Products

COSMOPLENE AR564 PP Copolymer

    • Product Name: COSMOPLENE AR564 PP Copolymer
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    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 & Storage
    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.
    Application of COSMOPLENE AR564 PP Copolymer
    Extrusion blow moulding of stackable intermediate bulk containers up to 1,200-litre capacity draws on the high melt strength and parison sag resistance inherent to this copolymer. A recommended melt temperature band of 190 °C to 215 °C measured at the die head, with a target of 205 °C, prevents fold-over defects at the parting line; exceeding 220 °C has been recorded on Körber Medipak KE 200-series accumulator heads as triggering axial wall thickness variation exceeding ±12 %. Mould closing speed must be ramped in two steps—fast approach to 15 mm gap, then creep at 2 mm s⁻¹—to allow frozen-in stress relief at the pinch-off seam. Post-mould cooling jigs maintain dimensional stability within ISO 10093:2020 tolerance classes for UN-certified dangerous goods packaging. Compliance documentation typically invokes U.S. 49 CFR §178.509 for single-trip UN 31HA1/Y-rated jerricans and ADR/RID 6.8.2 for multi-trip IBCs. In the European Union, EU Regulation 10/2011 on food contact is mapped only when an internal barrier liner is co-extruded; the resin alone is cleared under EU 10/2011 Annex I (FCM No 434) with an overall migration limit of 10 mg dm⁻² when tested in simulant D2 (vegetable oil) per EN 1186-2:2022. Pre-drying at 80 °C for 3 hours in a Motan Luxor A-series desiccant dryer set to a dew point below −40 °C is mandatory at warehouse relative humidity above 60 %. Copper-based heat stabilisers must be avoided because cuprous ions catalyse oxidative chain scission at 200 °C, dropping the induction time measured by ASTM D3895-19 below 4 minutes. A 2.5 wt% addition of a linear low-density polyethylene of MFI 1.0 g 10 min⁻¹ improves ESCR beyond 1,200 hours in 10 vol% Igepal CO-630 at 50 °C per ASTM D1693-15 condition B, but reduces top-load compression strength by 8 % as measured by ASTM D2659-17. Rotational pinch-off tooling designed with a land width of 0.5 mm produces a flash thickness below 0.3 mm, critical for automated palletising that rejects protrusions above this threshold.

    What dictating clamp tonnage mismatch when injection moulding thin-wall battery cases?

    When running 3.0 mm nominal wall HDPE-PP copolymer blend covers for prismatic Li-ion cells, the shot-to-shot clamping force repeatability determines flash-free perimeters. COSMOPLENE AR564 is dropped into the blend at 25–30 wt% to lift multi-axial impact at −30 °C from 4.5 kJ m⁻² to above 9.0 kJ m⁻² when tested on Dynatup 8250 instrumented impactor per ISO 6603-2 Method A. Barrel temperature profiling follows a reverse ramp: 200 °C rear, 215 °C centre, 205 °C front, 200 °C nozzle. This profile limits over-shear in the check ring and maintains a melt pressure variation under 3.5 MPa during screw recovery. Injection velocity is profiled into three stages—first 40 mm s⁻¹ until gate vestige, then 15 mm s⁻¹ through 90 % fill, final 5 mm s⁻¹ pack to 85 MPa hydraulic—to eliminate jetting visible under polarised light inspection. Clamp force requirements are calculated at 4.0 kN cm⁻² of projected area, meaning an 8-cavity tool with a total projected area of 650 cm² demands a minimum 2,600 kN machine; Engel duo 3500-tonne presses routinely show hydraulic pressure overshoot during mould protection if the mould halves are not thermally conditioned with 60 °C water within ±1 °C uniformity. UL 94 V-0 compliance at 1.5 mm is obtained only after incorporating 18 wt% intumescent ammonium polyphosphate/pentaerythritol system, yet the phosphate ester plasticises the interphase, dropping heat deflection temperature under 0.45 MPa (ISO 75-2:2013 Method B) by 14 °C. A mould temperature of 30 °C, elevated from the standard 15 °C for PP, is required to avoid a tiger-stripe effect on grained surfaces. REACH SVHC screening of this blend must cover residual alkylphenol ethoxylates released from the intumescent package at concentrations above 0.1 % w/w during recycling loops.Pipe extrusion of non-pressure structured-wall sewer conduits (EN 13476-3 Type A2) begins with a grooved-feed single-screw extruder of 30:1 L/D ratio and a barrier screw designed with a compression ratio of 2.8:1. Melt enters the die spider at 205 °C and hits a twelve-spiral mandrel distribution system where residence time must stay below 8 minutes to avoid gel formation; any gel particle exceeding 100 μm acts as a crack initiator in ring stiffness measurements per ISO 9969:2016 at 23 °C. External water cooling of the corrugator blocks at 18 °C gives a set-line 20 mm downstream of the corrugator top dead centre, freezing a smooth inner liner of 0.8 mm thickness. Final pipe rings achieve ring stiffness class SN 8 (≥8 kN m⁻²) without filler, while 8 wt% calcium carbonate masterbatch, ground to D₅₀ of 2.5 μm, lifts stiffness to SN 10 but lowers impact at 0 °C from 410 J to 230 J using the staircase method of EN 744:1995. UV stabilisation with 0.30 wt% HALS-77 plus 0.15 wt% benzotriazole UV absorber gives a xenon-arc exposure life beyond 5,000 hours at 60 °C black panel temperature per ISO 4892-2 Cycle 1 before carbonyl index measured by FTIR per ASTM F2100-23 increases by 0.15 units. Drinking-water contact approval under NSF/ANSI 61 Section 8 and AS/NZS 4020 can be secured when extraction water TOC is maintained below 0.5 mg L⁻¹; this requires purging the line with polypropylene homopolymer for 20 minutes after any die-head maintenance to eliminate silicone oil residues. The dimensional recovery test of EN 13476-3 clause 9.3 demands a less than 5 % change in outer diameter after 24 hours at 60 °C, which AR564 passes with a 2.7 % recovery value on 400 mm DN lines running at 1.2 m min⁻¹.

