| HS Code | 270995 |
| Polymer Type | Linear Low Density Polyethylene (LLDPE) |
| Density | 0.945 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 3.5 g/10 min |
| Tensile Strength At Yield | 17.0 MPa |
| Tensile Strength At Break | 24.0 MPa |
| Elongation At Break | 700% |
| Flexural Modulus | 700 MPa |
| Vicat Softening Point | 110°C |
| Deflection Temperature At 0 45 Mpa | 55°C |
| Hardness Shore D | 60 |
| Brittleness Temperature | < -70°C |
| Environmental Stress Crack Resistance | > 1000 h |
| Uv Stabilization | Present |
| Color | Green |
As an accredited LyondellBasell Icorene 3545 UV+ GRN 6413 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 3545 UV+ GRN 6413 is supplied in 25 kg polyethylene bags, palletized and stretch-wrapped; each pallet contains 1,000 kg. |
| Container Loading (20′ FCL) | 20′ FCL full container loading of LyondellBasell Icorene 3545 UV+ GRN 6413 Linear Low Density Polyethylene chemical resin. |
| Shipping | LyondellBasell Icorene 3545 UV+ GRN 6413 Polyethylene, Linear Low Density, is typically shipped as non-hazardous resin pellets in 25 kg bags, octabins, or bulk trucks/railcars. It is not regulated as dangerous goods. Transport in clean, dry equipment; avoid excessive heat, moisture, and packaging damage. |
| Storage | Store in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, sparks, and open flames. Keep original packaging sealed, palletized, and off the ground. Avoid moisture, dust, and contamination. Do not stack excessively. Maintain temperatures below 50°C (122°F), away from strong oxidizers. Protect from UV light and physical damage. Use first-in, first-out stock rotation. Follow the manufacturer's SDS and local regulations. |
| Shelf Life | LyondellBasell Icorene 3545 UV+ GRN 6413 has a shelf life of 12 months when stored in original, cool, dry, well-ventilated packaging. |
LyondellBasell Icorene 3545 UV+ GRN 6413 is processed as a rotational moulding powder in closed, biaxially rotated aluminium or fabricated steel moulds. In agricultural water storage and fertigation tank production, the powder is charged into cast A356 aluminium moulds with wall thickness targets of 6.0 mm to 12.0 mm for capacities between 1,000 L and 20,000 L. Venting through a 19 mm to 25 mm PTFE-lined vent stack maintains the internal cavity at near atmospheric pressure during the heating cycle, which on a carousel machine with a 4.0:1 primary-arm ratio and a 1.0:1 secondary-arm ratio typically runs at an oven setpoint of 285°C to 300°C for the green pre-coloured grade. The shot weight is calculated from the cavity surface area multiplied by the specified minimum wall thickness, the melt density from the lot certificate under ISO 1183-1 Method D, and a 3% to 5% process allowance for corner thinning and kiss-off consolidation. Peak internal air temperature is controlled at 195°C ± 5°C; plant records from multi-year production runs indicate that excursions above 215°C for more than 4 min may reduce notched impact values after post-mould annealing by more than 10% in some lots, although published data for this specific configuration is limited. The part is cooled with forced ambient air to an internal temperature of 80°C before exterior water mist is introduced; early water contact before 70°C increases warpage on flat sidewalls beyond the 0.5% flatness tolerance specified in ASTM D1998-21 for upright tanks. Terminal articles include 2,000 L to 10,000 L agricultural sprayer tanks, nurse tanks, and fertigation tanks for acidulated fertiliser solutions, where the LLDPE matrix provides environmental stress-crack resistance under ASTM D1693-15 conditions above 500 h in 10% Igepal CO-630 at 50°C for many rotational moulding grades, but end-users must request lot-specific ESCR data from the certificate of analysis before qualifying concentrated liquid fertiliser contact. A 20 wt% regrind ceiling is commonly applied to the UV-exposed outer skin when a three-layer structure is used; higher regrind levels are confined to the hidden middle layer and must not exceed 30 wt% unless a full UV weatherability study is performed under ISO 4892-3 cycle 1.
