| HS Code | 505181 |
| Productname | Borealis HDPE HE3490-LS-HW |
| Materialtype | High-density polyethylene |
| Polymerclassification | PE100 |
| Minimumrequiredstrength | 10 MPa |
| Density | 959 kg/m³ |
| Meltflowrate 190c 5kg | 0.25 g/10 min |
| Carbonblackcontent | 2.0-2.5% |
| Tensilestressatyield | 25 MPa |
| Tensilestrainatbreak | >600% |
| Flexuralmodulus | 1100 MPa |
| Charpynotchedimpactstrength 23c | 15 kJ/m² |
| Hardnessshored | 62 |
| Vicatsofteningtemperature | 125 °C |
| Oxidationinductiontime 200c | >20 min |
| Moisturecontent | <0.02% |
| Color | Black |
| Form | Pellets |
| Processingmethod | Extrusion |
| Uvstabilization | Yes |
As an accredited Borealis HDPE HE3490-LS-HW factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE HE3490-LS-HW is typically supplied in 25 kg polyethylene bags, 55 bags per pallet (1,375 kg). |
| Container Loading (20′ FCL) | 20′ FCL container floor-loaded with 25 kg bags of Borealis HDPE HE3490-LS-HW, approximately 22 MT net, securely stowed for transport. |
| Shipping | Borealis HDPE HE3490-LS-HW ships as non-hazardous polyethylene pellets, typically in 25 kg bags, octabins, or bulk. Transport in clean, dry containers or trucks at moderate temperatures. Protect from moisture, direct sunlight, heat, and contamination. No dangerous goods classification or special documentation is normally required. |
| Storage | Store Borealis HDPE HE3490-LS-HW in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep in original, sealed packaging on pallets to prevent moisture, dust, and contamination. Avoid excessive stacking and prolonged UV exposure. Separate from incompatible chemicals and follow the supplier’s safety data sheet and local regulations. Use first-in, first-out stock rotation. |
| Shelf Life | Store unopened in a dry, cool, ventilated area away from sunlight; typical shelf life is 12–24 months, subject to manufacturer’s recommendations. |
In municipal potable water transmission, the conversion of Borealis HDPE HE3490-LS-HW into pressure-rated pipe is governed by hydrostatic design life rather than short-term tensile properties. The compound is processed as the sole pressure-bearing layer at 100 wt%; no additional carbon black masterbatch is required because the grade already contains carbon black at 2.0–2.5 wt% when measured according to ISO 6964, and dispersion is controlled to ISO 18553. Closed-loop regrind of clean, unweathered pipe produced from the same compound is limited to 10 wt% of total extrudate and must be isolated from other PE grades because foreign contamination can reduce slow crack growth resistance under ISO 13479. Extrusion is performed on grooved-feed single-screw machines with L/D ratios of 30:1 to 36:1, barrel temperatures between 180 °C and 210 °C, die temperatures between 190 °C and 220 °C, and melt temperature held below 230 °C; above 230 °C thermo-oxidative chain scission shifts the ISO 9080 regression line, while below 170 °C the high molecular weight fraction raises melt pressure and can generate melt fracture in narrow spiral mandrel dies. Vacuum calibration and segmented spray cooling are followed by post-cooling temperature equilibration for wall thicknesses above 25 mm to reduce ovality and frozen-in stress. Batch-to-batch variance in melt flow rate is observable as drifting die-head pressure on grooved-feed extruders, and closed-loop thermal control of the feed throat reduces wall-thickness eccentricity. Material classification rests on ISO 9080 and ISO 12162 with an MRS of 10 MPa, and pipe system compliance is evaluated under ISO 4427-1, ISO 4427-2, EN 12201-1, EN 12201-2, and NSF/ANSI/CAN 61; rapid crack propagation resistance is confirmed by ISO 13477 and slow crack growth resistance by ISO 13479. Terminal products comprise PE100 potable water mains and distribution pipes from DN 20 to DN 1200 in SDRs of 7.4, 9, 11, 13.6, 17, 21, 26, and 33, with pressure ratings from 4 bar to 25 bar at 20 °C after a design coefficient of 1.25; any service above 20 °C requires derating factors from ISO 13760.
