| HS Code | 798653 |
| Material Type | Polyethylene, Linear Low Density |
| Density | 0.935 g/cm3 |
| Melt Index | 3.5 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 11 MPa |
| Tensile Strength At Break | 25 MPa |
| Elongation At Break | 800% |
| Flexural Modulus | 340 MPa |
| Izod Impact Notched | 0.5 J/cm |
| Vicat Softening Point | 100 °C |
| Melting Point | 124 °C |
| Hardness Shore D | 55 |
| Thermal Conductivity | 0.33 W/m-K |
| Coefficient Of Linear Thermal Expansion | 1.5E-4 cm/cm/°C |
| Specific Heat Capacity | 2.3 J/g-°C |
| Environmental Stress Crack Resistance | >1000 h |
As an accredited LyondellBasell Icorene 3560 BWO 9273 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 polyethylene bags, with 1,000 kg per pallet for industrial handling and storage. |
| Container Loading (20′ FCL) | 20' FCL: LyondellBasell Icorene 3560 BWO 9273 Linear Low Density Polyethylene, 25 kg bags, palletized, shrink-wrapped, secured for ocean transport. |
| Shipping | LyondellBasell Icorene 3560 BWO 9273 Polyethylene, Linear Low Density, is generally nonhazardous and not regulated for transport. Ship in sealed 25 kg bags, octabins, or bulk containers. Keep dry, cool, and away from UV, heat, and contamination. Follow the SDS and applicable local, national, and international shipping regulations. |
| Storage | Store in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers or bags tightly closed to prevent moisture, dust, and contamination. Use original packaging, stack securely, and avoid prolonged UV exposure. Maintain normal ambient temperatures; follow local regulations and the manufacturer’s SDS recommendations. Do not store near food, feed, or incompatible chemicals. Prevent static buildup and dust accumulation. |
| Shelf Life | Typically 24 months from manufacture when stored in original, unopened packaging in a cool, dry area away from direct sunlight. |
For vertical cylindrical water and liquid-feed tanks, LyondellBasell Icorene 3560 BWO 9273 Linear Low Density Polyethylene is dry-charged as a black UV-stabilized rotomoulding powder, with no additional carbon black masterbatch in the standard outdoor formulation because the BWO 9273 package already incorporates the light-shielding system. Outdoor agricultural storage containers in this category are specified to the dimensional and hydrostatic deformation requirements of ASTM D1998-15, while food-contact or drinking-water end uses are separately evaluated under EU No 10/2011 for overall migration at 10 mg/dm² or under finished-tank certification to NSF/ANSI 61. The baseline formulation is 100% as-supplied virgin powder; non-potable agricultural tanks may accept up to 20 wt% same-grade regrind if the regrind is screened below 500 µm and is free from polypropylene or silane-crosslinked contamination, while potable-water and food-contact tanks remain at 100% virgin material unless the certifying body approves a documented closed-loop regrind fraction. Production on a carousel or shuttle rotational moulding machine uses an oven setpoint of 280 °C to 310 °C and a peak internal air temperature of 190 °C to 205 °C; below 185 °C incomplete interparticle coalescence produces inner-surface pitting, and above 210 °C the weathering package can degrade into visible gas voids and reduced impact strength. For 6 mm to 10 mm nominal walls, heating time is 16 min to 24 min at a primary-to-secondary rotation ratio of 4:1 to 5:1, followed by forced-air cooling to 80 °C and water-mist cooling to 60 °C before demoulding. Terminal products include 500 L to 5000 L vertical storage tanks, transport tanks, liquid-feed troughs, and sprayer saddle tanks.
Chemical containment mouldings for acid day tanks, coagulant dosing stations and secondary spill containment require stress-crack resistance rather than short-term creep resistance, because the failure mode develops at internal wall discontinuities after prolonged exposure to surfactants, oxidizing agents or warm caustic. The applicable structural specification is ASTM D1998-15 for upright polyethylene tanks, while compatibility screening is performed by immersion in the actual service fluid at maximum operating temperature according to ASTM D543-20 or ISO 175:2010. The formulation rule is to remove regrind above 15 wt% unless the moulder has completed ESCR testing on finished parts; multi-pass regrind raises low-molecular-weight tails and can shift ASTM D1693-15 Condition B failure from ductile yielding to brittle crack propagation in surface-active service environments, especially at wall thickness below 4 mm. For aggressive oxidizer duty the starting formulation is 100% as-supplied Icorene 3560 BWO 9273 powder; where regrind is permitted, it is limited to 10 wt% to 15 wt% and pulled only from the same black outdoor grade, screened through a 35-mesh sieve, and dried to residual moisture below 0.05 wt% if condensation has occurred. Tooling is cast aluminium or fabricated steel; oven setpoint is held at 285 °C to 295 °C, peak internal air temperature at 195 °C to 205 °C, and the mould is maintained at peak temperature for 3 min to 5 min to complete densification. Controlled cooling from 100 °C to demoulding at 50 °C at not more than 6 °C/min reduces residual stress. Terminal products include 120 L to 2000 L vertical day tanks, bunded pallets, drainage sump liners, tank lids, and flanged manway fittings. Published data for this specific configuration are limited; chemical resistance must be validated on finished coupons at the maximum expected temperature and concentration.
