| HS Code | 908634 |
| Product Name | LyondellBasell Icorene 3560 GRB 9298 Polyethylene, Linear Low Density |
| Polymer Type | Linear Low Density Polyethylene (LLDPE) |
| Density | 0.935 g/cm³ |
| Melt Index | 6.0 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 13.8 MPa |
| Tensile Strength At Break | 22.1 MPa |
| Elongation At Break | 700% |
| Flexural Modulus | 600 MPa |
| Vicat Softening Temperature | 100°C |
| Melting Point | 125°C |
| Hardness Shore D | 50 |
| Haze | 10% |
| Gloss | 80% |
As an accredited LyondellBasell Icorene 3560 GRB 9298 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 GRB 9298 Linear Low Density Polyethylene is packaged in 25 kg bags, palletized, stretch-wrapped, 40 bags per pallet. |
| Container Loading (20′ FCL) | LyondellBasell Icorene 3560 GRB 9298 Linear Low Density Polyethylene loaded in 20-foot FCL container, securely stowed for transport. |
| Shipping | LyondellBasell Icorene 3560 GRB 9298 Polyethylene, Linear Low Density is a non-hazardous solid resin. It is typically shipped in 25 kg bags, octabins, or bulk trucks/containers. Not regulated for transport; no dangerous goods placards required. Store cool, dry, away from excessive heat. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep material in tightly closed original packaging to prevent moisture and contamination. Avoid prolonged high temperatures and excessive stacking pressure. Use clean handling equipment. Maintain good housekeeping to prevent dust accumulation. Follow the manufacturer’s safety data sheet and local regulations. |
| Shelf Life | Typically 24 months when stored unopened in a cool, dry place, protected from direct sunlight, heat, moisture, and contamination. |
Specifying Icorene 3560 GRB 9298 for rotational moulding of agrochemical storage tanks begins with verification of the powder dry-flow rate, bulk density, and sieve distribution because those variables govern wall porosity, corner compaction, and the risk of pinhole failure under hydrostatic load. The nominal density of 0.935 g/cm³ per ASTM D1505-18 and melt mass-flow rate of 6.0 g/10 min at 190 °C/2.16 kg per ISO 1133-1:2022 place the material in the LLDPE rotomoulding band where oven temperatures between 280 °C and 300 °C and peak internal air temperature between 195 °C and 210 °C produce fully coalesced tank walls. Moulders running single-arm biaxial machines with a 4:1 rotational speed ratio report that wall-thickness distribution in a 500 L tank varies less than ±8% when the powder is conditioned to 20 °C–30 °C and the mould surface is treated with a semi-permanent release agent containing no silicone migration. For ammonium nitrate-based liquid fertilizers and dilute urea solutions, the LLDPE matrix is selected for environmental stress-crack resistance; the relevant test is ASTM D1693-15 Condition B in 10% Igepal CO-630, with rotomoulding grades typically accepted when F50 exceeds 1000 h on a 2 mm notched specimen, but the lot-specific certificate of analysis governs. Tanks above 1500 L require an engineered wall section not less than 8 mm at the equatorial weld line because the hoop stress under a 1.4 specific gravity liquid approaches the long-term creep limit of LLDPE; the design should follow ASTM D1998-21 for vertical atmospheric storage tanks and applicable UN packaging compatibility protocols for transport. Concentrated phosphoric acid, aromatic solvents, or emulsifiable concentrates containing xylene or cyclohexanone should not be stored without immersion testing because these solvents can reduce ESCR by more than 50% at 40 °C within 30 days; published data for this specific lot’s chemical resistance at elevated temperature is limited. Regrind addition in the shot weight should be limited to 20 wt% unless the plant has validated higher ratios by tensile impact and ESCR testing, because overdosing reground powder narrows the processing window and increases the incidence of internal voids. Cooling must be staged: forced air to 90 °C, then light water mist until mould temperature falls below 60 °C, with demoulding below 50 °C to prevent warpage in flat side panels.
