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Borealis HDPE HE3493-LS

    • Product Name: Borealis HDPE HE3493-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 135435
    Density 958 kg/m³
    Meltflowrate 190c 5kg 0.25 g/10 min
    Tensilemodulus 1000 MPa
    Tensilestressatyield 23 MPa
    Elongationatbreak >600%
    Charpynotchedimpact 23c 10 kJ/m²
    Charpynotchedimpact Minus30c 4 kJ/m²
    Vicatsofteningtemperature 120 °C
    Thermalconductivity 0.4 W/m·K
    Carbonblackcontent 2.0-2.5%
    Oxidationinductiontime 200c >20 min
    Moisturecontent <0.02%
    Hardness Shored 60
    Coefficientoflinearthermalexpansion 1.4E-4 /°C
    Specificheatcapacity 1.9 kJ/kg·K
    Waterabsorption <0.01%
    Dielectricconstant 2.3
    Volumeresistivity >1E14 Ω·cm

    As an accredited Borealis HDPE HE3493-LS factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Borealis HDPE HE3493-LS is typically packaged in 25 kg polyethylene bags, 55 bags per pallet, totaling 1,375 kg.
    Container Loading (20′ FCL) 20′ FCL container loaded with Borealis HDPE HE3493-LS resin in bags, palletized, shrink-wrapped, and secured for ocean transport.
    Shipping Borealis HDPE HE3493-LS is shipped as solid, non-hazardous thermoplastic pellets in moisture-resistant 25 kg polyethylene bags, octabins, or bulk trucks. Keep containers sealed, palletized, and dry; store away from heat, sunlight, and ignition sources. Transport under standard regulations at ambient temperature. No special UN classification required. Use clean, dry conveyances.
    Storage Store Borealis HDPE HE3493-LS in its original, closed packaging in a cool, dry, well-ventilated area. Protect from direct sunlight, heat, moisture, and contamination. Keep away from ignition sources, strong oxidizers, and incompatible materials. Stack pallets securely to prevent bag damage. Maintain clean handling areas and avoid dust generation. Follow local regulations and the manufacturer’s safety data sheet.
    Shelf Life Borealis HDPE HE3493-LS has a shelf life of two years from production when stored unopened, dry, away from sunlight, below 50°C.
    Application of Borealis HDPE HE3493-LS

    When specifying a PE100 compound for potable water pressure pipe, the controlling classification is ISO 9080, which assigns a long-term minimum required strength of 10 MPa at 20 °C for a projected service life of 50 years. Borealis HE3493-LS is a bimodal high-density polyethylene supplied as a ready-to-use black compound with carbon black and UV stabiliser pre-dispersed; no separate carbon black masterbatch letdown is introduced at the extruder. The compound is processed on a single-screw grooved-barrel extruder with an L/D ratio of at least 30:1 and a barrier screw configured for high-density polyethylene pipe; screen packs of 80/120/80 mesh are common in production lines. Barrel set-points follow a rising profile from 180 °C at the feed zone to 220 °C at the metering zone, while the melt temperature measured after the screen pack is maintained between 200 °C and 230 °C. Die head pressure in DN 110 mm to DN 400 mm lines typically remains below 40 MPa to prevent excessive shear heating. Pipe wall thickness is selected by the standard dimension ratio: SDR 11 yields 16 bar nominal pressure, SDR 17 yields 10 bar, and SDR 26 yields 6 bar for water at 20 °C using the PE100 hydrostatic design basis. Hydrostatic proof testing follows ISO 1167, slow crack growth validation follows ISO 13479, and rapid crack propagation screening follows ISO 13477 at temperatures relevant to cold-water service. National potable water approvals such as NSF/ANSI 61, WRAS, and DVGW W270 are applied at the certification level where specific pipe systems are marketed. Exposure to free chlorine above 3 mg/L under continuous service requires accelerated chlorine resistance testing according to ASTM F2263 because standard PE100 grades may not retain full long-term hydrostatic strength under oxidative water disinfectant conditions. Hopper drying is not normally required for the as-supplied compound; if the material is stored outdoors and surface condensation has formed, a drying step at 70 °C for 2 h to 4 h using desiccant or vented hopper air is applied before extrusion. Regrind usage is limited to 10 wt% of the same production lot for pressure-rated solid-wall pipe; higher fractions may reduce slow crack growth resistance and are not recommended without full hydrostatic requalification. Terminal components include municipal water trunk mains, distribution laterals, service connection pipes, and pump station discharge headers in the nominal diameter range from DN 32 mm to DN 1200 mm.

