| HS Code | 552134 |
| Product Name | LyondellBasell Icorene 3560 CM GRN 6107 Polyethylene, Linear Low Density |
| Material Type | Polyethylene, Linear Low Density (LLDPE) |
| Density | 0.935 g/cm3 |
| Melt Flow Rate | 20 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 10.3 MPa |
| Tensile Strength At Break | 11.7 MPa |
| Elongation At Break | 750% |
| Flexural Modulus | 290 MPa |
| Vicat Softening Point | 94°C |
| Melting Point | 124°C |
| Hardness Shore D | 49 |
| Color | Green (GRN 6107) |
As an accredited LyondellBasell Icorene 3560 CM GRN 6107 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 CM GRN 6107 is supplied in 25 kg polyethylene bags, 40 bags per pallet (1,000 kg total). |
| Container Loading (20′ FCL) | 20′ FCL container loading for LyondellBasell Icorene 3560 CM GRN 6107 Linear Low Density Polyethylene: palletized bags, dry, secured, evenly distributed. |
| Shipping | LyondellBasell Icorene 3560 CM GRN 6107 Polyethylene, Linear Low Density is shipped as non-hazardous LLDPE resin pellets in bags, boxes, or octabins. It is not regulated by DOT, IMDG, or IATA. Keep dry, avoid excessive heat, and secure packaging during transport. Store cool and dry. |
| Storage | Store LyondellBasell Icorene 3560 CM GRN 6107 Polyethylene, Linear Low Density in a cool, dry, well-ventilated area. Keep containers tightly closed, away from direct sunlight, heat, moisture, and ignition sources. Avoid strong oxidizers and contamination. Keep packages off floors and walls; use first-in, first-out stock rotation. Follow local regulations and good industrial hygiene practices. Ensure proper ventilation during handling. |
| Shelf Life | Typically 24 months from date of manufacture when stored in original, unopened packaging, protected from heat, moisture, and direct sunlight. |
In rotational molding of static agricultural storage vessels, LyondellBasell Icorene 3560 CM GRN 6107 polyethylene, linear low density, is processed as a pre-colored green powder whose particle size distribution and bulk density control wall thickness uniformity in vertical cylindrical molds. The applicable compliance framework for water and neutral liquid tanks is defined by ISO 21138-1 and ISO 21138-2, while free-standing above-ground tanks are additionally specified under ASTM D1998-21 for material, design, and stress-basis criteria; vessels transported with fertilizers or agricultural adjuvants are evaluated under UN 1H1 packaging requirements. The base polyethylene belongs to the FDA 21 CFR 177.1520 family, but direct food-contact status of the green colorant in the compounded grade requires migration testing under EU 10/2011 before dual-use food/agronomic tanks are claimed. Formulation addition ratio for monolayer tank construction begins from 100 parts by weight of Icorene 3560 CM GRN 6107; where extended UV exposure at high altitude or tropical solar load is specified, a PE-carrier HALS/UV absorber masterbatch is dry-blended at 0.5–1.5 wt%, and total non-fusible additive loading above 2.0 wt% is discouraged because dispersed particles can pin the melt front and produce pinholes at the upper knuckle radius, a zone where thinning is already induced by powder trajectory during biaxial rotation. Production on a bridge-mounted or offset-arm biaxial rotational molding cell with clamped cast aluminum or steel molds charges the powder at ambient temperature and rotates the mold on a 4:1 primary/1.5:1 secondary ratio while the oven is maintained at 280–310 °C; the cook cycle continues until internal air temperature reaches 205–220 °C, after which a hold of 10–16 min allows the sintered powder to consolidate into a void-free melt skin. Cooling is executed with forced air followed by intermittent water mist once the part surface falls below 160 °C, and demolding is staged at 110–130 °C to prevent shrinkage-induced collar distortion. Terminal product types emerging from this process include 500 L to 20,000 L vertical storage tanks, cone-bottom fertigation reservoirs, chemical dosing cabinets, and monolithic secondary containment basins; the fitting boss on the lower cylindrical wall remains a known batch-to-batch variance zone when internal air temperature is below optimum by as little as 5 °C, with delayed pinholing appearing only after 72 h of liquid contact.