Thin-wall rotomoulded enclosures for irrigation valves and water meter pits are moulded from the same pre-coloured green powder, but cycle control differs from large tank production because the surface-area-to-volume ratio is higher. For a nominal wall thickness of 3.5 mm to 5.0 mm in a fabricated aluminium mould heated on an electrically heated shuttle machine, the oven dwell time is commonly 14 min to 20 min at a cavity surface target of 190°C to 200°C, and the peak internal air temperature is deliberately capped below 205°C. The ceiling is dictated by the tendency of UV-stabilised LLDPE to develop internal gloss and pinholing at sharp ribs when the inner melt is held above 200°C for more than 90 s. Vent stack diameter is reduced to 12 mm to 16 mm for these parts to retain enough internal pressure to force corner definition without blowing the mould parting line; a pressure bleed of 2 kPa to 5 kPa is typical. The powder is not pre-dried unless open storage has raised moisture above 0.05 wt%. Low-temperature impact acceptance is determined under ASTM D5276 or ISO 6603-2, but the procurement specification must state the minimum puncture energy because no universal norm fixes a single value for all greenhouse and landscape valve box geometries. End items include 300 mm to 900 mm round and rectangular valve boxes, water meter pits, and enclosures for drip irrigation manifolds, where resistance to seasonal temperature cycling and soil contact is more critical than food-contact status.
Chemical storage vessels and inner shells of composite intermediate bulk containers are rotomoulded from the same green LLDPE powder where the outer cage supplies structural support and the shell provides the liquid contact layer. The rotomoulded shell is typically produced at a wall thickness of 4.0 mm to 6.5 mm and then evaluated under the hydrostatic pressure test sequence of ADR 2023 or 49 CFR 178.704, depending on the shipment route; the vent opening and fill port are included in the test rather than trimmed off. Icorene 3545 UV+ GRN 6413 provides low-temperature impact and stress-crack resistance expected of linear low-density polyethylene, but the grade must not be used for strong oxidizers, aromatic hydrocarbons, or chlorinated solvents without a 30-day immersion screening under ASTM D543-21 using production-moulded coupons. In a three-layer shell construction, virgin green powder is charged first to form the outer skin, regrind from trimmed openings is limited to 30 wt% in the middle layer only, and virgin powder is again used for the inner contact layer to reduce extractables. This 30 wt% middle-layer regrind ceiling is drawn from standard rotomoulding practice for non-food chemical tanks; it is not a producer recommendation for this specific lot. The heating cycle uses a 290°C to 310°C forced-air oven with peak internal air temperature of 200°C ± 5°C. Because the green pigment increases the melt surface temperature under infrared oven conditions, line operators often reduce oven dwell by 2 min to 4 min compared with unpigmented LLDPE of equal wall thickness; this offset must be verified by a thermocouple log on each new mould geometry. Terminal products include 250 L to 2,000 L vertical and horizontal chemical storage tanks, secondary containment basins, and inner shells for composite IBCs used in agricultural adjuvant transport.
