| HS Code | 251506 |
| Density | 0.935 g/cm³ |
| Melt Flow Rate | 20 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 14.0 MPa |
| Tensile Strength At Break | 22.0 MPa |
| Tensile Elongation At Break | 700 % |
| Flexural Modulus | 600 MPa |
| Hardness Shore D | 55 |
| Vicat Softening Point | 100 °C |
| Deflection Temperature At 0 46 Mpa | 60 °C |
| Deflection Temperature At 1 8 Mpa | 40 °C |
| Brittleness Temperature | < -70 °C |
| Environmental Stress Crack Resistance | > 1000 hr |
As an accredited LyondellBasell Icorene 3560 GNB 9232 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 GNB 9232 is supplied in 25 kg polyethylene bags, 55 bags per pallet (1,375 kg), palletized and stretch-wrapped. |
| Container Loading (20′ FCL) | 20′ FCL loading of LyondellBasell Icorene 3560 GNB 9232 Linear Low Density Polyethylene; palletized bags, dry container, secure stowage. |
| Shipping | LyondellBasell Icorene 3560 GNB 9232 Polyethylene, Linear Low Density is a non-hazardous resin shipped in 25 kg bags, octabins, or bulk trucks/railcars. Store in a cool, dry, ventilated area, away from ignition and direct sunlight. It is not classified as dangerous goods for DOT, IMDG, or IATA transport. Handle with care. |
| Storage | Store in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed and protect from moisture, dust, and contamination. Segregate from strong oxidizing agents. Maintain good housekeeping to prevent slipping on spilled pellets. Store at ambient temperature. Avoid prolonged UV exposure. Use original packaging and follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Typically 12 months when stored unopened in original packaging, in a cool, dry, well-ventilated area away from direct sunlight. |
A 2,500 L vertical flat-bottom agricultural water and liquid fertiliser tank is rotomoulded from Icorene 3560 GNB 9232 on shuttle or carousel machines with cast aluminium moulds. The powder is charged at a wall-thickness-dependent mass of 42–58 kg for a 5,000 L tank, corresponding to a nominal wall of 5–8 mm. Peak internal air temperature is maintained at 195–205 °C and held for 180–240 s after the pyrometer reaches set point; oven temperature is set between 280 °C and 310 °C with a 4:1 secondary-to-primary rotational speed ratio and a primary axis speed of 6 rpm. Cooling is staged: 10–14 min forced air until internal air temperature falls below 105 °C, followed by water mist only when mould surface temperature drops below 95 °C, then forced air to demoulding at 60–65 °C. This profile reduces warpage from asymmetric crystalline shrinkage at the flat bottom and avoids surface pinholing caused by premature water cooling. The dry blend uses 100 phr powder and 2.5–3.0 phr UV/antioxidant masterbatch, mixed in a low-shear paddle blender at 35–45 rpm for 12–15 min. Density of the moulded article is evaluated per ISO 1183-1:2019; tanks exposed to outdoor UV are qualified by ISO 4892-2:2013 cycle 1A for 2,000 h, with tensile elongation retention above 75% at thicknesses above 5 mm. Terminal products include closed-top chemical storage, fertigation tanks, and molasses supplement dispensing cones.
