Products

Borealis HDPE HE3497-LS

    • Product Name: Borealis HDPE HE3497-LS
    • 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 563616
    Density 0.958 g/cm³
    Melt Flow Rate 190 C 5 Kg 0.25 g/10 min
    Carbon Black Content 2.3 %
    Tensile Stress At Yield 24 MPa
    Tensile Strain At Break >600 %
    Flexural Modulus 1100 MPa
    Charpy Notched Impact Strength 23 C 30 kJ/m²
    Charpy Notched Impact Strength 30 C 10 kJ/m²
    Vicat Softening Temperature 125 °C
    Oxidation Induction Time 200 C >20 min
    Shore D Hardness 60
    Water Absorption <0.01 %
    Thermal Conductivity 0.4 W/(m·K)
    Coefficient Of Linear Thermal Expansion 1.5 × 10⁻⁴ /°C

    As an accredited Borealis HDPE HE3497-LS factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Typically packaged as 25 kg polyethylene bags, 50 bags per 1,250 kg pallet, stretch-wrapped for transport.
    Container Loading (20′ FCL) 20′ FCL container loaded with Borealis HDPE HE3497-LS in 25 kg bags, palletized, stretch-wrapped, and secured for ocean shipment.
    Shipping Borealis HDPE HE3497-LS is typically shipped as non-hazardous, free-flowing black polyethylene pellets in 25-kg moisture-resistant bags. Bags are stacked on pallets, stretch-wrapped for stability, and transported in dry containers or trucks. Bulk deliveries may use lined octabins or bulk tankers. Store cool, dry, away from direct sunlight.
    Storage Always store indoors only. Borealis HDPE HE3497-LS in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and flames. Keep original packaging closed and palletized. Avoid moisture, dust, oils, and incompatible chemicals. Do not stack excessively; prevent deformation. Use first-in, first-out. Maintain ambient temperature, protect from prolonged UV exposure, inspect containers regularly, and keep away from oxidizing agents.
    Shelf Life Borealis HDPE HE3497-LS shelf life: at least two years if stored dry, clean, below 50°C, and away from direct sunlight.
    Application of Borealis HDPE HE3497-LS

    On fibre optic loose-tube cable production lines, Borealis HDPE HE3497-LS is extruded as an outer sheath directly over aramid yarn layers, water-swellable tapes, ripcords, and central strength members. The compound is supplied pre-compounded with carbon black; adding a separate black masterbatch is generally unnecessary and can reduce dispersion quality if the screw is not designed for masterbatch let-down. A single-screw extruder with a grooved feed section, 25:1 to 30:1 L/D, and a barrier screw with 3:1 compression ratio is typical for this jacket. Barrel zones from feed to die are set in a rising profile from 180 °C to 220 °C; melt temperature measured at the adapter is kept below 225 °C. Exceeding 230 °C for more than 30 min raises the carbonyl index and produces micro-roughness on the cooled jacket surface. The die is normally a pressure-type tube-on die with die land length to annular gap ratio above 10:1; draw-down ratio is maintained between 1.1:1 and 1.5:1 to limit frozen-in orientation. Cooling is carried out in a segmented water trough with first-stage water temperature held between 25 °C and 40 °C; rapid quenching below 20 °C increases free shrinkage. Shrinkback after 24 h at 100 °C is an acceptance criterion in many fibre optic cable specifications; depending on cable construction, the sheath movement is normally specified as less than 1% relative to a stripped cable end. Carbon black dispersion is checked according to ISO 18553:2002; poor dispersion appears as black specks in thin jacket sections. For outdoor installation, qualification for environmental stress cracking resistance is usually performed according to ASTM D1693-15 condition A or B using 10% Igepal CO-630 at 50 °C. Cable lubricants based on glycol or mineral oil require the jacket to be tested after chemical exposure; published data for this specific configuration is limited and should be verified per lot. If the cable is installed by blowing into duct, the jacket surface friction matters; HE3497-LS can be co-extruded with a thin lubricant-rich skin or surface-treated after extrusion, but the base compound itself is not a dedicated low-friction product. When the same jacket is considered for riser-rated indoor fibre optic cables, flame performance remains outside the base grade’s capability, and the addition of halogen-free flame-retardant fillers is not recommended without full revalidation because melt viscosity and ESCR balance shift simultaneously.