| Article / segment | Standard or code | Test method / clause | Production control note |
|---|---|---|---|
| Agricultural upright storage tank | ASTM D1998-21 | Wall thickness and flatness after conditioning | Verify minimum wall after corner thinning; warpage measured on flat sidewall |
| Chemical IBC inner shell | ADR 2023 / 49 CFR 178.704 | Hydrostatic pressure and leakproofness test | Use production-moulded part; gate and vent areas included |
| Playground panel | EN 1176-1:2017 and ASTM F1487-21 | Entrapment geometry, impact | Part-specific; no generic substitution from tank data |
| Dry food handling bin | FDA 21 CFR 177.1520(c) | Extraction and migration testing | Confirm density-specific olefin polymer classification |
| Marine float shell | ISO 62:2008 | Water absorption, 24 h at 23°C | Report as finished-wall sample; published data for this green grade limited |
Outdoor playground panels and roofs are a demanding downstream segment because the part must retain low-temperature ductility after years of ultraviolet exposure while satisfying head and limb entrapment geometry clauses in ASTM F1487-21 or EN 1176-1:2017. In this application, the green pre-coloured LLDPE is selected for a minimum nominal wall of 5.0 mm to 6.0 mm over panels up to 2.4 m in major dimension, using a female electroformed or CNC-machined aluminium mould with a parting-line draft of at least 1.5°. The powder is not pre-dried unless the granule moisture exceeds 0.05 wt% after open storage; this threshold is standard for polyolefin rotomoulding powders. Cycle development begins with an oven setpoint of 280°C to 295°C, and the internal air temperature at the mould centre is ramped to 200°C over 16 min to 22 min, depending on surface-to-mass ratio. The part is rotated at a primary-to-secondary arm speed ratio of 4:1, with the secondary axis held at 8 rpm to 12 rpm throughout the fusion stage; this speed band avoids powder bridging in deep pockets and minimises bubbles at rib intersections. The critical process limitation is warpage after demoulding: panels longer than 1.8 m are placed in a flat cooling jig immediately after release and held at 40°C to 60°C for 30 min to prevent edge curl beyond 3 mm per metre as measured by a straightedge and feeler gauge. The finished part is tested under ISO 6603-2 at −20°C for perforation energy, and under ASTM D638 Type IV at 23°C for tensile elongation at yield, but the procurement specification should request lot-specific values rather than relying on family data. End products include rotomoulded slide hoods, tunnel roofs, vertical play panels, and shading fins.
Marine aquaculture floats and mooring buoys impose a unique combination of continuous water absorption and ultraviolet exposure that is not reproduced by standard agricultural tank testing. Because float shells are closed, rotationally moulded bodies with wall thicknesses of 6.0 mm to 10.0 mm, the moulding cycle must produce a fully densified outer skin to limit water absorption under ISO 62 after 24 h at 23°C for many olefin polymers; the processor must confirm the value for this grade. The green colour in Icorene 3545 UV+ GRN 6413 reduces the need for post-mould painting, but abrasion from sand and boat contact can remove surface layers, exposing the UV-stabilized bulk. Therefore, superficial impact damage is evaluated by repeated drop testing from 3 m onto concrete per customer specification, and the part must not crack at −10°C. A key processing control is the cooling stage: after the peak internal air temperature of 195°C to 205°C is reached, the mould is cooled by ambient forced air to 90°C, then by air-mist to 50°C before opening; cooling too quickly through the 80°C to 60°C range creates residual stress at brass insert bosses, leading to water intrusion around metal threads. The incorporation of recycled LLDPE is limited to 20 wt% in the outer shell because higher levels have been associated with brittleness in cold-water impact in some lot evaluations; this limit should be validated for each UV-stabilized compound. Terminal outputs include rotomoulded floats for mussel and oyster lines, buoy shells for navigation markers, and flotation collars for fish cages. The article is not considered a food-contact item under EU Regulation 10/2011 unless a migration test specific to the finished part is performed; published data for this specific green-pigmented rotomoulding grade is limited.
Double-wall rotomoulded planters and public-space furniture segments combine a near-continuous outer skin with a partially foamed or hollow core, and the green pre-coloured powder is used for the outer skin because it does not require painting after demoulding. For a double-wall planter with a nominal outer wall of 5.0 mm to 8.0 mm, the mould is heated in a rock-and-roll machine with a 45° tilt angle and a rotation speed of 6 rpm to 10 rpm on the major axis; the peak internal air temperature is held at 195°C to 205°C to prevent collapse of the inner wall before the outer wall has fully sintered. A chemical blowing agent may be used at 0.5 wt% to 1.5 wt% in the core layer when weight reduction is specified, but this must be evaluated for interference with the UV stabilization package. Post-mould trimming generates irregular regrind; the addition of this regrind into the outer skin is limited to 15 wt% because higher levels increase surface roughness on the downstream side and may lower impact retention after 3,000 h of accelerated weathering under ISO 4892-3 cycle 1. The lack of a universal pass value for green colour retention means the finished planter specification should define a maximum ΔE and a minimum tensile elongation retention under ISO 527-2 at 23°C; published data for this specific green-pigmented rotomoulding grade is limited. Terminal products include large planters, street furniture bases, and architectural facade panels.
