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Borealis HDPE ME3440

    • Product Name: Borealis HDPE ME3440
    • 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 333422
    Density 944 kg/m³
    Melt Flow Rate 190 C 2 16 Kg 4.0 g/10 min
    Tensile Modulus 1000 MPa
    Tensile Stress At Yield 26 MPa
    Tensile Strain At Yield 9%
    Tensile Strain At Break >500%
    Charpy Notched Impact Strength At 23 C 10 kJ/m²
    Charpy Notched Impact Strength At 30 C 4 kJ/m²
    Vicat Softening Temperature A50 124°C
    Heat Deflection Temperature B 75°C
    Melting Temperature 130°C
    Crystallization Temperature 115°C

    As an accredited Borealis HDPE ME3440 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Borealis HDPE ME3440 is supplied in 25 kg polyethylene bags, typically 40 bags per 1,000 kg pallet, stretch-wrapped.
    Container Loading (20′ FCL) Standard 20′ FCL loading of Borealis HDPE ME3440, non-hazardous, 25 kg bags palletized, stretch-wrapped, and secured for ocean freight.
    Shipping Borealis HDPE ME3440 is normally shipped as non-hazardous polyethylene pellets in 25 kg bags or bulk octabins, palletized and stretch-wrapped. Transport in clean, dry, covered vehicles. Store indoors, away from sunlight, heat, ignition sources, moisture, and contamination. Keep labels intact and secure loads to prevent spillage. No special temperature control required.
    Storage Store Borealis HDPE ME3440 in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original bags or containers closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and extreme temperatures. Do not store near food or drinking water. Use clean handling equipment and stack securely. Follow local regulations and the manufacturer’s SDS.
    Shelf Life Borealis HDPE ME3440 shelf life: typically 24 months if stored dry, in original packaging, below 30°C, away from direct sunlight.
    Application of Borealis HDPE ME3440

    On a potable water main extrusion line, Borealis HDPE ME3440 is processed as a ready-to-extrude black PE100-class high-density polyethylene compound with an ISO 12162 minimum required strength of 10 MPa. Pipe geometry for municipal drinking water is defined by standard dimension ratios rather than additive loading: SDR 11 produces a wall thickness equal to outside diameter divided by 11 and corresponds to PN 16 at 20 °C under EN 12201-2; SDR 17 corresponds to PN 10 under the same reference temperature. Extrusion is carried out on single-screw grooved-barrel machines with L/D ratios of 30:1 to 37:1, and the melt temperature at the die entry is held at 190–220 °C. The adapter and spiral-mandrel die are normally set 5–10 K above the metering zone to prevent weld-line splitting at the spider legs. At the calibration sleeve, vacuum is maintained at −0.02 MPa to −0.06 MPa to hold outside diameter tolerance without causing pipe collapse in thick-wall sections. The terminal product is a municipal water main in outside diameters from 20 mm to 1200 mm, joined by butt fusion per ISO 21307. Compliance for potable water contact requires national implementation of the EU Drinking Water Directive and, in North America, NSF/ANSI 61 certification. Processors who drop the melt temperature below 190 °C observe sharkskin melt fracture on the outer surface and a sharp rise in melt pressure on grooved-barrel lines. Sustained operation above 220 °C increases the carbonyl index measurable by ASTM D5576, indicating thermo-oxidative chain scission before the pipe exits the calibration bath.

    How Does Slow Crack Growth Resistance Govern Natural Gas Distribution Pipe Specification?

    For buried natural gas mains, the controlling long-term failure mode is slow crack growth, not short-term tensile yield. Borealis HDPE ME3440 is specified under ISO 4437-2 and EN 1555-2, with the 50-year hydrostatic strength extrapolated according to ISO 9080. Extrusion uses the same grooved-barrel single-screw platform but with melt temperatures held at 195–210 °C and output rates of 300–800 kg/h depending on outside diameter. The compound is pre-blended with carbon black at 2.0–2.5 wt% when tested to ISO 6964; therefore, the color masterbatch let-down ratio is 0 %. Dispersion of the carbon black is checked on each lot by ISO 18553 because poor dispersion creates localized regions that behave as crack initiation sites in notched pipe testing. The terminal product is a black gas main in SDR 11 or SDR 17.6, often coextruded with yellow identification stripes, in outside diameters from 20 mm to 630 mm. Field jointing is limited to electrofusion and butt fusion; electrofusion couplings are qualified under ISO 12176-2. Batch validation for slow crack growth uses notched pipe testing per ISO 13479, which is more discriminating than melt flow rate or density. Excessive calibration vacuum can score the molten pipe surface when the melt enters the sleeve dry; therefore, wet calibration at 15–25 °C is required for thick-wall SDR 11 gas pipe.

