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PetroChina Dushanzi HDPE DGDX-6095

    • Product Name: PetroChina Dushanzi HDPE DGDX-6095
    • 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 138015

    As an accredited PetroChina Dushanzi HDPE DGDX-6095 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PetroChina Dushanzi HDPE DGDX-6095: 25 kg woven bags, 40 bags per pallet, totaling 1,000 kg per pallet.
    Container Loading (20′ FCL) Container Loading (20′ FCL): PetroChina Dushanzi HDPE DGDX-6095 in 25 kg bags, approximately 25 MT net, securely stowed for export.
    Shipping PetroChina Dushanzi HDPE DGDX-6095 is shipped as a non-hazardous thermoplastic resin, usually in 25 kg woven bags, jumbo bags, or bulk containers. Keep dry, cool, ventilated, and protected from UV, heat, and contamination. Ensure clean equipment, avoid package damage; not regulated as dangerous goods.
    Storage Store PetroChina Dushanzi HDPE DGDX-6095 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and oxidizing agents. Keep original packaging sealed to prevent moisture, dust, and contamination. Stack pallets securely, avoid excessive load or crushing. Use appropriate handling to minimize static buildup. Observe local regulations and the manufacturer’s safety data sheet.
    Shelf Life PetroChina Dushanzi HDPE DGDX-6095 shelf life is typically 12 months when stored cool, dry, ventilated, away from sunlight, in original packaging.
    Application of PetroChina Dushanzi HDPE DGDX-6095

    PetroChina Dushanzi DGDX-6095 is processed into pressure pipe for potable water distribution, transmission mains, service connections, and rehabilitation sliplining. The resin is a bimodal high-density polyethylene classified under ISO 12162:2009 as PE100 because the lower confidence limit of long-term hydrostatic strength at 20°C and 50 years is not less than 10.0 MPa. The resulting design stress for water pipe calculations is 8.0 MPa at 20°C under ISO 4427-2:2019. Density measured under ISO 1183-1:2019 is approximately 0.949 g/cm³. Melt mass-flow rate measured under ISO 1133-1:2022 at 190°C with a 5 kg load is approximately 0.23 g/10 min. These values place the grade in the low-sag, high-melt-strength region required for large-diameter pipe extrusion where molten tube collapse must be controlled before vacuum calibration.

    Production-scale extrusion of DGDX-6095 is configured around grooved feed bushings and single-screw extruders with L/D ratios from 30:1 to 38:1. Barrel temperature setpoints normally range from 180°C to 215°C, adapter zones are held near 210°C, and spiral mandrel die bodies are operated between 200°C and 215°C. The measured melt temperature is maintained between 190°C and 220°C. Melt temperature must not exceed 230°C for extended residence periods because thermo-oxidative chain scission reduces molecular weight and produces gel accumulations at the die lip. Vacuum calibration is applied at 0.03–0.07 MPa below ambient pressure, and cooling water is held at 15–25°C for pipe outside diameters from 110 mm to 630 mm. The spiral mandrel die is selected over spider-leg dies because the weld-line structure is less pronounced, which matters for slow crack growth performance under long-term internal pressure.

    Pressure class is derived from the standard PN formula using the PE100 design stress. For a pipe with standard dimension ratio SDR, PN in bar is calculated as 20 × 8.0 MPa / (SDR−1). The output values are rounded down to the nearest standard pressure class.

    SDRDesign stress at 20°CCalculated pressure classCalculation basis
    268.0 MPa6.4 barISO 4427-2:2019
    178.0 MPa10.0 barISO 4427-2:2019
    118.0 MPa16.0 barISO 4427-2:2019

    Potable water pipe produced from DGDX-6095 is hydrostatically qualified under ISO 1167-1:2006. A PE100 pipe is subjected to a hoop stress of 12.4 MPa at 20°C for 100 h without ductile failure. The same testing path supports the extrapolation model in ISO 9080:2012. In practice, the extruded pipe is used for municipal water mains and service laterals where butt fusion and electrofusion joints are executed according to ISO 21307:2017 and ISO 12176-2:2012. The pipe is also used for slip-lining deteriorated pressure mains because the outer surface can withstand insertion abrasion without losing the required hydrostatic margin.

