| HS Code | 344938 |
| Productname | LyondellBasell Icorene 3545 RED 4103 Polyethylene, Linear Low Density |
| Materialtype | Polyethylene, Linear Low Density (LLDPE) |
| Color | Red |
| Density | 0.935 g/cm³ |
| Meltflowrate | 4.5 g/10 min (190°C/2.16 kg) |
| Tensilestrengthatyield | 17 MPa |
| Tensilestrengthatbreak | 22 MPa |
| Elongationatbreak | 700% |
| Flexuralmodulus | 700 MPa |
| Shoredhardness | 55 |
| Vicatsofteningtemperature | 110 °C |
| Meltingtemperature | 125 °C |
| Processingmethod | Rotational molding |
| Uvstabilization | Yes |
| Form | Powder |
As an accredited LyondellBasell Icorene 3545 RED 4103 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 polyethylene bags, palletized; each pallet contains 1,000 kg of LyondellBasell Icorene 3545 RED 4103 Linear Low Density Polyethylene. |
| Container Loading (20′ FCL) | 20′ FCL: LyondellBasell Icorene 3545 RED 4103 LLDPE, 25 kg bags, palletized, typically loads 18–20 MT net. |
| Shipping | LyondellBasell Icorene 3545 RED 4103 is a non-hazardous linear low-density polyethylene resin, usually supplied as red pellets. It is not classified as dangerous goods for transport. Ship in dry, clean conditions, typically in 25 kg bags or 1000 kg bulk bags, palletized and stretch-wrapped, away from moisture and contamination. |
| Storage | Store LyondellBasell Icorene 3545 RED 4103 Polyethylene, Linear Low Density in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and open flames. Keep containers closed and separate from strong oxidizers. Avoid dust generation and accumulation. Use appropriate grounding and bonding during bulk handling to control static electricity. Follow the manufacturer’s Safety Data Sheet and local regulations. |
| Shelf Life | Shelf life is typically 12 months from date of manufacture when stored in cool, dry conditions in unopened original packaging. |
On shuttle and carousel rotational moulding lines producing non-potable chemical storage tanks, LyondellBasell Icorene 3545 RED 4103 polyethylene, linear low density powder is charged directly from sealed powder containers into cast aluminium moulds at a mass corresponding to a final wall thickness of 4–15 mm. The powder is integrally red-pigmented LLDPE; because the red pigment raises infrared absorption relative to natural LLDPE, oven residence time should be derived from peak internal air temperature rather than fixed historical setpoints. In a forced-air oven at 260–290°C, the mould is rotated biaxially at 4:1 to 8:1 speed ratio, with peak internal air temperature maintained between 200°C and 220°C until powder densification is complete. From a formulation standpoint, single-layer vertical tank walls use 100 parts by weight of Icorene 3545 RED 4103; clean in-house regrind from the same grade may replace 10–20 wt% of the charge, but regrind is excluded from the innermost layer in dual-layer constructions intended for aggressive liquid contact. The downstream process for chemical containment includes post-mould cooling in forced air or water mist, trimming at the parting line, drilling of fittings, and hydrostatic testing. The grade is specified for terminal parts such as 500–10,000 L upright cylindrical storage tanks, dosing tanks, acid and alkali secondary containment basins, and pump chambers. Compliance is anchored to ASTM D1998-21 for PE upright tank design, ASTM D1693-21 condition B stress-crack resistance, and ISO 1133-1:2022 melt flow-rate verification. If powder storage humidity exceeds 60% RH, tray drying at 60–70°C for 1–2 h before charging is necessary to prevent steam-induced micro-voids. The pigmented grade should not be combined with amine-based antistatic additives without testing, because such additives can alter surface skin formation and compromise weld-line strength.
Mobile waste container bodies made from Icorene 3545 RED 4103 are rotomoulded in two-part aluminium moulds on carousel lines. The powder charge is calculated to produce a 3–5 mm nominal wall in the lower body and a thicker rim zone. The formulation addition ratio for bin shells is 100 parts by weight virgin red LLDPE, with 15–25 wt% clean post-industrial regrind from the same production cell; the regrind fraction is limited by the EN 840-5:2020 drop test and by low-temperature impact retention. Peak internal air temperature is held at 200–210°C; the oven setpoint ranges from 270–285°C. Mould rotation ratios around 4:1 to 5:1 are used to reduce thick-thin variation at the base corner radius, where drop failures initiate. Terminal part types include 120 L, 240 L, and 360 L two-wheel bin bodies, with injection-moulded lids and axles assembled downstream. Compliance testing includes EN 840-1:2020 for dimensional interoperability, EN 840-5:2020 for performance and drop/impact testing, and ISO 179-1:2010 or ASTM D256-23 for material impact characterisation. If bins are stored outdoors, UV stabilisation must be confirmed on the certificate of analysis; where the grade is not UV-stabilised for the intended lifetime, a compatible LLDPE-based UV masterbatch at 1–3 wt% is dry-blended, but this is not required when the integrated stabiliser package is present.
