Products

Borealis HDPE HE3476-LS

    • Product Name: Borealis HDPE HE3476-LS
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 147286
    Density 946 kg/m³
    Melt Flow Rate 190 C 2 16 Kg 0.3 g/10 min
    Tensile Modulus 1100 MPa
    Tensile Stress At Yield 27 MPa
    Tensile Strain At Yield 9 %
    Tensile Stress At Break 30 MPa
    Tensile Strain At Break >600 %
    Charpy Notched Impact Strength 23 C 12 kJ/m²
    Charpy Notched Impact Strength 30 C 5 kJ/m²
    Vicat Softening Temperature A 125 °C
    Melting Temperature 132 °C
    Crystallization Temperature 115 °C
    Ball Indentation Hardness 55 MPa
    Environmental Stress Cracking Resistance Escr >1000 h
    Water Absorption <0.01 %
    Thermal Conductivity 0.4 W/m·K
    Coefficient Of Linear Thermal Expansion 1.5E-4 /K
    Volume Resistivity >1E14 Ω·cm
    Dielectric Constant 1 Mhz 2.3
    Flammability HB

    As an accredited Borealis HDPE HE3476-LS factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Borealis HDPE HE3476-LS is supplied in 25 kg polyethylene bags, typically palletized in 1,000 kg quantities for transport.
    Container Loading (20′ FCL) 20′ FCL container loaded with non-hazardous Borealis HDPE HE3476-LS, 25 kg bags, palletized, shrink-wrapped, securely stowed for safe export.
    Shipping Borealis HDPE HE3476-LS is supplied as non-hazardous polyethylene pellets. Typical packaging includes 25 kg bags, big bags, octabins, or bulk containers. Transport in clean, dry vehicles, away from heat, ignition sources, and moisture. Follow local regulations and the SDS. Secure bags to prevent spills.
    Storage Store Borealis HDPE HE3476-LS in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and strong odors. Keep original bags or containers sealed, clean, and dry on pallets; avoid moisture, dust, and contamination. Do not stack excessively. Maintain ambient storage temperatures, rotate stock, follow SDS/local regulations, and prevent UV degradation.
    Shelf Life Shelf life approximately two years when stored unopened in a cool, dry, well-ventilated area, protected from direct sunlight and moisture.
    Application of Borealis HDPE HE3476-LS

    Potable Water Transmission Mains Under Hydrostatic Design Basis and Hygiene Conformity

    HE3476-LS enters potable water extrusion as a fully formulated black PE100 compound; no carbon black concentrate is required at the extruder throat because the grade is supplied with carbon black content in the 2.0–2.5 wt% range measured by ISO 6964 and dispersion rating not exceeding ≤3 under ISO 18553. The formulation addition is therefore 100 parts by weight as supplied for virgin pipe; if clean in-house regrind from the same production run is added, the proportion is held below 10 wt% because the long-term hydrostatic design basis of the PE100 classification must be demonstrated on the actual blend under ISO 1167, and batches exceeding 5 wt% rework are commonly re-qualified for slow crack growth by the notched pipe test of ISO 13479. Compliance for drinking water service is anchored to EN 12201-2:2011+A1:2013 and ISO 4427-2:2019, with hygienic certification in North America required under NSF/ANSI 61 and in Australia under AS/NZS 4020; the material's PE100 classification corresponds to a minimum required strength of 10.0 MPa at 20 °C under ISO 12162, yielding a conventional water design stress of 8.0 MPa at 20 °C. Downstream processing uses a single-screw grooved-feed extruder with L/D 30–36, a barrier screw and static mixer; melt temperature at the die entry is typically maintained between 190 °C and 215 °C, while the pipe die is held at 200–210 °C to prevent dimensional drift. The low-sag character of HE3476-LS is used in thick-wall water mains where wall thickness exceeds 40 mm; vacuum calibration with multi-stage cooling at 20–35 °C and controlled internal pressure reduces ovality below 2% of mean diameter. Terminal products are black or black-with-blue-stripe PE100 solid-wall pressure pipes in nominal sizes from 200 mm to 1600 mm, produced in SDR 11 (PN16), SDR 17 (PN10), and SDR 26 (PN6) classes, joined by butt fusion or electrofusion and embedded in municipal distribution and transmission mains.

