| HS Code | 112533 |
| Density | 1.04 g/cm³ |
| Melt Flow Rate 230 C 2 16 Kg | 20 g/10 min |
| Tensile Stress At Yield | 25 MPa |
| Tensile Strain At Yield | 7 % |
| Flexural Modulus | 2100 MPa |
| Izod Impact Notched 23 C | 40 J/m |
| Izod Impact Notched 30 C | 20 J/m |
| Heat Deflection Temperature 0 45 Mpa | 115 °C |
| Heat Deflection Temperature 1 82 Mpa | 70 °C |
| Vicat Softening Temperature | 145 °C |
| Rockwell Hardness | 95 |
| Mold Shrinkage | 1.0 % |
As an accredited POLYfill PPC T20020 PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | POLYfill PPC T20020 PP Copolymer supplied in 25 kg heat-sealed polyethylene-lined paper bags, palletized and shrink-wrapped for safe transport. |
| Container Loading (20′ FCL) | 20′ FCL loading of POLYfill PPC T20020 PP Copolymer in 25kg bags, palletized and secured for safe transport. |
| Shipping | POLYfill PPC T20020 PP Copolymer ships as non-hazardous plastic granules in sealed moisture-resistant bags or bulk containers. Store in a dry, ventilated area away from heat and direct sunlight. Avoid dust accumulation and use proper grounding during transfer. Handle with standard PPE to minimize dust exposure and prevent contamination. |
| Storage | Store POLYfill PPC T20020 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 and dust buildup. Avoid contact with strong oxidizers. Maintain stable room temperature; under proper conditions, shelf life is typically 12 months from delivery. |
| Shelf Life | Shelf life is typically 12 months when stored in original, sealed packaging, protected from heat, moisture, and direct sunlight. |
In automotive interior structural carriers, POLYfill PPC T20020 PP Copolymer is introduced as the unfilled matrix for mineral-reinforced injection moulding compounds. The grade designation T20020 corresponds to a nominal melt flow rate of 20 g/10 min at 230 °C/2.16 kg under ISO 1133-1:2022, placing it between extrusion-typical melt flow and thin-wall packaging flow. This flow window permits filling of ribbed articles with nominal wall thickness 1.8–2.5 mm without excessive sink, while retaining enough melt strength to avoid gas entrapment in multi-cavity tools. A representative production formulation uses 55–75 wt% T20020 as carrier resin, 15–25 wt% high-purity compacted talc masterbatch with median lamellar particle size 1.5–2.5 µm, 5–15 wt% ethylene-octene impact modifier, 0.1–0.3 wt% hindered phenolic antioxidant masterbatch, 0.05–0.2 wt% sorbitol-based nucleating agent, and 1–3 wt% carbon black masterbatch for colour and UV screening. The dispersion step is carried out on a co-rotating twin-screw extruder with L/D 40:1–52:1, side feed for talc at zone 5 of 10, barrel temperature 180–230 °C, screw speed 350–650 rpm, and vacuum devolatilization at approximately -0.08 MPa. Finished articles are injection moulded at melt temperature 210–250 °C, mould temperature 30–60 °C, injection speed 80–180 mm/s, holding pressure 40–70 MPa, holding time 12–25 s, and clamp force 800–1,500 t depending on projected area. For door module carriers with flow length exceeding 350 mm, sequential valve gating is required because talc loadings above 20 wt% reduce weld-line tensile retention by more than 20% relative to unfilled PP. Terminal product types include door module carriers, instrument panel lower retainers, glove box bins, pillar trims and seat side shields. Compliance at final-article level is conditioned by flammability testing under ISO 3795 or FMVSS 302 with a maximum burning rate of 100 mm/min, substance restrictions under Directive 2000/53/EC Annex II with limit values of 0.1 wt% for lead, mercury and hexavalent chromium and 0.01 wt% for cadmium in homogeneous materials, and REACH SVHC communication obligations under Regulation (EC) No 1907/2006. Cabin-air quality requirements are typically specified according to VDA 278 or an OEM instrument-panel testing protocol; converters must verify fogging, odour and VOC on the final compound rather than on neat resin. Published data for this specific T20020 compound configuration is limited, and part-level thermal ageing under ISO 188 should be executed before series release.
