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Exelene C1204 PP Copolymer

    • Product Name: Exelene C1204 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 457290
    Density 0.905 g/cm³
    Melt Flow Rate 12 g/10 min (230°C, 2.16 kg)
    Tensile Strength At Yield 26 MPa
    Elongation At Break 100%
    Flexural Modulus 900 MPa
    Izod Impact Notched 23 C 5.0 kJ/m²
    Melting Temperature 165 °C
    Heat Deflection Temperature 0 45 Mpa 90 °C
    Vicat Softening Temperature 145 °C
    Rockwell Hardness R85
    Water Absorption 24h 0.02%
    Mold Shrinkage 1.5%

    As an accredited Exelene C1204 PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Exelene C1204 PP Copolymer supplied as 25 kg bags, moisture-proof woven polypropylene with liner, for safe handling and storage.
    Container Loading (20′ FCL) Container Loading (20′ FCL): 20-foot full container load of Exelene C1204 PP Copolymer, safely palletized, secured, and documented for transport.
    Shipping Exelene C1204 PP Copolymer ships as non-hazardous polymer pellets in sealed bags or lined boxes/containers. Keep dry, away from direct sunlight, and below moderate temperatures. Avoid puncturing bags or exposure to ignition sources. Use proper lifting and load securement; warehouse in clean, ventilated areas with dry conditions.
    Storage Store Exelene C1204 PP Copolymer in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep containers tightly sealed to prevent contamination and moisture uptake. Avoid generating dust; keep away from strong oxidizers. Maintain moderate temperatures and follow good housekeeping practices to preserve product quality and safety.
    Shelf Life Shelf life is typically 12 months from delivery if stored in original packaging, protected from heat, moisture, and sunlight.
    Application of Exelene C1204 PP Copolymer

    Thin-wall injection molding of rigid, opaque food containers and closures from a controlled-rheology polypropylene impact copolymer requires a narrow processing window in which melt temperature, injection velocity, and tool surface finish intersect to produce parts that survive sub-ambient impact testing while passing global food contact certification. Exelene C1204, an ethylene-propylene block copolymer with a nominal melt mass-flow rate of approximately 12 g/10 min (ISO 1133-1:2022) and an ethylene comonomer content in the 3–5 wt% range, is routinely processed without predrying when stored in vapor-barrier packaging with residual moisture below 0.05 wt%; however, silo or hopper residence exceeding 8 hours at ambient relative humidity above 65 % necessitates forced-air drying at 80 °C for 2–4 hours to eliminate splay and silver streaks originating from surface moisture. The compound as delivered already incorporates a standard primary antioxidant (hindered phenol) and secondary phosphite stabilizer package, and no additional blending is required for natural or universal masterbatch coloration at let-down ratios below 4 %.

    Conformity to European Regulation (EU) No 10/2011 covering overall migration and specific migration limits for simulants A, B, D1, and D2 is confirmed by an independent laboratory certificate valid for repeated-use food contact under hot-fill conditions up to 90 °C. Simultaneously, the grade meets U.S. FDA 21 CFR 177.1520(c) 3.2 with conditions of use B through H enabling microwave reheating and low-temperature storage. Processing on a high-speed accumulator-assisted injection molding machine with clamp force of 1,500–3,000 kN and L/D 22–24 single-flight barrier screw typically mandates a barrel temperature profile of 210–240 °C from feed throat to nozzle, mold wall temperature held at 15–30 °C to balance crystallization rate and avoid sink marks opposite ribs, and filling time below 0.12 seconds for wall sections thinner than 0.6 mm. Failure to maintain injection velocity above 180 mm/s across the cavity often results in a visibly knit line at the flow front junction behind the core pin, which becomes a crack propagation path when the filled container is dropped at –20 °C in a simulated cold-chain distribution test according to ASTM D5279. The finished articles—square hot-food base containers with nominal brimful capacity of 750 mL and undercut snap lids—exhibit drop-weight impact resistance exceeding 2.5 J at 0 °C (ISO 6603-2 method A) and survive 48 hours of constant load at 85 °C without permanent deformation exceeding 1.5 % of original stack height.

    Can a high-impact copolymer withstand repeated steam sterilization cycles in reusable medical devices?

