Dow Hdpe 30460m

Dow HDPE 30460M

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    Specifications
    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 & Storage
    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.
    Application of Dow HDPE 30460M
    Within automated filling operations for 20 L to 25 L open-head pails, Dow HDPE 30460M is processed at melt temperatures of 210 °C to 240 °C with a mould surface temperature held between 20 °C and 35 °C. The converter-level formulation is typically 96.0–98.0 wt% HDPE 30460M, 2.0–4.0 wt% UV-stabiliser masterbatch, and the balance as colour or antistatic concentrate, depending on whether the pail is intended for solvent-borne or combustible-product filling. Injection moulding is performed on clamp-force platforms of 900–1800 tonnes using single-flight polyolefin screws with L/D ratios of 22:1–24:1 and compression ratios of 2.8:1–3.2:1. The primary production-scale failure modes are gate blush around the lid-seat ring, weld-line porosity at the handle lugs, and post-mould ovality exceeding 1.5 mm on the top ID. Ovality is controlled by holding pressure profiles of 50–70 MPa and cooling time ratios above 1.2 s/mm of nominal wall. Compliance for dangerous-goods packaging requires conformance to UN Model Regulations Chapter 6.1, ADR/RID/IMDG Code requirements, and 49 CFR 178.504 where applicable, supplemented by EU 94/62/EC heavy-metal limits of 100 mg/kg aggregate for cadmium, lead, mercury, and hexavalent chromium. Food-contact pails fall under FDA 21 CFR 177.1520 and EU Regulation 10/2011 overall migration limits. Terminal products include UN-marked open-head pails, tamper-evident lid-and-spout assemblies, and stackable paint/coating containers in the 5 L to 25 L range. Continuous service above 65 °C and aggressive aromatic or halogenated hydrocarbon fills are outside the resin’s operational boundary because environmental stress cracking occurs at high hoop stress and elevated temperature.

    What Limits Injection Speed in Thin-Wall Storage Containers?

    For food-contact drawer organisers, stackable household units, and freezer trays with nominal wall thickness of 0.8 mm to 1.2 mm, the limiting process variable is not melt temperature but acceleration time of the injection unit. On a 450-tonne high-speed toggle press with a 4-cavity stack mould, cycle times of 6–9 s are achieved when the injection velocity exceeds 300 mm/s and the holding pressure is set between 35 MPa and 50 MPa. The formulation is 98.0–99.5 wt% HDPE 30460M, 0.5–2.0 wt% food-approved colour concentrate, and 0.1–0.3 wt% slip additive masterbatch, with the slip package adjusted only after sensory evaluation of fat-containing simulants because excess erucamide can raise hexane extractables. Melt temperature is maintained at 215–230 °C, mould temperature at 10–25 °C, and back pressure at 5–10 MPa to avoid trapped volatile degradation products. Compliance for cold-contact and room-temperature food storage relies on EU Regulation 10/2011, including overall migration below 10 mg/dm², FDA 21 CFR 177.1520(c) 2.1, and EC 1935/2004. Migration testing follows EN 1186-1 with 3% acetic acid, 10% ethanol, and vegetable oil or isooctane substitutes. Terminal products include thin-wall refrigerator boxes, stackable pantry containers, and low-temperature storage trays. The resin is not recommended for repeated high-temperature dishwasher cycles above 65 °C or for retort applications because dimensional distortion and oxidative embrittlement occur under sustained hot-water exposure.