The following matrix consolidates the compliance instruments referenced across the downstream scenarios.
| Standard or regulation | Application boundary | Relevant test or certification parameter |
| FDA 21 CFR 177.1520 | Food-contact tank liners, insulated fish box inner skins | Olefin polymer extraction and end-use temperature limits |
| EU No 10/2011 | EU food-contact mouldings | Overall migration ≤ 10 mg/dm² and specific migration limits per Annex I |
| NSF/ANSI 61 | Potable water contact tanks and liners | Finished-product extraction panel |
| ASTM D1998-15 | Polyethylene upright storage tanks | Design, hydrostatic deformation and quality control |
| ASTM D1693-15 Condition B | Environmental stress-crack resistance | Time to failure in surface-active environment |
| EN 71-3:2019+A1:2021 | Toy-like playground components | Element migration limits |
| ASTM F1487-21 | Public playground equipment | Consumer safety performance |
| ISO 8611 series | Distribution pallets | Stiffness and maximum working load |
Dredge pipeline floats and pontoon shells are rotomoulded on multi-axis carousel machines with steel or cast aluminium tooling, using Icorene 3560 BWO 9273 as the outer shell compound because the black weathering package resists ultraviolet embrittlement during continuous marine exposure. Procurement documents for this sector generally do not cite a single marine resin standard; they combine tensile property retention after accelerated weathering by ISO 4892-2:2013, tensile properties by ASTM D638-14, low-temperature brittleness at -20 °C by ASTM D746-20, and environmental stress-crack resistance by ASTM D1693-15 Condition B. The outer shell is charged at 100% as-supplied powder for seawater-immersion components; non-structural interior buoy cores may accept 20 wt% same-grade regrind if the regrind is dry, screened below 500 µm, and has not lost its stabilizer package from previous long-term immersion. Walls are maintained at 6 mm to 12 mm, with oven setpoint 270 °C to 300 °C and PIAT 190 °C to 205 °C; heating time is 18 min to 26 min depending on mould mass. After cooling to 55 °C, the hollow shell is filled with two-component closed-cell polyurethane foam at core density 35 kg/m³ to 50 kg/m³; the foam exotherm is kept below 110 °C to prevent localized polyethylene distortion. Terminal products include dredge pipe floats, pontoon sections, fender buoys, cable floats and aquaculture collar floats.
Potable water storage tanks, flanged riser sections and small filter housings require the certifier to evaluate the finished moulding rather than the powder or pellet alone; the moulder must demonstrate compliance with NSF/ANSI 61 for extraction and, in relevant markets, with EU Drinking Water Directive 98/83/EC or AS/NZS 4020:2018 for product contact. The permitted formulation is 100% virgin Icorene 3560 BWO 9273 because certifying bodies generally reject regrind, external mold release agents, and color masterbatches unless they have been tested within the final product matrix. Oven temperature is set at 280 °C to 300 °C, PIAT is held at 200 °C to 205 °C for 4 min to 6 min, and demoulding is performed at 55 °C to reduce post-mould warpage. Sintered vent tubes in blind threaded bosses prevent differential pressure collapse during cooling; after demoulding, vent openings are closed by fusion-welded plugs or moulded plugs rather than adhesives. Mould surfaces used for potable-water parts are cleaned without silicone release agents; internal threads and flanged openings are formed with mechanical inserts or roto-moulded bosses. Terminal products include 100 L to 2000 L potable water storage tanks, dosing tanks, filter housings and sealable manhole liners.