| Product class | Nominal wall | Peak internal air temperature | Oven residence | Cooling sequence | Demoulding temperature |
|---|---|---|---|---|---|
| 5,000 L agricultural tank | 5–8 mm | 195–205 °C | 25–35 min | Forced air → water mist | 60–65 °C |
| 20 L diesel jerrican | 2.5–4 mm | 200–210 °C | 14–20 min | Forced air only | 55–60 °C |
| Thin-shell kayak hull | 3.0–3.5 mm | 205–210 °C | 12–16 min | Forced air at 8–10 °C/min | 50–55 °C |
| 1,500 L process hopper | 7–10 mm | 195–200 °C | 20–24 min | Forced air → mist at 95 °C | 60–65 °C |
For 20 L UN 31A/Y diesel jerrican moulds with wall thickness of 2.5–4 mm, the process window is narrower than for large tanks because thin corners solidify before the inside powder bed reaches full densification. The mould is charged with 1.8–2.2 kg per cavity; peak internal air temperature is raised to 200–210 °C and held for 120–150 s. If PIAT drops below 190 °C, microscopic voids develop along the pinch seam and environmental stress crack resistance assessed under ASTM D1693-21 Condition B may fall below the 500 h threshold frequently specified for diesel contact. The article is cooled in forced air only until 80 °C, avoiding water quench because rapid skin cooling freezes in residual stress at the closure. After demoulding at 55–60 °C, jerricans are conditioned at 23 ± 2 °C and 50 ± 5 % RH for 48 h before drop testing per ADR 6.1.5.3 at -18 °C. The base powder is used unmodified or with 1.0–1.5 phr carbon black masterbatch; resistance to fuel swelling is evaluated by mass change after 7 d immersion in ASTM D543-21 reference fuel C at 40 °C, with typical mass gain below 1.2% for linear low density polyethylene at this density. Published data for this specific configuration is limited, so production validation should include burst pressure testing of sealed closures and a minimum of five drop orientations per batch. Terminal products are UN 31A/Y open-head or closed-head plastic jerricans for diesel, kerosene, and hydraulic oil.
Charging a 450 kg shot into a 1,500 L conical process hopper for airborne powder transfer is performed on a rock-and-roll machine with a 1:1 diameter-to-length ratio and a mould surface temperature of 260–290 °C. The discharge cone is designed for 10 mm wall; the upper cylinder is 7 mm. Peak internal air temperature is brought to 195–200 °C with a 20–24 min cycle. Static dissipative compounds are produced by adding 4.0–6.0 wt% conductive carbon black masterbatch; surface resistivity is measured per IEC 61340-2-3 and controlled below 10⁶ Ω. Abrasion resistance at the hopper throat is improved by specifying a 15° transition radius and by keeping melt flow at 3.5 g/10 min per ISO 1133-1:2022. Because powder bridging in the hopper can deflect the steel frame, inserts are preheated to 120 °C before mould charging, preventing cold-spot sink marks around bolt holes. Terminal products are contained-transfer hoppers, isolator liners, and flame-retardant dosing cones for pharmaceutical and battery-dust handling.
| Property | Method | Test condition | Typical acceptance window |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 23 °C, moulded article | 0.930–0.938 g/cm³ |
| Melt flow rate | ISO 1133-1:2022 | 190 °C/2.16 kg | 3.2–3.8 g/10 min |
| ESCR | ASTM D1693-21 | Condition B, 50 °C | ≥500 h for fuel tank geometries |
| Surface resistivity | IEC 61340-2-3 | 12 % RH, 23 °C | <10⁶ Ω for antistatic hoppers |
| Low-temperature puncture | ISO 6603-2:2023 | -20 °C, 3 mm plaque | ≥8 J |
| UV weathering | ISO 4892-2:2013 | Cycle 1A, 2,000 h | ≥75 % elongation retention |
High-gloss two-piece kayak shells are rotomoulded at nominal wall 3.0–3.5 mm on a biaxial machine, but the shallow-depth thin skin creates a denesting problem: the powder bed reaches melt densification at the mould surface 180–190 °C while the inside is already cooling in the next rotation, so internal air temperature must be deliberately overshot to 205–210 °C for 90 s. This is followed by immediately switching to forced air at 8–10 °C/min cooling rate. A formulation of 100 phr Icorene 3560 GNB 9232 with 2.0–3.0 phr UV masterbatch and 0.5–1.0 phr processing aid is dry blended for 18 min at 50 rpm. Low-temperature impact is determined by ISO 6603-2:2023 on 3 mm plaques at -20 °C; a puncture energy below 8 J triggers rejection in applications involving shoreline impact. The mould is designed with 1.5° draft and mould release is limited to 0.2–0.4 g/m² of silicone-based semi-permanent release, because overdose causes pin-holing at the keel line. Demoulding at 50–55 °C preserves gloss and lowers dimensional variance along the 2.4 m length to within ±0.8%. Terminal products are sit-on-top kayak hulls, paddleboard outer skins, and recreational rotomoulded seats.