For natural gas distribution, the governing failure mode is not slow crack growth alone; a running crack can propagate along the pipe at speeds faster than decompression, and therefore resistance to rapid crack propagation is evaluated under ISO 13477 at low temperature. The compound is extruded as the pressure-bearing wall at 100 wt% virgin material; in-plant regrind is generally excluded from gas pipe pressure walls because traceability and contamination control requirements in ISO 4437-2-based quality plans are stricter than those for water pipe. Co-extruded yellow identification stripes, where required by national gas distribution codes, are made from a compatible PE100 compound and occupy only a small external sector of the pipe; the stripe layer is not included in the calculated minimum wall thickness. Processing uses grooved-feed single-screw extruders with L/D 33:1 to 36:1, melt temperatures from 200 °C to 230 °C, spiral mandrel dies, vacuum calibration, and either coiling for diameters up to 110 mm or straight-length cutting for larger diameters. Compliance for the pipe system is established under ISO 4437-1, ISO 4437-2, EN 1555-1, and EN 1555-2; material performance is verified through ISO 9080, ISO 12162, ISO 13479 for slow crack growth, and ISO 13477 for rapid crack propagation. Terminal products are PE100 gas distribution mains from DN 20 to DN 630, typically in SDR 11 and SDR 17, supplied as coils or straight lengths and used for natural gas and compatible gaseous fuel networks after national approvals. Operational pressure limits are not selected from the water-pipe pressure rating table; gas-specific MOP values are determined by ISO 4437-5 or EN 1555-5 using the applicable design coefficient, and PE100 gas systems generally operate at MOP up to 10 bar.
In mining tailings and abrasive slurry transport, PE100 pressure pipe must withstand sustained hydrostatic stress, external point loads from rocky backfill, and internal slurry velocities that remove the pipe wall over time. The compound is used at 100 wt% for homogeneous thick-wall pipe; no abrasion-resistant inner liner or additional carbon black masterbatch is required, but an intentionally thicker wall is specified using a conservative design coefficient and an abrasion allowance. Extrusion of thick-wall pipe uses high-torque single-screw machines with L/D up to 36:1, controlled low-shear screw geometries, melt temperatures between 190 °C and 220 °C, and extended vacuum calibration with multi-zone spray cooling. Wall thicknesses above 60 mm require in-line post-cooling temperature equilibration because the outer surface freezes before the core, creating residual stresses that can accelerate slow crack growth under long-term internal pressure. Pipe system compliance for industrial applications is anchored to ISO 15494; material design basis is established by ISO 9080 and ISO 12162, while slow crack growth resistance is verified by ISO 13479. Terminal products include PE100 tailings lines, slurry transfer lines, and process water mains from DN 110 to DN 1600 in SDR 9 through SDR 41, with pressure ratings at 20 °C from 4 bar to 25 bar before derating for elevated temperature or abrasive service.
Pressure sewer and wastewater force main service differs from water distribution because the pipe sees intermittent flow, hydrogen sulphide, chlorinated disinfectants, and surge pressures from pump start-stop cycles. The compound is used at 100 wt% for the pipe wall, and clean in-plant regrind from the same compound is limited to 10 wt% when permitted by the system quality plan; no additional antioxidant masterbatch or carbon black concentrate is added because the grade is fully formulated. Pipe production is carried out on conventional PE100 pipe extrusion lines with grooved feed sections, L/D 30:1 to 36:1, melt temperatures 200–220 °C, and vacuum sizing; downstream, fabricated spools and fittings are joined by butt fusion at a melt bead temperature in the range 200–220 °C using alignment clamps that control bead-up pressure and joining force. Compliance for pressure sewer pipe is evaluated under ISO 4427-2, EN 12201-2, and ASTM F714; long-term hydrostatic strength is validated by ISO 9080 and slow crack growth by ISO 13479. Terminal products are PE100 sewage force mains and rising mains from DN 110 to DN 800, commonly in SDR 17, 21, and 26, supplied in straight lengths or butt-fused strings and installed by trenchless or open-cut methods.
