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Seculene PPR 1040 TV30 S0 PP Copolymer

    • Product Name: Seculene PPR 1040 TV30 S0 PP Copolymer
    • 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 638228
    Density Iso 1183 1.13 g/cm³
    Melt Flow Rate Iso 1133 230 C 2 16 Kg 10 g/10 min
    Tensile Modulus Iso 527 3200 MPa
    Tensile Stress At Yield Iso 527 27 MPa
    Tensile Strain At Yield Iso 527 3.0 %
    Flexural Modulus Iso 178 3000 MPa
    Charpy Notched Impact At 23 C Iso 179 1ea 4 kJ/m²
    Charpy Notched Impact At 20 C Iso 179 1ea 2 kJ/m²
    Heat Deflection Temperature 0 45 Mpa Iso 75 2 B 110 °C
    Heat Deflection Temperature 1 8 Mpa Iso 75 2 A 65 °C
    Vicat Softening Temperature B50 Iso 306 135 °C
    Mold Shrinkage 1.0 - 1.4 %

    As an accredited Seculene PPR 1040 TV30 S0 PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Seculene PPR 1040 TV30 S0 PP Copolymer is packaged in 25 kg moisture-proof bags, preserving quality and safe handling.
    Container Loading (20′ FCL) Container Loading (20′ FCL) packs Seculene PPR 1040 TV30 S0 PP Copolymer into a standard 20-foot container for safe, efficient bulk transport.
    Shipping Seculene PPR 1040 TV30 S0 is a polypropylene copolymer resin shipped as solid pellets. Transport in dry, clean containers or bulk bags, avoiding moisture and contamination. Non-hazardous per regulations, but protect from heat and direct sunlight. Standard handling precautions apply; store in a cool, ventilated area.
    Storage Store Seculene PPR 1040 TV30 S0 PP Copolymer in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture contamination. Avoid contact with strong oxidizing agents. Maintain warehouse temperatures below 40°C. Under these conditions, the material typically retains its properties for 12 months from date of delivery.
    Shelf Life Store in original packaging in cool, dry conditions; shelf life is typically 2 years from date of manufacture.
    Application of Seculene PPR 1040 TV30 S0 PP Copolymer

    Scope note: Seculene PPR 1040 TV30 S0 is processed in the following scenarios as a talc-reinforced polypropylene random copolymer compound with a nominal filler content of 30 wt%. The suffix TV30 is interpreted as the talc loading; S0 is handled as the supplier’s natural colour code. Lot-specific melt mass-flow rate, tensile modulus, impact performance, and stabiliser package must be confirmed against the mill certificate before barrel profiles are set. Published data for this specific configuration is limited; processing windows and property ranges cited below derive from ISO 19069-2:2016 specimen preparation protocols, ISO 1873-2:2007 material designation boundaries, and production-scale records for equivalent 30 wt% talc-filled polypropylene random copolymer compounds. The scenarios exclude extrusion blow moulding, pressure plumbing, and direct food-contact packaging where migration behaviour has not been validated on the specific lot.

    Does 30 wt% Talc Loading in Polypropylene Random Copolymer Open or Constrain the Injection Window for Automotive Interior Carriers?

    Seculene PPR 1040 TV30 S0 is introduced into thin-wall automotive interior substrates where the 30 wt% talc plateau reduces linear mould shrinkage to 0.5–0.9% in the flow direction and 0.8–1.2% across flow, measured after 48 h at 23 °C and 50% RH according to ISO 294-4:2018. The formulation addition ratio for door inner carrier brackets and instrument panel lower supports is 100 parts Seculene PPR 1040 TV30 S0, 2.0–4.0 parts colour masterbatch, 0.2–0.5 parts processing stabiliser masterbatch, and 10–25 parts closed-loop regrind of the same grade; total talc content after regrind dilution is maintained at 27–31 wt%. The downstream production process is injection moulding on hydraulic or servo-electric machines with screw L/D 20:1–24:1, compression ratio 2.5:1–3.0:1, barrel temperature profile 210–245 °C, mould temperature 25–45 °C, injection velocity 60–120 mm/s, holding pressure 55–75 MPa, and back pressure 0.5–1.2 MPa. Terminal finished product types include A/B/C pillar trim covers, instrument panel lower carriers, glove box housings, door inner panels, and rear parcel shelf supports. The relevant industry compliance standards are ISO 19069-2:2016, ISO 3795:1989 or FMVSS 302 for horizontal burn rate not exceeding 100 mm/min, VDA 278:2019 for VOC/SVOC desorption, ISO 6452:2021 for fogging reflectometric index, and IATF 16949:2016 for production process control. Weld-line sections in talc-filled PP exhibit tensile strength retention of only 50–65% relative to uninterrupted flow-path specimens under ISO 527-2:2012; gate locations should therefore be positioned so that weld lines fall in low-stress apertures or stiffening rib intersections, not along snap-fit beams or occupant-contact edges.

