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INEOS HDPE ELTEX TUB121N

    • Product Name: INEOS HDPE ELTEX TUB121N
    • 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 608912
    Polymertype High Density Polyethylene (HDPE)
    Density 0.959 g/cm³
    Meltflowrate 190 5 0.22 g/10 min
    Meltflowrate 190 21 6 6.0 g/10 min
    Mrs 10.0 MPa
    Peclassification PE100
    Color Black
    Carbonblackcontent 2.0-2.5 %
    Oxidationinductiontime >20 min at 200 °C
    Tensilestressatyield 25 MPa
    Tensilestrainatbreak >600 %
    Flexuralmodulus 1100 MPa
    Charpynotchedimpactstrength 10 kJ/m² at 23 °C
    Vicatsofteningtemperature 125 °C

    As an accredited INEOS HDPE ELTEX TUB121N factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing INEOS HDPE ELTEX TUB121N is packaged in 25 kg polyethylene bags, with 55 bags per pallet (1,375 kg total).
    Container Loading (20′ FCL) 20′ FCL loaded with INEOS HDPE ELTEX TUB121N pellets, non-hazardous, in 25 kg bags, palletized, shrink-wrapped; approx. 18–20 MT net.
    Shipping INEOS HDPE ELTEX TUB121N is normally shipped as non-hazardous polymer pellets in 25 kg PE bags on stretch-wrapped pallets. Use clean, dry, covered trucks/containers. Protect from moisture, UV, heat, and contamination. Maintain ambient conditions, avoid bag damage, keep labels intact, and check local transport regulations. No dangerous-goods documentation required.
    Storage Store INEOS HDPE ELTEX TUB121N in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, flames, and incompatible substances. Keep original bags sealed and pallets off the floor to prevent moisture and contamination. Avoid prolonged outdoor exposure. Maintain stable stacking, good housekeeping, and first-in, first-out stock rotation. Follow local regulations and the supplier SDS.
    Shelf Life Typically 24 months from production when stored unopened in original packaging, in a cool, dry area away from sunlight and moisture.
    Application of INEOS HDPE ELTEX TUB121N

    In municipal potable water pressure-pipe extrusion, INEOS HDPE ELTEX TUB121N is processed as a PE100-classified compound whose long-term hydrostatic strength at 20 °C for 50 years is not less than 10.0 MPa when regression analysis follows ISO 9080:2022 and material classification follows ISO 12162:2009. The applicable product standards are EN 12201-1:2011, EN 12201-2:2011, ISO 4427-1:2019, ISO 4427-2:2019, ANSI/AWWA C901-17, and ANSI/AWWA C906-15. The grade is supplied as a black compound with carbon black content controlled between 2.0% and 2.5% by weight, and its melt mass-flow rate is typically 0.20 g/10 min to 0.30 g/10 min at 190 °C under a 5 kg load when tested according to ISO 1133-1:2022. Density is typically 0.955 g/cm³ to 0.960 g/cm³ under ISO 1183-1:2019. Because drinking-water approvals are issued on the finished pipe rather than on the resin alone, the structural wall is maintained at 100% virgin TUB121N in most national schemes. Clean in-house regrind from the same production lot may be added only to the outer layer at a maximum of 10% by weight, provided the regrind has not been in chlorinated service, has not been stored outdoors for more than 12 months, and has passed hydrostatic revalidation at 80 °C for 165 h at 4.5 MPa on SDR 11 pipe before reintroduction.