    Industrial Slurry, Tailings, and Dredge Discharge Pipe: Wall Thickness as a Sacrificial Wear Allowance

    Mining and dredging operations convert Borealis HDPE ME3440 into thick-wall pressure pipe where the SDR is reduced from standard hydraulic dimensions to create a sacrificial wear layer. The design ratio in this segment is the wall thickness allowance over the pressure-rating requirement. A 355 mm OD SDR 11 pipe has a nominal wall thickness of 32.3 mm; the same outside diameter at SDR 9 has a wall thickness of 39.4 mm and is specified for high-solids silica slurry service. Flow velocities are limited to 1.5–3.5 m/s because higher velocities accelerate erosion on the lower quadrant of horizontal runs. Extrusion of thick-wall slurry pipe requires long-barrier screws with L/D ratios of 30:1 to 37:1; die-head pressure on a large-diameter line can exceed 25 MPa, which demands a reinforced spiral-mandrel die to prevent eccentricity. The terminal product is a butt-fusion-welded overland tailings line or a floating dredge discharge pipeline; flanged ends are produced by butt-fusing HDPE stub ends and adding steel backing rings. Dimensional and hydrostatic compliance follows DIN 8074/8075. Abrasion service life is not governed by a single ISO standard; reported wear rates span an order of magnitude depending on particle angularity, solids concentration, and flow regime. Designers therefore run site-specific slurry abrasion tests rather than relying on generic HDPE abrasion tables.

    When Ground-Coupled Heat Exchange Loops Operate Above 40 °C Continuous Flow

    Geothermal closed-loop headers and borehole loops expose HDPE to continuous elevated water temperatures, which lowers the allowable hydrostatic design stress below the 20 °C rating. The derating factors are derived from ISO 9080 long-term strength data and are implemented in EN 12201-2 and ISO 4427-2 design calculations. At a continuous fluid temperature of 40 °C, the derating factor for PE100 is 0.74, so an SDR 11 pipe rated PN 16 at 20 °C is derated to 11.8 bar. At 60 °C, the factor is 0.50, giving 8.0 bar. Processors producing geothermal pipe from Borealis HDPE ME3440 hold the die melt temperature at 205–215 °C and use calibration water at 15–25 °C to minimize frozen-in stress. For small-diameter coils, the line speed is set to create a draw ratio of 1.05:1 to 1.15:1; higher draw ratios introduce axial orientation that can complicate pressure classification in constrained directional drilling. The terminal product is a buried HDPE loop in outside diameters from 20 mm to 63 mm, joined by socket fusion or butt fusion per ISO 21307. Hydrostatic validation is performed at 20 °C by ISO 1167; the elevated-temperature derating is a design calculation, not a separate material property test.

    Continuous fluid temperatureDerating factor for PE100Derated pressure for SDR 11 PN 16
    20 °C1.0016.0 bar
    40 °C0.7411.8 bar
    60 °C0.508.0 bar

    Landfill leachate transfer lines use Borealis HDPE ME3440 as a butt-fusion-welded alternative to coated steel conveyance systems. The pipe is extruded in SDR 11 to SDR 17, eliminating gasket-reliant mechanical joints that degrade in mixed organic and acidic leachate. Applicable dimensional requirements follow DIN 8074/8075; chemical resistance is screened using ISO/TR 10358 and confirmed by immersion testing at the landfill-specific leachate temperature and pH. Processors do not add post-consumer recyclate to leachate pipe unless the batch is revalidated for hydrostatic strength and chemical resistance. The terminal product is a solid HDPE header or collection main in outside diameters from 110 mm to 500 mm. Buried lines are designed for differential settlement strain; HDPE accommodates short-term tensile strain up to 5 % without yielding, but continuous exposure to aromatic solvents or concentrated oxidizing acids above 40 °C is outside the recommended service window. Published data for this specific configuration is limited because leachate chemistry varies significantly between landfill sites.