    ParameterThin-wall section 1.2–2.0 mmThick-wall section 2.5–4.0 mmMeasurement basis
    Melt temperature230–250 °C215–240 °CNozzle thermocouple
    Mould surface temperature30–45 °C20–35 °CWater-channel contact sensor
    Injection velocity80–140 mm/s40–80 mm/sServo position transducer
    Holding pressure60–80 MPa40–60 MPaManifold pressure transducer
    Back pressure0.8–1.5 MPa0.3–0.8 MPaInjection cylinder hydraulic gauge
    Cooling time12–18 s18–30 sTimer from pack end to mould open

    Across appliance-grade washing-machine outer tub collars and dishwasher base frames, Seculene PPR 1040 TV30 S0 is dosed as the sole resin phase at 100 parts with 1.5–3.0 parts grey or white colour concentrate, 0.2–0.4 parts high-temperature processing aid, and up to 15 parts sorted in-house regrind; no amine-based antistatic additive is used because amine chemistry accelerates thermo-oxidative degradation of the PP matrix during prolonged hot-wash exposure. The typical production route is injection moulding on a machine with clamping force 800–1600 tonnes, barrel melt temperature 210–245 °C, mould surface temperature 20–40 °C, and holding pressure 50–70 MPa, producing parts with nominal wall sections of 2.0–3.5 mm. The talc-filled random copolymer reduces cycle time relative to unfilled PP because its thermal conductivity is 0.35–0.45 W/(m·K) under ISO 22007-2:2015, compared with 0.15–0.20 W/(m·K) for unfilled PP homopolymer; this allows ejection at 65–80 °C without post-mould deflection. Terminal finished product types include washing machine outer tub collars, dishwasher base frames, refrigerator toe panels, and laundry appliance structural brackets. Industry compliance standards are IEC 60335-1:2020 for household appliance safety, ISO 75-2:2013 method B for heat deflection temperature under 0.45 MPa, ISO 179-1/1eA:2020 for Charpy notched impact, and ISO 178:2019 for flexural modulus. The operating boundary is continuous hot-contact exposure above 80 °C under load: polypropylene-based compounds exhibit measurable creep above 80 °C, and sustained contact with aggressive detergent liquors above 90 °C is outside the material’s long-term property retention envelope.

    Logistics Container Wall Section Design and Low-Temperature Drop-Impact Retention

    Logistics containers moulded from Seculene PPR 1040 TV30 S0 use wall sections of 2.5–6.0 mm to meet stacking load requirements without foam core or gas-assisted filling. The formulation addition ratio is 100 parts grade compound, 1.5–3.0 parts UV masterbatch when outdoor storage is specified, 5–10 parts impact modifier masterbatch for containers exposed to -20 °C, and 10–20 parts same-grade regrind; total UV stabiliser addition should not exceed 3.0 wt% because excessive low-molecular-weight carrier resin alters mould shrinkage in the hinge area. The downstream production process is injection moulding on large-platen machines with accumulator-assisted injection units, melt temperature 220–250 °C, mould temperature 15–35 °C, injection pressure 80–110 MPa, holding pressure profile 60–75 MPa for 8–15 s, and cooling time 20–45 s depending on wall thickness. Hinge sections in foldable crates are moulded at the upper melt temperature limit of 245–250 °C to reduce orientation and prevent hinge whitening; the talc filler increases stiffness but also reduces elongation at break to 5–15% under ISO 527-2:2012, so hinge thickness must be 0.6–1.2 mm to maintain flexural endurance. Terminal finished product types include foldable vegetable crates, industrial pallet boxes, racking totes, and automotive parts distribution trays. Industry compliance standards are ISO 8611-1:2021 for flat pallet load ratings, ASTM D5276-19 for free-fall drop test, EC 10/2011 and FDA 21 CFR 177.1520 for food-contact logistics packaging when migration testing is completed, and ISO 2818:2018 for sample preparation from large mouldings.

