| HS Code | 200450 |
| Polymer Type | High Density Polyethylene (HDPE) |
| Pipe Grade | PE100 |
| Color | Black |
| Density | 958 kg/m³ |
| Melt Flow Rate 190 C 5 Kg | 0.25 g/10 min |
| Tensile Stress At Yield | 25 MPa |
| Tensile Strain At Break | >600% |
| Flexural Modulus | 1000 MPa |
| Charpy Notched Impact Strength 23 C | ≥10 kJ/m² |
| Vicat Softening Temperature | 125°C |
| Oxidation Induction Time 200 C | >20 min |
| Carbon Black Content | 2.0-2.5% |
| Minimum Required Strength Mrs | 10 MPa |
| Thermal Conductivity | 0.4 W/m·K |
| Specific Heat Capacity | 1.9 kJ/kg·K |
| Linear Thermal Expansion | 1.8 x 10^-4 /°C |
| Water Absorption | <0.01% |
| Dielectric Constant | 2.3 |
| Volume Resistivity | >10^15 Ω·cm |
As an accredited INEOS HDPE ELTEX TUB121 N3000 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg polyethylene bags, palletized; each pallet contains 55 bags (1,375 kg) of INEOS HDPE ELTEX TUB121 N3000. |
| Container Loading (20′ FCL) | INEOS HDPE ELTEX TUB121 N3000 in 20′ FCL: 25 kg PE bags, palletized and shrink-wrapped, approximately 22 MT net weight. |
| Shipping | INEOS HDPE ELTEX TUB121 N3000 is shipped as non-hazardous HDPE pellets, usually in 25 kg polyethylene bags on stretch-wrapped pallets. Transport in clean, dry trucks or containers, avoiding moisture, direct sunlight, and excessive heat. No dangerous goods placards or special shipping documentation are normally required. Protect packaging from damage and contamination. |
| Storage | Store INEOS HDPE ELTEX TUB121 N3000 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags closed, palletized, and off the floor to prevent moisture, dust, and contamination. Protect from UV radiation and maintain ambient temperature, preferably below 40°C. Use first-in-first-out stock rotation. Do not store near food, drinks, or incompatible materials. |
| Shelf Life | Shelf life is typically indefinite if stored dry, cool, in original packaging, protected from UV light, moisture, and contaminants; no specific expiry. |
The principal conversion route for INEOS HDPE ELTEX TUB121 N3000 in brownfield and greenfield potable water networks is solid-wall pressure pipe extrusion, in which the resin is fed as a single-component black compound rather than a let-down blend. Compliance is assessed under EN 12201-2 and ISO 4427-2, with material classification as PE 100 having minimum required strength 10 MPa at 20 °C for 50 years per ISO 12162. The formulation addition rate at the hopper is 100 wt% as-received resin; external carbon black masterbatch is 0 wt%, and the compounded carbon black content is 2.0–2.5 wt% when checked by ISO 6964. Downstream production on a grooved-feed single-screw extruder with L/D 30:1–37:1 uses barrel set-points from 180 °C in the feed zone to 230 °C at the adapter, die-head melt temperature of 210–230 °C, and vacuum sizing at −25 to −60 kPa. Common production failure modes include surface pitting from wet granules, excessive die build-up at melt temperatures above 240 °C, and sag on diameters above DN 800 when internal pipe cooling is insufficient. Terminal products are solid-wall black PE100 potable water pipes from DN 20 to DN 1200 mm in SDR 9, 11, 13.6, 17, and 21, often coextruded with blue identification stripes. Processors should pre-dry material exposed to ambient relative humidity above 60% at 80 °C for 2–4 h; blending with non-PE100 regrind is outside the product qualification envelope.
Under ISO 4437-2 and EN 1555-2, the pressure-bearing black core is classified as PE100; full-scale rapid crack propagation resistance is verified according to ISO 13477, and slow crack growth resistance according to ISO 13479. In coextrusion, the core layer is metered as 100 wt% ELTEX TUB121 N3000, while the yellow PE100 identification layer is added at 5–10 wt% of total pipe mass depending on SDR and network-operator identification stripe requirements; the black core itself carries 2.0–2.5 wt% carbon black per ISO 6964. Production equipment typically consists of separate extruders feeding a spiral mandrel die, with interlayer melt temperature held at 210–230 °C to prevent weld-line separation and yellow-layer delamination. Vacuum calibration and stepped cooling water at 15–25 °C reduce residual stress; on-line ultrasonic thickness scanning is used to map wall-thickness eccentricity in both the black core and the yellow identification layer. Field failure modes are concentrated in yellow-layer thickness variation, which can cause gas-network identity rejection, and in rapid crack propagation at low ambient temperatures when SDR selection does not match the design pressure. Terminal products are buried PE100 gas distribution pipes from DN 20 to DN 400 mm in SDR 11 or 17.6, with maximum operating pressure derived from ISO 4437-3 design coefficients rather than a single universal rating. Continuous service above 60 °C and blends containing more than 10 vol% hydrogen require project-specific fitness-for-service testing; published data for this specific resin under high-pressure hydrogen is limited.