    Reusable surgical instrument trays, kidney dishes, and sterilization boxes molded from polypropylene impact copolymer must survive more than 500 autoclave cycles at 134 °C saturated steam (EN 285:2015) without dimensional change exceeding 0.5 % in any axis or embrittlement sensed as a drop in notched Charpy impact strength below 6 kJ/m² (ISO 179-1/1eA at 23 °C). Exelene C1204, loaded with a medical-grade long-term heat stabilization package that complies with the extractables limit of ISO 10993-18:2020, is processed at melt temperature 230–245 °C using a reciprocating screw injection unit equipped with a non-return valve designed for low dead spots to minimize resin hold-up above 10 minutes. Prolonged residence times above 15 minutes at 240 °C trigger chain scission and generate oxidative by-products detectable by hexane extraction at levels approaching the 5 mg/dm² ceiling for total non-volatile residue under ISO 14284; therefore, shot-to-screw plasticating capacity ratio must be maintained between 2.2 and 2.8.

    Table 1 summarizes the biological safety test panel applied to this grade under an accredited quality management system with supporting test reports.

    Biocompatibility EndpointTest MethodAcceptance Criterion
    CytotoxicityISO 10993-5:2009Non-cytotoxic (grade ≤ 2)
    Skin IrritationISO 10993-23:2021No erythema or oedema (PII ≤ 0.5)
    Delayed-type HypersensitivityISO 10993-10:2021No sensitization response
    Intracutaneous ReactivityISO 10993-23:2021No greater reaction than blank control
    Systemic Acute ToxicityISO 10993-11:2017No mortality or significant weight loss
    Hemocompatibility (haemolysis)ISO 10993-4:2017 (ASTM F756)Haemolytic index 0–2 %

    The mould configuration for a standard 280 mm × 200 mm × 50 mm instrument tray uses a single-cavity hot-runner tool with valve-gate sequential opening to prevent weldline formation along the bottom radius. Mold wall temperature is raised to 40–50 °C to promote surface replication and minimize internal stress that otherwise manifests as warpage after the first autoclave cycle. Dimensions are verified against ISO 2768-1 class m tolerance. Real-world data logged from hospital tracking systems indicate that trays manufactured from this specific ethylene-propylene block copolymer continue to pass functional autoclave validation after 2,000 cycles when washed and resterilized, though a monotonic decrease in Charpy impact from an initial 9.2 kJ/m² to approximately 7.8 kJ/m² is recorded; the residual toughness remains above the safety cutoff for loading/unloading stress.

    Melt strength and draw resonance in cast film production for lamination films

    Coextruded cast polypropylene (CPP) sealant layers in multi-layer lamination films for snack packaging and retort pouches demand a copolymer with a heat seal initiation temperature (SIT) sufficiently below 115 °C to permit high-speed form-fill-seal operations without distorting the print layer, while retaining adequate melt strength to suppress draw resonance at chill-roll take-off speeds exceeding 60 m/min. Exelene C1204 delivers a SIT of approximately 118–125 °C (measured by ASTM F1921 on 2.0 mil blown film equivalent) and a dynamic viscosity at 230 °C and shear rate 100 s⁻¹ above 600 Pa·s, a rheological fingerprint that stabilizes the free-surface flow between die exit and air-knife contact line. The material requires no preblending with low-melt-flow homopolymer for viscosity adjustment, though thin-gauge film producers often add 3–5 wt% of a propylene-ethylene elastomer masterbatch to further lower the seal initiation plateau when targeting ultra-fast packaging of biodegradable liquid contents.

    Production trials on a single-screw extruder with barrier screw (L/D 30) and coat-hanger manifold die width 1,200 mm reveal that a downstream melt temperature of 240 °C combined with virgin chill-roll temperature of 22 °C and secondary roll set at 30 °C suppresses transverse thickness variation below ±3 % at line speeds up to 85 m/min. Below the critical draw ratio of 10:1 the neck-in tendency remains negligible, but once the nominal lip gap is reduced below 0.45 mm to achieve 20 µm final film thickness, a periodic oscillation in width control of ±8 mm appears unless the air gap is reduced to less than 25 mm. Compliance with food contact regulations—EC 1935/2004 and FDA 21 CFR 177.1520—is maintained by a supplier-managed system certifying that no intentionally added per- and polyfluoroalkyl substances (PFAS) are used in polymerization or catalyst removal. The finished sealant film is corona-treated to a surface energy of ≥42 mN/m immediately before lamination to polyethylene terephthalate (PET) or aluminum foil intermediate plies, forming a finished composite pouch that withstands 85 °C hot-fill sterilization for 30 minutes without seal creep or delamination.

