| HS Code | 911864 |
| Grade | PE100 |
| Density | 0.959 g/cm³ |
| Meltflowrate | 0.23 g/10 min (190°C/5 kg) |
| Tensileyieldstrength | ≥23 MPa |
| Elongationatbreak | ≥600% |
| Flexuralmodulus | ≥1000 MPa |
| Vicatsofteningtemperature | ≥125°C |
| Environmentalstresscrackresistance | ≥1000 h |
| Oxidationinductiontime | ≥20 min |
| Carbonblackcontent | 2.0-2.5% |
| Moisturecontent | ≤0.1% |
| Color | Black |
| Form | Pellets |
As an accredited PetroChina Dushanzi HDPE TUB121N3000 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PetroChina Dushanzi HDPE TUB121N3000 is packaged in 25 kg PP woven bags or 1000 kg jumbo bags. |
| Container Loading (20′ FCL) | Container loading (20′ FCL): PetroChina Dushanzi HDPE TUB121N3000 in 25 kg bags, palletized, stretch-wrapped, securely stowed for ocean freight. |
| Shipping | PetroChina Dushanzi HDPE TUB121N3000 is a non-hazardous high-density polyethylene resin. It is usually shipped in 25 kg bags or 1,000 kg jumbo bags, palletized, in clean, dry, covered containers. Standard sea/land freight applies; protect from moisture, sunlight, and contamination. HS code 3901.20. No special dangerous goods handling required. |
| Storage | Store PetroChina Dushanzi HDPE TUB121N3000 in a cool, dry, well-ventilated warehouse. Keep original bags sealed on pallets, away from direct sunlight, heat, ignition sources, and moisture. Prevent contact with oils, chemicals, or contaminants. Observe safe stacking limits and use first-in, first-out stock rotation. Avoid prolonged UV exposure and dusty conditions. Ensure good housekeeping and protect bags from physical damage. Consult SDS. |
| Shelf Life | PetroChina Dushanzi HDPE TUB121N3000 shelf life is about 24 months when stored cool, dry, ventilated, and in unopened original packaging. |
At a wall thickness above 63 mm, the processing window for PetroChina Dushanzi TUB121N3000 in municipal potable water mains narrows to a melt-temperature band of 190–220 °C during single-screw extrusion, because the bimodal molecular weight distribution that gives the resin its MRS 10 MPa classification also increases shear heating in the metering zone of a grooved-feed extruder with L/D 33:1 or longer. Under ISO 4427-2:2019, finished black pipe must retain a carbon black content of 2.0–2.5 wt% and a dispersion rating that permits no visible agglomerates above 125 µm in microscopic check, while EN 12201-2:2019 and GB/T 13663.2-2018 impose organoleptic and migration limits for potable water contact; pipe sold into North American projects additionally requires NSF/ANSI/CAN 61 certification. The standard let-down ratio for a 40% carbon black masterbatch into natural TUB121N3000 is 5.0–6.3 wt%, with 5.5 wt% set as the target on loss-in-weight gravimetric dosing units to account for pellet density variation between 0.545 g/cm³ and 0.565 g/cm³; under-dosing below 5.0 wt% produces wall sections that risk failing the ISO 9080:2012 long-term hydrostatic strength regression at 20 °C. On a production line using a 90/30D single-screw extruder with a barrier screw and a 200 mm die head, melt pressure upstream of the screen pack is typically 180–260 bar for SDR 17 pipe at haul-off speeds of 1.2–2.5 m/min; a sudden pressure drop of more than 30 bar while extruder rpm remains constant indicates gel or agglomerate breakthrough through the 80/120 mesh screen pack, a failure mode observed with black masterbatch batches containing recycled carrier resin. Downstream of the die, vacuum calibration at −0.3 to −0.5 bar in a 6 m vacuum-calibration tank followed by three spray-cooling zones at 18–35 °C is required to keep outer diameter within ±0.3% tolerance and to minimize residual stress; thick-wall pipe above SDR 11 is annealed in-line by reducing haul-off tension to below 0.5 MPa to prevent stress cracking. If pellets stored below 10 °C are introduced into a high-humidity production hall, surface condensation above 0.05 wt% moisture requires pre-drying at 70–80 °C for 1–2 h; otherwise microvoids form in the pipe wall. Terminal finished product types include SDR 11 PN16 municipal water mains in diameters DN 20–630 mm, SDR 17 PN10 distribution lines, and SDR 26 PN6 consumer service connections; all sizes are butt-fusion or electrofusion welded, with pipe ends prepared using a facing tool that removes at least 0.2 mm of oxidized surface before ISO 21307:2017 fusion procedures are applied.
