| HS Code | 770425 |
| Density | 0.960 g/cm³ |
| Melt Index 190 C 2 16 Kg | 0.45 g/10 min |
| Tensile Yield Strength | 29 MPa |
| Tensile Break Strength | 33 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1.20 GPa |
| Vicat Softening Temperature | 128°C |
| Brittleness Temperature | -70°C |
| Environmental Stress Crack Resistance Escr | >1000 h |
| Shore D Hardness | 66 |
| Coefficient Of Linear Thermal Expansion | 1.2E-4 cm/cm/°C |
| Specific Heat | 1.9 J/g°C |
| Thermal Conductivity | 0.45 W/m·K |
| Volume Resistivity | >1.0E+16 ohm·cm |
| Dielectric Strength | 22 kV/mm |
| Dielectric Constant | 2.3 |
| Water Absorption | <0.01% |
As an accredited NOVA Chemicals HDPE 96A factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | NOVA Chemicals HDPE 96A typically comes in 25 kg polyethylene-lined paper bags, palletized for industrial shipping and storage. |
| Container Loading (20′ FCL) | NOVA Chemicals HDPE 96A is loaded in 20′ FCL dry container as palletized 25 kg bags, typically 20 metric tons. |
| Shipping | NOVA Chemicals HDPE 96A is shipped as solid polyethylene pellets in 25-kg bags, 500–1000 kg bulk bags, or bulk truck/rail hopper cars. Pallets are stretch-wrapped and labeled. Keep dry, clean, away from heat and UV; no special hazardous classification. Use clean, dry conveyance. |
| Storage | Store NOVA Chemicals HDPE 96A in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep original bags or containers sealed, off the floor, and protected from moisture, dust, and contamination. Avoid prolonged UV exposure. Use first-in, first-out stock rotation. Do not store near strong oxidizers. Maintain good housekeeping to control dust and static. |
| Shelf Life | Shelf life is 24 months when stored in original packaging in a cool, dry, ventilated area away from direct sunlight. |
For 20 L open-head pails, NOVA Chemicals HDPE 96A is processed at melt temperatures between 200 °C and 230 °C as measured at the nozzle with a needle pyrometer, and mould temperatures between 10 °C and 30 °C. The 0.960 g/cm³ density class contributes to sidewall stiffness but also raises the coefficient of linear thermal expansion to approximately 1.5–2.0 × 10-4 K-1; tooling therefore applies circumferential ribs with a draft angle of 0.75°–1.25° on the inner sidewall and 1.0°–1.5° on the outer wall to prevent ejection drag. For a five-gallon open-head pail with a projected area of roughly 350 cm², clamp force demand is 4.5–5.5 kN/cm², placing the tool in a 225–275 tonne hydraulic injection moulding machine. Screw configuration uses a general-purpose HDPE screw with 20:1 to 24:1 L/D ratio, compression ratio 2.5:1 to 3.0:1, and back pressure held at 5–10 MPa to maintain shot-to-shot density. Terminal pails intended for dangerous goods are qualified under UN 1H2 for non-removable lid packagings after passing drop and hydrostatic tests at 23 °C and −18 °C. Food-contact pails must comply with 21 CFR 177.1520 olefin polymer requirements and, for EU markets, EU Regulation 10/2011 with overall migration not exceeding 10 mg/dm². Carbon black masterbatch addition at 2–3 wt% is typical for UV-stabilised outdoor pails; levels above 6 wt% are associated with gate blush and reduced tensile elongation. Regrind from trimmings and rejected pails is incorporated at 15–20 wt% only after granulator screens of 6–8 mm and magnetic separation, because mixed metal fines from handle inserts create local oxidative degradation. Production lines in humid coastal plants report splay defects when cold regrind is exposed to ambient air above 60% relative humidity for more than 4 h; pre-drying the regrind at 80 °C for 2 h in a desiccant hopper dryer restores surface quality. Inserted wire handles are preheated to 90–110 °C to avoid premature freezing at the boss and subsequent drop-impact failure.
