| HS Code | 930559 |
| Density | 1.08 g/cm³ |
| Melt Flow Rate 230 C 2 16 Kg | 20 g/10 min |
| Tensile Strength At Yield | 25 MPa |
| Elongation At Break | 15% |
| Flexural Modulus | 2600 MPa |
| Flexural Strength | 35 MPa |
| Izod Impact Notched 23 C | 4.5 kJ/m² |
| Heat Deflection Temperature 0 45 Mpa | 110 °C |
| Vicat Softening Temperature A 50 | 130 °C |
| Hardness Shore D | 70 |
As an accredited POLYfill PPC T25020 PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied as 25 kg bags of POLYfill PPC T25020 PP Copolymer granules, sealed for moisture protection and easy handling. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL) for POLYfill PPC T25020 PP Copolymer: 20-foot full container load, safely packed, for efficient transport. |
| Shipping | POLYfill PPC T25020 PP Copolymer ships as non-hazardous plastic pellets in sealed, moisture-resistant bags or bulk containers. Keep dry, avoid excessive heat, and store away from ignition sources. Use covered trucks or containers to prevent contamination. Standard handling with minimal dust exposure is advised; no special transport classification required. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep containers tightly closed to prevent moisture contamination and dust accumulation. Avoid prolonged exposure to temperatures above 50°C. No special restrictions; protect from mechanical damage. Under proper conditions, shelf life is typically 12 months from date of manufacture. |
| Shelf Life | Store in original, sealed packaging in cool, dry conditions away from sunlight. Shelf life is two years from manufacture date. |
Across thin-wall injection molding lines producing dairy cups, margarine tubs and reusable microwaveable containers, POLYfill PPC T25020 is metered as the continuous polypropylene copolymer phase at 100 phr. The grade designation indicates a nominal melt mass-flow rate of 25 g/10 min when tested according to ISO 1133-1:2022 at 230 °C/2.16 kg. The formulation addition ratio comprises an acid scavenger masterbatch at 0.03-0.08 phr, a nucleating package at 0.05-0.20 wt%, and a slip/antiblock masterbatch at 1-2 wt%. Nucleation above 0.30 wt% provides diminishing cycle-time benefit and may induce differential shrinkage-related warpage in rectangular containers. Melt temperature is controlled at 230 °C ±5 °C through a barrel profile of 180 °C feed, 210 °C compression, 230 °C metering, and 220 °C nozzle. Pre-drying at 80 °C for 2-4 h is required when storage relative humidity exceeds 60%; residual moisture can hydrolyze acid scavenger and produce splay on container surfaces. Thin-wall cavities with wall stock down to 0.8 mm are filled using injection velocities of 180-300 mm/s and holding pressures of 40-70 MPa on hydraulic toggle machines with clamp force from 1,300 kN to 4,000 kN. Mold temperature is maintained at 15-40 °C with turbulent cooling water at 10-20 °C to reduce cycle time while avoiding premature freeze-off. Compliance for food-contact output is governed by FDA 21 CFR 177.1520 for olefin polymers and EU EU 10/2011; overall migration must remain ≤10 mg/dm² under aqueous, acidic and fatty food simulant conditions. Terminal products include thin-wall dairy cups, microwaveable trays, reusable lunch boxes, and similar food storage articles.
For tooling designed for thin-wall dairy cups, gate dimensions and hot-runner balance are matched to the copolymer melt-flow rate; pressure drop across hot-drop systems is maintained below 15 MPa to avoid excessive shear heating. The nucleating package increases crystallization temperature and shortens cooling time, but gate blush and flow marks are controlled through valve-gated hot runners and mold surface temperatures at the upper end of the 15-40 °C range. Migration testing under EU 10/2011 uses simulant B for aqueous acidic contact and simulant D2 for fatty foods, with overall migration ≤10 mg/dm². Specific migration of nucleating agents and slip additives is evaluated against the assigned SML where listed in Annex I of EU 10/2011.
