| HS Code | 746479 |
| Melt Flow Rate 190 C 5kg | 0.23 g/10min |
| Melt Flow Rate 190 C 2 16kg | 0.07 g/10min |
| Density | 0.959 g/cm³ |
| Tensile Strength At Yield | ≥25 MPa |
| Tensile Strength At Break | ≥35 MPa |
| Elongation At Break | ≥600% |
| Flexural Modulus | ≥1000 MPa |
| Vicat Softening Temperature | ≥125°C |
| Brittleness Temperature | ≤-70°C |
| Environmental Stress Cracking Resistance | ≥1000 h |
| Oxidation Induction Time | ≥20 min |
| Moisture Content | ≤0.1% |
| Ash Content | ≤0.1% |
| Bulk Density | 0.55 g/cm³ |
| Hardness Shore D | 65 |
As an accredited PetroChina Dushanzi HDPE DGDB-6097 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PetroChina Dushanzi HDPE DGDB-6097 is supplied in 25 kg net-weight woven bags, stacked on 1,000 kg pallets. |
| Container Loading (20′ FCL) | 20′ FCL: PetroChina Dushanzi HDPE DGDB-6097 in 25 kg bags, palletized, approximately 17 MT net per container. |
| Shipping | PetroChina Dushanzi HDPE DGDB-6097 is a non-hazardous polyethylene resin. It is typically shipped in 25 kg PP/PE bags or 500–1000 kg jumbo bags, palletized and stretch-wrapped. Transport in clean, dry containers or trucks, avoiding moisture, direct sunlight, heat, and contamination. No special dangerous goods documentation is required. |
| Storage | Store PetroChina Dushanzi HDPE DGDB-6097 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags sealed, palletized, and off the floor. Prevent moisture, dust, and contamination. Maintain ambient temperatures below 50°C, protect from UV radiation and physical damage, and follow first-in, first-out stock rotation. Do not store near food, feed, or drinking water. |
| Shelf Life | Typically 24 months from production when stored unopened in a cool, dry, ventilated area, away from direct sunlight. |
In potable water networks operating at service pressures between 0.4 MPa and 1.6 MPa and ground temperatures from 4°C to 25°C, PetroChina Dushanzi HDPE DGDB-6097 is used as the primary PE100 pressure pipe resin in solid-wall extrusion lines producing pipes with nominal outside diameters from 20 mm to 1,200 mm. The grade's nominal density of 0.949 g/cm³ and melt flow rate of 0.23 g/10 min at 190°C under 5 kg load (ISO 1183-1:2019 and ISO 1133-1:2022) place it within the PE100 MRS 10 MPa classification defined by ISO 12162:2009. Compliance for water-contact service requires the final pipe compound, not the neat resin, to meet ISO 4427-2:2019 and EN 12201-2:2013+A1:2019 for hydrostatic pressure resistance, with long-term strength validated by ISO 9080:2022 regression data at 20°C and 60°C. For North American potable water contact, the finished pipe compound is tested under NSF/ANSI/CAN 61 and classified under ASTM D3350-21; the resin alone does not confer certification. The black pipe formulation loads DGDB-6097 at 93.75–95.0 wt% with a 40% carbon black masterbatch at 5.0–6.25 wt% to achieve a final carbon black content of 2.0–2.5 wt%, while blue potable water identification pipe uses 98.0 wt% DGDB-6097 with 2.0 wt% blue pigment masterbatch. Extrusion is performed on a single-screw extruder with a grooved feed section, barrier screw, and L/D ratio of 30:1 to 33:1; barrel zones are maintained from 180°C in the feed throat to 210–220°C at the metering section, with die head temperature held at 210–225°C and melt temperature limited to 200–220°C. Vacuum tank pressure is controlled at −0.03 to −0.06 MPa and cooling water at 15–25°C; haul-off speed is coupled to ultrasonic wall-thickness measurement to maintain SDR 17 or SDR 11 dimensional tolerance. If condensed moisture is present from cold warehouse transfer, pre-drying at 70–80°C for 2–3 hours in a desiccant dryer prevents surface pitting; melt residence time above 20 minutes at process temperature or melt temperatures above 230°C trigger oxidative degradation. End-product forms include PN 10 and PN 16 water mains, service laterals, and trenchless installation pipes in SDR 11 and SDR 17 configurations, as well as blue-striped potable water pipelines where above-ground identification is required.