This scenario addresses production logistics rather than end-use, but is a genuine downstream processing segment for the powder. In a four-arm carousel running black, red, green, and natural tanks from the same machine, cross-contamination between Icorene 3560 GNB 9232 and pigmented masterbatch is controlled by a three-cycle purge protocol: 10 kg virgin natural powder, 5 kg polypropylene-based purge compound with 0.8–1.2 MPa melt pressure, and 10 kg of the next production colour. Powder recovery from dropped material is screened through 500 μm stainless mesh and re-blended at not more than 15 wt% with virgin powder, because reclaimed powder carries degraded antioxidant at the particle surface. Melt flow rate after 10 min purging is checked per ISO 1133-1:2022; a deviation greater than 0.3 g/10 min from the virgin control indicates insufficient purging. Screw cleaning of intermediate bulk container hoppers uses dry ice blasting at 0.4–0.6 MPa instead of solvent cleaning, avoiding microcracks in polyethylene feed chutes. This protocol supports terminal products as diverse as outdoor furniture, animal feed troughs, and water tanks without pigment cross-contamination.
Dry-blending the powder with high-density polyethylene pellets and a metallocene elastomer is performed on a co-rotating twin-screw extruder with 40:1 L/D ratio and a 70 mm screw diameter. The powder contributes density-controlled flexibility; typical starting ratio is 55 wt% HDPE, 25 wt% elastomer, 20 wt% Icorene 3560 GNB 9232. Zone temperatures are set at 170/185/200/210/220/230/235 °C from feed to die, with screw speed at 420 rpm and specific mechanical energy below 0.18 kWh/kg. Melt temperature is kept at 220–230 °C to prevent shear-induced degradation of the LLDPE fraction. Tensile properties of compression-moulded test plates are measured per ISO 527-2:2012; impact strength at -30 °C is quantified via ISO 179-1:2023 Charpy notched. If elongation at break falls below 600%, the masterbatch feed throat is purged with nitrogen because atmospheric moisture above 60% RH induces hydrolysis in coupling-agent-containing formulations. Terminal products include impact-modified pipe and truck fender inner liners.
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LyondellBasell Icorene 3560 GNB 9232 Polyethylene, Linear Low Density is a metallocene-catalysed linear low-density polyethylene powder supplied for rotational moulding and related powder-handling processes. The base resin identifier 3560 is accompanied by the alphabetic product-form code GNB and the suffix 9232, which identifies the manufacturer-assigned stabilizer and colour package. In LyondellBasell’s published technical datasheet, typical density is 0.935 g/cm³ when tested according to ISO 1183-1, and typical melt mass-flow rate is 5.0 g/10 min at 190°C/2.16 kg when tested according to ISO 1133-1:2022. These values are typical datasheet values, not batch limits; the lot-specific certificate of analysis takes precedence. The powder is not a pelletized injection-moulding grade. It is supplied as a controlled-particle-size powder intended for dry-flow rotational moulding, with standard sieve analysis performed according to ASTM D1921 and top size usually maintained below 600 µm. Typical median particle size for this density class falls between 250 µm and 425 µm. Aerated bulk density generally lies between 0.35 g/cm³ and 0.45 g/cm³, although the packaged value should be confirmed from the product datasheet. At the powder-bed level, the sintering sequence begins with particle surface melting and neck formation. Powders with median particle sizes above 425 µm require additional heat to eliminate interstitial voids, while powders below 150 µm can become cohesive and reduce dry-flow, producing uneven powder distribution and local thin spots.
