| HS Code | 486627 |
| Polymer Type | Polypropylene (PP) Copolymer |
| Filler Content | 25% Talc |
| Uv Stabilization | Yes |
| Density | 1.05 g/cm³ |
| Melt Flow Rate | 20 g/10 min (230°C / 2.16 kg) |
| Tensile Strength At Yield | 27 MPa |
| Elongation At Break | 15% |
| Flexural Modulus | 2300 MPa |
| Izod Impact Strength Notched 23 C | 4 kJ/m² |
| Heat Deflection Temperature 0 45 Mpa | 125°C |
| Vicat Softening Temperature | 145°C |
| Rockwell Hardness | 95 R-scale |
As an accredited POLYfill PPC T25020 UV PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | POLYfill PPC T25020 UV PP Copolymer is packaged in 25 kg bags, ensuring safe handling and contamination-free delivery. |
| Container Loading (20′ FCL) | 20′ FCL: PP copolymer pellets packed in 25 kg bags, palletized and secured, maximizing space for safe transport. |
| Shipping | POLYfill PPC T25020 UV PP Copolymer ships as non-hazardous resin pellets in 25 kg moisture-resistant bags or bulk rail/truck. Keep away from sources of ignition and excessive heat. Store in a dry, covered area to prevent moisture contamination and maintain product quality. Handle with standard material-handling equipment. |
| Storage | Store POLYfill PPC T25020 UV PP Copolymer in a cool, dry, well-ventilated area, away from direct sunlight, UV radiation, heat sources, and open flames. Keep containers tightly sealed to prevent moisture contamination and product degradation. Avoid exposure to extreme temperatures. Use within recommended shelf life, handling with appropriate personal protective equipment to minimize dust generation. |
| Shelf Life | Shelf life approximately 2 years when stored in original, sealed packaging under dry, cool conditions away from direct sunlight. |
Seat back panels, lower B-pillar covers, and interior scuff plates are injection-molded with POLYfill PPC T25020 UV PP Copolymer when the part design requires reduced warpage after demoulding. The talc platelets act as heterogeneous nucleation sites, raising the crystallization onset temperature and reducing post-mould shrinkage anisotropy. For a nominal 2.5 mm wall thickness, linear mould shrinkage tested according to ISO 294-4 typically falls between 0.8% and 1.1% in the flow direction and between 1.0% and 1.3% transverse to flow, depending on gate location and packing pressure. A cold runner gating system with a rectangular edge gate of 2.0 mm to 2.5 mm land length is preferred, because pinpoint gates below 1.5 mm promote orientation-induced shrinkage variation in talc-filled systems. Mould temperature should be held at 30°C to 50°C. At mould temperatures below 25°C, the compound freezes too rapidly at the part surface and increases visible flow lines in low-gloss interior textures. Barrel profile from feed to nozzle is set at 200°C, 215°C, 225°C, and 230°C, with the nozzle at 225°C. Injection speed of 80 mm/s to 120 mm/s for wall sections of 2.0 mm to 3.0 mm reduces hesitation at ribs. Holding pressure between 40 MPa and 60 MPa is necessary to compensate for talc-induced viscosity increase. Without sufficient holding pressure, sink marks develop opposite reinforcing bosses and snap-fit features. The flexural modulus of a 20 wt% talc-filled UV PP copolymer measured according to ISO 178 typically ranges from 1,900 MPa to 2,300 MPa, which permits thinner wall sections in seat back panels relative to unfilled PP. Notched Charpy impact measured according to ISO 179-1/1eA typically remains in the 3 kJ/m² to 6 kJ/m² range, so attachment clips should not be placed at the centre of a flat panel without radiused transitions. For interior UV retention, validation is performed under SAE J2412 or ISO 4892-2 for xenon-arc exposure, with a maximum Delta E target commonly set at 3.0 after 300 h to 500 h. The actual datasheet for POLYfill PPC T25020 UV must be consulted for lot-specific values because filler particle size distribution and UV stabilizer package affect long-term gloss retention.
