| HS Code | 336584 |
| Product | Hanwha HDPE 8380 |
| Material Type | High Density Polyethylene (HDPE) |
| Density | 0.958 g/cm³ |
| Melt Flow Rate | 0.08 g/10 min (190°C/5 kg) |
| Tensile Strength At Yield | 25 MPa |
| Elongation At Break | >600% |
| Flexural Modulus | 1,100 MPa |
| Vicat Softening Point | 125°C |
| Brittleness Temperature | <-70°C |
| Environmental Stress Crack Resistance | >1,000 h |
| Carbon Black Content | 2.0-2.5 wt% |
| Oxidation Induction Time | >20 min |
| Pipe Grade | PE100 |
As an accredited Hanwha HDPE 8380 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Hanwha HDPE 8380 is supplied in 25 kg polyethylene-lined woven bags, palletized, with 40 bags per 1,000 kg pallet. |
| Container Loading (20′ FCL) | A 20′ FCL container loaded with Hanwha HDPE 8380 high-density polyethylene, 25 kg bags, palletized, shrink-wrapped, secured for ocean transport. |
| Shipping | Hanwha HDPE 8380 is a non-hazardous high-density polyethylene resin shipped as solid pellets in 25 kg bags, jumbo bags, or bulk liner trucks/containers. Store in a cool, dry, ventilated area away from sunlight, heat, and moisture. Standard freight applies; avoid package damage. Handle per SDS. |
| Storage | Store Hanwha HDPE 8380 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizing agents. Keep original bags or containers sealed, off the floor, and protected from moisture, dust, and contamination. Avoid excessive stacking or physical damage. Use first-in, first-out stock rotation. Maintain a clean handling area and follow local regulations and the safety data sheet. |
| Shelf Life | Hanwha HDPE 8380 shelf life: indefinite when stored unopened in original packaging, protected from direct sunlight, heat, and moisture. |
In thin-wall injection moulded dairy cups, margarine tubs, and single-serve food containers with nominal wall thickness from 0.35 mm to 0.60 mm, the processing window for Hanwha HDPE 8380 is governed by the interaction between fast crystallisation kinetics and the filling-pressure drop across the cavity. The melt-flow rate of 38 g/10 min under ISO 1133-1:2022 permits short injection times in multi-cavity stack tools, but the same flow class demands rigorous velocity profiling to avoid jetting at sub-runner transitions and flow hesitations at thin ribs. Melt temperature should be held between 190 °C and 230 °C, with mould temperature maintained at 15 °C to 30 °C through turbulent-flow conformal cooling circuits, because the high-density polyethylene matrix solidifies rapidly once the frozen-layer fraction exceeds approximately 20% of the cavity thickness. Published data for this specific configuration is limited; however, production-scale observations on similar high-flow HDPE grades indicate that melt temperature exceeding 240 °C for more than 5 min residence time can generate oxidation-related black specks and odour-active short-chain carbonyl compounds that are unacceptable for fatty food contact. Injection velocity should be set against a velocity-to-position profile rather than a single fixed speed, with initial filling velocities in the range of 80 mm/s to 150 mm/s depending on gate geometry and flow-length-to-wall-thickness ratio. Holding pressure between 50 MPa and 70 MPa is typically required to compensate for post-filling shrinkage without creating gate blush. Compliance for fatty food simulants under EU 10/2011 requires overall migration below 10 mg/dm² when tested with 3% w/v acetic acid, 20% v/v ethanol, and vegetable oil or 95% v/v ethanol according to EN 1186-1. Under FDA 21 CFR 177.1520(c), the olefin polymer must meet density and extractables limitations for non-alcoholic and alcoholic food-contact articles, and the converter must document that the stabiliser package is cleared for the intended food type.
