| HS Code | 884309 |
| Tensile Strain At Break Percent | >600 |
| Oxidation Induction Time 200c Min | >20 |
| Moisture Content Percent | <0.02 |
| Pe Classification | PE100-RC |
As an accredited Borealis HDPE HE3498-LS-H factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE HE3498-LS-H is supplied in 25 kg polyethylene bags; 55 bags per pallet, totaling 1,375 kg. |
| Container Loading (20′ FCL) | 20′ FCL container loading for Borealis HDPE HE3498-LS-H: palletized 25 kg bags, shrink-wrapped, strapped, and secured for safe ocean transport. |
| Shipping | Borealis HDPE HE3498-LS-H is shipped as non-hazardous polyethylene pellets, typically in 25 kg PE bags on pallets, octabins, or bulk trucks/containers. Transport at ambient temperature. Keep packaging dry, closed, and protected from heat, sunlight, and moisture. Avoid puncturing bags; no special dangerous-goods classification applies. Follow local transport regulations and workplace safety rules. |
| Storage | Store Borealis HDPE HE3498-LS-H in original, sealed packaging in a cool, dry, well-ventilated indoor area. Keep away from direct sunlight, heat, flames, moisture, oils, and strong chemicals. Palletize off the floor, avoid crushing, and maintain moderate temperatures. Prevent contamination and prolonged UV exposure to preserve resin properties. Follow local regulations and the supplier’s safety data sheet. |
| Shelf Life | Shelf life: Store dry, below 50°C, away from UV; approximately two years under recommended conditions in unopened original packaging. |
HE3498-LS-H is a bimodal PE100 high-density polyethylene with a nominal density of 0.959 g/cm³ according to ISO 1183-1 and an MFR of 0.23 g/10 min at 190 °C under 5 kg load according to ISO 1133-1:2022. Municipal pressure pipes manufactured from this compound fall under EN 12201-2 and ISO 4427-2, with the PE100 classification derived from long-term hydrostatic testing to ISO 9080 and ISO 12162 at an MRS of 10 MPa. In chlorinated potable water service, chlorine-based disinfectants oxidize the inner wall and create surface-initiated slow crack growth at flow-line discontinuities, weld beads, or field scratches; therefore the controlling material boundary is not minimum required strength alone but stress crack growth resistance under ISO 13479 notched pipe test conditions. The compound is supplied as a ready-to-use black compound with furnace carbon black content between 2.0 wt% and 2.5 wt%, eliminating the need for separate carbon black masterbatch addition. Extrusion is performed on a single-screw extruder with grooved feed section and L/D 30:1 or 36:1, with barrel temperatures between 180 °C and 210 °C and melt temperature held at 200–220 °C; back pressure ahead of the screen pack should remain below 250 bar to limit shear-induced molecular scission. The pipe is vacuum-sized and cooled through closed-loop tanks set at 40 °C, 30 °C, and 20 °C to control residual frozen-in stress. Clean in-house regrind from the same HE3498-LS-H production campaign may be reintroduced up to 10 % by mass under EN 12201-2, but national drinking water approval conditions in some jurisdictions reduce this to 0 % for product in direct contact with potable water. Terminal products include straight lengths and coils for urban water transmission, joined in the field by butt fusion according to ISO 21307 low-pressure single hot plate procedure or by electrofusion couplers according to ISO 12176-2.
Natural gas distribution networks impose a low-temperature brittle fracture criterion that water-only pressure standards do not fully capture. Pipes extruded from HE3498-LS-H for gas service are specified under EN 1555-2 and ISO 4437-2; in this application the limiting long-term risk is rapid crack propagation, which is evaluated by the ISO 13477 S4 full-scale test at low temperature and critical pressure above the operating envelope. The gas design coefficient of 2.0 lowers the maximum design stress to 5.0 MPa for the same MRS 10 MPa material, reducing allowable pressure at 20 °C for SDR 11 to 1.0 MPa and for SDR 17 to 0.625 MPa. Processing for gas pipe prioritizes retention of the high-molecular-weight fraction; therefore melt temperature is kept in the lower band of 190 °C to 205 °C, and screw speed is adjusted to keep melt residence time below 10 min at full throughput. The compound does not require drying under relative humidity below 60 %, but condensate on pellets moved from cold storage into a warm production hall is removed by drying at 80 °C for 4 h before the feed hopper. Pipe is extruded in diameters up to 630 mm with wall-thickness control by ultrasonic gauge; clean gas-pipe production scrap from the same formulation is limited to 10 % by mass under EN 1555-2. Butt fusion joints are made with a single hot plate at 220 °C ± 10 °C, bead-up pressure of 150–200 kPa, and cooling under pressure for 10 min per 25 mm wall thickness; electrofusion joints follow the time and voltage input printed on each fitting. Terminal products are buried gas mains and service lines, supplied as 6 m or 12 m straight lengths for larger diameters and as coils up to 125 mm outside diameter for rural distribution.