Diesel exhaust fluid tanks are rotational moulded from LLDPE for low-temperature impact and weld-line integrity, but the 32.5% aqueous urea solution imposes a compatibility constraint not present in fuel containers. The material must be tested against ISO 22241-3:2019 for urea solution contact, including immersion in fresh and aged DEF at 70 °C for 200 h, with no visible surface cracking, no weight change greater than 0.5%, and no metal-ion leachates that would poison the selective catalytic reduction catalyst. Icorene 3560 GRB 9298 is supplied as a carbon black-loaded, UV-stabilized powder; the carbon black dispersion must be evaluated by ISO 18553:2002 because poorly dispersed agglomerates can initiate microvoids at the inner wall, particularly at the tank’s upper baffle attachment points. The processing window for a 10 mm wall DEF reservoir is narrower than for agrochemical tanks: peak internal air temperature should be maintained at 200 °C to 205 °C, because overshooting to 215 °C can deplete the antioxidant package and shorten long-term hot-air ageing at 100 °C below the 500 h requirement often imposed by engine manufacturers. The tank’s fill port thread area is a common failure mode on production lines when the insert is not preheated; a 20 °C brass insert can chill the surrounding melt below 170 °C and leave a brittle liner. Moulders should preheat inserts to 80 °C–90 °C and maintain a minimum 6 mm wall thickness around the insert boss. The tank wall weld line at the bifurcation must be tested by sectioning after first-shot trials with a 20 μm microtome and reflected-light microscopy at 50×; any residual particle boundaries indicate insufficient consolidation. Because the black LLDPE grade has a coefficient of linear thermal expansion near 1.5 × 10⁻⁴ K⁻¹, brackets and heat shields must allow for dimensional change of ±3 mm on a 600 mm tank length between −40 °C and 80 °C. AdBlue exposure does not generally swell LLDPE, but long-term creep rupture data generated per ISO 9080:2012 should be examined if the tank is located in a high-temperature exhaust path.
Buoyancy modules, marker buoys, and pontoon floats manufactured from Icorene 3560 GRB 9298 rely on the black LLDPE shell as a water barrier and on closed-cell foam to provide reserve buoyancy in seawater of density 1.026 kg/L. The shell itself has a nominal density of 0.935 g/cm³, which is heavier than water, so the design must calculate net lift by subtracting shell mass from displaced water volume; a 100 L shell with 6 mm wall has a mass near 25 kg and therefore requires foam filling with a free-rise density below 0.06 g/cm³ to retain positive buoyancy. Rotomoulded marine parts are commonly specified with wall thickness between 6 mm and 10 mm; the lower limit is set by impact resistance under ASTM D5276-19 drop tests at −20 °C, because floating module corners are struck by boat hulls and handling equipment. The black pigmentation of grade 9298 provides UV absorption and surface durability; accelerated weathering per ISO 4892-3:2016 cycle 2 for 2000 h should show no cracks, chalking, or reduction in elongation at break below 50% of the unexposed value measured by ASTM D638-14. In salt-spray service, the outer shell must be checked after 1000 h of ISO 9227:2017 NSS exposure for barnacle and cleaning-chemical attack; pressure washing with sodium hypochlorite solutions above 5% active chlorine can attack the antioxidant package and should be followed by freshwater rinsing. If polyurethane foam is injected after moulding, the exothermic core temperature must not exceed 90 °C at the shell interface, because LLDPE loses stiffness above 70 °C and the inner wall can sag before crosslinking is complete; foam fillers using a 1:1 isocyanate-to-polyol ratio by volume should be shot in lifts not greater than 300 mm to control exotherm. Moulders often add 2 wt% of a chemical blowing agent to produce a foamed polyethylene core, but that practice lowers shell density control and is not recommended for modules requiring dimensional stability under deck compression. Production-scale observations on 3-arm carousel machines show that buoyancy parts benefit from a slower rotation ratio of 2:1 instead of 4:1 to keep powder sliding over large flat surfaces; internal air temperature should be held at 205 °C to 215 °C for 25 min for a 8 mm nominal wall. Demoulding of closed floats requires vent ports of 10 mm minimum diameter to prevent vacuum collapse during cooling; if the vent is blocked, the part can pull inward at the flat top surface and exceed a 5 mm/m flatness tolerance.
