temperature, away from direct sunlight, UV radiation, heat, ignition sources, and strong oxidizers. Keep original bags sealed, palletized, off the floor, and protected from moisture, dust, odours, and contamination. Avoid excessive stacking. Rotate stock first-in, first-out and use within supplier-recommended shelf life. Do not expose to open flames. |
| Shelf Life | Typically 12 months from production when stored dry, in unopened original packaging, below 50°C, away from direct sunlight. |
In chemical park utility corridors where demineralized water, glycol–water mixtures, and cooling tower blowdown circulate at sustained temperatures above 40°C, conventional PE100 compounds exhibit measurable creep acceleration and a progressive reduction in oxidative induction time. Borealis HE3466-RT is qualified under ISO 15494 for industrial polyethylene piping systems. The raised-temperature designation corresponds to long-term hydrostatic strength evaluated at service temperatures up to 60°C using the ISO 9080 reference methodology. The compound is processed on a grooved-barrel single-screw extruder with an L/D ratio of 30:1 to 33:1. Barrel zones are profiled from 190°C in the feed section to 230°C at the breaker plate. Die head temperature is held at 210°C to 220°C. A melt gear pump stabilizes output before a spiral mandrel die. Vacuum sizing with closed-loop water at 15°C to 25°C fixes the outside diameter. For pipe above OD 250 mm, the cooling rate is staged to limit frozen-in wall stress; longitudinal reversion is checked per ISO 2505. Finished pipe is supplied in SDR 11 to SDR 17 dimensions. Butt fusion jointing follows ISO 21307 with heater plate temperatures in the 200°C to 230°C range. A process limitation exists with strong oxidizers: chlorine dioxide or ozone exposure above 1.0 mg/L at temperatures above 40°C consumes stabilizers faster than predicted by hydrostatic tests alone, and chemical resistance should be confirmed under ISO 15494 Annex B before continuous service.
Where a copper tailings line crosses a valley floor with ambient air temperature reaching 45°C, the combined effects of abrasive slurry and elevated temperature shorten service life of standard PE100 resin unless slow crack growth resistance is explicitly selected. Borealis HE3466-RT is specified for slurry densities between 1.4 kg/L and 1.8 kg/L and flow velocities of 2 m/s to 5 m/s. The decisive material test is the notched pipe test per ISO 13479 at 80°C and 4.0 MPa hoop stress, which ranks slow crack growth under point loading and pipe wall scoring. In mining operations, wall thickness is selected from the ISO 12162 pressure rating table using an SDR 11 minimum for slurry lines subject to internal erosion. The pipe is produced on the same grooved-barrel extruder configuration used for industrial water pipe, but die land temperature is lowered to 205°C to suppress melt surging when running thick-wall SDR 11 dimensions above OD 450 mm. Carbon black dispersion is verified by ISO 18553. Field jointing uses electrofusion couplers per ISO 12176-1 for repair saddles and tap fittings. Published specific wear rates for this grade in slurry service are limited; abrasion performance is typically evaluated on site through wall-thickness ultrasonic surveys rather than from a single laboratory standard.
| Test method | Measured property | Relevance to HE3466-RT processing |
|---|---|---|
| ISO 9080 | Long-term hydrostatic strength | RT classification for 50-year service at elevated temperature |
| ISO 12162 | Minimum required strength | PE100-RT pressure rating basis |
| ISO 1167 | Hydrostatic strength at 20°C and 80°C | Batch release testing after extrusion |
| ISO 13479 | Notched pipe slow crack growth | Screening for slurry and point-load service |
| ISO 13477 | Rapid crack propagation critical pressure | Low-temperature gas and water line safety |
| ISO 18553 | Pigment dispersion | UV and oxidation resistance of black pipe |
Cyclic cleaning-in-place sequences impose rapid temperature swings that generate thermal wall stresses beyond those captured by static hydrostatic testing. A dairy processing line, for example, alternates between 4°C product water and 75°C caustic rinse cycles. Borealis HE3466-RT is rated for such intermittent thermal loads when cumulative damage is assessed under ISO 13760 Miner’s rule using the hydrostatic strength reference curves for the RT class. The pipe is extruded in SDR 13.6 and SDR 17 dimensions for process water distribution headers. Post-extrusion annealing is not required, but a minimum 24 h conditioning period at 20°C is specified before hydrostatic proof testing to 1.5 times the nominal pressure rating for 1 h. Sanitary process connections use PE stub ends with stainless steel backing flanges rather than threaded transitions. Food-contact compliance is established under EU Regulation 10/2011 and FDA 21 CFR 177.1520 for olefin polymers. The operational boundary is 80°C: steam sterilization cycles at 121°C are outside the allowable thermal envelope and will cause irreversible pipe deformation and fusion bead failure. Thermal expansion is 0.20 mm/m·K, so pipe brackets must accommodate axial growth rather than restrain it.