| Wall thickness range | Melt temperature | Mould temperature | Hold pressure | Drying requirement |
|---|---|---|---|---|
| 0.35 mm–0.60 mm | 210 °C–230 °C | 15 °C–25 °C | 50 MPa–70 MPa | Surface moisture below 0.05% |
| 0.70 mm–1.50 mm | 190 °C–220 °C | 10 °C–30 °C | 40 MPa–60 MPa | Surface moisture below 0.05% |
| 2.00 mm–3.00 mm | 180 °C–210 °C | 10 °C–25 °C | 35 MPa–50 MPa | No pre-drying unless condensation is visible |
In beverage closure tools with 96 to 128 cavities producing 28 mm PCO 1881 or 38 mm neck finishes, the high spiral-flow length of Hanwha HDPE 8380 reduces peak injection pressure but also increases the risk of flash if parting-line maintenance is not tightened to the material’s low-viscosity fill behaviour. The tamper-evident band, often moulded at 0.15 mm to 0.25 mm nominal wall, is the controlling dimension for fill consistency; valve-gate timing must be sequenced so that the band fills before the main closure panel reaches final packing. Gate diameters between 0.6 mm and 1.0 mm are commonly used, with short nozzle-to-gate flow channels and no dead spots to prevent material stagnation. Screw L/D ratios of 20:1 to 24:1 and compression ratios of 2.0:1 to 2.5:1 are appropriate for this melt-flow class. Residence time at 200 °C to 220 °C should be kept below 8 min to avoid shifting the MFR beyond its specified tolerance under ISO 1133-1:2022. The bridge structures connecting the tamper-evident band to the closure skirt are critical stress-concentration points; slit-bridge cracking under top-load conditions can be evaluated with drop-impact testing according to ISO 7765-1 or tensile testing of moulded plaques under ISO 527-2:2012. Environmental stress cracking resistance in closure applications is sensitive to detergent and sanitising agents used on filling lines; screening should be performed using ASTM D1693 Condition B with 100% Igepal CO-630, although published data specific to this configuration is limited because ESCR is strongly influenced by mould cooling rate and gate orientation. Mould temperature for closures is typically held at 10 °C to 20 °C to freeze the thin band quickly and prevent ovality, while post-mould dimensional checks should reference ISO 294-3 for shrinkage and ISO 291 standard conditioning atmosphere.
For returnable distribution crates, folding storage bins, and small logistics totes, Hanwha HDPE 8380 is constrained by the inverse relationship between melt-flow rate and environmental stress crack resistance. The material’s high-throughput injection properties reduce fill pressure in deep-ribbed sidewalls, but the same molecular architecture lowers resistance to slow crack growth when long-term tensile stress is applied in the presence of detergent residues or condensed humidity. Any stacking load specification must be derived from ISO 899-1 tensile creep testing at 40 °C or 60 °C and not from short-term flexural modulus alone. The short-term flexural modulus of comparable high-flow HDPE grades is often reported in the range of 800 MPa to 1,100 MPa under ISO 178:2019, but this value does not predict creep deflection in a loaded crate stored in a warehouse at elevated ambient temperature. The load-bearing rib pattern should be designed so that the maximum calculated compressive stress in the sidewall does not exceed 4 MPa to 6 MPa under continuous load if long service life is required; published data for this specific Hanwha grade under constant tensile load conditions are limited, and processors must generate in-house creep curves before rating crates for stack heights above 2 m. Impact toughness at low temperature is a further boundary condition: notched Charpy impact testing according to ISO 179-1:2010 or notched Izod testing under ISO 180:2000 should be performed on specimens cut from the actual sidewall because rapid crystallisation in thick sections can produce lower impact values than moulded plaques. The use of regrind is permitted only when the percentage of post-industrial reprocessed material is kept below 20% by mass and the MFR shift under ISO 1133-1:2022 is recorded on each batch to prevent excessive viscosity reduction. External exposure requires a carbon black or hindered amine light stabiliser package; unpigmented HDPE 8380 should not be specified for prolonged outdoor UV exposure beyond 500 h under ASTM G154 Cycle 1 without weathering data.