Outdoor playground components such as black tunnel sections, roof caps, slide bed supports and climbing handholds are produced from Icorene 3560 BWO 9273 without a post-painting step, removing volatile organic compound emissions and preventing paint adhesion failure at impact edges. The relevant compliance matrix for this sector includes EN 1176-1:2017 for playground equipment safety, ASTM F1487-21 for public playground equipment performance, and where components are accessible to children below 3 years or classified as toy-like, EN 71-3:2019+A1:2021 for element migration. Procurement specifications frequently add REACH Regulation (EC) No 1907/2006 Annex XVII restrictions for polycyclic aromatic hydrocarbons in extended-contact surfaces. The formulation is kept at 100% as-supplied black powder for load-bearing shells; regrind is held to 10 wt% or less because impact-critical sections require consistent low-temperature ductility. Moulding occurs at oven setpoint 275 °C to 300 °C, PIAT 185 °C to 200 °C, and forced-air cooling to 65 °C before demoulding, with draft angles of 1° to 2° on deep-draw cavities to avoid stress whitening. Terminal products include rotational-moulded slides, tunnels, climbing elements, roof sections and impact-absorbing ground-level panels.
Insulated fish boxes, pharmaceutical shipping containers and temperature-controlled process boxes use a two-pass rotational moulding sequence in which Icorene 3560 BWO 9273 forms the outer black UV-resistant shell and an FDA-compliant inner liner grade forms the product-contact surface. The outer shell is moulded first at 100% as-supplied black powder; the inner liner is then rotomoulded over the outer shell or a pre-foamed core, and closed-cell polyurethane foam is injected between skins at a core density of 35 kg/m³ to 40 kg/m³. Injection pressure is kept below 0.15 MPa, and foam fill must remain below 40 kg/m³ in large flat panels to prevent core exotherm from bowing the outer shell. Food-contact compliance is established on the inner liner through FDA 21 CFR 177.1520 and EU No 10/2011 overall migration testing, while the outer shell is assessed by ASTM D638-14 tensile property retention and ASTM D1693-15 Condition B environmental stress-crack resistance. Oven setpoint for the outer shell is 280 °C to 300 °C with PIAT 190 °C to 200 °C; demoulding is delayed until 50 °C to prevent foam-port plug distortion. Terminal products include insulated fish boxes, temperature-controlled sample boxes, pallet lids and insulated sump covers.
Heavy-duty material handling shells such as distribution pallets, tote bins and machine-guard panels are processed with Icorene 3560 BWO 9273 at 100% as-supplied powder when the part must endure repeated impact, forklift tine abrasion, and outdoor weather exposure. The applicable standard framework includes the ISO 8611 series for pallet stiffness and ultimate load, RoHS Directive 2011/65/EU for embedded metal fittings or electronic tags, and REACH Regulation (EC) No 1907/2006 for substances of very high concern. In this sector, regrind addition is limited to 15 wt% because thicker structural sections above 8 mm are more sensitive to internal void formation when recycled powder has higher bulk-density variability. The mould is heated to 280 °C to 300 °C, PIAT is kept at 190 °C to 205 °C, and cooling is staged with forced air to 80 °C followed by ambient cooling to 55 °C; metal inserts for fork pockets and hinge bosses are thermally preheated to 80 °C before charging to reduce local cold-spot porosity. Terminal products include pallets, tote boxes, machine guards, pump covers and containment trays.
Buried wastewater and stormwater retention structures are rotomoulded with Icorene 3560 BWO 9273 when the black UV-stabilized formulation must survive open-yard storage before installation and then perform under soil loading. The applicable standards include EN 12566-1:2016 for prefabricated septic tanks and ASTM D1998-15 for vertical storage tanks where applicable, with structural verification by ring stiffness or deflection testing to the purchaser’s civil specification. The formulation is 100% as-supplied powder; up to 20 wt% same-grade regrind may be used in non-structural manhole liners after a hydrostatic leak test on the finished part, but primary containment walls remain 100% virgin. Moulding uses an oven setpoint of 280 °C to 300 °C, PIAT 195 °C to 205 °C, and wall thickness from 10 mm to 15 mm; cooling is stopped at 55 °C before removal to rigid jigs that hold circular openings within ±5 mm during final shrinkage. Terminal products include 1000 L to 5000 L septic tanks, pump chambers, valve pits, stormwater manhole liners and retention tank shells.
