| HS Code | 609656 |
As an accredited PetroChina Jilin HDPE JHMGC100S / 100S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PetroChina Jilin HDPE JHMGC100S / 100S is supplied in 25 kg woven bags, 40 bags (1,000 kg) per shrink-wrapped pallet. |
| Container Loading (20′ FCL) | 20′ FCL: 25 MT PetroChina Jilin HDPE JHMGC100S/100S in 25 kg bags, palletized optional; securely loaded and sealed for export. |
| Shipping | PetroChina Jilin HDPE JHMGC100S/100S is typically shipped in 25 kg PP woven bags or 1000–1500 kg jumbo bags, palletized and stretch-wrapped. It is transported by truck, rail, or sea container, kept dry and away from direct sunlight, heat, and moisture. Classified as non-hazardous; secure export packaging ensures safe handling during international transit. |
| Storage | Store PetroChina Jilin HDPE JHMGC100S / 100S in a cool, dry, well-ventilated warehouse. Keep bags or containers sealed and palletized off the floor, away from direct sunlight, rain, heat, ignition sources, and strong oxidizers. Avoid prolonged UV exposure and contamination. Use first-in, first-out stock rotation. Maintain clean handling areas and follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Typically 24 months when stored cool, dry, and sealed in original packaging away from direct sunlight and heat. |
PetroChina Jilin JHMGC100S/100S is converted into municipal pressure pipe on grooved-feed single-screw extruders where the grade is processed as a bimodal PE100 pipe resin. The material classification is anchored to ISO 9080 and ISO 12162:2022, requiring a minimum required strength of 10 MPa at 20°C for a 50-year design life. The downstream pipe converter verifies lot-specific density, typically 0.950–0.960 g/cm³, and melt mass-flow rate under 5 kg at 190°C before compounding or direct extrusion. For drinking-water service, the finished pipe must satisfy ISO 4427-2:2019 dimensional requirements and, in North American export markets, NSF/ANSI/CAN 61 migration criteria. The compounding step adds a carbon black masterbatch to reach 2.0–2.5 wt% carbon black when black pipe is produced; dispersion is checked against ISO 18553 and must not exceed grade 3. Extrusion is carried out on a grooved-feed single-screw machine with 30:1–37:1 L/D, barrier screw geometry, and layered screen packs matched to throughput and die diameter. Melt temperature at the die entry is held in the 210–230°C band, and die head pressure is controlled below the extruder manufacturer’s maximum, commonly 35 MPa, to protect the gear pump and mandrel supports. The terminal product is a black or blue-striped pipe in SDR 11, SDR 13.6, SDR 17, or SDR 21, with long-term creep validation through ISO 13479:2022 notched-pipe testing at 80°C. The most common production bottleneck is wall-thickness eccentricity on small-diameter pipe below 110 mm, caused by inadequate vacuum calibration tank alignment or unstable melt pressure from worn screw elements.
| Service | Product standard | Material classification | Slow crack growth test | Fusion joining |
|---|---|---|---|---|
| Potable water | ISO 4427-2:2019 | ISO 12162:2022 PE100 | ISO 13479:2022 | ISO 21307:2017 |
| Natural gas distribution | ISO 4437-2:2014 | ISO 12162:2022 PE100 | ISO 13479:2022 | ISO 21307:2017 |
| Industrial slurry | ASTM F714 | ISO 12162:2022 PE100 | ASTM F1473 | ISO 21307:2017 |
In natural gas distribution, pipe made from JHMGC100S/100S is governed by ISO 4437-2:2014 and, for North American projects, ASTM F2619/F2619M. Slow crack growth resistance is the limiting design property, not short-term tensile strength. The bimodal molecular weight distribution of the PE100 resin maintains sufficient high-molecular-weight tie molecules to resist crack initiation at stress concentrations from rock impingement or butt-fusion bead notches. Gas pipe recipes typically include a phenolic-phosphite antioxidant package and, for yellow pipe, a high-load organic pigment system that does not offer the masking effect of carbon black; therefore stabilized yellow pipe requires elevated UV stabilization levels and more conservative warehouse storage times. Extrusion of gas pipe in diameters from 20 mm to 400 mm uses melt temperatures of 205–225°C at the die, lower than the upper limit for water pipe because gas pipe often runs at higher line speeds and residual oxidative degradation at the outer surface can reduce ISO 13479:2022 notched-pipe failure time. In-line thickness gauging with ultrasonic or laser sensors controls SDR 11 and SDR 17 dimensions, and the terminal pipe is pressure-tested at 20°C and 80°C before printing with the manufacturer’s code, nominal size, material designation, and production date. Butt fusion joints in the field are made under ISO 21307:2017; the critical field variable is heater plate surface temperature, which must not exceed 230°C because the outer melt layer of JHMGC100S/100S may undergo premature thermo-oxidative chain scission that lowers slow crack growth resistance at the joint zone.