Wiper cowl grilles and scuttle panels made from this copolymer are positioned at the base of the windscreen, where reflected UV radiation and stagnant wet microclimates act simultaneously. The weatherable stabilizer package in the UV grade retards free-radical chain scission at the polypropylene surface. Excessive melt residence time above 250°C destroys the hindered amine light stabilizer component before final part exposure. Barrel residence time must therefore not exceed 5 min at temperatures above 240°C, and shutdown purging with linear PP should be defined in the job card. Low injection shear in thin cowl ribs may create flow marks. An injection speed of 100 mm/s to 140 mm/s with a melt temperature of 220°C to 230°C is typically used. The mould surface should be etched to VDI 24 to VDI 29 texture to mask minor flow-line visibility. Parts are conditioned at 90°C for 2 h and measured on a granite surface plate with a dial indicator having 0.01 mm resolution to record local distortion. Although talc-filled PP has higher heat deflection than unfilled PP, its heat deflection temperature under 0.45 MPa load according to ISO 75-2/B remains in the range of 95°C to 110°C, so post-cure oven temperatures in paint lines above 120°C are incompatible for uncoated assemblies. Coating systems for PP require flame plasma or corona surface activation before adhesion. Without activation, crosshatch adhesion according to ISO 2409 falls below the Gt 1 acceptance limit. In applications requiring painted or low-gloss black cowl surfaces, the compound should be evaluated for surface polarity after 48 h of storage because hydrophobic recovery reduces dyne level.
| Regulation / Standard | Specific Provision | Boundary Condition |
|---|---|---|
| REACH Regulation (EC) No 1907/2006 | SVHC candidate list concentration below 0.1 wt% | Verify lot certificate; pigment masterbatch may alter SVHC status |
| RoHS Directive 2011/65/EU | Annex II restricted substances: lead, mercury, cadmium, hexavalent chromium, PBB, PBDE | Raw compound conformity must be confirmed by XRF screening or digestion testing |
| FDA 21 CFR 177.1520 | Olefin polymer provisions for food contact | Applies only if the specific talc and pigment package meet purity requirements |
| UL 94 | Flammability class at end-part thickness, commonly 1.5 mm or 3.0 mm | Talc-filled PP typically achieves HB; V-class ratings require validated FR modification |
| ISO 4892-2 / SAE J2527 | Filtered xenon-arc weathering | Acceptance limits depend on OEM or end-use specification |
| VDA 278 / VOC emission protocol | Thermal desorption emissions for interior components | Applies mainly to automotive interior uses, not exterior trims |
Outdoor metering cabinets and switchgear enclosures use the compound where polycarbonate cost is prohibitive and UV performance of standard PP is insufficient. The wall thickness for such enclosures is usually 3.0 mm to 4.5 mm, with multiple snap-fit features and sealing ribs. Injection moulding requires a clamp force of 3 kN/cm² to 5 kN/cm² of projected area. A 400 cm² projected-area enclosure face therefore demands a clamp force from 120 t to 160 t. This pressure range is required to prevent mould breathing at the sealing-rib land. Talc orientation at the melt front creates anisotropic weld lines at the confluence of flow around core pins. Weld-line strength at such locations typically drops to 50% of the base notched Charpy value. To preserve impact resistance, the gate should be positioned so that weld lines migrate to non-load-bearing edges. For outdoor UV exposure, accelerated weathering according to ISO 4892-2 with a filtered xenon-arc lamp at 0.51 W/m²/nm at 340 nm and a black-standard temperature of 65°C is used to compare Delta E and tensile impact retention. After 1,000 h of this cycle, tensile strength retention of a properly stabilized talc-filled PP should remain above 70%. If retention falls below this level, the UV package is insufficient. The material remains combustible and should not be specified where UL 94 V-0 is mandatory unless validated with an intumescent or halogen-free flame-retardant masterbatch that does not degrade UV stability. Published data for UL-rated fire enclosures using POLYfill PPC T25020 UV specifically is limited, so enclosure certification must be based on end-part testing rather than raw-material substitution.