Because red-pigmented LLDPE absorbs more radiant energy than natural rotomoulding powder, traffic bollard and delineator shells on shuttle machines frequently exhibit shorter oven cycles but higher risk of early surface gelation at sharp mould corners. The charging ratio for a 1.0–1.5 m hollow bollard shell is based on a 5–8 mm nominal wall and uses 100 parts by weight Icorene 3545 RED 4103; clean regrind from trimmed shells may be added up to 15 wt%. The production process involves charging the powder into steel or aluminium moulds mounted on a shuttle or rock-and-roll machine, biaxially rotating at 3:1 to 6:1, and melting at oven air temperatures of 260–280°C until internal air reaches 195–215°C. After moulding, the shell is cooled slowly to 70–80°C before demoulding to limit ovality and sink marks. Compliance for material properties is verified through ASTM D638-22 tensile yield, ASTM D256-23 notched Izod impact, and ASTM G154-23 accelerated weathering when outdoor service is specified. Terminal products include traffic delineator drums, roadworks warning bollards, sign base covers, and temporary barrier end caps. The grade is not suitable for load-bearing guardrail components; use is restricted to shells and covers where vehicle impact is not a mechanical design input.
Foam-filled marine marker buoys and float shells use Icorene 3545 RED 4103 in the outer skin because the red colour provides colour-coded marking without post-mould painting, which would reduce adhesion and require solvent-based coatings. In rock-and-roll processing, the outer skin is first moulded from 100 parts by weight of the solid red LLDPE powder to a wall thickness of 4–6 mm; after the skin has gelled, the second charge consists of the same powder dry-blended with 0.5–1.0 wt% of an azodicarbonamide-based chemical foaming agent to form a closed-cell PE foam core. The rock-and-roll machine uses a 1:4 to 1:5 ratio between major and minor axis rotation, with oven air temperatures at 250–270°C for the skin and 220–250°C for the foam core. Terminal products are navigation buoy hulls, mooring floats, pontoon floats, and fender shells. Compliance for material selection references ISO 1133-1:2022 for melt flow rate, ASTM D1693-21 for environmental stress-crack resistance, and ASTM D638-22 for tensile properties. Because no single ISO product standard governs all rotomoulded marine float categories, hydrostatic testing at the intended service depth is specified between buyer and moulder. The solid skin layer should not be thinned below 4 mm in highly loaded mooring floats, and the foamed core density should be specified from buoyancy calculations rather than fixed by resin supplier data.
Agricultural feed troughs and mineral supplement tubs are rotomoulded from Icorene 3545 RED 4103 at wall thicknesses between 4 mm and 8 mm. The charge formulation is 100 parts by weight virgin powder; 10–20 wt% clean in-house regrind is used for trough bodies, but the regrind is sieved to 500 µm maximum powder particle size before blending. Rotational moulding is performed in carousel or shuttle units at oven temperatures of 250–280°C with peak internal air temperature of 190–210°C. Terminal products include calf and cattle feed troughs, creep feeders, mineral lick tubs, and farrowing partition corners. Material compliance for feed-contact use is not equivalent to human food-contact clearance; FDA 21 CFR 177.1520 may apply to the base olefin polymer, but the final article must be assessed under the destination market's feed-contact and migration rules. ESCR testing per ASTM D1693-21 is specified where salt-containing mineral blocks are placed directly in the trough.
For rotomoulded playground tunnel sections, roof domes, and spring-rider bodies made from Icorene 3545 RED 4103, integral red pigmentation eliminates post-mould painting, which can crack on flexible LLDPE surfaces. The powder charge is set for a 5–10 mm wall, with 100 parts by weight virgin powder and up to 15 wt% clean regrind from the same moulding cell. Moulds are aluminium with polished internal surfaces to reduce parting-line flash on child-contact edges; oven temperature is 260–280°C and peak internal air temperature is 200–215°C. After demoulding, cutouts and fastener holes are machined, and edges are radiused to meet EN 1176-1 or ASTM F1487-21 entrapment and protrusion limits. Terminal part types include tubular tunnel sections, roof domes, activity panels, and spring-rider shells. Compliance for material weathering is checked by ASTM G154-23; mechanical characterisation is performed per ASTM D638-22 and ASTM D256-23. For outdoor UV stability, the certificate of analysis must confirm the UV stabiliser package because red pigment alone does not provide light stabilisation.