    Logistics Crate Regrind and the 25% Post-Consumer Recyclate Threshold

    Logistics crate production operates at the intersection of large-part injection moulding and regrind-induced viscosity shift. A compounding formula containing 70–80 wt% virgin HDPE 30460M and 20–30 wt% clean post-consumer bottle-grade HDPE regrind is used for collapsible boxes, vented produce crates, and beverage-bottle return crates. The regrind is pre-dried at 80 °C for 2–4 h whenever storage relative humidity exceeds 60%, because moisture above 0.05 wt% produces silver streaking and weld-line delamination. Moulding uses sequential valve-gated hot-runner systems on clamp-force platforms of 1200–2500 tonnes, with melt temperatures of 220–250 °C and mould temperatures of 20–35 °C. Injection pressure at the gate is held between 70 MPa and 110 MPa to ensure packing through ribs and hinge bosses. The main batch-to-batch variable is not average melt flow but the low-molecular-weight tail of the recycled fraction; when regrind melt flow exceeds 0.8 g/10 min to 1.2 g/10 min above virgin value, side-wall sag and inconsistent hinge geometry appear. Compliance for industrial distribution crates references ISO 17855-1:2016 and ASTM D4976 for polyethylene moulding and extrusion materials, EU 94/62/EC for packaging heavy metals, and RoHS Recast 2011/65/EU where crates carry electronic traceability tags. Food-produce crates additionally require EC 2023/2006 GMP compliance and migration testing under EU 10/2011. Terminal product sizes range from 600 mm × 400 mm standard euro crates to 1200 mm × 1000 mm collapsible distribution boxes. Long-term stacking at temperatures above 55 °C causes creep deformation, and post-consumer regrind loads above 30 wt% degrade drop impact strength at -20 °C.When a monolayer dairy cap is required to pass sensory panel evaluations, a torque-retention test after 48 h at 23 °C, and a leak test at 0.1 bar internal pressure, the resin’s organoleptic neutrality and low extractables become primary acceptance criteria. The closure formulation is 97.5–99.0 wt% HDPE 30460M, 0.05–0.15 wt% nucleating masterbatch for cycle-time reduction, 0.1–0.2 wt% slip additive, and 1.0–2.0 wt% colour concentrate matching processor-specific dosing limits. High-cavitation moulds of 64–128 cavities are used with hot-runner tip temperatures of 230–260 °C, melt temperature of 225–250 °C, and mould temperature of 15–30 °C. The tamper-evident band is formed through a slit ring gate, and post-mould cooling is applied to stabilise band geometry before ejection. Observed production rejects include incomplete cut-slit formation, sink marks on the cap crown when holding pressure falls below 40 MPa, and stress whitening when mould temperature is too low for the crystallisation rate of the nucleated formulation. Compliance for closure systems includes EU 10/2011 migration testing with milk simulants, FDA 21 CFR 177.1520, EC 1935/2004, and sensory evaluation under EN 1622 for packaging intended for drinking water. Terminal products include dairy cream caps, sterile water closures, oral-care flip-top caps, and low-pressure trigger-spray shrouds. Melt temperatures exceeding 260 °C cause molecular weight reduction and a fall in bridge-formance impact resistance, so hot-runner balancing must be verified at every colour change to avoid local overheating.