Condensate drain pans and fan ring housings in air-conditioning units require resistance to alternating wet-dry cycles, low creep under bolt load, and dimensional repeatability across mounting bosses. The copolymer component raises impact resistance relative to a 20 wt% talc-filled homopolymer PP while retaining modulus. For a typical drain pan with wall sections of 2.5 mm to 3.5 mm, the recommended melt temperature is 210°C to 230°C. A lower melt temperature than 200°C causes talc agglomeration at the check ring and intermittent short shots in long fan-ring ribs. The mould should be temperature-controlled at 35°C to 55°C. Higher mould temperatures up to 60°C improve weld-line strength across the drain outlet boss but increase cycle time by 20% to 30%. Pre-drying at 80°C for 2 h is required before processing if bags have been opened longer than 4 h or if plant relative humidity exceeds 60%. Residual moisture in talc-filled PP produces silver streaks and surface splay on textured drain pan surfaces. The grade’s shrinkage anisotropy means that long rectangular pans with asymmetric boss placement may exhibit out-of-plane warpage beyond 1.0 mm/m unless gating is located to balance flow length. Validation includes a thermal cycling test between 5°C and 80°C for 500 cycles, followed by a pressure-decay leak test at 0.05 MPa on the moulded pan using a calibrated differential pressure decay tester. Materials that crack or leak at the boss radius after conditioning are rejected. The UV package is relevant only if air-conditioning components are exposed during outdoor storage or service. Indoor components are typically over-specified for UV stabilization.
| Process Variable | Starting Range | Reference / Equipment |
|---|---|---|
| Pre-drying | 80°C for 2 h to 3 h | Desiccant dryer, dew point -30°C or lower |
| Barrel temperature profile | 200°C / 215°C / 225°C / 230°C | Reciprocating screw injection moulding machine, 20:1 to 24:1 L/D |
| Nozzle temperature | 225°C to 235°C | Open nozzle or spring shut-off nozzle with 3.0 mm minimum bore |
| Mould temperature | 30°C to 50°C | Water temperature control unit; use 60°C only for weld-line-critical parts |
| Injection speed | 80 mm/s to 140 mm/s | Adjust by wall section and flow-length/wall-thickness ratio |
| Holding pressure | 40 MPa to 60 MPa | Verify gate freeze time by weight stability across 10 consecutive shots |
| Back pressure | 0.5 MPa to 1.0 MPa | Screw recovery speed 50 rpm to 100 rpm |
| Residence time above 240°C | Below 5 min | Prevents UV stabilizer degradation |
String trimmer spools, blower housings, and hedge-trimmer body shells are moulded in colours that must survive prolonged sun exposure and occasional fuel or pesticide contact. The combination of high-flow copolymer and 20 wt% talc allows filling of thin acoustic ribs down to 1.4 mm in blower impeller housings without surface delamination. Hot-runner systems with valve gates are generally not advised for this talc concentration when gate diameter is below 1.0 mm, because high shear through the valve pin can break talc platelets and reduce flexural modulus by as much as 10% to 15% in the gate region. A heated sprue bushing with an open nozzle of 3.0 mm diameter is more robust for multi-cavity tooling. The material’s UV stabilization is evaluated under ISO 4892-2 with xenon parameters common for exterior components, but acceptance limits for garden power tools are usually less strict: Delta E below 8.0 and surface cracking absent after 1,000 h to 1,500 h. Impact-modified PP copolymer with talc also shows better low-temperature performance than homopolymer talc grades. Notched Charpy at -20°C is typically reduced by 20% to 30% relative to the 23°C value, but remains acceptable for clamshell housings. Solvent resistance should be checked with white spirit and commercial two-stroke fuel splashes. If stress cracking is observed on loaded snap-fits after 24 h of wet contact with mineral oil, the talc-filled copolymer is not suitable for fuel tank shells. This application describes housing components only, not fuel-contacting reservoirs.