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LyondellBasell Icorene 3560 BWO 9273 is a linear low density polyethylene powder supplied for rotational molding, dry blending, and selected extrusion applications. The grade designation identifies a polyolefin with a nominal density near 0.935 g/cm³ when determined by ISO 1183-1:2019 and a melt mass-flow rate near 6.0 g/10 min when measured at 190 °C under 2.16 kg load in accordance with ISO 1133-1:2022. The BWO 9273 suffix denotes a black weathering package in which carbon black and hindered amine light stabilizers are dispersed in the polyethylene matrix. The material is directed toward outdoor tanks, agricultural sprayer components, playground structures, industrial containers, and recreational vehicle parts where ultraviolet exposure and moderate chemical resistance require a thermoplastic that balances stiffness with impact behavior. Representative mechanical values for this density class include tensile yield stress from 15 MPa to 17 MPa, elongation at break above 700%, and flexural modulus between 500 MPa and 600 MPa; these values are not lot-specific and should be confirmed against the active LyondellBasell technical data sheet.
In rotational molding, the central process conflict is between adequate melt coalescence and excessive melt sag on vertical walls. At a melt mass-flow rate of 6.0 g/10 min and density 0.935 g/cm³, the material provides a wider densification window than many 0.940–0.942 g/cm³ medium density polyethylene grades in the same melt index band, but peak internal air temperature must still be controlled. Published data for this specific configuration remains limited; however, typical production-scale machines operate at oven setpoints of 280 °C to 320 °C, with peak internal air temperature held between 190 °C and 205 °C. Oven setpoints above 320 °C for cycles longer than 30 min risk thermo-oxidative chain scission, surface yellowing, and pitting. Powder particle size should be checked by dry sieve analysis according to ASTM D1921-18; a granulation with 95% passing 500 µm and a median particle size below 350 µm is commonly required for uniform wall thickness in complex molds.
On independent-arm carousel machines with three or four stations, the powder experiences prolonged preheat and multiple-axis rotation. Lot-to-lot melt index variation greater than ±0.5 g/10 min can shift oven residence time by 2 min to 4 min for a 6 mm nominal wall thickness and alter bubble defect density. The densification phase in LLDPE rotational molding is governed by surface-tension-driven sintering and melt coalescence; at 0.935 g/cm³ the polymer requires sufficient zero-shear viscosity to resist sag while retaining enough flow to eliminate trapped air. In production practice, this grade is pulverized to a powder with 100% passing 600 µm mesh and controlled fines below 150 µm, because excessive fines can create dry-flow segregation and electrostatic adhesion to cooled mold surfaces. The 0.935 g/cm³ density reduces stiffness relative to MDPE but improves ductility and environmental stress-crack resistance as measured by ASTM D1693-21. Process audits on shuttle rotational molding machines with mold clamp forces from 1.5 t to 3.0 t indicate that venting and pressure relief are required when molding enclosed containers with wall thickness less than 4 mm; published data for all mold geometries is limited.
The following representative values are drawn from typical LLDPE rotational molding data in the 0.935 g/cm³ density class. They are not a certificate of analysis and must be checked against the current manufacturer’s datasheet for lot-specific benchmarks.
| Property | Representative value | Test method |
|---|---|---|
| Density | 0.934–0.936 g/cm³ | ISO 1183-1:2019 |
| Melt mass-flow rate | 5.5–6.5 g/10 min | ISO 1133-1:2022 |
| Tensile stress at yield | 15–17 MPa | ISO 527-2:2012 |
| Tensile elongation at break | >700% | ISO 527-2:2012 |
| Flexural modulus | 500–600 MPa | ISO 178:2019 |
| Vicat softening point A50 | 115–120 °C | ISO 306:2022 |
| ESCR, 100% Igepal CO-630, 50 °C, F50 | >1000 h | ASTM D1693-21 |
| Carbon black content | 2.0–2.5% | ISO 6964:2019 |
| Weathering retention after 2000 h xenon-arc exposure | >70% elongation retention | ISO 4892-2:2013 |
In agricultural water tanks and outdoor furniture, the BWO 9273 stabilization system is intended to delay surface cracking and chalk formation. The carbon black absorber screens ultraviolet radiation, while hindered amine light stabilizers interrupt free-radical oxidation in the semicrystalline polymer. Accelerated weathering is evaluated by change in tensile elongation after xenon-arc exposure according to ISO 4892-2 and by carbonyl index development using FTIR spectroscopy. For a nominal 5 mm rotomolded wall section, retention above 70% of initial elongation is the practical acceptance limit for many outdoor specifications. The grade also provides improved low-temperature puncture resistance relative to LDPE; the ductile-to-brittle transition is shifted below -30 °C in instrumented impact testing according to ISO 6603-2.
