| HS Code | 297989 |
| Polymer Type | Polyethylene, Linear Low Density |
| Density | 0.935 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 6.0 g/10 min |
| Melting Point | 124 °C |
| Vicat Softening Point | 99 °C |
| Tensile Strength At Yield | 14 MPa |
| Tensile Strength At Break | 19 MPa |
| Elongation At Break | 700% |
| Flexural Modulus | 400 MPa |
| Hardness Shore D | 55 |
| Color | Green |
| Form | Pellets |
| Processing Method | Injection Molding |
As an accredited LyondellBasell Icorene 3560 GRN 6145 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 GRN 6145 Linear Low Density Polyethylene is supplied in 25 kg polyethylene bags, 40 bags per pallet (1,000 kg). |
| Container Loading (20′ FCL) | 20′ FCL loading of LyondellBasell Icorene 3560 GRN 6145 LLDPE: palletized bags, standard dry container, evenly distributed, secured for transport. |
| Shipping | Shipping Description: Polyethylene, Linear Low Density, non-hazardous. Not regulated by DOT/IMDG/IATA. Packaged in 25 kg bags, octabins, or bulk. Transport in clean, dry covered vehicles/containers. Avoid moisture, contamination, excessive heat, and direct sunlight. Maintain labels and SDS. No special transport placards required. Keep sealed until use. Follow manufacturer's handling instructions. |
| Storage | Store LyondellBasell Icorene 3560 GRN 6145 LLDPE in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and oxidizing agents. Keep containers closed to prevent moisture and contamination. Avoid dust generation and unstable stacks. Prevent pellet loss to drains or the environment. Follow local regulations and the manufacturer’s safety data sheet. Use first-in, first-out inventory and inspect regularly. |
| Shelf Life | Shelf life is typically 24 months from date of manufacture when stored in cool, dry conditions in unopened original packaging. |
Rotational moulding of chemical storage tanks with LyondellBasell Icorene 3560 GRN 6145 begins with powder particle-size control, because dry-blend homogeneity and oven sintering behaviour are determined by the fraction passing 35 mesh (500 µm). Storage in unsealed bulk bags at relative humidity above 60% can raise surface moisture above 0.05 wt%, which must be corrected by drying at 60–70 °C for 4 h before charging. The powder is dry-blended in a low-intensity ribbon blender for 10–15 min with a formulation consisting of 100 phr Icorene 3560 GRN 6145, 8–12 phr fractional-melt high-density polyethylene for hoop-stiffness modification, 0.8–1.2 phr hindered amine light stabilizer masterbatch, and 0.05–0.2 phr internal mould release agent. The blend is charged into fabricated stainless steel or cast aluminium moulds mounted on carousel-type biaxial rotational moulding machines with arm-speed ratios between 3.6:1 and 4.0:1. Oven air temperature is held at 280–300 °C until the internal air thermocouple reaches 200–205 °C; in a 5 mm nominal wall tank of 1,000 L capacity, the lag between oven air and internal air is typically 8–12 min, and total oven dwell is 25–40 min. Air cooling to 90 °C internal temperature is followed by water mist on exterior surfaces to reduce warpage; premature demoulding or rapid water quenching can generate stress concentration at bung threads and fitting bosses. Chemical resistance validation is performed by immersion in representative media according to ISO 175:2010; aggressive oxidizers and aromatic solvents at temperatures above 40 °C require case-specific testing because the grade is not universally resistant to all chemical classes. Terminal product types include vertical cylindrical static tanks from 500 L to 10,000 L, secondary containment basins, chemical metering pump skids, and pickling bath covers.
