| HS Code | 899418 |
| Density | 0.935 g/cm³ |
| Melt Flow Rate | 3.5 g/10 min |
| Tensile Strength At Yield | 11.0 MPa |
| Tensile Strength At Break | 17.0 MPa |
| Elongation At Break | 800% |
| Flexural Modulus | 550 MPa |
| Notched Izod Impact Strength | 0.80 J/cm |
| Vicat Softening Point | 100 °C |
| Melting Point | 125 °C |
| Hardness Shore D | 50 |
| Thermal Expansion Coefficient | 1.5E-4 1/°C |
| Dielectric Constant | 2.3 |
As an accredited LyondellBasell Icorene 3545 ORE 3218 Polyethylene, Linear Low Density factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg bags, typically palletized, for LyondellBasell Icorene 3545 ORE 3218 Linear Low Density Polyethylene. |
| Container Loading (20′ FCL) | 20′ FCL loaded with LyondellBasell Icorene 3545 ORE 3218 Linear Low Density Polyethylene in 25 kg bags, palletized and shrink-wrapped. |
| Shipping | LyondellBasell Icorene 3545 ORE 3218 Polyethylene, Linear Low Density is a non-hazardous solid resin. It is shipped in moisture-resistant bags or octabins, palletized, and secured for standard dry-van freight. No UN number, hazard class, or special transport placards are required. Keep dry, cool, and away from direct sunlight. |
| Storage | Store LyondellBasell Icorene 3545 ORE 3218 Polyethylene, Linear Low Density indoors on pallets in original, sealed packaging in a cool, dry, well-ventilated warehouse. Keep away from ignition sources, direct sunlight, heat, moisture, and strong oxidizers. Avoid dust/static; maintain stable stacking, protect from contamination, use first-in, first-out rotation, and follow SDS guidance. Do not store near food or incompatible materials. |
| Shelf Life | Shelf life: typically 24 months when stored unopened in original packaging, dry, below 50°C, and protected from direct sunlight. |
| Application | Nominal wall | Oven setpoint | Peak internal air | Cooling rate | Rotation ratio |
|---|---|---|---|---|---|
| Potable-water tank | 5.0 mm | 285 °C | 195 °C | 6 °C/min | 4:1 |
| Agricultural chemical tank | 8.0–10.0 mm | 290 °C | 200 °C | 8 °C/min | 4:1 |
| Marine buoy body | 6.0 mm | 270 °C | 190 °C | 3 °C/min | 2:1 |
| DEF reservoir | 4.0 mm | 280 °C | 195 °C | 4 °C/min | 4:1→2:1 |
| Insulated fish bin shell | 5.0 mm | 280 °C | 192 °C | 4 °C/min | 4:1 |
| Rotomoulded pallet deck | 6.0 mm | 280 °C | 195 °C | still air → mist | 4:1 |
| Playground tunnel section | 5.5–7.0 mm | 275 °C | 190 °C | 5 °C/min | 4.5:1 |
| End-use segment | Standard or regulation | Critical test parameter |
|---|---|---|
| Potable-water tank | NSF/ANSI/CAN 61, FDA 21 CFR 177.1520(c) | Extraction limits, hexane/xylene |
| Agricultural chemical tank | ASTM D1998, ASTM D1693 | Hydrostatic 1.5× capacity, ESCR |
| Marine buoy body | ISO 179-1/1eA, ASTM D570 | Charpy at -20 °C, water absorption |
| DEF reservoir | ISO 22241-3, ISO 22088-2 | Vacuum decay, ESCR in 50% DEF |
| Insulated fish bin shell | FDA 21 CFR 177.1520, ASTM D5276 | Migration, drop impact at -20 °C |
| Rotomoulded pallet deck | FDA 21 CFR 177.1520, ASTM D790 | Deflection under 1,000 kg, regrind traceability |
| Playground tunnel section | EN 1176-1, ASTM F1487, 16 CFR 1303 | Vandal resistance, lead content |
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LyondellBasell Icorene 3545 ORE 3218 is a linear low density polyethylene supplied in powder form for rotational moulding. The grade occupies the medium-flow region of the Icorene LLDPE rotomoulding family, where the design objective is to maintain a fine particle-size distribution and a controlled additive package for hollow industrial parts. LyondellBasell documentation identifies the material as a linear low density polyethylene rather than a high-density or plastomer resin. The 3545 designation is associated with a typical melt mass-flow rate of 3.0–4.5 g/10 min at 190 °C/2.16 kg under ISO 1133-1:2022 and a typical density of 0.930–0.937 g/cm³ under ISO 1183-1:2019 or ASTM D1505. The suffix ORE 3218 identifies a specific variant within the grade and should be checked against the current LyondellBasell technical data sheet and lot certificate of analysis. Because rotational moulding uses the powder directly rather than melt-compounded pellets, the powder dry-flow and sintering response are as important as the melt-flow value.
