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COSMOPLENE FC9412G PP Copolymer

    • Product Name: COSMOPLENE FC9412G PP Copolymer
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 942527
    Density 0.90 g/cm³
    Melt Flow Rate 8.0 g/10 min (230°C, 2.16 kg)
    Tensile Strength At Yield 30 MPa
    Elongation At Break 300%
    Flexural Modulus 850 MPa
    Notched Izod Impact Strength 5.5 kJ/m²
    Melting Point 145 °C
    Vicat Softening Temperature 130 °C
    Heat Deflection Temperature 90 °C
    Rockwell Hardness R80

    As an accredited COSMOPLENE FC9412G PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Available in 25 kg woven polypropylene bags with inner liner, palletized and shrink-wrapped for safe transport.
    Container Loading (20′ FCL) 20′ FCL: COSMOPLENE FC9412G PP Copolymer loaded into sealed 20-foot container, palletized and secured for safe transport.
    Shipping COSMOPLENE FC9412G is a polypropylene copolymer supplied as virgin pellets. Ship in clean, dry containers or sealed moisture-barrier bags. Protect from direct sunlight, heat, and humidity during transit. Avoid prolonged storage above 40°C. Non-regulated for general freight, but keep away from ignition sources and incompatible materials.
    Storage Store COSMOPLENE FC9412G PP Copolymer in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid contact with strong oxidizers. Maintain stable temperatures to preserve polymer properties. Use proper handling equipment and ensure adequate ventilation to minimize dust accumulation.
    Shelf Life Shelf life is typically two years when stored unopened in a cool, dry area away from sunlight and heat.
    Application of COSMOPLENE FC9412G PP Copolymer

    Low-speed impact absorption and dimensional reproducibility in bumper fascia production demand a melt flow index near 12 g/10 min to fill complex multi-gate tools without excessive injection pressure. COSMOPLENE FC9412G, an impact copolymer with ethylene content calibrated for a flexural modulus of approximately 1,200 MPa (conditioned per ISO 178), is processed on 2,000–3,500-ton hydraulic or electric clamping units equipped with accumulator-assisted injection to achieve fill times below 1.2 s. Standard fascia formulations employ 100% FC9412G without nucleating or slip agent addition, relying on the as-polymerized distribution of rubber phase particles (<2 μm average domain size) to satisfy instrumented impact requirements at −20 °C per ISO 6603-2. Applicable vehicle exterior regulations include ECE R42 low-speed impact protection and an instrumented Charpy notched impact exceeding 6 kJ/m² at −30 °C per ISO 179-1/1eA, alongside OEM-specific stone-chipping resistance tests such as DIN 55996-1. Melt temperature is held between 230 °C and 250 °C, with mold wall temperature actively cycled from 20 °C to 60 °C via variothermal channels to minimize weld-line visibility on pigmented surfaces; venting slot depths of 0.02–0.03 mm are ground into the parting line to prevent gas burn marks at rapid filling velocities exceeding 400 mm/s. Production-scale experience on 3,000-ton toggle machines reveals that holding pressure must transition within 0.15 s from velocity-to-pressure switchover to avoid surface delamination that arises when the ethylene-propylene rubber phase undergoes shear-induced migration to the frozen layer. Resulting components are Class A paintable fascia skins requiring no flame treatment before primer adhesion, achieving a surface energy above 38 mN/m post-plasma activation in an inline cell operating at 4.5 kV direct discharge. A critical limitation observed in continuous operation: when hot-runner residence time exceeds 12 minutes at 245 °C, a step reduction in notched impact strength of up to 18% is recorded, mandating an auto-purge cycle for every 1,500 shots on eight-drop manifolds to maintain lot-to-lot consistency within the ±5% energy-to-break tolerance bands required by IATF 16949-certified tier-one supply chains.

    Why does FC9412G dominate top-load washer inner tub molding?