    Production of potable water mains from TUB121N is carried out on grooved-feed single-screw extruders rather than twin-screw machines, because the grooved feed bushing generates the forward conveying force required to suppress slip in this high-molecular-weight melt. Screw designs with an L/D ratio between 30:1 and 36:1, a barrier section in the compression zone, and a spiral mandrel distribution head are typical on operating lines. Temperature settings from the feed throat to the die are staged from 180 °C to 210 °C in the barrel, 205 °C to 220 °C at the adapter, and 200 °C to 215 °C at the die; melt temperature measured at the extruder gate is kept between 195 °C and 225 °C. At melt temperatures below 195 °C, pipe lines can exhibit intermittent melt fracture at the die lip and carbon-black agglomerates can remain visible in the wall; above 230 °C, oxidation accelerates and peroxide-catalysed chain scission increases the gel count. Pipe calibration uses a vacuum tank held at −0.6 bar to −0.8 bar and spray-cooling water between 35 °C and 60 °C, with final pipe surface temperature below 25 °C before coiling or cutting. Terminal products include blue-striped or fully black potable water mains from DN 20 mm to DN 1200 mm in SDR 7.4 to SDR 41, supplied in 6 m and 12 m bars for larger diameters and 50 m to 150 m coils for small service pipes. Because HDPE is non-hygroscopic, predrying is normally unnecessary; however, if pellets are stored at relative humidity above 60% or exposed to rain during transloading, visible surface condensation is removed by a 2 h hot-air drying step at 80 °C before the material enters the feed hopper.

    What Practical Limits Govern TUB121N Use in Buried Gas Distribution Networks?

    Natural gas distribution pipes manufactured from TUB121N are regulated by ISO 4437-1:2014, ISO 4437-2:2014, EN 1555-1:2021, EN 1555-2:2021, ASTM D2513-20, and the performance requirements of 49 CFR Part 192 in the United States; European operators additionally reference DVGW GW 335. The addition-ratio parameter for gas pipe is narrower than for water pipe: the structural pipe wall is 100% virgin TUB121N, post-industrial or post-consumer regrind is not permitted, and if a coextruded yellow identification layer is specified, the yellow masterbatch is loaded in that skin layer at 4% to 6% by weight with the same PE100 carrier resin, giving a skin thickness of 0.2 mm to 0.4 mm. This exclusion of regrind is driven by rapid crack propagation resistance and the requirement for long-term hydrostatic strength without flaw populations.

    The production process for gas-distribution pipe consumes the same grooved-feed single-screw extrusion platform, but the operating window is deliberately tightened to a melt-temperature band of 205 °C to 220 °C and a screw-speed band that keeps head pressure above 220 bar on DN 90 mm to DN 315 mm lines. Insufficient homogenisation at lower pressures produces visible pigment striations and raises the probability of slow crack growth initiation at score defects. The extruded pipe is tested on every production run by notched pipe testing according to ISO 13479:2022 at 80 °C under hoop stress of 4.0 MPa or 4.5 MPa depending on SDR, and rapid crack propagation is characterised by the S4 test of ISO 13477:2022 or the full-scale test of ISO 13478:2022. Terminal products are black PE100 gas mains and service pipes with yellow identification stripes, DN 20 mm to DN 630 mm, SDR 11 and SDR 17, supplied in straight lengths up to 20 m or coils from 50 m to 150 m for small-diameter services.

    Compliance and formulation reference for TUB121N downstream applications
    ApplicationPrimary compliance standardsAddition ratioTerminal product types
    Potable water pressure pipeEN 12201-1:2011, EN 12201-2:2011, ISO 4427-1:2019, AWWA C901-17100% virgin wall; in-house regrind ≤ 10% outer layerDN 20 mm–1200 mm, SDR 7.4–41 mains
    Buried gas distributionISO 4437-1:2014, EN 1555-1:2021, ASTM D2513-20, 49 CFR Part 192100% virgin wall; regrind not permitted; yellow skin masterbatch 4%–6%DN 20 mm–630 mm, SDR 11/17 gas mains
    Landfill leachate handlingDIN 8074:2011, DIN 8075:2011, EN ISO 175:2016100% virgin wall; in-house regrind ≤ 5%DN 110 mm–400 mm perforated and slotted lines
    Mining slurry and tailingsISO 9080:2022, ISO 12162:2009, ISO 4427-1:2019, ASTM D4060-19100% virgin wall; in-house regrind ≤ 5%DN 160 mm–1200 mm, SDR 7.4–17 tailings pipes
    Closed-loop geothermal circuitsANSI/CSA C448.1-22, EN 12201-2:2011, ASTM D3035-21100% virgin compound; regrind excludedDN 25 mm–40 mm, SDR 9/11 loop coils
    HDD and trenchless rehabilitationASTM F714-19, ISO 11298-1:2018, ASTM F1962-21100% virgin structural wall; in-house regrind ≤ 5% outer layerHDD pipe strings and liners, SDR 7.4–11
    Cable protection ductingIEC 61386-24:2019, ASTM F2160-19, EN 61386-24:2010100% virgin outer layer; in-house regrind ≤ 20% inner wallDN 40 mm–200 mm solid-wall and double-wall conduits

