| HS Code | 692261 |
| Material Type | Polyethylene, Linear Low Density (LLDPE) |
| Density | 0.935 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 4.5 g/10 min |
| Color | Grey |
| Uv Stabilization | Yes |
| Form | Pellets |
| Processing Method | Rotational Molding |
| Tensile Strength At Yield | 17 MPa |
| Tensile Strength At Break | 20 MPa |
| Elongation At Break | 800% |
| Flexural Modulus | 600 MPa |
| Impact Strength Notched Izod | No Break |
| Hardness Shore D | 55 |
| Vicat Softening Temperature | 113 °C |
| Melting Point | 125 °C |
| Environmental Stress Crack Resistance | >1000 h |
As an accredited LyondellBasell Icorene 3545 UV+ GRY 7141 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 3545 UV+ GRY 7141 Linear Low Density Polyethylene is typically supplied in 25 kg polyethylene-lined bags, palletized and shrink-wrapped. |
| Container Loading (20′ FCL) | 20′ FCL loading for LyondellBasell Icorene 3545 UV+ GRY 7141 Linear Low Density Polyethylene: palletized 25 kg bags, shrink-wrapped and secured. |
| Shipping | Shipping description: Polyethylene, Linear Low Density, non-hazardous solid; not regulated under DOT/IMDG/IATA. Icorene 3545 UV+ GRY 7141 is supplied as gray UV-stabilized LLDPE pellets in moisture-barrier bags or octabins. Store dry, away from heat/ignition; secure loads. No UN number, hazard class, or packing group required. |
| Storage | Store LyondellBasell Icorene 3545 UV+ GRY 7141 Polyethylene, Linear Low Density, in a cool, dry, well-ventilated warehouse. Keep bags or containers tightly closed, palletized, and off the floor. Protect from direct sunlight, heat, moisture, dust, and contamination. Avoid ignition sources and strong oxidizers. Follow first-in, first-out stock rotation; maintain ambient temperatures, avoid excessive stacking, and ensure packaging remains intact. |
| Shelf Life | Shelf life is 24 months from delivery when stored unopened in original packaging, cool, dry, and away from direct sunlight. |
Rotationally moulded vertical chemical storage tanks produced from Icorene 3545 UV+ GRY 7141 are processed on multi-arm biaxial machines with a major-to-minor rotation ratio of 4:1 for cylindrical shells. Shell sections are typically specified at 6.0–9.0 mm for capacities between 5,000 L and 10,000 L, while bottom knuckles and flange faces are thickened to 25–40% above the nominal shell dimension to accommodate concentrated hoop stress and sealing loads. Oven temperatures are set at 280–300 °C. The peak internal air temperature is held between 190 °C and 195 °C for full densification of the LLDPE powder. Readings below 185 °C leave residual pinholes at the inner wall, and excursions above 200 °C accelerate oxidative chain scission at the outer surface. Cooling is staged: forced air to 80 °C, water mist to 45 °C, then ambient air to demoulding below 70 °C. Cooling rates above 30 °C/min across the 70–100 °C recrystallisation interval generate flange warpage that prevents sealing on the finished vessel. Pre-drying of the powder at 60 °C for 2–4 h is required if storage relative humidity exceeds 60% because surface moisture contributes to microvoid formation at the inner wall.
Regulatory control for above-ground chemical storage is anchored to ASTM D1998-21 for upright polyethylene tanks. Chemical resistance is verified under ISO 175:2010 using immersion in 20% sulphuric acid at 23 °C for 7 days. The grey 7141 pre-compounded colourant is not altered at the machine. Additional dry colour or liquid masterbatch above 1.5 wt% is not permitted because low-molecular carriers can reduce environmental stress crack resistance and introduce dispersion defects above 40 μm. The grade is not recommended for continuous immersion in strong oxidising media above 40 °C, such as 30% hydrogen peroxide or concentrated nitric acid. Published data for this specific grey-pigmented configuration under those aggressive media is limited; qualification testing is required before service. End products include secondary containment bunds, dosing skid sumps, and cylindrical static storage vessels.
