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INEOS HDPE ELTEX TUB124 N6000

    • Product Name: INEOS HDPE ELTEX TUB124 N6000
    • 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 162566
    Polymer Type High-density polyethylene (HDPE)
    Color Black
    Density 0.959 g/cm³
    Melt Flow Rate 190c 5kg 0.45 g/10 min
    Melt Flow Rate 190c 2 16kg 0.15 g/10 min
    Tensile Stress At Yield 25 MPa
    Tensile Strain At Break >600%
    Flexural Modulus 1200 MPa
    Charpy Notched Impact Strength 23c 15 kJ/m²
    Charpy Notched Impact Strength Minus30c 8 kJ/m²
    Vicat Softening Temperature 126 °C
    Oxidation Induction Time 200c >20 min
    Carbon Black Content 2.25%
    Moisture Content <0.02%
    Thermal Conductivity 0.38 W/m·K
    Coefficient Of Linear Thermal Expansion 1.5E-4 1/K
    Specific Heat Capacity 1900 J/kg·K
    Water Absorption <0.01%
    Dielectric Constant 2.3
    Volume Resistivity >1E14 ohm·cm
    Shore D Hardness 60
    Environmental Stress Crack Resistance >1000 h
    Minimum Required Strength 10 MPa
    Uv Stabilization Yes

    As an accredited INEOS HDPE ELTEX TUB124 N6000 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing INEOS HDPE ELTEX TUB124 N6000: 25 kg polyethylene bags, 55 bags per shrink-wrapped pallet, totaling 1,375 kg.
    Container Loading (20′ FCL) 20′ FCL container loaded with 25 kg PE bags of INEOS HDPE ELTEX TUB124 N6000 on pallets, shrink-wrapped and secured.
    Shipping INEOS HDPE ELTEX TUB124 N6000 is shipped as non-hazardous high-density polyethylene pellets, typically in 25 kg moisture-barrier bags or 1,000–1,250 kg octabins on stretch-wrapped pallets. It is not regulated for transport, with no UN number, hazard class, or special labels. Store dry, away from ignition sources, and avoid pellet spillage.
    Storage Store indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags closed, palletized, and off the floor. Avoid moisture, dust, dirt, and contamination. Maintain moderate temperatures and limit prolonged UV exposure. Follow local regulations and the manufacturer’s SDS.
    Shelf Life INEOS HDPE ELTEX TUB124 N6000 shelf life is typically two years stored unopened, dry, cool, well-ventilated, away from direct sunlight.
    Application of INEOS HDPE ELTEX TUB124 N6000

    Potable water mains manufactured from INEOS HDPE ELTEX TUB124 N6000 are specified under ISO 4427 and EN 12201-2, where the resin is classified as PE100 with a minimum required strength of 10 MPa at 20 °C for 50 years according to ISO 12162 and ISO 9080. The natural grade is compounded in-line with carbon black masterbatch at 2.0–2.5 wt% for black water pipe or coextruded with an outside striping layer at 4–6 wt% pigment masterbatch, depending on the utility specification for UV exposure and chlorine degradation. Extrusion is carried out on a grooved-feed single-screw extruder with L/D ratio 30:1–36:1, barrel temperature profile from 180 °C at the throat to 210 °C in the metering zone, and die/mandrel set at 200–210 °C. The measured melt temperature is held at 190–220 °C; below 190 °C the bimodal high molar mass fraction produces surface melt fracture on the pipe outer wall, while above 220 °C the oxidative induction time measured by differential scanning calorimetry under ISO 11357-6 can fall below the 20 min threshold commonly required in utility specifications. Vacuum sizing is run at −0.2 to −0.5 bar with water temperature 15–25 °C, and haul-off speed is adjusted to maintain SDR 11, SDR 13.6, or SDR 17 dimensions. Terminal products include buried distribution mains, service connection lines, and treatment plant transfer headers; each fusion joint is hydrotested at 1.5× the nominal pressure rating after installation.

    What Limits Rapid Crack Propagation in TUB124 N6000 Gas Mains at Low Ambient Temperature?