| Standard or regulation | Test method or clause | Criterion | Application condition |
|---|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymer specifications | Conforms for food-contact articles | Room temperature to microwave reheating |
| EU 10/2011 | Overall migration EN 1186 | ≤10 mg/dm² | Aqueous, acidic and fatty food simulants |
| EU 10/2011 | Specific migration limits | Assigned SML per listed additive | Nucleator and slip/antiblock packages |
| REACH (EC) 1907/2006 | SVHC Candidate List | <0.1 wt% per substance | All grade lots shipped to EU |
Automotive interior trim based on POLYfill PPC T25020 is formulated with an ethylene-propylene elastomer modifier to maintain notched Charpy impact above 10 kJ/m² at -30 °C when tested according to ISO 179-1/1eA. The formulation addition ratio places the PP copolymer at 70-85 wt%, the elastomer modifier at 10-20 wt%, talc at 5-15 wt%, and a primary antioxidant package at 0.2-0.5 phr. The low-temperature ductile-to-brittle transition is controlled primarily by the ethylene content of the copolymer and the particle-size distribution of the dispersed elastomer phase; excessively fine rubber particles generated by over-shearing reduce impact energy absorption, while agglomerates create surface defects and paintability failures. Compounding is performed on co-rotating twin-screw extruders with L/D from 40:1 to 44:1, maintaining a temperature profile from 180 °C to 220 °C, side-feeding talc after polymer melt formation, and applying vacuum devolatilization at -0.08 MPa to remove low-molecular-weight volatiles. The finished compound is injection molded at melt temperature 220-240 °C, mold temperature 30-60 °C, injection speed 80-180 mm/s, holding pressure 50-80 MPa, and cooling time 20-35 s for a 2.5 mm wall section. Automotive interior compliance includes flammability to FMVSS 302 and ISO 3795, VOC emissions according to VDA 278, total carbon emissions according to VDA 277, fogging according to ISO 6452, and REACH registration under (EC) 1907/2006. Terminal products include door panel lower trims, glove box housings, pillar covers, and seatbelt guide covers. Process limitations include avoiding amine-based processing aids, which can cause discoloration and premature thermo-oxidative degradation at melt temperatures above 220 °C; adhesion to polyurethane foam systems must be verified because mold release and slip agents used in packaging grades can reduce surface energy and weaken bond strength.
VDA 278 testing of compounded pellets after vacuum devolatilization typically targets total VOC below 100 µg/g and fogging condensation values below 2 mg according to ISO 6452, though acceptance limits are OEM-specific. Elastomer content and talc level operate as inverse levers: talc improves stiffness and scratch resistance but raises density and lowers impact, while elastomer raises low-temperature ductility but depresses modulus and increases VOC load. For pillar covers with visible surfaces, grain depth is typically 100-200 µm and grain retention is assessed after heat aging at 100 °C for 500 h according to OEM methods; published data for this specific formulation at the lower talc boundary is limited.
For closure systems molded from POLYfill PPC T25020, controlled additive migration keeps removal torque stable over warehousing periods up to 12 months at ambient temperatures below 40 °C. The formulation addition ratio is 100 phr copolymer, erucamide slip agent at 0.05-0.15 phr, and a phosphite/phenolic antioxidant package at 0.05-0.12 phr; antioxidant depletion caused by prolonged high-temperature storage shifts torque retention as the polymer surface oxidizes and friction increases. Slip agent loading above 0.20 phr may cause excessive bloom, lowering coefficient of friction and creating cap back-off risk on high-speed filling lines. Pre-drying is performed at 80 °C for 2 h when storage relative humidity exceeds 60%. Injection molding uses melt temperature 200-240 °C, hot runner temperature 220-240 °C, mold temperature 10-30 °C, and cycle time 6-12 s on 30-cavity tooling. Compression molding lines for polyolefin closures operate at melt temperature 160-180 °C and mold cooling at 8-15 °C. Torque retention is tested according to ASTM D3089-97; seal integrity is verified by vacuum decay or pressure differential methods on filled containers. Compliance for food and beverage contact draws on FDA 21 CFR 177.1520, EU EU 10/2011, and the REACH SVHC threshold of 0.1 wt%. Terminal products include tamper-evident closures for still water, carbonated soft drink caps requiring environmental stress crack resistance, and edible oil bottle caps.
