Exelene C0600 is a high-impact polypropylene copolymer engineered for injection molding applications where stiffness, processability, and low-temperature ductility intersect. The grade is formulated around a heterophasic structure—an isotactic polypropylene matrix incorporating a precisely controlled ethylene-propylene rubber (EPR) particle distribution. Available melt flow rate is typically 6.0 g/10 min (ASTM D1238, 230 °C, 2.16 kg), a viscosity window selected to balance thin-wall filling behavior with sufficient melt strength to resist jetting and flow marks in complex multi-cavity tools. Density at solid state registers 0.900 g/cm³ (ISO 1183-1), while tensile yield strength measured on 3.2 mm injection-molded plaques sits near 25 MPa (ISO 527-2/1A/50 mm/min). Notched Izod impact resistance at 23 °C typically exceeds 35 kJ/m² (ISO 180/A), a value that differentiates C0600 from lower-rubber-content copolymers that suffer brittle transitions at sub-ambient conditions. The product is supplied in natural, pelletized form stabilized with a phenolic/phosphite antioxidant package sufficient for multiple heat histories during recycling of runner and reject material.
What distinguishes the heterophasic architecture of C0600 from random and homopolymer grades?
Random PP copolymers incorporate ethylene units statistically within the propylene chain, depressing crystallinity uniformly and producing a single glass transition near 0 °C. Homopolymer polypropylene offers high stiffness but negligible impact strength below its glass transition. Exelene C0600, by contrast, relies on a discrete elastomer phase dispersed as domains of 0.5–2.0 μm in cross-section; the exact particle size distribution is influenced by compounding history and screw configuration. This two-phase morphology generates a secondary glass transition near −55 °C attributable to the EPR component, preserving impact resistance down to temperatures where homopolymers fail catastrophically. The ethylene content is held in the range of 8–12 wt%, sufficient to deliver ductile fracture behavior without excessive loss of flexural modulus. In practice, the flexural modulus of C0600 measured per ISO 178 at 2 mm/min registers approximately 1,100 MPa, a reduction of only 15–20% relative to a medium-flow homopolymer while impact toughness increases by a factor of four or more. This trade-off profile is particularly relevant in automotive interior trims where airbag deployment forces require predictable material fracture at defined temperatures; C0600 avoids the splintering failure mode observed in brittle grades.
Pre-drying thresholds and moisture-related processing anomalies
Although polypropylene generally exhibits low hygroscopicity, the compounded additive package in C0600 and the high surface-area-to-volume ratio of pelletized feedstock make moisture management non-trivial in high-humidity production environments. When ambient relative humidity exceeds 60%, superficial pellet moisture can reach levels causing surface splay, silver streaking, and dimensional instability in molded parts. Pre-drying for 2–3 hours at 80 °C in a desiccant dryer with a dew point below −30 °C is recommended before processing on open-hopper machines. Failure to pre-dry manifests initially as a pearlescent haze on gate-adjacent surfaces, progressing to measurable reductions in weld-line tensile strength—losses of 7–12% have been recorded on instrumented dog-bone specimens extracted across knit lines from under-dried feedstock.
A common processing window for C0600 in standard reciprocating-screw injection molding equipment targets a melt temperature of 220–250 °C and a mold temperature of 20–60 °C. At the lower bound of 220 °C, viscosity is adequate for filling moderate flow-length ratios (150:1 in nominal wall stock of 2.0 mm), but cold-slug formation at the nozzle tip becomes a recurring issue if the sprue bushing heat profile decays. Elevating melt temperature toward 250 °C improves surface replication of fine-grained mold textures but narrows the safe residence-time window: and a residence time exceeding 8 minutes at 250 °C initiates detectable molecular weight degradation as monitored by a reduction in melt viscosity of 10–15% on a capillary rheometer (ASTM D3835). Shot-to-consistency alarms on production monitoring systems invariably correlate with barrel-temperature overshoot events exceeding 5 °C above setpoint; consequently, heater-band PID tuning and thermocouple placement are critical when running C0600 on accumulator-head machines with long plastication barrels.Automotive interior carrier structures and airbag integration
Low-temperature ductility governs material selection for instrument panel retainers and door-trim carriers that must pass deployment tests at −30 °C. Exelene C0600 has been evaluated in ribbed structural panels molded with gas-counterpressure technology on 2,500-ton presses; fracture in drop-weight impact testing (ISO 6603-2, 4.4 m/s striker velocity at −30 °C) remains fully ductile with puncture energy exceeding 20 J. Incompatibility with long-glass-fiber reinforcement should be noted: the presence of EPR domains reduces interfacial adhesion at the glass-matrix boundary, leading to delamination at fiber ends under cyclic thermal load. For applications requiring stiffness beyond the neat copolymer’s capability, short-glass-fiber grades (0.2–0.5 mm fiber length) with aminosilane sizing designed for polypropylene are preferred, though published data for this specific configuration is limited to in-house comparative studies.