For natural gas distribution pipe extruded from TUB121N3000, ISO 4437-2:2019 and EN 1555-2:2021 require the pipe to demonstrate MRS 10 MPa hydrostatic strength at 20 °C, to pass the ISO 13477:2018 full-scale S4 rapid crack propagation test at 0 °C, and to exhibit slow crack growth resistance under ISO 13479:2009 notched-pipe testing at 80 °C for the duration specified by the gas utility specification. The formulation addition rate for gas-grade black pipe is controlled at 5.5–6.5 wt% of a 40% carbon black masterbatch to reach 2.2–2.5 wt% carbon black in the final wall; a separate coextruded yellow stripe layer, typically applied at 3–5 wt% of total wall thickness using a PA-free yellow HDPE masterbatch with inorganic pigments, provides visual identification without altering the pressure-bearing wall. The downstream production process uses a single-screw extruder with a grooved feed section and a 30:1–37:1 L/D ratio, with barrel temperatures set from 180 °C at the feed zone to 215 °C at the die zone; melt temperature is held below 220 °C to prevent oxidative chain scission that would lower the ISO 9080:2012 extrapolated 50-year strength below 10 MPa. On production-scale lines, the critical processing threshold occurs at the transition from SDR 17 to SDR 11 thick-wall gas pipe: at wall thicknesses above 29 mm, residual stress in the pipe wall can exceed 2.5 MPa if cooling is too rapid, and longitudinal reversion must remain below 3% under ISO 2505:2005. Extruder melt temperatures above 230 °C must be avoided because the additional stabilizer consumption shifts the long-term hydrostatic failure mode from ductile to brittle in the ISO 9080:2012 regression band. Terminal finished products include DN 20–400 mm SDR 11 PN16 gas distribution pipe, DN 63–630 mm SDR 17 PN10 gas mains, and piggable DN 250–630 mm lines with smooth internal weld beads; electrofusion sockets must meet ISO 12176-3:2011 stripping voltage and fusion time requirements, and butt fusion is performed under ISO 21307:2017 with bead width of 8–12 mm for wall thicknesses above 20 mm.
Because HDPE slurry pipe fails by erosion thinning rather than hydrostatic creep alone, the critical design input for TUB121N3000 in high-abrasion tailings service is wall-thickness loss rate, not short-term burst pressure. Published consensus standards for HDPE slurry pipe are limited; most project specifications invoke ISO 9080:2012 for long-term hydrostatic design and ISO 21307:2017 for butt fusion, and require the pipe to satisfy the carbon black and hydrostatic strength requirements of ISO 4427-2:2019 as a baseline, with no single ISO product standard specific to mining slurry service. Carbon black masterbatch addition is held at 5.0–6.0 wt% of a 40% carbon black batch to deliver 2.0–2.4 wt% carbon black in the final wall; no calcium carbonate or mineral filler is included because filler lowers slow crack growth resistance under cyclic pressure. Thick-wall tailings pipe in SDR 7.4 and SDR 9 is extruded at line speeds below 0.6 m/min for wall thicknesses above 50 mm, with cooling water at 35–45 °C in the first spray tank to prevent vacuum voids and residual stress above 2.0 MPa; the same wall-thickness eccentricity limits from ISO 4427-2:2019 apply because eccentric wall sections under slurry pressure produce stress concentrations that accelerate erosive wear. Terminal finished products include DN 110–1000 mm tailings lines, dredge discharge pipes, and process water return lines. Published data for the specific erosive wear rate of TUB121N3000 under ore slurry is limited; site-specific wear testing should be conducted rather than relying on a single universal abrasion index.
Under EN 13476-2:2018 for structured-wall storm drains, a dual-wall corrugator running TUB121N3000 with 4.5–5.5 wt% of a 40% carbon black masterbatch places 2.0–2.3 wt% carbon black in the outer corrugated wall, and the corrugating die is held at −0.6 to −0.8 bar vacuum with mold-block speeds of 0.8–1.8 m/min to produce DN 100–1000 mm storm culverts, land drains, and retention pipes under AASHTO M294-18.
