| HS Code | 429660 |
| Material | COSMOPLENE AR564 PP Copolymer |
| Type | Random Copolymer Polypropylene |
| Density | 0.9 g/cm³ |
| Melt Flow Rate | 8 g/10 min (230°C/2.16 kg) |
| Tensile Strength At Yield | 28 MPa |
| Flexural Modulus | 1000 MPa |
| Elongation At Break | 200% |
| Izod Impact Strength Notched 23 C | 6 kJ/m² |
| Heat Deflection Temperature 0 45 Mpa | 90°C |
| Vicat Softening Temperature | 130°C |
| Melting Point | 145°C |
| Rockwell Hardness | R80 |
As an accredited COSMOPLENE AR564 PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg multi-wall paper bags, COSMOPLENE AR564 PP Copolymer ensures safe handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL container loading of COSMOPLENE AR564 PP Copolymer ensures safe, secure transport with proper bracing, ventilation, and moisture protection. |
| Shipping | COSMOPLENE AR564 PP Copolymer ships as solid plastic pellets in clean, dry packaging such as sealed bags or bulk containers. Avoid exposure to moisture, heat, or contaminants. Properly label and secure loads. Transport via truck, rail, or sea under standard conditions; no special hazardous classification required. |
| Storage | Store COSMOPLENE AR564 PP Copolymer in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and open flames. Keep containers tightly sealed to prevent moisture contamination and foreign material ingress. Maintain room temperature conditions; avoid prolonged high temperatures. No special hazardous storage requirements apply, but follow standard polymer handling and good housekeeping practices. |
| Shelf Life | Shelf life is typically 12 months from delivery if stored in original packaging, away from heat, moisture, and direct sunlight. |
| Parameter | Extrusion blow moulding (1,000 L IBC) | Injection moulding (3 mm battery case) | Corrugated pipe extrusion (400 mm DN) |
|---|---|---|---|
| Melt temperature operating band | 190–215 °C (±2.5 °C at die) | 200–215 °C (±3 °C front zone) | 195–210 °C (±1.5 °C at adapter) |
| Shear rate threshold for sharkskin | 60 s⁻¹ at 205 °C | 18,000 s⁻¹ at gate | 80 s⁻¹ at mandrel tip |
| Pre-drying requirement (RH >60%) | 80 °C, 3 h, dew point −40 °C | 80 °C, 2 h (vacuum hopper optional) | Not required if vented screw used |
| Maximum allowable regrind ratio | 25% (virgin tail flash only) | 20% (avoid burn-spec shifts) | 35% (homogenised in-line scrap) |
| Critical property deviation at upper limit | Top-load drop 8% (ASTM D2659) | Notched Charpy drops 14% (ISO 179-1) | Ring stiffness variance >5% (ISO 9969) |
Competitive COSMOPLENE AR564 PP Copolymer prices that fit your budget—flexible terms and customized quotes for every order.
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The polypropylene impact copolymer designated COSMOPLENE AR564, manufactured by The Polyolefin Company (Singapore) Pte Ltd, is a nucleated, anti-gas fading-stabilized injection moulding grade engineered for applications demanding a balance of high melt fluidity, ambient and low-temperature impact toughness, and moderate stiffness. The nominal melt volume-flow rate (MVR) measured under 2.16 kg load at 230 °C is 10 cm³/10 min per ISO 1133‑1:2022, positioning the material at the upper end of the medium-flow spectrum and enabling consistent filling of thin-wall (0.8–1.5 mm) geometries with flow-length-to-wall-thickness ratios exceeding 250:1. Density at 23 °C is 0.90 g/cm³ (ISO 1183‑1:2019). The grade carries a proprietary nucleation package that accelerates crystallization kinetics, yielding a cycle-time reduction of approximately 10–15% relative to non-nucleated impact copolymers of equivalent impact strength, as well as a haze reduction in unpigmented parts attributable to a refined spherulite size distribution.
Uniaxial tensile testing of injection-moulded ISO 527‑2/1A specimens reveals a yield stress of 25 MPa and a nominal strain at break exceeding 50% at 23 °C when the testing speed is 50 mm/min. The secant flexural modulus, determined under ISO 178:2019 at 2 mm/min crosshead speed and a 64 mm support span, is 1200 MPa. This stiffness value places AR564 between typical high-impact reactor blends (modulus ~800–1000 MPa) and rigid homopolymer grades (modulus ~1500–1700 MPa), making it suitable for structural parts that do not require the full beam strength of a talc-filled compound but must survive drop-impact events. Notched Izod impact energy, following ISO 180/A with a Type A notch (r = 0.25 mm), measures 10 kJ/m² at 23 °C and 5 kJ/m² at −20 °C. The ductile-to-brittle transition temperature, interpolated from Charpy instrumented tests (ISO 179‑2), occurs at approximately −35 °C, below which fracture energy falls beneath 3 kJ/m² without rubber-phase modification beyond the standard ethylene–propylene dispersion. Published data for instrumented puncture performance at −40 °C on 2 mm plaques remain limited; field experience suggests that exposure below −35 °C under dynamic loading may trigger brittle crack initiation at knit-line weld zones, particularly when weld-line strength is compromised by insufficient melt temperature.