Rotomoulded bins and hoppers used in harvested produce handling and dry food ingredient transfer are produced from the same green LLDPE powder but require attention to regulatory classification under FDA 21 CFR 177.1520(c) because the density of the olefin polymer determines the applicable specification, not the rotomoulding grade name. A food-contact bin intended for dry bulk contact is normally moulded at 5.0 mm to 8.0 mm wall thickness and polished to a surface finish of 0.4 µm Ra or better on the contact side to minimize residue accumulation. The processor must not use external mold release systems containing silicone or fatty acid salts on the contact surface unless the release agent is separately covered by a food-contact listing; per-mould release evaluation is based on extraction testing under FDA 21 CFR 177.1520(c) and organoleptic screening. The recommended cycle for food-handling bins uses a lower oven temperature of 270°C to 285°C to avoid surface degradation that increases hexane extractables; peak internal air temperature is maintained at 185°C to 195°C, which is slightly below the agricultural tank target because colourants and residual catalyst constituents are more likely to migrate at higher heat history. Terminal products include 30 L to 600 L produce totes, dry ingredient hoppers, and conveyor discharge chutes, where the green colour provides zone identification without secondary labelling. Because this is a linear low-density grade, the finished bin has a lower flexural modulus than structural high-density polyethylene and may require external stiffening ribs when the unsupported span exceeds 600 mm.
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LyondellBasell Icorene 3545 UV+ GRN 6413 Polyethylene, Linear Low Density is a UV-stabilised, green-pigmented linear low density polyethylene rotational molding powder. The Icorene designation identifies the LyondellBasell rotomolding product family, while the numeric sequence 3545 is linked to a nominal melt flow rate of 4.5 g/10 min at 190 °C under 2.16 kg load when tested according to ISO 1133-1:2022. The suffix UV+ indicates an ultraviolet stabilizer package intended for prolonged outdoor exposure, and GRN 6413 is the manufacturer’s colour code for the green powder. The base resin has a nominal density of 0.935 g/cm³ under ISO 1183-1:2019. The comonomer responsible for the short-chain branching in the linear low density polyethylene is not declared in the publicly available LyondellBasell technical literature; the density and mechanical profile are consistent with an ethylene-butene or ethylene-hexene LLDPE, but the comonomer identity should not be treated as a specification. The material is supplied as a dry-flowing powder for carousel, shuttle, and satellite-type biaxial rotational molding machines, where it is processed through particle densification and sintering rather than continuous screw extrusion. Because the GRN 6413 pigment concentrate absorbs visible and near-infrared radiation differently from natural or white grades, surface temperature rise and colour change under outdoor exposure must be evaluated on the finished article rather than extrapolated from unpigmented base-resin data.
The functional difference from an unmodified linear low density polyethylene rotational molding powder is not limited to pigmentation. Three property domains change: weathering resistance, solar absorption behaviour, and internal additive burden. The UV+ package is formulated to delay ultraviolet-induced chain scission and loss of fracture resistance at the moulded surface. Accelerated weathering of the unpigmented UV+ base under ISO 4892-2:2021 or ISO 4892-3:2016 generally evaluates tensile elongation retention and Charpy impact retention after a defined xenon-arc or fluorescent UV exposure. Published lot-specific weathering data for the GRN 6413 green variant are limited; therefore, qualification of a production part should include colour change, gloss retention, and low-temperature impact testing after 2,000–4,000 h of artificial weathering. The green pigment increases visible-light absorption compared with white or natural powder, so the external surface of a large flat panel can operate at a higher temperature in direct sunlight. Thermocouple mapping of the moulded part and pyrometer measurement of the mould surface are advisable when the green part is compared against a natural control. The thermal expansion coefficient of the filled surface layer is not meaningfully different from the base polymer, but repeated solar heating can increase creep in large unsupported panels; long-term deformation should be screened under load at 50 °C or 60 °C before production release.
