| HS Code | 255723 |
| Density G Cm³ | 1.25 |
| Melt Flow Rate 230 C 2 16 Kg G 10 Min | 12.5 |
| Tensile Strength At Yield Mpa | 28 |
| Elongation At Break | 15 |
| Flexural Modulus Mpa | 2200 |
| Charpy Impact Strength Notched Kj M² | 5 |
| Izod Impact Strength Notched Kj M² | 4 |
| Heat Deflection Temperature At 0 46 Mpa C | 110 |
| Vicat Softening Temperature A50 C | 155 |
| Melting Temperature C | 150 |
| Rockwell Hardness R Scale | 90 |
| Water Absorption 24h | 0.05 |
As an accredited Seculene PPR 1250 TV40 S0 PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Seculene PPR 1250 TV40 S0 PP Copolymer: 25 kg polyethylene-lined bags, sealed for moisture protection and safe handling. |
| Container Loading (20′ FCL) | Seculene PPR 1250 TV40 S0 PP Copolymer packed in 20′ FCL, securely stowed, protected from moisture and heat, per handling regulations. |
| Shipping | Seculene PPR 1250 TV40 S0 is a polypropylene random copolymer supplied as free-flowing pellets. Ship in sealed, moisture-resistant bags or bulk containers to prevent contamination and moisture uptake. Store dry, away from heat sources. Standard freight with proper labeling is suitable; no hazardous transport restrictions apply. |
| Storage | Store Seculene PPR 1250 TV40 S0 PP Copolymer in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and ignition sources. Keep containers tightly sealed to prevent moisture contamination and physical damage. Avoid contact with strong oxidizers. Maintain stable temperatures; do not store outdoors. Proper storage preserves material properties and ensures safe handling. |
| Shelf Life | Store in a cool, dry place away from direct sunlight; shelf life is typically 12 months from manufacture if unopened. |
At melt temperatures of 230–250 °C and tool surface temperatures of 40–60 °C, the 40 wt% talc-filled polypropylene copolymer Seculene PPR 1250 TV40 S0 is injection moulded into automotive dashboard carrier substrates, HVAC distribution housings, demister nozzles and footwell duct connectors. In these components, the talc platelet network reduces the flow-direction coefficient of linear thermal expansion to 45–60 µm/m·K and transverse expansion to 70–90 µm/m·K when measured according to ISO 11359-2:2021; this contraction differential remains lower than that of neat polypropylene and reduces squeak-and-rattle failures between adjacent duct parts during thermal cycles from −30 °C to 100 °C. The compound is processed on reciprocating screw injection units with an L/D ratio of 20:1 to 25:1 and a compression ratio of 2.0:1 to 2.5:1; because the talc filler is abrasive, the screw and barrel are specified with bimetallic hardening and the non-return ring is specified with a wear-resistant coating to maintain a melt cushion of 3–6 mm across production runs exceeding 50,000 cycles. Holding pressure is set at 60–80% of peak injection pressure, screw back pressure is maintained at 5–15 bar, and gate freeze time for a nominal 3.0 mm wall is typically 8–12 s. Because weld lines in talc-filled polypropylene can reduce notched Charpy impact strength by 30–40% relative to unfilled material, sequential valve-gate control is used to displace the weld line into low-stress regions rather than across snap-fit bosses or screw bosses. Tooling allowances follow ISO 294-4:2018 using mould shrinkage values of 0.8–1.0% in the flow direction and 1.0–1.3% transverse; the combined effect of talc orientation and differential shrinkage is compensated in tooling by increasing draft angles to 1–2° and controlling nominal wall thickness to 2.5–3.5 mm with rib-to-wall ratios no greater than 0.5–0.6. Emissions compliance for interior applications is verified by VDA 278:2011 thermal desorption analysis, VDA 270:2018 odour testing and DIN 75201:2011 fogging; the grade requires a low-volatility stabilizer package consisting of 0.3–0.5 wt% hindered amine light stabilizer, 0.1–0.2 wt% phenolic antioxidant and 0.05–0.1 wt% calcium stearate acid scavenger to meet the typical cabin-air quality limit of less than 1 mg fogging condensate. The operational boundary is a continuous air-side operating temperature of 105 °C; above this sustained temperature, creep modulus decays sufficiently that load-bearing bosses lose clamp load, and the material should be replaced by a heat-stabilised glass-reinforced polypropylene or polyamide grade.