Municipal solid waste and recycling carts produced from LLDPE are subjected to repeated side-drop abuse on concrete pavements at ambient temperatures that can fall below −20 °C; controlling performance characteristics are therefore low-temperature notched impact as measured by ISO 179-1/1eA at −30 °C, environmental stress crack resistance by ASTM D1693 condition B in 10% Igepal CO-630 with an F50 failure time above 48 h, and tensile elongation at yield by ISO 527-2. Product-level compliance is supplied by EN 840-1 for dimensional consistency and EN 840-5 for two-wheel bins, which prescribe rigid-body drop tests, lid impact tests, and spectral weathering criteria; organic waste caddies may also require migration limits under EU 10/2011. Formulation addition ratio in the virgin outer skin is 100 parts by weight Icorene 3560 CM GRN 6107, while a recycled-content core can be introduced at 20–30 wt% of total shot mass only if the regrind is derived from the same LLDPE family, screened through a 150 µm sieve to remove degraded fines, and kept below 3 wt% moisture. Production on a carousel or shuttle rotational molding line for 120 L, 240 L, and 360 L two-wheel bins typically pre-warms the shot to 35–50 °C in cold weather to prevent condensation-induced powder clumping, then charges the mold and rotates at 4:1 primary/1.5:1 secondary ratios with the oven set to 300–320 °C. Internal air temperature is brought to 200–215 °C and the melt is held until the sidewall skin reaches uniform gloss; cooling begins with forced air and introduces water mist only after internal air temperature falls below 160 °C, because earlier mist contact across the parting line produces internal stress lines that reduce sub-zero drop impact. Terminal product types include 120 L, 240 L, and 360 L two-wheel bins, lift-assisted carts, organic waste caddies, and grit bins; the hinge boss is a defined defect zone and is measured with an ultrasonic wall-thickness gauge to a minimum of 3.5 mm after demolding, since fracture at the hinge pin under EN 840-5 drop testing is a primary failure mode in production audits.
Where rotationally molded distribution bins and hygienic pallets undergo fork tine impact and high-pressure washdown with alkaline detergents, the material must retain notch toughness across repeated thermal swings and resist stress whitening at rib intersections. The compliance framework for food-contact handling equipment derives from FDA 21 CFR 177.1520 for the olefin polymer and EU 10/2011 for overall migration, while the pallet mechanical test sequence is governed by ISO 8611-1 for tare load, corner drop, and fork tine durability; in some food-processing environments the equipment is additionally verified against NSF/ANSI 2 for cleanability and design hygiene. Formulation addition ratio for general material handling uses 100 parts by weight of Icorene 3560 CM GRN 6107; when demolding deep-draw bins with opposing ribs, 0.1–0.3 wt% of a PE-carrier internal mold release is dry-blended into the shot, but levels above 0.5 wt% must be avoided because the release agent can plate out on mold surfaces and generate low-gloss patches that obscure surface defects. Up to 20 wt% of clean internal regrind from the same green grade is acceptable in non-food-contact layers or the pallet core, while direct food-contact skins are maintained as 100% virgin LLDPE. Processing on shuttle rotational molding machines with cast aluminum molds operates at an oven temperature of 290–310 °C and brings internal air temperature to 210–220 °C for 12–18 min after complete powder pick-up; cooling fixtures are applied to the pallet deck immediately after demolding to hold flatness within the ISO 8611-1 deflection limit under rated load. Terminal products include 1200 × 1000 mm hygienic pallets, 300–1,200 L bulk distribution bins, meat lugs, and fish tubs; published migration data for this specific green colorant in high-fat fish oils is limited, so end-user-specific testing under EU 10/2011 is required before direct seafood contact is certified.