A closed-loop geothermal borehole field presents a different mechanical loading mode: sustained internal pressure combined with point loads where U-bend fittings are pushed into borehole annuli. Borealis HE3466-RT is specified for the header and vertical loop sections when formation temperatures exceed 35°C. The pipe is joined by butt fusion under ISO 21307 and by socket fusion for U-bend elbows, with fusion parameters adjusted for the density of 0.959 g/cm³ per ISO 1183-1 and MFR in the 0.20–0.30 g/10 min range at 190°C/5 kg per ISO 1133-1. Loop pressure ratings follow ISO 12162 with a minimum required strength of 10 MPa at 20°C for 50 years. For higher-temperature branches, the design stress is derated according to the service temperature. Slow crack growth is evaluated by ISO 13479 notched pipe test. Heat transfer fluid compatibility is limited to glycol and water mixtures; aromatic-based antifreeze compounds must be avoided because they induce environmental stress cracking at fusion interfaces. Pressure testing after loop installation uses water at 1.5 times the design pressure for 30 min per ISO 13274, but published data for this specific configuration is limited.
| Parameter | Range | Measurement point |
|---|---|---|
| Barrel feed zone | 190–210°C | Heater jacket thermocouple |
| Barrel compression zone | 210–230°C | Heater jacket thermocouple |
| Die head temperature | 210–220°C | Adapter entry |
| Vacuum sizing water | 15–25°C | Spray tank inlet |
| Screw L/D ratio | 30:1–33:1 | Extruder specification |
Produced water transfer lines in oilfield gathering systems increasingly use polyethylene instead of internally lined carbon steel. Borealis HE3466-RT is specified where the produced water exits the separator at 45°C to 60°C and carries chloride concentrations above 50,000 mg/L. The compound is listed under API Spec 15LE for polyethylene line pipe, with pipe dimensions governed by ASTM F714 for outside-diameter-controlled PE pipe. Pressure design follows ISO 12162 with an additional service temperature derating consistent with ISO 9080 reference curves. On the production side, a grooved-barrel extruder with L/D 33:1 runs SDR 9 through SDR 13.6 diameters for high-pressure gathering service. Fusion joints are made by butt fusion per ISO 21307. A limitation applies to produced water containing aromatic hydrocarbons: benzene, toluene, ethylbenzene, and xylene diffuse into the amorphous phase of polyethylene, and continuous BTEX exposure above 1.0% by volume requires a design review because swelling can reduce long-term tensile strength and induce environmental stress cracking at surface defects.
Buried beneath a shoreline revetment and pulled through a directionally drilled borehole, a high-density polyethylene outfall line must resist tensile pull forces, saltwater exposure, and UV degradation during above-water staging. Borealis HE3466-RT is specified for the diffuser section because the circulating water temperature in shallow tropical lagoons can exceed 35°C. Multi-hundred-metre strings are assembled on the beach by butt fusion per ISO 21307. Because the density of 0.959 g/cm³ is below seawater at 1.025 g/cm³, the pipeline must be weighted with concrete ballast collars to achieve negative buoyancy. Carbon black dispersion per ISO 18553 provides UV stabilization during the staging period. Diffuser ports are field-drilled after pressure testing, and the exterior surface is inspected for scoring before submersion because notch defects accelerate slow crack growth in marine burial conditions. Incompatibility exists with strong solvent plumes from port industrial discharges; continuous exposure to aromatic or chlorinated solvents above trace levels is outside the verified chemical resistance envelope for this configuration.