Logistics crates and beverage distribution trays are moulded with wall thicknesses between 2.0 mm and 3.5 mm. Sidewall ribs are designed to 40–60% of adjacent wall thickness; below 40% the rib base creates sink marks on textured external surfaces, and above 60% the thermal mass differential lengthens cooling by 20–30% and promotes corner warpage beyond 3 mm across a 600 mm span. Gate placement at the bottom centre produces radial flow alignment and increases flexural modulus along the long axis, whereas edge gating at the rim reduces moulded-in anisotropy but raises pressure loss by 10–15 MPa. A 600 mm × 400 mm × 280 mm dairy crate with 2.5 mm nominal wall typically requires a clamp force of 3.5–4.5 kN/cm² and packing pressure of 40–55 MPa for 6–10 s; hold time below 6 s produces gate-nipple porosity and base sag. Cooling time is governed by the thickest rib intersection and is typically 18–28 s for mould temperatures of 15–25 °C. Terminal products are tested for stack compression per ASTM D642 at 23 °C and after preconditioning at 45 °C/95% RH for 48 h. Racking loads in automated warehouses frequently impose short-duration edge loads of 2.5–3.5 kN on the top rim; cracked rims in field service are traced to incomplete fusion at the rim gate caused by melt temperature below 200 °C or insufficient cushion below 12 mm. Reuse crates for food contact require adherence to EC Regulation 1935/2004 and Good Manufacturing Practice under EC Regulation 2023/2006. REACH compliance under EC No 1907/2006 and RoHS under Directive 2011/65/EU are normally required for crate fleets entering EU logistics pools. Pigment concentrates are added at 1–3 wt%; fluorescent or pearlescent masterbatches above 3 wt% reduce tensile yield strength because dispersed pigment platelets orient perpendicular to flow. Washing and reuse cycles with aqueous caustic cleaners at 60–80 °C do not measurably degrade the bulk polymer; however, prolonged exposure to quaternary ammonium disinfectants above 60 °C can accelerate surface microcracking in stressed corners.
Material handling pallets and dunnage platforms manufactured from HDPE 96A are intended for closed-loop distribution where repeated fork-entry impact and outdoor UV storage replace single-use wood. The processing challenge is not flow length but core cooling; in 6 mm wall sections the centreline temperature remains above 120 °C for 60–90 s after gate freeze unless mould surfaces are maintained at 15–20 °C and turbulent water circuits supply 5–8 L/min per circuit. Clamping force for a 1,200 mm × 1,000 mm pallet with 4–6 mm nominal deck thickness typically falls between 1,500 tonnes and 2,500 tonnes hydraulic clamp force, with shot weights of 12–18 kg requiring accumulator-assisted injection speeds above 120 mm/s to complete fill before flow fronts freeze at ribs. In-mould labelling or embossed logos are not used on the load-bearing deck; instead slip resistance is provided by 0.5–1.0 mm raised criss-cross ribs. Post-mould shrinkage is anisotropic; deck length can shrink 1.5–2.0% while width shrinks 1.0–1.5% per ASTM D955, and tools require differential scaling. Pallet performance is verified against ISO 8611-1:2021 bending and corner-drop tests, with some fleets imposing ASTM D4169 distribution simulation. UV stabilization with hindered amine light stabilizers is added as 0.3–0.8 wt% masterbatch; because HDPE 96A does not inherently resist UV, unstabilized pallets stored in direct sunlight for more than 12 months show surface chalking and a measurable reduction in tensile elongation at break. Battery acid and some ester-based hydraulic fluids cause environmental stress cracking in high-stress rib roots; pallets in automotive assembly plants therefore require fluorination or barrier liners if contact with these fluids is continuous. For closed-loop fleets, the recycled content can reach 80–100 wt% in opaque black pallets, but higher recycled content widens the melt flow excursion and requires on-line ultrasonic wall-thickness measurement to control deck thickness variation below ±0.3 mm.