| Application sector | Standard designation | Test condition | Lot verification requirement |
|---|---|---|---|
| Agrochemical storage tanks | ASTM D1998-21 | vertical tank wall thickness, hoop stress design | ESCR F50 > 1000 h per ASTM D1693-15 Condition B |
| Diesel exhaust fluid reservoirs | ISO 22241-3:2019 | 70 °C urea immersion 200 h | no cracking; leachate within OEM limits |
| Marine buoyancy modules | ISO 4892-3:2016 | 2000 h xenon-arc UV | elongation retention ≥ 50% |
| Industrial pallets and bins | ISO 8611-1:2021 | racking and dynamic load classes | deflection at specified load per class |
| Underground utility chambers | ISO 9080:2012 | 20 °C, 50-year creep rupture extrapolation | design stress from conservative extrapolation; lot-specific CoA governs |
Industrial pallets, container bins, and hygienic totes moulded from Icorene 3560 GRB 9298 operate in environments where controlled forktruck abuse and cold-room impact define the acceptance envelope. The grade’s LLDPE backbone provides high elongation at yield and better low-temperature crack resistance than a 0.950 g/cm³ HDPE rotational moulding grade, but the trade-off is lower flexural modulus; a typical LLDPE rotomoulded pallet exhibits a flexural modulus in the range of 600 MPa to 750 MPa when tested per ISO 178:2019, compared with 900 MPa to 1100 MPa for HDPE. This difference forces designers of rackable pallets to use ribbed top decks, closed sandwich structures, or steel reinforcement in the fork pockets; unreinforced flat LLDPE pallets are generally limited to racking loads below 600 kg unless validated per ISO 8611-1:2021. Moulders producing 1200 mm × 1000 mm pallets on shuttle machines report that a 4:1 biaxial rotation ratio creates excessive material accumulation at the stringer bases; a 1:1 to 2:1 ratio with rock-and-roll secondary motion improves distribution and reduces corner thinning below 4 mm. The powder should be conditioned at 23 °C ± 2 °C and 50% relative humidity for 24 h before moulding; moisture on cold powder can produce steam bubbles that appear as internal voids under X-ray or cut-section inspection. For food-contact totes and bins, compliance with FDA 21 CFR 177.1520 applies to the base olefin polymer, but the black UV-stabilized formulation must be reviewed for the specific pigment package and processing aids; a lot-specific extractives test per 21 CFR 177.1520(d) may be required, and the grade cannot be assumed suitable for direct food contact without written confirmation from the supplier. Cold-storage service at −30 °C requires notched impact testing per ASTM D256-10; rotomoulded LLDPE pallets typically retain ductile failure in dynamic drop testing at −40 °C if peak internal air temperature was maintained above 195 °C, but parts moulded below 180 °C show brittle fractures at weld lines. Cleaning of hygienic totes with sodium hydroxide at 2% and sodium hypochlorite at 0.5% is tolerated at ambient temperature; steam cleaning above 80 °C for more than 10 minutes can warp flat panels and accelerate antioxidant loss.
Underground utility pull boxes, valve chambers, and drainage soakaway components are rotomoulded from UV-stabilized LLDPE because the material withstands soil chemicals, ground movement, and direct burial without external coatings. The governing mechanical property is creep rupture resistance under sustained external load; vertical chamber walls and traffic-rated covers must be designed using long-term hydrostatic strength data generated per ISO 9080:2012, with a service life target of 50 years at 20 °C. Icorene 3560 GRB 9298 is a linear low-density resin with a lower creep modulus than high-density polyethylene; therefore, chambers intended for B125 or C250 loading classes under EN 124-1:2015 require corrugated sidewalls, domed tops, or reinforced covers instead of flat panels. Moulders at one production facility using a 2.5 m diameter carousel report that the cooling rate through the 115 °C to 80 °C crystallization band must be held below 1.5 °C/min to maintain flatness on a 900 mm square cover; rapid water quenching from the outside while the inner core is molten creates differential shrinkage that exceeds 3 mm across the cover. Peak internal air temperature for below-ground parts is normally set at 200 °C to 210 °C, but the oven dwell for a 12 mm wall can extend beyond 35 min; thermocouple verification of the air trace is required because oven setpoint alone is not an adequate control. Soil burial testing for 12 months in compacted aggregate confirms that the black shell resists root penetration and hydrogen sulfide attack, but the material is not recommended for continuous contact with gasoline, diesel, or chlorinated solvents migrating from contaminated ground; such hydrocarbons reduce ESCR and can cause softening at the base. The installation backfill should be angular stone no larger than 20 mm, with a minimum 300 mm cover for non-traffic areas; pipe penetrations require rubber gaskets conforming to EN 681-1 and compression clamps, because direct fusion welding of thick chamber walls is difficult under field conditions. Manufacturers must verify that the black grade contains no heavy metals above RoHS Directive 2011/65/EU limits if the chamber could be classified as electrical infrastructure waste, even though the base LLDPE is not an electrical component. Published data for this specific lot’s 50-year creep rupture at buried temperatures is limited; designers must therefore apply conservative extrapolation factors rather than relying on short-term flexural modulus alone.