A four-cavity storage crate tool running a 2+2 hot-to-cold runner split will show consistent part mass only if hold-pressure transfer is set against screw cushion, not timer. In this configuration, the first-stage filling speed is increased until the cavity-pressure rise at the end of fill becomes detectable through transducer curves, then the second-stage holding pressure is lowered to the minimum that suppresses sink marks on the bottom grid. Because the high melt-flow rate of HDPE 8380 enables lower injection pressure, the check ring must seal within 1 mm of screw position to avoid inconsistent shot weight. Mould temperature for open-crate geometries is normally set at 15 °C to 25 °C and the cycle is controlled by handling demoulding when the part reaches a surface temperature below 80 °C. Demoulding draft angles of 1.5° to 2.5° are recommended for textured sidewalls because the rapid crystallisation of this grade can increase ejection friction. For food-contact crates used in meat or dairy logistics, the finished article must be tested under EU 10/2011 with the actual food simulant, because mould release agents and external lubricants can alter overall migration and organoleptic properties. Cleaning validation for returnable crates should include repeated exposure to 0.5% sodium hydroxide solution at 60 °C for 30 min, followed by visual inspection for environmental stress cracking under ASTM D1693 or a bending-failure screening method.
The injection moulding of industrial pails and open-top containers from Hanwha HDPE 8380 is limited to non-aggressive contents and to wall sections where drop impact dominates over long-term chemical exposure. Pail bodies of 5 L to 25 L nominal capacity require the seal ring area to be packed sufficiently to prevent ovality below 0.5 mm across the diameter, because lid gasket seating and closure integrity are controlled by roundness at the rim. The high melt-flow rate reduces filling pressure in the seal-ring zone, but it also increases the risk of sink marks below the rim if the part is packed too early. Holding pressure should be applied only after the flow front has passed the rim, with a profile that decays from 60 MPa to 30 MPa over 2 s to 4 s. Drop testing for dangerous goods packaging is governed by the UN Recommendations on the Transport of Dangerous Goods, Model Regulations, Chapter 6.1.5, with conditioning at −18 °C for plastic packagings intended for liquids. Stacking tests under ISO 2234:2000 and leakproofness tests under ISO 16467:2003 must be performed on the finished article with the intended closure system. Impact failure in a pail body often initiates at the injection gate, especially when the gate diameter is below 1.5 mm; valve gates or submarine gates should be positioned away from the bottom corner radius. Mould cooling in the rim area should be designed for a mould temperature of 10 °C to 20 °C to suppress warpage, while the sidewall runs at 20 °C to 30 °C to allow adequate impact crystallinity. Published data for this specific grade in UN-certified pail configurations is limited; qualification requires batch-specific drop, stack, and leakproofness testing because high-flow HDPE grades differ in impact behaviour from conventional pail-grade polyethylene. Chemical compatibility screening should follow ASTM D543 immersion testing for the intended filling liquid, and aggressive oxidising agents should be excluded because high-flow HDPE can exhibit reduced stress crack resistance relative to low-melt-flow blow moulded alternatives.
Because toy and juvenile product components are classified by mouth-contact probability rather than material volume, Hanwha HDPE 8380 can be used only after the finished article meets the applicable element migration limits and organic chemical restrictions. Under EN 71-3:2019+A1:2021, the material falls within Category III when it is not likely to be mouthed heavily but remains subject to migration limits for 19 elements; typical controlling values include lead below 160 mg/kg, cadmium below 17 mg/kg, and mercury below 94 mg/kg in the dried test portion. The relevant analytical methods for migration are specified in EN 71-3 and require particle size reduction below 0.5 mm and acid extraction under defined time-temperature conditions. For the United States, the applicable framework is the Consumer Product Safety Improvement Act, with phthalate restrictions in Section 108 and total lead content limits under 16 CFR 1303. The moulding process itself must be documented to prevent contamination from external lubricants or colourants that are not cleared for toy-contact use. Because HDPE 8380 is often coloured with custom masterbatch, each masterbatch component must be evaluated under EU 10/2011 if the toy is also food-contact or under EN 71-9 for organic chemical requirements. Thermal-oxidative stabilisers in the base resin must not contain substances listed in the REACH Candidate List of substances of very high concern above the communication threshold of 0.1% by mass. The small-part test under ASTM F963 or EN 71-1 remains a geometric requirement, but material ductility influences breakage mode when a component is dropped from the prescribed height. Notched impact testing should be performed on finished-component samples under ISO 179-1:2010 at −20 °C to verify that the grade does not become brittle in cold climates. The table below summarises the compliance matrix for toy-bound HDPE 8380.