| Talc addition (wt% in compound) | Flexural modulus (ISO 178:2019) | Charpy notched impact at 23 °C (ISO 179-1/1eA) | Melt flow rate at 230 °C/2.16 kg (ISO 1133-1:2022) | Heat deflection temperature at 0.45 MPa (ISO 75-2:2013) |
|---|---|---|---|---|
| 0 | 900–1,400 MPa | 8–20 kJ/m² | 20 g/10 min | 75–90 °C |
| 15 | 2,000–2,600 MPa | 5–9 kJ/m² | 13–17 g/10 min | 95–120 °C |
| 20 | 2,200–2,800 MPa | 4–8 kJ/m² | 12–16 g/10 min | 100–125 °C |
| 30 | 2,600–3,200 MPa | 4–7 kJ/m² | 9–13 g/10 min | 110–135 °C |
The table compiles generic published ranges for talc-filled propylene copolymer matrix compounds; it is not a product datasheet and must not be used as a guarantee for this specific POLYfill grade.
In high-cavitation thin-wall packaging, T20020 is processed as a near-neat resin with low addition of colour and slip masterbatch. The formulation commonly contains 96–99 wt% T20020, 1–3 wt% polypropylene carrier colour masterbatch, 0.1–0.5 wt% erucamide-based slip/antiblock masterbatch, and optionally 0.05–0.2 wt% nucleating agent to increase crystallization temperature and shorten cycle time by 5–15%. Total slip addition above 0.8 wt% is not recommended because it leads to mould-vent plate-out, erratic lid seal force and coefficient of friction reduction beyond the target range. The conversion route is accumulator-assisted injection moulding with clamp force 250–600 t, cavity counts 24–96, injection speed 200–400 mm/s, fill time 0.2–0.5 s, melt temperature 220–260 °C, mould temperature 10–30 °C, and cooling time 4–10 s. At melt temperatures above 250 °C, residence time should remain below 10 min because erucamide decomposition and thermo-oxidative chain scission can generate taste-visible defects; the production window at the upper melt-temperature boundary is therefore approximately ±5 °C for sustained multi-shift runs. Terminal products include dairy cups, deli containers, takeaway lids, food storage trays and insert-moulded thin-wall pails with wall thickness 0.3–0.8 mm. The compliance perimeter is governed by olefin polymer authorisations rather than resin-specific certifications. The matrix below details applicable frameworks.
| Jurisdiction | Standard/Regulation | Primary requirement | Test method |
|---|---|---|---|
| United States | 21 CFR 177.1520 | Olefin polymer use in food-contact articles; converter must operate under 21 CFR 174.5 GMP | Extraction cell test under 21 CFR 177.1520 |
| European Union | Regulation (EU) No 10/2011 as amended | Overall migration limit 10 mg/dm² for plastic articles; specific migration limits for additives apply | EN 1186-1; EN 13130-1 |
| China | GB 4806.7-2016 | Overall migration limit 10 mg/dm²; potassium permanganate consumption and heavy metal limits apply | GB 31604.1 |
| European Union GMP | Regulation (EC) No 2023/2006 | Good manufacturing practice for materials and articles intended to come into contact with food | Quality assurance system audit |
The resin pellet alone does not constitute a compliant food-contact article; migration testing is required on the finished cup, lid or tray in the intended food type and time-temperature condition. Hot-fill applications above 100 °C, retortable formats, high-alcohol content above 20% or fatty food simulants beyond EU food type D may require additional organoleptic and migration validation. Published data for this specific configuration is limited.
