Lyondellbasell Icorene 3560 Bue 5113 Polyethylene Linear Low Density

LyondellBasell Icorene 3560 BUE 5113 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3560 BUE 5113 Polyethylene, Linear Low Density
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 616305
    Density 0.935 g/cm3
    Melt Flow Rate 6.0 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 10.3 MPa
    Tensile Strength At Break 14.5 MPa
    Elongation At Break 700%
    Flexural Modulus 250 MPa
    Hardness Shore D 50
    Vicat Softening Point 95°C
    Melting Point 125°C
    Deflection Temperature At 0 46 Mpa 70°C
    Brittleness Temperature < -70°C
    Thermal Conductivity 0.33 W/m·K
    Coefficient Of Linear Thermal Expansion 1.5E-4 1/°C
    Volume Resistivity > 1.0E+15 ohm·cm
    Dielectric Constant 2.3
    Dissipation Factor 0.0002
    Water Absorption < 0.01%
    Oxygen Index 17%

    As an accredited LyondellBasell Icorene 3560 BUE 5113 Polyethylene, Linear Low Density factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell Icorene 3560 BUE 5113 Linear Low Density Polyethylene is supplied in 25 kg polyethylene bags, palletized and stretch-wrapped.
    Container Loading (20′ FCL) 20′ FCL: palletized 25 kg bags of LyondellBasell Icorene 3560 BUE 5113 LLDPE, stretch-wrapped, secured, net weight about 20–22 MT.
    Shipping LyondellBasell Icorene 3560 BUE 5113 Polyethylene, Linear Low Density is shipped as a non-hazardous solid resin in 25 kg bags, octabins, or bulk containers. It is not DOT/IMDG/IATA regulated. Store in a cool, dry area away from ignition sources and moisture. Handle using normal industrial hygiene.
    Storage Store in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, sparks, and open flames. Keep original packaging closed and pallets off the floor to prevent moisture and contamination. Avoid contact with strong oxidizers. Maintain moderate temperatures, use first-in-first-out stock rotation, protect from UV light, static discharge, and physical damage, and follow the manufacturer’s SDS and local regulations.
    Shelf Life Shelf life: two years when stored in original, unopened packaging in a cool, dry, well-ventilated area away from direct sunlight.
    Application of LyondellBasell Icorene 3560 BUE 5113 Polyethylene, Linear Low Density

    LyondellBasell Icorene 3560 BUE 5113 is a linear low-density polyethylene rotational molding powder supplied with a UV stabilization package and carbon black dispersion. The resin is characterized under ISO 1133-1:2022 at 190 °C with a 2.16 kg load. The powder is not hygroscopic, but pre-drying is required if condensation has formed during storage above 60% relative humidity. Processing should begin with an olefin-compatible mold release agent. Regrind addition above 25 wt% typically widens the melt-flow distribution and reduces low-temperature impact strength. The following application scenarios are governed by specific failure modes, regulatory limits, and production-scale process controls rather than generic rotomolding practice.

    Agricultural sprayer tanks for dilute herbicides, foliar nutrients, and aqueous adjuvants require continuous hoop stress resistance over service lives exceeding 10,000 h. Rotationally molded LLDPE tanks of 800 L to 15,000 L are produced with nominal wall thickness from 6 mm to 10 mm. The grade is compounded with carbon black at 2.0 wt% to 2.5 wt% to maintain UV protection across multiple outdoor seasons. ASTM D1998-21 governs upright polyethylene tank dimensions, wall thickness tolerance, fitting bosses, and hydrostatic test requirements. Environmental stress crack resistance is tested under ASTM D1693-15 Condition B in 10% Igepal CO-630 solution at 50 °C. Failure below 500 h at a boss fusion line indicates excessive residual cooling stress. The rotomolding cycle is controlled to a peak internal air temperature of 190 °C to 205 °C, followed by forced-air cooling at no more than 8 °C/min through the 120 °C to 80 °C crystallization window. Molded-in inserts must be preheated to within 10 °C of the mold wall temperature before charging to avoid localized shrinkage. The LLDPE matrix resists aqueous solutions of weak acids, alkalis, and many surfactant-loaded spray adjuvants. Prolonged contact with aromatic hydrocarbons, chlorinated solvents, or concentrated oxidizing acids causes swelling, stress cracking, or oxidative attack. High-load applications should be qualified by immersion testing under ISO 175:2010 at the intended chemical concentration and service temperature.

    What Limits Low-Temperature Impact in Rotationally Molded Diesel Tanks?