    Leachate collection and transfer lines in municipal solid waste containment systems are produced from TUB121N as solid-wall and post-extrusion perforated pipes where chemical resistance and stress-crack resistance dominate selection. Because no single harmonised product standard covers leachate pipe, the relevant compliance framework is normally DIN 8074:2011 and DIN 8075:2011 for pipe dimensions and material, ASTM D3350-21 cell classification for HDPE used in leachate collection, and chemical resistance testing according to EN ISO 175:2016. If the pipe is perforated, slotted, or used in a landfill drainage blanket, the design life requirement of 30 years under the EU Landfill Directive 1999/31/EC typically applies. The pipe wall is formulated at 100% virgin TUB121N; post-consumer recyclate is excluded, and in-house regrind is limited to 5% by weight because leachate pH can vary from 4 to 10 and organic constituents vary across cells. Carbon black content for UV-exposed sections is maintained between 2.0% and 2.5% by weight, which is normally already present in the compound.

    The extrusion process uses a 30:1 to 36:1 L/D grooved-feed single-screw line; melt temperature is held at 200 °C to 220 °C. Perforations are cut, drilled, or punched offline after vacuum calibration to avoid wall collapse. Butt fusion follows ISO 21307:2017 procedures, with bead size controlled by ring fusion pressure. Terminal products include perforated and slotted drainage pipe in DN 110 mm to DN 400 mm, SDR 11 and SDR 17, and solid-wall transfer lines for leachate pumping stations. Published data specific to TUB121N under long-term exposure to concentrated landfill leachate is limited; therefore site-specific immersion testing on finished pipe according to EN ISO 175:2016 is required before final material selection.

    When Coarse Particulate Slurries Justify a Thick-Wall HDPE Pipe

    For mineral tailings, dredging, and process-water return lines, TUB121N is selected when the piping system must combine pressure rating with abrasion resistance and resistance to lime-scaling. The governing pressure classification remains ISO 12162:2009 under ISO 9080:2022, and dimensional selection follows ISO 4427-1:2019 and ISO 4427-2:2019; for mining-process slurry applications, published design standards are less prescriptive than for potable water, so engineering firms often add the modified sand-slurry abrasion test of ASTM D4060-19 and the cumulative-damage estimation principles of ISO 13760:2018. The addition-ratio envelope for the structural wall is 100% virgin TUB121N; external recyclate is not used, and in-house regrind is capped at 5% because pipe extracted from abrasive service can retain embedded fines that create flaw sites. For tailings lines where a harder inner surface is desired, coextrusion with a black TUB121N skin layer containing 2.0% to 2.5% carbon black does not change the pressure-bearing cross-section, but addition of abrasive-resistant or UHMWPE modifiers to the inner layer is not covered by published INEOS data for this specific configuration.