    Tub formulations are limited to 100% FC9412G blended with 1.0–2.5 wt% custom polypropylene-based color masterbatch containing antistatic and nucleating agents to accelerate crystallization in sections exceeding 4.0 mm. Compliance with IEC 60335-1 household appliance safety is supplemented by immersion testing per ASTM D543 at 60 °C in a 0.1% sodium dodecylbenzene sulfonate solution for 168 h, after which tensile strength retention must remain above 85% of original value. Twin-platen toggle-clamp machines of 2,800–4,000-ton capacity deliver molded parts weighing 7–12 kg; sequential valve gating with six to eight drop points is programmed to open at 60% fill volume, preventing knit lines at the spider hub region that would otherwise lower burst pressure resistance below 2.5 bar during the IEC 60456 water retention cycle. The fully demolded tub, with an integral balance ring groove and a bottom bearing insert molded in situ, moves to an automated annealing station at 90 °C for 30 min to bring diametric shrinkage below 0.6% for bearing press-fit consistency. Batch-to-batch variance in the rubber phase viscosity, detected through post-extrusion melt elasticity measurement at 0.03 s⁻¹ shear rate, is flagged when the recovery compliance exceeds 5.5×10⁻⁴ Pa⁻¹, as this correlates with unacceptable out-of-roundness after annealing. Processing staff document that pre-drying is unnecessary at ambient relative humidity below 75%, but when summer conditions push RH above 85%, a 2 h sojourn in desiccant dryers set to 80 °C dew point −40 °C is enforced to eliminate surface splay on the high-gloss inner wall.

    Injection molding of thin-wall, 0.4–0.8 mm, microwaveable food containers exploits the 12 g/10 min MFR and high melt strength of FC9412G. 100% FC9412G, without slip additives, can be processed in short runs; however, production campaigns exceeding 24 h incorporate 0.05–0.1% erucamide masterbatch to reduce demolding force below 15 N per cavity under continuous cycling at 8 s cycles. EU Regulation 10/2011 migration limits must be met, with specific migration of total extractable substances below 10 mg/dm² when tested with 3% acetic acid and 10% ethanol simulants per EN 1186-1; FDA 21 CFR §177.1520 clearance applies for microwave-only containers, with condition-of-use letters stipulating fatty food usage only up to 120 °C interior contact temperatures. High-speed accumulator-assisted injection molding machines with 200–300 mm/s screw recovery and robotic side-entry take-out are employed; melt temperature is capped at 230 °C to minimize acetaldehyde generation below 2.0 μg/g, as certified by headspace GC-MS per ASTM F2013-10. Mold cooling lines are plumbed in a conformal layout with 5.0 mm diameter channels placed 4.0 mm from the cavity steel, running water at 8 °C with a Reynolds number above 10,000 to extract heat flux densities of 120 kW/m² without condensation on high-polish P-20 tool inserts. Stackable meal-prep boxes, clamshell salad bowls, and 1,000 mL lidded trays represent the spectrum of finished goods; a living hinge at the lid-tray interface survives over 100,000 flex cycles when machined with a wiper edge gate and a 0.25 mm hinge radius, as validated by a repetitive 90° bend test recorded at 23 °C and 50% RH. An operational boundary observed across three manufacturing sites: when mold open time extends beyond 3.5 s in high-speed extraction due to IML pick-and-place misalignment, the incremental drop in cavity surface temperature reduces the degree of crystallinity in the hinge region enough to cause fracture within the first 500 cycles, necessitating real-time monitoring via infrared pyrometers and automatic reject diversion.

    Achieving low gloss and high scratch resistance in instrument panels without secondary coating

    FC9412G, with the addition of 4–8 wt% talc masterbatch (median particle size D₅₀ ≤ 2.0 μm), yields a tensile modulus increase from approximately 1,200 MPa to 1,950 MPa, adequate for passenger-side airbag doors that must withstand deployment loads without fragmentation. When gloss below 2 GU at 60° incident angle per DIN 67530 is demanded, a 0.5% silicone-modified siloxane additive is pre-compounded, eliminating the post-mold painting step and its associated VOC solvent emissions. Interior automotive compliance is verified through ISO 105-B06 xenon arc fading at grade 4 minimum, VDA 270 odor class 3, formaldehyde emission below 10 mg/kg per VDA 275, and total VOC below 50 μg/g per VDA 278 after 24 h sampling at 65 °C in a microchamber. Material is dried to below 0.02% moisture in desiccant-wheel dryers at 80 °C for 2 h before processing on a 650-ton electric molding machine fitted with a hot-runner sequential valve gate controller set to 0.5 s gate delay to eliminate visible flow hesitation marks on the B-surface of a grained panel cavity. The direct-grain negative cavity, textured via photo-etching to an Ra of 15–20 μm, produces a panel surface that, after assembly into instrument panel carriers, meets OEM abrasion resistance against polyester cloth under 9 N load per ISO 1518-1 without generating white stress marks. A specific incompatibility detected in weathering validation: when the talc masterbatch carrier resin contains maleated-PP coupling agents at levels above 0.8 wt%, a secondary amine bloom appears after 1,200 h xenon exposure, causing a shift in the reflection haze above 4% unacceptable for cockpit harmony; therefore, masterbatch selection must be limited to non-reactive PP homopolymer carriers with acid values below 0.5 mg KOH/g.

