| HS Code | 434516 |
| Density | 0.935 g/cm³ |
| Melt Flow Rate | 0.60 g/10 min |
| Tensile Strength At Yield | 12.4 MPa |
| Tensile Strength At Break | 34.5 MPa |
| Elongation At Break | 700% |
| Flexural Modulus | 0.276 GPa |
| Dart Drop Impact | 200 g |
| Elmendorf Tear Strength | 250 g/mil |
| Haze | 12% |
| Gloss | 60% |
| Vicat Softening Point | 105 °C |
| Melting Point | 125 °C |
As an accredited LyondellBasell Icorene 3560 BEI 2205 Polyethylene, Linear Low Density factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell Icorene 3560 BEI 2205 Linear Low Density Polyethylene is supplied in 25 kg sealed bags, 40 bags per pallet (1,000 kg). |
| Container Loading (20′ FCL) | 20′ FCL: LyondellBasell Icorene 3560 BEI 2205 LLDPE loaded on pallets in 25 kg bags, securely stowed and shrink-wrapped. |
| Shipping | LyondellBasell Icorene 3560 BEI 2205 Linear Low Density Polyethylene is typically shipped as non-hazardous resin pellets in 25 kg bags, 1,000 kg bulk bags/octabins, or bulk truck/rail cars. It is not DOT/IMDG/IATA regulated. Keep packaging closed, dry, and away from excessive heat; avoid punctures and moisture contamination. |
| Storage | Store LyondellBasell Icorene 3560 BEI 2205 Polyethylene, Linear Low Density indoors at ambient temperature in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers tightly closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and excessive stacking. Follow SDS and local regulations; use first-in, first-out stock rotation. |
| Shelf Life | Shelf life is 24 months when stored in original, unopened packaging in a cool, dry area away from direct sunlight. |
In closed-loop returnable beverage crate manufacturing, LyondellBasell Icorene 3560 BEI 2205 is run as a 100 parts-by-weight virgin matrix with 20–30 wt% of same-cell regrind, because the regrind fraction controls barrel viscosity drift within ±0.5 g/10 min and reduces unfilled moulding cost without moving into post-consumer grades that would demand separate REACH Article 33 declarations for any substance of very high concern above 0.1 wt%. The applicable packaging-reuse framework is ISO 18603:2013, while the finished crate resin system is checked against EU 94/62/EC Article 6 for lead, cadmium, mercury and hexavalent chromium totals below 100 mg/kg. Moulding on 1,200 t hydraulic presses with 20:1 L/D barrier screws proceeds at 220–240°C melt temperature and 15–25°C mould-wall temperature; post-mould shrinkage is held below 1.5% after 24 h conditioning to ISO 294-4. The main processing fault appears at rib intersections when sequential valve-gated hot runners are pushed above 45 cm³/s per cavity: front velocity across the butene-branch melt becomes unstable and fold-line rejection on 24-cavity tools rises above 4%. Terminal parts include 24-bottle dairy crates, 20-bottle beverage shells, and stackable mushroom harvesting trays, each subjected to ISO 8611:2011 stack-load deformation testing.
The limiting variable in hot-filled closure performance is not tensile yield but residual annular stress after mould opening, which is controlled by injection speed and cooling time. The compound uses 100 parts by weight of Icorene 3560 BEI 2205, 1.5–3.0 wt% white TiO₂ masterbatch, 0.2–0.5 wt% slip-agent concentrate, and 0.10–0.15 wt% antioxidant masterbatch when regrind exceeds 15 wt%; linerless designs avoid oxygen-scavenger additives that would require separate migration evaluation. Food-contact compliance is assessed under FDA 21 CFR 177.1520(c) 3.2a and Regulation (EU) No 10/2011 Annex I, with overall migration by EN 1186-14 using simulant D2 at 70°C for 2 h, and taint resistance by EN 1622. Production is set on 64-cavity hot-runner tools on 350 t toggle injection presses, with a barrel profile from 210°C feed to 235°C nozzle and mould temperature 10–18°C; injection speed is detuned to 35–40 cm³/s per cavity to keep thread-root ovality below 0.35 mm. Cooling times below 4.2 s cause intermittent release-torque failure against a 0.8–1.4 N·m specification, while times above 6.0 s sacrifice output without gaining dimensional stability. The resin does not require predrying below 60% RH; above this threshold, 2 h at 70°C in desiccant dryers is applied to prevent splay on the upper closure face. Terminal products include closures for pasteurized milk, chilled juice, UHT dairy drinks, and edible oil caps.