In high-abrasion copper tailings, phosphate clay, and fine iron ore slurry networks, the selection of a PE100 pipe compound is driven by weld consistency and resistance to slow crack growth under sustained hoop stress rather than by simple tensile yield. No single harmonized ISO product standard defines slurry pipe service across all mining jurisdictions; pressure envelope design falls under ISO 4427-1 and material classification under ISO 12162, while purchasers commonly add sacrificial wall thickness according to site-specific wear models. Published abrasion-resistance data for this specific configuration is limited. The compound is delivered as a black PE100 with no external filler masterbatch added at the throat; formulation addition is 0 wt% additive adjustment and 100 wt% as-supplied resin. For thick-wall sections above 40 mm, in-house regrind is limited to 5 wt% or less because higher regrind fractions can reduce Charpy impact and rapid crack propagation margins. Production uses high-torque single-screw extruders with internal air-cooled mandrels and external spray cooling to manage sag; melt temperature at the die is typically 220–230 °C, and throughput is deliberately reduced compared with thin-wall pipe to keep wall-centre porosity below ultrasonic detection thresholds. Jointing in the field is by butt fusion at 220±10 °C, with weld bead geometry inspected because slurry erosion can accelerate at misaligned internal beads. Terminal products include tailings lines, concentrate pipelines, dredge discharge pipes, and heap-leach process distribution pipes from DN 160 to DN 1200 mm, usually in SDR 11 to 21. Continuous slurry velocity above 5 m/s with sharp sand or ground rock requires sacrificial wear thickness beyond standard pressure-wall calculation; published long-term abrasion factors for this specific compound are limited.
Pressure sewer rising mains are specified within the scope of EN 12201-2 and performance-tested under ISO 4427-5; the PE100 classification relies on minimum required strength 10 MPa per ISO 12162. The base pipe wall is extruded from 100 wt% ELTEX TUB121 N3000; external carbon black masterbatch is not required because the compound already contains 2.0–2.5 wt% carbon black per ISO 6964. Brown identification stripes, where specified by network operators, are coextruded at 1–3 wt% of total pipe mass. Downstream converting consists of solid-wall pipe extrusion with melt temperature 215–230 °C, followed by multi-zone vacuum calibration and cooling water at 15–25 °C to limit residual stress. Because sewer force mains experience intermittent pump cycling, production joints are butt-fusion welded and the weld is inspected for cold fusion caused by ambient pipe-end contamination; fatigue cracking in service is more often traced to weld defects than to base polymer yielding. Terminal products are black/brown striped pressure sewer rising mains from DN 90 to DN 630 mm in SDR 17 or 21. Sustained exposure to hot industrial effluents above 60 °C or to aromatic hydrocarbon-contaminated wastewater should be excluded or addressed through ancillary chemical resistance testing, as published data for this compound under such mixed effluent streams is limited.
Across pivot and drip irrigation blocks drawing from open canals or raw reservoirs, the compound is converted into UV-stable black mainline pipe where the design pressure is seasonal and surge-driven rather than constant creep-limited. Pipes for agricultural pressure water use are supplied under ISO 4427-2 and, where required in Europe, EN 12201-2; carbon black dispersion is assessed by ISO 18553. Formulation adjustment is limited to 0 wt% external carbon black masterbatch, since the delivered compound contains 2.0–2.5 wt% carbon black; in-house regrind from edge trim and cut-off is added at ≤10 wt% after metering validation. Coiling is practical for small diameters up to DN 125 mm; larger diameters are produced in straight lengths. Extrusion uses groove-fed screws and vacuum calibrators, with line speed set by wall-thickness stability rather than maximum melt output; the black carbon black level allows continuous above-ground exposure. Terminal products include irrigation mainlines, sub-main headers, and pump discharge lines from DN 50 to DN 800 mm in SDR 17, 21, and 26. For recycled or wastewater-based irrigation containing high levels of chlorine or ozone, material suitability must be confirmed because published long-term data for this specific compound under high oxidant concentrations is limited.