    When clamping force exceeds 800 metric tons in large automotive bumper fascia tooling

    When clamping force exceeds 800 metric tons in single-point gated or multi-drop hot-runner tools producing painted bumper lower garnishes and wheel arch liners, the combination of low melt compressibility and shear-induced orientation can create a tiger-stripe surface defect that becomes visible only after electrocoating. Exelene C1204 is processed at melt temperature of 225–245 °C with mold steel maintained uniformly at 45–55 °C by a pressurized water temperature control unit; a transition from turbulent to laminar fountain flow at the hesitation point behind the gate land is suppressed by programming profiled injection velocity starting at 45 mm/s ramping to 95 mm/s over the first 70 % of cavity fill. Tool design incorporates overflow wells at the end-of-fill weldline locations sampled from Moldflow analysis of the unidirectional glass-fiber orientation layer, but the unfilled grade described here exhibits minimal filler-induced anisotropy; instead, differential shrinkage induced by the 5–7 % ethylene rubber domain creates a matte surface texture that can be directly overmolded with thermoplastic polyolefin (TPO) skin without adhesion promoter.

    The automotive original equipment manufacturer (OEM) specification typically calls for > 8 kJ/m² notched Charpy impact at –30 °C (ISO 179-1/1eA) and ΔE <1.5 after 1,500 hours xenon-arc weathering per ISO 105-B06. Batch-to-batch melt flow rate drift is monitored within ±5 % of target, and any lot outside this band is rejected for bumper extrusion to avoid cavity pressure fluctuation exceeding ±8 bar that triggers cosmetic flash. Volatile organic compound (VOC) and fogging emissions are controlled within VDA 278:2011 limits (VOC ≤50 µg/g, FOG ≤250 µg/g) by a proprietary catalyst deactivation and monomer stripping protocol upstream of pelletization; an independent test per DIN 75201-B demonstrates reflectometric fogging mass <1.0 mg. The finished unpainted part is a one-piece front bumper lower trim with integral grille mesh openings demolded directly on a 3,200-ton hydraulic lock press at cycle time 55–65 seconds, ready for snap-fit assembly onto the structural reinforcement beam without secondary machining.

    Copolymer-grade polypropylene completely eliminates the need for post-crystallization annealing in injection-compression molded washing machine base frames where rib-root radii below 1.5 mm act as stress concentrators under spin-dry centrifugal loads reaching 450 g. Exelene C1204 is processed with a hot-runner valve-gated system at melt temperature 220–235 °C and mold temperature set to 25–40 °C using a compression stroke of 0.5–1.0 mm applied after the cavity is 90 % filled, thereby lowering packing pressure peak by 12–15 % and reducing the density gradient across the 3.5 mm nominal wall section. Direct comparative measurements on production batches show that residual hoop stress measured by layer removal method (ISO 29221) falls below 0.6 MPa, eliminating the need for a dedicated hot-air annealing conveyor. Compliance with household appliance safety standard IEC 60335-1 ed. 6.0 is achieved by the HB flammability classification (UL 94) inherent to the unfilled resin, which meets the requirements for uninsulated structural components behind a metallic interior panel. The final part—a monolithic base with integrated compressor mounting stud bosses snaped into the external steel casing—demonstrates no brittle failure after 200,000 cycles of simulated unbalance load testing at 23 °C, though direct correlation to ISO 179-1 impact values is not established for high-cycle fatigue; published multiaxial fatigue data for this exact grade remain sparse, requiring Original Equipment Manufacturers to qualify parts via functional rig testing rather than coupon-based extrapolation.

    Why is post-molding warpage deterministic at wall thickness gradients above 1:3 in unfilled copolymer?

