| HS Code | 978053 |
| Polymer Type | Polyethylene, Injection Grade |
| Density | 0.952 g/cm3 |
| Melt Flow Rate 190 C 2 16 Kg | 5.0 g/10 min |
| Tensile Strength At Yield | 23.0 MPa |
| Tensile Elongation At Break | 800% |
| Flexural Modulus | 1.00 GPa |
| Notched Izod Impact | 0.500 J/cm |
| Hardness Shore D | 65 |
| Deflection Temperature At 0 45 Mpa | 70.0 °C |
| Vicat Softening Point | 126 °C |
| Linear Mold Shrinkage | 0.020-0.025 cm/cm |
| Water Absorption | 0.010% |
As an accredited Bamberger Polymers Bapolene® 2272 Polyethylene, Injection Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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Injection molding of returnable transport packaging with Bapolene® 2272 is run as a high-flow HDPE system in the 20–30 g/10 min melt-index band. Side-wall sections are held to 2.0–3.5 mm, rib-to-wall ratios to 0.5–0.7, and untextured core-face draft angles to 0.5–1.5°. General-purpose reciprocating screws with L/D ratios of 20:1–24:1 and compression ratios of 2.5:1 are used. Melt temperature is maintained at 210–240 °C, mold temperature at 10–30 °C, and back pressure at 0.5–1.5 MPa. Injection velocity is profiled from 150 mm/s to 250 mm/s, while holding pressure is staged at 40–70 MPa. Cavity pressure sensors at the gate read 45–60 MPa during pack-and-hold. On 1,200 t toggle-clamp presses running 48-cavity pallet-foot tools, cooling time is controlled by thick boss sections: a 6 mm nominal diameter boss commonly requires 12–20 s additional hold before ejection without gate stringing.
For outdoor crates and totes, 0.2–0.5 wt% hindered amine light stabilizer and 1.5–2.5 wt% carbon black are dry-blended in a tumble mixer. The stabilizer package is selected against ISO 4892-2 cycle A weathering exposure. When the pigment and stabilizer carriers are olefin-based, the system retains compliance with FDA 21 CFR 177.1520 for incidental food contact. Mechanical acceptance commonly references tensile yield of 23–29 MPa per ASTM D638-14, flexural modulus of 900–1300 MPa per ASTM D790-17, and notched Izod impact of 2–4 kJ/m² per ISO 180/A. Deflection temperature under load for unfilled HDPE in this density band is typically 65–80 °C at 0.455 MPa per ASTM D648-18. Melt temperature above 260 °C should be avoided because molecular weight loss accelerates and can cause plate-out on core pins. Prolonged exposure to chlorinated cleaning agents at elevated temperature is not recommended; the high melt index that benefits rib filling reduces environmental stress-crack resistance relative to blow-molding HDPE grades.
Low-temperature impact response in thin-wall HDPE dairy containers is governed by wall thickness, processing-induced orientation, and spherulite size control. Bapolene® 2272 is processed in 0.8–1.5 mm wall sections with melt temperatures of 220–245 °C and mold temperatures of 15–25 °C. Fill time is set at 0.20–0.35 s, with a 0.05–0.10 s decompression stroke after screw recovery to reduce gate frost in cold-runner sub-gates. Peak cavity pressure should reach 45–70 MPa during filling to maintain density in rim and base vertices. If mold temperature falls below 15 °C, ductile-to-brittle transition shifts to warmer temperatures and freezer impact failure occurs at the base corner. High-cavitation molds with 32–48 cavities require hot-runner manifold temperatures of 230–250 °C; gate diameter should not exceed 0.8 mm to avoid gate stringing.
The resin is normally fed as 100% virgin high-flow HDPE. If notched Izod impact at −20 °C must exceed 3 kJ/m² per ISO 180/A, up to 5 wt% of a metallocene-catalyzed LLDPE with density below 0.920 g/cm³ is dry-blended. This addition raises low-temperature notched Izod by 10–25% but reduces flexural modulus by 8–15%; rib depth is reduced by 0.2–0.5 mm to preserve stacking stiffness. Migration testing under EU 10/2011 for repeated-use containers and cold-fill conditions is run after screw homogenization, because inadequate mixing can cause weld-line streaks and variable total migration. Published data for Bapolene® 2272 in freezer-grade dairy container configurations is limited; the processing window is derived from high-flow HDPE of equivalent melt-index class and should be validated on the actual production tool.
Caps and closures molded from Bapolene® 2272 concentrate dimensional tolerance in the sealing lip, tamper-evident band rupture points, and internal thread root. In a 28 mm PCO 1881 closure, roundness is held to ±0.10 mm and tamper-evident bridge length is held to 0.25–0.35 mm at the parting line. High-cavitation closure tools with 32–64 cavities are run at melt temperatures of 225–250 °C and mold temperatures of 10–20 °C. Valve-gated hot runners with 0.6–0.8 mm gate orifices produce gate vestige below 0.10 mm when decompression is set to 0.5–1.0 mm. On 130 t tie-bar-less molding machines, the limiting constraint is not injection speed but cooling uniformity across the cavity bank; a mold temperature variation of 3 °C between cavities can change removal torque by more than 5%.
