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NOVA Chemicals Sclair MDPE 8405 BK

    • Product Name: NOVA Chemicals Sclair MDPE 8405 BK
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@sinochem-nanjing.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 806339
    Density 0.938 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.50 g/10 min
    Tensile Strength At Yield 17.9 MPa
    Tensile Strength At Break 24.1 MPa
    Elongation At Break >=600%
    Flexural Modulus 896 MPa
    Escr 100 Igepal >5000 hr
    Escr 10 Igepal >1000 hr
    Vicat Softening Point 116 °C
    Brittleness Temperature <= -70 °C
    Hardness Shore D 60
    Thermal Conductivity 0.33 W/m·K
    Coefficient Of Linear Thermal Expansion 1.5E-4 cm/cm/°C
    Specific Heat 1.9 J/g·°C
    Dielectric Constant 2.3
    Dielectric Strength 20 kV/mm
    Volume Resistivity >=1E15 ohm·cm
    Carbon Black Content 2.0%

    As an accredited NOVA Chemicals Sclair MDPE 8405 BK factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing NOVA Chemicals Sclair MDPE 8405 BK is supplied in 25 kg moisture-barrier bags, palletized for convenient handling and storage.
    Container Loading (20′ FCL) 20-foot FCL container loaded with palletized 25 kg bags of NOVA Chemicals Sclair MDPE 8405 BK, securely stowed for transport.
    Shipping NOVA Chemicals Sclair MDPE 8405 BK is shipped as black medium-density polyethylene pellets in moisture-protected 25 kg polyethylene bags, palletized and stretch-wrapped, or in bulk trucks, railcars, or ISO containers. It is non-hazardous for transport; keep dry, away from sunlight and ignition sources, and handle per the SDS.
    Storage Store NOVA Chemicals Sclair MDPE 8405 BK in original, closed packaging in a cool, dry, well-ventilated warehouse. Protect from direct sunlight, heat, flames, sparks, and strong oxidizers. Keep bags sealed to prevent moisture, dust, and contamination. Avoid prolonged outdoor storage, excessive stacking, and physical damage. Follow local regulations and the manufacturer’s SDS.
    Shelf Life Shelf life is generally indefinite when stored dry, cool, and well-ventilated, away from direct sunlight, heat, and ignition sources.
    Application of NOVA Chemicals Sclair MDPE 8405 BK

    When NOVA Chemicals Sclair MDPE 8405 BK is converted into solid-wall natural gas distribution pipe, the material is supplied as a ready-to-extrude black compound with a dispersed carbon black package of 2.0–2.5 wt%. The carbon black dispersion must show no visible agglomerates above 20 μm when assessed under ISO 18553, because larger agglomerates act as stress concentrators during slow crack growth. On a grooved-feed single-screw extruder with an L/D of 30:1 and a barrier mixing section, barrel set points run from 180 °C near the feed throat to 220–230 °C in the metering zone. The melt temperature is held below 240 °C to prevent oxidative chain scission and rapid loss of the stabiliser package; the carbon black phase absorbs shear energy, so the safe processing window between homogenisation and antioxidant depletion is narrow. Die head pressure typically falls between 20 MPa and 35 MPa for pipe diameters of 32 mm to 225 mm, and the calibration train uses vacuum sizing at −20 kPa to −60 kPa with spray-water temperatures of 15–25 °C. The downstream product is an SDR 11 or SDR 17 gas main, conforming to ASTM D2513 and ISO 4437. Under the older gas-pipe nomenclature the material is identified as PE 2708, and under the ISO system it is typically classified as PE 80 with a 50-year minimum required strength of 8.0 MPa at 20 °C derived from ISO 9080 regression analysis. Hydrostatic pressure testing follows ISO 1167 at 20 °C, 60 °C, and 80 °C; slow crack growth is measured by the notched pipe test of ISO 13479 at 80 °C and 4.6 MPa, with PE 80 requirements generally exceeding 500 h. Oxidative induction time measured by ISO 11357-6 at 200 °C remains above 20 min in the pipe wall. The terminal product is a welded gas distribution main with butt fusion and electrofusion joints used in pressure tiers up to 0.4–0.8 MPa depending on SDR and derating factors.

    What Process Limits Govern Trenchless Slip-Lining of Ageing Cast-Iron Mains?

    Where the compound is used as a replacement string for deteriorated cast-iron or ductile-iron gas mains with internal diameters between 150 mm and 400 mm, the primary compliance framework shifts from new-pipe manufacture to trenchless insertion. ASTM D2513 continues to govern material and pipe dimensions, but the installation step is covered by ASTM F1804 for allowable tensile pull loads and ISO 11299-1 for renovation of underground gas supply networks. No change is made to the compound formulation; the carbon black level remains 2.0–2.5 wt%. External surface treatment is limited to water-based lubricants that do not migrate into the pipe wall or alter fusion compatibility. Field butt fusion is performed with ISO 21307 parameters: heater plate surface temperature of 200–230 °C, interfacial pressure of 0.15 MPa during heating and cooling, and cool-time extension to 10–12 min for 110 mm wall sections. Pull-in force is calculated using the allowable tensile load method of ASTM F1804, with safe pull stress generally capped at 0.50 × yield stress, and the maximum pulling load for a 110 mm SDR 11 string is typically kept below 50 kN to avoid ductile necking. Because insertion passes through scale, tuberculation, and ovalised carriers, resistance to slow crack growth is the dominant material property; proof tests include the notched pipe test of ISO 13479 and, where specified, the notch tensile test of ASTM F1473 under constant load. The terminal product is an inserted gas main segment that retains pressure capability after insertion and is terminated by mechanical or electrofusion transition fittings at the old main boundaries.