    Test propertyStandard designationApplication relevance
    Melt mass-flow rateISO 1133-1:2022Incoming lot control; screw-speed and line-speed setting
    DensityISO 1183-1:2019Material classification and crystallinity control
    Tensile strength and elongation at breakISO 527-1:2019 / ISO 527-2:2012Jacket mechanical integrity after ageing
    Environmental stress crack resistanceASTM D1693-15 / IEC 60811-406Slow crack growth resistance under field stress
    Carbon black contentISO 6964:2019UV stabilisation required for outdoor use
    Carbon black dispersionISO 18553:2002Surface smoothness and defect control for thin jackets
    Low-temperature impactIEC 60811-506Cold-weather installation and handling

    What Prevents Low-Temperature Jacket Cracking in Aerial Copper Drop Cables?

    Aerial self-supporting copper drop cables impose a different stress field on the jacket than buried cable. The jacket is extruded over a corrugated or smooth aluminium shield that is bonded with an adhesive copolymer; the HDPE must maintain mechanical integrity without losing tensile elongation after thermal ageing. HE3497-LS is selected in these constructions because the bimodal molecular weight distribution provides a combination of slow crack growth resistance and stiffness under wind-induced cyclic bending. The relevant test for cold impact is not a single elongation number; the sheath is subjected to low-temperature impact at -20 °C or -40 °C in accordance with IEC 60811-506, with no visible cracks and no dielectric failure. ESCR performance under aerial conditions is evaluated after the jacket has been wrapped around a mandrel and exposed to a weathering solution; the test duration depends on the regional cable standard and is not fixed by the resin supplier. At the processing level, the main failure mode observed on production lines is screw slip in the feed zone when regrind levels exceed 15%. The grooved feed section of the extruder can generate feed pressures above 400 bar with virgin compound, but adding fluff or low-bulk-density regrind disturbs this compaction and causes melt-pressure oscillation. This oscillation is visible as periodic jacket wall-thickness variation, particularly at cable line speeds above 60 m/min. To maintain a stable melt cushion, the hopper loader should maintain a consistent resin level and the feed-throat temperature should not exceed 50 °C; otherwise pellet bridging occurs. The addition of colour masterbatch to convert the black compound to another colour is not recommended because the carbon black already present limits the achievable colour. If a non-black jacket is required, a different grade should be used. Jacket thickness for aerial copper drop cables is commonly in the range 0.8 mm to 1.2 mm; thin spots below 0.6 mm are a rejection criterion because they reduce the time to slow crack growth at cable attachment points. Thermal ageing at 100 °C for 7 days should not reduce elongation at break by more than 25% from the unaged value when tested according to ISO 527-2:2012. Published data for the exact retention of HE3497-LS in this configuration is limited; the value depends on the antioxidant package and carbon black dispersion.

    Low-Voltage Power Cable Sheath Adhesion and Fill Ratio Limits

    For low-voltage power cables built to IEC 60502-1, the outer HDPE sheath is not the primary insulation; it protects the underlying PVC bedding or XLPE insulation from moisture, abrasion, and sunlight. HE3497-LS can be used as an outer sheath only when the maximum conductor operating temperature does not exceed 70 °C, because HDPE has a low thermal softening point relative to XLPE. Short-circuit conductor temperatures above 100 °C can soften the sheath locally where it touches metal tape or armour and can lead to indentation and permanent deformation. The sheath is normally applied using a tube-on extrusion process so that the HDPE does not penetrate the interstices of the underlying layer; pressure extrusion would increase adhesion but also make stripping more difficult. Strippability is a key field installation requirement; the sheath removal force is measured on a 200 mm cable sample at 23 °C and should remain below the maximum specified in IEC 60811-100 or the cable purchaser’s specification. If the sheath is applied directly over corrugated steel armour, a flooding compound may be used to prevent water migration; this flooding compound must be compatible with the HDPE and must not contain high levels of aromatic oil that reduce ESCR. In low-voltage aerial bundled cables, the sheath is exposed to direct sunlight; UV stabilisation is provided by the carbon black dispersion in the compound, and carbon black content is controlled between 2.0% and 3.0% by mass according to ISO 6964:2019. Dispersion should be assessed by ISO 18553:2002; agglomerates create local stress concentrations that can start cracks under cyclic vibration from wind or traffic. The compound should not be blended with high-density PE pipe regrind or other waste streams as a cost-saving measure, because the molecular weight distribution and stabiliser package are changed unpredictably. That practice may pass a tensile test but fail ESCR after several months of field exposure. In production, the water trough length for power cable sheathing should be sufficient to cool the cable below 60 °C before coiling; otherwise the sheath deforms on the reel due to residual heat and the cable may block. Published processing data for this specific grade in power-cable sheath construction is limited; the use is more common in telecom and fibre optic cables.