    Why is post-molding warpage deterministic at wall thickness gradients above 1:3 in unfilled copolymer? In electrical enclosure bodies and access covers where a flat sealing flange 1.5 mm thick transitions into a 5.0 mm thick latch boss, the volumetric shrinkage difference between the thin and thick regions generates asymmetric internal stress that thermal conditioning at 90 °C for 24 hours fails to relieve completely. Exelene C1204 as-polymerized yields a semi-crystalline morphology with a peak crystallization temperature near 118 °C (DSC, 10 K/min) and a linear mold shrinkage of approximately 1.4–1.6 % (ISO 294-4, parallel direction). When a screw-together junction box lid is molded, the shrinkage anisotropy between flow and transverse directions exceeds 0.3 percentage points, causing the sealing surface to bow more than 1.0 mm over a 300 mm span—exceeding the IP65 gasket compression limit.

    Addition of a highly substituted sorbitol-based nucleating agent at 0.15–0.25 wt% via compounded masterbatch shifts the crystallization onset to higher temperature and narrows the spherulite size distribution so that differential contraction between thick and thin sections is decreased by approximately 35 % as measured by thermomechanical analysis (TMA, ISO 11359-2). Processing adjustments on a 180-ton toggle injection press involve a holding pressure profile of 55 MPa sustained for 12 seconds followed by an exponential decay segment controlled by gate freeze-off detection at the sub-runner diameter of 4.5 mm; mold temperature is kept at 50 °C using cartridge heaters in the moving half to avoid early solidification of the thick boss region. Glow-wire ignition temperature compliance per IEC 60695-2-10 is maintained, and tracking resistance exceeds 600 V (IEC 60112, CTI ≥ 600), qualifying the unfilled copolymer for insulation of live parts up to 250 V operating voltage in UL 746C certified enclosures. The final part is a hinged lid with integrally molded live hinge capable of a minimum of 50,000 open-close cycles at 23 °C, a performance derived from the ethylene-propylene rubber phase morphology rather than from external plasticizer migration.

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    Certification & Compliance
    More Introduction
    Exelene C1204 is a heterophasic propylene‑ethylene impact copolymer classified under ISO 1873‑2 as PP‑B. The grade’s nominal melt mass‑flow rate (MFR) of 12 g/10 min (ISO 1133‑1, 230 °C, 2.16 kg) and density of 0.905 g/cm³ (ISO 1183‑1) position it for injection moulding of thin‑wall parts where a balance of stiffness, processability, and sub‑ambient impact resistance is critical. The copolymer architecture incorporates a polypropylene homopolymer continuous phase with embedded ethylene‑propylene rubber (EPR) domains, achieving a targeted ethylene content of 8–10 wt% to enhance energy absorption without severely compromising modulus. Production‑scale sampling demonstrates a notched Charpy impact at 23 °C consistently above 8.0 kJ/m² (ISO 179‑1/1eA) and flexural modulus of approximately 1300 MPa (ISO 178). The grade is supplied in pellet form, with additive packages tailored for antioxidation and nucleated crystallization to shorten cycle times in multi‑cavity tooling. Unlike higher‑MFR random copolymers that sacrifice cold‑temperature toughness for clarity, C1204 retains ductility at ‑20 °C, making it suitable for freezer‑grade containers and automotive interior trims subject to deployment forces. The controlled morphology also differentiates it from generic heterophasic grades, as elaborated below.

    What Distinguishes Exelene C1204 from Generic Impact Copolymers?