The class-typical control window for 40 wt% talc-filled polypropylene copolymer is shown below; production-lot certificate values should be used for tooling calculations.
| Property | Test method | Class-typical control window |
|---|---|---|
| Density | ISO 1183-1:2019 | 1.22–1.24 g/cm³ |
| Melt flow rate at 230 °C, 2.16 kg | ISO 1133-1:2022 | 11–14 g/10 min |
| Tensile stress at yield | ISO 527-2:2012 | 24–28 MPa |
| Tensile elongation at yield | ISO 527-2:2012 | 3–5% |
| Flexural modulus | ISO 178:2019 | 3,200–3,800 MPa |
| Charpy notched impact at 23 °C | ISO 179-1/1eA:2010 | 3.0–5.0 kJ/m² |
| Charpy notched impact at −20 °C | ISO 179-1/1eA:2010 | 1.5–2.5 kJ/m² |
| Heat deflection temperature B at 0.45 MPa | ISO 75-2:2013 | 120–130 °C |
| Vicat softening temperature A50 | ISO 306:2022 | 150–158 °C |
| CLTE flow / transverse | ISO 11359-2:2021 | 45–60 / 70–90 µm/m·K |
| Mould shrinkage flow / transverse | ISO 294-4:2018 | 0.8–1.0 / 1.0–1.3% |
| Filler content | ISO 3451-1:2019 | 38–42 wt% |
Outer tub mouldings made from Seculene PPR 1250 TV40 S0 are evaluated against detergent exposure at pH 9–11, water temperatures up to 95 °C, and spin-induced unbalanced loads. The polymer matrix has hydrolytic stability in hot water, but the talc filler raises the modulus to 3,200–3,800 MPa according to ISO 178:2019, which reduces creep deformation under the bearing insert when a 25 kg dry load is rotated at 1200 rpm. Tooling for outer tubs is typically run on hydraulic clamp units of 1800–2500 t, with sequential valve-gated hot runners and mould temperatures of 50–70 °C; the higher mould temperature is required to reduce frozen-in orientation at the tub rim, where radial weld lines can otherwise reduce Charpy notched impact strength at 23 °C from 3.0–5.0 kJ/m² to below 2.0 kJ/m². Formulation adjustment for subzero door-impact requirements often includes 3–5 wt% ethylene-octene copolymer; this addition raises the notched Charpy impact strength at −20 °C to approximately 2.5–3.5 kJ/m² but reduces flexural modulus by 15–20%, so the trade-off must be verified against the bearing boss deflection limit. Long-term fatigue performance is assessed by creep rupture testing at 60 °C under 10 MPa tensile load using ISO 899-2:2020; the talc-filled copolymer shows a logarithmic creep strain increase, and guard-bolted joints should be designed to a maximum strain of 0.8% after 1000 h to avoid loss of preload. Compliance with household appliance electrical safety is anchored to IEC 60335-1:2020 and IEC 60335-2-7:2019; flammability testing is conducted under UL 94 at 3.0 mm thickness, where the unmodified grade is classified HB. An operational incompatibility exists with continuous immersion in strong oxidising bleach solutions above 200 ppm available chlorine at 95 °C; under these conditions, surface microcracking can initiate at weld lines before the mechanical endpoint. The use of weld-line-free gate placement and generous corner radii above 1.0 mm is therefore mandatory for tub assemblies subjected to more than 2,000 spin cycles.