A pronounced sensitivity to pigmentation exists. Certain organic red and blue phthalocyanine pigments at loadings above 0.8 wt% act as nucleating agents, raising crystallization onset temperature by 8–12 °C and altering the spherulite size distribution. The result is a measurable shift in shrinkage anisotropy: parallel-to-flow shrinkage increases by 0.2–0.4% while transverse shrinkage decreases, leading to warpage in large flat panels. Pre-colored masterbatch trials should include full mold-flow simulation input calibrated with pvT data specific to the pigmented compound, not the natural feedstock.
When wall thickness falls below 0.8 mm—thin-wall packaging limits
High-speed thin-wall injection molding for food containers and closures subjects C0600 to shear rates in the gate region exceeding 50,000 s⁻¹. At these conditions, the apparent viscosity measured on a capillary rheometer with a 1.0 mm die drops to approximately 30 Pa·s at 230 °C, a value that permits filling of rectangular tubs with flow length-to-thickness ratios of 200:1 using injection velocities of 300 mm/s on accumulator-driven systems. However, the heterophasic structure introduces a strain-rate-dependent whitening phenomenon: at extreme elongation rates near the advancing flow front, EPR cavitation can initiate before the mold is fully packed, producing a blush patch visible on the ejector side. This cavitation-induced whitening occurs at a critical principal strain rate of approximately 150 s⁻¹ for this grade; maintaining clamp force above 150 tons on a 400-ton machine and setting pack pressure at 70–80% of injection pressure typically suppresses the defect. Thin-wall rigid packaging grades with higher MFR (20–35 g/10 min) avoid this blush window but sacrifice 50–70% of the impact toughness that C0600 retains; for applications requiring both high-flow and low-temperature drop resistance, a balanced MFR of 6 g/10 min is often the practical optimum.
| Property (unit) | Standard | C0600 | Homopolymer (MFR 12) | Random copolymer (MFR 8) |
|---|---|---|---|---|
| MFR at 230 °C/2.16 kg (g/10 min) | ISO 1133-1 | 6.0 | 12 | 8 |
| Tensile yield strength (MPa) | ISO 527-2 | 25 | 34 | 27 |
| Flexural modulus (MPa) | ISO 178 | 1100 | 1450 | 1050 |
| Notched Izod, 23 °C (kJ/m²) | ISO 180/A | 38 | 4 | 9 |
| Notched Izod, −30 °C (kJ/m²) | ISO 180/A | 6 | 1.5 | 2.5 |
| HDT at 0.45 MPa (°C) | ISO 75-2/B | 85 | 100 | 80 |
| Mold shrinkage, parallel (%) | ISO 294-4 | 1.4 | 1.6 | 1.5 |
Appliance enclosures and the warpage constraint
Large-scale molding of washing machine outer tubs or refrigerator inner liners using C0600 introduces a dimensional stability challenge rooted in the post-crystallization regime. After demolding, amorphous regions continue to densify over a period of 24–72 hours, generating anisotropic shrinkage that varies with local cooling rate differences between thick ribs and thin walls. Measurements on a tub prototype with a nominal wall of 3.0 mm and ribs of 4.5 mm revealed a post-mold shrinkage gradient of 0.15–0.25% between rib centers and adjacent flat sections, sufficient to produce a warp displacement of 2–3 mm over a 500 mm span. Constrained-cooling fixtures or post-mold annealing at 120 °C for 30 minutes can reduce warpage by stress relaxation of the amorphous phase, though annealing temperature must remain below the onset of EPR melt coalescence at approximately 135 °C, which causes a permanent drop in impact performance.
