| HS Code | 631340 |
| Polymertype | Medium Density Polyethylene (MDPE) |
| Density | 0.938 g/cm³ |
| Meltindex | 0.30 g/10 min |
| Tensilestrengthatyield | 19 MPa |
| Tensilestrengthatbreak | 25 MPa |
| Elongationatbreak | 600% |
| Flexuralmodulus | 1.10 GPa |
| Environmentalstresscrackresistance | >1000 h |
| Hardnessshored | 60 |
| Vicatsofteningpoint | 120 °C |
| Brittlenesstemperature | -70 °C |
| Melttemperature | 190-210 °C |
| Moldshrinkage | 1.5-3.0% |
As an accredited NOVA Chemicals Novapol MDPE NB-0338-U factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Typically supplied in 25 kg moisture-resistant bags; bulk supersacks or truck shipments may also be available. |
| Container Loading (20′ FCL) | NOVA Chemicals Novapol MDPE NB-0338-U is loaded in a 20-foot FCL container as palletized bags, securely stowed for transport. |
| Shipping | NOVA Chemicals Novapol MDPE NB-0338-U ships as non-hazardous medium-density polyethylene pellets in moisture-barrier bags, octabins, or bulk containers. Keep dry and away from ignition sources. It is not regulated by DOT/IMDG/IATA; follow the SDS and applicable transport rules. |
| Storage | Store NOVA Chemicals Novapol MDPE NB-0338-U in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and oxidizing agents. Keep original packaging closed and undamaged to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and high temperatures. Handle to minimize dust and static generation, and follow the supplier SDS and local storage regulations. |
| Shelf Life | Shelf life is typically 12 months from manufacture when stored dry, cool, and in original packaging. |
Within the production of rotationally moulded intermediate bulk container shells and static chemical storage vessels, NOVA Chemicals Novapol MDPE NB-0338-U is charged as a rotomoulding powder with a nominal density of 0.938 g/cm³ under ASTM D1505 and a melt index of 0.35 g/10 min under ASTM D1238 at 190°C/2.16 kg. The powder is dry-blended rather than melt-compounded; the particle size distribution, typically reported through the funnel flow time under ASTM D1895 Method A, controls how the powder distributes over the mould surface during the initial rotation stage, and an irregular dry-flow value causes thin-out at sharp radii, internal ribs, and metallic inserts. On a biaxial machine with a 4:1 primary-to-secondary axis ratio and primary rotation in the range of 4 rpm to 6 rpm, the charged mould enters a convection oven set between 260°C and 300°C. The governing process variable is the peak internal air temperature, maintained at 190°C to 205°C for a nominal wall section of 6.5 mm to 10 mm; oven dwell times from 22 min to 35 min are typical for these wall gauges. If the internal air temperature remains below 180°C, the process enters the incomplete-sintering regime, producing pinholes and low weld strength at the pinch-off line, while an internal air temperature above 220°C accelerates oxidative degradation of the antioxidant package and creates yellowing plus internal bubble formation. The formulation uses 2 wt% to 4 wt% of a UV stabilizer concentrate and, when colour is needed, 0.25 wt% to 1.0 wt% of a high-temperature-stable organic pigment masterbatch; no reprocessed powder is added unless the end use permits reduced impact resistance. After the oven step, forced-air cooling at 6°C/min to 10°C/min lowers the mould surface to 80°C, followed by water mist until the demoulding temperature falls below 60°C; demoulding above 70°C increases the risk of post-mould distortion in flat sidewalls. The component is a single-piece, weld-free tank shell with integrally moulded outlet bosses and lifting lugs; chemical storage tanks are hydrostatically loaded and, when the shell is used as a UN intermediate bulk container inner receptacle, the moulding is tested under UN 31H1 performance requirements with a service specific gravity rating up to 1.9 depending on wall thickness. The chemical resistance of the MDPE matrix to the intended stored liquid should be confirmed by immersion testing under ASTM D543.
Marine fender and dock float mouldings impose a different weathering and impact requirement because the part is exposed to saltwater spray, cyclic wave loading, and direct solar radiation without a protective coating. The -U designation in NB-0338-U indicates a UV stabilization package, but actual weathering retention depends on pigmentation and wall thickness; for black or dark grey formulations, a carbon black loading of 2.0 wt% to 2.5 wt% is specified to maintain the surface UV absorbance, and the notched impact margin is validated after an accelerated weathering interval under ISO 4892-2 or ASTM G154 Cycle 1 according to the end-use specification. The shell is rotationally moulded at a wall thickness of 4.5 mm to 8 mm, using an oven setpoint of 270°C to 310°C and a peak internal air temperature of 195°C to 210°C; the higher PIAT relative to potable water tanks is required because thin walls lose heat rapidly during mould rotation and a lower temperature would freeze off the coalescence front before the inner surface is fully sintered. Cooling is carried out with forced air at 5°C/min to 8°C/min, and the part is demoulded below 55°C to preserve the dimensional accuracy of mating flanges. After moulding, the shell is filled with a closed-cell polyurethane pour-in foam having a free-rise density of 32 kg/m³ to 48 kg/m³ to provide reserve buoyancy; the foam is injected only after the polyethylene surface reaches ambient temperature to avoid collapsing the foam cells at the interface. The terminal product is a dock float, pontoon segment, or fender shell with a moulded-in valve port and integrated mounting inserts, rated for continuous water temperatures from -10°C to 40°C; published data for prolonged chlorophyll or fuel exposure in this specific rotomoulding grade is limited, so the moulder should perform immersion testing under ASTM D543 before specifying it for fuel-splash zones.