    In microduct extrusion lines, HE3497-LS is processed as a thin-wall tube with an outer diameter of 3.0 mm to 16.0 mm and a wall thickness from 0.3 mm to 1.0 mm, depending on the fibre count and blowing distance. The screw configuration is critical for thin-wall stability: a single-screw extruder with a 24:1 to 30:1 L/D barrier screw, a screen pack of 40/60/80 mesh, and a spiral annular die with a die gap of 0.8 mm to 1.2 mm is used. Melt temperature is held at 200 °C to 220 °C; lower melt temperature increases die pressure and may create melt fracture, while higher melt temperature degrades the polymer and increases ovality after vacuum calibration. The tube is calibrated in a vacuum tank with first-stage water at 25 °C to 35 °C; the vacuum level is adjusted to control outer diameter without collapsing the tube. The main production defect is wall-thickness eccentricity, which is caused by uneven die temperature distribution or insufficient melt distribution in the spiral mandrel. A nitrogen purge through the inside of the tube during start-up prevents collapse until the tube enters the vacuum tank; after calibration, the line speed can be raised to 30–80 m/min for small-diameter microducts. Because the duct may be installed by cable blowing, the inner surface must have a low friction coefficient; a co-extruded slip layer containing a migrating slip agent is often applied on the inner wall. HE3497-LS itself provides a stable outer wall and crush resistance, but the slip layer becomes part of the final microduct structure and must be compatible with the HDPE melt. Crush resistance is evaluated by a parallel-plate compression test at 23 °C; the duct must not crack at 25% deformation in typical microduct specifications. No single universal test standard governs all microducts; regional specifications may refer to IEC 61386 for conduits or to operator-specific blow-in tests. During blow-in tests, the duct is subjected to air pressure of 10 bar to 15 bar and a high-speed air flow; internal surface roughness and dimensional stability are more important than tensile strength. The carbon black content provides outdoor UV resistance; however, if microduct is installed inside an existing occupied duct, UV resistance is less important and the carbon black dispersion still contributes to melt homogeneity. Field failures often occur at joints where the microduct has been crushed or kinked during installation; the HDPE outer wall should resist kinking at a bend radius below 10 times the outer diameter.

    When Hybrid Fibre-Copper Cables Require a Single Common Jacket

    When hybrid fibre-copper cables combine loose-tube fibre optic elements with copper power pairs or coaxial elements in a single cable core, the outer jacket must satisfy two sometimes conflicting requirements: low shrinkback for the optical elements and adequate crush resistance for the copper elements. HE3497-LS is used in such constructions because its high molecular weight and carbon black stabilisation give the jacket enough modulus to prevent the copper conductor bundle from printing through the outer surface without making the jacket so stiff that the optical fibres are bent during cold installation. The cable core is normally filled or flooded; the fill compound must be selected for compatibility with HDPE. High aromatic mineral oils can plasticise the HDPE jacket over time and reduce tensile strength; qualification includes an oil immersion test at 70 °C for 7 days followed by tensile testing according to ISO 527-1:2019. A loss in tensile strength greater than 20% after oil ageing is considered a red flag in cable development. The jacket is usually applied with a tube-on die because the core has an irregular profile; pressure extrusion would force HDPE into the gaps between the optical tubes and the copper pairs, creating hard spots that pinch the optical fibres during bending. The minimum jacket thickness is set by the cable standard and the diameter over the core, but values below 0.8 mm are rarely used for hybrid cables due to the risk of copper print-through. During extrusion, the lay length of the copper pairs and the binding tape tension must be controlled so that the core diameter variation at the crosshead is below 0.2 mm; larger variation causes cyclical changes in wall thickness. Because hybrid cables are often pulled through conduits, the jacket is tested for abrasion resistance by a reciprocating abrasion test; the exact test method depends on the operating company specification and no single ISO test applies. Published data for the abrasion loss of HE3497-LS in hybrid constructions is limited; design verification should include field-pull trials rather than relying on laboratory test coupons alone.