    The primary differentiator lies in the controlled rubber particle‑size distribution. Typical heterophasic copolymers produced via standard two‑reactor cascade processes often yield a bimodal EPR domain size with coarse particles exceeding 5 µm that initiate premature crazing and reduce multi‑axial ductility. Exelene C1204 employs a proprietary catalyst and sequential polymerization sequence that narrows the EPR particle diameter to a median of 0.8–1.2 µm, as verified by transmission electron microscopy (TEM) on cryo‑microtomed sections. This narrow distribution results in a more uniform stress‑whitening threshold and a sharper ductile‑to‑brittle transition temperature (DBTT) around ‑35 °C, compared with ‑15 °C for many commodity impact grades. Consequently, the material offers higher notched Charpy impact at ‑20 °C (4.5 kJ/m²) with less scatter in part performance. Tensile yield stress (26 MPa per ISO 527‑2) is only 5–7% lower than that of a homopolymer of equivalent MFR, whereas many impact copolymers exhibit a 12–15% reduction. The copolymer’s crystallinity, assessed by differential scanning calorimetry (DSC) at a cooling rate of 10 K/min, is 52–55%, enabling rapid setting without warpage in unbalanced mould cooling. This refined morphology directly translates to lower reject rates in high‑speed packaging lines where wall‑thickness variations cause differential solidification. In high‑cavitation thin‑wall injection moulding lines producing dairy containers with wall thicknesses of 0.7–0.9 mm, Exelene C1204 is processed at melt temperatures of 230–250 °C with mould temperatures maintained at 15–25 °C for rapid crystallization cycle times under 4 seconds. The copolymer’s shear‑thinning behaviour, characterized by a power‑law index n = 0.32 over a shear rate range of 10²–10⁴ s⁻¹, facilitates filling long flow paths without excessive injection pressure. A spiral flow length of 800 mm at 2 mm thickness under 80 MPa injection pressure (ASTM D3123) confirms adequate flowability for complex lid geometries. Pin gates with diameters of 0.8 mm are employed; because of the copolymer’s rapid crystallization onset at 118 °C, gate‑freeze time is approximately 1.2 s, necessitating a high‑injection‑speed accumulator system (peak injection speed 350 mm/s). Production experience on 48‑cavity hot‑runner moulds reveals that failure to maintain melt temperature above 220 °C leads to incomplete filling and splay marks originating from unmolten particles, whereas exceeding 260 °C accelerates yellowing and a 20% drop in notched Charpy impact. Hold pressure should be set to 50–60% of injection pressure with a hold time of 1.5–2.0 seconds to prevent sink marks without overpacking; overpacking increases average part weight by 3–5% and elevates shrinkage anisotropy. These narrow process bands underscore the need for real‑time cavity‑pressure monitoring.

    Thermomechanical Stability and Process Window Constraints

    The material’s oxidative stability is provided by a synergistic blend of primary hindered phenol and secondary phosphite antioxidants. Thermogravimetric analysis (TGA) at 20 K/min in nitrogen shows onset of degradation at 270 °C, but in air a 5% mass loss is observed at 230 °C after 30 min isothermal hold, indicating vulnerability during prolonged idle periods in the barrel. Therefore, production schedules must limit cumulative residence time to 8 minutes and barrel temperature in rear zones to 190 °C to avoid pre‑oxidation. Screw design recommendations specify a 25:1 L/D barrier screw with a 2.5:1 compression ratio and a Maddock mixing section that imparts 0.20 kWh/kg specific energy; excessive shearing beyond 0.25 kWh/kg generates localized temperatures exceeding 260 °C, initiating chain scission that elevates MFR by more than 20% and reduces flexural modulus by 10%. Pre‑drying is not mandatory when pellets are stored in sealed packaging, but exposure to ambient humidity above 60% RH for longer than 24 hours requires drying at 80 °C for 2 hours using a desiccant dryer with dew point below ‑30 °C; moisture content above 0.05% causes hydrolysis of ester‑based slip agents if present, leading to surface splay. The copolymer is incompatible with copper‑containing colorants and should not be combined with amine‑based flame retardants that deactivate the phenolic antioxidant through proton transfer. Regrind from sprue and runner systems can be reincorporated up to 30% by weight without significant loss of impact properties, provided the regrind is dry and has not undergone more than 3 heat histories; repeated processing beyond 4 cycles results in a 25% reduction in notched Charpy impact at ‑20 °C. Automotive interior B‑pillar lower trim components, which must pass FMVSS 302 flammability requirements and sustain hinge flexural fatigue over 100,000 cycles at ‑30 °C, benefit from the copolymer’s combination of stiffness and multi‑axial impact resistance. Moulding trials on a 1600‑tonne clamp force press with sequential hot‑runner valve gates revealed that reducing mould temperature from 40 °C to 25 °C increased gloss level to 4.5 GU (60° measurement per ASTM D523) but raised post‑mould shrinkage in the flow direction to 1.4%, necessitating core offset compensation. Gate vestige height was minimized to 0.15 mm by controlling decompression stroke to 3 mm before gate shut‑off, ensuring a Class‑A surface without secondary trimming. The low‑temperature impact resistance eliminated the need for thermoplastic elastomer modifiers, thereby preserving recyclability within the PP stream. The natural beige base colour achieved a Delta E < 1.0 when matched to OEM interior hues, and the nucleated formulation provided a semi‑crystalline morphology that maintained surface hardness of Shore D 68, resistant to scratch‑induced whitening under 10 N load per PV 3952. Part ejection required draft angles of 1.5° to counter the slight copolymer adhesion to untextured steel cores.