    Thick-wall pipe production for slurry service is a deep-dive process zone because cooling shrinkage and frozen-in stress become the dominant quality constraints. The same single-screw grooved-feed extruder is used, but the haul-off speed is reduced for wall thicknesses above 50 mm and the cooling tank water is staged from 60 °C in the first chamber to 20 °C in the final spray, limiting the cooling-rate differential to below 1.5 °C/min across the wall. Excessively fast cooling produces a radial residual-stress gradient that can lower long-term hydrostatic strength at the inner wall. Terminal products are SDR 7.4 to SDR 17 slurry lines from DN 160 mm to DN 1200 mm, with butt-fusion joints per ISO 21307:2017 and flanged adapters at pump stations.

    Closed-loop ground source heat pump circuits impose low internal pressures but demand a 50-year service life under cyclic thermal loading. The installation and product standards are ANSI/CSA C448.1-22, EN 12201-2:2011 for PE100 pressure pipe, and ASTM D3035-21 for standard outside-diameter controlled PE pipe. TUB121N is used at 100% virgin compound in the entire loop because in-house regrind is excluded from closed-loop ground heat exchangers subject to antifreeze solutions and thermal fatigue cycling from −5 °C to 40 °C. The polymer has a thermal conductivity of approximately 0.40 W/(m·K) to 0.42 W/(m·K); published data for this exact grade under geothermal heat-transfer fluid is limited, so fluid compatibility testing is required for propylene-glycol and ethanol-water mixtures.

    The pipe is extruded on small-diameter grooved-feed single-screw lines at melt temperatures of 200 °C to 220 °C, vacuum-calibrated to SDR 9 or SDR 11, and coiled into 150 m to 300 m loops. After loop fabrication, socket fusion and butt fusion per ISO 21307:2017 produce U-bend manifolds. Terminal products are vertical borehole U-bend loops and horizontal ground loops, typically DN 25 mm to DN 40 mm, with no threaded transitions because HDPE cannot be joined reliably by threading.

    HDD Rehabilitation Pipe Wall Conditions and Butt-Fusion Quality Windows

    Horizontal directional drilling and trenchless pipe renewal place TUB121N in a stress regime dominated by pull force, external collapse, and bending curvature rather than continuous internal pressure. The governing standards include ASTM F714-19 for solid-wall HDPE pipe used in water and sewer applications, ISO 11298-1:2018 for polyethylene pipe used in trenchless installation, and ANSI/AWWA C906-15 for pressure-class PE pipe; installation design is typically checked against ASTM F1962-21 for HDD pull force estimation. The formulation addition ratio is 100% virgin TUB121N in the structural wall, with in-house regrind restricted to 5% or less and located only in the outer layer; no post-consumer material is added because pull force calculations assume a uniform polyethylene matrix without contaminant flaw populations.

    Pipe strings for HDD are produced as thick-wall SDR 7.4 to SDR 11 pipe and butt-fused into lengths exceeding 500 m where site layout permits. The extrusion window is shifted slightly toward higher melt temperature 210 °C to 225 °C to reduce frozen-in orientation in thick pipe walls; calibration vacuum is maintained at −0.8 bar to control outside-diameter tolerance for butt-fusion alignment. On production lines, the limiting bottleneck is not the extruder but the cooling table length, because SDR 9 pipe above DN 500 mm requires staged cooling to keep the surface temperature below 25 °C before cutting. Terminal product forms include pull-in pipe strings for water and sewer pressure renewal, pipe-liner segments for sliplining, and sacrificial HDD casing strings where the HDPE pipe is used as the outer conduit.

    Power and fibre-optic cable ducting produced from TUB121N departs from pressure-pipe logic because the performance criterion is crush resistance and UV stability rather than hydrostatic strength. The applicable standards are IEC 61386-24:2019 for buried conduit systems, ASTM F2160-19 for solid-wall HDPE conduit, and EN 61386-24:2010 in the European market. Because these ducts are not pressure-rated, the formulation addition ratio can include up to 20% in-house regrind by weight in the inner wall or non-visible layers, while the outer exposed layer remains 100% virgin TUB121N with carbon black at 2.0% to 2.5% for UV stabilisation. Post-consumer regrind is still excluded unless it originates from the same HDPE conduit production line and is tested for density and melt mass-flow rate according to ISO 1183-1:2019 and ISO 1133-1:2022.