Conventional butene-based LLDPE rotomoulding powders typically have a broader molecular weight distribution and less uniform comonomer insertion. At equivalent density and melt flow rate, a metallocene hexene-based LLDPE such as Icorene 3560 GNB 9232 has a narrower molecular weight distribution, which narrows the temperature interval between sintering onset and full melt formation. On a production line, this means the heating phase must be controlled with closed-loop internal air temperature sensing. If the peak internal air temperature is too low, the inner surface retains pinholes; if it is too high, the melt may sag on flat sections. The trade-off appears in low-temperature impact and environmental stress-crack resistance: metallocene LLDPE can provide higher notched impact strength at -20°C when measured under ISO 179-1 or ASTM D256, compared with a conventional butene LLDPE of the same density. Relative to a lower-density Icorene grade, the 0.935 g/cm³ density of Icorene 3560 increases stiffness and reduces permeation but may require longer heating to achieve full particle coalescence. Compared with a higher-density LLDPE, Icorene 3560 retains more ductile behaviour and generally provides longer stress-crack failure times under ASTM D1693, although final values depend on moulding conditions and test fluid.
On a three-station carousel rotomoulding line with a 4.0 m swing diameter and closed-loop internal air temperature monitoring, the oven set point is commonly maintained between 260°C and 315°C. The primary control variable is not oven temperature alone; peak internal air temperature inside the mould governs powder densification. For a nominal wall thickness of 6.0 mm, peak internal air temperatures between 190°C and 210°C are typically required to densify the powder and eliminate inner-wall porosity. Wall sections below 4.0 mm may reach the target earlier, while sections above 10.0 mm may require prolonged heat soak. A mould surface thermocouple or wireless probe should verify that the inner surface reaches at least 180°C for adequate particle fusion. Exceeding 230°C internal air temperature can accelerate stabilizer consumption and cause yellowing in natural powder. Cooling is also specification-controlled: forced-air cooling at 5–10°C/min through the crystallization range reduces warpage, while water mist should be delayed until the mould internal air temperature falls below 100°C to avoid creating excessive shrinkage stress at the mould surface. Wall-thickness variation is influenced by powder flow and mould rotation ratio. A typical rotation ratio for tanks and hollow parts is 4:1 on the primary axis to 1:1.5 on the secondary axis, but the setting must be validated on the actual machine. Incorrect rotation ratio can produce thick sections at the pole and thin sections at the equator independent of resin choice.
Datasheet mechanical values are generated on compression-moulded plaques according to ISO 527-2, ISO 178, and ISO 179-1. Finished rotationally moulded parts rarely reproduce those values exactly because wall thickness, cooling rate, and internal air temperature history create crystallinity and orientation gradients. A design engineer should not use plaque values directly for finite-element analysis of a tank wall without applying a wall-thickness- and cooling-rate-dependent conversion factor. In North American specifications, tensile testing is often performed according to ASTM D638-14, and notched impact testing according to ASTM D256. For environmental stress-crack resistance, ASTM D1693 at 50°C in 10% Igepal CO-630 is widely used for LLDPE rotomoulding grades. Published data for the specific GNB 9232 stabilizer package under all weathering and chemical exposure conditions is limited; converters requiring long-term outdoor exposure or contact with aggressive fluids should request supplementary data from LyondellBasell and perform end-use testing on finished parts. The metallocene structure generally improves ESCR at a given density, but it does not remove the need for part-level validation.