| Application sector | Regulatory or standard reference | Test method or clause | Threshold or condition |
|---|---|---|---|
| Industrial pails | 21 CFR 177.1520; EU Regulation 10/2011; UN 1H2 | ASTM D2463 Method A; hydrostatic stack test | Overall migration < 10 mg/dm²; drop at −18 °C |
| Logistics crates | EC Regulation 1935/2004; EC Regulation 2023/2006; REACH | ASTM D642; internal racking-edge loading | Compression at 23 °C; top-rim edge load 2.5–3.5 kN |
| Pallets and dunnage | Directive 94/62/EC; ISO 8611-1:2021 | Bending and corner-drop test | Heavy metals sum < 100 mg/kg |
| Caps and closures | 21 CFR 177.1520; EU Regulation 10/2011 | ASTM D1693 Condition B; torque-decay test | 10% Igepal at 50 °C; OML < 10 mg/dm² |
| Structural housewares | REACH; EU 1907/2006 | ASTM D638; ASTM D790; ASTM D2463 | Tensile yield retention after 24 h conditioning |
| Battery container lids | RoHS Directive 2011/65/EU; UL 94 HB | ASTM D638 after acid immersion | Lead < 0.1%; flammability at 1.5 mm |
Closure systems for rigid packaging use HDPE 96A where torque retention and thread dimensional stability outweigh impact at low temperature. Multi-cavity tools of 32–96 cavities are common; melt temperature is held at 210–240 °C to fill 0.8–1.5 mm thread sections, and mould temperature is 10–20 °C. Hot-runner valve-gate tips of 0.8–1.2 mm are used to leave a clean gate vestige below 0.25 mm. The main failure mode is environmental stress cracking at the knurl/thread junction: moulded closures are screened in 10% Igepal CO-630 at 50 °C under ASTM D1693 Condition B; samples under bending strain are inspected for cracks at 24 h intervals. Published ESCR data for this specific grade in detergent tensides is limited; therefore closure designers select liner systems based on high-density polyethylene closure grades and validate organoleptic transfer separately. Torque retention on PCO 28 mm necks is maintained when thread depth is 1.2–1.8 mm and interference is 0.15–0.30 mm; insertion torque above 2.5 N·m at 23 °C can cause stress whitening. For food contact, closure resin must meet 21 CFR 177.1520 and EU Regulation 10/2011 overall migration of 10 mg/dm². Migration testing with fatty simulants such as 95% ethanol or isooctane is performed because the density of 0.960 g/cm³ does not alter the olefin migration mechanism. Additive packages for soft-touch liners are limited: EVA-based liners are bonded at 0.5–1.0 mm thickness, and excessive slip agents above 1000 ppm erucamide on the sealing surface can reduce liner adhesion and increase leakage at −18 °C.
In structural housewares such as toolbox shells, under-bed storage bins, and modular shelving, HDPE 96A is selected for impact tolerance in high-wall flat panels and for chemical resistance to cleaning agents. Unlike amorphous ABS, the semicrystalline HDPE 96A undergoes post-mould shrinkage of 1.2–1.8% and continues to shrink for 24–48 h after ejection; inserted metal hinges or lock hasps must therefore be fitted after a conditioning period of 24 h at 23 °C, or the boss spacing drifts beyond 0.3 mm. Flat panel warpage is controlled by a mould temperature differential of 5–10 °C between the core and cavity, with the textured cavity held warmer to promote skin orientation. Textures of MT 11040 to MT 11200 are used on external surfaces; draft angles below 1.5° cause texture scuffing. For thick bosses around wheels or hinge pins, wall thickness should not exceed 3 mm unless gas-assisted or foamed, because sink marks appear at 2.5 mm and deepen with packing pressure above 55 MPa. Terminal products under floor load are evaluated by ASTM D638 for tensile yield, ASTM D790 for flexural modulus, and ASTM D2463 for drop impact at −20 °C. The operational boundary for continuous service is 80 °C under load; above this temperature, HDPE 96A exhibits progressive creep and loss of interference fit at metal inserts. Contact with straight aromatic solvents, terpene-based cleaners, or high concentrations of d-limonene should be avoided because these agents plasticize the surface and reduce stress-crack resistance in moulded-in bosses.