    What Limits Regrind Addition in Gas Distribution Pipe Extrusion?

    In natural gas distribution, the dominant constraint is rapid crack propagation resistance rather than short-term burst strength; HE3476-LS is extruded as a black compound with carbon black dispersion verified under ISO 18553 and full-scale fracture screening under ISO 13477. The polymer base is a bimodal high-density polyethylene with density typically in the 958–961 kg/m³ range and melt flow rate at 190 °C/5 kg between 0.15 g/10 min and 0.25 g/10 min under ISO 1133-1:2022; this high-molecular-weight tail provides the low-sag melt strength needed for consistent wall thickness in small-diameter service pipes and large mains. Formulation addition is 100 wt% as-supplied compound, because additional carbon black masterbatch is not introduced into gas-grade pipe and would shift the carbon black dispersion distribution, reducing ISO 13479 slow crack growth resistance. Clean in-house regrind from the same gas-pipe production stream is acceptable only up to the processor's validated limit under ISO 4437-2:2014; post-consumer recyclate is excluded. Compliance is anchored to EN 1555-2:2010 and ISO 4437-2:2014, with the PE100 compound classified under ISO 12162 and marked in accordance with ISO 4437-2. Downstream production runs on grooved-feed single-screw extruders with 30:1 to 36:1 L/D, using co-extruded yellow identification stripes on a black pipe substrate; melt temperature is controlled between 190 °C and 210 °C to avoid thermal degradation and to retain the high-molecular-weight fraction responsible for resistance to slow crack growth. End products are PE100 gas mains and service lines in SDR 11 and SDR 17.6 classifications, outside diameters from 32 mm to 630 mm, joined by ISO 21307 butt fusion or ISO 12176 electrofusion sockets and installed in distribution networks at pressures typical of municipal gas grids.

    Extruded solid-wall HDPE for industrial effluent and process water service does not rely solely on the MRS classification; chemical resistance must be screened by ISO 175 immersion exposure to the actual process solution at 23 °C and 60 °C because stress crack resistance measured by ISO 13479 is the controlling long-term property when organic contaminants are present at low concentrations. HE3476-LS is processed without dilution at 100 parts by weight; fillers, plasticizers, or flame-retardant concentrates are not introduced because they reduce fusion weld strength and slow crack growth performance. For mildly acidic or alkaline effluents within pH 2–12 and operating temperatures below 40 °C, the compound is typically specified in SDR 13.6 and SDR 17 solid-wall pressure spools; exposure to free chlorine as sodium hypochlorite is kept below 1.0 mg/L continuous residual, and above this level pressure class selection is de-rated through reduced design stress factors under ISO/TR 10358. Compliance for industrial pressure piping is based on ISO 15494:2015 for thermoplastic pipe systems, with the pipe material classified as PE100 under ISO 12162; in North American project specifications, ASTM D3350 cell classification PE4710 with carbon black is frequently referenced. Pipe extrusion uses a single-screw grooved-feed extruder with 30:1 to 36:1 L/D and melt temperature between 190 °C and 210 °C; butt-fusion welding follows ISO 21307 with heater plate temperature 200–220 °C and interfacial pressure 0.15 MPa during bead formation. Resulting spool pieces, header manifolds, and pressure-rated effluent lines from 110 mm to 630 mm are installed in scrubber blowdown, acid neutralization discharge, and process water return systems where metallic piping would suffer chloride pitting.