    Compliance checklist for pressure rating design of HE3493-LS potable water pipe
    Property / TestStandard designationBoundary applied in potable water service
    Long-term hydrostatic strength, PE100 classificationISO 908010 MPa MRS at 20 °C, 50-year extrapolation
    Hydrostatic pressure resistanceISO 1167Water-in-water or water-in-air testing at 20 °C and 80 °C
    Slow crack growthISO 13479Notched pipe test at 80 °C for PE100 qualification
    Rapid crack propagationISO 13477S4 method at 0 °C to -20 °C range
    Pipe dimensions and tolerancesISO 4427SDR 11, SDR 17, SDR 26
    System conformity for potable waterEN 12201CE marking basis within EU pressure pipe scope
    Oxidative disinfectant validationASTM F2263Only required above 3 mg/L free chlorine

    What Limits Low-Sag Thick-Wall Pipe Extrusion Line Speed?

    The dominant constraint in thick-wall large-diameter pipe production is gravitational sag of the melt between the die exit and the first vacuum calibration sleeve. HE3493-LS is classified as a low-sag compound because the bimodal molecular weight distribution raises melt strength under elongational deformation without a corresponding rise in melt temperature. Thick-wall geometries with SDR 7.4 and SDR 9 are produced for high-pressure trunk mains where wall thickness can exceed 60 mm at diameters above DN 500 mm. Die exit melt temperature is held inside the 215 °C to 235 °C window; temperatures above 240 °C initiate oxidative degradation and create gel defects, while temperatures below 205 °C raise die swell and produce surface melt fracture. The cooling water entering the vacuum calibration tank is set between 15 °C and 25 °C; lower temperatures can quench the outer wall and lock in residual stress, and higher temperatures reduce the solidification rate and prolong the sagging window. Vacuum levels in the calibration sleeve normally range from 0.3 bar to 0.8 bar negative pressure, adjusted by ultrasonic wall thickness scanning around the circumference. A production-scale line for DN 800 mm SDR 11 pipe frequently operates at line speeds below 1 m/min; the exact speed is set by the cooling length, water spray arrangement, and haul-off force limits. Wall eccentricity control at these dimensions is maintained by closed-loop ultrasonic measurement, with a plant-specific target of less than 10% deviation from nominal wall thickness. Rapid crack propagation resistance remains a design requirement because large-diameter mains can transport cold water at low temperatures; qualification follows ISO 13477 at 0 °C or lower. Terminal outputs include high-pressure water transmission mains, subaqueous intake and outfall lines, and large-diameter industrial cooling water feeders.

    Before HE3493-LS is specified for industrial pressure piping, the conveyed medium is evaluated at the maximum continuous operating temperature because HDPE can undergo environmental stress cracking, permeation, and oxidative degradation. HDPE is resistant to dilute inorganic acids, caustic solutions, and many aqueous salt solutions at ambient temperatures, but the same material is unsuitable for continuous contact with aromatic hydrocarbons, chlorinated solvents, and strong oxidising acids, particularly above 40 °C. Chemical resistance ratings are obtained from ISO/TR 10358 and plant-specific immersion tests; a safety factor of 0.5 is applied to hydrostatic design stress when the medium is classified as partially resistant. Butt fusion joints follow ISO 21307 or DVS 2207-1, and hot-plate temperature is maintained at 200 °C to 220 °C. The compound is used at 100% virgin concentration for critical industrial service; regrind is excluded unless the same chemical resistance class and clean production history are documented. Pipe supports and flange connections are designed to limit excessive axial compressive loading because HDPE has a lower modulus than steel and will expand under elevated temperature cycles. Terminal applications include industrial wastewater force mains, acid and alkali transfer lines in treatment plants, chemical plant drainage headers, and cooling water return piping. For oxidizing media such as sodium hypochlorite above 5 g/L active chlorine, published data for this specific configuration is limited, and lifetime testing under representative pressure and temperature is required before specification.