    At -40 °C, the low-temperature impact response of rotationally molded diesel tanks shifts from ductile to brittle if the inner wall has been thermally oxidized during overcooking. Fuel tanks for off-road generator enclosures, agricultural tractors, and compact construction equipment are molded with wall thicknesses between 12 mm and 25 mm. The qualifying test is low-temperature falling-dart impact according to ASTM D3029-19 at -40 °C. LLDPE retains ductile failure at this temperature only when the peak internal air temperature does not exceed 205 °C. Overcooking at 220 °C accelerates oxidation at the inner wall and can shift the ductile-to-brittle transition upward by 5 °C to 10 °C. The mold surface temperature is held at 270 °C to 300 °C in the oven, with total cycle time from 25 min to 40 min for 20 mm walls. Diesel immersion testing is performed under ASTM D543-21 at 23 °C and 60 °C for 1,000 h. Volume swell below 3% is generally accepted for this tank class. Biodiesel blends above B20 introduce methyl ester fractions that increase permeation and may soften the inner surface; validation with the actual commercial fuel blend is required. Fill neck, vent, and outlet bosses create weld lines where impact cracks initiate after repeated thermal cycling. The boss insert should be within 10 °C of the mold wall temperature before powder charging. ASTM D1998-21 is referenced for tank dimensions, fitting performance, and hydrostatic integrity. The carbon black in Icorene 3560 BUE 5113 protects the exterior only when the dispersion remains uniform through grinding and regrind blending.

    Marine buoy shells require diffusion-limited wall thickness design.

    Because marine buoy shells are loaded hydrostatically from the outside and ballasted internally, the primary structural concern is not water absorption but buckling under nonuniform wall distribution. Navigation and mooring buoy shells are filled with closed-cell polyurethane foam, sand, or concrete ballast. Water absorption of rotationally molded LLDPE measured by ASTM D570-22 remains below 0.01% after 24 h immersion. A nominal wall thickness of 8 mm to 15 mm is common for buoys up to 3 m diameter. For walls below 5 mm, ovalization under wave impact becomes thickness-dependent. Wall nonuniformity above 15% leads to buoy tilt after ballast fill. Impact at -20 °C in northern waters is qualified using ASTM D3029-19. The black LLDPE containing 2.0 wt% carbon black resists UV embrittlement, but biofouling removal with high-pressure water above 500 bar can cause surface roughening and local stress whitening. The rotomolding cycle uses a peak internal air temperature of 195 °C to 210 °C. The lower set point reduces oxidation, while the upper set point improves particle coalescence around internal foam attachment features. Polyethylene has poor adhesion to polyurethane foam; mechanical anchors or rotationally molded ribs are required instead of adhesive bonding. Published data for Icorene 3560 BUE 5113 in deep-water buoy configurations with foam-filled annulus sections is limited; pre-production trials on the target mold are required to confirm void content and wall uniformity.

    Bulk handling bins for dry food ingredients are rotationally molded from LLDPE when impact resistance and cleanability outweigh the higher stiffness of HDPE. Capacities range from 200 L to 1,000 L. The resin must comply with FDA 21 CFR 177.1520(c) for food-contact olefin polymers. In the EU, overall migration into 10% ethanol and 3% acetic acid simulants must be below 10 mg/dm² under EU Regulation 10/2011. The carbon black package used in Icorene 3560 BUE 5113 must be verified against national food-contact positive lists. Interior surfaces require a polished mold cavity with controlled release agent transfer. Cleaning is performed with alkaline detergents at 60 °C to 80 °C; steam cleaning above 100 °C is not recommended because local softening and panel distortion occur. Wall thickness is designed from 5 mm to 8 mm, with sidewall ribs to reduce bulging. Full-volume drop tests at 0 °C are used to qualify the containers. Brittle failure at rib transitions indicates excessive cooling rate through the crystallization window. LLDPE has low odor carryover, but strongly flavored dry ingredients may require a flush cycle with sodium bicarbonate solution before first use.