    For injection-moulded electrical enclosures assigned to ordinary non-flame service, Seculene PPR 1040 TV30 S0 is introduced at 100 parts with 1.0–2.5 parts black colour masterbatch and 0.2–0.5 parts processing stabiliser masterbatch; the formulation does not contain halogenated flame retardants, and no conversion to UL 94 V-2 or V-0 classification is claimed unless a separate flame-retardant masterbatch is validated on the specific moulding because talc and conventional brominated packages can interact at melt temperatures above 240 °C. The production process is injection moulding with vertical or horizontal clamping units of 150–600 tonnes, melt temperature 220–245 °C, mould temperature 30–55 °C, and wall thickness 1.5–3.0 mm; screw geometry is a low-shear barrier screw with L/D 20:1 and compression ratio 2.2:1–2.8:1 to limit filler attrition. Terminal finished product types include surface-mount junction box bases, low-voltage distribution housings, terminal block shrouds, and cable duct fittings. The relevant compliance standards are IEC 60670-1:2015 for enclosure mechanical integrity, IEC 60112:2020 for proof tracking index, IEC 60695-2-11:2021 glow-wire flammability testing, RoHS 2011/65/EU Annex II for restricted substances, and REACH EC 1907/2006 Article 33 communication duties. The operational boundary is maximum continuous service temperature 65 °C for parts under electrical terminal contact pressure because creep modulus of PP/talc compounds declines markedly above 60–70 °C under sustained stress.

    RequirementStandard/test method
    Glow-wire flammabilityIEC 60695-2-11:2021
    Comparative tracking indexIEC 60112:2020
    Enclosure impact and thermal stressIEC 60670-1:2015
    Restricted substancesRoHS 2011/65/EU Annex II
    SVHC communication dutiesREACH EC 1907/2006 Article 33

    Sanitaryware and Public-Area Seat Mouldings Rely on the Same Talc Plateau but Not on Impact-Modified Grades

    Sanitaryware and public-area seat mouldings expose the compound to short-term water contact, chemical cleaning agents, and repetitive seated loads without sustained internal pressure. In this sector Seculene PPR 1040 TV30 S0 is formulated at 100 parts with 2.0–4.0 parts colour masterbatch, 0.2–0.4 parts antioxidant masterbatch, and 0–5 parts impact modifier masterbatch depending on whether the moulded part is a fixed interior seat base or an outdoor stadium seat shell; interior applications avoid impact modifier because the resulting drop in flexural modulus below 2.0 GPa makes the seat base too flexible under 100 kg static loading. The production route is injection moulding with melt temperature 220–250 °C, mould temperature 20–40 °C, injection speed 50–100 mm/s, holding pressure 45–65 MPa, and total cycle time 45–70 s for 3.0–5.0 mm wall stock. Terminal finished product types include toilet seat hinges and bases, bathroom shelving brackets, stadium seating shells, cinema seat backs, and public-area bench slats. Industry compliance standards are EN 12727:2000 for seating strength and fatigue where referenced by procurement specifications, ISO 306:2022 Vicat softening temperature method A50, ISO 179-1/1eA:2020 Charpy impact, and ISO 4892-2:2023 accelerated weathering for outdoor colours. The operational boundary is chemical contact with oxygenated solvents: ketones and aromatic hydrocarbons cause stress crazing in PP/talc compounds, and repeated exposure to undiluted isopropanol in disinfectant wipe tests can produce visible surface microcracking in highly oriented sections.