    Extrusion on a grooved-feed single-screw line at 190 °C to 210 °C is followed by vacuum calibration and spray cooling; corrugated double-wall construction adds a second extruder for the smooth inner wall, with the TUB121N outer shell providing ring stiffness. Terminal products include DN 40 mm to DN 200 mm solid-wall and double-wall corrugated ducts, fibre-optic microduct bundles, and high-voltage power conduits supplied on reels up to 1000 m.

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    Certification & Compliance
    More Introduction

    INEOS HDPE ELTEX TUB121N is a bimodal high-density polyethylene extrusion grade intended for pressure pipe manufacture. The grade is supplied in pellet form and carries the CAS number 9002-88-4. Its nominal density is 0.959 g/cm³ when tested to ISO 1183-1:2019, and its melt flow rate under 5 kg load at 190 °C is 0.22 g/10 min when tested to ISO 1133-1:2022. The material is classified as PE100 with a minimum required strength of 10.0 MPa at 20 °C for 50 years according to ISO 12162:2014, based on long-term hydrostatic strength data generated under ISO 9080:2022.

    Table 1: Typical published resin characterisation data for ELTEX TUB121N
    PropertyTest methodTypical value
    DensityISO 1183-1:20190.959 g/cm³
    Melt flow rate, 190 °C / 5 kgISO 1133-1:20220.22 g/10 min
    Tensile stress at yield, 50 mm/minISO 527-2:201225 MPa
    Nominal tensile elongation at breakISO 527-2:2012>600 %
    Flexural modulusISO 178:20191000–1200 MPa
    Environmental stress crack resistance, F20, 10 % Igepal CO-630, 50 °CASTM D1693-21>1000 h
    Oxidative induction time, 210 °CISO 11357-6:2018>20 min
    Minimum required strength, PE100 classificationISO 12162:201410.0 MPa

    Values in Table 1 are typical published values for resin characterisation and should not be read as pipe performance limits. Final pipe properties depend on wall thickness, cooling rate, pigment dispersion, extrusion conditions, and fusion procedure.

    Rheological and Thermal Specifications Governing Pipe Extrusion

    Thermal profiling for ELTEX TUB121N on a grooved-feed single-screw extruder normally begins with a water-cooled hopper zone at 40–70 °C to delay premature melting and stabilize feed pressure. Barrel zone settings increase from 180 °C in the feed section to 220–230 °C in the metering section. Die body and spider temperatures are typically held at 210–220 °C. The measured melt temperature at the die entry should remain within 200–230 °C. At melt temperatures exceeding 250 °C, the residence-time-dependent consumption of hindered phenolic antioxidant becomes detectable through a measurable decline in oxidative induction time under ISO 11357-6:2018. Because the grade has a low 5 kg MFR of 0.22 g/10 min, shear heating in the metering section can be substantial; screw cooling is therefore controlled rather than disabled, and screw speed is adjusted to maintain melt temperature rather than to maximize output.

    Pressure fluctuation before the breaker plate is a sensitive indicator of melt homogeneity. On 45 mm and 60 mm grooved-feed extruders with an L/D of 30:1, stable production of DN 110 to DN 315 pipe generally requires pre-die melt pressure variation below ±5 %. Larger fluctuations, caused by irregular feed bridging or worn screw elements, produce wall-thickness eccentricity that cannot be fully corrected by downstream vacuum calibration. Screen-pack pressure drop should be recorded and the pack replaced before reaching 60–80 bar above the clean-screen baseline; otherwise, melt temperature rises and the stabilizer consumption rate increases.

    Die geometry and drawdown are selected to avoid melt fracture. For SDR 11 pipe, a die gap in the range 0.8–1.2 mm and a land length-to-gap ratio between 15:1 and 25:1 are common. If sharkskin appears at high output, die-lip temperature is raised in 5–10 °C increments, or screw speed is reduced. Surface roughness is not only cosmetic; it can initiate pipe failure under internal pressure testing.

