| HS Code | 842038 |
| Polymer Type | Linear Low Density Polyethylene (LLDPE) |
| Color | Green |
| Form | Pellets |
| Processing Method | Rotational Molding |
| Density | 0.935 g/cm³ |
| Melt Index 190 C 2 16 Kg | 3.5 g/10 min |
| Tensile Strength At Yield | 15.0 MPa |
| Tensile Strength At Break | 20.7 MPa |
| Elongation At Break | 700% |
| Flexural Modulus | 690 MPa |
| Hardness Shore D | 55 |
| Vicat Softening Temperature | 110 °C |
| Melting Temperature | 125 °C |
| Brittleness Temperature | < -70 °C |
| Environmental Stress Crack Resistance | > 1000 hr |
| Uv Stabilizer | Yes |
As an accredited LyondellBasell Icorene 3560 GRN 6136 Polyethylene, Linear Low Density factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Typically supplied in 25 kg moisture-resistant bags or 1,000 kg bulk bags, palletized for transport. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): LyondellBasell Icorene 3560 GRN 6136 LLDPE, palletized bags, evenly distributed, securely braced and stowed for transport. |
| Shipping | Shipping description: LyondellBasell Icorene 3560 GRN 6136 Polyethylene, Linear Low Density, is a non-hazardous thermoplastic resin in pellet form. It ships in 25 kg bags, octabins, or bulk trucks/railcars. No UN number, hazard class, or special transport placards required. Keep dry, cool, and clean; avoid moisture, heat, and UV exposure. Standard freight. |
| Storage | Store in a cool, dry, well-ventilated warehouse at ambient temperature, in original sealed packaging. Keep palletized, away from direct sunlight, heat, flames, ignition sources, and strong oxidizers. Protect from moisture, dust, and contamination. Avoid prolonged UV exposure and excessive stacking. Use first-in, first-out rotation, follow local regulations and the SDS, and prevent pellet spills. |
| Shelf Life | Shelf life is typically two years from production when stored in original unopened packaging, dry, out of direct sunlight, below 40°C. |
LyondellBasell Icorene 3560 GRN 6136 is a linear low density polyethylene supplied as a pre-coloured rotational moulding powder with the green 6136 pigment package dispersed in the polymer matrix before pulverization. In downstream application development, the material is processed on carousel, shuttle, and rock-and-roll rotational moulding lines; it is not designed for injection moulding, blow moulding, or cast film despite the linear low density designation. The powder must be stored in sealed containers at 23 ± 2 °C and below 50% relative humidity. Residual moisture above 0.1 wt% by Karl Fischer titration can generate steam bubbles in walls thicker than 6 mm when oven air temperature exceeds 300 °C. Dry-flow behaviour through 35-mesh screens and bulk density control hopper bridging tendencies on production lines. Representative property envelopes for LLDPE rotational moulding grades of this density class are determined by ISO 1183-1, ISO 1133-1, ASTM D1693, ASTM D638, and ASTM D790. The converter should confirm the certificate of analysis for the exact grinded lot because pigment loading and grinding history alter low-temperature impact retention and inner-surface smoothness.
Table 1: Standard method envelope used to qualify LLDPE rotomoulding powder in downstream fabrication.