| Standard | Scope | Requirement relevant to Icorene 3560 GRN 6145 |
|---|---|---|
| ASTM D1998-21 | Upright polyethylene tanks | Minimum wall thickness, hydrostatic strength, impact resistance |
| EN 13575:2012 | Static thermoplastic tanks above ground | Hydrostatic pressure testing, chemical compatibility, UV ageing |
| ISO 175:2010 | Chemical resistance by immersion | Property retention after exposure to stored chemical at service temperature |
Playground component production imposes a narrower thermal window than chemical tank moulding because impact toughness must be retained after outdoor weathering and after moulded-in metal inserts. The dominant processing variables are peak internal air temperature, cooling rate, and stabilizer masterbatch dispersion. Compliance is evaluated under ASTM F1487-21 for public playground equipment in North America and EN 1176-1:2017 in the EU; heavy-metal migration from pigmented surfaces is assessed by EN 71-3:2019 Category III limits. Dry-blend addition ratios are 2.5–4.0 wt% UV/HALS masterbatch and 0.5–1.0 wt% antioxidant masterbatch based on 100 parts of Icorene 3560 GRN 6145. Glass-fibre reinforcement is not used because it increases rotomoulding viscosity and warpage. Aluminium moulds with electroformed or CNC-machined surfaces are heated on a biaxial carousel at oven air temperature 280–300 °C; rotation ratio is held at 4:1, and peak internal air temperature is maintained at 195–205 °C for 5–8 min to complete sintering of the inner wall. Mould release agent is limited to 0.1 g/m² of mould surface because excess release agent transfers to the part and interferes with post-mould decoration. Production-scale failures occur when demoulding is attempted before internal air temperature falls below 90 °C; premature ejection causes tear around steel inserts and stress whitening at rib roots. Finished terminal products include slide bedways, tunnel segments, climbable panels, and outdoor musical play elements, all supplied in the pigmented grade to avoid post-mould painting.
For agricultural rainwater tanks above 5,000 L, Icorene 3560 GRN 6145 is selected over standard high-density polyethylene rotomoulding powders primarily for low-temperature impact resistance and environmental stress-cracking resistance in exposed above-ground installations. The production process on a rock-and-roll machine differs from carousel moulding because single-axis rocking combined with a secondary rotation creates more uniform wall distribution in long cylindrical bodies than a fixed 4:1 carousel arm. Agricultural water tanks in the EU are supplied under EN 13575:2012; North American projects often reference ASTM D1998-21 as a specification baseline, while potable water contact requires NSF/ANSI 61 confirmation for the pigmented GRN 6145 formulation. Dry-blend addition ratios are commonly 1.5–2.0 wt% hindered amine/UV masterbatch and 0.5–1.0 wt% pigment masterbatch; carbon black levels above 0.5 wt% are avoided because excessive pigment can reduce dart impact strength. Rock-and-roll machines with a 1:4 arm-speed ratio and oven air temperature of 270–290 °C are used for horizontal cylindrical bodies. Internal air pressure of 10–20 kPa during cooling prevents wall delamination and reduces shrinkage voids at mould parting lines. Wall thickness is checked with ultrasonic gauges at 12 measurement points; minimum thickness is not less than 4 mm for 10,000 L tanks. Terminal products include horizontal leg tanks, vertical accumulator tanks, rainwater harvesting cisterns, and seed-treatment chemical induction tanks.
When floating dock floats are moulded as hollow shells with wall thickness 5–8 mm, the process window is defined not by peak oven temperature but by the balance between internal air pressure and cooling rate. If internal air pressure is dropped before the mould inner surface has solidified, the part wall can collapse inward at the parting line. EU marine equipment may be assessed under Directive 2014/90/EU when fitted on commercial vessels; physical property procurement specifications commonly require ASTM D638-22 tensile yield, ASTM D790-17 flexural modulus, and ISO 62:2008 water absorption below 0.1% after 24 h immersion. Formulation addition uses 100 phr of the grade, 2.0–3.0 phr UV/HALS masterbatch, and 0.1–0.3 phr processing antioxidant. Release agents must be non-silicone or removed by isopropanol wiping before two-part rigid polyurethane foam filling; otherwise polyurethane adhesion to the polyethylene inner wall is insufficient. Carousel rotomoulding at 285–305 °C with peak internal air temperature 200–205 °C is followed by forced-air cooling to 120 °C internal temperature, then water mist cooling on exterior surfaces only. Internal air pressure is maintained at 15–25 kPa until wall temperature is below 100 °C. Published data for this specific configuration is limited; adhesion testing should be performed per ASTM D429-14 Method B or equivalent. Terminal products are modular floating dock cubes, cylindrical mooring buoys, and navigation mark floats.
Material handling pallet boxes and insulated industrial containers represent a compression-loaded application in which the grade is processed with a high proportion of post-industrial regrind to control raw-material cost. The loading conditions are compression-dominated, so wall thickness and rib depth are adjusted rather than relying solely on material modulus. Pallet boxes used in automated warehouses are assessed under ISO 8611-1:2021 for flatness, racking stiffness, and drop performance; export packaging for dangerous goods may require testing under ADR/RID Chapter 6.5 when the box is used as an intermediate bulk container. Typical dry blend consists of 70 wt% virgin Icorene 3560 GRN 6145 and 30 wt% post-industrial rotomoulding regrind of identical chemistry; regrind above 40 wt% is avoided because particle-size distribution shifts toward fines and lowers bulk density below 0.35 g/cm³. Low-shear rotomoulding is carried out on carousel machines with oven air temperature 275–295 °C and biaxial rotation ratio 3.5:1; steel tube cores form forklift pockets. Cooling uses forced air at 25 °C for 15 min, then temporary steel side plates are bolted to the part to control flatness during final shrinkage. Terminal products include fork-liftable pallet boxes, insulated fish handling tubs, and stackable industrial tote boxes.
