| HS Code | 974188 |
| Density | 0.954 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.20 g/10 min |
| Tensile Strength At Yield | 27 MPa |
| Tensile Elongation At Break | 800% |
| Flexural Modulus | 1.10 GPa |
| Notched Izod Impact Strength | 0.15 J/cm |
| Vicat Softening Point | 126°C |
| Heat Deflection Temperature 0 46 Mpa | 75°C |
| Shore D Hardness | 65 |
| Environmental Stress Cracking Resistance | >1000 h |
| Brittleness Temperature | < -70°C |
| Melting Point | 134°C |
As an accredited TPC (Japan) HDPE KL272C factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | TPC (Japan) HDPE KL272C is supplied in 25 kg polyethylene-lined paper bags, palletized at 1,000 kg per pallet. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): TPC (Japan) HDPE KL272C high-density polyethylene resin, 25 kg bags, palletized and securely loaded for ocean freight. |
| Shipping | TPC (Japan) HDPE KL272C is a non-hazardous high-density polyethylene resin. It is typically shipped in 25 kg bags or bulk containers, palletized and stretch-wrapped. Not regulated as dangerous goods for transport. Store in a cool, dry, well-ventilated area away from direct sunlight and ignition sources. |
| Storage | Store TPC (Japan) HDPE KL272C indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original containers closed, labeled, and palletized; prevent moisture, dust, and contamination. Avoid excessive stacking, prolonged UV exposure, and incompatible materials. Use appropriate containment for spills. Follow supplier SDS and local regulations. |
| Shelf Life | Shelf life: typically 24 months when stored in original packaging under cool, dry, ventilated conditions, away from direct sunlight and moisture. |
Returnable beverage crates and logistics trays molded from TPC Japan HDPE KL272C place simultaneous demands on melt flow length, crush resistance, and post-industrial regrind tolerance. Before tool transfer, the lot-specific melt flow rate is confirmed by ISO 1133-1:2022 at 190 °C under 2.16 kg; this value controls the pack/hold window in deep-ribbed tools. On a reciprocating-screw machine with screw diameter between 50 mm and 60 mm, the barrel profile is set from 180 °C in the feed zone to 220 °C at the metering zone, with the nozzle held at 210 °C. Mold temperature is controlled between 15 °C and 30 °C by turbulent water channels; a flow velocity above 2.5 m/s in baffle-drilled water lines reduces warpage in the base grid without embrittling the sidewall ribs. Packing pressure is maintained at 55–75 MPa until shot-weight stability of ±0.4% indicates frozen gates. Stacking verification follows ISO 12048; however, published data generated on KL272C crate prototypes remain limited, and initial tool trials should be designed to verify top-load retention at 40 °C for 28 days against the purchaser’s maximum gross load. Post-industrial regrind from sprues and rejected crates can be incorporated at 15–30 wt% only after regrind melt flow rate and sieve size distribution are re-certified, because shifts in molecular mass distribution may reduce environmental stress-cracking resistance at rib intersections.
In multi-cavity closure tools running KL272C, the maximum cavity count is not determined by plastication alone; gate aesthetics and thread ovality are controlled by core temperature, gate diameter, and demolding torque. Core cooling water entering at 10–15 °C with turbulent flow is used to set cap threads before ejection; if the core surface exceeds 20 °C at the moment of unscrewing, thread crest deformation can reduce sealing torque retention. Gate diameter at the external cap face is normally held between 0.8 mm and 1.2 mm. Smaller gates generate excessive shear heating and local melt fracture, visible as gate blush; larger gates may produce stringing and require longer hold to prevent sink marks opposite the gate pad. Torque retention is measured according to ASTM D2063 and compared with the closure brand owner’s specification after conditioning at 23 °C and 50% RH. For linerless cap sealing beads, a short-shot study at 95–98% fill confirms bead formation without overpacking the outer thread. If demolding torque on unscrewing cores exceeds available ejection capacity, a PE-carrier erucamide masterbatch may be used at 500–1,200 ppm active amide, but migration limits under EU 10/2011 must be re-evaluated for fat-containing food contact. Environmental stress-cracking resistance of the cap in detergent-based bottling line lubricants is assessed by ASTM D1693 condition A in 100% Igepal at 50 °C, though the result is a comparative indication rather than a direct prediction of failure on a carbonated beverage line.