    When Powder Particle Size Distribution Controls Thin-Wall Chemical Liner Integrity

    Thin-wall liners of 3 mm to 5 mm are inserted into steel or composite pressure vessels for corrosive liquid storage. Rotational molding powder for thin walls requires a narrow particle size distribution. A fraction above 600 µm may not fully fuse at a 3 mm wall, producing pinholes at the mold surface. A fraction below 75 µm creates dust that follows airflow and deposits unevenly in corners. The Icorene 3560 BUE 5113 powder should be sieved on a 35-mesh screen before charging; retained fraction should be less than 1 wt%. The oven temperature is set to 260 °C to 280 °C, and the peak internal air temperature is held at 190 °C to 200 °C to minimize thermal degradation of thin sections. Mold rotation speed ratio is adjusted to vessel geometry; long cylindrical molds require higher minor-axis speed to prevent end-wall thinning. The liner is qualified by spark testing at 10 kV to 15 kV on the inner surface to detect pinholes. Chemical exposure is tested under ISO 175:2010 for 28 days at the intended concentration. LLDPE liners are suitable for acid concentrations below 30% and alkali concentrations below 50% at room temperature. Strong oxidizing acids, aromatic solvents, and chlorinated hydrocarbons remain outside the service envelope.

    Wall thicknessOven set temperaturePeak internal air temperatureForced-air cooling rate through 120 °C to 80 °CTypical cycle time
    3 mm to 4 mm260 °C to 280 °C190 °C to 195 °C8 °C/min to 12 °C/min8 min to 14 min
    5 mm to 9 mm280 °C to 300 °C195 °C to 205 °C6 °C/min to 8 °C/min14 min to 22 min
    10 mm to 19 mm290 °C to 310 °C200 °C to 207 °C4 °C/min to 6 °C/min22 min to 35 min
    20 mm and above300 °C to 320 °C205 °C to 210 °C2 °C/min to 4 °C/min30 min to 45 min

    Outdoor Playground Equipment and the UV Colorant Interaction

    Rotomolded LLDPE panels, sliding surfaces, and climber shells for playground equipment are designed to meet ASTM F1487-21 impact, entrapment, and protrusion criteria. The black UV-stabilized grade provides baseline weathering resistance. When custom colorants are added at 1 wt% to 4 wt%, organic pigments can absorb UV energy and destabilize the hindered amine stabilizer package. The result is accelerated surface oxidation, chalking, and microcracking before the expected service life of a black part is reached. Colorant systems must be tested under ASTM D2565-22 xenon-arc weathering for 2,000 h, with a delta b value below 3.0 and no surface crazing. Wall thickness ranges from 5 mm to 8 mm. The mold must include generous radii at all transitions; a radius below 6 mm can concentrate impact stress and produce a brittle crack under cold impact. Rotational molding temperatures are kept at the lower bound of 280 °C to avoid color shift. The final part is checked for heavy-metal release under RoHS 2011/65/EU and REACH Annex XVII where applicable. The exterior surface should not be flame-treated; corona treatment is not required for this non-bonding application.

    Spill containment pallets and sump decks for 200 L drums are rotationally molded with high corner thickness to resist fork tine impact. A typical design uses a 10 mm wall at the base and 6 mm at sidewalls. The LLDPE grade meets the chemical resistance demands of accidental spill exposure to common industrial liquids, but compatibility must be verified for each chemical. The pallet is tested under EPA 40 CFR 264.175 for secondary containment capacity, not for chemical compatibility. LLDPE is suitable for short-term contact with many oils, glycols, and weak acids. Long-term pooled exposure to strong solvents leads to swelling and distortion. The molded pallet is cooled in air to minimize warpage. A warp limit of 3 mm per 600 mm length is checked with a flatness fixture. The surface is slip-resistant by mold texture, not by additive. Regrind up to 25 wt% is used in the sump base only, not in the sidewalls, because the inner base has lower impact exposure.

    Multi-layer rotational molding of chemical tank walls introduces interfacial cooling gradients.

    Large chemical storage tanks above 10,000 L may be molded in two or three layers to combine foamed LLDPE cores with solid skins. The outer and inner skin layers use Icorene 3560 BUE 5113 for UV resistance and environmental stress crack resistance. The core layer uses a foamed LLDPE or recycled polyolefin to reduce weight. Interfacial cooling gradients arise because the outer skin cools first against the mold, while the inner skin solidifies last. A cooling rate mismatch of more than 5 °C/min between adjacent layers produces interlayer shear stress and delamination at the foam-to-skin interface. The oven cycle is staged: first charge the outer skin powder, then the foam core at 190 °C to 200 °C internal air temperature, then the inner skin. Peak internal air temperature must not exceed 200 °C in the foam layer to avoid cell collapse. The mold is cooled with forced air at 10 °C to 20 °C for the first 10 min, then mist cooling. Tanks are inspected ultrasonically in the wall thickness range 10 mm to 20 mm for voids. The finished shell is tested under ASTM D1998-21. Chemical resistance of the inner skin is validated under ISO 175:2010. Published data for Icorene 3560 BUE 5113 in multi-layer foam-core tank configurations is limited; pre-production qualification on the production mold is required to establish interlayer adhesion and void-free fusion.