Thin-walled freezer containers for delivered meal kits are moulded at 100 parts by weight of virgin resin, with 0.5–1.0 wt% white masterbatch and 0.05–0.10 wt% fluoroelastomer processing aid only when flow-length to wall-thickness ratio exceeds 150:1; in-house regrind is limited to 10 wt% to keep melt flow variation below 0.4 g/10 min over 48 h of continuous running. The grade’s 0.935 g/cm³ density and 6.0 g/10 min MFR under ISO 1133-1:2022 place it in the intermediate-flow range for thin-wall injection, while butene short-chain branching supports low-temperature puncture resistance that is checked by ISO 6603-2 instrumented puncture at -20°C. Compliance for fatty meal-prep applications uses FDA 21 CFR 177.1520(c) 3.2a and Regulation (EU) No 10/2011 Annex I, with EN 1186-2 overall migration into olive oil at 40°C for 10 days; residual metal content in the masterbatch is controlled through the colourant supplier’s REACH Annex XVII documentation. Accumulator-assisted high-speed presses with 18:1 L/D screws process at 215–235°C melt and 5–15°C mould temperature, producing 2.8–3.5 s cycle segments for wall sections between 0.9 mm and 1.4 mm. Above 245°C melt temperature, surface haze increases from low-molecular-weight oxidation by-products even at 0.15 wt% antioxidant loading. Terminal parts include 250 mL and 500 mL rectangular freezer bowls, 750 mL cold-chain trays, and clip-on lids that maintain ductile puncture after 7 days at -18°C.
When storage totes are specified for garage and basement use, the formulation uses 100 parts by weight Icorene 3560 BEI 2205 with 10–20 wt% of post-consumer LLDPE regrind melt-filtered at 120 μm; each delivered lot of regrind is checked by ISO 11357-6 for an oxidation induction time above 20 min at 210°C. Consumer product safety documentation follows EU Regulation 2023/988, and REACH Annex XVII entries 50 through 63 are screened for PAH and phthalate residues; colour masterbatch is 1.0–3.0 wt%, with 0.3–0.5 wt% hindered amine light stabilizer added only when the part is expected to exceed 12 MJ/m² annual UV exposure. Moulding takes place on 700 t two-platen presses with 22:1 L/D screws, using a reverse barrel profile of 235°C feed to 220°C nozzle to keep screw recovery below 4.0 s. Sink on rib intersections above 3.5 mm nominal wall is controlled by holding packing pressure at 55–65 MPa for 2.5 s before switchover; lower packing pressure leads to visible sink, while higher pressure extends cycle without improving drop performance. Terminal product types include stackable 35 L under-bed storage boxes, modular drawer organizers, and integrally moulded-handle totes qualified under the purchaser’s 1.0 J puncture-at--18°C inbound QA test.
Agricultural chemical pails are moulded with 100 parts by weight of Icorene 3560 BEI 2205 and 2.0–5.0 wt% of UV-stabilised black masterbatch, with carbon black kept above 2.5 wt% of total compound for prolonged outdoor stockpiling; 0.3–0.5 wt% antioxidant masterbatch is introduced when in-house regrind is held above 15 wt%. The packaging is certified as UN dangerous goods packaging under 49 CFR Part 178 for Group II and III liquids, requiring the 1.2 m drop test, 30 kPa leakproofness test, and 95 kPa hydraulic pressure test referenced in ADR 6.1.5. Moulding on 800 t injection presses with 22:1 L/D accumulator-assisted screws uses 220–245°C melt temperature and 10–20°C mould temperature to control pail rim flatness. At the handle pinch-off points, injection velocity is increased to 45–50 cm³/s in the final 20% of stroke to prevent interrupted flow; exceeding 55 cm³/s produces jetting streaks that exceed the supplier’s 1.5 mm² visual defect threshold. Amine-based antistatic packages are excluded from this formulation because secondary amine decomposition at the pail sealing lip produces yellowing that fails customer colour stability limits after 4 weeks of stacked storage. Predrying is not performed below 60% RH, but surface moisture above this limit requires 2 h at 70°C to avoid splay on the sealing lip. Terminal products include 5 L and 20 L open-head pails, tamper-evident agricultural chemical containers, and dry chemical transport pails for silane-crosslinkable powder additives.