| Control item | Method | Acceptance reference |
|---|---|---|
| Density | ISO 1183-1:2019 | 0.934–0.936 g/cm³ |
| Melt flow rate | ISO 1133-1:2022, 190 °C/2.16 kg | 3.5–4.5 g/10 min |
| Environmental stress crack resistance | ASTM D1693-15, condition B | F50 > 1,000 h |
| Tensile elongation at break | ISO 527-2:2012, type 5A | > 800% |
| Flexural modulus | ISO 178:2019, method A | 650–750 MPa |
| Weathering | ISO 4892-3:2024, UVA-340 | Delta E < 4.0 after 3,500 h |
In agricultural water retention and fertigation batch tank applications, rotationally moulded components are produced with wall thicknesses between 4.0 mm and 8.0 mm. For a 2,000 L horizontal transport tank, the mould is charged at a shot weight of 9.0–11.0 kg and processed at an oven set point of 285 °C. Oven dwell is 20–28 min, and the peak internal air temperature is held at 190 °C for 10–12 min after powder coalescence. The grey 7141 surface is left unpainted to avoid film delamination in constant sunlight and fertiliser contact. The UV+ package combined with grey pigmentation keeps the black panel surface temperature under ISO 4892-3:2024 exposure typically lower than an unpigmented black LLDPE reference by 10–15 °C. This temperature offset reduces thermal expansion cycling on long flat side walls and threaded fittings.
Compliance for agricultural water storage is limited to chemical registration under EU REACH and polymer marking under ISO 11469. These grey tanks are not certified for potable water contact. If a drinking-water claim is required, the finished part must be tested under NSF/ANSI/CAN 61 and EU Regulation (EU) No 10/2011, and published data for this specific grey-pigmented configuration is limited. End products include fertiliser batch tanks, sprayer rinse tanks, fire suppression water buffers, and irrigation header reservoirs.
Long-term immersion data for grey-pigmented LLDPE floats indicate that the limiting service condition is not water absorption but combined ultraviolet and oxygen attack at the outer skin. Double-skin floats produced from Icorene 3545 UV+ GRY 7141 are moulded with outer walls of 3.0–5.0 mm and internal cavities capable of receiving closed-cell polyethylene foam of 30–40 kg/m³ density. Cylindrical floats use a 4:1 biaxial rotation ratio; rectangular mooring buoys use 2:1. Oven set point is 285 °C, and the peak internal air temperature is held at 192 °C for 15–20 min after complete powder coalescence. If wall thickness falls below 2.5 mm, gas bubbles escape through the thin skin and leave pinholes at the inner radius. If the peak internal air temperature exceeds 200 °C, the hindered amine light stabiliser package is consumed faster, and surface chalking can appear after 24 months in tropical sea-surface exposure.
Weathering acceptance for marine service is based on ISO 4892-3:2024 using UVA-340 lamps; tensile elongation retention after 3,500 h should be at least 70%. Water absorption is evaluated under ISO 62:2008, method 1, with 24 h immersion at 23 °C; LLDPE grades of this type show values below 0.01%. Saltwater compatibility is additionally screened in substitute seawater per ASTM D1141-98(2021) at 40 °C for 1,000 h. End products include marina gangway floats, aquaculture cage collars, navigation buoys, and modular pontoon shells.
Outdoor furniture components and playground roofing elements are rotationally moulded from Icorene 3545 UV+ GRY 7141 in 3.0–5.0 mm wall sections. The mould surface texture is replicated directly on the part, and the in-mould grey 7141 colour removes the need for post-mould solvent-borne painting. That substitution eliminates a volatile organic compound source and retains a uniform UV-stabilised skin across all surfaces. Shot weights for bench seats and table tops are typically 2.0–4.0 kg/m² of projected area. Oven temperature is set at 285 °C. The peak internal air temperature is held at 190 °C for 12–15 min after powder coalescence. Moulding cycles are longer than those for thin-wall containers because the flat panel geometry exhibits differential shrinkage; released parts are cooled slowly through 70–100 °C to prevent bowing.