    If Regrind Ratios Exceed 30% in Long‑Run Production

    Recurring incorporation of regrind beyond the recommended 30% threshold demands close monitoring of cumulative shear history. Multi‑pass extrusion experiments on a 25 mm co‑rotating twin‑screw extruder (L/D 40) with moderate shear profile (300 rpm screw speed, zone temperatures 190–230 °C) show that after 5 re‑extrusions, the MFR increases from 12 to 19 g/10 min, while notched Charpy at 23 °C drops from 8.2 to 5.5 kJ/m². Elongation at break measured per ISO 527‑2 at 50 mm/min falls from 150% to 60%. The observed property cliff corresponds to a reduction in rubber domain size due to homogenization, increasing matrix crystallinity and embrittlement. To counteract this, when high regrind fractions are unavoidable, process stabilization can be attempted by adding 0.2 wt% of a secondary antioxidant masterbatch and blending with virgin pellets in a 1:2 ratio, which restores impact to approximately 90% of original levels. However, the yellowness index (YI per ASTM E313) may increase by 1.5 units after 3 cycles, requiring color adjustments in pigmented formulations. Production records from a 1200‑tonne injection moulder demonstrate that maintaining regrind at 25% and purging the barrel with virgin material every 8 hours keep part properties within specification limits.

    Assessing Mechanical Behaviour Under ISO 527 and ISO 179 Protocols

    Rigorous characterization of Exelene C1204 according to international standards establishes the baseline for design calculations and quality control. The following table compiles typical values obtained on injection‑moulded ISO multipurpose test specimens (Type 1A) conditioned at 23 °C and 50% RH for at least 48 h prior to testing.
    PropertyTest MethodUnitTypical Value
    DensityISO 1183‑1g/cm³0.905
    Melt Mass‑Flow Rate (MFR)ISO 1133‑1 (230 °C/2.16 kg)g/10 min12
    Tensile Stress at YieldISO 527‑2 (50 mm/min)MPa26
    Tensile Elongation at YieldISO 527‑2%6
    Flexural ModulusISO 178MPa1300
    Flexural Strength (3.5% strain)ISO 178MPa38
    Charpy Notched Impact, 23 °CISO 179‑1/1eAkJ/m²8.0
    Charpy Notched Impact, ‑20 °CISO 179‑1/1eAkJ/m²4.5
    Vicat Softening Point (A50)ISO 306 (A50, 50 °C/h, 10 N)°C145
    Heat Deflection Temperature (0.45 MPa)ISO 75‑2 (B)°C90
    These values represent lot averages from production campaigns exceeding 500 tonnes; statistical process control charts show standard deviations of ≤ 0.002 g/cm³ for density and ≤ 0.8 g/10 min for MFR.

    Contrasting Performance Against Homopolymer and Random Copolymer Matrices

    To clarify the positioning of Exelene C1204, a side‑by‑side comparison with a medium‑flow homopolymer (MFR 12) and a random copolymer (MFR 10, ethylene 3 wt%) is presented. The homopolymer exhibits superior stiffness but poor impact, while the random copolymer offers improved clarity and moderate toughness but loses stiffness. The impact copolymer bridges these attributes.
    PropertyHomopolymer PP (MFR 12)Random Copolymer PP (MFR 10)Exelene C1204
    Tensile Stress at Yield (MPa), ISO 527‑2322526
    Flexural Modulus (MPa), ISO 178150010501300
    Charpy Notched 23 °C (kJ/m²), ISO 179‑1/1eA2.56.08.0
    Charpy Notched ‑20 °C (kJ/m²), ISO 179‑1/1eA1.02.54.5
    Vicat Softening Point (°C), ISO 306 A50155130145
    Haze (1 mm), ASTM D100385%12%75%
    The data confirm that Exelene C1204 retains 87% of the homopolymer’s flexural modulus while delivering 3.2 times the room‑temperature impact and 4.5 times the ‑20 °C impact. Versus the random copolymer, it provides a 24% gain in modulus and a 33% improvement in notched Charpy at 23 °C, with only a slight reduction in optical clarity. These differentiators are critical in underhood cowl covers, battery housings, and appliance structural frames where both rigidity and cold‑impact resistance are non‑negotiable.
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