    When Non-Pressure Drainage Fittings Demand Higher Ring Stiffness Without Pressure-Rating Compromise

    Non-pressure drainage fittings in building discharge systems represent a narrow application for this compound where dimensional stability and moulded thread crispness outweigh pressure-pipe hydrostatic requirements. The formulation addition ratio is 100 parts Seculene PPR 1040 TV30 S0, 1.0–2.0 parts black or terracotta colour masterbatch, 0.1–0.3 parts calcium stearate-based acid scavenger, and 5–15 parts clean same-grade regrind; the regrind fraction is limited to 15 wt% because higher recycled content increases variability in fitting socket dimensions and can reduce notched Charpy impact strength below 3.0 kJ/m² under ISO 179-1/1eA:2020. Production is performed on injection moulding machines with rotating-core tooling for threaded traps and bends, melt temperature 215–240 °C, mould temperature 15–35 °C, injection pressure 70–100 MPa, holding pressure 50–65 MPa, and cooling time 15–25 s for 1.5–3.0 mm wall thickness. Terminal finished product types include bottle traps, socket plugs, wall brackets, access covers, and non-pressure inspection chamber fittings. The relevant industry compliance standards are EN 1451-1:2017 for PP discharge pipes and fittings within building drainage, ISO 3127:2019 for resistance to external blows at 0 °C in pipe systems, ISO 75-2:2013 method B for heat deflection, and EN 681-1:1996 for elastomeric seal compatibility where push-fit sockets are used. Published data for this specific configuration is limited; hydrostatic pressure rating is not claimed, and the material is excluded from pressurised water distribution systems under ISO 15874-2:2013 because the talc filler alters ductile burst behaviour.

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    Certification & Compliance
    More Introduction

    Seculene PPR 1040 TV30 S0 PP Copolymer is a polypropylene random copolymer whose main chain contains a controlled ethylene distribution. The grade segment 1040 functions as a melt-flow and stiffness descriptor within the producer’s nomenclature, while the suffix TV30 is read in several polypropylene compounding systems as a nominal 30% by weight talc reinforcement. The suffix S0 commonly indicates a natural or non-pigmented stabilisation package, although exact designation keys vary by manufacturer. Published data for this specific configuration is limited; the ranges in this description are therefore class-typical values for the corresponding unfilled PP-R pipe extrusion family and talc-modified PP-R structural family, and must be confirmed against the certificate of analysis for the production lot being qualified.

    Where the product is used as an unfilled PP-R random copolymer, its principal application is in pressure piping for potable water and heating systems. Under sustained internal pressure at 70°C, this polymer class derives long-term strength from creep rupture testing evaluated according to ISO 9080. Standard PP-R pipe materials commonly carry a design stress of 3.20 MPa for 50-year service at 70°C, corresponding to S5/SDR11 wall thickness under EN ISO 15874-2. Where the TV30 suffix denotes talc modification, the application profile shifts toward dimensionally stable structural components, enclosures, housings and interior trim, because the mineral phase reduces linear thermal expansion, increases flexural modulus, and suppresses post-moulding shrinkage, but simultaneously reduces long-term hydrostatic pressure retention and socket-fusion weld toughness.

    Property Profile and Processing Window for Seculene PPR 1040 TV30 S0

    Melt-mass flow behaviour is determined at 230°C under a 2.16 kg piston load according to ISO 1133-1:2022. Unfilled PP-R pipe extrusion grades typically fall between 0.20 g/10 min and 0.50 g/10 min; a mid-range value near 0.30 g/10 min is common because it balances melt strength for large-diameter pipe sag resistance against shear heating in single-screw extruders. Talc-filled variants can exhibit higher melt-mass flow rates depending on the intended forming process, with injection-grade PP-R compounds frequently above 5 g/10 min. Density for unfilled PP-R random copolymer is normally 0.895–0.910 g/cm³ under ISO 1183-1:2019, while a nominal 30% talc-filled version typically increases into the 1.10–1.15 g/cm³ range because of the reinforcing mineral phase.

    Property Unfilled PP-R class representative range 30% talc-modified PP-R class representative range Test method
    Tensile yield stress 2427 MPa 2833 MPa ISO 527-2:2012
    Flexural modulus 9001,200 MPa 2,9003,800 MPa ISO 178:2019
    Notched Charpy impact at 23°C 2060 kJ/m² 26 kJ/m² ISO 179-1/1eA
    Heat deflection temperature at 0.45 MPa 7085°C 120140°C ISO 75-2:2013
    Melt flow rate at 230°C/2.16 kg 0.200.50 g/10 min 515 g/10 min for structural moulding grades ISO 1133-1:2022

    Processing behaviour is strongly governed by the filler level. For unfilled PP-R pipe extrusion, single-screw extruders with 30:1 to 36:1 L/D and grooved feed sections typically run a barrel profile from 180°C at the feed throat to 230°C in the metering zone. Melt temperature at the die entrance is maintained at 220–240°C, and head pressure under stable output usually falls between 18 MPa and 28 MPa depending on die resistance and calibration tooling. Below 200°C melt temperature, incomplete plastication and elevated head pressure can produce unmolten particle defects in pipe walls. Above 260°C, thermo-oxidative degradation increases gel formation, melt fracture risk, surface roughness, and odour development in downstream water-contact applications.