    What Gas Distribution Qualification Tests Expose Slow Crack Growth Sensitivity?

    DGDX-6095 is extruded into black polyethylene gas distribution pipe with yellow identification stripes. Carbon black content is controlled at 2.0–2.5 wt% under ISO 6964:2019 to provide ultraviolet stabilization during outdoor storage and installation. Gas pipe is qualified under ISO 4437-2:2014, which references the same PE100 classification but adds specific slow crack growth and rapid crack propagation requirements because gas service leaks are not self-announcing. The critical failure mode is not ductile yielding but slow crack propagation from a surface flaw or butt fusion toe. Qualification therefore includes the notched pipe test under ISO 13479:2009 at 80°C, where internal pressure is applied to a pipe containing axial external notches. The rapid crack propagation resistance is measured under ISO 13477:2008 using the small-scale steady-state S4 test. A pipe with insufficient RCP resistance can fail at high crack velocity in a pressurized gas network, so a critical temperature below −10°C is commonly specified for PE100 gas grades.

    Melt mass-flow rate and density are not the only release controls. The gas-pipe qualification matrix also requires oxidative induction time testing under ISO 11357-6:2018 at 200°C to verify that the antioxidant package has not been consumed during compounding and extrusion. Carbon black dispersion is checked under ISO 18553:2002 because agglomerates larger than the specified grading limit can act as crack initiators under long-term hoop stress. Electrofusion and butt fusion jointing follow ISO 21307:2017 and ISO 12176-2:2012. For gas distribution, squeeze-off of small-diameter mains is performed only with tools that limit pipe wall crushing because a damaged squeeze-off zone can become a slow crack growth site when the pipe is returned to service pressure.

    Property or testStandard designationTypical test condition
    Melt mass-flow rateISO 1133-1:2022190°C, 5 kg
    DensityISO 1183-1:201923°C
    Hydrostatic strengthISO 1167-1:200620°C, 100 h, 12.4 MPa
    Notched pipe slow crack growthISO 13479:200980°C, internal pressure
    Rapid crack propagationISO 13477:2008S4 test, critical temperature
    Carbon black contentISO 6964:20192.0–2.5 wt%
    Oxidative induction timeISO 11357-6:2018200°C
    Carbon black dispersionISO 18553:2002Microtome film rating

    In gas service, the maximum operating pressure is not limited only by the PE100 pressure class but also by the regulatory code for the network. A 110 mm SDR 11 PE100 pipe has a calculated pressure class of 16 bar under ISO 4427-2:2019, yet distribution mains typically operate at 2–4 bar. The unused hydrostatic margin is allocated to surge, ground movement, and flaw tolerance over a 50-year service life. DGDX-6095 is not specified for odorized liquid aromatic hydrocarbons or for continuous hydrogen-rich gas streams unless the specific concentration, temperature, and pressure are qualified separately because small molecule permeation can alter the failure kinetics of the pipe wall.

    In water reclamation plants, DGDX-6095 pipe is used for filtered effluent transfer, dual-media filter backwash lines, sodium hypochlorite contact basin discharge, and membrane bioreactor permeate collection. The governing long-term threat is oxidative attack from free chlorine rather than hydrostatic overload. Continuous free chlorine concentrations below 5 mg/L at temperatures up to 40°C generally remain within the chemical resistance envelope for HDPE, but shock dosing at 25 mg/L can occur during membrane cleaning or basin disinfection. The combined effect of chlorine concentration, temperature, and tensile stress follows an oxidative induction depletion mechanism. ISO 11357-6:2018 OIT at 200°C is used as a release check, but it does not predict a specific service lifetime in chlorinated water. ISO/TR 10358:1993 classifies sodium hypochlorite solution exposure for plastic pipe materials, and published data for this specific configuration is limited above 10 mg/L free chlorine at 60°C. Pipe joints are made by butt fusion without solvent adhesives because the welded joint has no residual volatile organic layer and no stress-concentrating socket gap. Flanged connections at pumps and filter skids use full-face elastomer gaskets selected for hypochlorite resistance, typically EPDM or fluorocarbon grades, to avoid seal swelling and flange leakage.