The following matrix consolidates test designations and acceptance references across the application zones without repeating the full process descriptions.
| Application zone | Standard designation | Test method / condition | Typical acceptance reference |
|---|---|---|---|
| Agricultural storage tanks | ISO 21138-1 / ASTM D1998-21 | Hydrostatic pressure at 23 °C | No burst below design factor |
| Municipal waste carts | EN 840-5 | Drop impact at −20 °C | No visible crack >2 mm |
| Hygienic distribution pallets | ISO 8611-1 | Rated load 1000 kg, 48 h | Deformation ≤25 mm |
| Insulated seafood tubs | EU 10/2011 / FDA 21 CFR 177.1520 | Overall migration, 10 days, 40 °C | ≤10 mg/dm² |
| Outdoor playground components | ISO 4892-2 | Xenon-arc, 3000 h | ΔE ≤2.5, elongation retention ≥75% |
| Secondary containment shells | ASTM D543 / ISO 175 | 28-day immersion | Mass change ≤1%, tensile retention ≥80% |
Insulated containers for fresh and processed seafood impose simultaneous demands for food-contact migration control, impact strength at 0–8 °C cold-chain temperatures, and dimensional stability under continuous wet loading. The governing standards are FDA 21 CFR 177.1520 for the base polyethylene, EU 10/2011 for overall and specific migration, and NSF/ANSI 2 for hygienic design in food-processing equipment; structural impact resistance is assessed by ISO 179-1/1eA notched Charpy at −10 °C and environmental stress crack resistance by ASTM D1693 condition C. The charging formula in the food-contact inner layer is 100 parts by weight Icorene 3560 CM GRN 6107; where a foam-insulated wall is demanded, a separate LLDPE foam layer is compounded with 0.2–0.8 wt% azodicarbonamide blowing agent and charged sequentially between virgin inner and outer skins. Up to 15 wt% closed-loop regrind is allowed in the outer non-food-contact skin only when the regrind is confirmed to be free of contact with fish processing chemicals and to have retained a melt flow ratio above 80% of the virgin value under ISO 1133-1:2022. Downstream production uses multi-layer rotational molding on a shuttle or carousel cell: the inner skin powder is first deposited and sintered, the foam layer is charged and expanded during a second heat stage, and the outer skin is charged last; internal air temperature is held at 210–225 °C until blowing-agent decomposition is complete and the outer skin consolidates without visible pinholes. Cooling is controlled at 6–10 °C/min by forced air to 85 °C before demolding, because faster cooling creates asymmetrical wall shrinkage and lid seat warpage. Terminal product types include 300–1,000 L insulated fish tubs, 40–80 kg ice fish boxes, shellfish aquaculture bins, and seafood distribution totes; the lid rim seal is the primary field failure point and is inspected for flatness with a calibrated feeler gauge after demolding.
Continuously exposed rotomolded outdoor furniture and playground components require both UV resistance and controlled heat buildup in dark green surfaces, which shifts the design wall thickness and additive strategy. The product safety framework for playground structures is established by EN 1176-1 for general safety and impact attenuation, with slide-specific requirements in EN 1176-3; accessible parts may additionally be evaluated under EN 71-3 for migration of certain elements. Weathering performance is verified by ISO 4892-2 xenon-arc exposure for 3000 h, and mechanical property retention is measured by ISO 527-2 tensile elongation and ISO 178 flexural modulus. The shot formulation uses 100 parts by weight of Icorene 3560 CM GRN 6107 as the pre-colored green base; when a 10-year UV warranty is required, a PE-carrier HALS/UV absorber masterbatch is dry-blended at 0.5–1.2 wt%, while filler-type pigments above 5 wt% are avoided because they lower weld-line elongation and create visible stress whitening after impact. Processing on clamshell rotational molding machines with aluminum molds proceeds at an oven temperature of 280–310 °C and internal air temperature of 200–215 °C; the cooling sequence uses forced air to 150 °C, then a light water mist to 100 °C, and finally ambient air to 60 °C before removal from the mold. Demolded articles include playground slides, tunnel shells, benches, planter boxes, and resort sun loungers; dark green parts with wall thickness above 6 mm are limited to shaded or intermittent-sun locations unless the design includes surface texture or ventilation channels to reduce solar heat accumulation.
