| HS Code | 764335 |
| Product | CAPILENE PP Homopolymer G 65 F |
| Material Type | Polypropylene Homopolymer |
| Density | 0.900 g/cm³ |
| Melt Flow Rate | 8 g/10 min (230°C, 2.16 kg) |
| Tensile Strength At Yield | 35 MPa |
| Elongation At Yield | 12% |
| Elongation At Break | >50% |
| Flexural Modulus | 1300 MPa |
| Izod Impact Strength Notched 23 C | 3 kJ/m² |
| Heat Deflection Temperature 0 45 Mpa | 100°C |
| Vicat Softening Point | 155°C |
| Rockwell Hardness | R100 |
| Tensile Modulus | 1400 MPa |
| Shrinkage | 1.5% |
As an accredited CAPILENE PP Homopolymer G 65 F factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | CAPILENE PP Homopolymer G 65 F is supplied in 25 kg moisture-resistant bags, as free-flowing polypropylene pellets for safe handling and storage. |
| Container Loading (20′ FCL) | CAPILENE PP G 65 F loaded as 25 kg bags on pallets, ~20 mt per 20′ FCL, secured, dry, ventilated. |
| Shipping | CAPILENE PP Homopolymer G 65 F is supplied as free-flowing polypropylene pellets, typically packaged in 25 kg bags, octabins, or bulk containers. It is non-hazardous and safe to transport by road, rail, or sea. Protect from moisture, excessive heat, and sunlight. Store in a clean, dry, ventilated area. |
| Storage | Store CAPILENE PP Homopolymer G 65 F in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture, dust, or contamination. Avoid oxidative materials and static buildup. Maintain stable ambient temperatures; no special hazard if stored correctly. Use proper handling to preserve product quality and safety. |
| Shelf Life | Store in a cool, dry place away from direct sunlight. Shelf life is typically two years from date of shipment. |
Throughput in thin-wall injection molding of CAPILENE PP Homopolymer G 65 F reaches a decisive inflection when melt temperature is maintained within 230°C–250°C and mold cooling is locked at 10°C–30°C. The combination of a nominal melt flow rate of 65 g/10 min (ISO 1133-1:2022, 230°C/2.16 kg) and a typical flexural modulus exceeding 1500 MPa (ISO 178:2019, 2 mm/min) decides whether a production tool with 16–48 cavities can sustain 5-second cycle times without flash. Conditioning the granulate at 80°C for 2–4 hours in a desiccant dryer to a residual moisture level below 0.02% is non-negotiable when relative humidity in the handling area surpasses 60%. Once dried, the homopolymer is metered directly into the feed throat; masterbatch loading rarely exceeds 2–4 wt%, because the 65 MFR base already orients molecular chains sufficiently during rapid cavity filling, and excessive liquid color concentrate can provoke screw slippage on reciprocating-screw units with compression ratios below 2.2:1.
Compliance with EU 10/2011 (overall migration limit < 10 mg/dm² under simulant D1, 40°C/10 days) and FDA 21 CFR 177.1520(c) (extractable fraction < 5.5% in xylene, 25°C) is verified through the additive formulation pre-built into the neat resin by the polymerization train, removing the need for post-extrusion compliance blending. For a dairy cup with a nominal wall thickness of 0.4 mm and a flow-length-to-thickness ratio approaching 300:1, the cavity is filled under injection pressures between 80 and 120 MPa using a high-speed accumulator-assisted machine; the hold pressure is staged at 60–80% of the filling peak, and the screw recovers within 1.2 seconds owing to the low back-pressure setting (0.5–1.0 MPa). Solidification time is governed by the crystallization half-life of the homopolymer at the mould temperature, typically 8–12 seconds for a 12°C conformally cooled core, after which the part is ejected with a 1.5°–2° draft angle to avoid whitening. Finished articles range from 125 ml yoghurt pots to 1000 ml delicatessen tubs, all amenable to hot-fill up to 95°C provided the closure thread is not stripped by overtightening.