Returnable logistics trays, battery box bases, and outdoor furniture substructures use talc-filled PP copolymer for ribbed panel designs because it balances stiffness, impact at ambient temperature, and resistance to sun-fading during open-yard storage. Stacking loads of 250 kg to 500 kg require the base panel to be designed with crossing ribs and a wall thickness of at least 4.0 mm at load-bearing contact pads. The tensile creep modulus measured at 60°C under a constant stress of 4 MPa for 1,000 h according to ISO 899-1 is lower than the short-term modulus measured by ISO 527-2. Design calculations should apply a creep reduction factor of 0.6 to 0.7 unless the specific grade datasheet provides higher confidence data. The compound should be processed with a back pressure of 0.5 MPa to 1.0 MPa to disperse talc and maintain consistent density. Insufficient back pressure produces visual streaks of unmixed filler near the sprue. In outdoor furniture subframes, the UV-stabilized formulation resists chalking under ISO 4892-2 for 2,000 h with less than 5% tensile strength loss, according to typical talc-filled UV PP weathering curves. Direct contact with alkaline cleaning agents above pH 10 is not recommended because prolonged exposure may attack the talc surface and reduce impact properties at stress concentrators. For load-bearing certification, the final part must be tested under ISO 8611-1:2021 for plastic pallet loads or the relevant EN 581 standard for furniture stability. The raw material itself cannot guarantee compliance without geometry-specific evaluation.
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The grade designation POLYfill PPC T25020 UV PP Copolymer identifies a mineral-filled polypropylene impact copolymer supplied in pellet form. The segment “PPC” denotes the polypropylene copolymer matrix; the segment “T25020” is read as a nominal 25 wt% talc loading together with a nominal melt mass-flow rate of 20 g/10 min at 230 °C under 2.16 kg dead weight according to ISO 1133-1. The suffix “UV” indicates that the formulation contains a light-stabilizer package rather than a surface-applied UV coating. Exact lot-to-lot values are governed by the manufacturer’s certificate of analysis; the product data sheet remains the controlling specification. Product identity may be checked by filler ash content to ISO 3451-1, by differential scanning calorimetry for the copolymer melting endotherm, and by melt mass-flow rate to ISO 1133-1. Because the product is a talc-filled impact copolymer, the crystallisation behaviour, ethylene content, and filler particle-size distribution will influence final mechanical and thermal performance.
| Property | Standard | Typical reported range |
|---|---|---|
| Density | ISO 1183-1 | 1.08–1.15 g/cm³ |
| Melt mass-flow rate | ISO 1133-1 | 18–22 g/10 min |
| Tensile yield strength | ISO 527-2 | 24–30 MPa |
| Flexural modulus | ISO 178 | 2300–3200 MPa |
| Notched Izod impact at 23 °C | ISO 180/1A | 5–10 kJ/m² |
| Heat deflection temperature at 1.8 MPa | ISO 75-2/A | 70–85 °C |
| Mold shrinkage | ISO 294-4 | 0.006–0.012 mm/mm |
Published data for this specific configuration is limited. The ranges in Table 1 represent the relevant property class and are not a substitute for lot-specific certification.
The melt should be maintained at 220 °C to 250 °C, with a preferred melt temperature of 230 °C. Barrel set points on a conventional three-zone injection press are typically 190 °C to 210 °C in the rear zone, 200 °C to 220 °C in the centre zone, 220 °C to 240 °C in the front zone, and 230 °C to 250 °C at the nozzle. The temperature limit is defined by degradation kinetics rather than by melting: sustained melt temperatures above 270 °C can accelerate chain scission of the ethylene-propylene copolymer phase and consume the antioxidant package, resulting in yellowing, reduced impact strength, and surface splay. On production injection machines, barrel residence time should be held between 2 min and 8 min; longer residence times above 15 min at melt temperatures above 240 °C have been associated with batch-to-batch colour drift and lower weld-line strength.
