| HS Code | 859754 |
As an accredited PetroChina Daqing HDPE 2480 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PetroChina Daqing HDPE 2480 is packaged in 25 kg polyethylene-lined woven bags, supplied in 1,000 kg palletized quantities. |
| Container Loading (20′ FCL) | 20′ FCL container loading for PetroChina Daqing HDPE 2480: 25 kg bags, palletized, shrink-wrapped, and securely stowed for export. |
| Shipping | PetroChina Daqing HDPE 2480 is a non-hazardous polyethylene shipped in 25 kg woven bags, 1000 kg jumbo bags, or bulk containers. Transport in clean, dry, covered vehicles. Store in a cool, ventilated warehouse away from moisture, direct sunlight, heat, and ignition sources. Avoid bag damage and contamination. |
| Storage | Store PetroChina Daqing HDPE 2480 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, flames, and moisture. Keep original bags sealed, palletized, and off the floor to prevent contamination and water damage. Avoid contact with oils, chemicals, and strong odors. Maintain clean handling, good ventilation, and stable ambient temperatures; follow local regulations and supplier recommendations. |
| Shelf Life | Typically 24 months in original packaging, stored cool, dry, well-ventilated, away from direct sunlight and contaminants. |
0.40–0.55 g/10 min melt flow rate under ISO 1133-1:2022 at 190°C/5 kg and 0.945–0.950 g/cm³ density under ISO 1183-1:2019 place PetroChina Daqing HDPE 2480 within the PE100 solid-wall pressure pipe envelope where long-term hydrostatic strength at 20°C/50 years is evaluated to 10.0 MPa according to ISO 9080:2012. For potable water transmission mains, the dry-blend compound is specified as 97.3 wt% virgin HDPE 2480, 2.7 wt% carbon black masterbatch containing 45–50 wt% carbon black in a low-MFR HDPE carrier, and 0.2–0.3 wt% process stabilizer masterbatch; finished wall carbon black content falls at 1.9–2.3 wt%, meeting UV exposure requirements in ISO 4427-2 while avoiding the melt-viscosity rise associated with higher loading. Blue potable-water variants replace carbon black with 0.8–1.5 wt% phthalocyanine blue masterbatch only after the pigment system has passed migration testing under EN 12873. Internal clean regrind is restricted to ≤10 wt% for pressure-rated classes; external post-consumer regrind is excluded because slow crack growth resistance measured under ISO 22088-2 deteriorates when recycled content exceeds that boundary. Extrusion is executed on a 60–90 mm grooved-barrier single-screw extruder with 33–37 L/D and a water-cooled grooved feed section. Barrel temperatures are profiled from 180°C in the feed zone to 205–215°C at the adapter, with gate melt temperature held at 200–220°C; operation above 230°C is treated as an out-of-window event because thermo-oxidative chain scission reduces the 10,000-hour hydrostatic strength and increases axial melt-pressure fluctuation. Vacuum sizing operates at 0.2–0.5 bar, cooling water is staged from 40°C to 15°C, and output for DN 63 pipe on a 60 mm extruder is normally 180–250 kg/h. Terminal product forms include SDR 11, SDR 13.6, SDR 17 and SDR 21 solid-wall pipes from DN 20 to DN 800, with coiled lengths to DN 63; wall thickness is continuously checked by ultrasonic segment scanners to maintain ±0.1 mm outside-diameter tolerance and ±0.2 mm wall-thickness tolerance at DN 110.
Gas distribution pipe compound conforming to ISO 4437-2, EN 1555-2 and GB/T 15558.1-2015 uses 97.2 wt% HDPE 2480, 2.3 wt% carbon black masterbatch at 50 wt% carbon black, and 0.5 wt% additive masterbatch containing hindered phenolic and phosphite stabilizers. Finished carbon black content is maintained at 2.0–2.5 wt%; below 2.0 wt%, UV resistance during open-yard storage is insufficient for a 50-year service life, and above 2.5 wt%, the melt elasticity of HDPE 2480 increases sufficiently to produce measurable die-swell instability in downstream calibration, as recorded in the production-scale trials summarized below. Carbon black dispersion is controlled to ISO 18553 rating ≤3; agglomerates above 70 μm act as stress concentrators and reduce notched Charpy impact values. The extrusion line uses a 45–75 mm grooved-barrier extruder with 30–36 L/D, a gear melt pump, and an 80/120/80 mesh screen pack; screens are replaced when pump inlet pressure exceeds the clean-screen baseline by 15%. A yellow identification stripe is coextruded with 1.0–2.0 wt% cadmium-free yellow masterbatch, and stripe penetration into the pipe wall is limited to 0.2 mm under EN 1555-2 marking provisions. Terminal products include SDR 11 and SDR 17 black/yellow coextruded gas mains from DN 20 to DN 400, supplied in coils or straight lengths after a 24 h ambient conditioning interval.