The selection of a polypropylene impact copolymer for injection-moulded automotive interior trims involves a trade-off between instrumented puncture resistance at sub-ambient temperatures and the dimensional stability required to prevent gap formation after 1000 hours of thermal cycling between −30 °C and 80 °C. Mould shrinkage of AR564, measured on 60 × 60 × 2 mm plaques per ISO 294‑4:2018, is typically 1.2–1.6% in the flow direction and 1.3–1.7% transverse to flow. This anisotropy, driven by shear-induced orientation of the polypropylene matrix chains during cavity filling, must be compensated in tool design by non-uniform shrinkage allowances, especially for components with an aspect ratio greater than 4:1. Post-moulding secondary crystallization, which proceeds for up to 72 hours at ambient conditions, can generate an additional linear contraction of 0.05–0.1%, sufficient to alter critical snap-fit engagement dimensions. Conditioning at 80 °C for 24 hours accelerates this physical ageing and stabilizes the part geometry prior to metrology validation.
Trials conducted on a 250‑tonne clamping-force all-electric injection moulding machine with a 25 mm diameter general-purpose polyolefin screw (L/D ratio 22:1) and a fully vented barrel established a melt-temperature setpoint range of 210–250 °C, with optimal balance of impact retention and flow length achieved at 230–240 °C barrel front zone. Residence time at melt temperature must not exceed 15 minutes in the presence of residual humidity exceeding 0.05%, as the anti-gas fading stabilization package—primary antioxidant plus secondary phosphite and thioester synergists—can be consumed by hydrolysis of the phosphite component, leading to a melt-flow-rate drift of more than 15%. Material pre-drying at 80 °C for 3–4 hours using a desiccant dryer with a dew point of −30 °C or lower is therefore mandatory whenever containers have been opened for longer than 30 minutes in ambient relative humidity above 60%. Mold surface temperature, controlled by a turbulent-flow water unit with ±2 °C uniformity across 12 zones, should be held between 15 °C and 40 °C. At melt temperatures below 210 °C, jetting and flow-mark defects become prominent at gate lands narrower than 1.0 mm, while above 260 °C the onset temperature of base-polymer unzipping accelerates, generating acrid smoke and discoloration from decomposition of the clarifier/nucleator system.
When cycle-time reduction demands nucleated crystallization and fast mold release, the AR564 grade’s isothermal crystallization half-time at 130 °C is approximately 0.8–1.2 seconds, as measured by differential scanning calorimetry under ISO 11357‑3:2018. This rapid solidification allows ejection without deformation at cooling times as low as 4–5 seconds for a 1.0 mm wall, provided that the cavity pressure transducer signals a drop below 30 MPa before mold opening. Premature ejection—before the frozen skin layer reaches a thickness of 0.3 mm—results in gate blush, a cosmetic blemish characterized by whitening and micro-porosity at the gate vestige, linked to cavitational flow of the still-molten core under tensile stress during part extraction. Counter-pressure holding profiles must be ramped from an initial 30–40 MPa packing pressure for 2–3 seconds down to 10–15 MPa over a total hold time of 6–8 seconds to balance sink-mark suppression against frozen-in stress that causes warpage after demoulding.
In multi-cavity hot-runner tools with valve-gate sequencing, the shear-thinning behaviour of AR564—expressed by a power-law index n of 0.35–0.42 between apparent shear rates of 10² s⁻¹ and 10⁴ s⁻¹ at 230 °C—reduces viscosity from a zero-shear plateau of approximately 1500 Pa·s to 60–80 Pa·s at the runner wall, facilitating balanced filling of eight cavities with a weight variation below 0.3% of shot mass. Differences in gate freeze-off time across the cavities, however, become magnified when the runner-system thermal balance is perturbed by a variation of ±5 °C in manifold temperature, leading to a shot-mass deviation that can exceed 1.0% and produce flash on the hottest cavity while short-shooting the coldest. This sensitivity advocates the use of shear-controlled runner balancing rather than reliance on natural flow balance alone.