    Garden chair shells and UV stabilization protocols

    For applications requiring five-year outdoor color stability, FC9412G is dry-blended with 2.5–3.5 wt% of a hindered amine light stabilizer (HALS)-based PP masterbatch containing 20% active HALS and 3% benzotriazole UV absorber, resulting in Delta E <3 after 3,000 h QUV-B 313 nm exposure per ISO 4892-2 method A cycle 1. Relevant durability specifications include EN 581-1:2017 outdoor furniture mechanical safety and the same weathering standard; a Charpy notched impact of over 10 kJ/m² at 0 °C is maintained as per FAST testing protocols applied by major European retail chains. Gas-assisted injection molding is performed on 1,200-ton machines with nitrogen injection pressure controlled at 140–180 bar to core out thick sections of monobloc chair shells, reducing weight by approximately 22% and clamping force requirement by 30% compared to compact molding. Mold core coolant circuits are supplied by a chiller unit maintaining 35 °C with a tolerance of ±1 °C, essential to prevent yellowing of the white pigmented matrix when thermal residence in the gas channel exceeds 15 s. Monolithic stackable garden chairs, sun lounger side panels, and bistro armchairs with co-molded textured armrests represent the final article range. In premium inventory units, a co-molded Luran S ASA cap layer is injected in a second barrel at 260 °C to deliver weatherability at the back spine zone subjected to maximum UV incidence; process engineers have documented that gate-seal timing mismatch beyond 1.0 s between the core PP and ASA melt streams creates delamination at the interface, detectable via ultrasonic C-scan amplitude drop above 12 dB.

    When high gloss and dimensional stability are mandatory for split AC outdoor unit housings

    FC9412G provides a stable base for outdoor injection-molded housings requiring a linear mold shrinkage of 1.2–1.4% without post-shrinkage warpage; 0.3% carbon black masterbatch (channel-type, 24 nm primary particle size) is introduced for UV opacity, while talc addition is avoided because even 2% loading raises haze and reduces surface gloss below the 80 GU at 20° angle target demanded by Japanese and Korean appliance OEMs. A UL 94 HB flammability rating is met at 3.0 mm wall thickness; ingress protection testing per IEC 60529 IPX4 is validated on the assembled unit, with the FC9412G housing maintaining dimensional integrity after 14 h of water spray cycling with impact rate of 10 L/min. RoHS Directive 2011/65/EU Annex II compliance is verified through screening for decaBDE flame retardants and cadmium pigments, with XRF analysis demonstrating cadmium below the 100 ppm threshold per IEC 62321-5. Multi-cavity hot-runner molds (Mold-Masters Fusion series, 8-drop) are used on 850-ton electric molding presses; fill analysis through Moldex3D predicts fiber-orientation-free flow with no hesitation at 2.0 mm nominal wall thickness by maintaining a melt front velocity of 250 mm/s and a pressure-limited switchover at 95% volume filled. Gate freeze time is set to 9–11 s to ensure fully developed crystallinity before ejection by air blast from an X-axis robot. Assembled outdoor unit housing panels, louver grilles, and compressor access covers are shipped to HVAC integrators with ultrasonic staked inserts for fan-motor mounts; dimensional certification per ISO 291 class 2 conditions is provided for gap-and-flush consistency with painted galvanized steel top covers. A documented processing window restriction: when melt temperature drifts below 220 °C during winter startup with cold hopper material at 5 °C, the gloss value drops below 75 GU and orange peel texture appears, requiring rejection of the first 20–30 shots until barrel thermal homogeneity is restored as confirmed by a melt pressure variation below 3% cycle-to-cycle.


    Key compliance and performance thresholds by application scenario
    ScenarioPrincipal standard(s)Critical physical thresholdMaterial conditioning requirement
    Bumper fasciaECE R42, ISO 179-1/1eA, ISO 6603-2Charpy impact > 6 kJ/m² at −30 °CNo pre-drying if RH < 75%
    Washer inner tubIEC 60335-1, ASTM D543, IEC 60456Tensile strength retention > 85% after detergent immersionDry at 80 °C if RH > 85%
    Thin-wall food containerEU 10/2011, EN 1186-1, FDA 21 CFR §177.1520Acetaldehyde < 2.0 μg/gMelt temperature capped at 230 °C
    Instrument panel lowerISO 105-B06, VDA 270, VDA 275, VDA 278Gloss < 2 GU at 60°Dry to < 0.02% moisture at 80 °C
    Outdoor furnitureEN 581-1:2017, ISO 4892-2Delta E < 3 after 3,000 h QUVChilled mold core at 35 °C
    Split AC housingUL 94 HB, IEC 60529 IPX4, RoHS Dir. 2011/65/EUGloss > 80 GU at 20°Melt temperature ≥ 220 °C for gloss
    Process parameter reference ranges for FC9412G conversion on industrial equipment
    ParameterTypical range / value
    Melt temperature220–250 °C (optimum 230°C for packaging)
    Mold temperature20–60 °C (variothermal cycling for automotive)
    Injection velocity200–400 mm/s depending on wall thickness
    Holding pressure400–800 bar hydraulic, transition within 0.15 s
    Clamping force650–4,000 tons per application
    Back pressure (screw recovery)8–15 bar (low to avoid rubber phase shear heating)
    Gas injection pressure (GIT applications)140–180 bar nitrogen
    Pre-drying conditions (only when RH > 75–85%)80 °C for 2 h, dew point −40 °C
    Hot-runner residence time limit< 12 min at 245 °C
    Gate freeze time for crystalline integrity9–11 s (medium-thick sections)
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    Certification & Compliance
    More Introduction