    Gas distribution pipe converted from TUB124 N6000 is manufactured to ISO 4437 and EN 1555, with SDR 11 and SDR 17.6 wall configurations for buried mains operating up to 10 bar, although most distribution networks remain below 4 bar. The PE100 designation requires hydrostatic design basis from long-term regression testing under ISO 9080; the 50-year lower prediction limit at 20 °C must remain at or above 10 MPa. Rapid crack propagation is the limiting failure mode at low ambient temperature because a crack initiated at a flaw or impact can propagate along the pipe axis if the stress exceeds the critical arrest stress. Conversion parameters influence this arrest stress directly. Melt temperature above 220 °C, residence time beyond 5 min, or excessive die draw ratio lower the pipe's RCP resistance, which is validated with the small-scale steady-state S4 test under ISO 13477. Yellow gas pipe is made with a UV-stabilized yellow masterbatch at 4–8 wt%; black gas pipe uses carbon black at 2.0–2.5 wt% and dispersion is checked according to ISO 18553. Butt fusion joining is performed with heater plate temperature 220 ± 10 °C and interfacial pressure 0.15–0.25 N/mm²; electrofusion jointing uses the fitting manufacturer's energy input and melt displacement geometry. Terminal products include distribution mains, service risers, and valve transition pieces; fusion joints are peel-decohesion tested under ISO 13955 and crush tested under ISO 13956 before commissioning.

    Compliance and test matrix for pressure pipe applications
    ApplicationSystem standardMaterial or pipe testTypical acceptance value
    Potable water mainsISO 4427 / EN 12201-2MRS classification ISO 12162PE100, 10 MPa at 20 °C
    Fuel gas distributionISO 4437 / EN 1555RCP S4 test ISO 13477Arrest at specified temperature and pressure
    Slow crack growthISO 13479Notched pipe testPE100 utility specifications typically require ≥500 h at 80 °C / 4.0 MPa
    Melt flow rateISO 1133-1Condition 190 °C / 5 kg0.24 g/10 min per manufacturer datasheet

    Mining tailings lines convert TUB124 N6000 into high-wall-thickness pipe of SDR 9 or SDR 11 because the design case adds internal solids abrasion and external handling impact to long-term hydrostatic stress. The bimodal molecular weight distribution is the critical material feature for slow crack growth resistance; notched pipe specimens tested per ISO 13479 must withstand 4.0 MPa at 80 °C for the duration specified by the project, typically 500 h or more before ductile failure is accepted. Extrusion of large-diameter tailings lines uses a single-screw extruder with screw speed 40–80 min⁻¹, melt temperature 190–210 °C, and wall-thickness control according to ISO 4427-2. The pipe is butt-fused on site with heater plate temperature 220 ± 10 °C and bead width controlled to prevent cold fusion at the high wall thicknesses used in SDR 9. Terminal products include tailings transport, dredge discharge, and ash sluice lines. Abrasion resistance in HDPE is not governed by a single ISO pipe standard; published data for TUB124 N6000 under specific slurry regimes is limited, so plant-scale trials with representative particle angularity, solids loading, and flow velocity are required. Chemical resistance is screened against ISO/TR 10358, with continuous service generally acceptable in aqueous slurries between pH 2 and 12 at 20 °C; sustained exposure above 60 °C or contact with strong oxidizers and aromatic solvents shortens design life.

    Brine Transfer Pipe in Seawater Desalination and Industrial Chemical Service

    Desalination brine transfer lines use TUB124 N6000 in SDR 11 and SDR 13.6 because the pipe must withstand internal pressures up to 16 bar at 20 °C while carrying high-salinity water at 20–35 °C, with pressure ratings derived from ISO 4427. The resin is processed at melt temperature 190–215 °C and the extruded pipe is dimensionally checked against ISO 4427-2. In brine service, the polymer's non-polar matrix resists chloride-induced stress cracking at the fusion bond, provided butt fusion is executed according to ISO 21307 and the bead is allowed to cool under pressure. Terminal products include seawater intake lines, brine discharge diffusers, and interconnecting process pipe. Chemical resistance must be verified for each specific brine composition under ISO/TR 10358; concentrated hypochlorite and low-molecular-weight chlorinated solvents are not compatible with HDPE. Long-term hydrostatic strength remains governed by ISO 9080, but the designer must derate for thermal expansion and external seawater pressure when the pipe is submerged.