Buried natural gas distribution lines impose a narrower processing window than water pipe because rapid crack propagation (RCP) resistance is validated on the finished pipe, not the resin pellet. For DGDB-6097, gas pipe production in SDR 11 and SDR 17 geometries from 20 mm to 630 mm outside diameter requires the extruded pipe to satisfy ISO 4437-1:2020 and ISO 4437-2:2020; North American export is governed by ASTM D2513-21 and U.S. DOT 49 CFR Part 192. The RCP critical temperature is measured by ISO 13477:2008 small-scale steady-state S4 testing, and slow crack growth resistance is confirmed on notched pipe specimens under ISO 13479:2022 at 80°C and hoop stress conditions corresponding to the design factor. The addition ratio for black gas pipe is 93.75–95.0 wt% DGDB-6097 with 5.0–6.25 wt% of a 40% carbon black masterbatch, yielding 2.0–2.5 wt% final carbon black for UV stabilization; a coextruded yellow stripe layer is dosed with 3.0–5.0 wt% yellow masterbatch in a satellite extruder because stripe-layer discoloration or delamination is a reject criterion. Production equipment is typically a 33:1 single-screw barrier extruder with a spiral mandrel die, melt pump, and vacuum sizing; melt temperature is held between 200°C and 220°C, while die-head pressure above 10 MPa is maintained to reduce RCP sensitivity caused by unmelts. Regrind from in-process pipe is limited to 10 wt% or less because higher fractions of heat-histories lower the strain-hardening modulus and raise the RCP transition temperature. Gas pipe is not rated for continuous service above 40°C; exposure to hydrocarbon condensates above the design concentration may require a higher safety factor or alternative barrier layers. End-product types include PE100 gas mains, service risers, and direct-buried distribution laterals with pressure ratings up to 1.0 MPa depending on SDR and location class.
For mining tailings transport, dredge discharge, and chemical plant process water lines, DGDB-6097 is processed into solid-wall pressure pipe in which the limiting mechanism shifts from hydrostatic creep to abrasive wall loss and stress-cracking from polar process fluids. The pressure design basis is validated through ISO 9080:2022 long-term hydrostatic strength and ASTM D2837-21 hydrostatic design basis generation; chemical compatibility for process water is assessed with ISO 4433-1:1997 immersion testing, and environmental stress-cracking resistance is measured by ASTM D1693-15 in aggressive surfactant media. The compound uses 93.75–95.0 wt% DGDB-6097 with 5.0–6.25 wt% of a 40% carbon black masterbatch to achieve 2.0–2.5 wt% final carbon black, and no mineral filler is added because filler platelets create stress-concentration sites that reduce slow crack growth resistance in ISO 13479:2022 notched pipe tests. Abrasion-resistant slurry pipe is produced on a 30:1 to 33:1 grooved-barrel extruder with melt temperature at 210–220°C; wall thickness above 60 mm requires stepwise cooling in the sizing tank at 60–70°C to reduce frozen-in stress before final water quenching. For chemical process water containing hydrocarbons or polar solvents, the final pipe must be tested in the specific fluid at operating temperature because published data for this specific configuration is limited and generic polyethylene chemical resistance tables do not cover all combinations. End-product types are tailings transfer lines, dredge discharge pipes, and process water headers in outer diameters from 200 mm to 1,200 mm, typically with butt-fused joints rated for PN 6 to PN 16.