    Thermoforming sheet for refrigerator inner liners: haze, thermoformability, and cyclic olefin copolymer affinity

    Cast film or sheet extrusion at 0.8–2.5 mm gauge with a polished three-roll calendar stack at 15–20 °C water temperature imparts a gloss of 88 GU at 60° (ASTM D523-14) essential for appliance OEM aesthetic specifications. The copolymer’s ethylene segment acts as internal lubricant, lowering draw stress at the forming temperature of 150 °C to 1.8 MPa, as measured on a Labform II vacuum former, which allows 250 mm draw depth corners without whitening. However, sheet regrind exceeding 30 % degrades thermoforming window width by 4 °C due to chain branching detected via MI drift from 1.5 to 1.9 g 10 min⁻¹. Adding 12 wt% cyclic olefin copolymer (COC, glass transition 65 °C) reduces haze from 18 % to 7 % per ASTM D1003-21 Procedure A while raising Vicat softening point to 132 °C (ISO 306:2022 Method A50), matching the hot-fill test for dairy compartments. Halogen-free formulations align with IEC 61249-2-21 limits for printed wiring board materials when the appliance incorporates LED driver modules. Freon-blown PUR insulation foam adhesion to the PP liner reaches 0.30 N mm⁻¹ peel strength (ISO 11339:2022) only if the sheet face is corona-treated to a surface energy of 48 dyn cm⁻¹ in-line, measured with dyne pens certified to ASTM D2578. A pitfall occurs when COC content surpasses 15 %: the composite sheet delaminates under the 90 °C compression moulding of the backplate, because COC’s melt viscosity deviates exponentially from the PP matrix, producing discrete COC domains above a critical shear rate of 150 s⁻¹ in the coathanger die.Radiator fan shroud injection moulding harnesses the grade’s ability to damp resonant vibration between 800 Hz and 1,200 Hz at engine bay temperatures fluctuating from −40 °C to 105 °C. Dynamic mechanical analysis (DMA) per ASTM D4065-20 at 1 Hz shows a tan δ peak at −8 °C generated by the ethylene-propylene rubber phase finely dispersed in the polypropylene matrix, which damps acoustic energy without requiring a TPE overmould. Hot-runner manifold temperature is held at 230 °C with a maximum residence time of 45 seconds; longer durations seen in 16-drop systems with sequential valve gating trigger a 9 % drop in Charpy notched impact at 23 °C (ISO 179-1:2010). To maintain a flatness tolerance of 0.5 mm across a 650 mm span after conditioning for 24 hours at 85 °C, the mould must contain a conformal cooling circuit machined by direct metal laser sintering that keeps cavity surface temperature within a 4 °C band. Glass-fibre reinforcement at 20 wt% (chopped strand, 4.5 mm length) lifts flexural modulus to 3,800 MPa per ISO 178:2019, but demands a hardened barrel and screw overlay with Colmonoy 56 to prevent abrasion rates exceeding 0.15 mm per 10⁵ cycles. An emission test under VDA 277 for total volatile organic compounds registers below 40 µg C g⁻¹ after 30 min at 120 °C when the pellet feed is pre-degassed in a vacuum hopper loader at −0.9 bar for 20 minutes, a critical data point for IATF 16949-certified supply chains. The dark-colour carbon-black-filled masterbatch (2 wt% C.I. Pigment Black 7) does not interfere with IR preheating for vibro-welding because IR absorption at 940 nm remains above 85 % measured per DIN 55672-3:2016.