Secondary containment shells for corrosive liquid storage combine a low-extractables material matrix with a continuous shell wall that must remain crack-free under hydrostatic load and chemical attack. Regulatory compliance for industrial facilities in the United States is defined by 40 CFR 264.175, which specifies a containment volume equal to or greater than 110% of the largest primary vessel; material compatibility is evaluated by ASTM D543 and ISO 175 immersion trials over 28 days, with mass change not exceeding 1% and tensile retention not falling below 80% for the specified chemical classes. The base resin ratio is 100 parts by weight of Icorene 3560 CM GRN 6107; for high-purity corrosive service, no external pigment concentrate, calcium carbonate, or processing aid is added because such components can increase extractable fractions and reduce chemical resistance. Where a UV stabilizer is needed for outdoor bunds, 0.4–0.8 wt% of a PE-carrier HALS package is dry-blended, and any regrind usage is capped at 10 wt% because repeated heat history increases gel content and lowers notched impact resistance measured by ISO 179-1/1eA. Production on large-part rotational molding machines with offset-arm biaxial rotation charges the powder into steel molds and heats the assembly to an internal air temperature of 210–225 °C; the cage is held at temperature for 15–25 min to consolidate the shell wall, and cooling is deliberately slowed to 4–6 °C/min with forced air only, avoiding water mist entirely to prevent residual stress gradients that create premature environmental stress cracks at the bottom outlet boss. Terminal products include 1000 L to 50,000 L bunded tanks, sump liners, chemical distribution boxes, and dosing skid containment trays; ultrasonic thickness verification of the shell floor after demolding is used to ensure the minimum designed wall thickness is maintained, because the floor-to-wall transition is the most frequent location for failure in external audits.
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LyondellBasell Icorene 3560 CM GRN 6107 is a linear low-density polyethylene grade whose commercial designation encodes the Icorene polymer series, the 3560 grade number, the CM product-form or compound modifier, and the 6107 green colour package. The base polymer belongs to the ethylene/α-olefin copolymer class identified by the symbol PE-LLD under ISO 1043-1. In the designation system of ISO 1872-1, a fully standardised polyethylene designation would separately identify density, melt mass-flow rate, additives, and special properties; the commercial code 3560 CM GRN 6107 does not directly translate into that ISO designation block. Lot-specific density should therefore be measured by ISO 1183-1 or ASTM D1505, and melt flow rate by ISO 1133-1:2022 or ASTM D1238 at 190 °C/2.16 kg. Published data for this specific green-coloured configuration is limited, and generic data for unpigmented LLDPE rotational moulding grades do not replace the certificate of analysis.
Rotational moulding does not plasticate the polymer by screw shear. The powder is charged into a closed mould and heated while the mould rotates biaxially on a shuttle, carousel, rock-and-roll, or offset arm machine. Densification therefore depends on particle size distribution, bulk density, dry-flow pourability, and the ability of the particles to sinter at the mould wall. For general-purpose LLDPE rotational moulding powders, median particle size is typically below 500 µm, with substantial fractions between 150 µm and 400 µm. An excessively coarse cut can delay densification and produce pinholes in thin sections, while an excessively fine fraction can reduce dry flow and increase dusting. Dry-flow funnel measurements based on ASTM D1895 Method C and particle size distribution by ISO 565 test sieving or ASTM D1921 are therefore more process-relevant for Icorene 3560 CM GRN 6107 than a melt flow value alone.