Trenchless rehabilitation liners for potable water networks are specified under ISO 11298-1 and ISO 11298-2; for gas mains, the relevant framework is ISO 11299-1 and ISO 11299-2. The liner pipe is extruded from 100 wt% ELTEX TUB121 N3000; no external carbon black masterbatch is used because the compound contains 2.0–2.5 wt% carbon black per ISO 6964. Grout used after insertion is not part of the polymer formulation and is specified separately by the civil design. Downstream production involves continuous pipe extrusion followed by butt-fusion welding into long strings. Pull-in force is controlled by roller guides and pipe-clamping heads to prevent necking; the axial pull stress is checked against a derated short-term tensile yield value, and ovality recovery after pull-in is monitored at pipe ends. Published data for this specific configuration is limited, so pull-in calculations rely on site-specific bore geometry and lubricant friction coefficients rather than universal tables. Terminal products are structural or semi-structural PE100 liners from DN 100 to DN 1000 mm, typically SDR 26, 32.5, or 41. The grade is not intended for shell-free structural applications and must not be exposed to continuous service temperatures above 60 °C during steam cleaning of rehabilitated water mains.
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INEOS HDPE ELTEX TUB121 N3000 is a black, bimodal high-density polyethylene compound intended for extruded pressure pipe. The grade is classified as PE 100 under ISO 12162, with a minimum required strength of 10 MPa at 20°C for 50 years in water when evaluated against the long-term hydrostatic strength reference curves of ISO 9080. Pipe produced from the compound falls within the material requirements of ISO 4427-1, ISO 4427-2, and EN 12201-2 for water supply, pressure sewer, and industrial water networks. The N3000 designation distinguishes the black, carbon-black-stabilised compound from natural or coloured polyethylene grades in the same molecular-weight range. Typical published values for this grade include a density of 0.959 g/cm³ and a melt flow rate at 190°C/5 kg below 0.35 g/10 min, although the current certificate of analysis should be used for lot-specific acceptance. The product is intended for pipe extrusion rather than injection moulding or rotational moulding because its high melt viscosity provides the sag resistance required for thick-walled pipe.
Typical material properties reported on the certificate of analysis include density, melt flow rate, carbon black content, oxidation induction time, and tensile properties. Density is determined by ISO 1183-1:2019 and normally falls within 0.958–0.961 g/cm³. Melt flow rate at 190°C/5 kg is measured by ISO 1133-1:2022 and is expected below 0.35 g/10 min. Carbon black content measured by ISO 6964 is typically 2.0–2.5% by mass. Oxidation induction time at 210°C is determined by ISO 11357-6; PE100 pipe compounds of this class commonly show 20 min or longer, but the acceptance criterion is set by the applicable pipe product standard. Tensile yield stress measured by ISO 527-2 is normally above 22 MPa, and elongation at break exceeds 600%. These resin-level values are not substitutes for pipe-level hydrostatic testing.
The bimodal molecular weight distribution combines a low-molecular-weight fraction that improves melt processability with a high-molecular-weight fraction that increases tie-molecule density between crystalline lamellae. Slow crack growth resistance in notched pipe testing under ISO 13479 is highly sensitive to tie-molecule density; PE100 compounds of this architecture are therefore expected to exhibit longer failure times at 80°C than legacy unimodal grades of similar density. The long-term hydrostatic strength is not a single laboratory point but a regression analysis under ISO 9080, using stress-rupture data from pipe specimens tested at multiple temperatures. For PE100 classification under ISO 12162, the lower predictive confidence limit at 50 years must be at least 10 MPa at 20°C. This permits higher design pressures or reduced wall thickness relative to PE80, whose minimum required strength is 8 MPa under the same standard. Rapid crack propagation arrest is measured by the small-scale steady-state test ISO 13477; bimodal pipe grades typically show a higher arrest pressure than unimodal PE80 because the high-molecular-weight fraction increases resistance to dynamic crack propagation.
Published data for this specific configuration should be supplemented with pipe-level validation. The resin datasheet alone does not establish pipe performance; extruded pipe must meet the dimensional and mechanical requirements of the applicable product standard. The notched pipe test under ISO 13479 is carried out on pipe with a circumferential notch, and acceptance depends on wall thickness, test temperature, and internal pressure. The use of 80°C and a specified hoop stress is common for PE100 materials, but the exact stress level and failure time threshold are defined by the national or project specification.
Rheologically, the grade exhibits high shear sensitivity and a broad molecular-weight distribution. In capillary rheometry, the flow curve shows pronounced shear thinning, allowing high throughput at high die shear rates while retaining high melt strength at low shear. The high melt strength is essential for maintaining wall thickness in large-diameter pipe during vacuum calibration. A melt pump after the screw helps isolate die pressure from screw pulsation, but specific energy consumption and output are machine-dependent; published data for this specific configuration is limited.