    When TUB124 N6000 Replaces PE80 in Industrial Force Mains

    Industrial force mains handling treated effluent, cooling water, or process drainage are often re-specified from PE80 to PE100 using the same nominal pressure class. Because TUB124 N6000 has an MRS of 10 MPa, SDR 17.6 pipe can be substituted for PE80 SDR 11 at PN 10, reducing wall thickness and increasing internal bore without reducing the hydrostatic design envelope. The change alters the thermal and fusion behaviour on the extruder: the lower MFR of 0.24 g/10 min at 190 °C/5 kg increases backpressure through the screen pack and die, so screw speed must be adjusted to keep melt temperature below 220 °C. Butt fusion requires re-qualification because thinner walls change heating time, drag pressure, and bead geometry; heater plate temperature remains 220 ± 10 °C but interfacial pressure must be recalculated for the new wall cross-section. Terminal products include industrial transfer lines with flanged transitions, pump station headers, and plant drainage collectors. Cyclic pressure surges in force mains require slow crack growth validation with the notched pipe test of ISO 13479 in addition to steady-state hydrostatic testing.

    Ground-source heat exchange loops extruded from TUB124 N6000 use SDR 11 pipe with U-bend assemblies installed in vertical boreholes or horizontal trenches. The service envelope is −5 °C to 40 °C under aqueous antifreeze mixtures, which places less demand on hydrostatic pressure than on resistance to thermal expansion cycling and slow crack growth at fusion joints. Extrusion runs at melt temperature 190–215 °C with the same vacuum sizing and haul-off controls used for water pipe, but the converter must verify coil memory, ovality, and inside surface smoothness after coiling. Terminal products include U-bend probes, manifold headers, and buried loop circuits; butt fusion joints are made in the field with heater plate temperature 220 ± 10 °C and must be allowed to cool below 60 °C before pressure testing. Published data for TUB124 N6000 under long-term geothermal thermal cycling is limited; project qualification should include hydrostatic pressure tests at 1.5× design pressure after thermal shock cycling between 5 °C and 40 °C to expose fusion-joint defects.

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    Certification & Compliance
    More Introduction

    INEOS HDPE ELTEX TUB124 N6000 is a black high-density polyethylene compound supplied as a ready-to-use pellet for solid-wall pressure pipe extrusion. The product is classified as a PE100 material under ISO 12162, with a minimum required strength of 10 MPa derived from the long-term hydrostatic strength regression in ISO 9080. The melt flow rate measured at 190 °C under a 5 kg load is typically 0.23 g/10 min when tested by ISO 1133-1. Density is typically 959 kg/m³ when measured by ISO 1183-1. Carbon black is present at a nominal loading of 2.0–2.5 wt%, and dispersion is assessed by ISO 18553. The compound is intended for the extrusion of pressure pipe for potable water, raw water, wastewater, and, where national approvals permit, gaseous fuel distribution. It is not formulated for rotational moulding, film, sheet, or thin-wall injection moulding, because the high average molar mass and high melt viscosity under low shear restrict flow in those processes.

    The grade is positioned in the high-molecular-weight end of the HDPE pipe range. The 20 °C, 50-year hydrostatic strength is the reference point for PE100 classification. In water supply pipe systems conforming to EN 12201, the design stress for PE100 is conventionally 8 MPa, but the design value remains subject to the service coefficient in the system standard and national regulations. For gas distribution pipe systems conforming to EN 1555, the compound must additionally be listed against the relevant national gas approval; the raw material datasheet alone does not confer product certification. The black carbon black formulation provides ultraviolet protection for outdoor handling and storage, but the pipe system manufacturer must validate long-term weathering according to the applicable installation guidelines.

