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Borealis HDPE HE3492-LS-H

    • Product Name: Borealis HDPE HE3492-LS-H
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 976950
    Density 959 kg/m³
    Melt Flow Rate 190 C 5 Kg 0.25 g/10 min
    Melt Flow Rate 190 C 21 6 Kg 7.0 g/10 min
    Oxidative Induction Time 200 C >20 min
    Carbon Black Content 2.3 %
    Moisture Content <0.02 %
    Mrs 10.0 MPa
    Pe Classification PE100
    Stress Crack Resistance Fnct >5000 h
    Notched Charpy Impact Strength 23 C 11 kJ/m²
    Notched Charpy Impact Strength 30 C 8 kJ/m²
    Tensile Stress At Yield 25 MPa
    Tensile Strain At Break >600 %
    Flexural Modulus 1100 MPa
    Vicat Softening Temperature 120 °C
    Melting Temperature 130 °C
    Thermal Conductivity 0.4 W/mK
    Specific Heat Capacity 1900 J/kgK
    Coefficient Of Linear Thermal Expansion 1.5E-4 /K
    Water Absorption <0.01 %
    Hardness Shore D 60
    Brittleness Temperature < -70 °C
    Bulk Density 550 kg/m³
    Color Black
    Form Pellets
    Odor Odorless

    As an accredited Borealis HDPE HE3492-LS-H factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Borealis HDPE HE3492-LS-H is supplied as pellets in 25 kg polyethylene bags, stacked on transport pallets.
    Container Loading (20′ FCL) 20′ FCL loaded with palletized 25 kg bags of Borealis HDPE HE3492-LS-H, shrink-wrapped and secured for safe ocean transport.
    Shipping Borealis HDPE HE3492-LS-H is shipped as non-hazardous polyethylene pellets in 25 kg PE bags, octabins, or bulk containers. Transport in clean, dry trucks, railcars, or containers. Keep away from moisture, direct sunlight, and excessive heat. Standard PPE recommended; avoid dust generation. No special dangerous goods classification required. Follow local regulations.
    Storage Store Borealis HDPE HE3492-LS-H in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and oxidizing agents. Keep original packaging sealed, clean, and palletized. Protect from moisture, dust, and prolonged UV exposure; avoid excessive stacking. Maintain ambient temperatures, ideally below 50°C. Use clean handling equipment and observe local regulations. Do not store near food, feed, or incompatible materials.
    Shelf Life Store unopened in original packaging, dry, cool, well-ventilated area; protect from direct sunlight and heat; shelf life typically 24 months.
    Application of Borealis HDPE HE3492-LS-H

    Extrusion of PE100 potable water mains from Borealis HDPE HE3492-LS-H begins with the recognition that the compound is supplied as a fully formulated black PE100 material, with carbon black already dispersed at 2.0–2.5 wt% in accordance with ISO 6964. In potable water service, the bore layer is therefore set at 100 wt% HE3492-LS-H; no additional carbon black masterbatch is introduced because any let-down alters the density, melt viscosity, and certified hydrostatic design basis established during grade qualification. Clean in-house regrind from the same production run may be reintroduced into the non-pressure-bearing outer cap or middle annular layer at up to 15 wt%, provided the regrind has been ground, dedusted, and passed through a 1.5 mm screen, and provided the final pipe lot still meets the hydrostatic strength requirements of ISO 1167 at 20 °C/100 h and 80 °C/165 h. Blue or black identification stripes are coextruded from a PE-carrier masterbatch at 4–6 wt% in the stripe layer only; the main pressure wall remains uncoloured. The certification envelope includes ISO 4427-2, EN 12201-2, and PE100 classification under ISO 12162 with a minimum required strength of 10 MPa. Where potable water contact approvals are required for export, the producer must verify the specific national migration certificate, such as DVGW W270, WRAS, KTW-BWGL, or NSF/ANSI 61, against the grade’s current listing, because these are certification-body documents rather than intrinsic resin properties.