    For a 30% talc-filled PP-R compound, the processing window is narrower with respect to moisture and shear history. Talc platelets release surface-bound water above 130°C, and dispersion requires high-shear mixing elements rather than simple conveying screws. Twin-screw compounding or high-shear single-screw configurations with extended mixing zones are preferred because agglomerates create surface pits and local stress concentrations. Melt temperatures for talc-filled structural PP-R are generally held between 200°C and 230°C. Residence time should be minimised because prolonged exposure to shear at the higher filler loading can reduce the effective stabiliser package and shift colour toward yellow in natural grades.

    Under sustained hoop stress at 70°C, unfilled PP-R copolymers are preferred over talc-filled systems because the filler particles act as internal stress concentrators that can shorten the ductile-to-brittle transition in pressure pipes. Socket fusion welding of unfilled PP-R pipe requires a heating plate temperature of 250–270°C, with heating time determined by wall thickness and pipe diameter. Fusion joints must be held without movement during the cooling phase. Any moisture, talc-rich surface layer, or oxide skin at the weld interface is a known cause of brittle joint failure. Filled variants are not generally socket-fused in pressure service unless the supplier has qualified the specific formulation under ISO 9080 hydrostatic testing.

    What Distinguishes a PP-R Copolymer Grade from PPH, PP-B and Filled Compounds?

    The principal difference between PP-R random copolymer and propylene homopolymer is the distribution of ethylene segments along the polymer chain. This reduces crystallinity, lowers stiffness, increases impact resistance, and improves long-term hydrostatic pressure resistance at elevated temperature. Polypropylene homopolymer, or PPH, exhibits higher flexural modulus and heat deflection temperature, but its notched impact strength is lower and its long-term pressure retention at 70°C is less suited to hot-water piping. Polypropylene block copolymer, or PP-B, is a heterophasic system with rubber-like domains that provide excellent low-temperature impact resistance. However, PP-B grades generally show lower pressure-pipe design stress and higher creep at hot-water temperatures, so they are not interchangeable with PP-R in pressure plumbing systems.

    Material family Characteristic profile Typical application boundary Main limitation for pressure or structural service
    PP-H homopolymer Higher stiffness, higher heat resistance, lower impact Non-pressurised drainage, industrial profiles, laboratory fittings Reduced low-temperature ductility and lower hot-water pressure retention
    PP-B block copolymer High impact at −20°C, moderate stiffness Automotive battery cases, caps, cold-water fittings Lower creep resistance and hydrostatic design stress at elevated temperature
    PP-R random copolymer Balanced impact, weldability, long-term hot-water strength Plumbing and district heating pipe networks Lower modulus than PPH and mineral-filled grades
    PP-R with 30% talc High stiffness, lower shrinkage, lower CLTE, lower impact Structural panels, brackets, housings, interior automotive parts Reduced pressure-pipe durability and poor socket-fusion toughness unless specifically validated

    If regrind fractions above 20 wt% are introduced without adjusting the stabiliser package, long-term hydrostatic strength can decrease and surface quality may become inconsistent. Pre-drying is recommended at 80°C for 2–4 h for unfilled PP-R when moisture content exceeds 0.05 wt%, and at 90–100°C for 3–4 h for talc-modified grades because talc absorbs atmospheric moisture. Ultraviolet exposure without carbon black or hindered amine light stabiliser can cause surface embrittlement within 12–18 months in outdoor service. The formulation should not be combined with amine-based additives, residual halogenated flame retardants, or copper-ion catalyst systems unless the supplier has supplied documented compatibility data, because antagonistic interactions can consume the base stabilisation package and reduce thermal-oxidative stability.

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