| Property | Test method | Typical reported range for 0.930–0.940 g/cm³ LLDPE rotational moulding grades |
|---|---|---|
| Density | ISO 1183-1 | 0.930–0.940 g/cm³ |
| Melt mass-flow rate | ISO 1133-1 at 190 °C/2.16 kg | 3.5–6.0 g/10 min |
| Environmental stress crack resistance | ASTM D1693 Condition B, F50 | >1,000 h |
| Tensile yield stress | ASTM D638 | 15–20 MPa |
| Flexural modulus | ASTM D790 | 500–700 MPa |
| Water absorption | ISO 62, 24 h at 23 °C | <0.1% |
Within agricultural liquid storage and fertigation tank production, the powder is charged into cast aluminium or sheet steel moulds at ambient temperature and fused against the mould wall by biaxial rotation. For a 2,000 L vertical cylindrical tank with a nominal wall thickness of 8 mm, the carousel arm speed is normally set to give an off-axis ratio of 4:1 and a synchronous secondary rotation of 8–10 rpm. Oven set point is held at 280–320 °C, but the internal air temperature should not exceed 210 °C for more than 2 min before the melt film consolidates. Prolonged internal-air overshoot causes oxidative yellowing of the green tint and carbonyl formation at the inner wall. Production-scale cycle timing divides into a heat phase of 22–28 min, a dwell of 5–8 min, and a forced-air cooling phase of 25–35 min, with demolding temperature near 70–80 °C. Draft angles of 1–2° per side on cylindrical moulds reduce demolding deformation; above 3° draft, uniform wall thickness becomes difficult to maintain because peak internal air pressure pushes the melt into the lower-draft region. Fertigation tanks may contain dilute urea and potassium chloride solutions. LLDPE remains essentially unaffected by these ionic solutions at ambient temperature, but continuous exposure to sodium hypochlorite above 200 ppm free chlorine is discouraged because oxidative degradation can shorten ESCR from >1,000 h to below 500 h depending on temperature. The end product is a rotational moulded green tank fitted with brass or polypropylene fittings; insert integration requires moulded-in threaded bosses because post-moulding welding of PE bosses often introduces stress concentrations at the weld root.
Industrial secondary containment pallets, spill bunds, and tank base sump sleeves are produced from LLDPE when resistance to dilute mineral acids, caustic soda, and salt brines is required. The limiting factor in thick-section bunds is not the base resin’s response to acids or alkalis but the residual stress distribution in the floor plate and corner transitions. After demoulding, a 12 mm nominal floor section may retain a through-thickness residual stress differential of up to 0.8 MPa when quenching is too rapid; this can promote slow crack growth under load. To prevent this failure mode, the cooling phase on a shuttle machine is staged: ambient forced air for 10 min, then water mist at 45 °C for 15 min, then dry air at 60 °C for 10 min before the part is pulled. This staged cooldown keeps the crystalline shrinkage rate below 0.5%/min in corner radii. Chemical resistance of LLDPE is well documented: dilute sulphuric acid at 10 wt%, sodium hydroxide at 50 wt%, and saturated sodium chloride produce a mass change below 0.5% after 30 days at 23 °C when tested by ISO 175. Strong oxidizers such as fuming nitric acid, concentrated chromic acid, and liquid bromine are incompatible. Aromatic hydrocarbon solvents such as benzene, toluene, and xylene swell PE and reduce flexural modulus within hours; these exclusions must be printed on the bund manufacturer’s technical data sheet rather than claiming universal chemical resistance. The green pigment package in Icorene 3560 GRN 6136 should be considered when aggressive solvent contact is possible because surface colour change may precede measurable mass change. Finished products include 250 L sump trays and four-drum bunds with moulded-in drain bungs and forklift channels. The floor plate should be checked for sink marks at the intersecting ribs using a straightedge and feeler gauge; sink depth above 1.5 mm creates a pooling point for collected leaks.
Playground enclosures, tunnel segments, and slide hoods rely on a smooth internal skin with uniform green pigment distribution and acceptable impact energy absorption at sub-zero temperatures. The powder is processed at a peak internal air temperature of 190–205 °C; if the internal air temperature is raised too quickly beyond 210 °C, the outer layer oxidizes and the pigment can shift partly to the surface, creating a visible dusting on the demoulded part. In playground applications, the edge radius should not be below 3 mm; sharper radii cause localized thinning below 60% of nominal wall and can fail the entrapment provisions of ASTM F1487 after abuse loading. Pre-compounded colorants and low concentrations of process lubricants in the powder must be verified by the toy safety test method EN 71-3, which specifies migration limits for aluminium, antimony, arsenic, barium, boron, cadmium, chromium, cobalt, copper, lead, manganese, mercury, nickel, selenium, strontium, tin, organic tin, and zinc. The converter is responsible for obtaining a Notified Body report for the finished component. Mechanical acceptance is determined by drop weight impact at -20 °C using ISO 6603-2. A typical failure of incorrectly fused powder is a star-shaped brittle crack at the gate point, while a properly fused and cooled LLDPE shell yields and whitens but does not puncture. The final assembly uses stainless steel fasteners and moulded-in bosses rather than through-bolts in thin child-accessible surfaces. Long-term UV exposure is controlled with hindered amine light stabilizers already incorporated in the base resin; the supplier’s certificate of analysis should state the UV additive package retention. If a secondary acrylic topcoat is applied, it must not contain ketone or acetate solvents because these soften the polyethylene surface and reduce the impact values below 5 J/mm at the wall.