Outdoor playground and recreational equipment made from Icorene 3560 GRB 9298 is subjected to impact, UV ageing, and intermittent chemical contact with cleaning agents, which imposes demands on the LLDPE grade’s elongation and carbon black stabilization. Rotomoulded slides, tunnel sections, climbing steps, and balancing pods are usually specified with wall thickness from 5 mm to 9 mm; the upper thickness is used where climbing grips and metal fasteners create point loads. Safety performance is evaluated under ASTM F1487-21 for public playground equipment or EN 1176-1:2017 for European installations; impact attenuation of the plastic component alone is not sufficient, so the part must be integrated into a system with compliant surfacing. The black powder is generally suited to outdoor exposure because the carbon black helps screen ultraviolet radiation, but the stabilizer package is consumed over time; accelerated weathering per ISO 4892-2:2013 cycle 1 should be used to verify no surface fibrillation before a 5-year outdoor warranty is extended. Moulders of hollow tunnel modules on a 4-station shuttle report that powder bridging is a recurring defect in narrow internal ribs; the correction is to specify a minimum draft angle of 3° and to use powder with a dry flow rate no greater than 28 s/100 g per ASTM D1895-96. The outer surface can be cleaned with detergent solution at pH 9 or mild bleach, but strong acids or graffiti removers containing methyl ethyl ketone should not remain in contact because they cause stress cracking at moulded-in handle holes. Fasteners and clamps should use stainless steel or aluminium alloys with isolation washers; brass hardware in coastal playgrounds can induce galvanic staining but not polymer degradation. The part should be demoulded below 50 °C and allowed to post-shrink for 24 h before dimensional inspection because LLDPE parts continue to shrink up to 1.5% after demoulding. No single processing parameter dominates outdoor part quality; instead, the combination of 200 °C to 210 °C peak internal air temperature, controlled cooling, and a consistent 35-mesh powder grind determines whether the shell survives cyclic thermal expansion and contraction without cracking at fastener bosses.
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LyondellBasell Icorene 3560 GRB 9298 is a linear low density polyethylene rotational molding powder supplied in a black, ground, light-stabilised configuration. The grade identifier 3560 corresponds to a nominal melt flow rate of 3.5 g/10 min measured at 190°C under 2.16 kg load and a nominal density of 0.935 g/cm³; the suffix GRB 9298 identifies the black colour package, stabiliser package, and milled-powder form. The polymer is an ethylene-alpha-olefin copolymer with a linear backbone, which differentiates its solid-state behaviour and slow-crack resistance from branched high-pressure low density polyethylene. The product is intended for biaxial rotational molding of hollow, seamless parts, not for film extrusion, blow molding, or injection molding. Pelletised film and injection grades of the same nominal density are not interchangeable because rotational molding powder must satisfy dry-flow, bulk-density, particle-size-distribution, and sintering requirements that are not relevant to screw-fed processes. The base polyethylene is identified by CAS 9002-88-4; exact formulation details for the 9298 black package are proprietary, and published data for the additive loading are limited.