    When Mining Slurry and Tailings Lines Need Low-Sag Thick-Wall Sections Beyond SDR 17

    Mining slurry transport imposes cyclic pressure loading and abrasive wall contact that require the extruder to maintain wall thickness uniformity in thick cross-sections; HE3476-LS is selected where sag would otherwise produce eccentric wall and premature failure under the hoop stress conditions described in ISO 9080. The compliance baseline for mine process water and tailings lines is the PE100 classification under ISO 12162, with pipe tested by ISO 1167 for short-term hydrostatic strength and ISO 13479 for slow crack growth; for North American mining projects, ASTM D3350 cell classification PE4710 with carbon black is commonly referenced. Formulation addition is 100 wt% as-supplied compound, because the incorporated carbon black at 2.0–2.5 wt% provides weathering resistance during open-pit placement and no further UV masterbatch is required. Abrasive slurries may contain sharp aggregate; no mineral filler is added to the polymer, because filler platelets would initiate fatigue cracks at the pipe inner surface and reduce butt-fusion weld toughness. Extrusion for thick-wall mining pipe uses the low-sag melt properties of HE3476-LS with screw speeds and cooling rates adjusted to prevent density gradients across walls above 40 mm; die and vacuum calibration are configured for SDR 13.6, SDR 17, and SDR 21 products, with water cascades controlled to keep outer skin solidification ahead of inner wall collapse. Terminal products are butt-fused tailings and slurry transfer pipelines from 250 mm to 1600 mm diameter, often laid above grade with mechanical anchors at bends to absorb thrust and expansion.

    Application boundaryPrimary compliance baselineHE3476-LS addition approachTerminal product class
    Potable water transmissionEN 12201-2, ISO 4427-2, NSF/ANSI 61100 wt% as supplied; clean same-grade rework below 10 wt%, requalification above 5 wt%PE100 solid-wall pipe, SDR 11–26, 200–1600 mm
    Natural gas distributionEN 1555-2, ISO 4437-2100 wt% as supplied; validated in-house regrind onlyBlack PE100 gas main and service pipe, SDR 11/17.6, 32–630 mm
    Industrial effluent and process waterISO 15494:2015, ISO 12162, ASTM D3350100 wt% as supplied; no filler or additive masterbatchPE100 spool and header lines, SDR 13.6/17, 110–630 mm
    Mining slurry and tailingsISO 12162, ASTM D3350100 wt% as supplied; carbon black inherent at 2.0–2.5 wt%Thick-wall PE100 slurry pipe, SDR 13.6–21, 250–1600 mm

    When trenchless rehabilitation of failing concrete or metallic pressure mains is specified, HE3476-LS is used as the liner material where the renewed pipe must withstand both installation scratches and long-term internal pressure inside a deteriorating host. The governing compliance documents are ISO 11298-2:2018 for water network renovation and ASTM F585-14 for insertion practice; material registration remains PE100 under ISO 12162. Because any external surface damage during pull-in becomes a slow crack growth initiation site, installation specifications limit surface scratch depth to ≤10% of wall thickness, and the pipe wall is selected not only on pressure class but also on installation load. The compound is used at 100 wt% without additive modification; field welding is performed by butt fusion under ISO 21307, producing continuous strings of 200–400 m for slip-lining through access pits or pipe bursting. The critical processing step is not extrusion but joining: fusion bead dimensions and pressure cycles are recorded, and weld inspection follows ISO 13953 tensile testing on destructive coupons. Terminal liner products are solid-wall PE100 pipes with SDR 17 and SDR 26 classes, diameters from 250 mm to 1200 mm, inserted into water, wastewater, and gas host mains to restore pressure rating without full excavation.

    Chlorine Contact and Pressure De-rating in Desalination Brine Service

    In seawater reverse osmosis plants, HE3476-LS is fabricated into intake and outfall lines where low-sag extrusion allows large-diameter, thick-wall pipe to be floated into submerged service. Compliance for pressure-rated polyethylene pipe in plant process water is derived from ISO 4427-2 and EN 12201-2, with industrial variants evaluated under ISO 15494; the relevant degradation mechanism shifts from hydrostatic creep to oxidative attack when continuous free chlorine residual exceeds 0.5 mg/L at 20 °C. The compound is added at 100 wt% as supplied; no chlorine scavenger or antioxidant concentrate is blended at the pipe plant because the base stabilizer package is designed for clean-water service, and additional additives reduce fusion weld compatibility. Published data for this specific configuration is limited; therefore pressure class selection for chlorinated brine above 0.5 mg/L continuous residual is de-rated by applying reduced design stress factors under ISO/TR 10358 and verified by ISO 1167 hydrostatic tests performed on pipe samples conditioned in the actual chlorinated brine at the design temperature. Pipe production uses single-screw grooved-feed extrusion with melt temperatures between 190 °C and 210 °C, and the low-sag property is essential for thick-wall outfall sections with wall thickness above 30 mm that must survive submersion and current loading. Terminal products are butt-fused seawater intake lines, brine outfall pipelines, and cooling water return headers in outside diameters from 315 mm to 1600 mm, terminated with flanged adapters for pumps and diffuser manifolds.