When an LLDPE shell of 8 mm nominal wall thickness is rotationally moulded for a dock float or an aquaculture cage collar, the first quality risk is not impact failure but pinhole leakage caused by non-melted fines migrating into the inner skin. The powder fraction passing a 200 µm sieve should be below 12%; higher fines content produces a powdery inner surface and a network of microvoids that open into water penetration paths. On production shuttle machines with aluminium moulds, water immersion leak tests at 35 kPa internal air pressure are used to identify pinholes below 0.5 mm diameter. To achieve a void-free inner skin, the mould must reach a minimum mould surface temperature of 260 °C for at least 5 min before the cooling phase. A practical failure mode observed on rock-and-roll machines is the “orange peel” inner surface at wall thickness below 6 mm; this condition disappears when the charge weight is increased or the oven residence time is extended, but weight increase raises part cost and cooling time. Flotation shells must be joined with rotational moulded inserts and sealed with EPDM gaskets because post-moulded polyethylene weld seams show a 20–30% reduction in ESCR relative to the base sheet. The shell is subjected to a 24 h water absorption test according to ISO 62, with allowable mass gain below 0.1%. The green pigmented shell must also maintain a contact angle with seawater above 90° to minimize biofilm attachment, but this is affected by surface gloss rather than resin choice alone. Published data for biofilm adhesion with this specific green pigment in submerged LLDPE is limited; fouling control requires mechanical cleaning rather than relying on surface chemistry.
Wheeled municipal waste bins, public litter receptacles, and side-loading container bodies are rotationally moulded from pre-coloured LLDPE because the process permits double-wall construction with reinforcing ribs and a rigid inner frame without the melt-flow length restrictions of injection moulding. In this service, the material must withstand repeated lid hinge flexing, waste collector lift-arm compression, and outdoor UV exposure for service lifetimes of 5–8 years. The moulding cycle for a 1,100 L container is longer than for a thin-wall tank. The heat phase requires 30–40 min at an oven set point of 290–310 °C, and the cooling phase is extended to 45–60 min to prevent corner warpage. Wall thickness distribution on a production turret machine is measured at 6–8 mm on flat panels and 4–5 mm at the rim lip; rim thickness below 3 mm produces cracking around the wheel axle inserts. The material’s melt flow rate in the 3.5–6.0 g/10 min class allows good melt consolidation but increases cycle time compared to lower flow high-density PE. The waste container must meet the EN 840 series standards for mobile waste containers; specific clauses cover dimensional tolerance, lid opening angle, impact resistance at low temperature, and drain hole sizing. Impact testing on the finished body uses a 3 kg steel sphere dropped from 1 m at -10 °C, and acceptable results require no visible cracking. The green 6136 colour is checked against municipal branding codes with a spectrophotometer using CIELAB dE ≤ 1.0 under D65/10° illumination per ISO 7724. Outdoor storage can expose the lid to UV radiation; the carbonyl index measured by ASTM D5576 should not exceed 0.1 after 5,000 h of accelerated weathering in a xenon-arc apparatus with quartz filters and 0.51 W/m² at 340 nm. If the container body is intended for post-consumer recycling, the converter must avoid coating the inner wall with epoxy paint; LLDPE’s nonstick surface already resists waste adhesion, but the trade-off is poor paint wetting.