Horizontal-axis washing machine outer tubs and dishwasher spray-arm carriers use POLYfill PPC T25020 as the impact-modified continuous matrix in talc-reinforced formulations at 60-80 wt%. The formulation addition ratio for these structural appliance components comprises high-aspect-ratio talc at 20-40 wt%, organosilane coupling agent at 0.2-0.8 wt% based on filler mass, thermo-oxidative stabilizer at 0.2-0.5 phr, and carbon black masterbatch at 0.5-2 wt%. Compounding is carried out on co-rotating twin-screw extruders with L/D 44:1 and a barrel profile of 180-230 °C, side-feeding talc at zone 5, and vacuum venting at -0.08 MPa to remove moisture and volatile oligomers. Injection molding uses clamp force from 6,000 kN to 16,000 kN, melt temperature 220-250 °C, mold temperature 20-60 °C, holding pressure 40-70 MPa, and cooling time 30-60 s depending on wall thickness from 3 mm to 8 mm. Weld-line strength is a process control point because talc platelet orientation around ribs and mounting bosses can reduce local tensile strength relative to the unribbed wall; the reduction is governed by filler orientation and must be measured with ISO 527-2 specimens cut from the part. Mineral-filled compounds are dried before molding because talc can contribute moisture; a hopper dryer set to 80 °C with dew point below -30 °C is typical. Screw speed is limited to 200-300 rpm during compounding to prevent excessive filler attrition. Electrical safety is evaluated under IEC 60335-1, flammability rating is typically UL 94 HB at 1.5 mm, and UV weathering for external white-goods components follows ISO 4892-2. Terminal products include washing machine outer tubs, dishwasher spray arms, dryer blower housings, and water pump housings. Published data for this specific grade in hydrolytic conditioning beyond 1,000 h in hot detergent solution is limited; long-term exposure tests should be conducted on the finished part.
Because biological evaluation plans under ISO 10993-1 for non-implant, surface-contacting devices are tied to material formulation and processing history, manufacturers of diagnostic instrument housings and sharps containers evaluate POLYfill PPC T25020 as a 100 phr base polymer with a narrow additive package. The formulation addition ratio is 100 phr copolymer, nucleating agent at 0.05-0.15 wt%, and a low-phenolic antioxidant package at 0.05-0.15 phr; slip agents are normally omitted because surface migration can change adhesive bonding, reagent deposition, and marking inks. Injection molding is performed in ISO 13485-controlled cleanrooms with pre-drying at 80 °C for 2-3 h, melt temperature 190-230 °C, mold temperature 20-40 °C, and validated process parameters documented under IQ/OQ/PQ protocols. Sterilization compatibility is typically evaluated by ethylene oxide exposure or gamma irradiation up to 25 kGy; steam autoclave cycles at 121 °C for 20 min may introduce dimensional change and must be characterized on the finished part, especially for living hinges or snap features. Compliance references include FDA 21 CFR 177.1520 for olefin polymers, EU EU 10/2011 for indirect food-contact materials, ISO 10993-5 for in vitro cytotoxicity, and ISO 10993-10 for irritation and skin sensitization. Terminal products include IVD cartridge housings, sharps disposal containers, handheld diagnostic instrument casings, and spacer bodies for non-pressurized aerosol delivery. The grade is not specified for long-term implantable, blood-contacting, or invasive applications; published data for this specific configuration in hemocompatibility and implantation studies is limited, and device manufacturers must conduct gap assessments under ISO 10993-1.