| Application boundary | Applicable regulation | Analytical method | Controlling value |
|---|---|---|---|
| Element migration | EN 71-3:2019+A1:2021 | Acid extraction and ICP-MS | Lead 160 mg/kg, cadmium 17 mg/kg |
| Organic chemical safety | EN 71-9 | Solvent extraction | Substance-specific limits |
| Lead in surface coating | 16 CFR 1303 | CPSC-CH-E1003-09.1 | Lead 90 mg/kg |
| Phthalates | CPSIA Section 108 | CPSC-CH-C1001-09.3 | 0.1% per restricted phthalate |
| RoHS | Directive 2011/65/EU Annex II | IEC 62321-5 | Lead 1,000 mg/kg, cadmium 100 mg/kg |
Once cold-chain returnable totes are exposed to repeated high-humidity defrost cycles, the practical performance limit of Hanwha HDPE 8380 is defined by condensation-driven stress cracking at ribs and by impact retention after sub-zero conditioning. These totes are commonly injection moulded with wall thicknesses from 1.5 mm to 3.0 mm, and the high melt-flow rate permits filling of deep corner ribs without excessive clamp pressure. However, the same molecular structure may exhibit reduced low-temperature impact toughness when compared with medium-flow HDPE grades, so notched Charpy data under ISO 179-1:2010 at −20 °C should be generated from actual sidewall sections rather than from standard flat plaques. Mould temperature for cold-chain totes is often raised to 25 °C to 35 °C to improve impact strength and reduce frozen-in orientation, but this increases cycle time and can raise warpage if the cooling layout is uneven. The part should be designed with a minimum radius at the intersection of the sidewall and bottom of 2 mm to avoid a notch that accelerates crack initiation under repeated stacking loads. If the tote is to be washed in industrial tunnel washers, the detergent concentration, wash temperature, and drying temperature must be validated by immersion testing under ASTM D543 and by environmental stress cracking screening under ASTM D1693 Condition B. Published data specific to HDPE 8380 in this cold-chain configuration is limited because the stress crack response depends strongly on the colour concentrate, regrind fraction, and cooling rate; a production trial with 100 cycles of wash-and-freeze exposure is the only reliable qualification route for long-return logistics programmes.
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Hanwha HDPE 8380 is a high-flow homopolymer injection molding grade within the high-density polyethylene portfolio. The manufacturer’s published datasheet lists a nominal density of 0.957 g/cm³ under ISO 1183-1:2019 and a nominal melt flow index of 8.0 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg. The combination of high density and high melt flow index places the grade in the stiff, fast-cycling segment of HDPE: it flows sufficiently to fill thin-wall sections, but the lower molecular weight associated with high melt flow reduces environmental stress crack resistance compared with lower-flow blow molding and pipe grades. Typical application fields specified by the producer include industrial pails, transport crates, housewares, thin-wall food packaging, caps and closures, and small appliance components requiring high modulus and low warpage. The 8380 suffix is a supplier designation and should not be treated as a direct specification value; release testing against the lot certificate of analysis is required before tooling validation.
For structural part design, the mechanical property set includes tensile yield stress near 27 MPa under ASTM D638, flexural modulus near 1,100 MPa under ISO 178:2019, notched Izod impact near 4 kJ/m² at 23 °C under ASTM D256, and elongation at break above 500%. Heat deflection temperature under ASTM D648 at 0.455 MPa is typically reported near 75 °C, and Vicat softening point under ASTM D1525 is near 125 °C. These values should be used only for comparative screening; long-term creep predictions require time-dependent data under ISO 899-1:2003, for which published data on this specific grade are limited.