Drying is generally unnecessary when the moisture content remains below 0.05 wt% by Karl Fischer titration to ISO 15512. However, talc-filled PP can pick up surface moisture from high-humidity storage. If sacks are open for more than 24 h at relative humidity above 60 %, pre-drying for 2 h to 4 h at 80 °C in a desiccant dryer with a dew point of -30 °C or lower is recommended. Overdrying above 100 °C can increase yellowing and should be avoided.
The product should be processed on through-hardened screws because the talc filler is abrasive. A general-purpose injection screw with a compression ratio of 2.5:1 to 3.0:1 and an L/D ratio of 20:1 to 24:1 is adequate; the non-return valve must be designed for filled melts to prevent leakage and inconsistent shot weight. If the material is to be re-compounded or masterbatched, a co-rotating twin-screw extruder with L/D of 36:1 and atmospheric venting is preferred.
A single-point MFR of 20 g/10 min is not a complete rheological specification. Mold-filling simulation should use shear-viscosity data obtained by capillary rheometry from 10 s-1 to 10,000 s-1 at 230 °C, 250 °C, and 270 °C, together with pressure-volume-temperature data and thermal conductivity values. The talc filler raises thermal conductivity relative to unfilled PP, which shortens cooling time but also increases the risk of non-uniform crystallisation in thick sections. For thin-wall sections below 1.5 mm, mold-filling analysis should include the effect of shear heating on viscosity. Shear thinning is pronounced in talc-filled PP; the single-point MFR tends to overstate resistance to flow in thin-wall applications. Actual spiral flow tests on the target tool are recommended before tool steel is cut, because talc platelet orientation and wall thickness interact non-linearly with flow length.
Mold shrinkage for this grade is anisotropic because flow-induced orientation of talc platelets reduces shrinkage in the flow direction and increases shrinkage in the cross-flow direction. The anisotropy ratio for 25 wt% talc-filled PP impact copolymer is typically between 1:1.5 and 1:2.0. Toolmakers should not apply a single isotropic shrinkage factor; shrinkage should be measured on ISO 294-4 plaques in both flow and cross-flow directions. Lower absolute shrinkage relative to unfilled PP is obtained because the rigid talc platelets constrain thermal contraction. Mold temperatures between 20 °C and 60 °C are acceptable; however, for flatness-critical parts, mold temperatures of 40 °C to 60 °C and uniform cooling circuits reduce differential shrinkage. Weld lines are a primary weakness: a talc-filled PP impact copolymer can retain only 40 % to 60 % of the unfilled matrix tensile strength at a weld line. Gate location should therefore move weld lines away from high-tensile or impact load paths. Sharp internal corners below 0.5 mm radius should be avoided because the filled grade is notch-sensitive.
Relative to an unfilled PP impact copolymer, the 25 wt% talc-filled grade typically raises flexural modulus by a factor of 2.0 to 2.5 and reduces mold shrinkage by 40 % to 60 %. The trade-off is a reduction in notched impact strength at room temperature because the rigid talc platelets act as stress concentrators. The impact-copolymer matrix still retains better low-temperature toughness than a talc-filled PP homopolymer, because the ethylene-propylene rubber phase shifts the ductile-to-brittle transition to lower temperatures.
Compared with a 25 wt% calcium carbonate-filled PP copolymer, a talc-filled grade generally provides higher flexural modulus and lower creep at a given filler loading because the platy talc particles have a higher aspect ratio than spherical or blocky calcium carbonate particles. The trade-off is stronger anisotropy of shrinkage and lower surface gloss in high-speed injection molding. Compared with a 30 wt% short-glass-fibre reinforced PP, this grade offers lower density, lower warpage, smoother unpainted surfaces, and more uniformly isotropic mechanical response, but it does not match the tensile strength, flexural modulus, or heat deflection temperature of glass-fibre reinforced PP. Against a lower-MFR variant of the same talc-filled PP family, the 20 g/10 min grade provides better thin-wall filling but lower melt strength for profile extrusion or large-part blow molding.