The unmodified 40 wt% talc-filled copolymer is classified HB at 3.0 mm thickness under UL 94, which restricts its use to low-voltage enclosures where glow-wire ignition is not a specified safety requirement. For junction boxes, meter surrounds and distribution-box covers, the compound is injection moulded with a wall thickness of 2.0–3.0 mm at melt temperatures of 230–250 °C and mould temperatures of 40–60 °C. The electrical performance is characterised by a comparative tracking index that is typically above 600 V when tested per IEC 60112:2020 on solution A, but lot-to-lot mineral purity can shift this value; a production-lot acceptance criterion of CTI above 600 V is therefore used for insulating distances up to 400 V phase-to-phase in pollution degree 2 environments. Dielectric strength is measured at 25–30 kV/mm across 3.0 mm specimens per IEC 60243-1:2013; the enclosure design must still maintain creepage distances according to IEC 60664-1:2020. Where glow-wire resistance at 650 °C or 750 °C is required by IEC 60695-2-11:2021, the unmodified grade does not pass; a halogen-free intumescent or brominated flame-retardant package must be compounded at 2–5 wt% with antimony trioxide synergist, which typically raises density to 1.30–1.35 g/cm³ and reduces flexural modulus by 10–15%. Outdoor enclosures require 2.0–2.5 wt% carbon black masterbatch and 0.3–0.5 wt% UV stabiliser to meet ISO 4892-2:2021 weathering for 1,000 h with colour change below ΔE 5; without this additive, surface chalking and PP chain scission occur before 500 h. Moulding tolerance is governed by ISO 294-4:2018, with typical mould shrinkage of 0.8–1.0% in flow and 1.0–1.3% transverse, which is critical for maintaining the flatness of gasket sealing faces on IP54-rated enclosures tested per IEC 60529:2013. The compound must not be used for uninsulated busbar supports unless the specific lot is verified for CTI above 600 V and for hot-wire ignition per IEC 60695-2-10:2021; published data for this specific grade in high-current switchgear applications is limited.
| Requirement | Standard | Test condition / limit | Unmodified 40 wt% talc-filled PP result |
|---|---|---|---|
| Flammability class at 3.0 mm | UL 94 | Vertical burn | HB |
| Glow-wire flammability at 650 °C | IEC 60695-2-11:2021 | Contact 30 s | Not achieved without FR package |
| Comparative tracking index | IEC 60112:2020 | Solution A | Typically above 600 V; lot verification required |
| Dielectric strength | IEC 60243-1:2013 | 3.0 mm thickness | 25–30 kV/mm |
| Weathering | ISO 4892-2:2021 | 1,000 h, ΔE < 5 | Passes with carbon black and UV stabiliser |
| Ingress protection flatness | IEC 60529:2013 | IP54 gasket seal face | Requires 0.8–1.0% flow / 1.0–1.3% transverse shrinkage compensation |
Furniture structural mouldings produced from Seculene PPR 1250 TV40 S0 include chair base frames, armrest structural brackets, lumbar support shells and mechanism covers. The compound is processed with melt temperatures of 230–250 °C and mould temperatures of 30–50 °C; gas counter-pressure or chemical foaming with 0.5–1.0 wt% endothermic blowing agent reduces sink marks over rib intersections and cuts part mass by 8–12%. The talc filler provides a low-gloss, scratch-resistant surface without secondary coating, although dark colours require 1–2 wt% pigment masterbatch and 0.2–0.3 wt% processing lubricant to eliminate weld-line streaking. Structural validation is performed according to BIFMA X5.1-2017 for office chairs and EN 1335-1:2020 in the European market; armrest vertical load testing at 900 N requires corner radii above 1.0 mm and stiffening ribs with a height-to-thickness ratio below 5:1 to avoid stress whitening. Snap-fit assembly features must be designed with a maximum outer-fibre strain below 1.5% because repeated insertion at room temperature above 20 cycles can initiate crazing in talc-filled PP if the snap beam is over-constrained. The operational boundary is the use of aggressive ethanol-based cleaning agents: concentrations above 50 vol% ethanol can plasticise the amorphous PP interphase and reduce weld line strength by up to 25% after 24 h immersion, so furniture surfaces must be tested according to ISO 175:2010 if healthcare-grade disinfection is specified.