Toy components are compounded from 100 parts by weight of virgin Icorene 3560 BEI 2205, with 0.5–2.0 wt% pre-tested colour masterbatch and 0.2–0.5 wt% silicone slip agent to reduce ejection force on textured cavities; external post-consumer recyclate is excluded, and in-line regrind is limited to 5 wt% so that trace-element migration does not drift toward EN 71-3:2019+A1:2021 Category III limits, including barium 18,750 mg/kg, cadmium 17 mg/kg, and lead 23 mg/kg in scraped-off material. Conformity under Directive 2009/48/EC is documented by ISO 8124-3 migration testing, while ASTM F963-23 applies to U.S.-bound shipments; REACH Annex XVII entry 51 phthalate restrictions are satisfied by the absence of flexible PVC components. Moulding uses 150–250 t electric presses with 20:1 L/D screws, melt temperature 210–235°C, mould temperature 20–30°C, and injection speed controlled at 25–35 cm³/s to avoid weld-line blush on textured dinosaur-shell surfaces. If pack pressure drops below 40 MPa before gate freeze in parts with wall thickness above 3.0 mm, sink appears at the thickest rib root and the part fails the manufacturer’s 0.15 mm surface-level gauge inspection. Terminal articles include stackable building blocks with snap-fit tolerances, bath-time scoop toys, sand-play buckets, and educational shape sorters.
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LyondellBasell Icorene 3560 BEI 2205 Polyethylene, Linear Low Density is a linear low-density polyethylene grade in the Icorene portfolio. The numerical portion of the designation, 3560, is consistent with a nominal density of 0.935 g/cm³ and a nominal melt flow rate of 6.0 g/10 min when measured at 190°C under a 2.16 kg load according to ISO 1133-1:2022. The suffix BEI 2205 identifies the specific stabiliser and additive configuration; the exact package is proprietary and is reported on the certificate of analysis rather than inferred from the grade name alone.
The polymer belongs to the LLDPE class, meaning the molecular architecture is primarily a linear ethylene backbone with short-chain branches introduced by comonomer incorporation. This structure gives higher tensile and flexural stiffness at equivalent density than high-pressure low-density polyethylene, while retaining lower crystallinity than high-density polyethylene. The nominal density of 0.935 g/cm³ places the grade between typical LDPE homopolymer values of 0.918–0.930 g/cm³ and HDPE rotomoulding grades at 0.940–0.955 g/cm³.
The specification profile is controlled by standardised methods. Melt mass-flow rate is measured under ISO 1133-1:2022, and density is measured under ISO 1183-1:2019. Mechanical data are typically generated on compression-moulded plaques using ISO 527-2 for tensile properties and ISO 178 for flexural modulus. Published nominal values for this grade include tensile yield stress at 18 MPa, tensile elongation at break above 800%, flexural modulus near 650 MPa, Vicat softening temperature near 118°C under ISO 306 method A50, and environmental stress-cracking resistance above 1000 h under ASTM D1693 condition B in 10% Igepal CO-630 at 50°C. These values apply to moulded test specimens, not directly to as-built rotomoulded parts, because cooling rate, wall thickness, and residual stress modify final mechanical response.
Primary use is in rotational moulding of storage tanks, agricultural hoppers, intermediate bulk containers, material-handling bins, industrial housings, and removable vehicle components. The 6.0 g/10 min melt flow rate supports densification and bubble removal in sections commonly moulded between 8 and 12 mm. The 0.935 g/cm³ density balances stiffness with low-temperature impact and environmental stress-cracking resistance. Injection moulding and profile extrusion are possible when the processor can accommodate the moderate melt flow and the higher low-shear viscosity associated with linear polyethylene chains.
Compared with high-pressure LDPE of equivalent melt flow, the LLDPE grade has higher stiffness and significantly higher environmental stress-cracking resistance. The flexural modulus of 650 MPa is approximately two to three times the 200–350 MPa typical of LDPE homopolymers. The tensile yield stress of 18 MPa is also above common LDPE values of 8–12 MPa. These differences arise because the linear chains pack more efficiently than highly branched LDPE at equal density. The absence of long-chain branching, however, reduces melt extensibility and low-shear melt strength, which can influence bubble release and coating behaviour during the early stages of rotational moulding.
Relative to HDPE rotomoulding grades, the lower density of 0.935 g/cm³ reduces crystallinity and therefore lowers stiffness and top-load strength. Typical HDPE rotomoulding grades show flexural modulus values above 900 MPa, whereas this grade is nearer 650 MPa. The trade-off is improved low-temperature impact and enhanced stress-crack resistance. The ESCR value above 1000 h under ASTM D1693 condition B is a differentiating property for aggressive liquid storage and repeated temperature cycling. Many HDPE rotomoulding grades of comparable melt flow exhibit shorter failure times under the same test condition, although direct comparative data for this specific configuration is limited.