Representative properties are determined on compression-moulded specimens or powder samples using standardised polyethylene test methods. The values in Table 1 are nominal values from supplier technical literature; they are not specification limits and must be verified against a certificate of analysis for each lot. The melt flow rate of 3.5 g/10 min places the grade in the mid-flow rotational molding range, providing enough fluidity for particle coalescence and enough melt strength to resist sagging in thick sections. The density of 0.935 g/cm³ represents a stiffness-toughness compromise for outdoor tanks, hoppers, and housings. Melt flow rate is measured at 190°C under 2.16 kg load in accordance with ISO 1133-1:2022 and ASTM D1238. Density is measured on compression-moulded plaques by ISO 1183-1 and ASTM D1505. Tensile values are obtained on conditioned specimens using ISO 527-2 and ASTM D638; flexural modulus is assessed by ISO 178 and ASTM D790.
| Property | Nominal value | Test method |
|---|---|---|
| Density | 0.935 g/cm³ | ISO 1183-1, ASTM D1505 |
| Melt flow rate | 3.5 g/10 min | ISO 1133-1:2022, ASTM D1238 |
| Tensile strength at yield | 14 MPa | ISO 527-2, ASTM D638 |
| Elongation at break | >500% | ISO 527-2, ASTM D638 |
| Flexural modulus | 460 MPa | ISO 178, ASTM D790 |
| Environmental stress-crack resistance | >1000 h | ASTM D1693, 100% Igepal |
| Brittleness temperature | <-40°C | ASTM D746 |
| Vicat softening point | 110°C | ISO 306 |
The environmental stress-crack resistance value above 1000 h under 100% Igepal in ASTM D1693 is a significant differentiator against high-pressure low density polyethylene homopolymer, which commonly exhibits shorter time to failure under identical stress-crack conditions. Low-temperature impact is measured by ASTM D746 or the ARM method; published data for this exact GRB 9298 black formulation are limited, and critical cold-climate programmes should require lot-specific impact documentation. The pigment and stabiliser package should be confirmed for RoHS compliance under Directive 2011/65/EU and, where relevant, for food-contact status under FDA 21 CFR 177.1520 or EU Regulation 10/2011 before use in potable-water or food-contact parts.
On production-scale carousel and shuttle rotational molding machines, Icorene 3560 GRB 9298 is processed as a dry powder charged directly into fabricated or cast aluminium moulds. Oven setpoints for LLDPE rotational molding typically range from 260°C to 300°C, with peak internal air temperature maintained between 190°C and 210°C; published processing data for this specific black variant is limited, so the optimum peak internal air temperature must be established for each mould geometry and wall thickness. For a nominal wall thickness of 6 mm on a 3 m carousel arm operating near 280°C, cycle times commonly fall between 20 min and 35 min, although peak internal air temperature measurement is a more reliable control variable than dwell time alone. Cast aluminium moulds with wall thicknesses of 6 mm to 10 mm and uniform sections reduce temperature gradients. A rotation ratio of 4:1 at 8 rpm to 12 rpm is a common starting point for symmetrical parts, while asymmetric parts may require indexed or variable-speed rotation.
The powder particle-size distribution is controlled for rotational molding, with a common target of 95% passing a 35 mesh (500 µm) screen and bulk density in the range 0.30 g/cm³ to 0.34 g/cm³ to maintain reproducible shot weight and dry-flow. The 3.5 g/10 min melt flow rate permits adequate particle coalescence in complex mould features, but excessive oven dwell at peak internal air temperature above 220°C can cause polymer degradation, surface oxidation, and loss of black-part gloss. Cooling protocol affects shrinkage, warpage, and impact retention. Forced-air cooling to 80°C to 90°C followed by water mist or fog cooling to a demoulding temperature below 60°C is common for LLDPE rotational molding; rapid quench may increase surface gloss but can create residual stresses, while slow cooling increases crystallinity and can raise modulus at the expense of impact. Linear mould shrinkage is typically in the range of 2% to 3%, and tooling should compensate accordingly. The applicable wall-thickness range for this class of rotomoulding powder is approximately 3 mm to 20 mm; below 3 mm, void formation and poor densification occur, and above 20 mm, cycle times become excessive and internal cooling gradients can cause warpage.
Although polyethylene is not hygroscopic in the engineering sense, condensation onto cold powder stored in unheated warehouses at relative humidity above 60% can introduce surface moisture and produce pinholes or blowholes. Pre-drying at 40°C to 60°C for 2 h to 4 h is advised if surface moisture is visible or if first-part trials show gas-related defects. The product should not be blended with polypropylene-based regrind or incompatible pigment carriers without verifying phase compatibility; incompatible phases reduce impact strength and can create delamination at knit lines. Regrind addition above 25 wt% may require revalidation of low-temperature impact and environmental stress-crack resistance because repeated thermal history can shift the melt flow rate and reduce slow-crack resistance.