The substitution calculation is not straightforward because a 40 wt% talc-filled PP copolymer provides a flexural modulus of 3,200–3,800 MPa according to ISO 178:2019, whereas a typical 30% glass-fibre-reinforced PA6 delivers 8,000–9,500 MPa; rib height and wall thickness must therefore be increased by 30–50% to recover equivalent bending stiffness. In under-bonnet beauty covers, the lower density of 1.22–1.24 g/cm³ versus 1.34–1.38 g/cm³ for PA6-GF30 reduces part mass by approximately 9%, but the continuous-use temperature limit falls from approximately 180 °C to 110–120 °C because oxidative chain scission accelerates above 130 °C. The compound is injection moulded with melt temperatures of 240–250 °C and mould temperatures of 60–80 °C; a heat-stabilizer package containing 0.4–0.6 wt% hindered phenol, 0.2–0.3 wt% phosphite and 0.1–0.2 wt% thioester is used so that tensile bars heat-aged at 130 °C for 1,000 h retain at least 50% of original elongation when tested per ISO 527-2:2012. Torque retention on moulded bosses is evaluated by inserting threaded metal bushings after ultrasonic insertion; at 120 °C, the compressive creep modulus of talc-filled PP declines and clamp load loss of 25–35% can occur after 100 h, which requires either reduced bolt torque or metallic insert reinforcement if the joint load exceeds 500 N. Resistance to engine oil at 100 °C is acceptable for splash exposure, but continuous contact with hot ethylene glycol coolant at 105 °C or above is an incompatibility because glycol diffuses into the talc-matrix interphase and reduces Charpy notched impact strength by 30% after 500 h. Under-bonnet thermal cycling is validated per ISO 16750-4:2010 across −40 °C to 120 °C; the cover must be designed with grommet retention features that tolerate the higher CLTE of 45–60 µm/m·K in flow and 70–90 µm/m·K transverse. The material is not suitable for direct mounting within 150 mm of an exhaust manifold or turbocharger heat shield unless surface temperatures are verified below 110 °C. Published data for this specific grade in engine beauty cover applications is limited; validation should be conducted on production tooling with reverse-pin screws of L/D 22:1 because talc orientation and weld-line placement dominate long-term acoustic and fatigue performance.
Because the 40 wt% talc platelets reduce post-mould shrinkage anisotropy, Seculene PPR 1250 TV40 S0 is used in dishwasher door inner frames, base rails, salt reservoir brackets and detergent dispenser housings. These components are injection moulded with wall thicknesses of 2.5–3.0 mm at melt temperatures of 230–250 °C and mould temperatures of 50–60 °C; pre-drying is not required if the material has been stored in sealed bags below 60% relative humidity, but storage above 60% RH for more than 48 h requires a desiccant dryer at 80 °C for 2 h to prevent surface splay caused by moisture adsorbed on the talc filler. The compound withstands detergent and rinse-aid solutions at pH 3–10 and temperatures up to 70 °C in the base frame, but the dispenser housing must be checked against concentrated rinse aid at 50 °C using ISO 175:2010; citric acid-based detergents at 5 wt% concentration do not significantly reduce tensile yield stress, which remains at 24–28 MPa per ISO 527-2:2012. Creep modulus under 70 °C and 10 MPa flexural load is used to validate base frame flatness after 1000 h; the talc-filled copolymer shows less than 0.5% creep strain under these conditions, which preserves the door seal gap. Ultrasonic welding of the salt reservoir bracket to the door panel requires a joint design with an energy director height of 0.4–0.6 mm and amplitude of 30–40 µm because the talc filler attenuates ultrasonic energy. The material must not be used for steam sterilizer components with continuous exposure above 120 °C, and repeated exposure to sodium hypochlorite solution above 2 wt% at 60 °C causes surface oxidation and gloss loss before 500 h.