Cold-fill dairy spread and food service containers can be injection molded from KL272C when the complete formulation is qualified under FDA 21 CFR 177.1520 and EU 10/2011. The food-contact status is not provided by the base resin alone; the selected color masterbatch, processing lubricant, and any regrind stream must be declared and migration-tested for the intended food simulant. For container walls between 0.8 mm and 1.2 mm, melt temperature is maintained between 200 °C and 230 °C, while injection velocity above 100 mm/s is normally required to fill the rim before freeze-off. Venting depth along the parting line is limited to 0.02–0.03 mm; deeper vents flash the sealing edge and shallower vents produce gas burns at the base of the container. Shrinkage is evaluated by molding plaques per ISO 294-4 using the standard test specimen geometry, then corrected for cavity thickness because production walls are thinner than the standard plaque. Anisotropic shrinkage between flow and cross-flow directions must be corrected in the rim and base gussets. If the tool uses hot-runner valve gates, the valve-pin delay is set to avoid weld-line displacement at the base, but published data for this specific configuration in KL272C food containers is limited and should be verified with short-shot series on the production tool.
Open-top industrial pails molded from KL272C are used for paints, water-based emulsions, and non-hazardous liquid products; when stacking loads exceed 200 kg, sidewall buckling and lid deflection become non-linear responses that cannot be extrapolated from standard tensile data. For a 20 L pail with a nominal wall thickness of 1.1–1.4 mm, static stack testing is frequently performed at 40 °C for 28 days with the closure in place, following the principles of ISO 12048 for filled transport packages. If the pail is intended for regulated dangerous goods, the package must undergo leakproofness, drop, and stack testing under ASTM D4919 or the applicable UN qualification protocol for plastics containers; a favorable result on one cavity geometry does not transfer automatically to another, and tool-specific verification is required. Handle lugs and lid retention beads should maintain a minimum radius of 0.5 mm to reduce notch stress concentration during cold drop at -18 °C. During molding, injection pressures above 80 MPa on large-diameter pails tend to introduce flow-induced molecular orientation that increases hoop strength but lowers sidewall dart impact after aging. Since published KL272C-specific data for UN-certified pails is limited, each new tool should be qualified with production-scale samples and not with laboratory-scale plaques alone.
| Application scenario | Key verification | Standard code | Test condition |
|---|---|---|---|
| Crates and logistics trays | Top-load and stack stability | ISO 12048 | 23 °C / 50% RH |
| Closures | Torque retention | ASTM D2063 | controlled application and removal |
| Food containers | Total migration | EU 10/2011 | simulant selection by food type |
| Industrial pails | Hazardous goods stack | ASTM D4919 | 40 °C, 28 days |
| Automotive washer reservoirs | Charpy notched impact | ISO 179-1/1eA | -30 °C |
| Thin-wall containers | Molding shrinkage | ISO 294-4 | standard plaque geometry |
Injection molded washer reservoir halves produced from KL272C are joined by hot-plate or vibration welding, making the weld line and the filler neck the controlling sites for low-temperature failure. Methanol-containing washer fluids at 30–50 vol% can act as environmental stress-cracking agents; relative ESCR screening is performed by ASTM D1693 condition A in 100% Igepal at 50 °C, but direct exposure testing in the actual fluid composition at 60 °C is required because the failure mechanism is fluid-specific. Notched Charpy impact on specimens cut across the weld line is measured according to ISO 179-1/1eA at -30 °C; unnotched drop impact of the complete reservoir assembly can be evaluated by ISO 6603-2 at the same temperature after conditioning. The molding process must avoid overpacking the gate area, because high residual stress at the injection gate lowers environmental stress-cracking resistance when the reservoir is exposed to repeated thermal cycling from -30 °C to 80 °C. Ultrasonic inspection of the weld zone is used to confirm bond continuity before fluid-fill testing at 1.5 bar internal pressure. Published data on KL272C welded reservoir shells is limited; seam strength should be established on production-welded parts rather than on injection molded plaques alone.
When KL272C is used for thin-wall containers with wall sections below 0.6 mm, short fills and flow marks are frequently misattributed to low melt temperature. High injection velocity, adequate venting, and machine hydraulic response determine flow length more than a 10–15 °C barrel adjustment. Injection speed at the screw is commonly set above 120 mm/s for thin-wall molds, with peak melt pressure at the machine nozzle typically in the range of 80–120 MPa. Venting depth along the flow path must remain between 0.015 mm and 0.025 mm; if venting is insufficient, gas compression at the end of fill generates burned regions even when melt temperature is raised. Residence time should be limited below 6 minutes at 230 °C, because prolonged exposure initiates thermo-oxidative chain scission that increases melt flow rate while reducing environmental stress-cracking resistance. Mold temperature in the 15–25 °C range is used for dimensional stability, but lower temperatures reduce gloss and may require higher injection pressure. Tool trials should use cavity pressure sensors to determine gate freeze rather than relying on timer-based hold; KL272C-specific published data in sub-0.6 mm flow channels is limited, so short-shot progression and gate-seal studies on the actual tool are mandatory.
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