In mining and dredging applications, the pipe is not governed by potable water approval but by the combined effects of internal slurry abrasion, external rock impingement, and sustained hydrostatic load. HE3498-LS-H is extruded into thick-wall pressure pipe with SDR 9 or SDR 7.4 dimensions, using the hydrostatic design basis of ISO 4427-2 as the dimensional reference while fluid compatibility is assessed separately against the specific tailings chemistry. The processing challenge shifts from melt output to solidification control: a thick-wall section cools non-uniformly from the outer surface inward, and void formation in the core can act as a slow crack growth initiation site. To suppress core voids, the extrusion line uses a grooved feed extruder with L/D 36:1, melt temperature at 190–200 °C, and cooling tanks programmed in gradual steps from 40 °C to 20 °C rather than a single quench. Clean in-house regrind is restricted to 10 % by mass and only from thick-wall pipe produced in the same extrusion campaign; no external recycled polyethylene should be blended into pressure-bearing layers. Where mine dewatering water temperature exceeds 40 °C, the maximum allowable operating pressure is multiplied by the ISO 4427 derating coefficient, reducing the pressure rating to approximately 0.74 of the 20 °C value at 40 °C. Terminal products are tailings transfer lines, dredge discharge segments, and mine dewatering mains. Abrasive service life under specific slurry geometries is not defined by the pipe pressure standard alone; published data for HE3498-LS-H under tailings slurry wear is limited, so plant-specific wear-loop trials remain mandatory for reliable service life prediction.
Buried wastewater rising mains manufactured from HE3498-LS-H are cyclic-pressure pipelines rather than constant-pressure water lines. The controlling product standard remains EN 12201-2 or ISO 4427-2, but the design must include surge allowance because pump start-stop sequences generate transient pressure peaks that can exceed nominal pressure by 50 % if air valves are undersized. In these pipes, slow crack growth at electrofusion socket inlet geometries and butt fusion bead roots is the principal failure mechanism, which is why notch-resistant bimodal HDPE is selected over lower slow crack growth resistance materials. Processing for sewage force mains uses the same 220 °C ± 10 °C single hot plate fusion procedure according to ISO 21307, with extended heating times for wall thicknesses above 20 mm; electrofusion couplers are installed only after scraping 0.1–0.3 mm of oxidized surface from the pipe. The pipe is extruded in SDR 17 and SDR 13.6 dimensions, with the former rated at 1.0 MPa and the latter at 1.27 MPa at 20 °C using a design stress of 8.0 MPa. No separate black masterbatch is added because the compound is already stabilized with carbon black in the 2.0–2.5 wt% range. Terminal products include buried force mains between sewage pumping stations and treatment plants, supplied as butt-fused strings that are pulled into the trench after welding.
In agricultural irrigation networks, HE3498-LS-H is processed into large-diameter trunk mains subjected to intermittent pump operation and rapid valve closure. Surge absorption from PE100 viscoelastic response reduces but does not eliminate the need for air-release and vacuum-break valves; design practice commonly adds a surge allowance of 1.5 times nominal pressure unless transient analysis provides a lower value. The extrusion process for 315–630 mm outside diameter pipe uses a barrier screw with grooved feed and a gear pump to stabilize melt output, with barrel set points from 180 °C to 210 °C and melt temperature at 210 °C. Above-ground sections do not require additional UV stabilizer because the compound’s carbon black content of 2.0–2.5 wt% provides weathering resistance. Pipe dimensions for irrigation laterals are typically SDR 17 or SDR 26, giving nominal pressure ratings of 1.0 MPa and 0.64 MPa at 20 °C, respectively, at a design stress of 8.0 MPa; mainlines and pump discharge headers are commonly SDR 11 at 1.6 MPa. Clean rework from the same production campaign may be reintroduced at up to 10 % by mass, but water quality restrictions for fertigation systems may require 0 % rework where concentrated fertilizer salts and chlorine flushes are expected. Terminal products are buried mains for drip irrigation blocks, center-pivot supply lines, and seasonal surface headers that are butt-fusion joined to minimize joint leakage.