Compared with a high-density polyethylene rotational molding powder of similar melt flow rate and wall thickness, the Icorene 3545 UV+ base has lower flexural modulus, higher elongation at break, improved environmental stress crack resistance, and lower heat deflection temperature. This characteristic provides greater tolerance for impact and flexural fatigue in outdoor service, but it reduces suitability for static structural loads at elevated temperature. Compared with low-flow LLDPE rotomolding grades in the 2.0–3.0 g/10 min melt flow range, the 4.5 g/10 min melt flow rate of Icorene 3545 UV+ improves bubble removal and can assist densification in complex or narrow mould sections. The trade-off is a greater tendency for anisotropic shrinkage in thick sections if cooling is too rapid. The exact stabilizer chemistry is not publicly disclosed, but the UV+ designation implies a package selected to retain impact and tensile properties after outdoor weathering for longer periods than the non-UV+ base. Processors should not interpret the UV+ label as a universal weathering warranty; service life depends on wall thickness, pigment concentration, surface erosion, and regional solar irradiance.
The nominal values below are taken from the natural UV+ technical data profile and are provided as a screening matrix. The green-pigmented GRN 6413 lot should be checked against the certificate of analysis, and a shift of up to ±5 % in modulus and impact values may occur due to pigment concentrate dilution. The table is not a release specification; the lot-specific certificate of analysis remains the binding document for acceptance testing.
| Property | Test method | Unit | Nominal value |
|---|---|---|---|
| Melt flow rate, 190 °C, 2.16 kg | ISO 1133-1:2022, ASTM D1238-20 | g/10 min | 4.5 |
| Density | ISO 1183-1:2019, ASTM D1505-18 | g/cm³ | 0.935 |
| Tensile modulus | ISO 527-2:2012, ASTM D638-14 | MPa | 550 |
| Tensile stress at yield | ISO 527-2:2012, ASTM D638-14 | MPa | 16 |
| Tensile strain at yield | ISO 527-2:2012, ASTM D638-14 | % | 12 |
| Flexural modulus | ISO 178:2019, ASTM D790-17 | MPa | 520 |
| Charpy notched impact, 23 °C | ISO 179-1:2010 | kJ/m² | 7 |
| Environmental stress crack resistance, condition B | ASTM D1693-21 | h | >1,000 |
For incoming inspection, melt flow rate and density are normally sufficient for lot-to-lot consistency. The green pigment can influence melt flow rate slightly, but this is usually within the reproducibility limit of ISO 1133-1. For applications where low-temperature impact is critical, the processor should also request lot-specific notched Charpy or instrumented puncture data according to ISO 6603-2:2023, because rotational molding powder particle size distribution can influence the sintering quality and the resulting impact performance.
On a four-arm carousel rotomolding machine with a gas-fired clamshell oven, the green powder is charged into the mould, the mould is rotated about two perpendicular axes, and the polymer densifies onto the heated cavity surface. For a 4 mm nominal wall section, an oven set temperature of 280–300 °C and a peak internal air temperature of 200–220 °C are common starting points. If the peak internal air temperature fails to reach 190 °C, the inner surface can retain sintering porosity, and low-temperature instrumented puncture impact under ISO 6603-2:2023 may fall below the value expected from a fully coalesced wall. A peak internal air temperature above 230 °C accelerates consumption of the antioxidant and UV stabilizer package, producing yellowing and embrittlement at the inner surface, especially in thick sections that experience extended cool-down. The 4.5 g/10 min melt flow rate permits densification at a somewhat lower peak internal air temperature than a 2.0–3.0 g/10 min rotomolding LLDPE, but it does not permit the elimination of the soak period; the oven cycle should not be terminated until the thermocouple has remained in the target range for the wall-thickness-dependent hold time.