Large-diameter irrigation supply lines in arid agricultural regions are extruded from the compound at 100 wt% without additional UV stabilizer masterbatch because the carbon black formulation provides long-term weathering resistance; pipe compliance is evaluated under ISO 8772 and ISO 4427-2, while material classification follows ISO 9080 and ISO 12162 at an MRS of 10 MPa. Production uses conventional vacuum-calibrated PE100 pipe extrusion lines with L/D 30:1 to 36:1, melt temperatures between 190 °C and 220 °C, and coiling for diameters up to 110 mm; larger diameters are cut into straight lengths. Terminal products include PE100 irrigation mainlines and submains from DN 50 to DN 500, typically SDR 17 through SDR 26, with pressure ratings from 6 bar to 10 bar at 20 °C.
Submerged marine outfalls, desalination intakes, and power plant cooling water pipelines fabricated from the compound are joined on shore into long strings before controlled sinking because continuous bead-to-bead fusion reduces the number of underwater joints. The compound is used at 100 wt% as the pressure-bearing wall; no additional carbon black masterbatch or weathering additive is required, and concrete ballast collars are attached externally without reducing the pressure wall. Pipe production uses PE100 extrusion lines with grooved feed, L/D 30:1 to 36:1, melt temperatures 200–220 °C, and vacuum sizing; for diameters above 800 mm, wall-thickness control and ovality monitoring are critical because out-of-roundness affects butt-fusion alignment and tow stress. Mechanical joining by butt fusion is performed with automated fusion machines that record joining pressure, heating time, and pipe drag resistance in compliance with ISO 21307. Pipe system compliance is evaluated under ISO 4427-2, EN 12201-2, and ASTM F714; material classification uses ISO 9080 and ISO 12162, and slow crack growth resistance is verified by ISO 13479. Terminal products include PE100 intake and outfall pipelines from DN 315 to DN 1600, SDR 13.6, 17, 21, and 26, and diffuser sections with marine-grade ballast and anchor assemblies.
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Borealis BorSafe HE3490-LS-HW is a black bimodal high-density polyethylene pipe extrusion compound classified within the PE100 hydrostatic design category. The grade is supplied as ready-to-extrude pellets with carbon black and stabilizer additives already dispersed in the polymer matrix. The LS-HW suffix denotes a low-sag melt response combined with improved weldability relative to standard PE100 pipe grades; however, the commercial suffix is not itself a recognized classification and must be read alongside the manufacturer’s release specification and the applicable pipe-system standards. Primary usage includes pressure piping for potable water, wastewater force mains, irrigation networks, and industrial aqueous transfer, with pipe dimensions and operating limits governed by ISO 4427-1, ISO 4427-2, and national installation codes. The material is not formulated for thin-wall injection moulding or film extrusion.
In hydrostatic design, HE3490-LS-HW is assigned a minimum required strength of 10.0 MPa at 20 °C for 50 years according to ISO 9080. This places the product in the PE100 class under ISO 12162. The distinction from PE80 is quantitative: PE80 carries an MRS of 8.0 MPa, so at equal service factors the PE100 grade can achieve an allowable design stress of 8.0 MPa rather than 6.3 MPa. That increase permits thinner walls for a given nominal pressure rating and can lower material consumption per linear metre of pipe. The same strength increase, however, requires tighter thermal control during extrusion because the high-molecular-weight fractions responsible for long-term strength also raise melt viscosity and reduce flow.
Standard PE100 pipe grades may exhibit satisfactory tensile and hydrostatic properties while still sagging during thick-wall extrusion. HE3490-LS-HW is formulated with a controlled broadening of the molecular weight distribution and a high-molecular-weight tail. This molecular architecture increases melt elasticity and die swell without proportionally increasing shear viscosity. On production-scale grooved-feed single-screw extruders with screw diameters of 90–120 mm and 30:1 to 36:1 L/D, the practical effect is a wider operating window for wall thicknesses above 80 mm. The melt remains geometrically stable between the die and calibration sleeve, reducing gravitational wall thinning compared with standard PE100 lots of equivalent melt flow rate.
