Products

INEOS HDPE ELTEX TUB 124N2025

    • Product Name: INEOS HDPE ELTEX TUB 124N2025
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 949067

    As an accredited INEOS HDPE ELTEX TUB 124N2025 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing INEOS HDPE ELTEX TUB 124N2025 is supplied in 25 kg polyethylene bags, with 55 bags per pallet (1,375 kg total).
    Container Loading (20′ FCL) 20′ FCL container loaded with palletized 25 kg bags of INEOS HDPE ELTEX TUB 124N2025, securely strapped and evenly distributed.
    Shipping INEOS HDPE ELTEX TUB 124N2025 is a non-hazardous high-density polyethylene resin supplied as pellets. It ships in 25 kg bags, jumbo bags, or bulk containers. No dangerous goods classification or UN number is required. Keep dry, clean, and protected from heat and UV exposure during transport and storage.
    Storage Store INEOS HDPE ELTEX TUB 124N2025 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, and ignition sources. Keep original packaging sealed and pallets off the floor to prevent moisture and contamination. Avoid prolonged high temperatures and UV exposure. Maintain clean handling areas, rotate stock using first-in, first-out principles. Do not store outdoors or near strong oxidizers.
    Shelf Life Shelf life is typically two years when stored in original, unopened packaging under cool, dry conditions away from direct sunlight.
    Application of INEOS HDPE ELTEX TUB 124N2025

    In potable water pressure pipe extrusion, INEOS HDPE ELTEX TUB 124N2025 is processed as the base resin for PE100-class pressure pipe; melt mass-flow rate under ISO 1133-1:2022 condition T is typically in the range 0.20–0.30 g/10 min, and density under ISO 1183-1:2019 is in the range 0.955–0.960 g/cm³. Compliance for drinking-water pipe is assessed under EN 12201-1:2011+A1:2013 for compound properties and EN 12201-2:2011+A1:2013 Table 1 for SDR 11 and SDR 17 dimensions, with potable-water contact under NSF/ANSI/CAN 61:2022 Section 5 and organoleptic testing under EN 1622:2006. Where supplied as a natural compound for black pipe manufacture, the formulation is 100 parts by weight base resin and 5.0–6.25 parts by weight of a 40% carbon black masterbatch, yielding 2.0–2.5 wt% carbon black in the finished pipe wall as required by ISO 4427-1:2019 Annex B; for blue potable-water pipe, a phthalocyanine-blue masterbatch is dosed at 2–4 wt%, and carbon black is limited to co-extruded identification stripes. On a 60 mm grooved-feed extruder with L/D 33 and barrier screw, barrel zone setpoints for DN 110 SDR 11 are typically 180 °C, 195 °C, 205 °C, and 210 °C, die zones at 200–210 °C, and melt temperature at 190–220 °C. The spiral mandrel die feeds a vacuum calibration sleeve held at -0.3 bar, with water bath temperature at 15–25 °C; haul-off speed is set to 1.2–2.0 m/min for DN 110 SDR 11 and trimmed by ultrasonic wall-thickness measurement to hold wall thickness within ±0.2 mm. Melt temperature excursions above 230 °C accelerate thermo-oxidative degradation of the bimodal molecular weight distribution and reduce slow crack growth resistance under ISO 13479; hopper drying is required only when surface moisture exceeds 0.02%, normally at 80 °C for 2 h after storage at relative humidity above 60%. Terminal finished products are PE100 drinking-water pipes in DN 20–630 mm, SDR 11 and 17, black with extruded blue identification stripes or fully blue; DN 20–63 mm is coiled in 50 m, 100 m, and 150 m coils, while DN 75–630 mm is supplied in 6 m and 12 m straight lengths or fabricated spools.

    What limits slow crack growth in PE100 gas distribution pipe extrusion?

    Gas distribution pipe manufactured from INEOS HDPE ELTEX TUB 124N2025 is required to retain high resistance to slow crack growth and rapid crack propagation after extrusion, because buried gas mains operate under sustained hoop stress and seasonal ground movement. The governing system standards are ISO 4437-1:2014 for compound and pipe requirements, ISO 4437-2:2014 for dimensions, EN 1555-2:2011 Table 1 for SDR series, and ASTM D2513-20 for thermoplastic gas pressure pipe in North America. The blend is composed of 100 phr base polymer with 5.0–6.25 phr of a 40% carbon black masterbatch, producing 2.0–2.5 wt% carbon black in the pipe wall; external recyclate is excluded under EN 1555-1:2011, and only clean in-house rework up to 10% is permitted if dried and free of contamination. On 90 mm pipe lines with grooved feed and L/D 33, melt temperature is held at 190–220 °C, die head temperature at 200–210 °C, and for DN 90 SDR 11 output is typically 350–450 kg/h, vacuum calibration at -0.3 bar, and line speed at 1.8–2.4 m/min. Melt temperature at the die exit is monitored with an immersion thermocouple; excursions above 230 °C degrade the high-molecular-weight tail and are accompanied by downward shift in notched pipe test survival under ISO 13479, while insufficient thermal homogenisation can lower rapid crack propagation resistance under ISO 13477. Residence time in the extruder is kept below 15 min by matching screw speed to downstream demand, and melt pressure fluctuation is maintained within ±2% to avoid surge-induced wall-thickness variation. Finished products are PE100 gas pipes in DN 20–630 mm, SDR 11 and 17/17.6, black with co-extruded yellow identification stripes, supplied as coils up to DN 125 or as 6 m and 12 m straight lengths; fittings are produced from separate injection-moulding grades and are not extruded from this material.