    Trenchless Liner Collapse Resistance under External Hydrostatic Pressure

    Under external groundwater pressure after close-fit sliplining, collapse resistance is governed by Timoshenko long-cylinder buckling under uniform external pressure, with failure pressure reduced by ovality, wall thickness tolerance, and long-term creep modulus. HE3493-LS is selected for pressure-rated renovation liners because the PE100 classification provides a defined long-term modulus basis for buckling calculations when combined with installation standards such as ASTM F585 and system standards for water or sewer rehabilitation. The liner is butt-fused on site into continuous lengths, winched into the host pipe, and re-pressurised to test the jointing system; pull-in force is calculated from pipe unit weight, buoyancy, and friction coefficient, while maximum allowable pulling stress is limited to less than 15% of short-term yield stress to prevent necking. Grouting of the annular space, when specified, is executed in controlled lifts with pressure held below the calculated critical buckling pressure; a common control limit is below 2 bar for grout injection unless a buckling analysis supports a higher value. The final liner serves as a pressure-rated water, sewer, or industrial main inside deteriorated concrete, cast iron, or steel host pipes.

    When Abrasive Slurries Replace Clear Water in Pressure Pipe Networks

    In mining and dredging slurry transport, the failure mechanism shifts from hydrostatic rupture to erosive wall loss, particularly in mineral tailings and dredged material lines. HE3493-LS retains the PE100 hydrostatic classification, but slurry lines require a sacrificial wear allowance added to the pressure-calculated wall thickness. Flow velocity is the single largest operational variable; velocities below 2 m/s may cause solids deposition in horizontal sections, while velocities above 7 m/s accelerate wall erosion at elbows and fittings. Solids loading in mineral processing often reaches 30 wt% to 40 wt%; published data for this specific configuration is limited, and local wear tests with representative particle size distribution and pH are used to confirm the selected wall thickness. Joints are made by butt fusion to ISO 21307, with electrofusion couplers for repair tie-ins; flanged adaptors connect to pumps and valves. Regrind addition is held below 5 wt% in slurry service because contamination from embedded mineral fines can create point defects. Terminal components include mining tailings discharge lines, dredge discharge floating and submerged lines, fly ash conveyance lines, and abrasive process water return headers.

    Cyclic Pressure Fatigue in Irrigation Pump Main Service

    For irrigation pump mains, service loading is dominated by repeated surge and start-stop events rather than steady hydrostatic stress. HE3493-LS is fabricated into buried SDR 17 and SDR 21 pipe strings, with nominal pressure ratings of 10 bar and 8 bar for water at 20 °C. Pressure surge allowance is evaluated against the PE100 design envelope; occasional peak pressures of 1.5 times nominal pressure are permitted for short-duration events, but continuous pressure cycling above 1.2 times nominal requires fatigue evaluation according to project-specific surge analysis and long-term strength data from ISO 9080. The black UV-stabilised compound permits above-ground valve stations and pivot supply risers, though dark surface temperatures in full sunlight can reach 60 °C to 70 °C, and pressure derating above 20 °C is applied. Terminal products include drip irrigation mainlines, center-pivot and linear-move supply lines, pump discharge manifolds, and low-pressure transfer mains for agricultural reuse water.

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    Certification & Compliance
    More Introduction

    Borealis HDPE HE3493-LS is a bimodal high-density polyethylene compound classified as a PE 100 pressure pipe material under ISO 9080:2012 and ISO 12162:2022. The designation identifies a high-density ethylene-α-olefin copolymer produced with a controlled molecular weight distribution: a low molecular weight fraction contributes shear thinning and melt extension during extrusion, while a high molecular weight fraction supplies tie molecules that resist slow crack growth at pipe surface defects. The compound exhibits a minimum required strength of 10.0 MPa at 20 °C for 50 years, a density of approximately 959 kg/m³ under ISO 1183-1:2019, and a melt flow rate at 190 °C under a 5 kg load of typically 0.23 g/10 min under ISO 1133-1:2022. The primary difference from conventional unimodal HDPE lies in this bimodal molecular weight distribution, which increases low-shear melt strength for large-diameter pipe without reducing long-term hydrostatic strength.