    TABLE 1. Typical published property values for INEOS HDPE ELTEX TUB124 N6000
    PropertyTest methodUnitNominal value
    DensityISO 1183-1kg/m³959
    Melt flow rate, 190 °C/5 kgISO 1133-1g/10 min0.23
    Carbon black contentISO 6964wt%2.0–2.5
    Carbon black dispersionISO 18553grade≤3
    Minimum required strengthISO 9080 / ISO 12162MPa10
    Tensile stress at yieldISO 527-2MPa24
    Elongation at breakISO 527-2%>600

    The values in Table 1 are typical literature values and are not release limits. For a specific production lot, the certificate of analysis remains the controlling document. Release testing for pipe-grade black polyethylene generally includes melt flow rate, density, carbon black content, carbon black dispersion, and oxidative induction time. The notched pipe performance and long-term hydrostatic strength are type-tested under qualification procedures rather than repeated on every production lot. The hydrostatic design basis is not a material property alone; it is derived from the long-term hydrostatic strength regression and the design safety factor. ISO 12162 defines the MRS category, and the compound’s PE100 classification is a necessary but not sufficient condition for pressure pipe compliance.

    Where Does ELTEX TUB124 N6000 Fit Within the INEOS HDPE Pipe Grade Range?

    Within the INEOS HDPE pipe portfolio, ELTEX TUB124 N6000 is specified as a PE100-RC grade, where RC denotes raised resistance to slow crack growth and point loading. The suffix N6000 identifies the black compound form of the product. This places it alongside conventional PE100 grades but differentiates it from standard pipe compounds that are primarily intended for open-trench installation in stone-free, compacted bedding. The density and melt flow rate of TUB124 N6000 are not greatly different from those of standard PE100 black compounds; the distinction is expressed in component-level tests such as ISO 13479 and full-scale point-load evaluations. A conventional black PE100 grade may show the same minimum required strength of 10 MPa under ISO 9080 but fail earlier under notched conditions. In practical terms, the product is selected when the pipe will be exposed to surface damage, point forces, or tensile installation loads above the baseline buried-pipe case.

    Compared with ELTEX TUB121 N6000, a black PE100 grade intended for conventional pressure pipe service, TUB124 N6000 has a deliberately modified molecular architecture and comonomer distribution that improves slow crack growth resistance without shifting density or melt flow rate into a different product class. The two products are not direct substitutes in specification writing; a design engineer should verify the required PE100-RC performance class and the specific certification status. Compared with PE80 pipe compounds, the shift from an MRS of 8 MPa to 10 MPa allows higher design stress and reduced wall thickness at equal internal pressure, but the pipe system must still meet the minimum wall thickness provisions and installation damage limits in the applicable pipe standard. ELTEX TUB124 N6000 also differs from black compounds used for corrugated pipe or structured-wall pipe; those products may use lower-density or lower-molecular-weight grades because the wall stress regime and installation methods are different. PE100-RC materials are specified under documents such as PAS 1075 for alternative installation techniques. The designation is not defined by ISO 12162; it is a sector-specific classification developed to identify materials with raised resistance to slow crack growth for trenchless installation and rocky ground. Certification to these documents is completed at the pipe system level, not by the raw material alone.

    If Pipe Installation Is Carried Out by Trenchless Methods or in Rocky Ground, the Slow Crack Growth Response Becomes Controlling

    The long-term pressure resistance of high-density polyethylene pipe is usually described by the stress-rupture relationship in ISO 9080. At high stress and short times, failure is ductile and occurs by yielding of the pipe wall. At low stress and long times, failure occurs by slow crack growth through the pipe wall. A surface scratch, rock contact, or bending point introduces a local stress concentration that can move the failure mode toward the brittle branch at shorter times. The ISO 13479 notched pipe test is used to compare materials under this damage mechanism. A circumferential notch is machined into the outer surface of a pipe specimen, and the pipe is pressurised at elevated temperature, typically 80 °C, until failure. The failure time under these conditions is a comparative indicator of slow crack growth resistance. The pass/fail value is not fixed by the material supplier but by the relevant pipe product standard or certification scheme. Published data for this specific product configuration should be requested from the pipe manufacturer because the result depends on pipe diameter, wall thickness, notch depth, test pressure, and specimen preparation.