| Standard | Purpose | Typical test endpoint | Application boundary |
|---|---|---|---|
| ISO 10993-1 | Biological evaluation planning | Contact duration and nature classification | Surface-contacting, non-implant |
| ISO 10993-5 | In vitro cytotoxicity | Manufacturer-defined cell viability criterion | Extract dilution test |
| ISO 10993-10 | Irritation and skin sensitization | No erythema or edema above grade 1 | Intact skin contact |
| ISO 13485 | Quality management system | Process validation IQ/OQ/PQ | Cleanroom injection molding |
When power tool housings are overmolded onto structural bosses and threaded inserts, POLYfill PPC T25020 is processed at 90-100 wt% as the base resin, with an impact modifier at 0-10 wt% where drop resistance below -10 °C is required. For stiffened configurations, short-glass fiber is added at 10-30 wt% with a coupling agent at 0.3-0.6 wt% based on fiber mass, plus a UV stabilizer package at 0.2-0.5 phr and antioxidant at 0.1-0.2 phr. Formulation loading shifts with part stiffness targets; glass fiber above 30 wt% reduces flowability and increases tool abrasion, while unfilled copolymer may not satisfy long-term creep limits in high-torque tool bodies. Injection molding is conducted with pre-drying at 80 °C for 2 h, melt temperature 220-250 °C, mold temperature 30-60 °C, and screws with low compression ratios and chromium-alloy check rings for glass-filled materials. Wall thickness transitions from 5 mm at mounting pillars to 1.5 mm at air vents are processed with holding pressure 50-80 MPa and cooling time 25-45 s. Shrinkage is anisotropic in glass-filled configurations; mold-flow simulation with fiber-orientation tensor models predicts warpage, with typical shrinkage of 0.2-0.5% in the fiber direction and 0.8-1.2% transverse depending on wall thickness and gate location. Gates are placed away from high-stress bosses to prevent jetting and reduce weld-line sensitivity. Compliance includes RoHS Directive 2011/65/EU including amendment (EU) 2015/863, UL 94 HB at 1.5 mm or 3.0 mm, and REACH SVHC screening below 0.1 wt%. Terminal products include angle grinder housings, battery pack covers, and circular saw guards. The copolymer should not be specified where sustained contact with chlorinated solvents or turpentine is expected because environmental stress cracking can occur in polypropylene; threaded insert pull-out strength must also be revalidated when operating temperatures exceed 80 °C.
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The material designated POLYfill PPC T25020 is a polypropylene copolymer compound in which a mineral filler is dispersed in a copolymer matrix. The grade identifier PPC denotes polypropylene copolymer; T25020 is interpreted as a grade identifier commonly associated with a 20 wt% mineral loading because the final two digits match a filler-content convention used in mineral-reinforced polyolefin nomenclature. The exact filler chemistry, particle-size distribution, and surface treatment require confirmation against the supplier’s certificate of analysis. Published datasheet values for this specific configuration are limited; the engineering data presented here are therefore drawn from the class of 20 wt% talc-filled polypropylene copolymer compounds and should be verified lot by lot. The compound occupies an intermediate position between unfilled PP copolymer and higher-filler polypropylene compounds, targeting semi-structural injection-molded parts in which stiffness, dimensional stability, and low-temperature impact retention are selected simultaneously.
The main technical effect of a 20 wt% mineral filler in a PP copolymer matrix is the simultaneous increase in flexural modulus and heat deflection temperature, with a smaller loss in ambient-temperature impact than a homopolymer matrix of equivalent filler loading. In representative 20 wt% talc-filled PP copolymer compounds, density is controlled within 1.05–1.06 g/cm³ when tested to ISO 1183-1:2019. Melt volume-flow rate, measured at 230 °C under 2.16 kg to ISO 1133-1:2022, typically falls between 8 cm³/10 min and 15 cm³/10 min for injection-molding grades, although the T25020 identifier should not be read as a direct melt-flow value. Flexural modulus, determined by ISO 178:2019, is commonly between 2200 MPa and 2600 MPa, compared with 1100–1400 MPa for unfilled PP copolymer. Tensile yield stress, measured to ISO 527-2:2012 or ASTM D638-14, is normally 25–30 MPa. Notched Charpy impact at 23 °C under ISO 179-1:2010 is typically 6–12 kJ/m², while at -20 °C the value decreases to 2.5–4 kJ/m². The copolymer component is critical to this low-temperature behavior; an equivalent 20 wt% talc-filled PP homopolymer can exhibit one-third to one-half lower notched impact at -20 °C.