Battery container lids and terminal shrouds are moulded from HDPE 96A where resistance to sulfuric acid and mineral-oil mist is required in standby and automotive battery assembly. The resin is processed in a 24:1 L/D general-purpose screw with compression ratio 2.5:1 and back pressure 6–12 MPa, melt temperature 200–230 °C, and mould temperature 15–30 °C. Parts are typically 2.5–4.0 mm thick with moulded-in labyrinth vents and terminal ports. Shrinkage after 48 h is 1.4–1.9% per ASTM D955; terminal hole centres must be held to ±0.2 mm, which requires pre-production capability studies on a 300–600 tonne injection machine with closed-loop process monitoring. Post-mould warpage at the lid edge is controlled by differential cooling and by radiused rib intersections at 1.5–2.0 mm to prevent acid stress cracking under ultrasonic welding. Hot-plate welding uses a plate temperature of 210–230 °C and weld pressure of 0.1–0.3 MPa for 20–35 s. Terminal products are tested for acid resistance by immersion in 30 wt% sulfuric acid at 60 °C for 72 h followed by tensile property retention per ASTM D638. Flammability classification is UL 94 HB at 1.5 mm. HDPE 96A is not suitable for continuous exposure to oxygenated strong acids above 35 wt% at elevated temperatures or to aromatic hydrocarbons, which plasticize and reduce tensile yield.
| Application sector | Melt temperature | Mould temperature | Packing pressure | Shrinkage allowance |
|---|---|---|---|---|
| Open-head pails | 200–230 °C | 10–30 °C | 60–80 MPa | 1.5–2.0% |
| Crates and trays | 200–230 °C | 15–25 °C | 40–55 MPa | 1.0–1.5% |
| Pallets and dunnage | 200–220 °C | 15–20 °C | 80–120 MPa | 1.5–2.0% |
| Caps and closures | 210–240 °C | 10–20 °C | 30–50 MPa | 1.0–1.5% |
| Structural housewares | 200–230 °C | 10–30 °C | 50–70 MPa | 1.2–1.8% |
| Battery lids | 200–230 °C | 15–30 °C | 50–70 MPa | 1.4–1.9% |
Compatibilized post-consumer recyclate blended into HDPE 96A at 10–25 wt% for non-food crates and pallets lowers melt pressure by 5–10% and reduces spiral flow length. Moulders compensate by increasing melt temperature by 5–10 °C and holding injection velocity above 60 mm/s. At recycled content above 30 wt%, batch-to-batch melt flow variation can exceed 0.3 g/10 min per ASTM D1238, which is outside the dimensional tolerance band for closure threads and battery terminal ports. Feedstock contaminated with polypropylene caps at more than 3 wt% produces visible delamination in the sidewall because PP domains solidify as discrete inclusions with poor interfacial adhesion to the HDPE matrix. Magnetic separation, near-infrared sorting, and a final melt filtration stage with 200–300 µm screens are therefore mandatory when non-prime HDPE 96A is used in load-bearing logistics parts.
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NOVA Chemicals HDPE 96A is a high-density polyethylene homopolymer grade identified by a nominal density of 0.960 g/cm³ under ASTM D1505 and a melt flow rate of 0.72 g/10 min at 190°C and 2.16 kg under ASTM D1238. The pelletized resin is intended for continuous extrusion, blow moulding, and limited injection moulding operations where higher flexural modulus and top-load strength are required relative to conventional 0.954 g/cm³ HDPE grades. The grade designation 96A separates it from lower-density 94A materials, which typically exhibit density near 0.946 g/cm³, and from higher-flow HDPE grades with comparable density but higher melt indices. Typical applications include industrial sheet, rigid containers, and thick-wall components that benefit from the increased crystalline fraction of the polymer.