    Material Property Ceilings and Standardized Test Data

    The following values are typical lot averages from manufacturer technical literature and are not independent specification limits. The grade is normally supplied as a black compound for ultraviolet stabilization, although natural forms may be available where the converter operates color-dosing equipment. In black compound, carbon black content is controlled at 2.0–2.5 % by mass under ISO 6964:2019, and dispersion is assessed under ISO 18553:2002. Short-term mechanical values are measured on compression-moulded plaques or extruded specimens after conditioning; pipe producers should use these values only for material acceptance screening, not for replacing long-term pipe pressure testing.

    PropertyTest methodTypical value
    DensityISO 1183-1:2019959 kg/m³
    Melt flow rate at 190 °C and 5 kgISO 1133-1:20220.23 g/10 min
    Tensile stress at yieldISO 527-2:201225 MPa
    Elongation at breakISO 527-2:2012>600 %
    Flexural modulusISO 178:20191000 MPa
    Carbon black contentISO 6964:20192.0–2.5 %
    Oxidation induction time at 210 °CISO 11357-6:2018>20 min
    Minimum required strength at 20 °C for 50 yearsISO 9080:201210.0 MPa
    Hydrostatic design stressISO 12162:20228.0 MPa

    Because HE3493-LS is classified as PE 100, the governing long-term value is the minimum required strength of 10.0 MPa. The hydrostatic design stress of 8.0 MPa at 20 °C is the water-service design value; gas-service design requires additional design factors and national standards.

    What Limits Extrusion Throughput in Large-Diameter Pipe Production?

    On production-scale single-screw extruders with grooved feed zones and L/D ratios between 30:1 and 36:1, throughput is governed by feed-zone efficiency, melt temperature uniformity, and die-head pressure rather than by the melting capacity of the screw alone. HE3493-LS processes at barrel settings from 180 °C to 210 °C, with melt temperature at the adapter and die controlled between 200 °C and 220 °C. If the feed throat is not maintained below 40 °C, softened granules can bridge in the grooved bushing, producing melt pressure oscillations of ±5 % or greater and visible wall-thickness variation in the finished pipe. At the die lip, the low-sag character of the grade permits thicker wall sections to be extruded without uncontrolled flow; this is relevant for outside diameters above 500 mm and SDR values below 11. The shear-thinning response of the bimodal molecular weight distribution reduces apparent melt viscosity at extrusion shear rates, but die head pressure remains sensitive to tooling geometry. Excessive melt temperature above 230 °C, particularly for residence times longer than 30 min, depresses oxidation induction time and may produce surface pitting.

    Because HDPE is not hygroscopic, desiccant drying is not required. Surface moisture from condensation can be removed by allowing the material to reach ambient temperature before processing or by drying at 80 °C for 4 h only when free water is visible.

    When Hydrostatic Design Basis Governs Pipe Wall Selection

    For buried pressure pipe, wall thickness is calculated from the hydrostatic design basis rather than from short-term tensile yield. Under ISO 12162:2022, HE3493-LS carries a design stress of 8.0 MPa at 20 °C; this is the stress used to derive pressure ratings for water service. A pipe manufactured to SDR 11 has a nominal pressure rating of approximately 16 bar at 20 °C for water, while SDR 17 gives approximately 10 bar. These values assume butt-fusion joints made according to ISO 21307:2017 or electrofusion joints installed to the fitting manufacturer’s protocol. Long-term hydrostatic strength under ISO 9080:2012 is evaluated at elevated temperatures and extrapolated to 50 years; the lower prediction limit must remain above the MRS. The bimodal architecture shifts the ductile-to-brittle transition to longer times, which permits the same pipe to survive higher hoop stress than a PE 80 material, whose design stress is limited to 6.3 MPa at 20 °C.