On production rotational moulders, heating is normally controlled by internal air temperature rather than by oven temperature alone. For LLDPE parts with nominal wall thickness of 3–6 mm, internal air temperature is commonly raised to approximately 200–220 °C before cooling starts; thicker sections or filled moulds may require peak internal air temperatures up to 250–260 °C. Primary axis speeds of 4–8 rpm and secondary axis speeds of 8–16 rpm are frequent industrial starting points, but the actual ratio depends on mould geometry, offset dimensions, and the flow behaviour of the green 6107 powder. Powder charge weight is calculated from required wall thickness and mould surface area; for a 5 mm nominal wall on a 1 m² surface, the charge is determined from bulk density rather than from pellet feed factor. Premature cooling or demoulding of LLDPE produces residual stress, warpage, and undercured inner surfaces, which can be detected as reduced notched impact values by ISO 179-1 or ASTM D256 on cut specimens.
The Icorene name identifies the LyondellBasell polyethylene range; 3560 is the grade number and should not be interpreted as a blend ratio or as a direct melt flow value. The CM suffix may indicate a compound, colour-modified, or product-form variant, depending on LyondellBasell’s internal coding; it is not a recognised ISO designation term. GRN 6107 is the green colour reference. For design and incoming inspection, the controlling properties are density, melt mass-flow rate, tensile yield stress, elongation at break, flexural modulus, notched or Charpy impact resistance, and environmental stress crack resistance. Independent verification should use ISO 1183-1 for density, ISO 1133-1:2022 for melt flow rate, ISO 527-2 or ASTM D638 for tensile properties, ISO 178 or ASTM D790 for flexural modulus, ISO 179-1 or ASTM D256 for impact, and ASTM D1693 for ESCR. Because the green colour package can alter solid-state properties relative to the unpigmented base resin, specification limits for the pigmented version should be used for lot acceptance.
| Property | Preferred method | Alternative | Process or design relevance |
|---|---|---|---|
| Density | ISO 1183-1 | ASTM D1505 | Charge weight, wall thickness |
| Melt mass-flow rate | ISO 1133-1:2022 | ASTM D1238 | Lot identity, low-shear processing |
| Tensile yield stress | ISO 527-2 | ASTM D638 | Durable load-bearing design |
| Elongation at break | ISO 527-2 | ASTM D638 | Ductility and puncture resistance |
| Flexural modulus | ISO 178 | ASTM D790 | Wall stiffness and buckling |
| Charpy notched impact | ISO 179-1 | ASTM D256 | Low-temperature toughness |
| Environmental stress crack resistance | ASTM D1693 | ISO 22088-1 | Chemical containment service |
| Particle size distribution | ISO 565 | ASTM D1921 | Dry flow and densification |
| Moisture content | ISO 15512 | — | Porosity and steam defects |
Mechanical testing of rotationally moulded LLDPE requires careful reporting of specimen preparation. Compression-moulded test sheets prepared according to ISO 293 or ASTM D4703 are useful for resin characterisation but may not reproduce the cooling rate or residual stress distribution of a rotationally moulded part. For design validation, specimens should be cut from flat sections of the actual moulded article or from rotomoulded plaques produced on the same machine. Test orientation, distance from mould parting lines, and wall thickness must be recorded because rotational moulding often creates gradients in crystallinity through the wall thickness.
Relative to high-density polyethylene rotational moulding grades of similar melt flow, an LLDPE such as Icorene 3560 CM GRN 6107 typically displays lower flexural modulus, lower crystalline melting point, and greater low-temperature ductility. The difference arises primarily from short-chain branching in the polyethylene backbone; copolymerisation with 1-butene, 1-hexene, or 1-octene reduces lamellar thickness and changes slow crack growth behaviour. In service, LLDPE parts often show higher environmental stress crack resistance by ASTM D1693 than HDPE counterparts but lower resistance to buckling under long-term vertical load. Compared with low-density polyethylene produced by high-pressure autoclave or tubular processes, the linear backbone of LLDPE provides higher tensile strength and puncture resistance at equivalent density, although the absence of long-chain branching reduces melt strength in processes that rely on extensional flow. For rotational moulding, that difference is less critical because the process is not dominated by extruder head pressure or parison stability.