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In the absence of a lot-specific certificate of analysis, the designation Seculene PPR 1250 TV40 S0 PP copolymer identifies a polypropylene random copolymer grade whose processing boundary cannot be fixed solely from nomenclature. The suffix TV40 and S0 are not defined by a referenced public standard; if TV40 denotes a 40 % talc modification, the mechanical and rheological profile would differ substantially from an unfilled PP-R pipe resin. Published data for this specific configuration is limited, and class-level PP-R data should not be substituted for supplier-validated values. Melt mass-flow rate under ISO 1133-1:2022, tensile properties under ISO 527-2, and notched impact strength under ISO 179-1/1eA require product-specific test reports before die design, screw selection, or hydraulic design proceeds.
For polypropylene random copolymers intended for ISO 15874 piping systems, preliminary handling boundaries include pre-drying at 80 °C for 2 h to 4 h when storage relative humidity exceeds 60 %, melt temperatures maintained below 260 °C, and screw designs with low compression ratios suitable for random copolymer melts. These are class-level controls. The grade identifier 1250 should not be interpreted as a melt flow rate of 0.1250 g/10 min or 12.50 g/10 min; neither reading can be assumed for this product.
Because the TV40 and S0 suffixes are not defined by a public standard, the processing window must be established on a pilot line before production-scale start-up. Polypropylene random copolymers used in ISO 15874 piping systems are normally extruded on single-screw machines with grooved intake zones and L/D ratios from 30:1 to 40:1. Barrel settings for unfilled PP-R typically range from 180 °C in the feed zone to 230 °C at the die, but mineral-filler modification, if encoded by TV40, reduces melt elasticity and shifts pressure consumption. When talc loading approaches 40 %, melt viscosity increases and extrusion head pressure per unit output typically rises; the exact shift for this grade is not publicly available. Start-up should therefore begin at the lower melt-temperature boundary and increment only after pressure stability, melt-fracture observation, and wall-thickness variation are recorded.
At 230 °C and 2.16 kg, random copolymer melt mass-flow rates for pipe extrusion commonly fall between 0.20 g/10 min and 0.50 g/10 min. A single low-shear MFR point does not govern extrusion head pressure or wall-thickness control. Capillary rheometry under ISO 11443 at 190 °C to 230 °C is recommended to establish the power-law index and temperature sensitivity, particularly if S0 indicates a controlled-rheology additive that narrows molecular-weight distribution. In pipe diameters above 110 mm, insufficient melt strength produces sag; excessive melt strength raises die swell and complicates vacuum calibration. The grade’s behaviour in this regard cannot be confirmed from designation alone, and trial evaluations should include sag ratio and die-swell coefficient measurement under controlled melt-pressure conditions.
When the grade is compared against homopolymer and block copolymer feedstocks, crystallinity, impact resistance, and long-term creep behaviour differ systematically. The random copolymer class is specified for hot-water pressure piping because ethylene comonomer interrupts isotactic sequences, lowering crystallinity and improving slow crack growth resistance while reducing stiffness. A product such as Seculene PPR 1250 TV40 S0 would be expected to fall within the random copolymer family only if the grade suffix does not include an incompatible filler system. The comparison in Table 1 uses class-level unfilled data obtained from ISO 527-2, ISO 179-1/1eA, ISO 306, and ISO 75-2; product-specific values require a supplier certificate.
| Property | Test method | PP-R random copolymer | PP-H homopolymer | PP-B impact/block copolymer |
|---|---|---|---|---|
| Tensile modulus | ISO 527-2 | 900–1200 MPa | 1300–1800 MPa | 800–1100 MPa |
| Tensile yield stress | ISO 527-2 | 22–27 MPa | 32–38 MPa | 18–24 MPa |
| Notched Charpy impact at 23 °C | ISO 179-1/1eA | 20–35 kJ/m² | 3–5 kJ/m² | 15–25 kJ/m² |
| Vicat softening temperature A50 | ISO 306 | 120–130 °C | 150–155 °C | 120–130 °C |
| Heat deflection temperature B at 0.45 MPa | ISO 75-2 | 70–85 °C | 95–110 °C | 65–80 °C |
The values above are representative for unfilled injection-moulded specimens. They do not constitute a datasheet for Seculene PPR 1250 TV40 S0, and direct substitution of these ranges into pipe design or mould-filling simulation is not permitted without lot-specific confirmation.