Because street and park seating shells contain large, relatively flat surfaces, constrained cooling after demoulding is the determining factor for meeting flatness tolerance. The grade is suitable for this application when the mould is designed with double-wall channels and the demoulded part is placed in a metal cooling fixture for the first 30 min after ejection. Outdoor furniture for the European market is tested under EN 581-1:2017; North American municipal purchase specifications often reference ASTM D638-22 for tensile properties and ASTM D256-23 for notched Izod impact. Addition ratios are 100 parts Icorene 3560 GRN 6145, 3.0–4.0 phr UV/HALS masterbatch, and 5–10 phr high-density polyethylene to increase surface hardness; pigment is included in the grade code, so no additional masterbatch is needed for base colour. Cast aluminium moulds maintain mould surface temperature 60–80 °C before charging; oven air temperature is held at 285–300 °C, and peak internal air temperature is maintained at 200 °C for 6 min. After demoulding, the shell is transferred to a water-cooled aluminium fixture that applies 0.5–1.0 kPa uniform pressure to the outer surface while fan cooling continues until part temperature is below 70 °C. Terminal products are single-piece park benches, modular outdoor chairs, and tree-pit planters.
Competitive LyondellBasell Icorene 3560 GRN 6145 Polyethylene, Linear Low Density prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618005193850
Email: sales8@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
LyondellBasell Icorene 3560 GRN 6145 is a linear low density polyethylene compound identified by a manufacturer-specific grade designation and an integrated green colourant package. The base polymer is an ethylene/α-olefin copolymer produced under low-pressure catalytic polymerisation conditions in which short-chain branching density controls crystallinity, density, and low-temperature ductility. LLDPE resins of this structural class are routinely classified between 0.916 g/cm³ and 0.940 g/cm³ under ISO 1183-1, while the green masterbatch component may shift moulded density by 0.001–0.003 g/cm³ relative to natural resin. The designation GRN 6145 indicates a colour concentrate rather than an uncoloured base grade, and therefore any food-contact evaluation must consider the pigment carrier resin as well as the LLDPE matrix. Compared with high-pressure LDPE, the linear low density architecture contains a higher proportion of linear backbone with controlled short-chain branches rather than long-chain branching, producing higher tensile properties at equivalent density but lower bubble stability in blown film. Compared with HDPE, the lower crystalline fraction of Icorene 3560 GRN 6145 is expected to give lower stiffness, higher environmental stress crack resistance, and improved impact behaviour at sub-ambient temperatures. The exact melt mass-flow rate of this green-compounded grade is not publicly confirmed in this review; for LLDPE extrusion grades in this density range, ISO 1133-1 values at 190 °C and 2.16 kg frequently fall between 0.5 g/10 min and 2.0 g/10 min, though users should treat this as a class-wide expectation rather than a certified lot value.
The green colorant carrier resin and pigment dispersion can influence oxidative stability because the masterbatch dilutes the base stabilisation package and introduces additional metal-containing pigments. For polyolefin compounds of this type, oxidative induction time measured under ISO 11357-6 or ASTM D3895 should be obtained on the compounded green material rather than inferred from natural-grade data. A decrease in oxidative induction time of 5–20% relative to uncoloured LLDPE has been observed in some colour-compounded polyolefin systems, although published data for this specific Icorene formulation is limited. The pigment can also act as a nucleating agent, increasing crystallisation temperature by 1–3 K, which may alter shrinkage and warpage in injection moulded parts. If long-term heat ageing is specified, the compound should be evaluated under ISO 188 oven ageing rather than relying on unstabilised natural LLDPE data.
On blown film lines using 30:1 L/D single-screw extruders with barrier screws, LLDPE grades of this density class are typically processed at melt temperatures between 190 °C and 240 °C. The green pigment does not normally require a separate predrying stage unless condensation has formed during storage; if surface moisture is observed at relative humidity above 60%, a hopper dryer set to 60–70 °C for 1–2 h is used to remove surface water without introducing thermal degradation. Screw speed adjustments should be made gradually because linear low density polyethylene can exhibit a lower shear-thinning response than long-chain branched LDPE, leading to higher motor torque and melt pressure at equivalent throughput. Melt temperature should be monitored at the adapter and die zones; sustained residence above 240 °C for more than 10 min should be avoided because chain scission generates carbonyl species detectable by infrared spectroscopy.