Heavy metal migration on playground-contact surfaces is verified under EN 71-3:2019. Structural safety of fixed playground equipment is assessed under EN 1176-1:2017. Weathering retention is measured under ISO 4892-3:2024; surface appearance after 3,000 h is expected to show Delta E below 4.0 with no chalking. End products include public benches, picnic table tops, playground roof panels, bus shelter louvers, and screened enclosure panels.
For off-road equipment reservoirs with capacities from 20 L to 150 L, wall thickness is specified at 5.0–7.0 mm. Brass or stainless steel inserts are preheated to 190 °C and positioned in the mould before the LLDPE powder is charged. Shot weight is controlled at 3.5–5.0 kg/m² of projected area. The mould is rotated at 4:1 for cylindrical reservoirs and 2:1 for irregular flat tank shells. The peak internal air temperature is held between 190 °C and 195 °C for 10–15 min after all powder has densified. Corner wall thickness variation is kept within ±10% of the nominal shell because local thinning at sharp bosses creates stress concentration during dynamic pressure pulses. Internal corner radii are specified at a minimum of 5.0 mm to avoid crack initiation at the transition between the shell and an integrally moulded sump.
Diesel resistance is evaluated under ISO 1817:2015 using reference fuel at 70 °C for 70 h; volume swell is typically below 3% and tensile retention above 80%. Finished reservoirs are leak-tested at 0.3 bar air pressure under water for 5 min. Hydraulic oil compatibility is screened with mineral hydraulic oil per ISO 11158 HM type. End products include diesel fuel tanks for compact loaders, hydraulic oil reservoirs for aerial work platforms, and engine day tanks for generator sets.
Municipal waste enclosures and bulk handling trays are rotomoulded from Icorene 3545 UV+ GRY 7141 in 4.0–10.0 mm walls, with under-rib sections thickened to 6.0–8.0 mm to resist wheel axle loads and drop impact. Large wheeled bins are produced on 2.0 m swing biaxial machines with a 4:1 rotation ratio. Oven set point is 290 °C, and the peak internal air temperature is held at 190 °C for 10–12 min after powder coalescence. Cooling is carried out with forced air for 35–45 min because thick-wall sections and deep ribs release residual heat slowly. Demoulding below 70 °C prevents rib distortion on the hot part.
Mobile waste containers are evaluated under EN 840-1:2020 for dimensions and EN 840-5:2020 for durability under simulated handling. Low-temperature impact resistance is assessed by drop testing conditioned containers at -20 °C; published data for this specific grey-pigmented configuration is limited and requires part-level validation. The grey 7141 colour is suitable for general waste and recycling bodies but does not replace colour-coded lids used in municipal source-separation systems. End products include 120–1,100 L wheeled bins, recycling banks, bulk agricultural trays, and heavy-duty material handling containers.
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LyondellBasell Icorene 3545 UV+ GRY 7141 Polyethylene, Linear Low Density, is a rotational molding grade supplied as a precompounded gray powder. The product identity carries specification information: Icorene designates the manufacturer’s polyethylene resin line, 3545 identifies the grade within the series, UV+ indicates an enhanced ultraviolet stabilization package, and GRY 7141 is the controlled gray color code. The resin class is linear low-density polyethylene under ASTM D883 terminology and falls within the designatory principles for polyethylene molding materials described in ISO 1872-1. The product is intended for hollow parts produced by biaxial rotational molding in which the powder is sintered against the internal wall of a heated mold. Because the gray pigment and the stabilizer package are incorporated during resin production, the material removes the need for separate masterbatch addition at the machine but imposes stricter incoming inspection for color consistency, powder cleanliness, and dry flow behavior. Incoming resin is commonly checked for melt flow rate under ASTM D1238 or ISO 1133 at 190 °C and 2.16 kg, density under ASTM D1505 or ISO 1183, and powder characteristics that influence mold filling. A natural-powder process recipe should not be transferred to this precompounded gray grade without verifying the heating and cooling response because the pigment changes the thermal absorptivity of the powder bed.