    Where buried fibre-optic infrastructure is installed by trenchless methods, the HDPE duct wall must resist installation pull-in forces without necking and maintain a low-friction internal surface for cable blowing over long distances. Conduit compliance is evaluated under IEC 61386-24:2004 Clause 7 for underground conduit classification and EN 61386-24:2004 for mechanical performance; North American projects may additionally reference Telcordia GR-315-CORE for duct physical requirements. The formula uses 100 parts base resin with carbon black adjusted to 2.0–2.5 wt% in the wall; because high-speed microduct extrusion creates die drool and build-up, a fluoropolymer process aid may be added at 0.2–0.4 phr. No mineral filler is used, because filler increases brittle failure in microduct walls under bending radii below 200 mm. Multi-tube microduct bundle production requires individual single-screw extruders with grooved feed, L/D 24–30, and precision dies of 7/3.5 mm or 10/6 mm. Barrel zones are set at 190–220 °C, die at 200±5 °C, melt temperature at 195–215 °C, vacuum calibration at -0.15 to -0.3 bar, and water cooling at 12–20 °C. Line speeds are 30–80 m/min for 7/3.5 mm microducts and 15–40 m/min for 40/33 mm sub-ducts. Outer diameter is controlled by triple-axis laser gauges to ±0.05 mm; the cooling water temperature differential between first and last vacuum tank is held below 10 °C to limit residual stress and preserve roundness during coiling. Terminal products are colour-coded black, red, green, and blue HDPE microduct bundles in 7-way, 12-way, and 24-way configurations, 40/33 mm and 50/42 mm sub-ducts, and continuous coils of 1000–2000 m for fibre-optic trunk and distribution networks.

    Abrasion-Resistant HDPE Slurry Piping in Mineral Processing

    Mineral processing circuits use thick-wall HDPE pipe fabricated from bimodal high-molecular-mass resins because of resistance to wet abrasion and chemical attack in acid-leach slurries. Dimensional control follows DIN 8074:2011; long-term hydrostatic strength is evaluated under ISO 9080:2012, and in Australian installations AS/NZS 4131:2010 Section 5 governs pipe dimensions and pressure derating. Chemical resistance is checked against ISO/TR 10358:1993 for acid-leach slurries and reagents. The compound is charged at 100 parts base polymer, with carbon black maintained at 2.0–2.5 wt% for outdoor storage; where wall thickness exceeds 25 mm, a fluoropolymer process aid at 0.3–0.6 wt% is sometimes used to control melt pressure in high-shear grooved-feed extruders. No mineral filler is used because filler reduces butt-fusion weld quality and lowers elongational flexibility under slurry surge loading. Thick-wall pipe from DN 200 to DN 1200 is extruded on single-screw machines with L/D 30–36 and output 400–1200 kg/h. Barrel zones are set at 180 °C to 220 °C, die zones at 200–210 °C; because wall thickness exceeds 20 mm, residual stress is managed by stepped water cooling at 40 °C, 30 °C, and 20 °C, with vacuum sizing at -0.3 to -0.5 bar. Butt fusion joining for flanged ends uses 220±5 °C, 0.15 MPa interface pressure, and cooling to ambient under restraint per ISO 21307:2017; ovality is held below 2% by automated diameter logs. Published slurry abrasion data for this specific grade is limited; wear life in silica slurry depends on flow velocity, solids concentration, and particle impact angle. At flow velocities above 3 m/s, a sacrificial wall-thickness allowance is required, and sharp-edged particle slurries with impingement angles above 60° should be handled with rubber-lined spools or ceramic-lined sections rather than bare HDPE. Terminal products are solid-wall HDPE slurry pipelines DN 110–1200 mm, flange adapters, stub ends, HDPE-lined steel pipe sections, and rubber-lined spools for pump stations.

    When seasonal thermal cycling demands high-stress-crack resistance from ground-loop pipe

    Ground-loop heat exchanger pipe manufactured from INEOS HDPE ELTEX TUB 124N2025 is produced as solid-wall SDR 11 or SDR 13.6 pipe, then assembled into U-bend loops by butt fusion. The governing material standard is ISO 13275:2010 for polyethylene pipes and fittings for ground-source heat pump systems, with fusion compatibility verified under ISO 12176-1:2022 and pressure-rated dimensions under EN 12201-2:2011; North American installation practice may reference ASTM D3035 for outside-diameter-controlled PE pipe. The formulation is 100 parts base polymer with 2.0–2.5 wt% carbon black in the pipe wall; no colour masterbatch is used, and regrind from unknown sources is prohibited because geothermal pipe must remain fusion-weldable over decades. Lower-viscosity blending resins are avoided, since a reduction in high-molecular-weight fraction reduces slow crack growth resistance under cyclic thermal stress. Pipe is extruded in DN 20–50 mm, SDR 11 and 13.6. On a 45 mm or 60 mm grooved-feed extruder with L/D 30–33, barrel temperatures are 190–220 °C, die temperature 200–210 °C, vacuum -0.2 bar, and cooling water at 15–25 °C. For 32 mm SDR 11 pipe, line speed is typically 10–18 m/min; for 40 mm SDR 11, 8–14 m/min. Coil set is relaxed by storing coils at 5–30 °C for 24 h before U-bend assembly. Butt fusion at 220±5 °C with 0.15 MPa bead-up pressure and 10 min cooling for 40 mm SDR 11 is followed by visual bead inspection to ISO 12176-1:2022. Chlorine dioxide exposure above 1 ppm in the heat-transfer fluid should be avoided, and antifreeze solutions should use inhibited propylene glycol or ethanol per heat-pump manufacturer limits. Finished products are U-bend loops in DN 20–50 mm, horizontal and vertical borehole heat exchangers, manifold headers, and prefabricated coil bundles of 150 m and 300 m.

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