Red-pigmented LLDPE is rotomoulded into underground cable joint chambers and valve boxes where red is used as a buried-infrastructure warning colour. Large rectangular chambers require 6–12 mm wall sections and ribbed designs to resist soil and light vehicle loads; the powder charge is 100 parts by weight virgin red LLDPE with 10–25 wt% recycled material only from the same chamber production line. Processing is performed on a shuttle machine with oven setpoints of 260–285°C and internal air temperature of 195–215°C. Demoulding is delayed until the part cools below 70°C to avoid stress relaxation that creates lid-sealing surface distortion. Terminal products include underground telecommunications joint chambers, cable pits, irrigation valve enclosures, and marker posts. Compliance is assessed through ASTM D638-22, ASTM D790-17 flexural modulus, and ASTM D1693-21 ESCR. Load-bearing chamber covers should be tested to the applicable access-cover standard in the destination country rather than to material-only values.
When dilute acids, alkalis, and chloride-bearing cleaning regimes govern material handling in industrial plants, Icorene 3545 RED 4103 is rotomoulded into bins and trays rather than painted metal or glass-reinforced plastic. The dry-blend ratio for these parts is 100 parts by weight virgin red LLDPE with 15–25 wt% clean in-plant regrind; for trays holding aggressive liquids, regrind inclusion is capped at 15 wt% to preserve stress-crack resistance. The moulding process uses shuttle or carousel machines, aluminium or fabricated steel moulds, and wall thicknesses from 5 mm to 12 mm; peak internal air temperature is controlled between 200°C and 215°C. Terminal part types include open-top tote boxes, 4-way entry hopper bins, drum spill trays, and custom work-in-progress containers. Compliance for material properties is verified via ISO 1133-1:2022, ASTM D638-22, and ASTM D1693-21. This grade is not formulated for static-dissipative duty; service in zones requiring surface resistivity below 109 Ω/square requires an external conductive pathway to be engineered into the part or an alternative conductive grade.
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LyondellBasell Icorene 3545 RED 4103 is a pre-coloured linear low-density polyethylene compound based on the Icorene 3545 rotational-moulding grade. The RED 4103 suffix identifies a red colour preparation dispersed into the LLDPE matrix before particle-size reduction. The product is evaluated as a sinter-moulding feedstock rather than as a high-shear injection-moulding resin; melt viscosity, oxidation stability, pigment dispersion, particle-size distribution, and impact retention after biaxial rotation are the controlling parameters. Exact property values for the pigmented compound are less frequently published than for the unpigmented base resin; lot-specific certificate data from LyondellBasell or the compounder therefore remain mandatory before tooling and process parameters are fixed.
The base resin Icorene 3545 is classified as an LLDPE rotational-moulding grade with a nominal melt mass-flow rate in the 4.0–5.0 g/10 min range when determined at 190 °C under 2.16 kg load according to ASTM D1238 or ISO 1133-1:2022. Solid-state density for the natural base resin is typically reported in the 0.934–0.938 g/cm³ range according to ISO 1183-1:2019 or ASTM D1505-18. The RED 4103 pigment package modifies the matrix enough that the pigmented compound commonly exhibits a density 0.002–0.006 g/cm³ higher and a melt flow rate 0.2–0.6 g/10 min lower than the unpigmented version; exact shifts depend on pigment concentration and dispersion conditions. Mechanical property expectations for the class are summarised below.
| Property | Test standard | Typical class range | Unit |
|---|---|---|---|
| Melt mass-flow rate | ASTM D1238 / ISO 1133-1:2022 | 4.0–5.0 | g/10 min |
| Solid-state density | ISO 1183-1:2019 / ASTM D1505-18 | 0.934–0.938 | g/cm³ |
| Tensile yield stress | ISO 527-2:2012 | 17–20 | MPa |
| Tensile elongation at break | ISO 527-2:2012 | >800 | % |
| Flexural modulus | ISO 178:2019 / ASTM D790-17 | 600–750 | MPa |
| Vicat softening temperature, A50 | ASTM D1525-17e1 | 112–120 | °C |
| Low-temperature brittleness | ASTM D746-20 | <-60 | °C |
These ranges are not contractual specifications. Rotomoulding product control is normally based on density, MFR, particle-size profile, colour strength, and pigment dispersion rather than on tensile or flexural values alone. Published data for this specific red configuration is limited, so laboratory-scale sintering trials should precede production mould construction.
On a Ferry-type carousel rotational-moulding machine with arm radii between 1.2 m and 2.4 m, the material is subjected to biaxial rotation at 4–8 rpm on the primary axis and 0.8–1.5 rpm on the secondary axis. The powder must compact against the mould surface and undergo densification before complete melting. Residual particle boundaries are the dominant defect when peak internal air temperature remains below 190 °C; tensile elongation at break measured by ISO 527-2:2012 commonly drops below 400%, compared with >800% for fully sintered sections, because the particle interfaces act as crack-initiation sites. Production-scale observations show that peak internal air temperature between 210 °C and 230 °C, with oven setpoints of 280 °C to 310 °C, produces acceptable coalescence for 4–6 mm wall thickness. The heating rate measured by a baffle-mounted thermocouple inside the mould should be 8–12 °C/min for medium-walled parts.