    On the production floor, potable water pipe is extruded on a grooved-feed single-screw extruder with L/D 30:1 to 36:1 and a barrier screw designed for high-molecular-weight HDPE. Barrel set points run from 180 °C in the feed zone to 220 °C in the metering zone; die head and adapter zones are maintained at 200–225 °C, while melt temperature measured at the die entry is kept within 190–215 °C to prevent degradation and maintain homogenisation. The melt passes through a 60/80/100 mesh screen pack and enters a spiral mandrel die with die-land geometry selected to suppress weld-line weakness. Vacuum calibration is performed in a first spray tank at −0.2 to −0.6 bar, followed by multi-stage water cooling at 15–40 °C; haul-off speed is controlled by wall-thickness feedback from ultrasonic sensors arrayed around the circumference. The resulting pipe is tested for dimensional stability under EN 12201-2 and for hydrostatic design basis on a lot-by-lot basis. Failure modes observed on production lines are typically centre-line voids from excessive melt temperature, surface melt fracture from an undersized die gap, and eccentricity drift from unstable haul-off tension. Terminal articles from this segment include blue-striped and black municipal water pressure pipes in SDR 11, SDR 13.6, and SDR 17, with outside diameters from 20 mm service tubing to 1200 mm distribution mains, as well as electrofusion-compatible pipe ends and spooled service pipe in DN/OD 20–110 mm coils.

    When Wall Thickness Exceeds 60 mm, Low-Sag Behaviour Governs Die Design

    At wall thicknesses above 60 mm and outside diameters above 800 mm, the main constraint shifts from plastication rate to melt-phase sag between die exit and calibrator entry. HE3492-LS-H carries the LS-H designation for low sag and high stiffness, meaning the bimodal molar mass distribution raises zero-shear viscosity and elastic recovery during the open melt path. The pressure-bearing wall is run at 100 wt% HE3492-LS-H; if a coextruded sacrificial outer layer is used for handling damage, it is normally a PE100 or PE80 black compound applied at 10–15 wt% of total wall thickness and is not counted in the SDR calculation for pressure rating. No molecular-weight modifier or processing aid is added because the low-sag rheology is chain-architecture-driven; wax-based process aids can reduce slow crack growth resistance as measured by ISO 13479.

    These lines are typically built around 90 mm to 120 mm single-screw extruders with L/D 30:1 to 36:1, delivering output of 600–900 kg/h on larger machines, and a spiral mandrel die with up to 12 or 16 spiral segments. Melt temperature at die entry is held in the lower band of 185–205 °C to raise melt viscosity and increase residence time in the calibrator; die head pressure stabilises between 20 MPa and 35 MPa depending on output and die gap. The first vacuum tank applies stepwise negative pressure to prevent bore collapse, and water temperature in the first cooling zone is kept above 35 °C to reduce thermal shock; downstream tanks then drop to 15–25 °C. Pipe producers monitor circumferential wall thickness in real time with 8–16 point ultrasonic arrays and use differential haul-off or thermal die centring to correct eccentricity above 5%. Finished products include large-diameter potable water transmission mains at DN/OD 710–2000 mm in SDR 11 to SDR 26, thick-wall collection mains, and fabricated spools with factory-fused joints.

    In industrial effluent and slurry transfer, selection of HE3492-LS-H is driven by resistance to slow crack growth under constant internal pressure and by the absence of any need for additional black masterbatch. The pipe layer is run at 100 wt% neat HE3492-LS-H; where local specifications permit, clean in-house PE100 regrind may be added up to 20 wt% in the outer cap of a coextruded pipe, but the pressure-bearing layer remains virgin to preserve the 10 MPa minimum required strength of ISO 12162. In abrasive slurry service, addition of silicone-based or wax-based processing aid masterbatch is not recommended because it can compromise butt fusion weldability and interfere with the interfacial fusion pressure window. The applicable standards include ISO 15494 for industrial piping systems, ISO/TR 10358 for chemical resistance, and EN ISO 15494 where European market conformity is required. For mining and dredge applications, designers reference ISO 4427-2 for pressure rating and ISO 1167 for long-term hydrostatic strength; where abrasive slurries are present, wall thickness is increased from the nominal pressure rating rather than changing the base formulation, because wear allowance is a geometric factor.