Additionally, appliance specifications demanding UL 94 HB or V-2 classification at thicknesses below 1.5 mm require flame-retardant masterbatch addition. Brominated flame retardants supported by antimony trioxide synergists, when incorporated at levels yielding 0.8–1.2% bromine content, maintain the required rating but can reduce notched Izod values by 15–20% due to particulate stress concentration. Exelene C0600 accepts standard FR packages with less impact penalty than homopolymers because the EPR phase absorbs some of the stress concentration energy; however, trials on twin-screw-extruded pre-compounds with L/D 40:1 suggest that feeding FR additives via a side stuffer downstream of the primary melting zone preserves the EPR particle integrity better than a single hopper feed.Medical device housings and sterilization chemical resistance
Exelene C0600 has found application in non-implantable portable medical device enclosures where repeated exposure to hydrogen peroxide vapor, ethylene oxide, and quaternary ammonium disinfectants is routine. The grade’s polypropylene backbone exhibits no stress-cracking under ethylene oxide exposure at 55 °C and 70% relative humidity for 12-hour cycles—a condition known to attack polycarbonate and certain acrylonitrile-butadiene-styrene grades. However, the impact modifier phase introduces a vulnerability to lipid-based cleaning agents; prolonged (24-hour) contact with 10% isopropyl alcohol/water mixtures at 50 °C can swell the EPR domains, increasing isotropic swelling to 0.8% and dropping the glass transition temperature of the rubber phase by 3–5 °C. This is a reversible physical swelling rather than chemical degradation, but dimensional recovery requires 48–72 hours under ambient desiccation.
Mold-filling simulation for thin-section medical housings (wall thickness 1.0–1.5 mm) using Cross-WLF viscosity coefficients derived for C0600—with n of 0.35, τ* of 35,000 Pa, and zero-shear viscosity of 1,200 Pa·s at 230 °C—indicates that gate freeze time is reached at 5–6 seconds for a 1.0 mm diameter pin gate. This demands a hold-pressure profile that decays from 80 MPa to 40 MPa over 4 seconds to avoid sink marks opposite mounting bosses. Validation runs on a 120-ton electric injection molding machine with mold-temperature control units holding 40 °C ± 1 °C confirmed process capability indices (Cpk) above 1.67 for critical-to-quality dimensions.
Regulatory status and food-contact compliance
Exelene C0600, in its natural uncolored form, complies with the compositional requirements of EU Regulation (EC) No 1935/2004 and its specific measure for plastic materials, Regulation (EU) No 10/2011, covering overall migration limits and specific migration limits for monomers and additives. The base polymer and antioxidant system have been evaluated under the US FDA’s 21 CFR §177.1520(c) for olefin polymers, with conditions of use up to 100 °C for all food types except alcohol content exceeding 8%. Certification for REACH and RoHS compliance is available through the supplier’s documentation portal. No substances of very high concern (SVHC) above 0.1% threshold are present.
| Parameter | Range | Unit |
|---|---|---|
| Melt temperature | 220–250 | °C |
| Mold temperature | 20–60 | °C |
| Injection velocity | 100–300 | mm/s |
| Hold pressure | 40–80 | MPa |
| Hold time | 4–8 | s |
| Screw back pressure | 5–15 | bar |
| Screw speed (medium size, D=50 mm) | 80–150 | rpm |
| Pre-drying | 2–3 h at 80 °C | — |
The long-term thermal stability envelope of C0600 under air atmosphere, as measured by onset of oxidation via differential scanning calorimetry (ASTM D3895, isothermal at 190 °C), exceeds 30 minutes, sufficient for multiple hot-runner cycles without additive depletion. Nevertheless, prolonged contact with copper-based heat-transfer components should be avoided; copper ions catalyze peroxide decomposition and accelerate oxidative chain scission, a degradation pathway observed as a sharp drop of 0.5–1.0 dL/g in intrinsic viscosity over 24 hours at 140 °C in copper-sandwich aging tests.