Cooling rate determines crystal size, density, and residual stress. Rapid air cooling at 20–30 °C/min to demould below 80 °C increases productivity but lowers stiffness and may produce higher internal stress. Slow cooling at 5–10 °C/min through the crystalline solidification range improves dimensional stability and environmental stress-crack resistance but extends cycle time. Non-uniform cooling over deep draw areas produces warpage; measured shrinkage in a 150 mm × 150 mm × 3 mm plaque can range from 1.5% to 2.5% under forced-air cooling.
Pre-drying is generally unnecessary for dry powder, but surface condensation at relative humidity above 80% or storage-temperature swings greater than 15 °C can raise moisture content above 0.07 wt%. Bubbles form when volatiles are released during sintering; hopper dryers set to 70–80 °C for 1–2 h are used before production. The powder should be free of fines below 75 µm at levels above 10 wt% because excessive fines reduce bulk density and cause uneven melt distribution in narrow ribs. A typical rotomoulding feedstock is 35-mesh powder with 80–95% by mass between 150 µm and 500 µm. Particles coarser than 500 µm increase pinholing, while bulk density below 330 kg/m³ is associated with inconsistent wall thickness.
The Icorene 3545 RED 4103 class differs from standard rotomoulding HDPE in the 0.940–0.954 g/cm³ density range and from high-flow injection-moulding LLDPE with MFR of 20–50 g/10 min. The lower density of the Icorene 3545 class provides higher elongation at break and better environmental stress-crack resistance under ASTM D1693-21; the unpigmented base can exceed 1000 h in typical ESCR testing. Rotomoulding HDPE offers higher flexural modulus, lower gas permeability, and better chemical resistance for fuel tanks and aggressive agricultural containers. High-flow injection-moulding LLDPE is unsuitable for rotomoulding because its low zero-shear viscosity prevents uniform wall build-up; conversely, the Icorene 3545 RED 4103 class is not suitable for high-speed injection moulding because MFR below 5 g/10 min requires excessive melt temperature and injection pressure.
| Material class | Normal solid-state density | Normal MFR | Shear environment | Rotomoulding sintering range |
|---|---|---|---|---|
| Icorene 3545 RED 4103 class | 0.934–0.938 g/cm³ | 4.0–5.0 g/10 min | Low-shear, biaxial rotation | 210–230 °C peak internal air |
| Unfilled rotomoulding HDPE | 0.940–0.954 g/cm³ | 3.0–6.0 g/10 min | Low-shear, biaxial rotation | 210–240 °C peak internal air |
| High-flow injection-moulding LLDPE | 0.916–0.930 g/cm³ | 20–50 g/10 min | High-shear, screw plastication | Not applicable |
Red pigmentation imposes separate differences. The RED 4103 colour package may contain organic or inorganic red pigments dispersed in an LLDPE carrier; composition must be verified before food-contact use. Pigment agglomerate size should remain below 20 µm for streak-free surfaces. In twin-screw extrusion compounding at L/D 36:1 and melt temperature 190–210 °C, a 250 µm downstream screen pack is commonly used to remove coarse agglomerates. Failure to control pigment particle size creates visible red streaks on thin-walled parts and lowers colour consistency under the CIE L*a*b* system measured with a spectrophotometer using D65 illuminant and 10° observer.
Regulatory status cannot be inferred from the product name alone. The unpigmented LLDPE base may meet the olefin polymer requirements of 21 CFR 177.1520(c) if the specified extractables limits are met, but the RED 4103 colour package requires separate authorisation under 21 CFR 178.3297 or equivalent migration testing per EU Regulation (EU) No 10/2011 when direct food contact is intended. REACH Regulation (EC) No 1907/2006 registration for the colour preparation must be obtained from the supplier. RoHS Directive 2011/65/EU as amended by (EU) 2015/863 limits lead, cadmium, mercury, hexavalent chromium, and selected phthalates; verification should follow IEC 62321 test methods. If the part will be used outdoors, ultraviolet stabilisation must be specified separately because red pigmentation does not automatically provide sufficient UV resistance; dark red grades may show higher surface temperature under solar load, accelerating oxidation without additional UV stabiliser.
Oxidising agents, high levels of free-radical initiators, and certain amine-based flame-retardant packages can alter the red colour and reduce molecular weight during processing. Processing above 240 °C internal air temperature for extended periods is not recommended because oxidative chain scission reduces notched impact performance tested under ISO 179-1/1eA. The compound should not be stored in direct sunlight for more than 12 months; inventory should be consumed first-in first-out. If regrind is reintroduced, the red pigment concentration must be corrected to account for pigment decomposition and dilution.