| Property | Test method | Unfilled PP copolymer | 20 wt% talc-filled PP copolymer | 40 wt% talc-filled PP homopolymer |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 0.90–0.91 g/cm³ | 1.05–1.06 g/cm³ | 1.22–1.24 g/cm³ |
| Flexural modulus | ISO 178:2019 | 1100–1400 MPa | 2200–2600 MPa | 3500–4500 MPa |
| Tensile yield stress | ISO 527-2:2012 | 22–27 MPa | 25–30 MPa | 28–33 MPa |
| Notched Charpy impact, 23 °C | ISO 179-1:2010 | 8–12 kJ/m² | 6–12 kJ/m² | 3–5 kJ/m² |
| Notched Charpy impact, -20 °C | ISO 179-1:2010 | 4–6 kJ/m² | 2.5–4 kJ/m² | 1.5–2.5 kJ/m² |
| Heat deflection temperature, type B | ISO 75-2:2013 | 85–100 °C | 110–125 °C | 125–140 °C |
| Mold shrinkage | ASTM D955-08 | 1.2–1.8% | 0.8–1.2% | 0.5–0.8% |
In compounding, the dispersion of a 20 wt% mineral filler is controlled less by the nominal filler content than by screw design and barrel-temperature management. On a 40:1 L/D co-rotating twin-screw extruder, the filler is typically side-fed downstream of the polymer melting zone to limit attrition of the copolymer molecular weight and to preserve impact performance. Melt temperature at the die is usually maintained between 220 °C and 250 °C. Vacuum venting at 0.08 MPa to 0.09 MPa reduces volatile carryover and surface splay. Screw speeds in the range 300–500 min⁻¹ are common, but throughput must be balanced against torque and residence time; excessive specific energy input can shift the molecular weight distribution and reduce notched impact. Filler dispersion quality is monitored by filter pressure rise, optical microscopy, and ash content according to ISO 3451-1:2019. Batch-to-batch variance in a 20 wt% talc-filled PP copolymer is lower when the filler is fed by gravimetric side feeder and the base copolymer has a controlled melt-flow ratio.
For injection molding, the processing window for 20 wt% talc-filled PP copolymer is broad enough for multi-cavity tools but narrow enough that melt residence time must be controlled. Barrel settings from feed to nozzle are typically 200–220 °C, 220–240 °C, 230–250 °C, and 230–250 °C. Mold temperature is usually held between 20 °C and 50 °C; higher mold temperatures improve weld-line strength and surface gloss, while lower mold temperatures reduce cycle time but can increase molded-in stress. Injection velocity should be moderate or high enough to prevent premature freeze-off in thin sections, with holding pressure commonly 60–80% of injection pressure. Screw back pressure of 0.5–1.0 MPa assists homogenization without excessive shear heating. Required clamp force is governed by projected part area; a practical starting value for mineral-filled PP copolymer is 3–5 kN/cm² of projected area.
If packaging has been breached at relative humidity above 60%, pre-drying at 80 °C for 2–3 h in a desiccant dryer is recommended to avoid surface defects; PP is not inherently hygroscopic, but talc surfaces can adsorb moisture. The mold shrinkage of this class is 0.8–1.2% in both flow and cross-flow directions under ASTM D955-08, which is substantially lower than unfilled PP copolymer at 1.2–1.8%. This reduction in shrinkage anisotropy is often the primary reason for selecting 20 wt% mineral-filled PP copolymer over unfilled copolymer. On typical multi-cavity tools, a melt cushion of 3–5 mm is retained to avoid decompression voids and nozzle drool. Hot-runner systems should be designed with low-shear channels and no stagnation zones because mineral-filled PP copolymer can form filler-rich deposits in dead spots at elevated temperatures.
Application selection for POLYfill PPC T25020 is concentrated in injection-molded semi-structural components requiring a measurable increase in flexural modulus and a reduction in part warpage compared with unfilled PP copolymer. Typical industrial roles include interior automotive trim carriers, HVAC deflectors, air-cleaner housings, appliance structural supports, electrical enclosures, and office furniture frames. In these applications, the material is selected over 20 wt% talc-filled PP homopolymer when low-temperature ductility and knit-line toughness are judged more important than maximum heat deflection temperature. Compared with 40 wt% talc-filled PP homopolymer, the 20 wt% mineral-filled PP copolymer flows more readily in thin-wall sections, has lower density, and generates less abrasive wear on screws and check rings; however, it also exhibits lower flexural modulus and higher mold shrinkage. Against glass-fiber reinforced PP, the mineral-filled copolymer produces lower tensile strength and lower creep resistance, but offers more isotropic shrinkage, lower warpage, and lower equipment abrasion.