    Trenchless installation methods, including pipe bursting, slip lining, close-fit lining, and horizontal directional drilling, impose axial tension, bending, and surface scoring that are not present in conventional open-trench laying with sand bedding. The pipe may be pulled over fragments of the old pipe, angular stones, or borehole debris. The outer surface can accumulate scratches that act as crack initiation sites. A PE100-RC grade is formulated to resist crack initiation and propagation under these conditions more effectively than a standard PE100 grade. In service, the same resistance is relevant for pipes buried in rocky ground or in soils that settle unevenly. For such conditions, material selection is not based on hydrostatic design basis alone; the slow crack growth classification and the component-level point-load performance are specified by additional documents such as national PE100-RC requirements or PAS 1075 where applicable.

    In the notched pipe test, the notch depth, test temperature, and hydrostatic stress are selected according to the pipe standard or certification scheme. For comparative ranking, the test temperature is generally 80 °C; the internal pressure is set to give a defined hoop stress for the specific pipe dimension. The failure time is recorded, and the failure mode is classified as ductile or brittle. A long brittle failure time indicates slow crack growth resistance; a short brittle failure indicates that the material or pipe processing has reduced the resistance. Because extrusion-induced orientation and thermal history influence test results, the test must be performed on pipe produced under commercial conditions, not on compression-moulded plaques. Published datasheets for the raw material often do not include ISO 13479 failure times because these values are strongly dependent on pipe dimension and extrusion line.

    Slow Crack Growth Mechanisms and Bimodal Molar Mass Distribution

    Slow crack growth in high-density polyethylene is controlled by the density and orientation of tie molecules that connect adjacent crystalline lamellae. When a crack tip advances, tie molecules are stretched and eventually fail; materials with a higher density of tie molecules can sustain more damage before the crack propagates through the bulk. Bimodal HDPE resins use a low-molar-mass fraction to provide melt processability and a high-molar-mass fraction to increase tie-molecule density. The comonomer location and chain length distribution in the high-molar-mass fraction are critical variables. In conventional PE100, these parameters are balanced for hydrostatic strength and extrusion output. In a PE100-RC grade such as ELTEX TUB124 N6000, the molecular design is shifted further toward slow crack growth resistance while retaining the 10 MPa MRS required for PE100. This trade-off is possible because the creep rupture response and the notched pipe response are related but not identical; a material can have the same long-term hydrostatic strength as another and still exhibit longer failure times under a notched or point-load condition.

    The shear thinning behaviour of a bimodal PE100 is also important for pipe extrusion. The low-load melt flow rate of 0.23 g/10 min is not a direct measure of high-shear processability; pipe extrusion grades are often additionally characterised by the high-load melt flow rate at 21.6 kg. The ratio between high-load and low-load MFR gives a qualitative indication of shear sensitivity, but it does not predict slow crack growth resistance. Differences between TUB124 N6000 and other products with similar low-load MFR can therefore be invisible in routine melt flow testing. This is why notched pipe testing and full-scale installation trials are specified for PE100-RC materials. The material supplier’s published datasheet provides the baseline characterisation; the pipe manufacturer must generate the component-level data for the specific pipe dimensions and processing line.

    Pipe extrusion of ELTEX TUB124 N6000 is normally performed on grooved-barrel single-screw extruders with screw diameters between 45 mm and 120 mm and length-to-diameter ratios of 30:1 to 36:1. The grooved feed zone improves solids conveying for the high-molar-mass polymer and stabilises output against pressure fluctuations. A melt temperature at the die entry of 200 °C to 230 °C is typical; melt temperatures above 250 °C should be avoided because they consume stabiliser and reduce oxidative induction time. The die temperature is commonly maintained at 200 °C to 220 °C to control surface finish and wall thickness distribution. The exact temperature profile depends on screw geometry, output rate, and pipe diameter; the manufacturer’s processing guidance and melt temperature verification are used to establish the profile. Pre-drying is not required under normal dry storage. If pellets are exposed to a humid atmosphere above 60% relative humidity and then moved to a warmer hopper, surface condensation can introduce surface defects. In that case, a hopper dryer operating at 70–80 °C can remove surface moisture.