For rehabilitation of deteriorating cast-iron or asbestos-cement pressure mains, HE3498-LS-H is extruded into smooth-wall PE100 strings that are butt-fused into continuous lengths and inserted by close-fit sliplining or pipe bursting. The applicable installation standard is ISO 11298-2, which governs the use of polyethylene pipes for renovation of water supply networks; the pipe material itself still satisfies EN 12201-2 or ISO 4427-2. In this configuration, longitudinal bending and axial tensile load during insertion are the immediate processing concerns after pipe manufacture, not hydrostatic stress alone. The pipe is supplied in reduced outside-diameter designs such as SDR 17 or SDR 26 to preserve hydraulic capacity after insertion into the host pipe; tensile pull-in force is limited by the manufacturer’s allowable pulling stress, which is derived from the material’s yield stress and the joint fusion quality. Butt-fusion joints are made according to ISO 21307, and each joint is visually inspected for double bead geometry outside the pipe. The extruder setup for this application uses a vacuum calibrated sizing sleeve with diameter tolerance below 0.3 % of nominal outside diameter to maintain insertion clearance between the PE pipe and host pipe wall. Terminal products are close-fit rehabilitation strings pulled through existing water or sewer corridors without complete excavation.
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Borealis HE3498-LS-H is manufactured as a bimodal, black high-density polyethylene pipe compound in which the molar mass distribution contains a controlled high-molar-mass fraction for slow crack growth resistance and a lower-molar-mass fraction for extrusion output. The grade is classified as PE100-RC under ISO 12162 and has a minimum required strength of 10.0 MPa derived from long-term hydrostatic testing according to ISO 9080. The material is supplied as a ready-to-extrude compound with carbon black at 2.0–2.5% by mass for ultraviolet stabilisation and an antioxidant/acid-neutraliser package. It is intended for solid-wall pressure pipe in drinking water, wastewater, industrial fluid transport, and for non-conventional installation methods including sandless trench installation, horizontal directional drilling, pipe bursting, and relining. The low-sag designation separates it from general-purpose PE100 and from PE100-RC grades that do not resist molten-wall creep during large-diameter thick-wall extrusion.
The compound is characterised by the following typical property set. The melt flow rate is determined at 190 °C under a 5 kg load, not the 2.16 kg condition used for injection-moulding grades; the 0.23 g/10 min value is therefore an extrusion-grade rheology indicator and should not be compared directly with standard melt index data.
| Property | Test method | Typical value |
|---|---|---|
| Density at 23 °C | ISO 1183-1 | 0.959 g/cm³ |
| Melt flow rate, 190 °C/5 kg | ISO 1133-1 | 0.23 g/10 min |
| Tensile stress at yield | ISO 527-2 | 25 MPa |
| Tensile strain at break | ISO 527-2 | >600% |
| Flexural modulus | ISO 178 | 1000 MPa |
| Carbon black content | ISO 6964 | 2.0–2.5% |
| Oxidation induction time, 210 °C | ISO 11357-6 | >20 min |
The 0.959 g/cm³ compound density reflects the base polyethylene density plus the 2.0–2.5% carbon black content determined by ISO 6964. Carbon black dispersion is controlled to meet ISO 18553 because agglomerates in pipe-grade HDPE can act as stress concentrators in slow crack growth. The oxidation induction time above 20 min at 210 °C under ISO 11357-6 indicates that the primary hindered phenolic antioxidant remains active after normal extrusion heat history. The tensile yield stress of 25 MPa and flexural modulus of 1000 MPa place the material in the upper stiffness range for PE100 pipe compounds. The melt flow rate condition is selected because the 2.16 kg load used for low-viscosity injection-moulding grades does not produce a measurable, repeatable flow value in this high-molecular-mass pipe extrusion compound.
In large-diameter pipe extrusion, gravitational sag acts on the unsupported melt between the die exit and the calibration sleeve. At pipe diameters above DN800 and wall thicknesses above 45 mm, the body force on the molten tube can produce wall-thickness thinning at the 12 o’clock position and thickening at the 6 o’clock position before cooling water solidifies the outer surface. Conventional PE100 compounds with lower melt strength require continuous die-centring compensation and sometimes reduced output to keep wall-thickness variation within the tolerance bands of ISO 4427-2 or EN 12201-2.
The low-sag response of HE3498-LS-H is achieved by tailoring the high-molar-mass tail of the bimodal distribution, which increases zero-shear viscosity and extensional melt strength without proportionally increasing screw torque. On production-scale grooved-barrel single-screw extruders with L/D ratios of 30:1 to 37:1 producing DN1000 SDR 17 solid-wall pipe, ultrasonic wall-thickness gauges at the cooling section record smaller 6 o’clock/12 o’clock deviations than with conventional PE100 at the same melt temperature and line speed. The effect is less significant below DN315, where the melt plug is shorter and the ratio of gravitational force to melt stiffness is lower. The low-sag property is not a standard ASTM or ISO material classification parameter; it is verified in production by direct wall-thickness mapping on large-diameter pipe at line speeds between 0.5 m/min and 1.5 m/min.