    Extrusion uses the grooved-feed single-screw platform common to potable water lines, with die temperatures biased toward 200–220 °C for thicker industrial SDR classes. Spiral mandrel dies are used for solid-wall pipe, and vacuum calibration is followed by online laser or ultrasonic gauging; industrial pipes above 500 mm may require internal air cooling with chilled air at 10–20 °C to stabilise the inner surface. Butt fusion welding trials are conducted on production samples at 210–220 °C hot plate temperature with 0.15–0.20 MPa interfacial pressure during bead-up and 0.02–0.05 MPa during fusion, according to ISO 21307; weldability is verified by bend-back or tensile impact tests. Terminal goods include solid-wall process water and effluent lines, mining slurry discharge pipe, dredge pipe, chemical transfer lines where resistance has been validated against ISO/TR 10358, flange adapters, and fabricated spools with butt-fused joints in DN/OD 110–1600 mm.

    Gas Distribution Pipe Requires a Separate Yellow Shell, Not a Different Base Resin

    When the utility specification references ISO 4437-1 or EN 1555-2 for PE100 gas pipe, the same HE3492-LS-H pressure core is operated at 100 wt% in the inner and main wall. The yellow identification layer is coextruded as a separate PE-based shell or as longitudinal stripes at 5–10 wt% of total pipe mass; the base resin is not blended with colour masterbatch in the pressure wall because gas utility rules require the black core to remain certified to the design stress of 10 MPa under ISO 12162. Clean in-house regrind is generally prohibited in gas distribution pipe unless the national gas code specifically permits rework of the same grade at a defined upper limit; where permitted, it is kept below 10 wt% and only in the outer non-pressure cap. Published data for the precise regrind upper limit varies by national code; the value stated here represents a common utility maximum and must be confirmed against the applicable national annex.

    Production lines for gas pipe are configured similarly to water pipe extrusion, but the quality plan expands to include rapid crack propagation testing per ISO 13477 on each new resin lot or die change, because gas mains must resist axial crack propagation at low temperature. Melt temperature at die entry is held at 190–215 °C, and the pipe is cooled in vacuum water tanks with controlled water quality to avoid microcracking. Ultrasonic wall inspection is supplemented by spark testing of the outer yellow layer for pinholes when specified. Pipe ends are cut square to butt fusion protocols and supplied with protective end caps. Terminal products include yellow-striped or yellow-shell PE100 gas mains and service lines in DN/OD 20–630 mm, with SDR 11 and SDR 17.6 as common pressure classes, plus transition fittings and tapping tees assembled by the utility.

    Injection-Moulded PE100 Fittings: Clamp Force, Gate Design, and Shrinkage Compensation

    The injection-moulding route for PE100 fittings from HE3492-LS-H is used for butt fusion and electrofusion fittings where the pipe manufacturer requires a matched PE100 system. The feedstock is specified at 100 wt% virgin compound; regrind from sprues and rejected short-shot fittings may be reintroduced up to 10 wt% if it is dry, free of contamination, and processed within the same shift. Conformal stainless steel or beryllium-copper moulds are used, with gate thickness not less than 60% of the part wall to avoid premature freeze-off and sink marks at the boss. Shot weight is calculated from melt density at 190 °C rather than solid density to avoid flash.