    Pallets Produced from HDPE 30460M Require Structural-Foam Processing Discipline

    Replacement of wooden stringers in export pallets with injection-moulded HDPE requires control of two variables that are normally ignored in solid moulding: blowing-agent dispersion and gas counterpressure in the cavity. The formulation for low-pressure structural-foam pallets is 75–85 wt% virgin HDPE 30460M, 15–25 wt% clean post-industrial HDPE regrind, 2–3 wt% UV-stabiliser masterbatch, and 0.5–1.0 wt% chemical blowing agent or the equivalent nitrogen gas-injection setting. Processing is performed on 2000–4500 tonne clamp-force low-pressure machines with shot weights of 15–25 kg, melt temperatures of 215–235 °C, mould temperatures of 25–45 °C, and gas counterpressure of 0.2–0.6 MPa during filling. The core transition is regulated by holding pressure decay rather than a fixed switchover point, because premature holding pressure at > 30 MPa collapses the cellular core and increases part mass without improving load-bearing performance. Cooling time ranges from 90 s to 180 s depending on wall sections under the pallet feet and the solid skin thickness target of 1.5–2.5 mm. The dominant production failure mode is surface splay from blowing-agent decomposition before the melt front reaches the vapour pressure threshold; uncontrolled loading above 1.0 wt% also produces internal void convergence that cuts flexural modulus by 15–20% compared with a homogeneous skin-core profile. Compliance for pallet performance references ISO 8611-1:2021 for test methods and load classifications and ASTM D1185-24 for pallet and related structures, while environmental compliance uses REACH Regulation EC 1907/2006 and EU 94/62/EC heavy-metal limits. The table below documents the principal compliance matrix for export pallets.
    StandardTechnical designationRelevant parameterApplication category
    ISO 8611-1:2021Pallets for materials handlingRacking, compression, impactExport and rackable pallets
    ASTM D1185-24Standard test methods for palletsDurability, load distributionNorth American distribution
    EU 94/62/ECPackaging and packaging wasteHeavy metals 100 mg/kgEU-bound pallets
    REACH EC 1907/2006Article 67 restrictionsSVHC absenceGlobal industrial use
    Terminal products include 1100 mm × 1100 mm export pallets, 1200 mm × 1000 mm hygienic one-piece pallets for pharmaceutical handling, and rackable pallets with local steel reinforcement inserts overmoulded into the feet. Continuous service above 60 °C on racking beams is not recommended because creep deflection can exceed 25 mm under sustained load. Strong oxidising acids and long-term UV exposure without stabiliser packages reduce the reclaim value of the pallet at end of life.

    Toy Compliance under EN 71-3 Introduces Extraction Limits for Heavy Metals

    Injection-moulded toy geometries with internal undercuts, snap-fit interlocking features, and living-hinge straps expose HDPE 30460M to long dwell times and local shear heating in the hot runner. The formulation is 97–99 wt% virgin HDPE 30460M, 1–3 wt% colour masterbatch, and 0.1–0.2 wt% nucleating additive where dimensional stability is critical for block-to-block tolerance. Recycled material is excluded from production unless the recyclate has been tested for heavy-metal migration under EN 71-3 and physical safety under EN 71-1. Processing uses melt temperatures of 200–230 °C, mould temperatures of 20–30 °C, and holding pressures of 40–60 MPa to maintain dimensional consistency below ±0.1 mm across multi-cavity tools. Cavity count varies from 16 to 96 depending on part size, with hot-runner systems preferred because cold-runner regrind increases gate blush and colour variation on interlocking surfaces. Compliance for the US market requires ASTM F963-23 heavy-element migration limits, while EU compliance requires EN 71-1, EN 71-2 for flammability, and EN 71-3 extraction limits for 19 elements; REACH Annex XVII restrictions on phthalates and short-chain chlorinated paraffins also apply. Terminal products include interlocking building blocks, stackable toddler toys, and rigid outer shells for learning toys. Steam sterilisation at 121 °C is outside the resin’s operational limit; chemical sanitisation should be carried out at temperatures not exceeding 60 °C to prevent warpage and gate-area stress cracking.
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    Certification & Compliance
    More Introduction

    DOW HDPE 30460M

    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.

    Table 1: Representative physical-property release values for DOW HDPE 30460M
    PropertyTest methodTypical value
    Melt flow rate, 190 °C/2.16 kgISO 1133-14.5 g/10 min
    DensityISO 1183-10.964 g/cm³
    Tensile yield stress, 50 mm/minISO 527-228 MPa
    Tensile modulus, 1 mm/minISO 527-21250 MPa
    Flexural modulus, 2% secantISO 1781400 MPa
    Notched Charpy impact, 23 °CISO 179-1/1eA5 kJ/m²
    Vicat softening temperature, 50 °C/hISO 306/A50127 °C
    Environmental stress crack resistance, 10% Igepal, F50ASTM D169330 h
    Shore D hardnessISO 86865

    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.

    How Does 30460M Differ from Lower-Density or Higher-Flow HDPE Grades?

    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.

    Processing Boundary Conditions in Multi-Cavity Tools

    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.

    When Environmental Stress Cracking Resistance Governs Container Design

    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.

    Regulatory Status Is Not Automatically Transferable to Finished Articles

    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.

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