Embrittlement in unpigmented LLDPE is governed by autocatalytic hydroperoxide decomposition initiated by carbonyl and hydroperoxide chromophores. In a black stabilized compound, carbon black with primary particle size between 20 nm and 50 nm absorbs UV across the 290 nm to 400 nm range and reduces the penetration depth of photo-oxidation to the outermost polymer surface. Hindered amine light stabilizers then suppress free-radical propagation through the Norrish I and II oxidation pathways. The weathering package is not a remedy for oxidative failure at elevated service temperatures; continuous exposure above 80 °C can shorten the induction period despite UV screening. Oxidation induction time can be measured by differential scanning calorimetry according to ISO 11357-6; typical black rotomolding LLDPE grades in this class show an OIT above 30 min at 200 °C in oxygen, but the active datasheet must be consulted for the exact value. In accelerated exposure under ISO 4892-2 with daylight filters at 60 W/m² irradiance and black standard temperature 65 °C, the time to 50% retained elongation for well-dispersed carbon black LLDPE is generally two to four times longer than unpigmented LLDPE of equivalent molecular architecture. Published data for Icorene 3560 BWO 9273 specifically is limited; differentiation should be validated on actual molded part geometry.
The primary conversion route for this grade is rotational molding; injection molding and compounding are possible but are not design-intent uses. When screw plasticizing is used, conventional single-screw extruders with L/D 24:1 to 30:1 and a compression ratio of 3:1 can process the material at melt temperatures from 200 °C to 240 °C. High-shear compounding above 260 °C should be avoided because the stabilizer package can be partially consumed and the carbon black can agglomerate if dispersion conditions are poor. In rotational molding, the processing boundary is defined by the ratio of peak internal air temperature to oven setpoint. A frequent failure is premature demolding at internal mold surface temperatures above 85 °C; this produces warpage and sink marks. Controlled cooling with forced air and water mist is preferred before mold release. For double-walled parts, removal from the mold at 70 °C to 80 °C reduces post-mold distortion.
Compared with a conventional Ziegler-Natta 0.940 g/cm³ MDPE rotomolding grade, Icorene 3560 BWO 9273 provides lower flexural modulus but higher ESCR and low-temperature impact retention. Compared with cross-linked polyethylene, it remains thermoplastic and can be reground and recycled within plant scrap streams; however, the stabilizer package and carbon black make recyclate dark and unsuitable for unpigmented or light-colored layers. Compared with butene-based LLDPE of the same density and melt index, a hexene-based resin can deliver higher dart impact in film, but the distinction is less pronounced in rotomolded wall sections of 3 mm to 6 mm. Published data for the comonomer type in Icorene 3560 BWO 9273 is limited; the purchaser should request comonomer identification from the supplier if chemical compatibility or migration modeling is required.
The powder should be stored in sealed hoppers below 50 °C and protected from direct sunlight; storage at relative humidity above 60% may introduce surface moisture that appears as pinholes or bubbles during the early densification phase. The material is thermoplastically processable, but it should not be blended with amine-based additives or pro-oxidant masterbatches because such additives can reduce oxidation induction time and alter stabilizer response. External mold release agents should be evaluated for compatibility with carbon black surfaces; silicone-containing release agents can reduce paint adhesion if post-molding decoration is required.
Compliance status must be confirmed by the supplier for the destination market and use temperature. The following matrix lists typical standards and regulations applicable to black UV-stabilized LLDPE compounds.
| Reference | Applicability | Verification |
|---|---|---|
| EU No 10/2011 | Plastic food-contact materials; overall migration below 10 mg/dm² requires end-use verification | Supplier declaration of compliance |
| FDA 21 CFR 177.1520 | Olefin polymers for food contact under specified end-use conditions | Supplier food-contact statement |
| REACH SVHC | Candidate list substances below 0.1% per article under Article 33 | SDS Section 15 |
| RoHS Directive 2011/65/EU | Restricted heavy metals: Pb <1000 mg/kg, Cd <100 mg/kg, CrVI <1000 mg/kg | Producer declaration |
| ASTM D3350 | Polyethylene classification cell class with weathering suffix | UL yellow card or certification |
| ISO 11469 | Recycling marking code >PE-LLD< | Lot inspection |
For continuous chemical immersion service, specific compatibility testing is required because environmental stress-crack resistance values determined by ASTM D1693-21 do not automatically predict performance in aggressive agricultural adjuvants or hydrocarbon contact. The lower density of Icorene 3560 BWO 9273 relative to MDPE provides improved crack resistance, but it also reduces load-bearing stiffness; designers should compensate by increasing wall section or adding external reinforcement when static loads exceed 25 kPa on unsupported surfaces.