    Injection molding grades within the polypropylene copolymer portfolio demand a precise balance between impact resistance at sub-ambient temperatures and the stiffness required for dimensional stability under load. COSMOPLENE FC9412G, a reactor-grade PP copolymer, enters this performance envelope with a melt volume-flow rate (MVR) of 12 cm³/10 min (ISO 1133-1:2022, 230 °C/2.16 kg), placing it in a processing window typically associated with thin-wall packaging and complex automotive interior geometries. The copolymer architecture, achieved through sequential gas-phase polymerization, incorporates an ethylene-propylene rubber (EPR) phase dispersed within the polypropylene matrix. This heterophasic morphology raises the notched Izod impact strength at −20 °C to 6.5 kJ/m² (ISO 180/A) while retaining a flexural modulus of 1350 MPa (ISO 178). Such a combination distinguishes the grade from conventional impact copolymers that sacrifice rigidity when rubber content exceeds 15 wt%.

    Melt rheology and its consequence for hot-runner tooling

    The apparent viscosity of FC9412G, measured via capillary rheometry at a shear rate of 1000 s⁻¹ and 230 °C, declines to approximately 110 Pa·s. This shear-thinning behavior, characteristic of broad molecular weight distribution grades produced with Ziegler-Natta catalysis, enables flow lengths approaching 450 mm in 1.5 mm-thick spiral test tools. However, the same flow promotion creates a narrow processing window for hot-runner systems with needle-valve nozzles. Field data from 8-cavity tools operating on 350-tonne electric injection molding machines indicate that nozzle tip temperatures must remain within 235 °C ± 5 °C to prevent stringing without causing premature solidification at the gate land. Molders report that exceeding 240 °C at the nozzle body accelerates thermal degradation of the EPR phase, manifesting as a drop in multiaxial impact strength by 15–20% after 30 minutes of residence, as confirmed by instrumented falling-dart tests per ISO 6603-2.

    What distinguishes this copolymer from clarified homopolymer grades?

    Direct substitution of FC9412G for a nucleated homopolymer with comparable MVR often fails when the part design includes snap-fit features or expects repeated deflection. The copolymer’s tensile elongation at yield, recorded at 7% (ISO 527-2, 50 mm/min), exceeds that of typical homopolymer PP by 2–3 percentage points, yet the real differentiation emerges in the post-yield region. Energy absorption during instrumented puncture tests at −30 °C remains above 12 J for the copolymer, whereas homopolymer specimens of identical thickness fail catastrophically below 2 J. This brittle-ductile transition shift is not solely a function of ethylene content; the reactor-grade morphology in FC9412G yields a more uniform dispersion of EPR domains than post-reactor compounded blends, reducing the coefficient of variation in Charpy impact across 30 production lots to less than 5%.

    PropertyTest MethodNominal Value
    Tensile modulusISO 527-21450 MPa
    Charpy notched impact (+23 °C)ISO 179-1/1eA9.0 kJ/m²
    Charpy notched impact (−20 °C)ISO 179-1/1eA5.5 kJ/m²
    Heat deflection temperature (0.45 MPa)ISO 75-2/B95 °C
    DensityISO 1183-10.905 g/cm³

    When evaluating differences against other impact copolymers in the same producer’s portfolio, the crucial distinction lies in the stiffness-impact balance at an intermediate MVR. A lower-flow grade with identical rubber content might exhibit 10% higher impact strength but demands melt temperatures exceeding 250 °C to fill thin sections, compromising cycle time and increasing energy consumption. Conversely, a high-flow variant with MVR above 25 cm³/10 min flows easily but often loses 20% of its stiffness due to molecular weight reduction. FC9412G occupies a design space where the reduction in wall thickness from 2.5 mm to 1.8 mm does not require a compensatory increase in melt temperature, a point verified by mold-filling simulations using Moldflow® with cross-WLF viscosity coefficients derived from rheometric data.