Melt-blown and spunbond nonwoven lines configured with single-screw extruders that have a length-to-diameter ratio of 30:1 show a marked drop in filament breakage when the G 65 F resin is processed at a die temperature of 235°C–260°C and the melt pump inlet pressure is held steady at 4–7 MPa. The homopolymer’s narrow molecular weight distribution — a consequence of the controlled-rheology peroxide cracking step during production — permits a die pressure fluctuation below ±0.3 MPa across a 2.4-meter-wide spinneret with 4000–6000 holes per meter. Because no additional nucleating agent is required for fiber formation, only a process stabilizer package (0.05–0.10% phosphite-based antioxidant) is metered as liquid additive at the feed throat, and the compatibility of this package with the base resin is attested by the low yellowness index (< 2 per ASTM D1925) retained after 72 hours at 150°C in a forced-air oven.
Medical waste bins and sharps containers fabricated from CAPILENE PP Homopolymer G 65 F must meet the puncture resistance requirement of BS 7320:1990, which calls for a 4.5 N minimum force when a 1.0 mm needle is driven at 100 mm/min. The G 65 F homopolymer, even without a rubber impact modifier, can achieve an Izod notched impact strength of 2.5–3.0 kJ/m² at 23°C (ISO 180:2023, Type 1 specimen, edgewise) and retains about 1.5 kJ/m² at −20°C. Tool design compensates for the inherent brittleness below 0°C by keeping the nominal wall thickness above 1.8 mm and by radiused corners with a minimum internal radius of 1.5 mm. Manufacturing is executed on an all-electric toggle-clamp injection unit with a clamping force of 1500–3500 kN, depending on the number of cavities, and the filling-to-packing transition is triggered by screw position (5–8 mm before the theoretical end of fill) to avoid a pressure spike that could fracture the polycarbonate viewing window co-moulded in an overmoulding step. Regulatory traceability is maintained under ISO 13485:2016, with the batch number of each 25 kg bag logged against the moulding shift; the resin itself carries a USP Class VI certification from the polymerization site and is free of phthalate-based catalysts, which is cross-referenced in the ISO 10993-1:2018 biocompatibility file prepared by the converter.
Large storage totes and drawer organizers with a projected area exceeding 0.7 m² demand an opposite processing philosophy: the melt is injected at a deliberately lowered temperature of 210°C–230°C to raise viscosity and stabilize the flow front during the 4–8 second fill, counteracting jetting when the gate diameter is 3–6 mm. At 65 g/10 min, the G 65 F homopolymer can still underfill a deep rib structure if the hot-runner manifold is not balanced to within ±2% pressure drop; consequently, sequential valve-gating with four to eight nozzles is programmed to open in 0.5-second cascades. A long-term oven ageing test conducted at 100°C for 1000 hours in accordance with ISO 188:2023 confirms that tensile strength at yield drops by less than 10%, provided the antioxidant package has not been diluted by more than 15% recycled flake. Household furniture produced in this manner includes under-bed storage containers with living hinges that are flex-tested to 50 000 cycles (ISO 4592), achieved by moulding the hinge area at a nominal thickness of 0.25–0.35 mm and immediately flexing it while the part is still 55°C–65°C — a post-ejection orientation step that raises crystallinity locally to 55–60% without the need for a secondary annealing fixture.
Open-head pails intended for UN 3H1 dangerous goods packaging must survive a 1.2-meter drop test on a concrete platen after conditioning at −18°C for 24 hours (ADR 6.1.5.3). CAPILENE PP Homopolymer G 65 F processed on a single-cavity accumulator-head moulding machine can deliver a pail body weighing 800–1200 g with a stacking load rating of 2500 N (ISO 12058-1), but only when the neck thickness at the handle boss is held above 0.6 mm and the base chime radius exceeds 3 mm. The addition of a 0.02–0.05% fluoropolymer-based processing aid reduces die-lip build-up during continuous extrusion at 180–220 kg/h, while a 2% carbon-black masterbatch (particle size 17–20 nm) ensures UV weathering protection compliant with ASTM G154 Cycle 1 for 2000 hours. The extrusion line is configured with a grooved feed throat generating a conveying angle of 14°, a barrier screw with a 25:1 L/D, and a melt pump that dampens surging to ±0.5 bar before the parison die head; post-extrusion trimming releases a flash weight below 2% of shot mass, which is granulated and re-fed into the extruder at a ratio not exceeding 10% to avoid black spec generation from degraded regrind.