    Specific energy consumption for high-molecular-weight HDPE pipe extrusion is typically 0.20–0.28 kWh/kg on grooved-feed machines. Lower values may indicate insufficient plasticization, while higher values may signal excessive shear. Screw speed and torque limits should be obtained from the extruder manufacturer because the low melt flow rate of TUB121N increases drive motor load compared with medium-density or PE80 resins. On a 60 mm grooved-feed extruder, motor current draw is commonly maintained below 85 % of the nameplate rating to avoid over-temperature trips.

    Gel formation due to melt stagnation in blow-head channels is possible if the die is held at temperature for more than 2 h without purge. Oxidized gel particles appear as pits or contaminant inclusions in the final pipe. Before each start-up, purging with a compatible high-MFR HDPE or a controlled purge compound is used to displace degraded material from the die lips and spider legs.

    What Separates ELTEX TUB121N from PE80 and Unimodal HDPE Grades?

    The main differentiation from PE80 and unimodal HDPE grades is the combination of high-density stiffness and high slow-crack-growth resistance. PE80 has an MRS of 8.0 MPa under ISO 12162:2014, while PE100 such as ELTEX TUB121N is rated at 10.0 MPa. Design stress is calculated as MRS divided by the service coefficient, typically 1.25 for PE. The resulting design stress is 8.0 MPa for PE100 and 6.4 MPa for PE80. At SDR 11, PE100 allows a nominal pressure rating up to PN 16 for water at 20 °C under ISO 4427-2:2019, whereas PE80 is typically rated PN 12.5 at the same SDR. For a given outside diameter and pressure rating, the PE100 wall is thinner than the PE80 wall, reducing material consumption without reducing design stress.

    Compared with single-reactor unimodal HDPE at similar density, the bimodal distribution in pipe-grade PE100 resins separates the high-molecular-weight chains responsible for slow crack growth resistance from the medium-to-low-molecular-weight chains that lower melt viscosity. The result is a simultaneous improvement in processability and long-term crack resistance that is difficult to achieve with a single-peak molecular-weight distribution.

    In slow crack growth testing, the ESCR result for ELTEX TUB121N is generally reported as >1000 h in ASTM D1693-21 condition F20 with 10 % Igepal CO-630 at 50 °C. This is a comparative resin rank, not a pipe lifetime. Pipe-level slow crack growth resistance is validated through notched pipe tests such as ISO 13479:2022. Published data for this specific grade in ISO 13479 is limited; the user should verify pipe-level performance on the actual diameter and SDR.

    Compared with PVC-U pipe, the flexural modulus of HDPE is lower, typically 1000–1200 MPa versus approximately 3000 MPa for rigid PVC. Buried HDPE pipe relies on soil support and pipe wall section to meet ring stiffness; design must follow ring stiffness testing under ISO 9969 rather than direct substitution for PVC. Within the PE100 family, some grades are further classified as PE100-RC for high resistance to slow crack growth, which can be used with reduced or no sand embedding for trenchless installation and re-rounding. TUB121N is a standard PE100 grade; unless the manufacturer has published PE100-RC supporting data for this exact grade, such applications require separate validation.

    Table 2: Primary resin and pipe validation methods
    Validation targetMethodTypical requirement
    Long-term hydrostatic strength of pipe materialISO 9080:2022PE100 MRS 10.0 MPa
    Classification and design coefficientISO 12162:2014PE100, design coefficient 1.25
    Water pressure pipesISO 4427-2:2019PN rating per SDR
    Gas distribution pipesISO 4437-2:2021Hydrostatic and RCP requirements
    Slow crack growth at pipe levelISO 13479:2022No failure under specified hoop stress
    Thermal stabilizer retentionISO 11357-6:2018OIT >20 min at 210 °C