On 350-tonne toggle-clamp injection molding machines equipped with 40 mm diameter reciprocating screws at L/D 22, the resin’s viscosity permits barrel settings between 200 °C and 240 °C, with the feed zone typically maintained 10 °C to 15 °C below the nozzle zone. Mold temperatures from 20 °C to 50 °C are sufficient for dimensional stability; chilled water at 8 °C to 15 °C is applied when cycle-time targets fall below 8 s for thin-wall lids. Hydraulic back pressure between 5 bar and 15 bar is sufficient to maintain shot weight consistency without excessive shear heating. At screw surface speeds above 80 m/min on a 40 mm screw, melt temperature can rise by more than 5 °C; this condition has been observed as flash and burn streaks in multi-cavity hot runner tools when the injection unit is undersized relative to shot volume. The material does not require pre-drying at ambient relative humidity below 50%, but outdoor silos in high-humidity monsoon service have yielded surface condensation that causes gate splay. In such cases, a dehumidified air source with a dew point of −40 °C or lower should be connected to the hopper inlet.
Residence time is a controlling constraint on injection units with large shot capacity relative to part weight. On 250-tonne hydraulic machines with 35 mm diameter L/D 20 screws, shot mass below 30% of barrel capacity has produced melt residence times above 8 min during high-cavitation production. Long residence time promotes chain extension and viscosity increase, causing mid-run part weight drift. Shot mass between 40% and 60% of barrel capacity is recommended. The hopper throat should be water-cooled to prevent pellet bridging; bridge formation at the throat is a recurrent failure mode in humid plants when chilled water lines are routed near the feedthroat and condensation enters the hopper.
Thin-wall container molders running HDPE 8380 in four-cavity valve-gated hot runner systems should analyze the fill phase as pressure-limited rather than velocity-limited. On tools with flow length-to-wall thickness ratios above 200:1, injection pressure at the transfer point can reach 700 bar to 1,000 bar on accumulator-equipped machines. Gate diameters below 0.8 mm generate shear rates above 50,000 s⁻¹; local viscous heating at those shear rates can depress viscosity and destabilize the flow front, producing core displacement and wall-thickness variation. Hold-pressure control is therefore more critical than injection speed for this grade. Premature release of hold pressure before gate freeze creates sink marks; excessive hold pressure increases frozen-in stress and warpage. Mold shrinkage measured on plaques under ASTM D955-08 is typically reported in the range of 1.5% to 2.0% in the flow direction. Published data for highly filled tool-specific thin-wall geometries with rapid cooling are limited and should not replace tool-specific measurement.
Cold runner sizing for HDPE 8380 should follow high-flow HDPE practice: full-round runners with diameters between 6 mm and 8 mm for multi-cavity layouts, coupled with a heated sprue bushing to reduce gate stringing. Submarine gate diameters between 0.8 mm and 1.2 mm provide clean shear-induced break with acceptable pressure loss; gate diameters below 0.8 mm freeze too early in high-flow material, while diameters above 1.5 mm leave excessive vestige on visible surfaces.
Differentiation from lower-flow HDPE grades is most clearly seen in melt viscosity and environmental stress crack resistance. A low-flow blow molding HDPE with MFR near 0.35 g/10 min has a melt viscosity roughly one order of magnitude higher than HDPE 8380 under comparable shear stress. High-flow HDPE of this type is therefore not suitable for extrusion blow molding or pipe applications that require high parison melt strength or long-term hydrostatic strength under ISO 9080. Conversely, HDPE 8380 reduces injection fill pressures and shortens cycle time in thin-wall molds. The trade-off appears in constant-strain environmental stress crack resistance measured under ASTM D1693: high-flow HDPE homopolymers typically display single-digit to low-double-digit hours in Igepal CO-630 at 50 °C, while lower-flow blow molding grades often exceed 100 h in the same test. Published head-to-head ESCR data for Hanwha HDPE 8380 against all adjacent grades are limited in public literature; the stated relationship is therefore based on the general behavior of high-density ethylene homopolymers. Compared with polypropylene copolymers of similar nominal MFR, HDPE 8380 has higher density, higher flexural modulus, and lower heat deflection temperature. Retort or hot-fill applications above 100 °C should not be designed around this grade without supplementary heat deflection data from ASTM D648 or dynamic mechanical analysis.