For under-hood polypropylene compounds, T20020 is used as a high-impact diluent matrix in mineral-filled formulations where low temperature ductility and filler wetting are more critical than melt flow. Industrial compounding lines typically proportion 60–80 wt% T20020, 20–40 wt% talc or calcium carbonate masterbatch, 2–5 wt% ethylene-propylene rubber impact modifier, 0.2–0.5 wt% primary hindered phenolic antioxidant and 0.1–0.2 wt% secondary phosphite process stabilizer. The compounding extruder is a co-rotating twin-screw unit with L/D 40:1 to 52:1, side feeding at zone 5 of 10, screw speed 300–600 rpm, barrel temperature 200–240 °C, and motor torque limited to 85% when filler content approaches 40 wt% to prevent high specific energy spikes and local overheating. Injection moulding of finished under-hood articles uses melt temperature 220–250 °C, mould temperature 30–60 °C, and clamp force 600–1,600 t depending on part mass. Terminal products include engine covers, battery trays, radiator fan shrouds, washer reservoir brackets and air intake housings. The compliance perimeter is defined by UL 94 HB at 1.5 mm and 3.0 mm, thermal ageing under ISO 188 at 140–150 °C for 1,000 h, heat deflection temperature under ISO 75-2:2013, REACH under Regulation (EC) No 1907/2006, and RoHS heavy metal restrictions under Directive 2011/65/EU when the part is incorporated into an electrical/electronic assembly. Continuous under-hood exposure above 150 °C or direct contact with coolant containing ethylene glycol above 50% by volume requires replacement by glass-filled homopolymer or polyamide; published data for this specific T20020 under-hood formulation is limited and must be validated on the final part drawing.
Returnable transport packaging produced from T20020 is driven by impact retention after multiple cycles rather than by food-contact migration. Typical compositions are 95–100 wt% T20020, 3–8 wt% ethylene-propylene elastomer impact modifier added as a pre-compounded masterbatch, 0.2–0.5 wt% heat stabilizer masterbatch, and for outdoor exposure 1–3 wt% HALS/UV masterbatch with 1–2 wt% carbon black. The injection moulding process is set at melt temperature 210–260 °C, mould temperature 20–50 °C, injection speed 100–250 mm/s, holding pressure 30–60 MPa, cooling time 30–70 s for wall thickness 5–10 mm, and clamp force 400–2,000 t. For large pallet boxes, the initial injection speed near the sprue or valve gate is reduced to 40–60 mm/s to avoid jetting and flow hesitation; hot runner manifolds with sequential valve gates are recommended when flow length exceeds 800 mm. Terminal product types include foldable crates, collapsible bulk containers, pallet boxes, dunnage trays and returnable dairy cart frames. Compliance is verified through dimensional and mechanical testing under ISO 8611-1:2011 for pallet performance, material tensile/yield testing under ISO 527-2:2012 or ASTM D638-14 when specified by the buyer, flammability classification under UL 94 HB, and REACH obligations under Regulation (EC) No 1907/2006. For sub-zero distribution below -20 °C, unnotched impact testing under ISO 179-1/1eU is more predictive than notched Charpy because crate ribs and corner nodes fail from multiaxial loading rather than notch propagation; all load-bearing internal radii should be at least 2 mm. Published data for this specific configuration is limited and stack-load creep must be validated on the finished crate design.
A separate downstream route uses T20020 in cast film extrusion as the sealant web of laminated flexible packaging. In this route, the formulation is typically 80–95 wt% T20020 and 5–20 wt% propylene-ethylene plastomer, with 0.1–0.3 wt% antiblock masterbatch and a slip masterbatch adjusted to target a coefficient of friction below 0.30 under ISO 8295. The plastomer addition reduces seal initiation temperature into the 95–110 °C range, but addition above 20 wt% causes chill-roll tack and film blocking. Cast film extrusion parameters are melt temperature 230–260 °C, die gap 0.5–1.0 mm, chill roll temperature 18–35 °C, line speed 100–250 m/min, and air gap 10–30 mm; the film is typically drawn to 15–40 µm and corona-treated to at least 38 mN/m for lamination adhesion. Terminal product types include sealant webs in laminated food pouches, lamination films for non-food overwrap, and sealant layers in non-implantable medical device packaging. Compliance is governed by Regulation (EU) No 10/2011 for food-contact laminates, 21 CFR 177.1520 for olefin polymers in contact with food, and ISO 11607-1:2019 for terminally sterilised medical device barrier systems when the final pouch is validated by the medical device manufacturer. The resin layer alone is not a sterile barrier and must be evaluated as part of the full lamination; published data for this specific T20020 sealant-web configuration is limited.