    Fittings are validated under ISO 4427-3, EN 12201-3, and ISO 17885 where applicable, with hydrostatic testing of assemblies at 80 °C/165 h or 20 °C/100 h per ISO 1167. Dimensional control follows ISO 1133-1 for melt flow rate stability and ISO 1183-1 for density verification. Processing on a reciprocating screw injection moulding machine with L/D 20:1 to 25:1 uses melt temperatures of 200–230 °C, injection pressures of 70–100 MPa, and hold pressures of 50–70 MPa; mould temperature is controlled at 15–40 °C for rapid solidification and dimensional stability. Because HE3492-LS-H is a high-molecular-weight bimodal grade, screw recovery time and injection speed must be set to avoid shear heating above 240 °C; processors monitor melt cushion consistency and gate blush as leading indicators of degradation. Shrinkage compensation is applied at 1.5–2.5% in tool design, with post-mould cooling fixtures used on large tees and reducers to maintain roundness at the fusion ends. Finished products include injection-moulded butt fusion elbows, tees, reducers, end caps, flange adapters, and electrofusion sockets in DN/OD 20–400 mm, supplied with milled or protected fusion surfaces.

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    Certification & Compliance
    More Introduction

    Borealis HDPE HE3492-LS-H is supplied as a black bimodal high-density polyethylene compound intended for pressure pipe extrusion and injection-moulded fittings in potable water, sewerage, and industrial piping. The material is classified as PE100-RC under ISO 12162, indicating that long-term hydrostatic strength extrapolated according to ISO 9080 meets a minimum required strength of 10 MPa at 20 °C for 50 years. Manufacturer technical literature lists a melt mass-flow rate of 0.30 g/10 min at 190 °C under 5 kg load (ISO 1133-1) and a density of 959 kg/m³ (ISO 1183-1). Carbon black content is controlled between 2.0 % and 2.5 % by mass (ISO 6964), providing ultraviolet absorbance for above-ground storage and installation periods. Oxidation induction time at 200 °C is reported above 20 min (ISO 11357-6). The bimodal molecular-weight distribution combines a low-molecular-weight fraction for melt processability with a high-molecular-weight fraction that increases tie-molecule density. This architecture shifts the limiting long-term failure mode away from brittle crack propagation under point loading and toward ductile yielding under sustained stress. The product remains an HDPE and does not rely on cross-linking or comonomer-induced flexibility for its service properties.

    Unlike standard PE100 materials that assume compacted sand or select granular backfill, HE3492-LS-H is specified where trench reinstatement uses excavated native soil containing angular stones and debris. The installation route is assessed through the notched pipe test ISO 13479, in which an axial notch is machined into the pipe wall and the specimen is pressurised at 80 °C. The material must resist notch propagation over long durations while backfill particles or bore-path obstructions apply concentrated radial forces. In engineering terms, the pipe no longer depends on a surrounding granular cushion to distribute a point load; the pipe wall itself absorbs the stress concentration. This changes the allowable backfill envelope and reduces imported fill in municipal projects. The relevant property is not short-term burst strength, which remains within the usual PE100 range, but the time-dependent crack growth resistance of the high-molecular-weight fraction.

    What changes when ISO 13479 notched pipe data control the buried pipe specification?

    The notched pipe test is a discriminating requirement because it introduces a sharp external notch that simulates damage caused by stone impingement during backfill or horizontal directional drilling. The notch depth is controlled to 20 % of the minimum pipe wall thickness, with a sharp tip radius that suppresses ductile blunting. Test specimens are held at 80 °C under a hoop stress of 4.0 MPa in water or air; the time to failure is recorded. Standard PE100 materials may fail after several hundred hours under these conditions, while PE100-RC resins are expected to exceed 1 000 h and may exceed 8 760 h depending on pipe diameter and notch preparation. The test accelerates slow crack growth because tie-molecule disentanglement and chain scission are thermally activated at 80 °C. The practical consequence is that the designer selects a material with higher low-stress crack growth resistance, not a material with higher stiffness. Modulus and tensile yield remain within the PE100 range, so ring deflection calculations under external load are not altered; the improvement appears only when the pipe is notched, scratched, or loaded by a sharp particle.