For paddlesport hulls and small watercraft components, the rotomoulded LLDPE shell is valued for lower environmental stress cracking in immersion and high impact toughness when compared with many high-density PE rotomoulding grades. The powder is processed in aluminium clamshell moulds with water-cooled beryllium-copper inserts at the seat mounts. The charge weight is calculated from the surface area and a target wall of 7–10 mm; a 5.0 mm minimum wall is specified at the deck hatch rim. Differential cooling between the thick keel line and thin deck can produce a bent or twisted hull; moulders therefore check flatness with a three-point measurement jig and adjust cooling air velocity between 2.0 m/s and 6.0 m/s on the hull side. Shrinkage allowance is set at 2.0–2.5% for longitudinal dimensions and 2.5–3.0% for transverse dimensions; for a 4.2 m kayak, this means a steel mould length of approximately 4.285 m. Release agents with silicone wax are avoided because they transfer to the hull surface and prevent post-moulding trim adhesion; instead, PTFE mould release systems are used. Water absorption after 24 h immersion per ISO 62 is typically below 0.02% for unfoamed LLDPE, so hull weight change due to water uptake is negligible. The hull is tested for puncture resistance with a 25 mm radius striker at 10 J impact energy at -10 °C; cracking at the mould parting line indicates insufficient fusion of powder at the parting-line pinch. Accessories such as footrails and handles are attached by spin-welding or moulded-in inserts. The green colour is formulated with an ultraviolet stabilizer package; however, prolonged outdoor storage in direct sunlight still increases surface oxidation and gloss loss after 3,000 h in ASTM G154 UVA exposure, so hull storage under cover is recommended. Published data for Icorene 3560 GRN 6136 in paddlesport-specific testing is limited; the stated target values are derived from standard LLDPE rotational moulding grade behaviour in similar service.
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LyondellBasell Icorene 3560 GRN 6136 is a linear low-density polyethylene supplied as a pigmented rotational moulding powder. The designation 3560 identifies the base resin grade, while GRN 6136 denotes a green colour formulation incorporated before final grinding. The material is used in rotomoulded tanks, outdoor enclosures, agricultural equipment covers, and marine components where a pigmented LLDPE is required. In such applications, the grade is specified for its combination of low-temperature ductility, stress-crack resistance, and stabilised coloured appearance rather than for load-bearing stiffness. Because the green pigment is melt-compounded or dry-blended prior to grinding, it can alter melt rheology, crystallisation rate, and part-surface appearance; qualification therefore should be performed on the green-pigmented material rather than on an unpigmented analogue.
The LLDPE architecture is defined by the incorporation of an alpha-olefin comonomer along the polyethylene chain. In rotational moulding, this architecture reduces spherulite size and crystallinity, producing a lower flexural modulus and a higher elongation-to-break than a Ziegler-Natta HDPE of equivalent 2.16 kg melt flow. The density near 0.935 g/cm³ places the resin between medium-density and low-density classifications; the material is sometimes described as a lower-density LLDPE rather than a true medium-density grade because density is achieved through comonomer incorporation. The consequence for part design is that Icorene 3560 GRN 6136 will exhibit more creep under sustained load than an HDPE and will require thicker sections for equal bending stiffness.
Icorene 3560 GRN 6136 is differentiated from injection moulding or extrusion LLDPE grades by its powder morphology and stabiliser design. Injection moulding LLDPE is normally supplied as pellets and compounded for short, high-shear exposure; the rotomoulding grade must survive prolonged oven dwell at 260–300°C without excessive viscosity increase or colour drift. The melt flow range near 3.5 g/10 min is moderate: higher-flow grades may sinter more quickly but produce more bubbles, while lower-flow grades may require extended peak-temperature hold times and reduce corner fill.
Standardised property data for the Icorene 3560 family are generated on compression-moulded plaques. The following table summarises the property envelope used in specification screening for a 0.935 g/cm³ LLDPE rotomoulding powder. Values are indicative of the base-resin class and are not a certificate of analysis for every pigmented lot.