Weldability of the high-weldability variant is verified through butt fusion welding according to ISO 21307 and electrofusion welding according to ISO 12176-1. The grade is also positioned for slow crack growth resistance; PE100-RC-type assessments use notched pipe testing based on ISO 13479 and rapid crack propagation testing based on ISO 13477. The LS-HW designation should not be interpreted as automatic certification to every national PE100-RC scheme. Third-party listing and pipe-manufacturer qualification remain the controlling evidence for installation without sand bedding or for aggressive trenchless techniques.
Low-sag behaviour is not solely a function of melt flow rate. It is evaluated by measuring sag of a freely extruded parison or by monitoring wall-thickness eccentricity in the calibration section. The melt strength of a low-sag PE100 may show die swell values 15–25% greater than a reference PE100 under identical shear conditions. This higher die swell requires slightly larger calibration sleeves or reduced haul-off tension. If haul-off tension is too high, the pipe diameter can be drawn below tolerance even though the melt is thermally stable. Conversely, insufficient tension can produce irregular wall thickness as the pipe enters the vacuum tank.
Extrusion processing is typically performed with barrel temperatures from 180 °C to 220 °C and a die-head setpoint of 210 °C to 225 °C. The melt temperature must remain below 230 °C; excursions above that limit can reduce oxidation induction time and create gel defects on the inner wall. Below 190 °C, the high-molecular-weight fraction may not homogenize fully, causing surface roughness or carbon black agglomeration. The resulting process window is therefore narrower than for many general-purpose HDPE grades.
On a 120 mm grooved-feed single-screw extruder running DN 315 SDR 11 pipe, line rates are commonly reported between 400 kg/h and 600 kg/h. The exact rate depends on screw design, die-head pressure, and calibration length. A recurrent failure mode observed on manufacturing lines is an undulating inner wall when the first vacuum tank water temperature falls below 15 °C. Raising the first cooling-zone water temperature to 25–30 °C often restores smooth internal geometry. Inadequate cooling at high line speeds can produce sag and eccentricity even with a low-sag grade, so ultrasonic wall-thickness gauges are used to maintain die centring and minimum wall thickness.
Batch-to-batch melt flow rate variation should be monitored with an online rheometer or by sampling every 4 h according to ISO 1133-1:2022. Variations exceeding ±15% from the reference lot may require adjustment of screw speed or barrel profile. Quality control on incoming lots should include density, melt flow rate, carbon black dispersion, and oxidative stability. Carbon black dispersion is assessed by ISO 18553, and a significant change in oxidation induction time below 15 min may indicate stabilizer under-dosage or thermal abuse during compounding and should lead to quarantine.
The following table lists typical physical and mechanical values published for HE3490-LS-HW. The values are not batch-release limits; specification values must be obtained from the current supplier certificate because manufacturing tolerances and additive packages can shift within the approved range.
| Property | Test method | Typical value |
|---|---|---|
| Density | ISO 1183-1 | 0.959 g/cm³ |
| Melt mass-flow rate | ISO 1133-1:2022 at 190 °C/5.0 kg | 0.31 g/10 min |
| Tensile stress at yield | ISO 527-2/1A | 25 MPa |
| Tensile strain at break | ISO 527-2/1A | >600 % |
| Flexural modulus | ISO 178 | 1050 MPa |
| Charpy notched impact at -30 °C | ISO 179-1/1eA | 12 kJ/m² |
| Oxidation induction time at 210 °C | ISO 11357-6 | >20 min |
| Carbon black content | ISO 6964 | 2.0–2.5 % |
| Vicat softening temperature | ISO 306/A50 | 124 °C |
| Shore D hardness | ISO 868 | 62 |
Thermal conductivity is approximately 0.38 W/(m·K) at 23 °C when measured by transient plane source methods. Heat capacity and thermal diffusivity should be used in cooling-length calculations for thick-wall extrusion. The carbon black loading of 2.0–2.5% by mass provides long-term ultraviolet stabilization for above-ground temporary storage, but buried installation remains the intended service environment.