The principal quality risk in 20 wt% mineral-filled PP copolymer is not the average filler content but the spatial distribution of the filler particles. Poorly dispersed talc agglomerates act as stress concentrations and can reduce notched Charpy impact by 20–40% relative to a well-dispersed lot, even when ash content within the same lot is within ±1 wt%. Dispersion quality is evaluated on a production-scale twin-screw extruder by measuring melt-filter pressure increase across a 100 µm or 200 µm screen pack; a rising pressure trend indicates filler agglomeration or screen blinding. The use of a 40:1 L/D or 44:1 L/D co-rotating twin-screw line with a downstream side feeder and two high-shear kneading blocks is typical for this material class. Screw temperature control in the kneading zone is maintained below 230 °C to limit oxidative degradation of the copolymer phase. Lot consistency is further controlled through capillary rheometry at 230 °C and ash testing according to ISO 3451-1:2019. The processing limit is reached when filler loading is increased beyond 25 wt% without adjusting the base resin melt-flow rate; at that point, melt instability and screw and barrel wear increase disproportionately.
Exposure of mineral-filled PP copolymer to strong oxidizing acids, long-term hot hydrocarbons, or sustained UV without an adequate stabilizer package is not recommended. Continuous service temperature under load is governed by the heat deflection temperature and oxidative stability of the copolymer phase; for 20 wt% talc-filled PP copolymer, heat deflection temperature type B under 0.45 MPa is typically 110–125 °C, but long-term air-aging resistance above 100 °C requires lot-specific thermal stability data. The material is not inherently flame retardant; flammability under UL 94 is typically HB at 1.5 mm or 3.0 mm unless a flame-retardant package is specified. For food-contact use, compliance with FDA 21 CFR 177.1520 is possible only for olefin polymers that meet the specified migration limits; a grade-specific compliance statement is required. The migration kinetics of low-molecular-weight additives in mineral-filled PP copolymer are affected by filler surface adsorption; therefore unfilled PP migration data cannot be transferred directly to this compound.
| Parameter or regulation | Designation/test method | Relevance to PPC T25020 | Verification requirement |
|---|---|---|---|
| Density | ISO 1183-1:2019 | Class specification | Certificate of analysis |
| Melt flow rate | ISO 1133-1:2022 | Injection-processing window | Lot test |
| Flexural modulus | ISO 178:2019 | Stiffness comparison | Type test |
| Notched Charpy impact | ISO 179-1:2010 | Low-temperature toughness | Type test |
| Heat deflection temperature | ISO 75-2:2013 | Short-term thermal resistance | Type test with specimen conditioning |
| Ash content and filler dispersion | ISO 3451-1:2019 | Filler content and batch control | Lot test |
| Heavy metals and RoHS | Directive 2011/65/EU | Electrical and electronic parts | Supplier declaration |
| REACH | Regulation (EC) No 1907/2006 | General market access | SDS and SVHC declaration |
| Food contact | FDA 21 CFR 177.1520 | Food-contact applications | Grade-specific migration data |
| Flammability | UL 94 | Electrical enclosures | UL yellow card for exact grade and thickness |
In selecting POLYfill PPC T25020 against a 20 wt% talc-filled PP homopolymer, the copolymer matrix is the defining difference. At equivalent filler content, the copolymer grade retains a higher fraction of ambient-temperature ductility and improved low-temperature impact, but exhibits slightly lower tensile yield and heat deflection temperature than a filled homopolymer. The practical consequence is a narrower processing window for high-temperature demolding: mold temperature should not exceed 60 °C for mineral-filled PP copolymer unless ejection is assisted, because hot parts can distort under ejection forces. In multi-cavity tools, runner and gate diameters greater than 2.0 mm are preferred to minimize shear heating and apparent viscosity loss. Published data for this specific configuration is limited; the above boundaries are industrial defaults for the material class and should be replaced by lot-specific or application-specific data before release.