The polymer sits in the LLDPE region intentionally. HDPE rotomoulding powders at 0.940–0.950 g/cm³ provide higher flexural modulus and tensile yield stress, but exhibit lower environmental stress crack resistance and poorer sub-zero impact when compared under equivalent rotational moulding conditions. Metallocene plastomer powders at 0.900–0.915 g/cm³ provide exceptional low-temperature impact, but their flexural modulus can fall below 120 MPa, causing excessive deflection in large tanks and unsupported sidewalls. Icorene 3545 ORE 3218 is therefore placed in the 0.930–0.937 g/cm³ density band and the 3.0–4.5 g/10 min melt-flow band, where short-chain branch distributions are high enough to generate tie-molecule networks across the crystalline lamellae while retaining sufficient stiffness. Tensile yield stress for rotomoulded plaques of this class typically falls between 12 MPa and 18 MPa under ISO 527-2:2012, and flexural modulus between 400 MPa and 600 MPa under ISO 178:2019. ESCR values under ASTM D1693, condition B, 100% Igepal, at 50 °C are commonly above 1000 h for the class, whereas HDPE rotomoulding powders often fall between 50 h and 500 h.
Compared with a conventional LLDPE extrusion grade, Icorene 3545 ORE 3218 is not supplied as pellets. It is supplied as a rotomoulding powder with controlled particle shape, limited pellet-grade fines, and a stabilisation package intended for longer oven residence. Extrusion-grade LLDPE is stabilised for melt processing in a screw extruder, while rotomoulding grades must withstand heating and cooling inside closed moulds without mechanical mixing. Compared with crosslinkable rotomoulding polyethylene, the present grade is a thermoplastic and does not require peroxide-induced crosslinking during the moulding cycle. That distinction simplifies process control and permits regrind reuse within defined boundaries, but it also lowers heat distortion resistance and creep resistance relative to crosslinked parts.
For this product class, the mass median particle diameter is generally controlled between 250 µm and 500 µm. The powder is dry-blended with colour or UV stabiliser masterbatches at 0.5–2.0 wt% before charging. Low-shear tumble blending is preferred because high-shear mixers generate fines and electrostatic charge, causing non-uniform mould-wall coverage. The control of particle size is critical because a powder with excessive fines below 75 µm can segregate during mould rotation, melt early, and form rough outer surfaces. Coarse particles above 600 µm may require longer sintering time and leave pinholes at the inner wall. Bulk density is typically 0.35–0.42 g/cm³ by ASTM D1895 Method A, and dry-flow can be checked by ISO 6186:1998. The exact sieve profile and dry-flow limit are stated in the certificate of analysis.
On production-scale carousel and shuttle machines with mould swing diameters of 1.5–4.0 m and rotation ratios of 4:1 to 5:1, powder distribution is governed by dry-flow more than by pellet melt viscosity. A persistent bottleneck observed in moulding of complex geometries is bridging of poorly flowing powder in feed hoppers and delayed powder pickup in narrow channels. The powder is supplied with a controlled pourability window; however, the moulder should measure dry-flow after storage because moisture absorption at relative humidity above 60% can reduce flow and introduce surface flaws.
The sintering and densification sequence starts with powder pickup and surface coalescence. For a particle with radius near 150 µm and melt viscosity in the low-shear range of 10³–10⁴ Pa·s, the characteristic neck growth time is on the order of seconds to minutes when the mould-wall temperature is maintained near 180–200 °C. The zero-shear viscosity inferred from the melt-flow window of Icorene 3545 ORE 3218 is low enough to permit bubble removal but high enough to limit melt drainage on vertical walls. If the viscosity were too low, thin sidewall sections would sag under gravity. If too high, entrapped air bubbles could not migrate to the inner surface, producing a porous inner skin. The density of this class also affects crystallisation shrinkage; linear mould shrinkage is typically 1.5–2.5%, depending on cooling rate and wall thickness.
For LLDPE rotomoulding, oven air temperatures are commonly set between 260 °C and 300 °C, and the peak internal air temperature is typically held at 180–200 °C. The temperature difference between the oven air and the powder bed is a function of mould thermal mass, rotational speed, and wall thickness. When oven air exceeds 280 °C, the inner surface of the moulding can remain above the crystalline melting region for an extended period while the outer layer is already solidified. This condition can consume the stabilisation package and reduce the oxidation induction time, measured by ASTM D3895 or ISO 11357-6. Published data for the exact ORE 3218 variant are limited; therefore, the oxidation induction time should be determined on the as-supplied powder during qualification. A practical failure signature is a brittle inner skin with micro-pinholes and low elongation at break, commonly detected after the part has been in chemical service for several months.