Pipe extrusion is typically performed on grooved-feed single-screw extruders with screw length 30 L/D to 36 L/D, barrel temperatures from 200°C to 220°C, and melt temperature below 240°C. Prolonged residence time above 240°C accelerates oxidative degradation, measurable as a reduction in oxidation induction time under ISO 11357-6. A desiccant dryer is not mandatory for sealed packages; if the granules are exposed to relative humidity above 60%, pre-drying at 80°C for 2–4 h removes surface moisture and reduces pinholing. Die-head pressure, melt pump speed, and haul-off ratio are adjusted to control diameter and wall thickness; vacuum calibration tanks with water at 15–25°C are used to set the outer diameter and cool the pipe. Weld lines at the spider legs of the die require sufficient melt temperature and backpressure to maintain a homogeneous wall. Screen packs of 40/60/40 mesh are common for contamination control. Regrind addition should be limited to clean, unpigmented pipe of the same compound; additions above 10% should be qualified by melt flow rate measurement and notched pipe performance because repeated extrusion lowers stabiliser content and may increase gel formation.
Batch-to-batch variation is controlled by the manufacturer, but processors should compare the certificate of analysis against internal process limits. A deviation in melt flow rate of more than ±0.05 g/10 min from the qualified baseline can alter die pressure and wall thickness control, particularly in large-diameter pipe lines. Processors using automatic die centring should recalibrate the ultrasonic wall-thickness gauge if the regrind fraction or melt temperature is changed.
The design basis for pressure rating is established by ISO 9080 regression, not by short-term burst strength. For PE100, the lower predictive limit at 20°C and 50 years must be at least 10 MPa; pipe standards apply a design coefficient, commonly 1.25, to convert this to an allowable service stress. Under ISO 4427-2, SDR 11 PE100 pipe is rated for 16 bar at 20°C for water, while the same SDR in PE80 is rated for 12.5 bar. This is a direct consequence of the difference between 10 MPa and 8 MPa minimum required strength. The carbon black loading specified by ISO 6964 is typically 2.0–2.5% by mass and must be finely dispersed; agglomerates above the specified size act as stress concentrators and may reduce slow crack growth resistance under ISO 13479. Ultraviolet stabilisation by carbon black allows outdoor storage of black pipe, but national water utility specifications may still limit storage duration because surface oxidation can affect fusion quality.
Fusion joining of TUB121 N3000 is performed by butt fusion, electrofusion, or socket fusion according to ISO 21307 and the fitting manufacturer's procedure. The melt flow rate of the pipe and fitting must be within the compatibility limits specified; mixing PE100 with PE80 or with a non-black HDPE of different molecular weight can produce a weaker melt interface. Butt fusion machines should maintain specified bead-up pressure, heater plate temperature, and cooling time; the joint is then evaluated by bend-back or tensile testing according to the applicable national standard. Failure to remove oxide skin or to align pipe ends produces fusion defects that may not be evident until service load is applied; ISO 21307 requires that the heater plate be clean and within calibrated temperature.
PE100-RC materials are a specialised sub-class of PE100 with additional resistance to slow crack growth and point loading, validated through notched pipe tests, full-scale point-load tests, and extended-duration hydrostatic tests that exceed standard PE100 requirements. TUB121 N3000 is a standard PE100 pipe compound and should not be assumed to carry PE100-RC status unless current INEOS documentation or a national certification body explicitly lists that classification. For trenchless installation, sandless bedding, or recycled aggregates with sharp stones, project specifications may require PE100-RC; standard PE100 may be acceptable only where the design stress is reduced or a protective sand layer is provided.
In chlorinated potable water service, pipe-level oxidation resistance is affected by disinfectant concentration, temperature, and pressure. Standard PE100 compounds may be used within the limits given by national potable water specifications, but accelerated chlorine immersion tests such as ASTM F2263 or evaluation procedures based on ISO 1167 with chlorinated water are used to verify fitness. Published data for TUB121 N3000 in high-chlorine service is limited; pipe manufacturers should request current test reports from the compound supplier or perform pipe-level testing on the finished product.
Compared with non-black PE100 grades used for cable conduit or temporary surface pipe, the carbon black in TUB121 N3000 improves ultraviolet resistance but can complicate visual inspection of weld quality and may not meet colour codes for gas distribution. Gas pipe applications are specified under ISO 4437 and frequently require yellow PE100 with a different stabiliser package and higher melt flow rate for smaller diameters. TUB121 N3000 is suitable for water and pressure sewer applications; it is not designated for natural gas unless specifically approved for that service. In comparison with high-density polyethylene materials outside the pipe industry, such as bottle or film grades, this pipe grade has a much lower melt flow rate and higher notched pipe test performance, but it has lower melt processability and is not suitable for thin-wall injection moulded articles.