Torque retention is influenced by thread-core creep and sealing-liner recovery. The resin is processed without filler; oleamide may be added at 0.05–0.10 wt% to reduce friction during induction sealing. Closures for aqueous, acidic, and low-alcohol food contact are tested under FDA 21 CFR 177.1520(c) and EU 10/2011. For household chemical bottle closures, stress-crack resistance is evaluated under ASTM D1693-15 condition B in a 10% Igepal CO-630 solution at 50 °C. Melt temperature above 255 °C during color changes should be avoided because degradation residues accumulate on hot-runner tips and cause gate stringing. Published data for Bapolene® 2272 in beverage closure torque retention is limited; liner compression can override the resin contribution and must be validated on the specific induction-sealed liner.
Injection molded open-head pails require rim hoop strength and handle boss load transfer without stress whitening. Bapolene® 2272 is applied in pails with nominal rim thickness of 2.5–4.0 mm and handle boss diameter of 16–20 mm. Melt temperature is set at 215–235 °C, while rim and boss mold temperatures are maintained at 20–30 °C to control post-mold ovality. Packing pressure is profiled at 55–75 MPa for 4–8 s, followed by cooling of 20–35 s depending on floor thickness. On a 650 t hydraulic press running a 4-cavity pail mold, handle boss voids are eliminated by reducing injection velocity at the boss transition to 80–120 mm/s and applying a short decompression after screw recovery. Shrinkage after 48 h at 23 °C and 50% RH is typically 1.5–2.0% in rim diameter for HDPE of this density class.
Pails intended for dangerous goods are evaluated under 49 CFR 178.601 or UN Model Regulations performance tests, including stacking at 40 °C for 28 days. High-flow injection HDPE may show lower environmental stress-crack resistance than high-molecular-weight HDPE used in blow-molded pails; open-head pails exposed to aggressive hydrocarbons may require a liner or barrier layer. Industrial pails can be colored with carbon black at 1.0–2.0 wt% without affecting RoHS 2011/65/EU thresholds for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE when applicable. The table below summarizes the compliance matrix for injection molded pail applications.
| Standard or regulation | Test focus | Application condition for injection molded pails |
|---|---|---|
| FDA 21 CFR 177.1520(c) | Olefin polymers for food contact | Applicable only to pails intended for direct food contact; migration depends on use conditions A through H. |
| EU 10/2011 | Overall and specific migration | Repeated-use pails with cold-fill or ambient storage; overall migration limit 10 mg/dm². |
| 49 CFR 178.601 | UN performance testing | Stacking, drop, and leakproofness for dangerous goods pails; test limits depend on packaging group. |
| RoHS 2011/65/EU | Restricted substance thresholds | Applies only when the pail is a component in electrical or electronic equipment. |
Published data for Bapolene® 2272 in UN-certified pail configurations is limited; tooling validation should include load-deflection measurement on the handle boss after 24 h ambient conditioning and post-mold diameter measurement at 23 °C and 50% RH before release for stacking qualification.
Structural requirements shift from thin-wall fill to ribbed load-bearing floors. Bapolene® 2272 fills complex rib patterns at melt temperatures of 220–245 °C, but gate velocity above 300 mm/s can create jetting at the flow front. For bins with shot weights above 1.5 kg, screw-back speed is set at 60–100 rpm and nozzle decompression is limited to 0.5 mm to prevent air entrapment. Mold temperature is set at 20–30 °C. Floor sections of 4–6 mm require holding pressure of 60–80 MPa for 10–20 s to avoid sink marks at rib intersections. Ejection temperature should not exceed 55 °C to prevent distortion of unsupported floor panels.
For vented bins used in industrial logistics, the formulation may include 1.0–2.0 wt% carbon black and 0.3–0.8 wt% antioxidant package. Antistatic grades require an internal antistat at 0.5–1.5 wt%, which reduces surface resistivity to 10^9–10^11 Ω per IEC 61340-2-3 but may slightly lower flexural modulus. Dimensional tolerance for mating lids is held to ±0.25 mm across a 600 mm span, requiring uniform mold cooling and post-mold fixturing for 24 h at 23 °C. High-flow HDPE of this class has lower environmental stress-crack resistance than high-molecular-weight HDPE; bins exposed to aromatic solvents or concentrated detergent solutions may require compatibility testing before production release.
In multi-cavity toy tooling, parting-line deflection on small cores is the primary source of dimensional rejection rather than material shrinkage. Bapolene® 2272 is processed with melt temperatures of 215–235 °C and mold temperatures of 12–25 °C. For action figures with 1.5–2.5 mm wall sections, injection speed is profiled from 60 mm/s at the core pin to 180 mm/s at the torso cavity to reduce core shift. Pigment masterbatches are added at 1–3 wt%; dispersion is verified under ASTM D6290-19 on flat plaques. Compliance with EN 71-3, ASTM F963-17, and REACH Annex XVII is required for toy-grade material; because the base resin is an unplasticized polyethylene, phthalate migration risk is below the regulated limit when the pigment masterbatch is also phthalate-free.
The high-flow nature assists filling of thin limbs and undercuts but reduces melt strength for microfeature retention. Ejection temperature should not exceed 55 °C to prevent distortion of unsupported appendages. Shrinkage after 48 h at 23 °C and 50% RH is in the range of 1.2–2.0% for unfilled HDPE of this density band; mold cavities are cut with 1.4% isotropic shrink allowance. Published data for Bapolene® 2272 in toy-grade formulations is limited; the shrink allowance is based on equivalent high-flow HDPE grades and should be confirmed with a pilot cavity before full tooling is completed.
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