Appliance structural components use T20020 in talc-filled compounds where the lower flow rate supports thick ribs and insert-bearing bosses. A representative formulation contains 65–85 wt% T20020, 15–35 wt% talc masterbatch, 2–6 wt% ethylene-propylene or ethylene-octene impact modifier, and 0.2–0.5 wt% heat stabilizer. Injection moulding is performed at melt temperature 210–250 °C, mould temperature 40–70 °C, holding pressure 40–70 MPa, and clamp force 800–2,000 t. Hot runner systems with sequential valve gates are preferred when moulding washing machine top frames or dishwasher base frames because knit lines at load-bearing bosses can reduce fatigue life by more than 30%; all internal rib junctions should be radiused to at least 3 mm. Terminal product types include washing machine top frames, outer tub fronts, dishwasher base frames, vacuum cleaner housings and water heater shrouds. The compliance perimeter for this application includes IEC 60335-1:2020 clause 30 for resistance to heat and fire, glow wire testing under IEC 60695-2-11:2021 at 650 °C or 750 °C depending on final product current and connectivity, UL 94 HB at 1.5 mm, RoHS Directive 2011/65/EU and Regulation (EC) No 1907/2006. Vibration fatigue resistance is not covered by any single material standard; washing machine spin cycles at maximum rated dry textile load 8–12 kg impose a service-life requirement that must be verified on the finished assembly. Published data for this specific T20020 appliance compound is limited.
In non-regulated industrial houseware moulding, T20020 is injection moulded at melt temperature 220–250 °C and mould temperature 30–50 °C with a formulation of 100 wt% virgin pellets plus 0.1–0.2 wt% pigment masterbatch, producing storage totes, hanger clips and dividers under the general compliance perimeter of Regulation (EC) No 1907/2006 REACH registration; published data for this specific configuration is limited.
Competitive POLYfill PPC T20020 PP Copolymer prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618136850665
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
POLYfill PPC T20020 PP Copolymer is a polypropylene impact copolymer whose model designation places it in the 20 g/10 min melt mass-flow rate class at 230 °C under a 2.16 kg piston load when tested to ISO 1133-1:2022. The PPC prefix identifies a propylene-rich copolymer produced by sequential gas-phase polymerization; the ethylene-comonomer modification creates a dispersed elastomer phase within a semi-crystalline polypropylene matrix. This two-phase structure is the controlling difference between the grade and polypropylene homopolymer or single-phase random copolymer. Product-specific certificate-of-analysis values should be requested from the supplier because stabilizer packages, reactor lot variations, and nucleation systems influence actual mechanical, rheological, and shrinkage performance.
Unfilled density for this melt-flow class generally falls between 0.900 g/cm³ and 0.910 g/cm³ when measured to ISO 1183-1:2019. The resulting article mass is approximately 8–10% lower than polystyrene of equivalent wall section and roughly 35–40% lower than rigid PVC. Because density alone does not predict cycle time, the semi-crystalline nature of the polypropylene matrix requires gate-freeze and packing-pressure calculations that differ from amorphous thermoplastics.
In multi-cavity cold-runner tools, the material is typically processed at melt temperatures of 220–250 °C and mold temperatures of 20–50 °C. Mold-temperature settings near the upper end of this range are preferred on grained or textured surfaces to reduce flow marks and improve replication of micro-roughness. The product targets injection-molded technical parts with nominal wall sections from 1.2 mm to 4.0 mm, including appliance internal brackets, automotive interior carrier structures, battery housings, and extruded profiles requiring a balance of stiffness and low-temperature ductility.