| Property | Test Method | AR564 | Medium-Flow Impact Copolymer (MFR ~4) | PP Homopolymer (MFR ~11) |
|---|---|---|---|---|
| Melt flow rate (230 °C/2.16 kg) | ISO 1133‑1 | 10 g/10 min | 4 g/10 min | 11 g/10 min |
| Tensile yield stress | ISO 527‑2 | 25 MPa | 23 MPa | 34 MPa |
| Flexural modulus | ISO 178 | 1200 MPa | 1000 MPa | 1500 MPa |
| Notched Izod impact (23 °C) | ISO 180/A | 10 kJ/m² | 15 kJ/m² | 3 kJ/m² |
| Notched Izod impact (−20 °C) | ISO 180/A | 5 kJ/m² | 8 kJ/m² | 1.5 kJ/m² |
| Heat deflection temperature (0.45 MPa) | ISO 75‑2/B | 85 °C | 80 °C | 95 °C |
| Mould shrinkage (flow) | ISO 294‑4 | 1.2–1.6% | 1.3–1.7% | 1.4–1.8% |
The medium-flow comparator above represents a grade often selected for deep-draw parts requiring higher melt strength and superior sub-zero impact, but its spirality under identical injection pressure is 30% lower than AR564, limiting the attainable flow path length in complex geometries. The homopolymer provides a stiffness advantage of 25% in flexural modulus and a higher heat distortion temperature, yet the notched Izod impact energies, particularly at −20 °C, render it unsuitable for applications where ductile failure under incidental drop or crash events is non-negotiable. AR564 occupies a deliberate design position that supplies sufficient low-temperature toughness for automotive interior trims (pillar covers, door panels, center console substrates) and appliance housings while preserving enough stiffness to avoid the need for talc reinforcement—thus eliminating the compounding cost, density penalty, and machine wear associated with mineral-filled systems.
| Regulation / Standard | Scope | Status for AR564 |
|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymers in contact with dry food | Base resin compliant; specific application requires migration testing |
| EU No. 10/2011 | Plastic materials for food contact | Additive package within positive list; overall migration limit 10 mg/dm² |
| REACH (EC 1907/2006) | Registration, evaluation, authorization of chemicals | Polymer exempt; additives pre-registered |
| RoHS 2011/65/EU | Restriction of hazardous substances | Compliant—no PBBs, PBDEs, phthalates, or listed heavy metals intentionally added |
| ISO 3795 | Burning behaviour of interior materials (automotive) | Passes <100 mm/min burning rate in as-moulded state without flame retardant additives |
| VDA 278 | Thermal desorption analysis of automotive interior emissions | TVOC below 50 µg/g at 90 °C, Fog below 250 µg/g in gravimetric test |
The anti-gas fading stabilization system is specifically designed to retard the discoloration caused by phenolic antioxidants reacting with nitrogen oxide gases in closed-vehicle environments; accelerated testing under DIN 75201 (Method B, 48 hours at 60 °C in a NOx atmosphere) results in a Delta E of less than 2.0 units for natural-grade material. This performance is a differentiating feature compared to commodity impact copolymers employing conventional phenolic stabilizers, which often exhibit yellowness indices exceeding 15 after equivalent exposure, triggering warranty claims on visible interior components. The nucleating agent—a proprietary sorbitol-based clarifier—also contributes to a gloss value of 75 GU at 60° incident angle (ISO 2813:2014) on a polished mold surface, meeting the aesthetic requirements of OEM appearance panels without secondary lacquering. Where paint adhesion is necessary, flame treatment (equivalence ratio > 0.95) or corona discharge at 45–50 mN/m surface energy is required because the low surface energy of the polypropylene matrix (29–31 mN/m unmodified) prevents wetting by waterborne primers.
Compatibility with thermoplastic polyolefin elastomers (TPO) as impact modifiers in a dry-blend setting has been demonstrated on twin-screw extrusion lines with downstream water-ring pelletizing; however, the addition of more than 5 wt% of an EPR or EPDM masterbatch raises the elongation viscosity sufficiently to cause pellet-cutting smearing unless the die-face temperature is increased by 15–20 °C. Moreover, blending with calcium stearate at levels above 0.15 wt% can plate-out on mold surfaces within the first 500 shots, creating maintenance intervals that interfere with high-volume production. Avoid combination with copper-based heat stabilizers or amine-based antioxidants (e.g., aromatic amine anti-degradants) because amine residues interact with the clarifier, causing loss of nucleation efficiency and haziness accompanied by an increase in mould shrinkage anisotropy of up to 0.3% absolute.