Batch-to-batch variation in rotational molding powder particle size distribution can alter dry-flow angle and heating rate, shifting the measured peak internal air temperature by ±3–5 °C. When a new powder lot is introduced, the heating recipe should be re-verified with a thermocouple placed at the mould vent. Differential scanning calorimetry of LLDPE in this density class typically shows a broad melting endotherm between 105 °C and 125 °C, with peak melting near 120 °C; the green masterbatch may shift the apparent melting peak by ±2 °C depending on dilution and pigment carrier resin. Sintering behaviour is governed by zero-shear viscosity, particle surface area, and heating rate. Because Icorene 3545 UV+ has a higher melt flow rate than many impact-modified rotational molding LLDPE grades, bubble elimination in the inner surface is generally improved. Nevertheless, excessive oven time at high set temperature does not compensate for non-uniform mould wall thickness; thick sections may develop a hot inner surface while the outer surface remains below the degradation threshold, creating a through-thickness thermal gradient that leads to warpage after cooling.
Cooling after oven removal is divided into forced-air, mist, and spray stages. The highest warpage risk occurs between 120 °C and 80 °C, when rapid heat removal from the mould surface sets a temperature gradient through the wall. Cooling rates above 10 °C/min in this interval have been associated with flat-panel warpage on production-scale clamshell machines; rates below 4 °C/min reduce residual stress but increase cycle time and cost. The green pigment can make mould release residue less visible on the finished surface; therefore, external release agent application should not be driven solely by visual contamination. Silicone-based external demoulding agents that remain on the mould surface can be transferred to the green part and interfere with post-moulding painting or adhesive bonding. If the part is specified for adhesive assembly, a release-agent-free trial should be run and surface energy checked under DIN 55660-2:2011 or a comparable contact-angle method.
Powder stored at high relative humidity can carry surface moisture. If dry-flow performance or bulk density testing indicates clumping, the material may be pre-dried in a dehumidified hopper at 60–70 °C for 2–4 h. Drying above 80 °C can cause incipient particle sintering and hopper bridging. The material is optimised for rotational molding; continuous extrusion processing should be validated separately because the stabilizer package and particle morphology are tailored to long oven residence and low shear conditions.
| Processing parameter | Starting range for 4 mm wall | Measurement equipment |
|---|---|---|
| Oven set temperature | 280–300 °C | Gas-fired clamshell oven, calibrated thermocouple |
| Peak internal air temperature | 200–220 °C | Mould vent thermocouple, data logger |
| Biaxial speed ratio | 4:1 ± 0.5 | Carousel arm encoder |
| Forced-air cooling to 100 °C | 8–15 min | Part surface infrared pyrometer |
| Demoulding temperature | 50–60 °C | Mould surface contact thermocouple |
The processing ranges in the second table are starting points for a 4 mm wall section and are not product-specific guarantees. Production settings must be established by thermocouple mapping of the specific mould geometry, because part corners, ribs, and metal frame contact points create local heating and cooling differences that cannot be captured by a single oven set temperature.
In outdoor rotational molded components such as agricultural tanks, chemical storage units, playground structures, and moulded furniture, the green UV-stabilised LLDPE is selected where the part must tolerate repeated impact and weathering. The Icorene 3545 UV+ base offers higher elongation and better environmental stress crack resistance than a typical rotational HDPE with a density near 0.945–0.955 g/cm³, but the trade-off is lower modulus and lower heat deflection temperature. For direct food contact applications, compliance with FDA 21 CFR 177.1520 for the unpigmented olefin base should not be assumed for the GRN 6413 green variant; the colorant package must be cleared separately. Published weathering data for the green-pigmented powder are limited, so pre-production testing according to ISO 4892-2:2021 or ASTM D2565-21 is required when long outdoor service life is a specification requirement. If the moulded parts are to be painted or adhesively bonded after moulding, the external release agent protocol should be interrupted for a controlled trial to verify that surface energy and adhesion are not degraded by transferred release chemistries.