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    Certification & Compliance
    More Introduction
    LyondellBasell Icorene 3560 BUE 5113 is supplied as a powder-form linear low density polyethylene for rotational molding. The grade is identified in trade literature as a butene-comonomer material with a density of approximately 0.934–0.936 g/cm³ under ISO 1183-1:2019 and a melt flow rate in the 5–6 g/10 min range at 190°C/2.16 kg under ISO 1133-1:2022. The 5113 designation is understood from LyondellBasell product literature as a weather-resistant stabilizer formulation; the exact additive composition is proprietary and must be confirmed with the supplier’s product safety datasheet. This density position places the resin at the high-density end of the LLDPE range, giving higher flexural modulus than 0.918 g/cm³ film grades while retaining the stress-crack resistance associated with short-chain branching. Lot-specific property values are to be taken from the certificate of analysis. In rotational molding, the powder is ground to a nominal 35 mesh (500 µm) particle size. Particle size distribution controls dry flow, mold fill, and air removal. A broad distribution with a fines fraction below 10% through 140 mesh is generally preferred; excess fines can increase static charge and reduce bulk density, while oversized particles can create pinholes at the inner surface. The powder is charged into a sheet-metal or cast-aluminum mold, and the mold rotates biaxially at a speed ratio commonly between 3:1 and 4:1. Published data for this specific grade’s bulk density is limited; standard LLDPE rotomolding powders in this density and melt index range typically exhibit bulk densities of 0.33–0.38 g/cm³, but the certificate of analysis should be consulted.

    What separates a stabilized butene-LLDPE rotomolding powder from high-pressure LDPE and unimodal HDPE?

    The molecular architecture of Icorene 3560 BUE 5113 consists of a linear ethylene backbone with short-chain branching introduced by butene comonomer. Unlike high-pressure LDPE, which contains long-chain branching, this grade has no significant long-chain branching. The result is a narrower shear-thinning response and a different melt-phase sag behavior during rotational molding. At equal density, butene LLDPE exhibits higher tensile yield and elongation than high-pressure LDPE, and the environmental stress crack resistance under ASTM D1693-15 is typically more than an order of magnitude higher than unimodal HDPE rotomolding resins. Compared with HDPE of density 0.945 g/cm³, the lower density of this grade reduces flexural modulus but improves impact and low-temperature behavior. The integrated UV stabilization package further differentiates it from general-purpose LLDPE rotomolding powders, which require post-blending with UV masterbatch and may show inconsistent additive dispersion. Process stability on single-arm shuttle machines and fixed-arm carousel machines requires control of oven airflow, mold rotation ratio, and peak internal air temperature. The recommended oven temperature for this grade family is commonly 260–290°C, but the controlling variable is the internal air temperature measured at the mold centerline. A peak internal air temperature of 190–215°C is typically sufficient to complete densification. Exceeding 230°C increases the risk of oxidative degradation, visible yellowing, and loss of antioxidant efficacy. During cooling, forced air to 100°C followed by water mist to 60–70°C is used to limit warpage. The mold should not be opened above 80°C for large flat parts because the partially crystalline matrix has insufficient thermal dimensional stability at that stage.