A single-point melt mass-flow rate at low shear does not sufficiently predict filling behavior at injection shear rates. Capillary rheometry on analogous 20 g/10 min impact-copolymer resins indicates pronounced shear thinning at processing-relevant shear rates; mold-filling simulation therefore requires viscosity curves generated at 190–230 °C using a capillary rheometer with Bagley and Rabinowitsch corrections, not reliance on MFR alone. At a 2.0 mm nominal wall thickness, production-scale trials on 80–100 tonne injection machines with 25 mm general-purpose reciprocating screws have shown that melt temperatures below 200 °C can produce hesitation lines and short shots in multi-drop hot-runner tools. Raising melt temperature to 230 °C generally lowers fill pressure but may add 5–10 s of cooling time in thick bosses and at the junction of reinforcing ribs. Weld-line impact retention in this material class is lower than bulk-material impact values, and the loss is controlled primarily by melt-temperature and mold-temperature gradients, vent placement, and gate sequencing. Published data for this specific branded configuration in hot-runner multi-cavity weld-line applications is limited; first-article impact testing on welded areas is required before production approval.
The following class-level ranges are representative for unfilled 20 g/10 min polypropylene impact copolymers. They are suitable for preliminary tooling calculations and material selection but do not replace batch-specific values from the manufacturer.
| Property | Test method | Unit | Representative range |
|---|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 | g/10 min | 18–22 |
| Density | ISO 1183-1:2019 | g/cm³ | 0.900–0.910 |
| Tensile stress at yield | ISO 527-2:2012 | MPa | 24–28 |
| Tensile modulus | ISO 527-2:2012 | MPa | 1,100–1,400 |
| Charpy notched impact at 23 °C | ISO 179-1:2010 | kJ/m² | 6–10 |
| Heat deflection temperature at 0.45 MPa | ISO 75-2:2013 | °C | 80–100 |
| Mold shrinkage | ISO 294-4:2018 | % | 0.8–1.4 |
Because the material is semi-crystalline, cooling rate modifies final crystallinity, density, and post-mold shrinkage. Fast injection-molding cooling generally reduces the degree of crystallinity relative to slower extrusion-sheet cooling; this can lower short-term stiffness slightly while improving impact ductility. In edge-gated plaques, machine-direction shrinkage and transverse-direction shrinkage commonly differ by 0.1–0.3 percentage points, with the larger value measured transverse to flow. The dispersed elastomer phase disrupts spherulitic growth and reduces shrinkage anisotropy compared with a comparable melt-flow polypropylene homopolymer. Post-mold dimensional audits should therefore be performed after conditioning at 23 °C and 50% relative humidity for at least 24 h to separate reversible moisture effects from true mold shrinkage.
Compared with a 20 g/10 min polypropylene homopolymer, the impact-copolymer version provides higher notched Charpy impact strength at 23 °C and at −20 °C, but sacrifices tensile modulus and yield stress. The elastomer phase typically reduces tensile stress at yield by 15–25% relative to a comparable homopolymer, while increasing elongation at break from below 50% to above 100% in standard ISO 527-2:2012 tests. This trade-off directs the grade toward applications requiring low-temperature ductility and repeated-impact tolerance rather than maximum short-term static stiffness. Compared with a 20 g/10 min polypropylene random copolymer, the impact-copolymer morphology increases haze and lowers gloss at 2.0 mm plaque thickness, but improves low-temperature impact resistance and reduces the risk of brittle failure at stress concentrations. The optical difference is quantified by haze per ISO 14782:2021 and specular gloss per ISO 2813:2014. For thin-wall transparent packaging where clarity is the primary acceptance criterion, a random copolymer remains more appropriate; the impact copolymer is justified only where impact-toughness requirements override optical quality.
Compared with a 50 g/10 min high-flow impact-copolymer grade, the 20 g/10 min melt-flow class generally requires higher injection pressure and exhibits a wider processing window for moderate-to-thick sections. In thick-section moldings above 4.0 mm, the lower melt-flow grade reduces the incidence of drool from open nozzles and improves melt-cushion stability. In wall sections below 1.0 mm, a high-flow variant is likely to provide more reliable cavity filling. The choice between T20020 and a high-flow alternative should therefore be based on the limiting wall section, gate type, and clamp force available on the molding machine.