    Typical property profile published in manufacturer technical literature
    PropertyTest methodPublished typical value
    DensityISO 1183-1959 kg/m³
    Melt mass-flow rateISO 1133-10.30 g/10 min
    Carbon black contentISO 69642.0 %–2.5 %
    Oxidation induction time at 200 °CISO 11357-6>20 min
    Tensile stress at yieldISO 527-223 MPa
    Elongation at breakISO 527-2>600 %

    Rheological and thermal processing boundaries on grooved-barrel extruders

    Pipe extrusion of HE3492-LS-H on a grooved-barrel single-screw extruder with an L/D ratio from 30:1 to 36:1 should be carried out with a melt temperature between 190 °C and 230 °C. Barrel profiles typically ramp from 170 °C at the feed throat to 220 °C at the die head. Screw speed must be limited to avoid melt-temperature overshoot; if the melt temperature exceeds 240 °C, the oxidation induction time is consumed rapidly and gel particles may appear at the die lip. Melt pressure ahead of the screen pack should remain below 40 MPa for standard continuous screen changers. Pre-drying is not generally required when the granulate is stored at relative humidity below 60 %; however, if condensation occurs in outdoor silos, desiccant air drying at 80 °C for 2 h is recommended. The compound displays lower die swell than a monomodal HDPE at equivalent melt index because the high-molecular-weight fraction constrains the molecular relaxation spectrum. Extrusion lines using melt pumps should maintain suction-side pressure above 5 MPa to prevent cavitation and output fluctuation.

    The stabiliser package is sensitive to residence time as well as temperature. At a melt temperature of 220 °C, a residence time of 10 min can reduce oxidation induction time by half, depending on screw geometry and oxygen ingress through the hopper. Nitrogen blanketing of the feed hopper reduces oxidative consumption of the phenolic antioxidant during extended start-up or shutdown. In-house regrind from this grade can be re-introduced at up to 15 % by mass provided the resulting pipe retains an oxidation induction time above 20 min and the melt mass-flow rate does not shift outside the specified control range. The limiting variable is not the mechanical property loss but the remaining stabiliser concentration. Repeated extrusion consumes the antioxidant system, and regrind fractions above 15 % may fail the OIT criterion even when the extrudate appears visually acceptable. Carbon black masks early darkening from degradation, so OIT measurement is necessary for thermal abuse detection.

    On production lines using water-ring or underwater pelletising, residual moisture can be trapped in the granule pores. A hopper dryer with a dew point below -30 °C is preferred because the carbon black-filled compound absorbs moisture slowly but releases it in the metering section. Extruders equipped with vented barrels should not be operated without vacuum because volatiles from the antioxidant package can generate surface defects. Pipe marking according to ISO 12176 requires wall thickness, material class, and production date; print adhesion on the carbon black surface is generally acceptable with hot-foil or ink-jet systems using polyethylene-compatible inks. In co-extrusion of striated or co-coloured layers, the tie-layer between HE3492-LS-H and a natural HDPE skin must be a PE100-compatible polyethylene, and the skin layer thickness should not exceed 10 % of total wall thickness unless the pipe standard permits otherwise.

    When resistance to slow crack growth redefines allowable trench profile and backfill

    In conventional buried pipe design, the embedment zone below and around the pipe is filled with compacted granular material to spread soil overburden and live loads. HE3492-LS-H permits a reduction in the thickness or complete elimination of the sand embedment, depending on water utility specifications. The controlling engineering parameter is the pipe’s resistance to point loads from angular backfill particles. The notched pipe test ISO 13479 is the accepted surrogate because it creates a stress concentration similar to a stone indentation. The native excavated material may be reused if the local design code limits maximum particle size and minimum cover are satisfied; the material removes the requirement for imported sand, not the requirement for compaction. For installations beneath trafficked roads, the minimum soil cover should still be calculated from the pipe ring stiffness and the traffic load model in the relevant national code. The slow crack growth resistance also supports horizontal directional drilling where the pipe is pulled through a bore and encounters gravel, rock fragments, and existing service connections. In these operations, the pipe surface is scratched, and the ability of the material to tolerate scratch-induced stress concentration is the main determinant of service life.