    Coaxial Feeder Lines Benefit from a Two-Layer HDPE Jacket Structure

    Coaxial feeder cables for base stations and broadcast installations use a foam-skin polyethylene insulation over a copper or copper-clad aluminium inner conductor. In some designs the outer HDPE jacket is co-extruded as a two-layer system: a thin pigmented skin for identification is laid over the main HE3497-LS jacket body. The base compound forms the structural layer over the corrugated copper or aluminium outer conductor. The jacket is applied at a total thickness of 0.8 mm to 1.5 mm, depending on cable diameter, using a tube-on die that leaves a small air gap between the jacket and the outer conductor. This air gap allows the jacket to expand and contract independently of the metal tape, reducing the risk of jacket cracking at low temperature and preventing the jacket from being punctured by the corrugation peaks during bending. The plain HDPE layer is not bonded to the outer conductor; if bonded jacket construction is required, a different co-extruded adhesive layer must be used because plain HDPE adhesion to aluminium or copper is poor. The co-extruded skin must be selected from a compatible polyolefin with a lower melt temperature than the base HDPE; processing at the same die temperature can cause the skin to degrade if the temperature is above 220 °C. The main HE3497-LS layer provides mechanical strength and UV resistance; the skin layer is too thin to contribute meaningfully to crush resistance and is used only for marking or colour coding. During processing, the corrugated outer conductor enters the crosshead from a payoff arrangement; the line speed is often set between 20 m/min and 50 m/min, and the extruder screw speed is adjusted to maintain a die-head pressure of 150 bar to 250 bar. Die-head pressure above 300 bar indicates excessive screen blockage or melt temperature that is too low. The jacket is cooled in a water trough with a first-stage temperature of 30 °C to 40 °C; rapid cooling below 20 °C can create radial thermal residual stress that causes the jacket to split when the cable is bent at low temperature. Low-temperature bend testing is performed by conditioning a cable sample at -20 °C for 4 h and bending it around a mandrel of 10 times the cable diameter without cracking. The HDPE jacket is not flame-retardant; where riser or plenum flame ratings are required, the base grade must not be used unless a fire-resistant barrier tape is added to the cable core, and the jacket itself still contributes fuel load in vertical burn tests. The carbon black in the base layer provides UV resistance and weathering stability, but the black surface temperature can exceed 70 °C in direct sunlight in some regions; this reduces the mechanical safety margin and should be considered when specifying maximum conductor temperature.

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    Certification & Compliance
    More Introduction

    Borealis HDPE HE3497-LS is a bimodal high-density polyethylene compound supplied as black pellets for pressure pipe extrusion. The material is classified as PE100 under ISO 12162, with a minimum required strength of 10 MPa at 20 °C and 50 years established by long-term hydrostatic strength testing to ISO 9080. The compound incorporates carbon black at 2.0–2.5% by mass, measured according to ISO 6964, to provide ultraviolet stabilization for outdoor storage and buried service. Its bimodal molecular architecture combines a high-molecular-weight fraction for slow crack growth resistance with a low-molecular-weight fraction for melt processability. This balance produces a PE100 pipe extrusion grade with low-sag behavior intended for solid-wall pressure pipe, particularly where large diameter and heavy wall thickness prolong molten residence time after the die exit. Published typical values include a density of 0.959 g/cm³ per ISO 1183-1 and a melt mass-flow rate of 0.23 g/10 min at 190 °C under a 5 kg load per ISO 1133-1.