ASTM F1962-11 distinguishes between pullback force at the bore entry and axial force at the fusion shoulder; for PE100 pipe extruded from TUB121N3000, the governing installation practice limits axial tensile stress at the fusion shoulder to about 11 MPa, equivalent to 50% of nominal tensile yield strength, to avoid ductile tearing at butt-fusion welds. The formulation is identical to gas-grade black pipe: 5.5–6.5 wt% of a 40% carbon black masterbatch yields 2.2–2.5 wt% carbon black in the pressure wall, and no external release agent is permitted on the fusion surfaces because ISO 21307:2017 requires facing cuts to remove 0.2–0.5 mm of oxidized and contaminated surface before heating. Welds are qualified under ISO 13953:2001 with ductile failure in the pipe body rather than brittle separation at the fusion plane. Downstream production for HDD lengths typically uses the same 90/30D grooved-feed extruder as pressure pipe, but pipe is coilable in diameters up to DN 200 mm; above DN 200 mm, straight lengths are butt-fused on site, hydrostatically tested at 1.5 times design pressure for at least 1 h, and then pulled into the bore path with a swivel connection to prevent torsional rotation. The terminal finished product types are river-crossing water and gas pipelines, DN 100–1000 mm SDR 11 or SDR 17 pressure pipes for trenchless installation, and bundled utility conduits installed by horizontal directional drilling.
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PetroChina Dushanzi HDPE TUB121N3000 is a black-coloured, bimodal high-density polyethylene pipe compound positioned within the PE100 hydrostatic design strength class under ISO 12162:2014. The model designation TUB121N3000 separates it from film, blow-moulding, and injection-moulding HDPE grades produced at the Dushanzi site. The published density is 0.959 g/cm³ when measured under ISO 1183-1:2019, and the melt flow index is 0.30 g/10 min at 190 °C/5.0 kg under ISO 1133-1:2022. These values place the material in the low-melt-flow-index, high-molecular-weight pipe extrusion class. The black pellets are precompounded with carbon black and a hindered phenolic-phosphite stabiliser system intended for long-term hydrostatic pressure at 20 °C.
| Parameter | Test method | Specification range |
|---|---|---|
| Melt flow index | ISO 1133-1:2022 | 0.25–0.35 g/10 min at 190 °C/5.0 kg |
| Density | ISO 1183-1:2019 | 0.957–0.961 g/cm³ |
| Tensile yield stress | ASTM D638-14 | ≥23 MPa |
| Elongation at break | ASTM D638-14 | ≥600% |
| Carbon black content | ISO 6964:2019 | 2.0–2.5 wt% |
| Oxidation induction time | ISO 11357-6:2018 | ≥20 min at 200 °C |
| Hydrostatic design basis / MRS | ISO 9080:2022 / ISO 12162:2014 | 10 MPa / PE100 |
The polymer is produced through a cascaded-reactor process that creates a bimodal molecular weight distribution. The low-molecular-weight fraction lowers melt viscosity under extrusion shear, while the high-molecular-weight fraction contributes tie-molecule density and slow crack growth resistance. The bimodal distribution gives the grade a higher shear-thinning index than typical unimodal HDPE, observed as an elevated flow-rate ratio between 21.6 kg and 5.0 kg loads. Comonomer insertion in the high-molecular-weight fraction is controlled to produce short-chain branching that interrupts lamellar thickness regularity, shifting long-term failure away from brittle slow crack growth. Environmental stress crack resistance is reported above 1000 h F50 under ASTM D1693-15 in 10% Igepal CO-630 at 50 °C. This value is relevant for pipe installed in aggressive soils and for butt-fusion and electrofusion weld zones.
Carbon black dispersion is controlled by the use of a pre-dispersed masterbatch. The finished compound contains 2.0–2.5 wt% carbon black under ISO 6964:2019. The lower bound maintains ultraviolet weatherability under ISO 16871-1:2016, while the upper bound avoids excessive viscosity rise and loss of impact strength. At carbon black loadings above 3.0 wt%, butt-fusion weld quality deteriorates because carbon black particles undergo shear-induced agglomeration in the melt zone. At loadings below 2.0 wt%, ultraviolet stabilisation falls below the accepted threshold for open-air stockpiling beyond 12 months. Dynamic oscillatory shear tests at 190 °C indicate a high relaxed plateau modulus and a crossover frequency that shifts to lower values as molecular weight increases. The zero-shear viscosity is expected to exceed 100 000 Pa·s, which accounts for low sag behaviour and high melt strength in thick-walled pipe.
Class assignment follows ISO 9080:2022 hydrostatic strength testing in which pipe specimens are pressurised at 20 °C, 40 °C, 60 °C, and 80 °C to generate a lower confidence limit. The minimum required strength is 10 MPa at 20 °C for 50 years. The PE100 classification therefore allows a design stress of 8 MPa with a design coefficient of 1.25. The high-molecular-weight fraction in TUB121N3000 contributes to retention of hydrostatic strength at elevated temperature. At 80 °C, the material is required to withstand hoop stresses of 5.5 MPa, 5.0 MPa, 4.6 MPa, 4.2 MPa, and 3.9 MPa in stepped-pressure or constant-pressure tests. Published data for this specific configuration is limited beyond 50 years, so service lifetimes above this horizon are extrapolated rather than directly measured.