The UV+ designation indicates that the material contains a weathering protection package, not that the product has unlimited service life in every outdoor condition. In polyethylene, solar radiation in the 290 nm to 400 nm band initiates photo-oxidative chain scission unless the polymer is protected by a combination of UV absorber, hindered amine light stabilizer, and pigment screening. Accelerated weathering is usually evaluated under ASTM D2565 or ISO 4892-2, with color change, gloss loss, and mechanical retention tracked against an unexposed control. Gray pigment can screen UV near the exposed surface, but the protection is thickness-dependent and can be reduced at thin corners, sharp edges, and undercured regions. Published data for this specific configuration is limited in open literature, so outdoor qualification should be performed on production-thickness rotomolded panels exposed at the same orientation and geographic climate as the intended part.
The difference is concentrated in process control. For natural rotomolding powder, the molder must meter a separate color masterbatch into the powder stream, and this addition can show variation when hopper bridging, screw feeder pulsation, or static segregation occurs. For Icorene 3545 UV+ GRY 7141, the pigment and UV stabilizer are already dispersed in the polymer matrix; therefore, the molder’s mixing step is eliminated, but the supply chain must protect the material from cross-contamination with natural or differently colored powders. A single contaminated batch can generate streaked parts, localized color deviation, and ultraviolet failure in the unpigmented zones. The gray pigment also modifies the way the powder bed absorbs infrared energy in the oven. In some tooling, the precompounded gray product may require a shorter or longer oven dwell time than a natural LLDPE of similar melt flow rate, because surface temperature and heat transfer through the powder bed depend on color. The correct control is not the oven setpoint alone but the internal air temperature history and the measured wall thickness at selected locations. When switching from a natural grade to this product, molders should log PIAT, oven residence time, cooling time, and part weight; a production trial should evaluate cure at the inner wall rather than relying on exterior surface appearance.
In production-scale equipment, the powder is distributed within a closed mold mounted on a multi-axis arm. For large cylindrical tanks, an arm ratio near 4:1 is often used, but the optimum depends on mold geometry and swing diameter. The mold rotates inside an oven in which the air temperature is commonly controlled between 260 °C and 320 °C for LLDPE rotational molding. The material closest to the mold melts first and forms a skin; additional powder continues to deposit and sinter until the wall reaches the target thickness. The temperature of the internal air rises more slowly than the mold surface temperature, and the time at which the powder no longer rattles against the mold is a practical indication that the bulk of the material has consolidated. If the oven is removed too early, the part displays a powdery inner surface, low drop impact strength, and a tendency to crack at the mold parting line. If the oven is held too long, the stabilizer package can be consumed, the outer surface may oxidize, and the part can become brittle. These failure signatures are not always visible optically; impact testing on cut sections or complete parts is required to confirm the cure state.
The datasheet values for a rotomolding resin are generally measured on compression-molded specimens under controlled cooling, not on the final rotomolded wall. Tensile properties are determined under ASTM D638 or ISO 527-2, flexural modulus under ASTM D790 or ISO 178, and density under ASTM D1505 or ISO 1183. These values allow resin comparison but do not substitute for testing on the production part. A rotomolded wall cools slowly from one side, develops a different crystalline morphology through the thickness, and contains residual stresses from mold removal. A part may therefore show lower stiffness than expected from the datasheet or higher impact strength in ductile regions. For low-temperature transport and outdoor storage applications, impact testing under ASTM D5276 or ISO 11173 is commonly performed at -18 °C or -40 °C. The gray grade is intended for applications in which a precompounded dark color and UV stabilization are required for multiyear outdoor use without post-mold painting.
Compared with high-density polyethylene rotational molding grades, the linear low-density material of Icorene 3545 UV+ GRY 7141 generally exhibits lower flexural modulus and higher resistance to environmental stress cracking in many aqueous detergent and cleaning-agent environments. This does not imply compatibility with all chemicals: oxidizing acids, halogens, and certain organic solvents can attack polyethylene, and the chemical resistance of the rotomolded part must be tested under ASTM D543 or ISO 175 for the specific fluid, concentration, and service temperature. Compared with unmodified butene-LLDPE rotomolding powder, the UV-stabilized gray product offers an integrated additive package that can reduce the number of raw-material handling steps and improve lot-to-lot appearance, but it is not a universal drop-in replacement because the pigmentation changes infrared heating behavior and the stabilizer package imposes storage and processing boundaries.