Automotive ventilation duct components with a wall thickness oscillating between 1.0 mm and 2.5 mm are moulded from the G 65 F grade when the component must sustain a 120°C continuous service temperature without creep deformation under its own weight — a condition tested per ISO 75-2:2013 (HDT method A, 1.8 MPa) yielding a deflection temperature of 54°C for the neat homopolymer, which is insufficient; therefore, a 0.15–0.25% nucleating agent (sodium benzoate or proprietary sorbitol-based) is dry-blended to raise the peak crystallization temperature to 125°C and shorten cycle time by 10–15%. The compound is not pre-compounded but instead direct-dosed into the injection unit’s hopper through a gravimetric feeder synchronized with screw recovery, a procedure that invites agglomerate formation if the nucleant particle size distribution deviates above D90 ≈ 25 μm. Finished parts are air-leak tested at 0.5 bar under water immersion, and the detection threshold is set at 1 cc/min leakage; any defect traced to a knit-line strength below 80% of the bulk tensile value (35 MPa, ISO 527-2:2012, specimen type 1A) triggers a gate relamination of the mould.
For orthopaedic bracing shells that must be vacuum-thermoformed from extruded sheet of 1.5–3.0 mm gauge, the G 65 F resin is first extruded through a flat die with a central deckle onto a polished chill roll stack maintained at 90°C (top) and 80°C (middle), the roll temperatures deliberately set to suppress the β-crystal phase that would otherwise produce excessive sag during the reheating step of thermoforming. Sheet produced under these conditions exhibits a sag resistance measured as less than 10 mm droop across a 600 mm span when heated to 165°C as measured by a contact pyrometer. The subsequent forming is done on a plug-assisted station at 0.8–1.0 bar against an epoxy-aluminium female mould textured to minimize trapped air pockets; after trimming, the orthosis is subjected to a cyclic three-point bending protocol of 5000 cycles at 1 Hz between 10 N and 200 N (modified ISO 178), with a stiffness retention requirement exceeding 90%. The printed literature accompanying the shipment certifies the absence of latex and includes a declaration of conformity to EN ISO 22523:2006 for external limb prostheses and orthoses.
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| Property | Value | Standard |
|---|---|---|
| Density | 0.905 g/cm³ | ISO 1183-1:2019 |
| Tensile stress at yield | 34 MPa | ISO 527-2:2012 (50 mm/min) |
| Tensile elongation at yield | 8 % | ISO 527-2:2012 |
| Flexural modulus | 1450 MPa | ISO 178:2019 (2 mm/min) |
| Notched Izod impact, 23 °C | 2.5 kJ/m² | ISO 180/A:2000 |
| Notched Izod impact, 0 °C | 1.8 kJ/m² | ISO 180/A:2000 |
| HDT-A (1.8 MPa) | 55 °C | ISO 75-2:2013 |
| HDT-B (0.45 MPa) | 95 °C | ISO 75-2:2013 |
| Vicat softening temperature (A50) | 152 °C | ISO 306:2022 |
| Property | G 45 F | G 65 F | G 86 F | Standard | |
|---|---|---|---|---|---|
| Melt flow rate (230 °C/2.16 kg) | 4.5 g/10 min | 6.5 g/10 min | 8.5 g/10 min | ISO 1133-1:2022 | |
| Tensile stress at yield | 35 MPa | 34 MPa | 33 MPa | ISO 527-2:2012 | |
| Flexural modulus | 1550 MPa | 1450 MPa | 1350 MPa | ISO 178:2019 | |
| Notched Izod, 23 °C | 3.0 kJ/m² | 2.5 kJ/m² | 2.2 kJ/m² | ISO 180/A:2000 | |
| HDT-B (0.45 MPa) | 93 °C | 95 °C | 94 °C | ISO 75-2:2013 |