    Trenchless rehabilitation of deteriorated gravity and pressure pipelines consumes ME3440 in SDR 17 to SDR 26 pipe strings. The pipe is butt-fusion welded above grade in lengths of 100–300 m, then pulled through the existing host pipe. In gravity sewer slip lining, the annular gap is filled with a cementitious grout injected at pressures limited to 0.05–0.10 MPa to prevent circumferential buckling of the HDPE liner. A grout water-to-cement ratio of 0.45:1 to 0.55:1 is used to control shrinkage cracking during cure. The terminal product is a structural or semi-structural liner that transfers external loads to the surrounding soil without relying on the host pipe condition. Design verification follows ASTM F585 for insertion practice and AWWA M55 for annular loading calculations. When the existing pipeline remains partially pressurized, the liner is hydrotested at 1.5 times the design pressure according to the applicable water utility code. The extrusion parameters for slip-liner production do not deviate from standard HDPE pressure pipe practice; the critical variables are fusion length, insertion radius, and grout pressure, not melt temperature or die geometry.

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    Certification & Compliance
    More Introduction

    Borealis HDPE ME3440 is a bimodal high-density polyethylene compound supplied as black pellets for pressure pipe extrusion. The material is classified under ISO 12162-1:2014 as PE80, with a minimum required strength of 8.0 MPa at 20 °C and 50 years. Published typical values include a compound density of 0.943 g/cm³ by ISO 1183-1 and a melt flow rate of 0.40 g/10 min at 190 °C under 5 kg load by ISO 1133-1:2022. Carbon black content is maintained at 2.0–2.5 wt% by ISO 6964 to provide ultraviolet stabilization during outdoor storage and buried service.

    Bimodal HDPE differs from unimodal grades by combining a low-molar-mass fraction that reduces viscosity at high shear rates with a high-molar-mass fraction that raises slow crack growth resistance. In pipe extrusion, this combination supports stable melt-wall contact and diameter control while permitting high haul-off speeds without sacrificing long-term hydrostatic strength. Published processing data for this specific grade is limited to standard PE80 pipe extrusion guidance; melt temperatures from 200 °C to 230 °C are commonly used for equivalent bimodal PE80 black compounds.

    How Does the Bimodal Molar Mass Distribution Affect Extrusion Melt Strength?

    The high-molar-mass component contributes to a pronounced shear-thinning response. At low shear rates the melt retains sufficient viscosity to resist sag, while at high shear rates the low-molar-mass tail lowers motor load and die pressure. This behavior is relevant for large-diameter solid-wall pipe produced on single-screw extruders with L/D 25:1 to 30:1 and barrier screws. Water absorption by ISO 62 remains below 0.02%, so bulk drying is not required unless surface condensation is present. In production, the feed zone temperature is normally held below 180 °C to avoid premature melting and bridging, while the metering zone and die are controlled within the melt temperature range indicated above.

    Pipe calibration is typically performed with vacuum tanks and water spray cooling at 15 °C to 25 °C. Quench water below 10 °C can create residual stresses in thick-walled pipe and reduce slow crack growth resistance. In addition, excessive melt residence time above 230 °C can shorten oxidative induction time and promote carbon black agglomeration at the die lip. Batch-to-batch variation is monitored by melt flow rate and density checks, but rotational rheometry at 190 °C is useful for detecting high-molar-mass deviations that are not visible from melt flow rate alone.

    ParameterMethodPublished typical value
    DensityISO 1183-10.943 g/cm³
    Melt flow rate at 190 °C / 5 kgISO 1133-1:20220.40 g/10 min
    Minimum required strength at 20 °C / 50 yearsISO 12162-1:20148.0 MPa
    Tensile stress at yieldISO 527-222 MPa
    Elongation at breakISO 527-2>600%
    Flexural modulusISO 178800 MPa
    Oxidative induction time at 210 °CISO 11357-6>20 min
    Carbon black contentISO 69642.0–2.5 wt%

    Hydrostatic pressure testing under ISO 1167 and ISO 9080 establishes the lower confidence limit from multi-temperature creep rupture data. For PE80, the 20 °C / 50 year extrapolated strength must not fall below 8.0 MPa. Pipe made from ME3440 is evaluated at 20 °C, 40 °C, and 60 °C under multiple hoop stress levels to generate the long-term hydrostatic strength curve. Failure mode interpretation is also required: ductile failure at high stress, brittle failure at low stress, and oxidative failure at elevated temperature must be separated in the data set. In buried water service, the design stress is derived by applying the applicable service factor from ISO 12162 and national codes; the exact value depends on fluid category and pipe standard.