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Borealis HDPE HE3466-RT is a black, bimodal high-density polyethylene compound supplied as compounded pellets for pressure pipe extrusion. The grade is classified in the PE100 family under ISO 12162, and the RT suffix indicates that long-term hydrostatic strength has been evaluated at elevated temperatures beyond the standard 20°C reference condition of ISO 9080. This distinction is critical: HE3466-RT is not a low-density PE-RT resin of the type covered by ISO 22391 for domestic hot and cold water plumbing. The product is intended for industrial pressure pipe systems conveying water, process water, slurries, and aqueous media at elevated service temperatures. The formulation combines a high-molecular-weight HDPE resin, a carbon black masterbatch for ultraviolet stability, and a stabiliser package formulated to preserve slow crack growth resistance after thermal exposure. The principal conversion route is single-screw extrusion of solid-wall pipe; the product is not optimised for injection moulding of pressure fittings.
In comparison with PE80 pipe grades, HE3466-RT permits thinner wall sections at identical pressure rating because of the higher minimum required strength. Against a standard PE100 compound, the RT grade is selected only when the service temperature exceeds the ambient design basis; at 20°C the two materials may appear interchangeable in short-term tensile terms, but the RT grade carries a more demanding stabiliser system and a narrower processing window. It is also distinct from PE-RT materials used in domestic hot and cold water systems under ISO 22391, which are typically lower-density copolymers and are not designed for thick-wall industrial pressure service.
PE100 classification under ISO 12162 requires a lower confidence limit of long-term hydrostatic strength of 10 MPa at 20°C and 50 years when tested in pipe form and regressed according to ISO 9080. The classification is not based on a single burst test; it requires failure points distributed over multiple internal pressure levels and extrapolation to 50 years at the reference temperature. The raised-temperature extension does not alter the 20°C MRS value; it adds hydrostatic regression points at elevated temperatures, commonly 60°C and, for some product qualifications, 70°C. The engineering significance is not higher burst pressure at ambient temperature, but slower loss of allowable hoop stress as wall temperature increases. A standard PE100 black pipe compound can show a steep decline in long-term strength at 60°C; the RT grade is formulated and validated to retain a higher creep rupture strength in that band. The exact allowable design stress is not obtained from material classification alone, because pipe standards apply design coefficients such as 1.25 in water service. Pipe produced from HE3466-RT can be specified within ISO 4427-1 for pressure water systems, or within ISO 4437-1 for gas distribution, only when the pipe manufacturer has completed the applicable pipe-standard qualification. Resin classification alone is not a substitute for finished pipe certification.
At the molecular level, the bimodal molecular weight distribution increases the high-molecular-weight fraction and tie-molecule density across the lamellar structure. This architecture improves slow crack growth resistance and rapid crack propagation arrest. ISO 13479 notched pipe testing is used to evaluate slow crack growth; typical PE100-RT qualification runs use 80°C water and hoop stresses near 4.6 MPa, but the supplier datasheet should be consulted for exact durations because published data for this specific configuration are limited. Rapid crack propagation resistance is assessed by ISO 13477; the material must arrest a fast-moving crack at 0°C and at a critical pressure above the designated pipe design pressure. In production practice, the black compound contains 2.0–2.5 wt% carbon black to provide ultraviolet weathering stability during outdoor storage and service. Dispersion quality is assessed by ISO 18553; poor dispersion leads to agglomerates that reduce pressure resistance and create local crack initiation sites in the pipe wall.
Minimum required strength is defined as the lower prediction limit at 50 years rounded down to the next lower standard class. A PE100 material has an MRS of 10 MPa. The design stress is the MRS divided by the design coefficient. For water applications, ISO 4427-1 uses a design coefficient of 1.25, giving a design stress of 8 MPa at 20°C. At elevated temperatures, design stress must be reduced using a service temperature derating factor. The value of the RT grade is that the derating at 60°C is less severe than for standard PE100; however, the exact derating factor is pipe-system-specific and must be confirmed against the relevant pipe standard.