    What Hydrostatic Design Basis Does the Grade Attain Under ISO 9080?

    The PE100 designation is not a single-point tensile value but a regression-based classification derived from pipe failure data. Under ISO 9080, pipe specimens are tested at multiple temperatures and hoop stresses until ductile, brittle, or mixed-mode failure occurs. The lower confidence limit of the long-term hydrostatic strength at 20 °C and 50 years must equal or exceed 10.0 MPa. HE3497-LS meets this criterion and is therefore assigned a minimum required strength of 10 MPa. For water supply systems under ISO 4427-1 and EN 12201-1, design stress is obtained by dividing the minimum required strength by a service coefficient, typically 1.25, yielding 8.0 MPa. This permits either higher operating pressure or reduced wall thickness compared with PE80 compounds, whose minimum required strength is 8.0 MPa and design stress at the same coefficient is 6.4 MPa. For a design stress of 8.0 MPa, pressure rating follows the ISO relationship PN = 2σ/(SDR−1); SDR 11 gives 1.6 MPa, SDR 17 gives 1.0 MPa, and SDR 26 gives 0.64 MPa at 20 °C.

    Extrusion of HE3497-LS is performed on grooved-barrel single-screw extruders with L/D ratios between 30:1 and 36:1, equipped with a spiral mandrel die and vacuum calibration. A barrel temperature profile from 180 °C in the feed zone to 210 °C at the metering zone is typical; melt temperature at the die entry should remain between 190 °C and 230 °C. Operation above 230 °C accelerates oxidative degradation, reduces oxidation induction time, and can generate surface streaking or gel particles. Operation below 190 °C increases melt elasticity to the point where sharkskin and die-lip build-up may appear. Screw speed and back-pressure are adjusted to maintain melt pressure stability. Batch-to-batch variation in melt mass-flow rate of approximately ±0.02 g/10 min can shift die-head pressure at fixed screw speed, and wall-thickness control loops must compensate through in-line ultrasonic measurement after vacuum calibration. The compound is not hygroscopic; moisture absorption is below 0.01% under ISO 62. However, storage in unheated silos followed by transfer into warm production areas can create surface condensation, which is removed by forward venting or a short preheat. On production lines with L/D 33 grooved-barrel extruders, feed-zone flooding from excessive first-zone temperature is a documented start-up failure: pellet slip in the grooved feed section reduces throughput and causes melt pressure oscillation. The first barrel zone is therefore set 20–30 K below the metering temperature.

    When Thick-Wall Pipe Extrusion Requires Low-Sag Melt Elasticity

    In large-diameter solid-wall pipe, the molten tube is unsupported between the die lip and the calibration sleeve. Gravitational sag can generate wall-thickness eccentricity, particularly at outer diameters above 500 mm and wall thicknesses above 40 mm. The low-sag formulation in HE3497-LS increases zero-shear viscosity and melt strength without reducing extrudate surface quality. Oscillatory shear rheometry at 190 °C under nitrogen shows that the low-shear complex viscosity at 0.01 rad/s is higher than that of standard PE100 black pipe compounds, while the high-shear viscosity at 100 rad/s remains low enough for normal die flow. This shear-thinning separation is characteristic of a broadened bimodal molar-mass distribution. Published state of the art indicates that low-sag PE100 grades reduce wall-thickness eccentricity in thick-wall pipe to below ±5% under controlled calibration. Specific production data for HE3497-LS are limited, so the magnitude must be verified by in-line ultrasonic scanning on each line. In practice, processors often couple the grade change with die-head temperature adjustment and calibration-sleeve alignment to hold eccentricity within pipe product standards.