    Downstream calibration and cooling of ELTEX TUB121N require particular attention because of the high recrystallization shrinkage and low coefficient of thermal conductivity of HDPE. Vacuum calibration tank pressure is typically controlled at 0.3–0.6 bar below atmospheric, with spray water maintained at 15–25 °C. Cooling gradients above 30 °C across the pipe circumference increase frozen-in stress and can reduce slow crack growth resistance. For thick-walled pipe above SDR 17, stepwise cooling with multiple tanks is used; the first tank should be tempered rather than chilled to avoid skin solidification before the core is dimensionally stable. Pipe puller speed must be synchronized to extrudate swell; uncontrolled drawdown beyond 1.05:1 may reduce wall thickness below the tolerance band required by ISO 4427-2:2019.

    For black pipe, carbon black masterbatch is typically added at 0.5–2.5 % by mass depending on masterbatch carrier resin and final carbon black concentration. Dispersion is assessed by ISO 18553:2002; agglomerates above the acceptable rating act as crack initiators in pressure service. For outdoor pipe, the carbon black content in the final compound is maintained at 2.0–2.5 % by mass and the dispersion grade is specified in ISO 4427-1:2019. Continuous ultrasonic wall-thickness monitoring is standard because wall-thickness tolerance is pipe-standard dependent and directly affects pressure rating.

    When Oxygen Induction Time Determines Post-Process Durability

    Oxygen induction time as measured on the compounded resin or pipe wall is a control for thermal stabilizer content. A typical PE100 compound used in water pipe manufacture carries an OIT at 210 °C above 20 min when tested with ISO 11357-6:2018. Values below 20 min after multiple passes on a recycling line indicate that the antioxidant package has been partially consumed and that further regrind addition should be restricted. The stabilizer system in PE100 water pipe grades typically combines a hindered phenolic primary antioxidant with a phosphite or phosphonite secondary antioxidant. During melt processing, the secondary antioxidant consumes hydroperoxides, preserving the primary antioxidant for long-term service. A drop in OIT from >20 min to <5 min after five extrusion passes corresponds to near-complete primary antioxidant depletion. For that reason, in-plant regrind content is usually limited to 10–20 % of total feed for pressure pipe unless the regrind is re-stabilized.

    For long-term hot-water service, stabilizer depletion is accelerated. Hydrostatic stress rupture testing under ISO 1167-1:2006 at 80 °C and 1.0 MPa hoop stress is commonly used to confirm resistance to oxidative failure. ELTEX TUB121N is not intended for continuous use above 60 °C in wet service unless the detailed stress-temperature relationship is validated for the specific pipe design. Short-term burst testing at 20 °C may not detect slow crack growth defects; therefore elevated-temperature hydrostatic tests are used. The failure mode should be ductile for valid stress regression.

    Applications for extruded pipe from ELTEX TUB121N include water distribution, sewerage rising mains, industrial process water, and gas distribution. In gas distribution, the final pipe must satisfy odorant and permeation requirements and is usually tested under ISO 4437-2:2021. In mining slurry applications, abrasion resistance depends on pipe wall thickness, particle size, flow velocity, and solids loading; no universal wear lifetime exists. Published data for this specific configuration is limited; laboratory slurry abrasion testing under ISO 15527:2022 is recommended. The grade is not suitable for continuous exposure to strong oxidizers, aromatic hydrocarbons, or chlorinated solvents above 60 °C. For chemical resistance data, refer to ISO/TR 10358:2021. Pre-drying is not necessary for virgin pellets from closed packaging. If cold pellets are taken into a warm extruder hall, condensation can introduce 0.05–0.1 % moisture by mass; a hopper pre-heat at 50–60 °C prevents surface defects. Pellets should be stored under clean conditions to avoid contamination; even low concentrations of polypropylene or PET contamination can cause melt gel defects. Metal detection and magnetic separation are recommended before extrusion. Operating outside these extrusion and installation limits can reduce the pipe’s long-term hydrostatic strength in ways that are not detected by short-term melt flow tests.

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