| HS Code | 603920 |
| Productname | Dow HDPE 30460M |
| Chemicaltype | High Density Polyethylene |
| Density | 0.960 g/cm³ |
| Meltindex | 0.30 g/10 min at 190°C/2.16 kg |
| Meltingpoint | 130 °C |
| Vicatsofteningpoint | 126 °C |
| Tensileyieldstrength | 26 MPa |
| Tensilebreakstrength | 30 MPa |
| Elongationatbreak | 600% |
| Flexuralmodulus | 1100 MPa |
| Hardnessshored | 65 |
| Environmentalstresscrackresistance | >1000 h |
| Brittlenesstemperature | -70 °C |
| Thermalexpansioncoefficient | 1.2E-4 cm/cm/°C |
| Dielectricconstant | 2.3 |
| Volumeresistivity | >1E16 ohm·cm |
| Waterabsorption | <0.01% |
| Thermalconductivity | 0.45 W/m·K |
| Specificheat | 1.9 J/g·°C |
As an accredited Dow HDPE 30460M factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dow HDPE 30460M is typically packaged in 25 kg polyethylene bags or 1,000 kg bulk octabins for safe transport. |
| Container Loading (20′ FCL) | Dow HDPE 30460M resin is loaded into a 20-foot FCL container, palletized in bags, shrink-wrapped, and secured for safe ocean transport. |
| Shipping | Dow HDPE 30460M is a high-density polyethylene resin, non-hazardous and not DOT/IMDG/IATA regulated. It ships as pellets in bags, octabins, bulk trucks, or railcars. No UN number, hazard class, or packing group required. Store dry, away from heat, sunlight, and moisture; follow local transport rules. |
| Storage | Store Dow HDPE 30460M in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original containers or bags closed and palletized to prevent moisture, dust, and contamination. Avoid prolonged UV exposure. Do not stack excessively; ensure stable storage. Maintain clean, dry floors to prevent pellet slip hazards. Use first-in, first-out rotation. Consult the SDS and local regulations. |
| Shelf Life | Dow HDPE 30460M has a recommended shelf life of 24 months when stored dry, cool, and away from direct sunlight. |
| Standard | Technical designation | Relevant parameter | Application category |
|---|---|---|---|
| ISO 8611-1:2021 | Pallets for materials handling | Racking, compression, impact | Export and rackable pallets |
| ASTM D1185-24 | Standard test methods for pallets | Durability, load distribution | North American distribution |
| EU 94/62/EC | Packaging and packaging waste | Heavy metals 100 mg/kg | EU-bound pallets |
| REACH EC 1907/2006 | Article 67 restrictions | SVHC absence | Global industrial use |
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DOW HDPE 30460M is a high-density polyethylene injection-molding resin supplied as pelletized strand-cut material. The resin has a nominal density of 0.964 g/cm³ determined under ISO 1183-1 and a melt flow rate of 4.5 g/10 min measured at 190 °C with a 2.16 kg load under ISO 1133-1:2022. It is specified for rigid injection-molded articles such as open-top pails, industrial crates, tote boxes, trays, and transport containers in which top-load stiffness, impact resistance, and environmental stress cracking resistance are functional requirements.
| Property | Test method | Typical value |
|---|---|---|
| Melt flow rate, 190 °C/2.16 kg | ISO 1133-1 | 4.5 g/10 min |
| Density | ISO 1183-1 | 0.964 g/cm³ |
| Tensile yield stress, 50 mm/min | ISO 527-2 | 28 MPa |
| Tensile modulus, 1 mm/min | ISO 527-2 | 1250 MPa |
| Flexural modulus, 2% secant | ISO 178 | 1400 MPa |
| Notched Charpy impact, 23 °C | ISO 179-1/1eA | 5 kJ/m² |
| Vicat softening temperature, 50 °C/h | ISO 306/A50 | 127 °C |
| Environmental stress crack resistance, 10% Igepal, F50 | ASTM D1693 | 30 h |
| Shore D hardness | ISO 868 | 65 |
The tabulated values are laboratory typicals, not release specifications. Lot-to-lot variability occurs, and design verification should use the lot certificate of analysis against the end-use requirements. Density and melt flow rate are commonly used as incoming quality-control indicators because they reflect crystallinity and chain-length distribution, respectively.
On production-scale equipment, DOW HDPE 30460M is processed on conventional three-zone reciprocating-screw injection molding machines with a clamp force from 2000 kN to 8000 kN. Screws with an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.5:1 to 3.5:1 are normally used. The melt temperature window is 200 °C to 230 °C. Barrel zone settings are typically rear 180 °C, center 200 °C, front 210 °C, and nozzle 200 °C; these setpoints are adjusted to maintain the actual melt temperature within the specified window. Mold temperature ranges from 15 °C to 40 °C. Higher mold temperatures reduce frozen-in stress but lengthen cooling time; lower mold temperatures reduce cycle time but can increase flow-line visibility and residual stress near gates.
The resin is not hygroscopic. Pre-drying at 80 °C for 2 h is applied only when condensation or long outdoor storage has occurred. Melt residence time above 250 °C should be minimized to avoid oxidative degradation and yellowing. Shut-off nozzles are preferred to prevent drool during screw retraction. For hot-runner tools, externally heated manifolds with balanced channels are preferred; valve-gate sequencing should be based on mold-fill analysis.