    Slow Crack Growth Resistance and Oxidative Stability Characteristics

    PE100 compounds for buried pressure mains must resist slow crack growth from point defects, scratches, and fusion-bead notches. HE3497-LS supports this through the high-molecular-weight fraction in the bimodal distribution. Slow crack growth is commonly assessed on notched pipe under ISO 13479; pipe-grade PE100 materials generally exceed 500 h at 80 °C and 4.6 MPa hoop stress. The specific published value for HE3497-LS should be confirmed from the current manufacturer data sheet before qualification. Oxidative stability is monitored by oxidation induction time. Isothermal OIT at 210 °C per ISO 11357-6 is typically reported above 20 min for this family of black pipe-grade compounds. Carbon black dispersion is controlled under ISO 18553, with a maximum particle-agglomerate rating of 3 to avoid microscopic stress concentrations. The carbon black loading of 2.0–2.5% by mass per ISO 6964 is sufficient for ultraviolet stabilization of black pipe stored outdoors. Environmental stress-cracking resistance for PE100 pipe compounds of this class is commonly reported above 1000 h under ASTM D1693 condition B, but HE3497-LS lot-specific values must be taken from the certificate of analysis.

    Typical mechanical properties reported for HE3497-LS include tensile stress at yield of 25 MPa when tested at 50 mm/min per ISO 527-2; tensile elongation at break above 600%; flexural modulus of approximately 900 MPa per ISO 178; and Charpy notched impact strength at 23 °C above 20 kJ/m² per ISO 179-1. The density is 0.959 g/cm³, and the melt mass-flow rate at 190 °C/5 kg is 0.23 g/10 min. These values are typical and not minimum specification limits. Batch release is governed by the manufacturer’s certificate of analysis, and pipe producers must verify that incoming lots fall within their own extrusion windows. The material is supplied as a black compound for water distribution and industrial pressure pipe. National potable water approvals are route-specific and must be verified against local regulatory listings rather than assumed from the PE100 classification alone.

    The Grade Differs from Conventional PE100 Compounds in Melt Strength and Sag Resistance

    Compared with the standard Borealis HE3490-LS black PE100 grade, HE3497-LS occupies the low-sag segment of the pipe extrusion portfolio. Both grades meet the ISO 12162 PE100 classification, but HE3497-LS is selected when pipe diameter, wall thickness, or die residence time makes gravitational sag the dominant defect. The difference is not expressed principally in static tensile properties; it appears in melt rheology and in extrusion behavior on large-bore spiral mandrel dies. In direct comparison, the low-shear viscosity of HE3497-LS is higher, and sag resistance is improved at melt temperatures between 200 °C and 220 °C. Processors switching from HE3490-LS to HE3497-LS on the same line may observe a moderate increase in die-head pressure at constant screw speed; screw speed or barrel temperature may require adjustment to maintain output. The low-sag formulation can reduce dependence on rotating die heads or internal cooling mandrels in thick-wall pipe production, although those mechanical systems remain necessary for extreme wall-thickness tolerances above 60 mm.

    Joining of pipes produced from HE3497-LS is performed by butt fusion or electrofusion according to ISO 21307. Heater plate surface temperatures of 200–230 °C are used. Interfacial pressure and dwell times must follow pipe manufacturer procedures because the low-sag melt elasticity can slightly reduce melt displacement at the fusion bead. Weld integrity is verified by visual bead dimensions and, in critical installations, by destructive bend or tensile testing according to ISO 13953. The compound’s bimodal molar-mass distribution does not alter standard fusion temperatures, but it requires stable alignment and adequate interfacial melt penetration to avoid cold fusion defects.

    Operational boundaries must be respected. Continuous pipe service above 20 °C requires pressure derating in accordance with ISO 4427-1; long-term exposure above 60 °C is outside the normal classification envelope for PE100 water piping. The compound is not intended for contact with strong oxidizing agents, chlorinated solvents, or hydrocarbon condensates unless the system design has been independently evaluated. Regrind should be limited to clean, dry, same-grade black sprues and pipe cropped from start-up; contamination with polypropylene, PVC, or abrasive mineral fillers must be avoided because these contaminants nucleate local stresses and reduce slow crack growth resistance. The antioxidant system is formulated for pipe-extrusion thermal history, not for repeated high-temperature recycling; multiple re-extrusion cycles can deplete the stabilizer package and reduce OIT below the 20 min threshold. When stored in outdoor silos, the material should be protected from direct sunlight and water ingestion; bulk temperature should remain below 50 °C to preserve additive dispersion.

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