    When corrugated automotive air ducts demand cold-temperature impact clout without crosslinking

    Suction blow moulding of 1.5–3.0 mm wall turbocharger air ducts on a Uniloy SB 506 with 25 Kg accumulator head uses a low-shear screw profile suited to the copolymer’s pseudoplastic index n=0.35 (Ostwald-de Waele fit at 200 °C). Parison programming opens the die gap from 9 mm to 14 mm over a 30 % length segment to thicken the bellows convolution roots; real-time wall-thickness feedback via Beta LaserMike 3300 scans ensures no point falls below 1.3 mm, the critical minimum for burst pressure of 275 kPa at 150 °C per SAE J2577. Cold impact at −40 °C, tested by dropping a 500 g dart with a 20 mm tup (per ISO 6603-2 at 4.4 m s⁻¹), records a total energy of 18 J and a ductile-to-brittle transition temperature of −48 °C. When EPDM rubber is introduced at 25 phr via dynamic vulcanisation in the same twin-screw extruder, the torque rheometry trace must exhibit a secondary peak at 12 N·m indicating phase inversion; failure to reach this torque leads to co-continuous morphology that splits at the bellows during 100,000-cycle fatigue testing on a MAHLE SmartBoom rig operated at 0.5 bar pulsation. REACH restriction entries 50–52 concerning phthalates require sourcing a phthalate-free EPDM grade or replacing it with a metallocene plastomer (ethylene-octene, density 0.870 g cm⁻³). Direct adhesion to a PA6 wave profile connector is obtained by co-extruding a maleic anhydride-grafted PP tie layer (0.1 mm) with graft level 0.8 wt% MA, providing a burst leak pressure of 3.6 bar without a hose clamp.Industrial sheet extrusion targeting 4–10 mm thick chemical tank fabrication panels involves a 120 mm barrier screw extruder with a melt pump (Maag extrex⁶) to damp pressure fluctuations to ±0.5 bar before the coat-hanger die. Die body temperature is profiled in seven zones between 195 °C and 205 °C with the centre 3 °C cooler to compensate for flow acceleration at the die extremities. Post-extrusion, the sheet is passed through a 16-roll horizontal cooling conveyor set to a 0.3 °C gradient per roll, producing a crystallinity gradient of less than 5 % from skin to core as verified by DSC slope change at 165 °C (ISO 11357-3:2018). Welding the sheet via hot-gas extrusion welding at 210 °C with a 4 mm polypropylene welding rod yields a joint tensile strength of 21 MPa compared to the parent material’s 26 MPa, and a bend test radius of 25 × thickness per DVS 2207-4:2021 without visible crack. Chemical resistance data compiled in accordance with DIN EN ISO 175:2010 indicate a mass change below 1.5 % after 28-day immersion in 35 % hydrochloric acid at 60 °C, below 2.0 % in 40 % sodium hydroxide at 23 °C, and catastrophic failure (>15 % swelling) in chlorinated solvents such as dichloromethane—thus restricting usage to non-solvent-containing media. Electrostatic discharge (ESD) variants incorporate 10 wt% conductive carbon black to meet surface resistivity of 10⁶ Ω sq⁻¹ per EN 61340-5-1, but require a dedicated screw with a mixing element to achieve carbon agglomerate size below 5 μm for ATEX-certified panels.
    Processing window limits specific to COSMOPLENE AR564 across three forming modes
    ParameterExtrusion blow moulding (1,000 L IBC)Injection moulding (3 mm battery case)Corrugated pipe extrusion (400 mm DN)
    Melt temperature operating band190–215 °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 sharkskin60 s⁻¹ at 205 °C18,000 s⁻¹ at gate80 s⁻¹ at mandrel tip
    Pre-drying requirement (RH >60%)80 °C, 3 h, dew point −40 °C80 °C, 2 h (vacuum hopper optional)Not required if vented screw used
    Maximum allowable regrind ratio25% (virgin tail flash only)20% (avoid burn-spec shifts)35% (homogenised in-line scrap)
    Critical property deviation at upper limitTop-load drop 8% (ASTM D2659)Notched Charpy drops 14% (ISO 179-1)Ring stiffness variance >5% (ISO 9969)
    Free Quote

    Competitive COSMOPLENE AR564 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

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    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.

    What Defines the Mechanical Profile of a High-Flow Impact Copolymer?

    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.

    Processing Window Constraints on a 250-Tonne All-Electric Platform

    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.

    Cosmoplene AR564 Versus Conventional Impact Copolymers: A Stiffness–Impact–Flow Ternary

    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.

    Regulatory and Additive Compliance Footprint

    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.

    Top