Telecommunications duct and low-voltage power conduit production uses DGDB-6097 at higher haul-off speeds than pressure-grade water pipe because the product is not hydrostatically pressure-rated; dimensional stability and crush resistance are the primary acceptance criteria. The relevant product standards are ASTM F2160-22 for solid-wall controlled-outside-diameter HDPE conduit, NEMA TC 7-2021 for smooth-wall coilable polyethylene electrical conduit, and UL 651A where North American electrical installation codes require rigid nonmetallic conduit listing. The compounding ratio for black conduit is 93.75–95.0 wt% DGDB-6097 with 5.0–6.25 wt% of a 40% carbon black masterbatch to reach 2.0–2.5 wt% final carbon black for outdoor UV exposure; no pressure-related hydrostatic design basis is required. Typical production uses a 24:1 to 30:1 single-screw extruder with a pipe die and vacuum calibration, melt temperature of 200–215°C, and line speeds up to 15 m/min for small-diameter duct; wall thickness is set by outside diameter and crush resistance under ASTM F2160-22, not by SDR pressure class. Low-temperature brittleness is controlled by resin density and comonomer distribution, so scrap or regrind from higher-density HDPE grades is not blended into DGDB-6097 conduit because this shifts the ductile-to-brittle transition temperature upward. End-product types are rigid conduit for fiber optic backbones, direct-buried electrical raceways, and innerduct bundled configurations.
In coastal seawater intake and outfall pipelines, DGDB-6097 is designed to the same PE100 pressure basis as potable water lines, but the service environment introduces chlorine residual, marine growth, and wave-induced cyclic loading that standard potable water certification does not capture. Pressure design is governed by ISO 4427-2:2019 and EN 12201-2:2013+A1:2019, with long-term hydrostatic strength evaluated under ISO 9080:2022 at 20°C and 60°C; the material class is PE100 with MRS 10 MPa under ISO 12162:2009. Because no standalone ISO marine standard exists, project specifications typically require the fused pipeline to pass hydrostatic test pressures of 1.5× design pressure for a defined hold period and to generate chlorine-exposure data from the actual seawater chemistry; published data for this specific configuration is limited. The extrusion formulation is 93.75–95.0 wt% DGDB-6097 with 5.0–6.25 wt% of a 40% carbon black masterbatch to maintain 2.0–2.5 wt% final carbon black for UV stability, with no filler or regrind added for marine service. Pipe production uses a 33:1 grooved-barrel extruder with melt temperature between 200°C and 220°C; thick-wall sections above 40 mm are cooled in multiple calibrated vacuum tanks with water temperature raised to 30–35°C to reduce internal stress. End-product types are desalination intake headers, power plant cooling water pipes, and outfall diffusers with open-sea discharge sections; field joints are predominantly butt-fused and pressure-tested after installation.
Construction site dewatering operations and irrigation mainline installations use DGDB-6097 only in pressure-rated SDR 11 or SDR 17 configurations because the pipe is handled repeatedly, dragged over granular soil, and occasionally exposed to sunlight. Governing standards are ISO 4427-2:2019 for pressure service and AS/NZS 4130:2019 for Australian-New Zealand water supply; for agricultural mainlines in the United States, the pipe is specified under ASTM D3350-21 resin classification and the pressure rating is established by ASTM D2837-21 hydrostatic design basis. The compound ratio is 93.75–95.0 wt% DGDB-6097 with 5.0–6.25 wt% of a 40% carbon black masterbatch; because site-stored pipe may be exposed to UV for multiple construction seasons, the final carbon black content is held at 2.0–2.5 wt% rather than substituting a lower-cost blue-pigmented system. Extrusion conditions follow the same 200–220°C melt temperature range and vacuum calibration as pressure pipe, but wall-thickness tolerance is tightened to +0.1 mm/−0 mm on critical sections to prevent thinning during drag-in. Scrap-containing recyclate is not permitted in temporary bypass service because field abrasion scratches can initiate slow crack growth, and the addition of reprocessed HDPE from unknown sources reduces stress-cracking resistance below the validated PE100 design floor. End-product types are temporary surface water bypass pipes, irrigation district mainlines, and construction dewatering headers, typically in diameters from 90 mm to 500 mm and pressures from PN 6 to PN 16.