The melt flow rate of 4.5 g/10 min is a single-point viscosity index. For accurate simulation of filling pressure and gate freeze-off, capillary rheometry data at 200 °C, 215 °C, and 230 °C over shear rates from 100 1/s to 1000 1/s is used. Apparent viscosity at 1000 1/s and 230 °C is lower than that of high-molecular-weight HDPE grades, which permits shorter filling times in multi-cavity tools but reduces melt strength during gate-stringing control.
Standard nitrided steel screws are acceptable because the grade contains no abrasive fillers or halogenated flame-retardant additives. A non-return valve with a flat seat and tight clearance should be maintained; shot-to-shot cushion stability below 2 mm prevents inconsistent packing. Clean internal regrind can be added at levels up to 20 wt% when the material is dried and free of contamination. Higher regrind levels increase melt-flow variability and should be evaluated by ISO 1133-1 before use.
Mold shrinkage for unfilled HDPE at a nominal wall thickness of 2 mm is typically 0.018 mm/mm to 0.025 mm/mm, measured after 24 h at 23 °C following ISO 294-4. Tool designers use these values for initial cavity sizing; prototype measurements are required because shrinkage varies with packing pressure and gate freeze-off.
The density of 0.964 g/cm³ places DOW HDPE 30460M at the upper end of the injection-molding HDPE density range. Higher density increases flexural modulus and top-load rigidity because crystallinity is increased. The corresponding trade-off is a reduction in environmental stress cracking resistance, since lower comonomer content and higher crystallinity reduce the tie-molecule population that delays crack growth. Compared with a lower-density injection grade near 0.955 g/cm³, DOW HDPE 30460M typically shows a higher flexural modulus under ISO 178 and a lower ESCR F50 under ASTM D1693.
Compared with higher-flow HDPE injection grades with melt flow rates above 10 g/10 min, DOW HDPE 30460M retains better notched impact and ESCR, but its thin-wall fill capability is lower. For wall sections below 1.0 mm, a higher-flow grade may be necessary; DOW HDPE 30460M is better suited to wall thicknesses of 1.5 mm and above in stackable containers where top-load resistance is more important than extreme thin-wall penetration.
Compared with high-molecular-weight HDPE grades used for extrusion blow molding, DOW HDPE 30460M has substantially lower melt strength and is not intended for parison formation. The resin is specifically formulated for injection molding and should not be processed on blow-molding or film lines.
In multi-cavity pail and crate tools, the processing boundary is controlled by gate freeze-off, cavity pressure drop, and ejection stiffness. For open-top pails with a flow length of 150 mm and wall thickness of 1.5 mm, a starting screw forward speed of 20 mm/s to 40 mm/s is used; actual mold-fill time is 0.8 s to 1.5 s. Holding pressure is set at 50 MPa to 70 MPa with hold time adjusted until gate seal. Cooling time for this wall thickness is commonly 8 s to 15 s, depending on mold temperature and water-line design.
Mold temperatures below 15 °C may produce surface flow lines and high residual stress; mold temperatures above 40 °C may extend cycle time and increase the risk of ejection sticking if core draft angles are insufficient. Differential shrinkage between cavity and core can produce sidewall warpage; core-to-cavity mold temperature differences should therefore be kept below 10 °C for close-tolerance cylindrical parts.
Sink marks opposite ribs and bosses are controlled by increasing packing pressure or reducing demolding temperature. Warpage is addressed by reducing the mold temperature difference between cavity and core, not by increasing melt temperature, because excessive melt temperature accelerates degradation and may lower impact performance.
ESCR becomes the controlling requirement when containers are exposed to surfactants, detergents, mineral oils, or cleaning agents under structural load. The F50 value from ASTM D1693 is a comparative screening test and is not a direct service-life prediction. Molded-in stress at gates, ejector marks, and sharp corners can reduce the effective ESCR of the final part below the plaque value. To preserve the resin’s ESCR, the tool should avoid restrictive pinpoint gates, ejector marks should be shallow and located away from high-tensile-stress regions, and sharp internal corners should be replaced by radii of at least 0.5 mm to 1.0 mm.
Published data for specific chemical environments is limited. When the container is intended for transport of dilute surfactant solutions above 40 °C, chemical resistance testing under stack load is required before specifying DOW HDPE 30460M. Test coupons cut from molded pails near the gate and near the sidewall may show different ESCR values; both locations should be examined because gate-area frozen-in stress is higher.
DOW HDPE 30460M is supported by food-contact compliance documentation for olefin polymers. The resin can be evaluated under 21 CFR 177.1520 for food-contact uses and under Commission Regulation (EU) No 10/2011, subject to migration testing with the intended food simulant and time-temperature conditions. Compliance is not automatic for all end uses; the final article’s surface-to-volume ratio, processing history, and contact duration determine the applicable migration limits. The supplier should be consulted for specific lot-level food-contact certificates.
REACH registration obligations under EC No 1907/2006 apply to the supplier. RoHS restrictions may be relevant for electronic packaging applications. If recycled or externally sourced regrind is added to the process, the resulting formulation must be re-evaluated for food-contact and regulatory status.
For transport containers used in cold-room logistics at temperatures down to -20 °C, the notched impact performance of DOW HDPE 30460M under ISO 179-1/1eA should be verified on molded sidewall specimens, because impact values from compression-molded plaques do not fully represent gate-area frozen-in stress in a pail.