| Property | Test method | Value |
|---|---|---|
| Density | ISO 1183-1:2019 method D | 0.935 g/cm³ |
| Melt flow rate | ISO 1133-1:2022, 190°C/2.16 kg | 3.5 g/10 min |
| Tensile yield stress | ISO 527-2/5A/50 | 14 MPa |
| Elongation at break | ISO 527-2/5A/50 | 800 % |
| Flexural modulus | ISO 178, 2 mm/min | 550 MPa |
| Notched Charpy impact, 23°C | ISO 179-1/1eA | No break |
| Notched Charpy impact, -40°C | ISO 179-1/1eA | 10–14 kJ/m² |
| Environmental stress-crack resistance, F50 | ASTM D1693B, 100% Igepal | >1,000 h |
These values represent the property class of a 0.935 g/cm³ LLDPE rotomoulding powder; the certificate of analysis for GRN 6136 governs production batches. Published data for the specific pigmented configuration are limited if the colourant system is supplied through a masterbatch rather than reactor-grade compounding.
As supplied for rotational moulding, the powder is ground to a particle size distribution designed for dry flow and corner fill. A typical control range for rotomoulding LLDPE powders is 35 mesh (500 µm) through 200 mesh (75 µm), with the fraction below 75 µm limited to prevent dusting and melt-pool irregularities. Dry flow, measured in a flow cup by ASTM D1895 Method A, is commonly used for incoming inspection; lot-specific dry flow values should be compared with the supplier control range. Grinding-induced fines can reduce bulk density and increase surface area, which in turn increases oxygen uptake during oven heating and can shift colour retention after ultraviolet exposure.
On production-scale carousel, shuttle, and clamshell machines, Icorene 3560 GRN 6136 is processed as a free-flowing powder. The powder is charged into the cold or preheated mould, and the mould is rotated biaxially in a forced-air gas oven. Oven setpoints are typically maintained at 260–300°C, with peak internal air temperature for LLDPE moulding generally controlled at 190–210°C. These values are lower than typical HDPE peak internal air temperatures by approximately 10–20°C; a line audit that substitutes this LLDPE into an HDPE cycle without reducing oven temperature will frequently produce over-cure, discolouration, and excessive part shrinkage.
Sintering and densification require sufficient particle coalescence at the mould surface. Because the melt flow rate of the base resin is near 3.5 g/10 min, melt viscosity is sufficient to resist excessive drip at the peak temperature while permitting bubble dissolution. If the peak internal air temperature remains below 190°C or the time above 180°C is too short, the inner surface of the moulding may retain pinholing and grain-boundary voids. Conversely, if the material is held above 210°C for extended periods, the inner surface can develop oxidation-induced yellowing and the impact retention of the moulded part may fall below the value expected from plaque data. Oven residence time therefore has a narrower practical window than for a lower melt flow HDPE.
Cooling rate is an additional processing variable. In forced-air and mist-cooling operations, demoulding is commonly initiated when the part inner surface reaches 60–80°C. Uneven cooling across a large moulding can generate residual stresses and warpage, particularly in green-pigmented materials where pigmentation modifies the rate of heat absorption and radiation. On carousel machines with multiple arms, cycle-to-cycle variation in ambient-temperature cooling fans has been observed to produce batch-to-batch warpage differences exceeding ±2 mm on flat panels with a wall thickness of 5 mm. Process development may require instrumented moulds with data-logging thermocouples placed at the thickest and thinnest wall sections. The difference between external mould temperature and internal air temperature can exceed 30–50°C during early heating; controlling this differential is necessary to prevent thin-wall burn-off in parts with thickness transitions from 3 mm to 10 mm.
When compared with a 0.945 g/cm³ HDPE rotational moulding powder of similar melt flow, the LLDPE base of Icorene 3560 GRN 6136 shifts the failure mode from brittle rupture in notched tests to yielding and tearing at room temperature. The lower crystallinity reduces flexural modulus from approximately 900–1,200 MPa for HDPE to the 500–600 MPa range; the trade-off is a softer part surface and lower resistance to compressive creep. In rotational moulded tanks, outdoor enclosures, and marine components, the specification driver is often environmental stress-crack resistance rather than stiffness. The ASTM D1693B ESCR value of the LLDPE class is commonly recorded at >1,000 h, while many HDPE rotomoulding grades exhibit shorter failure times under identical 100% Igepal conditions.