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PetroChina Dushanzi HDPE DGDB-6097 is a high-density polyethylene pipe extrusion compound classified as a PE100 pressure pipe material under ISO 9080:2012 and ISO 12162:2009. Published technical data list a density of 0.959 g/cm³ determined by ISO 1183-1:2019, a melt flow rate of 0.22 g/10 min at 190 °C under a 5 kg load according to ISO 1133-1:2022, a tensile yield stress of 24 MPa and elongation at break greater than 800 % according to ISO 527-2:2012. The product is supplied as pellets and is intended for pressure piping systems in water distribution and gaseous fuel transport where the long-term hydrostatic design stress of 10.0 MPa at 20 °C for a 50-year service reference is required.
| Property | Test method | Published typical value |
|---|---|---|
| Density at 23 °C | ISO 1183-1:2019 | 0.959 g/cm³ |
| Melt flow rate, 190 °C / 5 kg | ISO 1133-1:2022 | 0.22 g/10 min |
| Tensile yield stress, 50 mm/min | ISO 527-2:2012 | 24 MPa |
| Elongation at break | ISO 527-2:2012 | >800 % |
| Flexural modulus | ISO 178:2019 | 900 MPa |
| Notched Charpy impact, -30 °C | ISO 179-1:2023 | 12 kJ/m² |
| Environmental stress crack resistance, F50, 10 % Igepal CO-630, 50 °C | ASTM D1693-15 Condition B | >1,000 h |
| Oxidation induction time at 200 °C | ISO 11357-6:2018 | >40 min |
| Hydrostatic design stress, 20 °C / 50 years | ISO 9080:2012 | 10.0 MPa |
The tabulated values are published batch-release or typical figures for the resin; pipe-grade certification is completed on extruded pipe rather than on pellets alone. For pressure pipe, the controlling standards are ISO 4427-2:2019, EN 12201-2:2011+A1:2013 and, for gas, ISO 4437-2. The grade should be considered a PE100 resin with a design coefficient of 1.25, giving a design stress of 8.0 MPa as defined in ISO 12162:2009.
Size-exclusion chromatography of the resin reveals a bimodal molecular weight distribution. The high-molecular-weight copolymer fraction raises slow crack growth resistance and hydrostatic strength; the lower-molecular-weight fraction contributes enough flow under shear to permit thick-wall pipe extrusion. This separation is not found in a conventional unimodal PE100 where a single broad molecular weight distribution can yield a similar melt flow rate but lower resistance to brittle crack propagation at the same density. The practical distinction is the pressure class: DGDB-6097 is specified at an MRS of 10.0 MPa at 20 °C for 50 years under ISO 9080:2012, while PE80 materials are limited to 8.0 MPa. In a DN 110 mm PN 16 pipe, this permits an SDR 11 wall thickness of approximately 10.0 mm for PE100 versus an SDR 9 wall thickness of approximately 12.2 mm for PE80 at the same pressure class when the design stress of 8.0 MPa for PE100 and 6.4 MPa for PE80 is used.
Environmental stress crack resistance measured by ASTM D1693-15 Condition B at 50 °C in 10 % Igepal CO-630 is reported above 1,000 h; this value is several times higher than typical unimodal HDPE pipe grades of equal density. The difference arises from the higher tie molecule concentration in the bimodal long-chain fraction. In notched pipe testing under ISO 13479:2022, PE100 formulations of similar architecture commonly resist hoop stress of 4.0 MPa at 80 °C for more than 500 h; published data for this specific grade’s notched-pipe lifetime are limited.
If supplied as a black pipe compound, carbon black content should be controlled at 2.0–2.5 wt% with dispersion assessed according to ISO 18553:2002. Poor dispersion of carbon black lowers U.V. stabilization and creates local stress concentrations that can reduce slow crack growth resistance; DGDB-6097 differs from natural HDPE grades in that the pigment system is already incorporated, but compounding conditions and pellet homogeneity still require batch verification. Unlike commodity injection moulding or blow moulding HDPE grades with similar density, DGDB-6097 is subject to pipe-grade qualification. A general-purpose HDPE with comparable melt flow rate cannot be substituted because its slow crack growth resistance and long-term hydrostatic strength are not validated under ISO 9080:2012 and ISO 13479:2022.