    Filtration of the melt is normally performed with screen packs of 40/60/80 mesh or finer, depending on the pipe wall thickness and the sensitivity of the downstream calibrator. Melt pressure upstream and downstream of the screen pack is monitored; increasing pressure drop indicates screen blockage or insufficient barrel temperature. Screw speed and haul-off speed are matched to maintain outer diameter and wall thickness under vacuum calibration. High-molecular-weight HDPE exhibits high melt strength, which helps resist sag in large-diameter or thick-wall pipe. However, the same high melt viscosity requires sufficient cooling time in the calibrator and spray baths to prevent residual thermal stresses. Cooling should be gradual enough to avoid excessive frozen-in stress, which can reduce slow crack growth resistance in the finished pipe. High-molar-mass HDPE compounds also require higher specific energy input than lower-molecular-weight grades. Extruder drive current and melt temperature should be monitored together; increasing screw speed without increasing barrel heat may raise melt temperature through viscous dissipation. The optimum melt temperature is the lowest temperature at which surface finish and wall thickness consistency are achieved. Overheating the melt to reduce melt pressure can shorten the induction time and create gels; underheating can leave unmolten resin or poor homogenisation.

    Carbon black at 2.0–2.5 wt% is the principal weather-resistance additive in the black compound. The dispersion rating by ISO 18553 is a release parameter because undispersed agglomerates act as stress concentrations and can reduce notched pipe performance. For pipe-grade polyethylene, a dispersion rating of ≤3 is generally accepted, but some water and gas specifications require a tighter limit. Carbon black also absorbs ultraviolet radiation and prevents photodegradation of the pipe wall during outdoor storage. Black pipe can tolerate longer outdoor exposure than unpigmented pipe, but stabiliser depletion eventually occurs at high irradiance and temperature; storage practices should follow the pipe manufacturer’s instructions. Colour variants of pipe compounds use pigment systems that do not provide the same ultraviolet screening as carbon black. The black compound therefore has a different outdoor storage profile than blue, yellow, or orange PE100 grades. The use of ELTEX TUB124 N6000 in black pipe is common in water and gas distribution, but the colour of the pipe is not a substitute for installation marking or system identification.

    The oxidative induction time determined by ISO 11357-6 is used as a measure of stabiliser package adequacy. The minimum OIT is set by the product specification and varies between water and gas applications; it should be obtained from the current material certificate. Like other HDPE pressure pipe grades, ELTEX TUB124 N6000 resists aqueous solutions, saline water, and many neutral chemicals. It is not resistant to strong oxidising acids, aromatic hydrocarbons, chlorinated solvents, or some surfactant solutions; these fluids may reduce long-term strength through environmental stress cracking or plastication. For industrial effluent applications, the chemical resistance of the pipe system must be assessed using the methods in the relevant pipe standards or chemical resistance data. The compound should not be blended with lower-density polyethylene or post-consumer recyclate in pressure pipe unless the blend has been revalidated for the intended pressure class. Recycled material in pressure pipes is restricted by EN 12201 and EN 1555 and is not permitted except in defined layers under the rules of the specific pipe standard.

    Continuous service at elevated temperature requires derating of the pipe pressure rating. The PE100 minimum required strength is referenced to 20 °C; at higher temperatures the long-term strength is lower and the service coefficient and design life must be recalculated according to the pipe system standard. The upper service temperature for pressurised water is typically limited by national standards and is not a material-only property. The product should not be processed above 250 °C, and it should not be exposed to open flame or welding temperatures beyond those used for standard HDPE butt fusion. Avoid combination with additives that generate acid or amine degradation products during extrusion; such additives can accelerate chain scission and reduce oxidative stability.

    Production of PE100 pressure pipe under EN 12201 or EN 1555 requires raw material lot traceability, melt temperature records, dimensional inspection, and periodic short-term hydrostatic testing per ISO 1167. The raw material certificate of analysis issued with ELTEX TUB124 N6000 typically reports melt flow rate, density, carbon black content, carbon black dispersion, and oxidative induction time. Pipe manufacturers must additionally perform type qualification tests, including long-term hydrostatic strength and slow crack growth resistance, on the finished pipe. For site-specific installation conditions, the pipe manufacturer and certification body should be consulted to confirm that the selected pipe and material meet the required PE100-RC performance class.

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