On production-scale grooved-barrel single-screw extruders with L/D ratios of 30:1 to 37:1 and barrier mixing sections, HE3498-LS-H is processed at measured melt temperatures between 200 °C and 230 °C. Barrel set points are ramped from 180 °C in the feed zone to 220 °C in the metering zone, with adapter and die temperatures held 5–10 K below the metering set point to control die swell and maintain pipe ovality. Pre-drying is normally unnecessary because the polyethylene backbone does not hydrolyse; if ambient relative humidity exceeds 60% or rain-wetted regrind is used, a hopper dryer set at 80 °C for 2–3 h removes surface moisture before melt feeding. Melt temperature should not exceed 240 °C: extended residence time above this threshold depletes the hindered phenolic antioxidant, raises the carbonyl index, and can reduce long-term hydrostatic strength. Extruder head pressure is die-dependent, but gear-pump-assisted lines typically operate with stable melt pressure and use infrared melt-temperature monitoring at the adapter to detect shear heating before degradation begins.
Dispersive mixing is still required because the pelletised compound contains a carbon black masterbatch component. Screen packs of 40/60/40 mesh are commonly installed to trap carbon black agglomerates and foreign particles; a pressure rise across the breaker plate above 50 bar indicates progressive screen blinding and requires replacement. Extruder screw speed and output are limited not only by melt viscosity but also by heat removal in the calibration and cooling tanks. Cooling water temperatures in the first vacuum calibration zone are normally maintained between 10 °C and 20 °C to freeze the pipe surface rapidly and preserve the dimensions set by the calibration sleeve. Twin-screw extruders are not required for melt mixing because the material is already compounded; additional melt residence time contributes to oxidative degradation without improving dispersion.
PE100-RC materials are specified when pipe is installed with reduced sand embedment, with direct backfill of excavated soil containing stones, or with surface scoring from pipe-bursting and horizontal directional drilling. The critical performance parameter is slow crack growth from surface defects. In notched-pipe testing according to ISO 13479, PE100-RC compounds are required to withstand ≥ 8760 h at 4.0 MPa and 80 °C; conventional PE100 grades may satisfy the lower notched-pipe requirement but are not required to reach this PE100-RC threshold. Rapid crack propagation resistance is assessed separately by the S4 test under ISO 13477; published critical pressure values are installation-specific and should be obtained from the pipe manufacturer’s S4 test report for the relevant wall thickness and temperature.
| Feature | Conventional PE100 | HE3498-LS-H | Basis |
|---|---|---|---|
| Long-term hydrostatic strength | MRS 10.0 MPa | MRS 10.0 MPa | ISO 9080 / ISO 12162 |
| Slow crack growth from notches | Standard PE100 requirement | ≥ 8760 h at 4.0 MPa and 80 °C | ISO 13479 |
| Rapid crack propagation resistance | Assessed by S4 | Assessed by S4, enhanced for PE100-RC | ISO 13477 |
| Low-sag extrusion | Moderate | High | Gravitational sag measurement on large-diameter pipe |
| Typical installation envelope | Open trench with compacted bedding | Sandless trench, HDD, pipe bursting, relining | EN 12201-2, ISO 11298 |
The combination of PE100-RC slow crack growth resistance and low-sag extrusion behaviour separates HE3498-LS-H from conventional PE100 and from low-sag PE100 grades that do not carry the RC designation. Substitution on the basis of density or melt flow rate alone is not sufficient because the bimodal molar mass distribution and stabiliser package control field performance under point loads and scratches. Compared with PE80 pipe compounds, the 10.0 MPa minimum required strength allows thinner walls at the same nominal pressure or higher pressure ratings at the same standard dimension ratio when the design coefficient C=1.25 from ISO 12162 is applied. Chemical compatibility remains bounded: continuous exposure to strong oxidising acids, aromatic hydrocarbons, or chlorinated solvents at elevated temperature can reduce service life, and chemical resistance should be checked against ISO/TR 10358 or the pipe manufacturer’s chemical resistance tables. Pressure ratings are referenced at 20 °C; service at higher temperatures requires derating according to ISO 13760. The grade is not intended for high-temperature service above the normal HDPE pressure-pipe limit, and regrind streams must be kept free of polypropylene or PVC contamination because melting-point mismatch creates unmelted domains and reduces butt-fusion weld strength.
Butt-fusion and electrofusion welding of HE3498-LS-H pipe should be qualified under ISO 21307. The high molecular mass of the compound can widen the melt bead and increase squeeze-out during butt fusion if interfacial pressure is not controlled within the specified range. Joint cooling times are longer than for lower-viscosity PE80 because the bimodal high-molar-mass fraction retards melt relaxation. Batch-to-batch variance in carbon black content is normally monitored by ashing under ISO 6964; melt flow rate checks under ISO 1133-1 at 190 °C/5 kg are used to detect molar mass drift before extrusion. Published data for this specific configuration is limited where field installation involves chemically aggressive soils, and site-specific testing under ISO/TR 10358 is recommended before use in such environments.