On a grooved-feed single-screw extruder with a 33:1 L/D ratio and 60 mm screw diameter, pipe extrusion of DGDB-6097 is normally started with barrel set points from 180 °C at the feed throat to 210 °C at the metering zone, with adapter and die settings at 210–220 °C. The melt temperature measured at the adaptor should remain between 215 °C and 225 °C; excursions above 240 °C reduce oxidation induction time and increase gel formation in the pipe wall. Melt pressure before the screen changer is commonly 20–30 MPa at screw speeds of 60–90 min⁻¹ on a 60 mm grooved-feed machine, depending on pipe diameter and die resistance. The resin is not hygroscopic, but surface moisture from humid storage should be removed by drying at 80 °C for 2 h in a desiccant hopper when wet pellets, frost, or condensate are visible; otherwise moisture-driven surging and pinholes may occur.
Melt filtration with a 600–900 µm screen pack and a breaker plate is appropriate for pipe diameters above 110 mm. For smaller diameters or thin-wall tube, use 400–600 µm screens to protect the die lips without excessive back-pressure. Materials returned from start-up scrap should not exceed the pipe manufacturer’s validated regrind level; unless specified by a qualified procedure, re-feed of oxidized surface layers from stored pipe is not recommended because fusion weld quality decreases when oxidized material is incorporated.
When DGDB-6097 is substituted for a PE100 with a 5 kg MFR of 0.30 g/10 min or higher, the head pressure typically increases by 15–30 % at constant screw speed. This pressure rise is caused by the higher molecular weight fraction and the shear-thinning behaviour of the bimodal distribution. The die swell at 190 °C is slightly greater; operators may need to adjust the calibrator position, vacuum level, and haul-off speed to maintain outer diameter and wall thickness. A grooved-feed extruder with a 33:1 or 36:1 L/D ratio is preferred; smooth-bore single-screw machines designed for low-viscosity HDPE may not plastify the material completely at high output, leading to unmelts and surface roughness. If a melt pump is installed, the inlet pressure should be kept below 25 MPa to avoid excessive shear heating; barrel cooling zones should be set to maintain the rear barrel below 150 °C to maintain solids conveying.
Butt fusion welding of DGDB-6097 pipe should follow ISO 21307:2017 or a qualified weld procedure developed for PE100. The heating plate surface temperature is typically 200–220 °C; below 190 °C the high-molecular-weight fraction may not produce a uniform melt bead, and above 230 °C the stabilizer package may be consumed prematurely. Bead size, bead-up pressure, and dwell time should be taken from the machine manufacturer’s tables; changing from a lower-viscosity PE100 to DGDB-6097 usually requires an increase in heater plate temperature or bead-up time rather than a reduction. Electrofusion joints require removal of the oxidized pipe surface with a rotary peeler to a minimum depth of 0.2 mm; hand scraping with steel scrapers can produce irregular peel depth and reduce joint strength.
Hydrostatic testing of finished pipe sections is performed according to ISO 1167-1:2006 or the corresponding product standard. For water supply pipe under ISO 4427-2:2019, the pipe must withstand 20 °C and 80 °C pressure test regimes without ductile or brittle failure. Slow crack growth resistance is further checked by notched pipe testing under ISO 13479:2022; this test is more discriminating than ESCR on compression-moulded plaques because it evaluates the pipe wall after extrusion. Published data for this specific configuration is limited; however, PE100 pipe-grade resins with a comparable MFR and density generally exhibit a notched-pipe failure time greater than 500 h at 80 °C and 4.0 MPa hoop stress.
DGDB-6097 is not intended for continuous service with strong oxidizing agents, aromatic hydrocarbons, or concentrated mineral acids; the chemical resistance of the finished pipe should be checked against ISO 10358 or a similar published chemical resistance data source for the specific fluid. Potable water compliance is a pipe-system property, not solely a resin property; certification under NSF/ANSI/CAN 61, GB/T 17219, or EN 12873-1 must be verified on the extruded pipe. Outdoor storage should be limited because ultraviolet exposure, even with carbon black, can oxidize the outer surface and reduce fusion joint quality after prolonged exposure; the product should be stored in closed, dry conditions below 50 °C. If condensation is present or resin has been stored more than 12 months, drying and laboratory melt flow verification are advised before use.