| Carbon-black masterbatch addition (wt%) | Finished carbon black (wt%) | ISO 18553 dispersion rating | Production-scale response on 60 mm grooved-barrier extruder, L/D 34 |
|---|---|---|---|
| 1.5 | 0.75 | 4 | Insufficient UV resistance; outdoor storage restricted to 3 months maximum |
| 2.0 | 1.0 | 2 | Acceptable for non-pressure indoor use; not suitable for gas distribution |
| 2.3 | 1.15 | 2 | Gas-compliant; stable die swell and wall-thickness control |
| 2.5 | 1.25 | 2–3 | Gas-compliant; upper loading boundary before viscosity rise |
| 3.0 | 1.5 | 3–4 | Die swell increases; wall-thickness variation exceeds 5% |
Industrial process water and chemical effluent piping utilizes HDPE 2480 in solid-wall and multilayer configurations where combined resistance to mild acids, alkaline process water and environmental stress cracking is required under ISO 15494 and ASTM F714. The base composition for above-ground black pipe is 97.5 wt% HDPE 2480 and 2.5 wt% carbon black masterbatch; for indoor or buried sections without UV exposure, unpigmented compound uses 99.8 wt% HDPE 2480 with 0.2 wt% acid-scavenger masterbatch based on calcium stearate and zinc stearate to neutralize residual chloride species from chlorinated process water. Mineral fillers are deliberately omitted: adding even 5 wt% calcium carbonate would reduce tensile elongation and create interfaces that accelerate notch propagation in oxidizing effluents. Thick-wall extrusion is performed on a 75–120 mm grooved-barrier extruder with 33–37 L/D, a gear melt pump, and a spiral mandrel die; melt temperature is held at 195–210°C, lower than for thin-wall pipe because a thick cross-section retains heat and can develop internal voids if discharge temperature exceeds 220°C. Calibration uses a multi-stage vacuum tank at 0.3–0.6 bar and counter-current chilled water at 15–20°C. Chemical resistance boundaries are verified by immersion testing per ISO 22088-2 and chemical resistance charts in ISO/TR 10358; service with strong oxidizing acids above 60°C falls outside the application envelope. Terminal products include PN 10 and PN 16 solid-wall piping from DN 20 to DN 400 for deionized water loops, acid waste drainage, and chlorinated process water.
Structured-wall stormwater culvert and retention pipe produced from HDPE 2480 is governed by EN 13476-2 and AASHTO M294 for high-density polyethylene corrugated pipe. The black structured-wall compound is 98.0 wt% HDPE 2480 and 2.0 wt% carbon black masterbatch; an external lubricant package based on ethylene bis-stearamide at 0.2–0.4 wt% is added only when corrugator release force on aluminum mold blocks exceeds the baseline established at 60°C mold temperature. In-line edge trim is reintroduced at 10–15 wt% for non-pressure stormwater pipe, but not into pressure-rated layers. Processing uses a 75–120 mm grooved-barrier extruder with 33–36 L/D feeding a rotating die head; parison temperature is maintained at 198–208°C, and corrugator vacuum is set at 0.6–0.8 bar. At parison temperature above 212°C, semi-molten web sagging between mold blocks produces asymmetric wall distribution and rib thinning, while below 192°C, the vacuum cannot fully form rib profiles and notch resistance measured by ISO 179-1 drops. Mold block temperature is controlled between 45°C and 60°C; water spray cooling then reduces the formed pipe to ≤40°C before cutting. Terminal products include DN 100–800 corrugated stormwater, detention and road culvert pipe with smooth interior sections, supplied as straight lengths or nested bundles.
Mining slurry and dredge pipelines are a high-wear application in which HDPE 2480 is selected for its slow crack growth resistance rather than for any filler-derived abrasion modification; the compound is 98.0 wt% HDPE 2480, 2.0 wt% carbon black masterbatch, and 0.2 wt% antioxidant masterbatch. Inorganic wear fillers are excluded because particulate interfaces reduce failure time under ISO 22088-2 detergent-induced stress cracking and increase the risk of sudden crack propagation in suspended abrasive service. For thick-wall mining lines the extrusion installation is a 90–150 mm grooved-barrier extruder with 33–37 L/D, gear melt pump, and vacuum calibration tank length matched to output; melt temperature is set at 195–215°C and outlet surface temperature is kept below 70°C before cutting to prevent post-sag. Wall thickness is monitored by ultrasonic segment scanners, and wall-thickness eccentricity above 3% at DN 250 and larger triggers recalibration. Pipe is produced in SDR 7.4, SDR 9, and SDR 11 solid-wall configurations from DN 90 to DN 400, typically with butt-fused joints and flanged adapters for tailings lines, dredge pump discharge, and mine dewatering mains. Compliance for industrial pressure service is verified against ISO 15494 and ASTM F714, with additional hydrostatic pressure testing at 1.5 × nominal pressure for 1 h on each welded string.
Close-fit pipe rehabilitation liners made from HDPE 2480 are specified under ISO 11298-3 for potable water network renovation and under AWWA M55 design practice for water pressure pipe. The compound uses 97.5 wt% HDPE 2480 with 2.5 wt% carbon black masterbatch; no external regrind is permitted because the folded-in-place process imposes bending strains that require the full slow crack growth resistance of a virgin PE100 compound. The liner pipe is first extruded as a standard SDR 17 or SDR 11 pipe on a grooved-barrier extruder, then butt-fused into insertion strings. Diameter reduction is performed by cold swaging or die drawing to 8–12% reduction, and the folded cross-section is retained by restraining bands during insertion. Reversion to circular cross-section uses controlled water pressure at ambient temperature; insertion temperature below 5°C is avoided because HDPE 2480 flexural modulus rises and fold spreading becomes difficult, while insertion temperature above 35°C softens the wall and increases the risk of scoring against host-pipe debris. Notch resistance during installation is evaluated by ISO 179-1 Charpy impact on specimens taken from the pipe wall, and collapse pressure after reversion is verified by short-term hydrostatic testing at 1.5 × working pressure for 1 h per ISO 11298 procedures. Terminal products include DN 100–800 tight-fit and folded-in-place liners for rehabilitation of corroded metallic or concrete water mains, supplied as site-butt-fused strings with pull-head fittings and sacrificial outer jackets where required by site conditions.
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