    Free Quote

    Competitive Borealis HDPE HE3476-LS prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618136850665

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Borealis HDPE HE3476-LS is a bimodal high-density polyethylene pressure pipe resin supplied as a ready-to-extrude black compound. The material is classified as PE100 under ISO 12162, which requires a long-term hydrostatic strength of at least 10 MPa at 20 °C for 50 years when regression analysis is performed in accordance with ISO 9080. The grade is intended for extruded pipe in potable water, industrial water, and gaseous fuel distribution systems, where resistance to slow crack growth and long-term creep under internal pressure are the controlling design parameters. It is differentiated from PE80 by an MRS of 10 MPa rather than 8.0 MPa, allowing higher design stress for a given wall thickness under the installation and operating conditions defined in ISO 4427-1, EN 12201-1, and ISO 4437.

    Product-specific values for compound density, melt mass-flow rate, tensile properties, and oxidation induction time are controlled by lot release and appear in the manufacturer’s current technical datasheet. The specification framework relevant to the grade is summarised in the table below.

    Standard or methodScopeRelevance to HE3476-LS
    ISO 12162Classification and designation of thermoplastic materials for pressure pipes using minimum required strengthDefines the PE100 MRS of 10 MPa used in design stress calculations
    ISO 9080Determination of long-term hydrostatic strength of thermoplastics materials in pipe form by extrapolationProvides the regression basis for hoop stress curves at 20 °C and 50 years
    ISO 4427-1Polyethylene piping systems for water supply under pressureGeneral material and design requirements for potable and non-potable water
    EN 12201-1European standard for PE pressure pipes for water supplyEstablishes material conformity and pipe system requirements
    ISO 4437Polyethylene piping systems for gaseous fuelsControls long-term performance in gas distribution service
    ISO 1183-1Density measurement of non-cellular plasticsUsed to verify compound density against the PE100 envelope
    ISO 1133-1Melt mass-flow rate determination at 190 °C and 5 kgMonitors lot-to-lot flow consistency for extrusion control
    ISO 6964Determination of carbon black content in polyolefinsConfirms UV stabilisation loading in the black compound
    ISO 18553Assessment of pigment or carbon black dispersion in polyolefinsControls agglomerate levels that can initiate localised flaws
    ISO 13479Determination of resistance to slow crack growth on notched pipesRanks long-term crack propagation resistance under hydrostatic stress

    The class-typical envelope for a black PE100 pipe compound is given in the following table. It is not a product-specific release specification but defines the technical space in which HE3476-LS must operate.

    PropertyTest methodTypical class envelope for PE100 black pipe compoundOperational significance
    Compound densityISO 1183-10.950–0.965 g/cm³Affects pipe mass, stiffness, and wall-thickness calculations
    Melt mass-flow rateISO 1133-1 at 190 °C/5 kgbelow 0.30 g/10 minCorrelates with extrusion pressure, shear thinning, and sag behaviour
    Tensile yield stressISO 527-222–25 MPaShort-term pipe strength and fitting retention
    Carbon black contentISO 69642.0–2.5 wt%Provides weathering resistance and UV shielding
    Oxidation induction timeISO 11357-6 at 200 °Cabove 20 minIndicates residual antioxidant package integrity
    Slow crack growth resistanceISO 13479notched pipe failure time depends on pipe wall and test conditionDistinguishes long-term failure resistance from short-term strength

    What Limits Slow Crack Growth Resistance in PE100 Pipe Compounds?