When a rotational moulding grade is evaluated as an alternative to injection moulding LLDPE, the difference is not only physical form but also stabiliser package and melt flow target. Injection moulding grades are often pelletised with higher melt flow and may contain mould release agents. Rotational moulding powders are formulated for extended oven residence times; therefore, antioxidant and heat stabiliser packages are selected for repeated heating cycles of 15–30 min at high temperature. A rotational moulding grade may have a lower melt flow rate measured by ISO 1133-1:2022 to maintain impact properties measured by ISO 179-1 after slow cooling, while an injection moulding grade may be designed for rapid cavity filling at high shear. Replacing one with the other without adjusting processing parameters and testing specimens can produce parts that pass melt flow inspection but fail low-temperature impact or warpage requirements.
The product is normally packaged in multi-wall sacks or bulk containers. Because rotational moulding powders can segregate, silo unloading should be followed by in-line sieving or controlled refilling of day bins. The bulk density of the lot should be checked against the certificate of analysis; changes in bulk density may indicate lot-to-lot differences in particle geometry or colour concentrate incorporation. Bulk density measured by ASTM D1895 Method A is not a perfect predictor of mould-filling behaviour, but abrupt shifts are a quality alarm.
Colour compounding can change heat absorption, low-shear viscosity, and solid-state morphology. The green 6107 package is dispersed in a polyolefin carrier; the concentration and pigment chemistry are proprietary, but the presence of inorganic pigments may increase emissivity in the infrared region used by mould-surface pyrometers. This can cause the measured mould temperature to differ from the internal air temperature, particularly on thin-walled steel or cast aluminium tools. Process validation should therefore include a visual densification check at multiple draw points and, if possible, differential scanning calorimetry by ISO 11357-3 to confirm the melting endotherm. For applications governed by food-contact legislation, the base polyethylene may be evaluated under 21 CFR 177.1520, but the colourant must independently comply with 21 CFR 178.3297 or the relevant EU framework. Similarly, REACH and RoHS declarations must reference the finished coloured compound, not the unpigmented base resin. If ultraviolet stabilisation is specified, the presence of a green colour package does not automatically provide long-term UV resistance; separate hindered amine light stabiliser or UV absorber packages are required and should be verified by accelerated weathering under ISO 4892-2 or ASTM D2565.
LLDPE rotomoulded tanks used for surfactant solutions, weak acids, or agricultural chemicals are often selected for environmental stress crack resistance rather than for high heat deflection temperature. In chemical containment service, the service stress should be kept below the long-term hydrostatic design basis for the specific grade and temperature. Hydrostatic design data generated under ISO 9080 or ASTM D2837 are recommended; without those data, a short-term tensile or flexural value is insufficient for pressure-pipe or tank-wall stress calculations. The grade’s behaviour in the presence of aggressive chemicals cannot be inferred solely from density and ESCR; immersion testing under ISO 175 or ASTM D543 is required for the intended chemical and service temperature.
Incoming storage conditions influence processing more than the base resin’s inherent moisture absorption. LLDPE rotational moulding powders are not hygroscopic in the manner of polyamide or polyester, but surface condensation forms when cold sacks are moved into humid processing halls. If steam is generated during heating, the result can be internal porosity, surface pinholes, or a weak weld line at the inner surface. Warehouses should be kept at 10–30 °C, and sacks should be conditioned for 8–12 h before charging. Sampling for particle size distribution must follow a defined plan because vibration during transport can stratify fine and coarse fractions; a single bag sample may not represent the lot. For critical parts, mechanical testing should be performed on specimens cut from production-moulded plaques or parts rather than from compression-moulded sheets prepared from resin, because densification level and cooling rate differ between laboratory moulding and rotational moulding. Process holds above 260 °C internal air temperature should be avoided, and prolonged exposure of LLDPE to air at temperatures above 270 °C can produce oxidative discolouration, odour, and loss of impact strength. Published data for this specific configuration is limited when high-temperature holds exceed these boundaries; therefore, process capability trials should be performed on the intended machine before locking cycle parameters.