The primary use of HE3490-LS-HW is extruded pressure pipe produced to ISO 4427 dimensional series. Potable water pipes are typically installed as butt-fused strings with fusion parameters from ISO 21307. When local codes permit trenchless installation without sand bedding, slow crack growth resistance becomes the controlling material property. Point loads from stones and backfill can initiate cracks in lower-resistance PE100 grades but are better accommodated by PE100-RC-qualified materials. The product has been reported in large-diameter water mains; published data for extreme diameters is limited and should be confirmed through pipe-manufacturer qualification and third-party certification.
Compliance for pressure-pipe service is demonstrated through material classification, pipe testing, and installation jointing standards. The following table identifies the principal standards and verification functions associated with the grade when used in water piping systems.
| Standard or regulation | Designation | Role in pipe qualification |
|---|---|---|
| ISO 12162 | PE100 classification | Classifies material by minimum required strength |
| ISO 9080 | Hydrostatic strength | Long-term creep rupture and design basis |
| ISO 4427-1 | PE water pipe | Material, dimensions, and service conditions |
| EN 12201-1 | PE drinking-water pipe | European product standard for potable water systems |
| ISO 21307 | Butt fusion welding | Jointing procedure and qualification |
| ISO 13479 | Notched pipe test | Slow crack growth assessment |
| ISO 13477 | Rapid crack propagation test | Critical pressure and temperature resistance |
| EU Regulation No 10/2011 | Food-contact plastics | Relevant only if national potable approval is additionally granted |
The hoop stress for a thin-walled pipe under internal pressure is calculated as σ = P × (SDR − 1) / 2, where P is internal pressure, SDR is the ratio of outer diameter to wall thickness, and σ is wall stress. For PE100 with a design stress of 8.0 MPa derived from MRS 10.0 MPa and a service factor of 1.25, SDR 11 corresponds to a pressure rating of 16 bar at 20 °C for water. SDR 17 corresponds to 10 bar. These ratings fall as temperature increases; at 40 °C, the allowable design stress must be reduced using the derating factors given in the applicable pipe standard.
For pipe diameters above DN 500, the low-sag characteristic has a direct effect on wall-thickness tolerance. A standard PE100 melt may produce eccentricity of 2–3% in SDR 17 wall thickness after calibration, whereas a low-sag grade can hold the same within approximately 1% when cooling is optimized. Because hydrostatic resistance is governed by minimum wall thickness, improved concentricity translates into less material consumed to meet the same pressure rating. The relationship is not linear; at SDR 11, even a 1% reduction in minimum wall thickness can reduce the design margin by a measurable but code-compliant amount.
For no-dig installation, slow crack growth resistance is the differentiator. In pipe bursting and directional drilling, external scratches from rock or tooling can initiate cracks if the pipe is dragged under high tensile load. PE100-RC formulations are designed to resist crack propagation from such point loads. The notched pipe test of ISO 13479 uses a circumferential external notch and an elevated-temperature internal pressure; a PE100-RC material must exceed the standard PE100 threshold by a substantial margin. The exact threshold for HE3490-LS-HW must be taken from the certification body because national schemes differ in test stress and acceptance criteria.
Operational boundaries must be observed. The material should not be processed at melt temperatures above 230 °C or with prolonged hold-up at high temperature; oxidative degradation reduces long-term hydrostatic strength and can lower oxidation induction time below 20 min. Avoid contact with strong oxidizing agents, aromatic hydrocarbons, and chlorinated solvents because these media accelerate environmental stress cracking. Regrind use should be restricted to clean, unpigmented process scrap from the same grade, and its proportion in the blend should be validated by slow crack growth testing when national pipe standards require full notch-pipe re-qualification. Pipe sections stored outdoors for more than 12 months should be assessed for surface oxidation before butt fusion welding.