    Slow crack growth is the dominant failure mode for pressurised polyethylene pipe after the initial elastic response. In HE3476-LS, the bimodal molecular weight distribution and controlled short-chain branching increase tie-molecule density while preserving extrudability. The high-molecular-weight fraction raises resistance to craze fibril rupture and crack propagation; the low-molecular-weight fraction contributes shear thinning at the shear rates encountered in pipe extrusion. Accelerated testing under ISO 13479 on notched pipes and under ASTM F1473 on notched rectangular bars is used to rank material performance against reference grades. Product-specific failure times should be obtained from the manufacturer’s technical datasheet; published data for this specific configuration in the open literature is limited. The governing material requirement is not a single measured point but the complete creep rupture curve generated under ISO 9080, because the change in failure mode from ductile yielding to brittle slow crack growth is time-dependent and temperature-dependent.

    For original sealed pellets, no dedicated predrying is required. Production-scale pipe extrusion with HE3476-LS generally uses grooved-barrel single-screw extruders of 30D to 36D length. Feed-zone temperatures are maintained below 90 °C to prevent premature pellet compaction and preserve the forced conveying capacity of the grooves. Melt temperatures at the die entry are controlled within the manufacturer’s recommended range; extended hold-up above 220 °C can deplete the antioxidant package and reduce oxidation induction time measured by ISO 11357-6 at 200 °C. Regrind containing surface moisture above 0.05 wt% can generate splay and surface pitting, so closed-loop handling and dry regrind storage are required where recycled in-plant material is added.

    Melt Rheology, Sag Resistance, and Wall-Thickness Uniformity in Large-Diameter Extrusion

    Low-sag behaviour is controlled by the high zero-shear viscosity and shear-thinning character of the bimodal resin. Under the low shear rates relevant to gravitational flow in the cooling pipe, the compound retains enough elasticity and viscosity to resist radial slump. At die-exit shear rates above 100 s⁻¹, the viscosity drops sufficiently to avoid excessive melt pressure and excessive die swell. Large-diameter pipe lines above 250 mm outer diameter use vacuum sizing and multi-zone spray cooling; sag-induced wall thinning is monitored by ultrasonic thickness scanning after calibration, and acceptance criteria for wall thickness and eccentricity follow the dimensional tolerances of ISO 4427-2. Die head design and melt temperature interact: if the stock temperature is increased to reduce melt pressure, sag resistance decreases because zero-shear viscosity falls with temperature. The operating window therefore combines melt temperature, draw ratio, and cooling rate rather than relying on a single setpoint.

    For potable water service, the black compound must comply with national drinking water approvals and with organoleptic and migration test requirements such as EN 12873-1. Carbon black dispersion is controlled by ISO 18553 to avoid agglomerates larger than the specified rating. Prolonged contact with concentrated strong oxidising acids, halogens, or aromatic hydrocarbons can soften or embrittle PE100 and is outside the intended service envelope. Ultraviolet exposure is mitigated by the carbon black loading, and outdoor storage can be undertaken provided the material is protected from direct sources of heat and ignition.

    When HE3476-LS Is Compared With Unimodal PE80 and Standard PE100 Resins

    Unimodal PE80 grades have lower MRS, generally 8.0 MPa, and often lower slow crack growth resistance; their use at the same pressure requires greater wall thickness. Compared with conventional PE100 without low-sag formulation, HE3476-LS is intended to improve processing stability in thick-wall, large-diameter pipe rather than to increase the hydrostatic design basis. The difference is not a higher MRS but a combination of controlled molecular architecture, carbon black dispersion, and antioxidant formulation that affects sag, weldability, and long-term stability. Standardised comparisons should be made on the basis of ISO 9080 regression curves and ISO 13479 failure times, not on melt index alone. The lower melt flow rate of bimodal PE100 grades relative to many PE80 compounds also means that extruder pressures are higher for the same output, and screw temperature profiles must compensate for the higher viscosity at low shear rates.

    Electrofusion and butt fusion welding of HE3476-LS pipes require conformity with the fusion procedures of ISO 21307 and the equipment requirements of ISO 12176-2. The material should be welded only to compatible PE100 grades and fittings; mixing with resins outside the approved fusion range is not recommended. Peel and tensile tests on joints are performed according to ISO 13954 and ISO 13953 respectively, with ductile failure required to confirm joint integrity.

    Top