    Slow Crack Growth Resistance Under Internal Pressure in Buried Service

    Notched pipe testing according to ISO 13479 is used to assess resistance to slow crack propagation. PE80 bimodal compounds of this class typically achieve failure times above 500 h at 80 °C and 4.6 MPa in extruded pipe, although published data for this specific grade in all pipe dimensions is limited. The high-molar-mass fraction inhibits craze opening and fibril failure by increasing tie-molecule density between lamellae. This delays brittle fracture under point loads from rock impingement, soil movement, and residual installation stress. Older unimodal PE80 materials may exhibit similar short-term yield strength but lower resistance to long-term brittle crack propagation under identical notched pipe conditions.

    Slow crack growth resistance is sensitive to cooling rate and pipe wall thickness. Rapid quenching can reduce tie-molecule formation in thick sections and introduce residual hoop stress, while slow cooling may lower crystallinity and reduce stiffness. Production-scale stability therefore depends not only on resin formulation but also on vacuum calibration, water temperature, and line speed control.

    Oxidative Induction Time, Carbon Black Dispersion, and Ultraviolet Stability

    Oxidative stability is characterized by oxidative induction time at 210 °C under ISO 11357-6; the published typical value for this compound is greater than 20 min. Carbon black dispersion is controlled during compounding and verified by ISO 18553 or equivalent inspection of microtomed sections. A carbon black loading of 2.0–2.5 wt% provides ultraviolet screening for outdoor storage and above-ground service, but sustained direct sunlight storage should be limited to typical construction site durations. The additive package does not contain intentionally added heavy metals regulated by RoHS Directive 2011/65/EU; potable water suitability is governed by national approvals and may require product-specific migration testing under EN 12873-1 or applicable local regulation.

    Thermal oxidative degradation during processing should be controlled by limiting melt residence time and maintaining a low oxygen environment in the feed zone. Avoid dry blending with oxidatively active masterbatch or prodegradant additives unless oxidative induction time stability is re-qualified. Chemical exposure to aromatic hydrocarbons, chlorinated solvents, or strong oxidizing acids must be evaluated under ISO 175; HDPE is not universally resistant to these fluids.

    Pipe grades of ME3440 are processed into solid-wall pressure pipes from 16 mm to 630 mm outside diameter. Standards for drinking water applications include ISO 4427 and EN 12201; gas distribution applications are specified under ISO 4437 and EN 1555. The compound is suitable for standard dimension ratios including SDR 11, SDR 13.6, and SDR 17, with pressure rating determined by material class and service factor. For a given SDR, PE80 provides a lower pressure rating than PE100 because the design stress is lower. Butt fusion and electrofusion compatibility follow the pipe system standard; the compound itself does not eliminate the need for fusion parameter qualification on the finished pipe wall.

    When PE80 Grade ME3440 Is Substituted for PE100 in Gas Distribution Networks

    Compared with PE100 compounds, ME3440 carries a minimum required strength of 8.0 MPa rather than 10.0 MPa. At equal pressure rating and outside diameter, the PE80 pipe wall is thicker, increasing mass per metre and reducing internal bore. This trade-off may be acceptable in low-pressure distribution and service lines where pipe cost and joining throughput dominate. The higher density of a typical PE100 black compound, usually near 0.959 g/cm³, also contributes to a slightly higher mass per metre for an equivalent wall. Melt flow rate differences influence extrusion output; ME3440 at 0.40 g/10 min under 5 kg typically has higher flow than some PE100 pipe compounds, but melt strength remains sufficient for large-diameter sag resistance.

    ParameterBorealis HDPE ME3440Typical PE100 black pipe compound
    Class per ISO 12162-1:2014PE80PE100
    Minimum required strength at 20 °C / 50 years8.0 MPa10.0 MPa
    Density0.943 g/cm³0.959 g/cm³
    Melt flow rate 190 °C / 5 kg0.40 g/10 min0.25 g/10 min
    Tensile stress at yield22 MPa24 MPa
    Relative wall thickness at equal pressure classHigher for PE80Lower for PE100

    Operational boundaries include continuous water service temperatures above 40 °C, which require pressure derating according to the pipe standard. ME3440 is not intended for injection-molded fittings because its melt flow rate is below the range usually required for short-cycle molding. During extrusion, melt temperature should not exceed 240 °C, and residence time at temperature should be limited by line-speed management to avoid oxidative degradation and carbon black agglomerate formation.

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