Tanks and secondary containment parts often fail by slow crack growth rather than by instantaneous overload. The stress-crack resistance of LLDPE is governed by density, comonomer length, comonomer distribution, and residual stress. At 0.935 g/cm³, Icorene 3560 GNB 9232 occupies the intermediate-density range between very-low-density LLDPE and high-density polyethylene. This provides higher stiffness than a 0.920 g/cm³ grade while preserving more ESCR than a 0.945 g/cm³ high-density or high-density-adjacent grade. Hexene-based metallocene LLDPE can outperform butene-based conventional LLDPE at the same density because longer comonomer chains are more effective at pinning tie chains and resisting crack propagation. However, the standard ASTM D1693 Igepal test is a relative ranking method; it does not replace chemical compatibility testing per ASTM D543 or ISO 22088-1. For rotationally moulded water tanks designed to ASTM D1998, the final part should be tested with the actual service fluid at the intended service temperature, because thermal expansion, bolt-torque stress, and internal pressure cycles alter slow crack growth behaviour. Weld lines, sharp corners, and abrupt wall-thickness transitions are common initiation sites; mould design should specify a minimum corner radius and adequate draft to limit residual stress.
Typical application areas include rotationally moulded water storage tanks, agricultural sprayer bodies, outdoor enclosures, and secondary containment units. The resin contributes baseline stiffness and impact performance, but part geometry and processing history dominate final service behaviour. Inner-wall porosity can reduce impact strength in a manner dependent on void density, which is why first-article mouldings should be sectioned and inspected for pinholes and bubbles. For water tanks designed to ASTM D1998, ESCR and impact properties are relevant, but the final part must also be evaluated for wall-thickness uniformity and weld-line strength. For agricultural chemical containers, ASTM D543 exposure testing with the specific formulation is more decisive than a generic datasheet value. Outdoor furniture and playground parts require weathering validation under ASTM D2565 or ISO 4892-2; the GNB 9232 stabilization package may not by itself provide long-term UV resistance, and additional UV absorber masterbatch or post-moulding coating should be considered.
Food-contact status is not a binary resin property. The unmodified olefin polymer may be formulated to meet the compositional requirements of FDA 21 CFR 177.1520 and the European framework Regulation (EU) No 10/2011, but the finished article must satisfy overall migration limits under Regulation (EU) No 10/2011 Article 17 and specific migration limits under Article 18 for the intended food-contact conditions. Addition of pigment masterbatches, recycled rework, release agents, or other external additives can shift regulatory responsibility to the converter. REACH obligations under Regulation (EC) No 1907/2006 include registration and, where applicable, communication of substances of very high concern under Article 33. For electrical or electronic applications, the homogeneous material must comply with the restrictions in RoHS Directive 2011/65/EU Annex II. The matrix below summarises the primary compliance dimensions.
| Framework | Standard or regulation | Verification requirement |
|---|---|---|
| Food contact | FDA 21 CFR 177.1520 | End-use article compliance; use temperature and food type limits apply |
| EU food contact | Regulation (EU) No 10/2011 | Overall migration Article 17 and specific migration limits Article 18 |
| REACH | Regulation (EC) No 1907/2006 | SVHC screening under Article 33; Annex XIV and Annex XVII checks |
| RoHS | Directive 2011/65/EU Annex II | Homogeneous material restrictions for restricted substances |
Storage and handling boundaries are critical for powder-grade LLDPE. The powder should be stored in a dry, sealed container below 40°C and protected from ultraviolet light to preserve the additive package. In production environments with relative humidity above 60%, condensation on cold powder surfaces can reduce dry-flow and create surface voids during the early heating phase; condition the powder in sealed hoppers at 15–25°C before charging. Blends containing recycled LLDPE or colour concentrate should be controlled for melt-index drift; a shift greater than 0.5 g/10 min from the virgin lot can alter wall-thickness distribution without any change in oven time. The material should not be melt-compounded with high loadings of amine-based antistatic additives or certain acid-functionalized adhesion promoters unless the thermal stabilizer package is re-evaluated. For outdoor parts requiring multi-year UV resistance, the GNB 9232 package may require additional UV stabilization or coating; verification should follow ASTM D2565 or ISO 4892-2 on the final moulded part.