For injection molding, a general-purpose screw with an L/D ratio between 20:1 and 24:1 and a compression ratio of 2.5:1 to 3.0:1 is commonly used. Hot-runner systems should be equipped with open-pipe or valve-gate layouts sized for the expected shear rate; excessively small gate diameters may generate shear heating and cause local material degradation at high fill speeds. The processing window for melt temperature is typically 220–250 °C, with barrel zones profiled from 200 °C at the feed throat to 240 °C at the nozzle. Decompression, suck-back, and screw-back pressure settings should be adjusted to prevent air entrapment in the melt; back pressure between 50 bar and 80 bar is a practical starting range for uniform melt quality without excessive shear work.
At storage relative humidity above 60%, surface moisture adsorption can produce splay, silver streaks, or voids in thick sections. Pellets stored in opened bags or silos exposed to humid plant air should be desiccant-dried at 80 °C for 2–3 h before melt processing. Regrind addition up to 20 wt% with virgin pellets is generally manageable if the regrind is clean and dried; higher regrind fractions may shift melt viscosity and reduce impact retention. The grade is not recommended for continuous hot-water pressure-pipe service unless long-term hydrostatic strength has been validated to ISO 9080:2022 with the specific stabilizer package and fitting geometry.
In sheet extrusion, thermally stable extruder configurations with barrier screws and screen packs are preferred. Melt temperatures of 210–240 °C across the die are typical, with polished roll stacks set to 80–100 °C on the first cooling roll to control sheet crystallinity and surface quality. For subsequent thermoforming, sheet thicknesses from 1.2 mm to 4.0 mm can be processed by plug-assisted forming; the lower melt-flow class delivers improved sag resistance relative to high-flow grades, particularly on large-format tools with long heating cycles. Pre-dried extruded sheet is recommended before thermoforming when storage conditions exceed 60% relative humidity. Published data for this specific product configuration in deep-draw thermoforming is limited; tool-temperature mapping and wall-thickness surveys should be performed on initial production trials.
Untreated polypropylene copolymer surfaces have low surface energy, typically near 29–31 mN/m, which is insufficient for structural bonding, printing, or painting. Corona discharge treatment to 38–48 mN/m, gas-flame treatment, or low-pressure plasma treatment is required for adhesion. The treatment decay rate varies with antioxidant and slip-additive packages; in production, treated parts should move to bonding, printing, or lamination within 24–72 h unless treatment level is verified immediately before the downstream operation.
| Regulatory scope | Reference | Verification boundary |
|---|---|---|
| Polyolefin food-contact base resin | FDA 21 CFR 177.1520 | Final compound must meet extractive limits and end-use condition constraints; supplier clearance does not automatically cover downstream colorants or processing aids. |
| EU food-contact plastics | EU 10/2011 and amendments | Overall migration and specific migration limits depend on final article geometry, contact duration, and temperature. |
| Hazardous substances restriction | Directive 2011/65/EU as amended by (EU) 2015/863 | Declarable heavy metals and restricted phthalates require supplier documentation for each production lot. |
| REACH registration and SVHC communication | EC 1907/2006 | Article 33 communication obligations depend on SVHC content in supplied pellets, additives, and final articles. |
| Designation of polypropylene molding and extrusion materials | ISO 1873-1:2015 | Designation requires producer-assigned classification; the T20020 brand designation is supplier-defined and may not map directly to standardized block-copolymer designations. |
On injection-molding lines producing appliance structural brackets with hot-runner valve gates, the nozzle melt temperature is typically held at 230–240 °C and holding pressure is set to 60–80% of peak injection pressure until gate freeze. This practice reduces sink marks opposite reinforcing ribs and stabilizes part mass within ±0.5% across 8–12 h production runs. For ultrasonic-welded or vibration-welded assemblies made from this impact-copolymer class, joint strength is highly dependent on weld geometry, glass-fiber content, and surface condition. Published data for this specific product configuration in welded assemblies is limited; lap-shear and pressure-decay performance must be established on production-representative joints rather than extrapolated from bulk material data.