    In landfill gas collection and anaerobic digester systems, the same black MDPE compound is used for perforated and solid-wall gas laterals operating under negative pressure of −5 kPa to −30 kPa and continuous temperatures near 40 °C. The formulation is not adjusted for biogas service; the carbon black loading remains 2.0–2.5 wt% and no antistatic agent is introduced, because the pipe wall is not formulated to provide surface conductivity and static dissipation must be addressed at system level if required. Since dedicated global standards for landfill gas piping are limited, project specifications typically reference ISO 4437 for the pipe material and require methane permeability testing according to ISO 17455 on extruded wall specimens. Process conditions are identical to natural gas pipe extrusion, but downstream inspection adds gas-transmission-rate measurement and butt-fusion decohesion testing according to ISO 13953. Published data for the permeability of this specific compound at landfill gas partial pressures are limited; engineering reviews therefore use conservative design factors and account for methane partial pressure rather than total gas pressure. At 40 °C service temperature, the system pressure rating is derated by a factor of 0.74 relative to the 20 °C rating, consistent with standard polyethylene pressure derating curves. The terminal product is a 110 mm or 160 mm SDR 17 collection lateral with butt-fused joints and flame-arrestor transition connections to gas recovery equipment.

    When Low Ambient Temperatures Dominate Open-Trench Installation in Northern Latitudes

    At ambient temperatures below −20 °C, the compound’s lower crystallinity relative to unimodal HDPE reduces the probability of rapid crack propagation during fieldwork, but does not eliminate handling restrictions. The material must demonstrate small-scale steady-state rapid crack propagation resistance under ISO 13477 at 0 °C or colder as specified by the utility, and incoming lots may be screened with ISO 9854-1 Charpy tests. The formulation ratio remains unchanged; pipe conditioning before installation requires exposure to temperatures above −5 °C for at least 24 h when the pipe has been stored below −20 °C. Field bending is restricted to a radius not less than 25 × outside diameter for SDR 11 pipe, and squeeze-off of gas flow is avoided below −10 °C unless the pipe is reheated and the squeeze-off tool is fitted with rounded bars sized to the specific diameter. Butt fusion in low-temperature environments is performed inside heated shelters, with heater plate surface temperature maintained at 200–230 °C and the fusion surface protected from ice-crystal formation. The terminal product is a cold-climate gas main or service lateral that retains joint integrity during temperature cycling and satisfies ASTM D2513 and ISO 4437 supplemental low-temperature requirements.

    Coiled Service-Line Extrusion and Residual Stress Management

    Small-diameter gas service lines from 20 mm to 63 mm are extruded from the same ready-to-use black compound into SDR 11 coils. Compliance for Canadian and European utilities includes CSA B137.4, ISO 4437, and ASTM D2513. The carbon black concentration is controlled at 2.0–2.5 wt% for UV stability during outdoor storage, and clean in-house regrind is limited to 10 wt% unless the utility specification permits otherwise. The extrusion line is configured with a die gap of 1.5–2.0 × wall thickness and a vacuum calibration tank to minimise residual hoop stress. Coiling is performed with constant-tension winders set below 0.25 × the tensile yield stress, and coil diameter is maintained above 20 × outside diameter to prevent kinking and local stress concentrations that accelerate slow crack growth. Electrofusion and butt fusion joints are qualified by peel or crush decohesion tests under ISO 13954 and ISO 13955, and service-line squeeze-off is qualified under ISO 13955 or the relevant utility practice for flow interruption. The terminal product is a coiled PE 80 service line in lengths of 50 m or 100 m, uncoiled in the field at temperatures above −10 °C without kinking.

    The Grade Functions as a Pressure Barrier in Coalbed Methane Gathering Networks

    In coalbed methane gathering service, the compound is fabricated into 90 mm to 180 mm SDR 17 lines that run from wellheads to central processing stations. The governing regulatory framework often combines ASTM D2513 for the pipe material with ASME B31.8 for gas transmission and distribution piping, although the final specification depends on the producing jurisdiction. The carbon black loading remains 2.0–2.5 wt%; no additional internal layer or compatibiliser is used. The pipe is butt-fused in wind-shielded conditions at ambient temperatures above 5 °C, with the same ISO 21307 parameters as natural gas distribution pipe. Because wellhead gas may contain water, coal fines, and light aliphatic hydrocarbons, the operational pressure rating is derated from the 20 °C rating according to standard polyethylene pressure derating curves, which gives a factor near 0.87 at 30 °C and approximately 0.74 at 40 °C. Continuous exposure to liquid aromatic hydrocarbons is excluded, as such environments reduce polyethylene long-term strength and are outside the intended service envelope. The terminal product is a buried gathering line with butt-fused joints and transition fittings that connect to steel wellhead piping.

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