The UV suffix differentiates this grade from non-UV talc-filled PP copolymers. Non-UV analogues are unsuitable for sustained exterior exposure, whereas the UV-stabilized version is intended for applications where sunlight exposure is intermittent or continuous. The stabilizer package is not a substitute for black pigment protection; carbon black in weather-resistant formulations should be selected with neutral or alkaline surface chemistry to avoid deactivating hindered amine stabilizers.
Outdoor durability is controlled by the stabilizer package, pigment selection, part thickness, and solar UV dose. Polypropylene undergoes photo-oxidative chain scission in the presence of UV radiation; hindered amine light stabilizers and UV absorbers slow the rate of gloss loss, chalking, and embrittlement but do not eliminate them. Accelerated weathering is tested to ISO 4892-2 or ASTM D4329, but published data for this specific configuration is limited. For exterior parts, the complete colour-matched formulation should be tested in the final part geometry. The grade is not recommended for continuous load-bearing service above 90 °C without long-term heat aging data per ISO 4577. Avoid direct contact with strong oxidizing acids, chlorinated hydrocarbons, and ketones; polypropylene is not rated for continuous contact with these media.
Incoming quality control should monitor ash content, melt mass-flow rate, tensile yield strength, notched Izod impact, and colour, with tolerances established from the supplier’s certificate of analysis. The ash method should use 30 min ignition at 600 °C according to ISO 3451-1; filler content is reported as dry-basis mineral residue. Storage should be in unopened bags in a dry area below 40 °C, away from direct sunlight. After opening, bags should be resealed to prevent moisture uptake and dust contamination. A maximum of 20 % regrind by weight is a common production ceiling for talc-filled UV-stabilized PP, provided that the regrind is well-blended and free of dust or degraded particles. Higher regrind levels reduce impact strength and increase surface defects. Batch-to-batch variance in filler particle size and stabilizer concentration can produce measurable changes in flexural modulus and accelerated-weathering retention. Incoming resin should be evaluated against a retained reference sample; a shift in the talc residue curve by more than 2 wt% from the reference should trigger a supplier review.
Candidate application categories include automotive wheel arch liners, exterior lower trim, cowl covers, HVAC housings, electrical enclosures, and outdoor furniture. These applications use the combination of medium-flow moldability, reduced shrinkage, and UV stabilization. For automotive interior applications, flammability must be validated according to FMVSS 302 or ISO 3795, and the lot-specific certificate should state the pass/fail result. Paint adhesion to talc-filled PP is not automatic; talc enrichment at the surface can reduce coating adhesion. Surface preparation by flame or corona treatment and cross-cut adhesion per ISO 2409 should be trialled on production tooling, particularly on machines with clamp force above 5000 kN, because laboratory plaques do not reproduce the packing pressure, shear, and orientation experienced on production-scale equipment.
| Compliance area | Governing instrument | Verification boundary |
|---|---|---|
| US food contact | FDA 21 CFR 177.1520(c) | Supplier formulation letter; end-use temperature and food type limitations |
| EU food contact | Regulation (EU) No 10/2011 | Overall migration per EN 1186-1; specific migration limits for additives |
| RoHS | Directive 2011/65/EU Annex II | Supplier declaration for Pb, Hg, Cd, Cr VI, PBB, and PBDE below 0.1 wt% in homogeneous material |
| REACH | Regulation (EC) No 1907/2006 Article 33 | No SVHC above 0.1 wt% per article unless notification is provided |
Compliance is formulation-specific and must be confirmed by the producer or a retained test laboratory; it cannot be inferred from the base polymer grade alone. For appliance parts such as washing-machine tubs or dishwasher components, long-term hydrolytic stability of the talc coupling agents and antioxidants should be evaluated in the actual detergent solution at service temperature, because published data for this specific configuration is limited.