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PetroChina Dushanzi HDPE TUB121N3000M

    • Product Name: PetroChina Dushanzi HDPE TUB121N3000M
    • 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 581405

    As an accredited PetroChina Dushanzi HDPE TUB121N3000M factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PetroChina Dushanzi HDPE TUB121N3000M is supplied in 25 kg woven bags, with 40 bags per pallet, totaling 1,000 kg.
    Container Loading (20′ FCL) 20′ FCL container: PetroChina Dushanzi HDPE TUB121N3000M, 25 kg PP bags, palletized, stretch-wrapped, floor-loaded, maximum payload, secured for ocean export.
    Shipping PetroChina Dushanzi HDPE TUB121N3000M is a non-hazardous high-density polyethylene resin. Normally shipped in 25 kg bags or 1000 kg jumbo bags, palletized and shrink-wrapped, or in bulk. Not regulated for transport (no UN number). Keep dry, clean, and protected from sunlight, heat, moisture, and contamination during storage and handling.
    Storage Store PetroChina Dushanzi HDPE TUB121N3000M in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original bags closed and palletized to prevent moisture, dust, and contamination. Do not store outdoors. Avoid prolonged UV exposure and excessive stacking pressure. Maintain clean handling areas and follow local regulations and supplier recommendations.
    Shelf Life Shelf life is typically 24 months from production when stored dry, cool, ventilated, in original sealed packaging, away from sunlight.
    Application of PetroChina Dushanzi HDPE TUB121N3000M
    PetroChina Dushanzi HDPE TUB121N3000M is converted into pressure pipe through annular die extrusion in which the long-term hydrostatic strength classification, not short-term tensile elongation, governs the allowed design stress. In a solid-wall potable water line, the resin is fed into a grooved-barrel single-screw extruder with an L/D ratio between 30:1 and 36:1; a barrier screw with a shear mixing section is normally specified to homogenize the melt before the screen pack and spiral mandrel die. The melt temperature at the die is maintained within a narrow band, typically 200 °C to 230 °C, to prevent thermal oxidation while ensuring adequate melt strength during vacuum calibration. The resulting pipe is assessed under ISO 4427-2 and ISO 4427-3 for wall thickness, ovality, and hydrostatic pressure resistance; the material classification rests on the ISO 9080 and ISO 12162 framework, in which PE100 materials exhibit a minimum required strength of 10 MPa at 20 °C for a 50-year service life in water. Butt fusion and electrofusion joints are accepted only when the machining and heating cycles follow the fusion machine supplier’s interfacial pressure tables, because a generic weld pressure cannot be transferred across diameters and SDR classes without risking cold fusion or excessive melt displacement. Dimensional control on production lines is influenced by the vacuum calibration tank and the first haul-off temperature; any variation in melt flow rate outside the producer’s specification will shift the die pressure and change the draw-down ratio.

    What Limits Slow Crack Growth in Buried Gas Distribution Pipe Resins?

    In natural gas distribution, the dominant failure mechanisms are slow crack growth under residual stress and rapid crack propagation under decompression waves; both mechanisms are governed by the resin’s molecular architecture and are checked with laboratory-scale or full-scale pipe tests. A PE100 pipe made from TUB121N3000M is given a pressure rating by the design stress derived from the minimum required strength and the appropriate service coefficient; SDR 11 and SDR 17.6 are common dimensions for gas mains and service lines, but the maximum operating pressure is not fixed by the resin alone. The S4 rapid crack propagation test described in ISO 13477 is performed at low temperature on notched pipe or pipe sections, and the arrest criterion ensures that a propagating crack does not travel long distances along the pipe run. Slow crack growth resistance is evaluated by the notched pipe test under elevated temperature hydrostatic loading, as defined in ISO 13479; the pipe must survive a specified number of hours at a stress that is high enough to discriminate PE100 from lower classifications. Gas composition moderates performance: condensed aromatic hydrocarbon fractions can permeate the pipe wall over time and may require chemical compatibility review before the same pressure rating is accepted for odorized gas, sour gas, or high-Btu streams with heavy fractions. Field defects introduced by electrofusion couplers, scraper damage, or butt fusion misalignment are often more severe than laboratory notches; therefore joint qualification follows ISO 4437-2 and EN 1555-2 for gas systems, with inspection by phased array ultrasonic testing in critical mains.