    Butt fusion welding of HE3492-LS-H follows ISO 21307. The welding window is narrower than for lower-viscosity PE100 because the high-molecular-weight fraction increases melt elasticity and can produce a more pronounced bead. Standard dual-pressure welding procedures should be validated with bend tests and hydrostatic pressure tests at 80 °C; a typical fusion joint is made at a heater plate temperature of 225 °C. The pipe ends must be faced to remove carbon black-rich surface layers and to prevent contamination of the melt interface. If the facing chips are rough or the pipe is not square, incomplete molecular diffusion at the weld interface can reduce slow crack growth resistance at the joint, which is often the limiting location in notched pressure systems.

    The practical distinction from standard PE100 is defined by slow crack growth performance

    The density, melt mass-flow rate, and short-term tensile properties of HE3492-LS-H remain within the normal PE100 range. The distinction appears in slow crack growth and notch sensitivity tests. Standard PE100 grades meet the hydrostatic strength requirement of ISO 9080 but may not pass extended notched pipe testing under ISO 13479; HE3492-LS-H belongs to the PE100-RC subset that is specifically formulated for notch resistance. Compared with conventional PE100, the material has a higher density of tie molecules connecting crystalline lamellae, which retards crack propagation under low and moderate stress. The melt index is deliberately held near 0.30 g/10 min to preserve weldability and extrusion stability while providing high molecular weight. The carbon black level is higher than in many natural or coloured PE100 compounds, because carbon black acts both as a UV stabiliser and as a stress-concentration modifier when well dispersed. Poor carbon black dispersion, however, can create localised agglomerates that act as crack initiation sites; therefore the material must be processed with sufficient dispersive mixing in the extruder screw. A generic PE100-RC material may offer similar classification, but the pipe fabricator must still confirm that the specific grade meets the relevant national drinking water and construction product requirements, because classification as PE100-RC does not automatically cover all potable water approvals.

    Compliance matrix relevant to pressure pipe applications
    RequirementStandard or test methodApplication boundary
    Long-term hydrostatic strength classificationISO 12162, ISO 9080MRS 10 MPa at 20 °C for 50 years
    Notch propagation resistanceISO 13479Hoop stress 4.0 MPa at 80 °C
    UV resistance during storageISO 6964Carbon black 2.0 %–2.5 %
    Thermal stability of the compoundISO 11357-6OIT > 20 min at 200 °C
    Potable water contact migrationEN 12873 or national equivalentCompliance statement required from fabricator

    The material’s regulatory status depends on the destination market. Under the European Construction Products Regulation, the pipe fabricator remains responsible for demonstrating that the finished pipe meets the relevant harmonised European standard for plastics piping systems. The compound is supplied in black form with carbon black meeting ISO 6964 for weathering resistance, but this also makes near-infrared optical sorting in recycling streams difficult unless a black-specific sensor or density-based separation is used. For industrial pressure systems conveying aqueous solutions, chemical compatibility follows ISO/TR 10358. The grade should not be used with strong oxidising acids such as 98 % sulfuric acid at temperatures above 40 °C, because oxidative attack reduces surface molecular weight and can initiate crack growth under stress. Aromatic hydrocarbons and chlorinated solvents are not recommended above 23 °C due to swelling and environmental stress cracking. For abrasive slurry applications, the pipe wall can be eroded by quartz particles; the erosion rate depends on particle size, shape, velocity, and impact angle, and published data for this specific compound under slurry wear is limited. Slurry piping designs should therefore include site-specific wear testing before replacement of steel or rubber-lined systems. The material is also limited by the maximum operating temperature of HDPE pressure systems; continuous service above 60 °C requires derating of the pressure rating according to the temperature factors in the relevant national design code.

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