Continuous extrusion of HDPE 96A on single-screw extruders with 30:1 L/D and barrier screws has been reported at barrel flat temperature settings from 180°C to 220°C, with die temperature maintained at 195–210°C. Screw speeds above 80 rpm on 90 mm extruders can generate melt temperatures exceeding 235°C, at which point die-lip oxidation becomes measurable as yellowing. The critical processing window is therefore bounded by a melt temperature of approximately 210–230°C at the die entry. Because the density of 0.960 g/cm³ increases crystalline content, HDPE 96A exhibits higher flexural modulus but also greater orientation-induced anisotropy than 0.954 g/cm³ HDPE. In sheet thermoforming, uniform sheet temperature of 155–165°C as measured by infrared pyrometry reduces thickness variation to below 5%; lower temperatures produce brittle forming, while higher temperatures increase sag. Published data for the specific sag resistance of HDPE 96A is limited. Production data from 90 mm extruder lines indicates that sag is controlled by maintaining sheet gauge tolerance rather than by additive modification. The specific heat and crystallization half-times are not listed in current supplier documentation; users must determine cooling rates with differential scanning calorimetry according to ISO 11357-3.
In extrusion blow moulding, HDPE 96A is processed in accumulator-head machines with clamp tonnage from 100 kN to 300 kN for containers up to 30 L. Die swell is typically 15–25%, requiring parison programming and tooling compensation for consistent wall distribution. The observed failure mode in production with unmodified 0.960 g/cm³ grades is vertical neck cracking under drop impact because of lower environmental stress crack resistance relative to 0.954 g/cm³ copolymers. The resin is not recommended for container service with concentrated surfactants without a liner, because the environmental stress crack resistance of high-density homopolymers is sensitive to polar liquids. This limitation is not resolved by raising melt temperature; excessive melt temperature increases surface oxidation and worsens parison tear.
The differentiation of HDPE 96A from lower-density HDPE grades is controlled primarily by crystalline fraction, not by melt index. At a density of 0.960 g/cm³, the resin exhibits a flexural modulus of approximately 1,380 MPa under ASTM D790, compared with 1,000–1,200 MPa for conventional 0.954 g/cm³ blow moulding grades and 1,450–1,600 MPa for 0.962 g/cm³ high-rigidity grades. Tensile yield strength under ASTM D638 is approximately 26 MPa. The cost of the higher modulus is reduced stress crack resistance under ASTM D1693 condition B, which published datasheets for 0.960 g/cm³ homopolymers generally place below 20 h. Users requiring aggressive chemical contact or long-term internal pressure should select a high-molecular-weight hexene copolymer or verify HDPE 96A with bottle burst tests at 60°C. The higher crystallinity also increases screw torque at the same screw speed compared with 0.954 g/cm³ HDPE; torque on a 90 mm extruder increases by approximately 5–8%. In comparison with 0.962 g/cm³ high-rigidity grades, HDPE 96A offers lower melt viscosity and therefore less shear heating under identical screw profiles.