    Municipal potable water distribution is the principal application for HE3493-LS solid-wall pipe from 32 mm to greater than 1200 mm outside diameter. The grade is also extruded into wastewater rising mains, industrial slurry lines, and natural gas distribution pipe where national standards permit PE 100 materials. For potable water contact, the finished pipe must meet the applicable national scheme, such as EN 12201-1 and EN 12201-2 in Europe or local drinking water approvals, because the resin alone does not confer product certification. In chlorinated water service with residuals above 2 mg/L at continuous temperatures above 40 °C, oxidative degradation interacts with slow crack growth; published data for this specific configuration are limited, and project-specific validation under ASTM F2263 or an equivalent oxidative test is required. The material is joined by butt fusion at heater plate temperatures from 200 °C to 230 °C and by electrofusion, with cooling per fitting manufacturer instructions.

    For natural gas distribution, the resin classification is not sufficient to establish pressure rating. Gas pipe specifications such as ISO 4437 and EN 1555-1 require the finished pipe to demonstrate rapid crack propagation arrest under ISO 13477:2005, ISO 13478:2005, or full-scale tests. Published data for HE3493-LS in these exact configurations are limited, so pipe producers must validate the extruded pipe and jointed system rather than rely solely on the PE 100 resin designation.

    Regulatory compliance for potable water and gas pipe is product-specific. The compound may be evaluated under EN 12201-1, EN 12201-2, ISO 4427-1, and ISO 4427-2 for water service, and under ISO 4437 for gas distribution. National drinking water approvals are pipe-level certifications and depend on the converter’s formulation and extrusion conditions. Under European Union Regulation (EC) No 1907/2006 REACH, polyethylene is exempt from polymer registration, but monomer and additive registrations remain the responsibility of the supplier. The compound is not expected to contain lead, cadmium, mercury, hexavalent chromium, or brominated flame retardants above the maximum concentration values of Directive 2011/65/EU; however, compliance documentation should be verified for the specific lot.

    Benchmarking HE3493-LS Against PE 80 and Monomodal PE 100 Grades

    A comparison with PE 80 and monomodal PE 100 clarifies the position of HE3493-LS in extruded pressure pipe. PE 80 materials are limited to an MRS of 8.0 MPa and a design stress of 6.3 MPa; they therefore require thicker walls for the same pressure rating and outside diameter. Monomodal PE 100 grades achieve the 10.0 MPa MRS but may have lower low-shear melt strength because a narrower molecular weight distribution reduces the elastic component needed to resist sag in thick-wall, large-diameter extrusion. HE3493-LS retains the PE 100 MRS while the bimodal molecular weight distribution improves sag resistance and slow crack growth performance. The LS suffix in the Borealis designation identifies low-sag rheological behavior for large-diameter pipe, not a separate MRS class.

    Classification parameterPE 80Monomodal PE 100HE3493-LS
    Minimum required strength under ISO 9080:20128.0 MPa10.0 MPa10.0 MPa
    Hydrostatic design stress under ISO 12162:20226.3 MPa8.0 MPa8.0 MPa
    Molecular architectureunimodal or lightly bimodalunimodalbimodal
    Low-sag behavior in thick-wall extrusionlimitedmoderatespecified by LS designation
    Notched pipe test under ISO 13479pressure derating may be requiredpasses general PE 100 requirementspasses general PE 100 requirements; PE 100-RC not implied

    For trenchless installation and point-load applications, PE 100-RC grades are evaluated under ISO 13479 and may carry additional resistance designations. HE3493-LS does not automatically carry a PE 100-RC classification; such performance must be confirmed by the finished pipe manufacturer.

    In service, the operational boundary is defined by the hydrostatic design stress and the chemical environment. Continuous exposure to strong oxidizers, aromatic hydrocarbons, or hydrocarbon condensates can plasticize or oxidize the pipe and reduce long-term strength; direct contact with PVC decomposition products during recycling should be avoided because residual hydrogen chloride can cause acid-catalyzed degradation. The material is not intended for injection molding or thin-wall film extrusion; its low melt flow rate would require excessive injection pressure and would retain high orientation. Field-production experience shows that the most common extrusion defects are sharkskin melt fracture at high shear rates, die-lip build-up from degraded polymer at excessive die temperatures, and wall-thickness variation caused by feed-throat temperature above 40 °C or by surging from worn screw elements. These defects are minimized by maintaining melt temperature below 230 °C, controlling die land shear rate, and verifying screw and barrel wear against the extruder manufacturer’s tolerances.

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