Typical values from supplier technical literature are summarised below. These are not purchase specifications; batch-to-batch variation must be controlled by incoming inspection against an agreed specification and by the finished pipe qualification.
| Property | Method and condition | Typical value |
|---|---|---|
| Density | ISO 1183-1 | 0.959 g/cm³ |
| Melt mass-flow rate | ISO 1133-1, 190°C/5 kg | 0.25 g/10 min |
| Tensile stress at yield | ISO 527-2 | 25 MPa |
| Elongation at break | ISO 527-2 | >600% |
| Flexural modulus | ISO 178 | 1000 MPa |
| Charpy notched impact strength | ISO 179-1/1eA, 23°C | 14 kJ/m² |
| Charpy notched impact strength | ISO 179-1/1eA, -30°C | 8 kJ/m² |
| Carbon black content | ISO 6964 | 2.0–2.5 wt% |
| Oxidative induction time | ISO 11357-6, 210°C | >20 min |
On production-scale pipe extrusion, HE3466-RT is processed on grooved-feed single-screw extruders with screw lengths between 30:1 and 33:1 L/D. Barrel profiles are normally set from a feed-zone temperature of 40–60°C, through a compression zone at 180–200°C, to a metering section and adaptor at 200–220°C. Melt temperature at the die entry is held below 230°C to limit thermo-oxidative chain scission. A barrel profile that falls below 180°C in the compression zone reduces homogenisation of the high-molecular-weight fraction and can produce sharkskin on the outer pipe surface or internal weld-line porosity at the spider legs. Screen packs of 40/60/80 mesh are commonly used to raise back pressure and remove carbon black agglomerates; screen pressure must remain within the extruder manufacturer’s limit. Pellet pre-drying is not required for hygroscopic moisture absorption, but condensation on cold pellets stored below plant dew point can create steam marks. In such cases, an 80°C hot-air hopper dryer for 2 h is applied before extrusion, particularly when plant relative humidity exceeds 60%.
Substitution onto an existing standard PE100 extrusion line is not automatically drop-in. The high-molecular-weight fraction of the bimodal melt increases low-shear viscosity, which can raise die-head pressure and reduce melt flow uniformity in lines with insufficient L/D. Extruders below 25:1 L/D may not provide enough residence time to homogenise the melt; the result is unstable melt pressure downstream of the breaker plate, wall-thickness transients, and periodic melt fracture at the die lip. Melt pump suction pressure is controlled within pump manufacturer’s limits, commonly 30–80 bar; values below 20 bar can cause output surging. Vacuum sizing tanks should maintain cooling water at 25–35°C for thick-walled pipe. Quenching below 15°C freezes the outer surface before the inner wall has densified and can increase residual stress. Pipe calibration sleeves may need adjustment because the melt exhibits less draw-down and higher die swell than lower-viscosity PE100 grades. Operators sometimes compensate by raising melt temperature, but this is unsafe for long-term stabiliser retention. The correct response is to adjust screw speed, cooler barrel set-points, or haul-off ratio while holding melt temperature below 230°C. Compared with standard PE100 black grades, HE3466-RT may show nearly identical density and melt-flow rate; the difference becomes measurable only in elevated-temperature hydrostatic testing and in slow crack growth resistance after thermal aging.
Long-term performance is governed by both creep rupture and thermo-oxidative degradation. Above 60°C, the rate of oxygen uptake in the amorphous phase increases and the stabiliser package becomes the limiting variable. ISO 11357-6 oxidative induction time at 210°C is a quality-control indicator, but it does not directly predict service life in hot water. Hydrostatic tests at 80°C and 90°C are used to accelerate extraction and depletion of stabilisers; published data for this specific configuration are limited above 70°C. The stabiliser package is sacrificial, and extraction into hot water is thermally activated. Thick-walled pipes have a greater stabiliser reservoir but also higher thermal gradients during cooling, so surface and core stabiliser concentration may differ. The material should not be specified for continuous exposure to strong oxidisers, aromatic hydrocarbons, or chlorinated solvents. Stress cracking resistance can be reduced by polar surfactants, cutting fluids, and certain oilfield chemicals. In mining slurry lines, wall erosion and notched crack initiation at internal scratches depend on solids loading and particle size; hydrostatic ratings alone do not capture abrasive wear. The practical upper service limit for continuous water service is commonly held at 60°C unless the pipe system design is supported by material-specific regression curves and hydrostatic testing at the application temperature.