Potable water and rainwater harvesting vessels produced from medium-density polyethylene are regulated by FDA 21 CFR 177.1520(c), which covers olefin polymers used as articles or components of articles intended for food contact, and by NSF/ANSI 61 for drinking water system components in North America. The raw resin does not carry the final potable-water certification; the rotationally moulded tank must be tested with the exact colour masterbatch and processing conditions because degradation byproducts from excessive oven residence can migrate into the stored water. A typical 500 L to 5,000 L tank uses 100 parts of virgin NB-0338-U powder and 1.0 wt% to 2.5 wt% of a TiO₂-based white masterbatch; regrind from non-potable production is excluded to avoid cross-contamination, and the mould cavity is purged before the first potable cycle. The oven setpoint is held at 260°C to 290°C, with the peak internal air temperature limited to 185°C to 200°C; this lower PIAT reduces oxidative breakdown of the stabilizer package and lowers the concentration of volatile extractables that would affect organoleptic neutrality. The cooling ramp is limited to 5°C/min through the crystalline solidification range, and the tank is released from the mould below 50°C. After demoulding, the tank is hydrostatically loaded at 1.5 times the service head for 1 h to verify wall integrity and fitting seal. The terminal product is a one-piece, seamless potable water tank with integrally moulded outlet bosses, inspection port, and baffle pockets for mobile applications. Operation above 60°C is outside the design boundary because creep of the MDPE matrix causes threaded connections to relax and gasketed joints to leak.
Outdoor playground components such as slide hoods, tunnel sections, and climbing elements are moulded from the same MDPE powder because the material combines enough flexural modulus to support static child loads with a ductile failure mode that avoids sharp shards. The design and performance of public playground equipment are governed by ASTM F1487 in the United States and EN 1176 in Europe; impact loading, head entrapment dimensions, and structural integrity are evaluated on the finished assembly, not the raw resin. The rotomoulding process uses mould charging of 5.5 kg/m² to 7.0 kg/m² of powder per projected area to produce a wall thickness of 5 mm to 9 mm. The oven is set at 270°C to 300°C, and the internal air temperature is controlled at 185°C to 200°C. The cooling step is the most sensitive variable for playground parts: forced-air cooling at 6°C/min to 9°C/min is used until the mould reaches 80°C, then the part is cooled to demoulding below 55°C without water quenching, because water quenching creates a steep thermal gradient that can warp large flat panels and reduce the notched impact energy at -20°C. A typical outdoor colour formulation contains 2.0 wt% to 4.0 wt% of a hindered amine light stabilizer masterbatch and 0.3 wt% to 0.8 wt% of an exterior-grade organic pigment masterbatch; dark colours additionally incorporate 1.5 wt% to 2.5 wt% of carbon black. The terminal parts are post-trimmed at moulded-in flanges, mechanically fastened to support structures, and inspected for sink marks at bosses because sink marks on a sliding surface can create a pinch point. The operational temperature limit is 50°C for continuous exposure to direct sunlight in hot climates.
Agricultural pesticide and fertilizer storage tanks above 12 mm wall section demand a different oven dwell and cooling ramp than thin-walled playground parts because the long cooling path through a thick MDPE section creates a thermal gradient that can shrink the inner surface away from the mould and produce cavitation at the pinch-off line. The resin is rotationally moulded at an oven temperature of 260°C to 285°C with a peak internal air temperature of 190°C to 205°C; for wall sections from 8 mm to 15 mm, the dwell time is extended from 35 min to 60 min. The powder is dry-blended with 2 wt% to 3 wt% of a UV/antioxidant masterbatch and, for black tanks, 2.0 wt% to 2.5 wt% of carbon black masterbatch; carbon black loading increases the outer-surface heat absorption in the oven and can reduce the required oven dwell by 3 min to 5 min compared with white or coloured versions. The governing standard for vertical polyethylene agricultural storage tanks is ASTM D1998, which specifies wall thickness, hydrostatic test, and environmental stress-crack resistance for linear polyethylenes. Environmental stress-crack resistance is assessed in an Igepal CO-630 environment under ASTM D1693 Condition B, with rotomoulding MDPE grades normally required to exceed 500 h F50; published data for this specific configuration should be confirmed from the batch certificate. The terminal product is a single-wall, seamless vertical tank of 5,000 L to 30,000 L, with integrally moulded lifting lugs and outlet bosses, rated for liquids up to a specific gravity of 1.5 unless a thicker bottom knuckle is moulded. The outer surface should not be exposed to direct flame or to organic solvents such as xylene, which plasticize the MDPE matrix and reduce ESCR.
Off-highway hydraulic oil reservoirs moulded from medium-density polyethylene are confined to systems where the bulk oil temperature remains below 60°C and the hydraulic fluid is compatible with the polyethylene matrix. The part is formed in cast aluminium tooling with steel thread inserts encapsulated during the moulding cycle; the inserts are preheated to 120°C to 150°C before placement to reduce the quench effect and ensure that molten polymer fills the knurled retention grooves. Mould charging is calculated at 6.0 kg/m² to 8.0 kg/m² of projected area, yielding a wall thickness of 6 mm to 10 mm. Oven setpoint is 270°C to 300°C, internal air temperature is held at 195°C to 210°C, and cooling is conducted in still air until the mould reaches 90°C, then forced air to 60°C before demoulding, which minimizes warpage around the insert bosses. The resin is dry-blended with 2.0 wt% to 3.0 wt% of a carbon black masterbatch to provide outdoor UV resistance and to stabilise the hydraulic oil reservoir against ultraviolet exposure through engine compartment openings. Finished tanks are pressure-tested at 35 kPa to 70 kPa internal air pressure and leak-tested under factory procedure; the limiting operational boundary is the low tensile creep modulus of medium-density polyethylene at elevated temperature, and hydraulic systems that exceed 70°C near the return line require a thermoset- or metal-lined reservoir instead of a single-wall MDPE tank.
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