For PP-R piping, long-term hydrostatic strength is the controlling parameter. ISO 9080 extrapolation from multi-temperature rupture data supplies the reference curves from which design stress values are derived. Grade validation for 50-year service at 70 °C normally requires hydrostatic testing at 20 °C, 60 °C, 80 °C, and 95 °C, with failure populations analysed according to ISO 9080 statistical procedures. A PP-R resin with insufficient comonomer distribution or excessive filler can exhibit a knee in the creep-rupture curve that moves the ductile-to-brittle transition into the design window. This is one reason talc-filled grades are not automatically interchangeable with unfilled PP-R in pressure piping. Published data for this specific configuration is limited, so any hydraulic design based on Seculene PPR 1250 TV40 S0 must use supplier-validated ISO 9080 regression coefficients rather than class-level PP-R curves. The S0 suffix may refer to a stabiliser package; if it denotes a non-food-contact additive system, compliance with FDA 21 CFR 177.1520 and EU 10/2011 cannot be assumed.
Before regulatory compliance is accepted, the supplier documentation must be cross-checked against the methods and declarations in Table 2. The matrix covers the standards most relevant to PP-R piping and general olefin polymer regulation. Absence of any listed certificate should be treated as a data gap rather than a technical failure, because compliance is supply-chain specific.
| Requirement | Standard or regulation | Typical parameter | Product-specific evidence required |
|---|---|---|---|
| PP-R piping system | ISO 15874-2 | Hydrostatic design stress at 70 °C | Supplier declaration |
| Long-term hydrostatic strength | ISO 9080 | Creep rupture from 20 °C to 95 °C | Regression data |
| Melt mass-flow rate | ISO 1133-1:2022 | 230 °C, 2.16 kg | Lot certificate |
| Tensile properties | ISO 527-2 | Yield stress, tensile modulus | Test report |
| Notched impact strength | ISO 179-1/1eA | 23 °C and 0 °C | Test report |
| Food contact | FDA 21 CFR 177.1520, EU 10/2011 | Migration limits | Compliance declaration |
| RoHS | 2011/65/EU | Lead, mercury, cadmium, chromium VI, PBBs, PBDEs | Supplier certificate |
| REACH | 1907/2006/EC | SVHC candidate list | Material declaration |
During injection moulding of PP-R fittings and manifolds, melt temperatures from 220 °C to 250 °C and mould temperatures from 20 °C to 60 °C are common class-level settings. Holding pressure must compensate for the high volumetric shrinkage of polypropylene, and gate freeze time should be determined from ISO 294-1 specimen plaques under identical thermal conditions. Weld lines in multi-gated fitting tools represent the critical mechanical boundary for random copolymers; when filler is present, weld-line strength retention falls more sharply than in unfilled PP-R. Mould-filling analysis should therefore use pressure-dependent melt viscosity data rather than a single MFR value. If TV40 indicates a 40 % talc-filled variant, injection pressure and clamp force requirements are typically higher than for an unfilled grade of equivalent flow length because the filler increases melt viscosity. Hot-runner systems require balanced thermal profiles to avoid dead spots where residence time exceeds 5 min at 240 °C; thermo-oxidative decomposition under such conditions can generate carbonyl species and shift the odour and colour profile.
Under humid storage above 60 % relative humidity, surface moisture can condense on cold pellets entering the extruder feed throat and produce surface defects in extruded pipe. Pre-drying at 80 °C for 2 h to 4 h is a practical control. The grade should not be blended with copper-based heat stabilisers without supplier confirmation, because interactions between hindered phenolic antioxidant packages and metal deactivators can alter long-term thermal oxidative stability. Acid-scavenging stabilisers used in some filled PP compounds may shift melt pH and colour. Extrusion purging should avoid uncontrolled residence above 260 °C, and shutdown procedures should include a viscosity-stable purge material to displace the grade from the die gap and screen pack. Lot-to-lot variation in comonomer content and filler dispersion, if present, should be monitored by melt mass-flow rate after conditioning at 23 °C and 50 % relative humidity for 88 h according to ISO 291.