Process engineers control the cycle by measuring the internal air temperature and not solely by oven residence time. If the peak internal air temperature overshoots the grade-specific limit, the part may pass initial wall-thickness and impact tests but fail long-term ESCR. Pre-drying is required only after open storage at relative humidity above 60%. Drying at 60–70 °C for 1–2 h in a dehumidified hopper is typical. Avoid exposing the powder to ambient temperatures above 40 °C for prolonged storage, as sintering of the powder bed can occur in silos and bulk containers.
Cooling rate governs warpage and impact. Forced-air cooling at 10–25 °C/min produces smaller crystalline spherulites and better impact than slow cooling in the mould; however, rapid cooling also increases thermal stresses and part warpage. A common production problem is warpage of flat sides when cooling is nonuniform. This can be reduced by maintaining the rotational motion during cooling until wall temperature falls below 80 °C. Mould release spray, mould surface preparation, and cooling air distribution must be held constant during qualification runs because they affect shrinkage and ESCR independently of the resin.
The property ranges in the following matrix are class-level values from published rotomoulding polyethylene technical data sheets and are not a substitute for the lot-specific certificate of analysis for ORE 3218. Specimen orientation and moulding cycle must be reported with every qualification set because rotomoulded wall properties vary from outer skin to inner skin.
| Property | Test method | Icorene 3545 ORE 3218 class | HDPE rotomoulding class | Plastomer rotomoulding class |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 / ASTM D1505 | 0.930–0.937 g/cm³ | 0.940–0.950 g/cm³ | 0.900–0.915 g/cm³ |
| Melt mass-flow rate | ISO 1133-1:2022, 190 °C/2.16 kg | 3.0–4.5 g/10 min | 5.0–7.0 g/10 min | 3.0–6.0 g/10 min |
| Tensile yield stress | ISO 527-2:2012 | 12–18 MPa | 18–24 MPa | 6–10 MPa |
| Flexural modulus | ISO 178:2019 | 400–600 MPa | 600–900 MPa | 60–120 MPa |
| Environmental stress crack resistance | ASTM D1693, condition B, 100% Igepal, 50 °C | >1000 h | 50–500 h | >1000 h |
| Notched Charpy impact at -20 °C | ISO 179-1 | 60–90 kJ/m² | 20–40 kJ/m² | No break |
Because rotational moulding produces anisotropic wall properties, the specimen cutting location and moulding cycle must be recorded in qualification reports. Tensile and impact values are sensitive to peak internal air temperature, cooling rate, and mould release spray. When comparing data, specimens should be cut from the same wall region of the same mould; otherwise, property differences can mask resin differences.
Polyethylene of this class may be assessed for food-contact use under FDA 21 CFR 177.1520 and EU Regulation 10/2011, but the exact clearance status of ORE 3218 must be confirmed from the supplier’s regulatory statement. End-use compliance requires migration testing on the finished rotomoulded part because wall thickness, surface-to-volume ratio, and processing history influence overall and specific migration. Under EU Regulation 10/2011, the overall migration limit for polyolefin food-contact materials is 10 mg/dm² when determined with prescribed simulants. REACH and RoHS declarations for the base polymer do not automatically cover dry-blended colorants or UV additives added by the moulder.
LLDPE of this class resists dilute acids, alkalis, and aqueous salt solutions but is not suitable for strong oxidising acids, aromatic hydrocarbons, or halogenated solvents. Chemical compatibility should be tested per ISO 175:2022 or ASTM D543 on rotomoulded samples at service temperature, because moulded-in stress and cooling rate affect uptake. The data-sheet ESCR value does not override environmental attack by polar liquids. Direct regrind use in chemical tanks is limited by the oxidative history of the first moulding cycle. High levels of amine-based antistatic or migratory lubricants should not be incorporated without supplier validation because they can reduce ESCR. Reuse of regrind above 10–20% in structurally loaded parts is generally avoided unless the process is requalified, though the final limit must follow the application specification.
During first-article validation, the processor should record oven setpoint, peak internal air temperature, oven residence time, cooling mode, rotational ratio, and ambient humidity. Sections removed from the 90° polar location and the equatorial weld region can be tested for low-temperature impact and ESCR. Batch-to-batch variation in powder flow or melt-flow should trigger sieve and oxidation induction time checks before a new lot is introduced to production.