For linear low density polyethylene, sharkskin melt fracture typically initiates at wall shear stresses between 0.14 MPa and 0.30 MPa, depending on die geometry, melt temperature, and molecular weight distribution. Compared with long-chain branched LDPE, LLDPE may exhibit a narrower stable extrusion window in high-shear processes such as blown film, so die land length, die gap, and melt temperature must be configured to keep shear stress below the critical threshold. In cast film or extrusion coating operations, draw resonance can occur if the draw ratio exceeds 10:1 to 15:1 unless melt strength is modified through polymer architecture or processing additives. Published data for Icorene 3560 GRN 6145 specific melt fracture limits is limited, but the linear low density architecture indicates that processing should be designed with lower shear sensitivity than for branched LDPE. Screens and breaker plates should be inspected for pigment agglomerate retention because colour concentrate dispersion defects can create localised pressure fluctuations.
Cold-chain packaging produced from LLDPE benefits from short-chain branching because the ductile-brittle transition temperature is lower than that of HDPE at equivalent wall thickness. Impact strength measured under ISO 179-1/1eA or ASTM D256 remains meaningful only when test temperature and conditioning are explicitly stated. For LLDPE compounds in this density segment, notched Izod impact at -40 °C frequently exceeds 50 kJ/m², though exact values for the green-compounded grade are not published. The green pigment may slightly increase modulus and reduce elongation at break by 2–8%; tensile properties should be measured under ISO 527-2 at 23 °C and 50 mm/min on conditioned specimens. Environmental stress crack resistance measured by ASTM D1693 may exceed 1000 h in 100% Igepal CO-630 for well-stabilised LLDPE, but conformance must be verified on the coloured compound because pigment dispersion and masterbatch carrier resin can alter stress crack initiation. In rotomoulded parts, wall thickness variations between 3 mm and 6 mm can change local cooling rate and crystalline morphology; impact at corners may therefore be lower than in flat sections due to wall-thickness-dependent crystallinity and residual stress.
Compliance status of Icorene 3560 GRN 6145 must be confirmed against lot-specific documentation because the green colourant package may introduce substances not present in the natural LLDPE base resin. The compound should not be assumed suitable for food-contact applications solely on the basis of the olefin polymer clearance; the pigment formulation and its carrier resin must be evaluated under the applicable migration test conditions. For outdoor service, the green pigment alone does not confer ultraviolet resistance. Unless the grade is explicitly formulated with hindered amine light stabilisers and ultraviolet absorbers, retention of mechanical properties after prolonged weathering should be validated under ISO 4892-2 or ASTM G154.
Before using Icorene 3560 GRN 6145 in food-contact or electrical equipment applications, the following verifications apply. The table summarises common regulatory frameworks and the corresponding test or documentation requirements.
| Framework | Clause or method | Limit or requirement |
|---|---|---|
| EU food contact | Regulation (EU) No 10/2011 | Overall migration limit 10 mg/dm²; specific migration of pigment metals subject to Annex II limits |
| U.S. food contact | 21 CFR 177.1520 | Olefin polymer clearances; extraction limits depend on food type and use condition |
| RoHS | Directive 2011/65/EU | Pb 1000 ppm, Cd 100 ppm, Cr(VI) 1000 ppm in homogeneous material |
| REACH SVHC | Regulation (EC) No 1907/2006 | No SVHC above 0.1 wt% unless authorised; pigment dispersion must be documented |
Injection moulders evaluating this grade should establish a melt temperature profile between 200 °C and 230 °C at the nozzle and maintain clamp force settings sufficient for the projected part area. Because the green concentrate may increase viscosity relative to natural resin at high shear rates, cavity fill should be verified using short-shot studies. Mould cooling at 20–40 °C is typical for LLDPE; however, for dimensionally stable parts, the cooling time should be set by part wall thickness and the crystallisation rate of the compounded material rather than by natural LLDPE reference data. Part weight and dimensions should be monitored after 24 h conditioning at 23 °C and 50% relative humidity to account for post-mould crystallisation and shrinkage. If the grade is used in multilayer coextrusion, adhesion to HDPE or LDPE layers should be verified under ASTM F904 or the applicable peel test because green pigment surface migration can reduce interfacial weld strength in certain structures.