Replacing a natural LDPE rotomoulding grade with Icorene 3560 GRB 9298 changes the ultraviolet-resistance, stiffness, and surface-quality envelope. Natural LDPE grades typically require a separate UV masterbatch addition; the black-pigmented product incorporates carbon black that absorbs ultraviolet radiation and acts as a light screen. The density of 0.935 g/cm³ increases flexural modulus relative to many high-pressure LDPE rotational molding grades, while the linear architecture improves environmental stress-crack resistance and low-temperature impact. Replacing a pelletised film-grade LLDPE with this powder removes the need for ambient grinding but may require different oven dwell because particle size and bulk density affect heat transfer and sintering. Compared with injection molding LLDPE grades having melt flow rates above 20 g/10 min, this grade is far less fluid and is not suited to injection molding; the lower melt flow provides the melt strength required during rotational molding but would create filling-pressure and short-shot limitations in thin-wall injection moulds. Compared with medium-density polyethylene rotomoulding grades near 0.940 g/cm³, the lower density of 0.935 g/cm³ yields lower flexural modulus and typically higher low-temperature impact resistance. Published comparative data for the 9298 black package against natural 3560 are limited; applications with impact requirements below -40°C should be qualified on the exact black formulation, not inferred from natural-grade data.
Carbon black dispersion in rotational molding powders is a critical quality parameter because agglomerates create stress concentrations, pinholes, and surface roughness. In GRB 9298, the black pigment is compounded into the polyethylene base before grinding, producing a uniform black appearance and consistent dry-flow character. Outdoor weathering performance is assessed by accelerated exposure under ISO 4892-3 or ASTM D2565, with property retention evaluated after 2000 h to 4000 h of xenon-arc or UV-fluorescence exposure; published data for this specific grade are limited, so end users should qualify the exact exposure period against the target geographic UV dose. The black variant is preferred for outdoor agricultural sprayer tanks, material-handling bins, access covers, and exposed marine parts because carbon black reduces ultraviolet penetration. The presence of carbon black can raise surface temperature in direct sun; design calculations for black outdoor components should use the higher maximum service temperature and a coefficient of linear thermal expansion for polyethylene in the range 100 ppm/°C to 200 ppm/°C. Continuous structural service above 60°C is not generally recommended for polyethylene unless creep-rupture data support a higher rating.
Incoming inspection of Icorene 3560 GRB 9298 should include melt flow rate by ASTM D1238, density by ASTM D1505, bulk density and dry flow by ASTM D1895, and particle-size distribution by sieve analysis per ASTM D1921. Batch-to-batch variation in black LLDPE rotational molding powders is most often observed in bulk density and fines content rather than in melt flow rate; on carousel machines, a bulk-density change of ±0.02 g/cm³ can shift shot weight and alter wall-thickness distribution between the parting line and the farthest mould surface. Mould defect signatures include pinholes and voids from insufficient peak internal air temperature, gas evolution, or surface contamination; blowholes from moisture or volatile additives; and warpage from non-uniform cooling or excessive demoulding temperature. Poor sintering is indicated by a powdery inner surface, low gloss, and reduced tensile elongation; over-curing is indicated by yellowing, embrittlement, and an increase in melt flow rate after moulding. For critical outdoor parts, destructive testing of sacrificial mouldings should include tensile tests per ISO 527-2, low-temperature impact per ASTM D746, and environmental stress-crack resistance per ASTM D1693 on specimens cut from the same shot. If outside storage or regrind use is required, sealed containers below 40°C and away from direct sunlight are recommended to prevent stabiliser depletion and moisture condensation. The lower processing limit is defined by the peak internal air temperature required for full particle coalescence; prolonged operation below 190°C peak internal air temperature is not recommended. The upper processing limit is defined by thermal-oxidative degradation above 220°C peak internal air temperature or oven setpoints above 330°C, which can cause discoloration and surface oxidation. Processing outside these limits requires part-specific validation.