For rotomolded outdoor tanks, the grade is most often selected for applications such as agricultural chemical storage, water tanks, industrial hoppers, and outdoor equipment enclosures. The gray color is commonly chosen for its ability to mask surface soiling and to provide uniform appearance over large surfaces, but color uniformity depends on wall thickness and mold surface finish. When the final part is intended for food contact or potable water, the molder must verify extraction and migration performance on the rotomolded article; a resin compliance statement alone does not cover the effects of mold release agents, post-mold machining, or assembly inserts. For parts subject to continuous internal pressure or static head, creep and long-term hydrostatic strength should be evaluated under the appropriate pipeline or tank standards and not inferred from short-term tensile data.
Warpage becomes a process risk when the part is removed from the mold before the core has developed sufficient dimensional stability. A tank wall with nominal thickness above 6 mm can retain heat at the inner surface while the outer surface cools rapidly; if the part is demolded too early or cooled unevenly, the open face can distort and bolt-hole spacing can shift. The preferred cycle uses forced air after the part separates from the mold surface, followed by a controlled water mist only if dimensional data support the need. An aggressive quench can increase molded-in stress and reduce impact performance, particularly at low temperatures. Part design should distribute wall thickness as uniformly as possible because sharp transitions in thickness produce differential shrinkage and local residual stress. In flat-walled panels, stiffening ribs and corner radii should be sized so that powder can flow into the feature without bridging; ribs that are too deep or too narrow can trap air and create unfilled sections.
The presence of a UV stabilizer package does not eliminate the need for proper storage of the powder before molding. The powder should be kept in sealed original packaging away from direct sunlight and strong artificial UV sources, because prolonged exposure of the powder itself can consume a portion of the protective chemistry before the part is formed. The material is not hygroscopic in the manner of polyamide, but condensation on cold powder or tooling can vaporize during heating and produce surface microvoids; therefore, cold packaging should be allowed to reach ambient temperature before opening. The powder should not be blended with unapproved additives because acidic residues, certain halogenated compounds, and incompatible stabilizer chemistries can antagonize hindered amine light stabilizers and reduce outdoor performance. If a mold release or maintenance chemical is changed, a trial should include melt flow stability, surface appearance, and accelerated weathering of the molded part against the previous release system.
| Standard / Code | Parameter or Scope | Relevance |
|---|---|---|
| ASTM D883 | Plastics terminology | Defines linear low-density polyethylene classification and general terms. |
| ASTM D1238 / ISO 1133 | Melt flow rate at 190 °C and 2.16 kg | Used for incoming lot consistency; not a single direct rotomolding process parameter. |
| ASTM D1505 / ISO 1183 | Density | Confirms resin density class and detects gross batch deviation from specification. |
| ASTM D638 / ISO 527-2 | Tensile yield strength and elongation at break | Provides standardized mechanical data on prepared specimens. |
| ASTM D790 / ISO 178 | Flexural modulus | Indicates stiffness; values depend on specimen thickness and strain rate. |
| ASTM D2565 / ISO 4892-2 | Accelerated weathering exposure | Ranks weathering performance; requires outdoor correlation for service-life prediction. |
| ASTM D1693 / ISO 16770 | Environmental stress crack resistance | Measures slow crack growth under constant strain; specimen preparation affects rank order. |
| ASTM D543 / ISO 175 | Chemical resistance | Determines compatibility with specific chemical agents, concentration, and temperature. |
| FDA 21 CFR 177.1520 / EU 10/2011 | Food-contact regulatory status | Final compliance must be confirmed on the finished article under the applicable migration conditions. |
| REACH / RoHS re-cast | Chemical registration and restricted substances | Applicability depends on article type and regional regulatory obligations. |