Pipe converters serving acid processing, mining, and paper mill effluent operations process JHMGC100S/100S into solid-wall HDPE pipe where the primary design inputs are chemical resistance and wall-thickness wear allowance. Chemical resistance data are taken from ISO/TR 10358 rather than from generic compatibility tables; the resin does not tolerate concentrated oxidizing acids at elevated temperature, and the service limit must be fixed by immersion testing on coupons cut from the extruded pipe in the actual mixed effluent. For abrasive slurries, the wall thickness is increased from the standard SDR by the designer’s corrosion-erosion allowance, usually 2–10 mm, depending on particle size and flow velocity. Extrusion of thick-wall slurry pipe differs from municipal water pipe in that some converters incorporate clean in-plant regrind from their own pipe trimming at up to 10–20 wt%, provided the regrind has a melt mass-flow rate within the converter’s internal lot-to-lot tolerance band and a retained OIT greater than 20 min at 200°C under ISO 11357-6. Melt temperature is held at 200–220°C to reduce regrind thermal history effects. The finished pipe is inspected by dimensional checks against ASTM F714, tensile elongation per ISO 6259-1, and environmental stress crack resistance assessed with ASTM D1693 or the notched constant tensile load method in the process fluid.
To fabricate ground-source heat pump loops from JHMGC100S/100S, the converter extrudes 25–40 mm SDR 11 pipe and coils it while the pipe is still above ambient temperature immediately after the vacuum calibration tank. The key process metric is wall-thickness eccentricity; coiling into 300 m reels imposes a bending strain that can exceed the material’s allowable strain if wall thickness deviates by more than 0.25 mm around the circumference, so ultrasonic thickness scanning is applied at the haul-off. In geothermal service, the material is not in continuous contact with potable water but must still pass long-term strength tests at 40°C and 80°C under ISO 9080; loop temperatures up to 35–40°C reduce the allowable design stress relative to 20°C. No separate ISO product standard exists for HDPE ground-loop pipe in most export jurisdictions, so the finished product is commonly dual-marked against ISO 4427-2:2019 dimensions and ASTM D3035 outside diameter tolerances, with the PE100 designation shown in the print line. Field joining uses electrofusion or butt fusion per ISO 21307:2017, with the U-bend assembly formed by pre-fabricated molded fittings. The terminal installation is hydrostatically tested at 1.5 times the maximum operating pressure for 30 min or as specified by the geothermal system designer, and all buried joints are left exposed for inspection until thermal backfill procedures are completed.
In butt fusion joining of JHMGC100S/100S pipe, the welding machine must maintain a heater plate surface temperature of 210–225°C, because the bimodal resin’s high-molecular-weight fraction controls bead formation under low shear and requires enough soak time to reach a uniform molten layer without exceeding 230°C. Bead-up pressure is set at 0.15–0.20 MPa, fusion pressure at 0.15–0.25 MPa, and cooling time is determined by wall thickness and ambient temperature as tabulated in ISO 21307:2017 or the user’s national code. The most frequent field failure mode is the cold weld: a joint with no visible double bead but with sufficient short-term strength to pass a quick hydrotest yet substantially reduced notched-pipe test time under ISO 13479:2022. For this reason, production welds on gas or water networks are subjected to destructive bend-back testing each day and tensile tests of selected coupons per ISO 13953. The terminal product is not the pipe itself but the welded joint, which must display uniform double-bead geometry with root bead width within the machine manufacturer’s acceptance window and no surface porosity larger than 1 mm. In high-humidity environments above 60% RH, the pipe ends must be wiped dry and re-faced immediately before heating; condensate on the heater plate creates vapor pits that weaken the weld interface.
Where seawater intake or outfall pipe is specified in diameters of 500–1600 mm, converters produce JHMGC100S/100S in SDR 17 to SDR 26. The extrusion line uses a grooved-feed single-screw extruder with 37:1 L/D and an intensive barrier screw; melt temperature at the die is controlled between 205°C and 225°C, while haul-off speed is set to keep wall thickness within +1.0/−0.5 mm around the circumference. Extended vacuum calibration tanks with multiple spray cooling zones prevent sag in thick walls; cooling water temperature is held below 20°C to limit crystallinity gradients that can cause pipe out-of-roundness. Because marine outfall strings are welded onshore and floated into position, the pipe sections are butt-fused under ISO 21307:2017 and then hydrotested to 1.5 times the design pressure for 24 h before launch. Compliance after fabrication is generally assessed under ASTM F714 for dimension and ISO 4427-2:2019 for long-term pressure rating, while surface oxidation is checked by OIT testing per ISO 11357-6. The finished marine line is ballasted with concrete weights and submerged; no additional internal liner is used because the HDPE wall itself resists marine biofouling and chloride-induced corrosion.
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