Relative to metallocene-catalysed LLDPE grades, the short-chain branching distribution may be broader if conventional Ziegler-Natta catalysis is used. The result can be lower clarity and lower dart impact in thin-wall sections, but the broader branching distribution can improve processability in thick sections and reduce shrinkage anisotropy. Published comparative data for this specific configuration is limited; direct moulding trials are required for critical applications.
In production-scale carousel-type rotational moulding, the powder is charged into steel or aluminium multi-cavity tools without pelletisation. Control of particle-size distribution is critical. A 35-mesh top cut is common for rotomoulding powders, and excessive fines increase uneven cavity packing while coarse particles sinter slowly and create pinholes at the internal surface. Typical oven air temperatures for this grade are 280–320°C. Mould internal surface temperature during densification generally reaches 180–220°C, and peak internal air temperature is maintained between 190 and 210°C to complete sintering. Above 220°C, thermo-oxidative degradation accelerates; below 190°C, bubble removal may be incomplete. The effective peak internal air temperature window for complex multi-cavity moulds can be as narrow as ±5°C around the target before under-sintered pinholes or oxidative embrittlement appear.
Biaxial rotational speed ratios of 4:1 or 3:1 are adjusted to distribute powder into deep pockets. Improper speed ratio produces thick corners and thin sidewalls, particularly in moulds with high aspect-ratio cavities. After densification, cooling is typically staged with forced air followed by water mist. Linear tooling allowance of 2.5–3.5% is generally applied, with the higher value required for large open mouldings. Rapid water quenching can increase warpage and residual stress. Mould-release temperature is usually limited to 70–80°C to reduce distortion.
Pre-drying is normally unnecessary at relative humidity below 60%. If powder has been stored outside sealed packaging or exposed to RH above 60%, drying at 70–80°C for 2 h in a desiccant dryer is recommended before charging. Surface moisture on powder particles causes steam pinholes at the mould surface and weakens weld lines at the powder-air interface.
After demoulding, rotomoulded LLDPE parts of this grade are commonly machined by routing, sawing, and hot-plate welding. Hot-plate temperature of 220–240°C with contact times of 20–40 s is typical for LLDPE, but welding parameters must be developed on production parts because weld strength depends on interdiffusion across the melt interface. Ultrasonic insertion of metallic inserts is less effective than in stiffer HDPE because of the lower modulus and higher mechanical damping of the LLDPE.
Avoid contact with copper, copper alloys, or transition-metal ions during processing, as these can catalyse oxidative chain scission. Prolonged melt exposure in air above 260°C should be avoided. The grade should not be dry-blended with high-molecular-weight HDPE powders without verifying viscosity compatibility; viscosity mismatch can produce visible flow lines and reduced impact strength.
Regulatory compliance depends on the additive package and conversion conditions, not solely on the base resin. The base olefin polymer is typically suitable for food-contact use under FDA 21 CFR 177.1520 and EU Regulation No 10/2011, provided the finished article meets overall migration limits and the BEI 2205 additive package is confirmed for the intended use. For industrial applications, REACH requires substances of very high concern to remain below 0.1 w/w per article under Regulation (EC) No 1907/2006 Article 33. RoHS Directive 2011/65/EU applies only when the moulded part is within the scope of electrical and electronic equipment.
| Regulatory domain | Reference standard or method | Verification point |
|---|---|---|
| US food contact | FDA 21 CFR 177.1520 | Base polymer identity, additive package, end-use temperature limit |
| EU food contact | EU Regulation No 10/2011 | Overall migration 10 mg/dm²; specific migration limits for additives |
| REACH SVHC | Regulation (EC) No 1907/2006 Article 33 | SVHC content 0.1 w/w per article |
| RoHS | Directive 2011/65/EU | Pb, Hg, Cd, Cr6+, PBB, PBDE limits when in EEE scope |
Conformance to these standards must be re-verified on the finished article because processing aids, colour masterbatch, and post-moulding operations can alter migration behaviour and surface composition. A laboratory migration test according to EN 1186-1 or CEN/TS 14234 is required for final compliance where food contact is claimed. The supplier’s product safety datasheet remains the controlling document for lot-specific regulatory status.