    When Tailings Velocity Falls Below 1.2 m/s, Abrasion Is Not the Only Concern

    DGDX-6095 is used in mining tailings and mineral slurry pipelines where the primary advantage is not only chemical resistance but also a high strain capacity and low surface energy compared with carbon steel. The pipe is extruded in SDR 11 and SDR 17 pressure classes and joined by butt fusion to eliminate internal bead interference at the invert. In a slurry line, the design must maintain a transport velocity above the deposition threshold. When the mean slurry velocity falls below 1.2 m/s, coarse solid particles settle into a moving bed at the pipe invert, and the wear mechanism changes from low-angle erosion to concentrated bed abrasion. The resulting wall loss is localized at the 5 o’clock to 7 o’clock position in horizontal pipe, not uniformly distributed around the circumference. For this reason, field installations use thickened-wall pipe segments or field-rotatable pipe that can be turned to expose an unworn surface. The pressure rating for slurry service is calculated using the 8.0 MPa PE100 design stress at 20°C under ISO 4427-2:2019, but the operating pressure is often much lower than the rated class because the line is gravity-assisted or pump-assisted with limited static head.

    On production-scale mining installations, unplanned shutdowns cause slurry to settle inside the pipe. Restarting a settled line requires flushing at high velocity to fluidize the settled bed, and the pump capacity may be insufficient if the deposit extends over several hundred meters. The restart pressure can also exceed the steady-state friction loss because the settled bed reduces the effective pipe cross-section. Operators therefore install clean water flushing connections at low points and allow reverse pumping through parallel standby piping. HDPE pipe in above-ground mining service is supported on sleepers or pipe racks at intervals that account for thermal expansion and creep modulus, and the support spacing is calculated using the flexural and creep data of the pipe material rather than short-term tensile data. External mechanical damage from mobile equipment is a more frequent failure cause than internal abrasion, so sacrificial concrete or steel guard barriers are placed at crossing points.

    Geothermal Loop Pipe Qualification Relies on Weld Integrity Under Low Ambient Temperatures

    DGDX-6095 is extruded into closed-loop geothermal ground-source heat pump pipe, typically in coil form for 32 mm to 63 mm outside diameters and SDR 11. The pipe loop carries a water–antifreeze mixture at fluid temperatures that can fall below 0°C in winter and exceed 35°C in summer. The pressure rating at 20°C for an SDR 11 PE100 pipe is 16 bar, but the allowable operating pressure is derated at elevated loop temperatures. Under ISO 4427-1:2007, the derating factor for PE100 at 40°C is approximately 0.74, reducing the permissible continuous pressure to about 11.8 bar for the same SDR. This derating is applied because long-term hydrostatic strength decreases as the amorphous phase of the polyethylene softens and oxygen diffusion into the pipe wall increases.

    Cold-weather butt fusion is the limiting production variable for geothermal loop installation. When the ambient temperature is below 5°C, the pipe ends lose heat rapidly after facing and before the fusion heater plate is withdrawn. The interfacial temperature during joining must be maintained within the 210–220°C range, and a cold pipe surface can quench the melt front before full molecular entanglement develops. ISO 21307:2017 specifies fusion pressure cycles, heater surface temperature, and cooling time as a function of wall thickness. In field conditions below 0°C, shelters are erected around the fusion machine, and the pipe ends are preheated with dry air to bring the surface temperature above the minimum specified value. The completed joint must remain clamped during cooling. Release of clamping pressure too early produces a weld with residual stress and a visible root bead that can crack during loop pressure testing. Coils are pressure-tested with air or water at 1.5 times the design pressure before backfilling, and the trench is padded with sand to prevent rock impingement damage to the pipe wall.

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