    StandardTest scopeConditionRelevance to TUB121N3000M
    ISO 9080Long-term hydrostatic strength20 °C waterPE100 MRS of 10 MPa
    ISO 12162Polyethylene grade classificationExtrapolation from ISO 9080 dataPE100 design stress basis
    ISO 13477Rapid crack propagation S4 testLow-temperature pipe testArrest criterion for gas network design
    ISO 13479Slow crack growth notched pipe testElevated temperature hydrostatic loadingDiscrimination of PE100 grades
    ISO 4437-2Buried polyethylene gas pipesGas distribution systemsMOP derived from MRS, SDR, service coefficient
    ISO 4427-2Polyethylene pipes for water supplyPotable and raw water systemsPressure rating and dimensional compliance
    During horizontal directional drilling and pipe-bursting upgrades, the pipe wall experiences longitudinal tensile stress, hoop stress from the borehole pressure, and external surface scoring from soil inclusions; the controlling parameter is not the short-term tensile strength at yield but the resin’s resistance to crack propagation from surface damage. For TUB121N3000M, installation design should follow ASTM F1962 or ISO 11298-2 as applicable, with pullback force calculated from borehole friction, buoyant weight, and the pipe’s allowable tensile stress during the installation window. The pipe is typically pulled as a fused string, and every butt fusion face is aligned to minimize an external bead that can increase pullback resistance; on production-scale HDD paths, the acceptable bending radius is commonly set at 25 to 40 times the outside diameter for solid-wall PE100 pipe, but the final limit must be confirmed by the producer’s short-term and long-term bending strain criteria. Hydrostatic pressure testing after pullback is recommended before connecting to the distribution network; testing at elevated temperature requires derating in accordance with the standard pressure-temperature relationship, with a derating factor near 0.7 at 40 °C for many water pipe standards. Published data specific to TUB121N3000M under long-term installation scratch conditions may be limited in public literature; a project-specific notched pipe ring test and FNCT screening can provide comparative validation when the bore path crosses rocky ground or compacted coarse fill.

    Industrial slurry, tailings transfer, and abrasive process water

    Mining and mineral processing plants apply HDPE pressure pipe to transfer fine tailings, reclaim water, and clarified process streams. The resin selection criterion is often the slurry abrasion resistance of the pipe wall under controlled flow velocities; for TUB121N3000M, the wall is used in the as-extruded condition with no internal lining, and the service life depends on particle size distribution, solids concentration by weight, flow velocity, and pipe orientation. More than one variable cannot be isolated: a reduction in slurry velocity below the critical deposition velocity creates a sliding bed that accelerates local wall loss, while an increase in velocity beyond the economic optimum increases frictional pressure drop and may intensify impingement wear at elbows. The use of HDPE rather than carbon steel is generally justified when the solids are fine and the pH is below the range where corrosion dominates; for sharp, freshly crushed quartz particles, rubber-lined steel or ceramic alternatives should be compared. Continuous exposure at ambient temperature to dilute acids and alkaline liquors is accepted; concentrated nitric acid, hot hypochlorite solutions, and strong oxidizing brines are excluded because they attack the polyethylene chain. Butt fusion welds in slurry service require post-weld bead cleanliness and, where possible, the use of long-radius fabricated bends to avoid bolt-on steel elbows that introduce internal turbulence at flange transitions.

    Landfill leachate transfer lines and process effluent headers impose a combination of internal pressure, aggressive aqueous chemistry, and long dwell times at near-ambient temperature. The main concern is environmental stress cracking when the pipe is exposed to wetting agents, organic acids, and settled leachate fractions; the resin should be screened against the full-notch creep test in accordance with ISO 16770 because the bent-strip ESCR test is not a direct substitute for pipe-grade slow crack growth performance. For TUB121N3000M, electrofusion saddles and couplers must be fused exactly at the manufacturer’s energy input because leachate service eliminates the possibility of compensating for a weak weld through internal pressure relaxation. The pipe is normally pressure-rated in the same manner as water or drainage force mains, but the engineer must apply the appropriate chemical resistance factor if the leachate contains high concentrations of aromatic hydrocarbons or solvent-like components that plasticize the amorphous fraction of the polymer. Visual inspection after first exposure does not capture long-term molecular weight degradation, so annual coupon extraction or in-line pressure decay testing is recommended in critical cells. Published data on this specific grade under leachate conditions is limited; conservative pressure derating and joint inspection intervals are advised until plant-specific validation is obtained.

    When TUB121N3000M is Coextruded as the Outer Layer of Multilayer Pipe

    Multilayer pipe production uses the resin as one of several melt streams in a coextrusion head; the driving requirement is rheological compatibility with the other polyethylene layers. If the grade is supplied with a bimodal molecular weight distribution and a carbon black masterbatch system, it can serve as the outer pressure-bearing layer over a core of recycled or transition material, provided the layer thickness ratio is sufficient to carry the design stress. Coextrusion dies are fitted with spiral mandrels or plate dies; the total output is divided across extruders sized according to the layer percentage, and melt pressure is balanced at the die entrance to prevent layer instability. For TUB121N3000M, the producer’s melt flow rate and shear viscosity curve should be compared with the adjacent layer compound at the same shear rate encountered in the die land; mismatches above a critical ratio produce visible weld lines or a nonuniform layer thickness that cannot be corrected by downstream sizing alone. The pipe wall must still conform to the applicable product standard, such as ISO 4427-2 or EN 12201-2 for water, and the outer layer must provide the UV stabilization expected for outdoor storage if the grade is black or otherwise stabilised. Multilayer constructions should not be used to hide lower-quality internal material when the pipe is intended for long-term pressure service unless the layer design is validated by full-scale hydrostatic tests on the finished wall.

    Fused outlet fabrication is a secondary conversion route for pressure-rated pipe sections

    Solid-wall pipe extruded from TUB121N3000M can be machined and fabricated into stub flanges, side-outlet tees, and blind flanges by cutting the pipe and butt-fusing injection-molded or extruded fittings under controlled heating plate temperature and fusion pressure; the resulting assemblies are tested according to ISO 13953 for weld tensile strength and ISO 4427-3 for pressure cycling.

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