The grade’s impact response shows a pronounced temperature transition. Notched Izod impact at 23 °C under ASTM D256 is typically near 4 kJ/m²; at −20 °C the failure mode shifts from ductile to brittle because the beta transition lies below the test temperature. Published data for Hanwha HDPE 8380 at negative test temperatures are limited, but homopolymer HDPE generally loses more than 50% of room-temperature impact resistance by −20 °C. Therefore, gate location should be placed away from corner radii and snap-fit undercuts, and weld-line positions should not be located in load-bearing sections. Weld-line strength in unfilled HDPE is retained at approximately 50% to 60% of nominal values when tensile bars are tested under ASTM D638.
Incoming lot inspection should include melt flow index by ASTM D1238 or ISO 1133-1:2022, density by ASTM D1505, and visual inspection for foreign black specks. Contamination from wood splinters and film backing from pallet wrapping is a documented production-line failure mode because it plugs small gate tips and can produce short shots in multi-cavity molds. For export product lines, establish a retained sample program and run differential scanning calorimetry to confirm the melting range before full lot release.
Regulatory documentation for the neat resin is supplied in the producer’s product stewardship summary and must be re-verified for each export destination. The uncolored base resin is positioned for food-contact applications under FDA 21 CFR §177.1520(c) 3.1a for olefin polymers. Under Regulation (EU) No 10/2011, the final article must respect an overall migration limit of 10 mg/dm² for plastic materials intended for food contact. Because these determinations apply to the base resin and not to the final article, color concentrates, slip agents, and processing aids must themselves comply with the same migration and residual-content framework. Incompatibilities have been observed when amine-based stabilizer packages and certain organic peroxide-driven crosslinking additives are compounded into the melt; the interaction can shift oxidative induction time and alter melt viscosity. Under RoHS Directive 2011/65/EU, the resin does not contain intentionally added lead, mercury, cadmium, hexavalent chromium, polybrominated biphenyls, or polybrominated diphenyl ethers above the prescribed thresholds. For materials requiring REACH documentation under EC 1907/2006, the supplier provides a statement of supported use and SVHC content below 0.1 wt% per lot.
| Regulation | Designation | Verification condition |
|---|---|---|
| U.S. food-contact olefin polymer | FDA 21 CFR §177.1520(c) 3.1a | Applies to uncolored base resin; final-article migration is the converter’s responsibility |
| EU food-contact plastics | Regulation (EU) No 10/2011 | Overall migration limit 10 mg/dm²; specific migration limits apply to additives |
| REACH | EC 1907/2006 | SVHC content below 0.1 wt% lot-specific documentation |
| RoHS | Directive 2011/65/EU | No intentionally added restricted substances |
Storage of the resin in outdoor silos is acceptable if the silo wall temperature remains below 50 °C and the headspace is purged with dry air. Bagged resin should be kept off concrete floors and away from direct sunlight to prevent condensation and pellet degradation. Reprocessing of hot-runner scrap is typically limited to 20 wt% with neither measurable shift in melt flow index nor loss of tensile yield stress; 100% regrind operation has been associated with viscosity increase and part-weight drift because of oxidative chain extension during repeated heating. In multi-material molding with thermoplastic elastomers, adhesion to HDPE 8380 is weak unless a tie layer or mechanical interlock is designed into the part. No solvent-bonding system is recommended for this resin because of the nonpolar polyolefin surface.
When high-speed closures are molded in high-cavitation tools with cycle times below 5 s, the thermal diffusivity of HDPE 8380 becomes a dominant constraint. The crystalline melting range is approximately 130 °C to 135 °C; demolding before the surface cools below this range can cause ejection pin penetration and ovality. On tools with 24 or more cavities, cavity-to-cavity temperature control must be held to ±2 °C to maintain consistent gate freeze and seal dimensions. Chilled water circuits are configured in counterflow around each cavity rather than in a single series loop; series-loop configurations have shown a 3 °C to 5 °C temperature gradient from inlet to outlet, producing cavity weight variation and inconsistent closure dimensions. Hot runner systems with valve gates should maintain manifold temperatures of 220 °C to 230 °C and drop temperatures of 210 °C to 220 °C. Manual or raise/lower hot runner controllers must be tuned for the low melt viscosity of this grade; an uncalibrated controller can create gate freeze-off and cold slugs. These boundaries are not unique to HDPE 8380, but they are sharpened by its high melt flow index and high crystallinity.