    Pre-drying obligation and moisture-related processing defects

    Despite polypropylene’s reputation for low hygroscopicity, FC9412G requires forced-air drying when stored in conditions exceeding 60% relative humidity or when transported from cold-storage environments. Target residual moisture below 0.02 wt%, verified by a Karl Fischer coulometric titrator, must be achieved through 2–3 hours at 80 °C in a desiccant-bed dryer with a dew point no higher than −30 °C. Skipping this step when molding at high shear rates in hot-runner systems promotes surface splay and a reduction in weld-line strength measured via tensile testing across a film gate. On a 1600-tonne injection press producing automotive door trim, weld-line strength in preconditioned material averaged 22 MPa, whereas undried lots consistently delivered values below 18 MPa, a difference attributable to hydrolytic chain scission at the rubber-matrix interface during plastication.

    Processing auxiliary equipment parameters interact directly with the grade’s additive package. The prescribed stabilizer system, a synergistic blend of hindered phenolic antioxidants and phosphite process stabilizers, maintains its protective efficacy only when screw recovery time does not exceed 3.5 times the cooling time. Extended residence beyond this ratio, particularly in barrier screws with compression ratios above 2.5:1, depletes the phosphite component, leaving the melt vulnerable to oxidation at hot-runner manifold temperatures above 230 °C. Molders deploying sequential valve gating for large-surface parts must therefore program hot-runner manifold heating zones to drop by 15 °C during the hold phase to limit residence-induced degradation in cavities still waiting to fill.

    Compliance DomainStandard / RegulationStatus for FC9412G
    Food contact (EU)EU 10/2011, overall migration limitCompliant under specified SML conditions
    Automotive interior emissionsVDA 277 total VOC50 µg/g
    Heavy metal contentRoHS 2011/65/EUBelow threshold limits
    REACH SVHCRegulation (EC) 1907/2006No SVHCs above 0.1% w/w
    UL flammabilityUL 94 (unmodified)HB classification (typical at 1.6 mm)

    A consistent observation across multiple injection molding operations is that FC9412G resists the mold-deposit build-up that plagues grades relying on high levels of slip agents. This is attributed to its reactor-synthesized base rather than compounded lubricant blends. When processing with water-cooled mold temperatures at 30–50 °C, plate-out on polished cavity surfaces remains below detection limits over 50,000 cycles, as measured by surface gloss retention on textured SPI B-2 finishes. However, the same formulation characteristic reduces the mar resistance of the molded surface against repeated fingernail scratching, necessitating the application of an in-mold label or post-mold coating for visible interior parts.

    When a switch from ABS is contemplated for cost reduction

    Replacing ABS with FC9412G in an interior structural carrier shifts the primary design constraint from a heat deflection temperature above 100 °C to a stiffness-per-density ratio. The PP copolymer’s lower density (0.905 versus 1.05 g/cm³ for general-purpose ABS) provides a 13% mass reduction advantage at equivalent thickness. However, the tensile modulus of FC9412G is roughly 60% that of ABS, which forces rib reinforcement and increases part thickness from 2.0 mm to 2.7 mm for equivalent bending stiffness as calculated from the product of modulus and moment of inertia. In applications where part mass remains the overriding metric, the copolymer’s advantage survives the geometry penalty, but in space-constrained designs the thickness increase can negate the packaging benefit. Published data for this specific substitution scenario, including creep modulus at 1000 hours under 20 MPa load, is limited; preliminary testing per ISO 899-1 suggests a creep modulus decline of 25% after 1000 h at room temperature, placing it below ABS in long-term load-bearing components subject to sustained static stress.

    Differences from another common grade, a high-impact PP copolymer with MFR near 20 g/10 min (ASTM D1238, 230 °C/2.16 kg), surface during color compounding. FC9412G accepts carbon black masterbatch dispersions with a filter pressure value (FPV) below 2 bar/g after twin-screw extrusion at 200 rpm on a 40 mm co-rotating extruder with a 40 L/D configuration. The higher-flow comparator grade, due to its lower melt viscosity, often traps agglomerates, producing FPV values above 5 bar/g and visible particle counts exceeding 100 per ton in inline extrusion melt filtration. For electrical enclosure applications requiring consistent dielectric strength, this cleanliness level matters because impurity particles serve as charge concentration sites, reducing breakdown voltage per IEC 60243-1.

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