Pipe extrusion of TUB121N3000 employs grooved-feed single-screw extruders with L/D ratios between 25:1 and 30:1. Melt temperatures of 210–230 °C are typical at the die entry. Temperatures above 240 °C for residence times above 5 min can initiate oxidative gel formation; temperatures below 190 °C produce sharkskin melt fracture at die shear rates above 200 s⁻¹. On a 60 mm barrier screw extruder producing 110 mm SDR 11 pipe, output rates of 250–350 kg/h are limited by vacuum calibration cooling rather than by plastication. The melt pump should be installed downstream of the barrel to reduce pressure pulses, and the breaker plate should use 60/80/100 mesh screens to capture carbon black agglomerates. Pre-drying is not normally required below 60% RH. Pellets stored above 60% RH require 80 °C hopper drying for 4 h. Residual moisture above 0.05 wt% produces microvoids visible as fisheyes in the pipe wall.
Substitution of PE80 pipes with TUB121N3000 permits wall-thickness reduction for the same pressure rating. For a PN 10 water main at 20 °C, a PE100 material with an MRS of 10 MPa can use SDR 17 instead of SDR 11, increasing internal bore area by approximately 15% and reducing polymer mass per metre by approximately 20%. The calculation follows ISO 4427-2:2020 using a design coefficient of 1.25. Wall-thickness reduction is contingent on pipe ovality remaining below 5% and on proper side-fill compaction, because HDPE has a tensile modulus of approximately 900 MPa under ASTM D638-14. Compared with ductile cast iron, TUB121N3000 removes corrosion-induced tuberculation and lowers installation mass, but it requires external support to resist deflection under AASHTO H-20 live loads. For chlorinated water service above 40 °C, published data for this specific configuration is limited.
Because the melt flow index under 2.16 kg falls below 0.1 g/10 min, TUB121N3000 is not suitable for injection moulding at pressures below 120 MPa. Thin-wall extrusion below 1 mm also tends to produce melt fracture and dimensional instability. This distinguishes it from high-flow Dushanzi HDPE grades such as DMDA-8007, which is designed for blow moulding and containers. The high notched Charpy impact strength of TUB121N3000, above 30 kJ/m² at 23 °C under ISO 179-1:2023, is achieved at the expense of spiral-flow length. Compared with unimodal pipe grades, TUB121N3000 shows a higher rheological polydispersity index and better sag resistance in large-diameter pipe. In pipe diameters above 250 mm, the high molecular weight reduces melt drawdown, but it also increases the risk of incomplete fusion if electrofusion pressure is not maintained.
Potable water and gaseous fuel compliance is anchored to ISO 4427-2:2020 for water piping systems and ISO 4437-3:2014 for gas distribution. The black compound meets the carbon black dispersion and ultraviolet resistance requirements of ISO 4427-3:2020 when extruded into pipe. Oxidation induction time above 20 min at 200 °C under ISO 11357-6:2018 indicates sufficient antioxidant capacity for melt processing. However, the grade is not classified as PE100-RC unless the final pipe is separately tested for rapid crack propagation resistance under ISO 13477 small-scale steady-state crack arrest testing. For gas pipe above 250 mm, national regulations may require additional full-scale crack arrest verification because published data for this specific configuration is limited.
TUB121N3000 requires butt-fusion welding protocols with heating plate temperatures of 210–220 °C. The high-molecular-weight fraction raises melt viscosity at the weld interface, so bead geometries must be controlled to prevent cold fusion. In electrofusion, the slow crack growth resistance of the resin reduces sensitivity to scrape defects in the fusion zone. However, welding to PE80 or lower-molecular-weight HDPE can produce asymmetric melt fronts; joints should be qualified under ISO 13953 peel-decohesion testing. The carbon black level influences dielectric heating uniformity; localised carbon black agglomeration above 3.0 wt% can produce hot spots during electrofusion. Storage under ambient conditions at or below 50 °C in sealed containers is recommended to prevent moisture uptake and antioxidant loss. The grade should not be combined with bare copper or copper-based stabilisers because copper ions catalyse thermo-oxidative degradation of polyethylene. This incompatibility is relevant for fittings and inserts embedded in the pipe system. The material is also not recommended for continuous exposure to strongly oxidising chemicals such as concentrated nitric acid at temperatures above 25 °C.