The replacement changes three design variables: wall thickness, gross mass, and fastening load limits. For a part designed to a constant bending stiffness, wall thickness must increase by approximately 20–30% because stiffness scales with the cube of thickness and the flexural modulus is roughly 50% lower. The lower density of 0.935 g/cm³ partially offsets the added mass; a thickness increase of 25% yields a net mass increase of about 17% if all other dimensions remain constant. The practical consequence is that LLDPE parts may be thicker and heavier for an equivalent load-distribution performance, but their post-impact damage tolerance and cold-temperature ductility are often superior.
The reduced oven temperature requirement also affects energy input. Because the peak internal air temperature is 10–20°C lower, the cycle time on an existing HDPE program can sometimes be shortened after the oven setpoint is reduced. However, shorter cycle time is not guaranteed, since lower thermal conductivity and altered particle packing from pigments can slow heat transfer into the powder bed. Production trials on a 2.4 m shuttle moulding machine should include temperature verification at the mould parting line and in the powder mass, because the green pigment may cause radiant heat absorption differences relative to natural LLDPE.
Regulatory status for the uncoloured base resin does not automatically transfer to GRN 6136. The base LLDPE may be manufactured to meet food-contact requirements under 21 CFR 177.1520 for olefin polymers, but the green pigment system must be evaluated separately under the appropriate colourant framework. Where the part is intended for potable water or food contact, migration testing under EU Regulation 10/2011 may be required; overall migration limits for food-contact plastics are typically 10 mg/dm² under the assigned test conditions, but the specific simulant and temperature conditions are application-dependent.
| Regulatory domain | Standard or clause | Verification requirement |
|---|---|---|
| Food contact | FDA 21 CFR 177.1520 | Base olefin polymer clearance; pigment-specific extraction data required |
| EU food contact | EU Regulation 10/2011 | Overall migration and specific migration limits for the colourant system |
| RoHS | Directive 2011/65/EU | Cadmium, lead, mercury, hexavalent chromium, PBDE, PBB content below homogenous-material limits |
| REACH | EC 1907/2006, SVHC list | SVHC content 0.1% w/w per article; no restriction for the base polymer |
| Heavy metals in packaging | CONEG Model Toxics in Packaging | Sum of lead, cadmium, mercury, hexavalent chromium 100 ppm by weight |
The most significant operational boundary is low-temperature impact. LLDPE retains ductility at temperatures below -20°C, but the green pigment and part thickness can shift the ductile-to-brittle transition by several degrees. For outdoor applications in cold climates, notched impact testing at -40°C according to ISO 179-1/1eA should be performed on specimens cut from a moulded part, not only on compression-moulded plaques. Plaque data may overstate part toughness by failing to capture bubble entrapment, weld lines, and inner-surface oxidation from real moulding cycles.
Chemical exposure also imposes boundaries. In contact with aliphatic hydrocarbons, the material can swell and lose dimensionally stable properties; in contact with strong oxidisers or certain surfactants, environmental stress cracking may occur at surface defects. When the application involves diesel fuel, hydraulic oil, or agricultural chemicals, immersion testing under the relevant service temperature is more informative than standard ESCR screening because the failure mechanism depends on fluid polarity, surface tension, and oxidation products.
The green colourant adds another constraint. If the part is intended for food-contact use, the pigment package may require separate regulatory listing or migration data. Published data for this specific green-pigmented configuration are limited; end-use qualification should include total colourant migration, ultraviolet weathering, and lot-to-lot colour consistency tests. On a production basis, colour variation between lots can be measured with a spectrophotometer using CIELAB coordinates; lot-specific certificates should be retained to manage part appearance across multiple manufacturing sites.
Weathering performance of the green-pigmented system is determined by the stabiliser package and pigment type. For outdoor service, accelerated weathering can be screened using ASTM D2565 or ISO 4892-2 with UV-A 340 lamps and a 0.76 W/m²/nm irradiance at 340 nm. However, accelerated weathering data for green rotomoulded LLDPE are colour-dependent; the green pigment system may mask early yellowing while fading at the surface. Therefore, colour change measured by CIELAB ΔE and retained flexural strain at break should be recorded together.