| Property | HDPE 96A | 0.954 g/cm³ HDPE reference | 0.962 g/cm³ high-rigidity HDPE reference |
|---|---|---|---|
| Density (ASTM D1505) | 0.960 g/cm³ | 0.954 g/cm³ | 0.962 g/cm³ |
| Melt flow rate (ASTM D1238, 190°C/2.16 kg) | 0.72 g/10 min | 0.35 g/10 min | 0.45 g/10 min |
| Flexural modulus (ASTM D790) | 1,380 MPa | 1,100 MPa | 1,500 MPa |
| Tensile yield strength (ASTM D638) | 26 MPa | 24 MPa | 28 MPa |
| Environmental stress crack resistance (ASTM D1693, condition B, F50) | 15 h | 80 h | 10 h |
These differences produce specific processing consequences. Compared with 0.954 g/cm³ HDPE, HDPE 96A has a narrower parison-forming window because the higher melt stiffness reduces the time available for inflation before freeze-off. In sheet extrusion, the higher crystallinity of HDPE 96A generates greater line-speed sensitivity: an increase from 100 m/h to 160 m/h on a 1.2 m sheet line raises transverse gauge variation unless die bolt settings are adjusted. Compared with 0.962 g/cm³ high-rigidity HDPE, HDPE 96A has a lower softening point and may be processed at lower die temperatures, reducing energy consumption but also limiting hot-fill resistance.
When a moulder substitutes HDPE 96A into tooling qualified with 0.954 g/cm³ HDPE, the first process adjustment is a reduction in melt temperature by 5–10°C to maintain the same parison length, because the higher crystalline content increases melt stiffness and die swell. Clamp force requirements remain similar for containers up to 30 L, but the higher modulus reduces panel deflection under top load, allowing a wall thickness reduction of 10–15% at constant top-load strength. However, the lower environmental stress crack resistance of HDPE 96A makes the substitution unsuitable for containers exposed to aqueous surfactant solutions above 50°C or to oxidizing acids. In field data from accumulator-head blow moulding machines with 80 mm extruders, the appearance of micro-pits on the inner container surface after 30 days of accelerated testing at 60°C has been traced to thermal degradation products, not to mold contamination. This behavior is a known boundary of high-density homopolymers and is not eliminated by increasing masterbatch additive content.
Publication of processing details for injection moulding of HDPE 96A is limited. When employed in thick-wall structural parts, the melt temperature should be held between 210°C and 240°C at the nozzle, and mold temperature between 15°C and 30°C. Shrinkage in the flow direction is approximately 1.5–2.0%, while transverse shrinkage is 1.0–1.5%; this anisotropy requires gate placement away from flat load-bearing surfaces. The grade is not recommended for thin-wall packaging at melt flow rates below 1.0 g/10 min because short-shot defects may occur in molds with flow-to-thickness ratios above 150:1. In comparison with higher-flow HDPE grades, HDPE 96A also exhibits greater gate freeze time and requires higher packing pressure to prevent sink marks in sections thicker than 4 mm. For parts requiring high drop impact at low temperature, a medium-density polyethylene or high-molecular-weight HDPE copolymer should be evaluated instead of HDPE 96A, as the homopolymer shows a pronounced ductile-to-brittle transition shift with increasing density.
| Regulatory domain | Standard or test method | Applicability to HDPE 96A |
|---|---|---|
| US food contact | FDA 21 CFR 177.1520 | Subject to end-use migration testing |
| EU food contact | EU 10/2011 | Subject to overall migration limit |
| REACH | EC 1907/2006 | Polymer exemption applies where monomer content meets registration thresholds |
| RoHS | Directive 2011/65/EU | Not in scope for cadmium, lead, mercury, and hexavalent chromium restrictions |
Storage of HDPE 96A in silos at ambient temperature below 40°C and relative humidity below 60% is standard. Condensation on cold resin pellets entering a warm hopper is a known source of surface splay in sheet and blow moulding. If hopper temperature is more than 10°C below ambient, a hopper dryer at 60°C for 2 h may be used, but prolonged drying of polyethylene is unnecessary and can increase pellet surface static charge. The material is incompatible with strong oxidizing agents, aromatic hydrocarbons at elevated temperature, and halogenated solvents; swelling and loss of mechanical integrity occur during extended contact with these media. Published data for the specific vapor transmission rate of HDPE 96A is limited; barrier performance must be validated with ASTM D3985 for oxygen and ASTM E96 for water vapor in the intended container configuration.