    Mechanical property validation under ISO 527-2 and ASTM D1693-15 protocols

    Typical mechanical values for this grade family are determined on compression-molded plaques or rotomolded specimens. Tensile yield is generally measured in the range 17–19 MPa with elongation at yield of 10–15%; tensile elongation at break commonly exceeds 800% under ISO 527-2:2012 at 50 mm/min. Flexural modulus is usually 550–700 MPa under ISO 178:2019. The notched Izod impact at 23°C may be reported as non-break, while at -40°C the failure mode transitions to ductile or brittle depending on cooling rate and plaque thickness. The environmental stress crack resistance under ASTM D1693-15 condition B in 100% Igepal CO-630 at 50°C is typically reported above 1000 h, which is substantially higher than many unimodal HDPE grades; however, ESCR is strongly influenced by density, cooling rate, and residual stresses.
    Representative property envelope for Icorene 3560 BUE 5113
    PropertyTest methodTypical range or value
    DensityISO 1183-1:20190.934–0.936 g/cm³
    Melt flow rateISO 1133-1:20225–6 g/10 min
    Tensile yield stressISO 527-2:201217–19 MPa
    Elongation at breakISO 527-2:2012>800%
    Flexural modulusISO 178:2019550–700 MPa
    Vicat softening temperature A/50ISO 306:2022116–122°C
    Melting peak, DSC, 10 K/minISO 11357-3:2018124–128°C
    ESCR, 100% Igepal, 50°CASTM D1693-15>1000 h
    Brittleness temperatureASTM D746-20<-70°C
    Outdoor service life in rotomolded tanks and playground components depends on the stabilizer package of the 5113 lot. Accelerated weathering by ISO 4892-2:2013 can show a decrease in elongation at break after 3000–5000 h of Xenon arc exposure, but published data for this specific grade and thickness configuration is limited. The stabilizer system is intended for long-term UV protection in natural color or pigmented parts; carbon black or titanium dioxide pigmentation at 1–2 wt% further reduces photodegradation. Painted or metallized surfaces, however, may create interfacial adhesion issues because the nonpolar surface energy of LLDPE is below 35 mN/m. Food-contact compliance is generally claimed for uncolored Icorene 3560 BUE 5113 under FDA 21 CFR 177.1520 and EU Regulation No 10/2011, subject to migration limits and end-use temperature conditions. The resin is expected to comply with REACH and RoHS for heavy metals, but converters must verify specific additive and colorant contributions. The material is not recommended for continuous immersion in aromatic hydrocarbons, strong oxidizing acids, or chlorinated solvents at elevated temperatures because these environments can induce swelling, environmental stress cracking, or surface whitening. Aqueous inorganic solutions, dilute acids, and many alcohols are generally compatible at ambient temperature.

    When narrow oven temperature control must be maintained on biaxial rotational molding machines

    Because the density of this grade lies near 0.935 g/cm³, the melting curve is sharper than a 0.918 g/cm³ LLDPE and the sintering interval is compressed. On a shuttle machine with dual ovens, the peak internal air temperature should reach 200–210°C and remain within that band for at least 2–4 min to allow complete bubble removal; a peak internal air temperature below 180°C can leave unconsolidated powder at the mold inner surface, while a peak internal air temperature above 230°C can produce oxidation-induced embrittlement. The thermal history also sets the cooling rate: slow cooling at 5–10°C/min increases crystallinity and flexural modulus but raises shrinkage, while rapid cooling at 15–25°C/min improves impact strength but can induce warpage. Post-mold annealing at 80–90°C for 30–60 min is used on thick sections to reduce residual stress, but published data for this specific grade under annealing is limited.
    Rotational molding process envelope
    Processing parameterSetpoint or bandFailure mode outside range
    Oven air temperature260–290°CSurface oxidation, yellowing
    Peak internal air temperature200–210°CPinholes, incomplete fusion
    Time at peak internal air temperature2–4 minResidual bubbles, oxidative embrittlement
    Demolding temperature<80°CWarpage, dimensional instability
    Cooling rate10–20°C/minImpact/stiffness imbalance
    Mold rotation ratio3:1–4:1Wall thickness variation
    Shrinkage in rotomolded parts made from this grade is generally anisotropic: values of 1.5–2.0% in the mold-plane direction and 2.0–2.5% through the thickness are common after slow cooling. This should be accounted for in tool design, particularly for flat surfaces and ribs. Sharp transitions and corners with inner radii less than 3 mm can produce localized thin-out because powder bridging occurs more readily in high-density LLDPE with a narrow melt window. The use of mold release agents such as zinc stearate can alter surface gloss and interlayer adhesion; silicone-based agents should be validated because silicone migration can interfere with painting or adhesive bonding. For multi-layer rotational molding, Icorene 3560 BUE 5113 can be used as a structural layer beneath a solid pigmented outer layer or with a foamed core. The interfacial fusion temperature must be matched: the second layer should be introduced when the first layer’s internal air temperature reaches at least 150–160°C to ensure cohesive bonding. If the first layer is allowed to cool below 100°C, interlayer adhesion weakens because the surface crystallizes and cannot interdiffuse with the next melt. Co-extrusion is not applicable here; the material is powder-form and requires rotational molding or selective sintering-like powder processes. The polymerization mechanism for this grade is understood to be conventional multi-site rather than metallocene catalysis. This gives a broader molecular weight distribution and a higher melt strength than metallocene LLDPE at similar melt index, which aids in powder fusion and prevents excessive melt flow on vertical walls. However, metallocene grades may provide higher dart impact and clarity. The butene comonomer reduces the melting point compared with ethylene homopolymer, but because butene has lower α-olefin chain length than hexene or octene, tie-molecule concentrations at equivalent density are lower; for severe low-temperature impact applications, hexene or octene LLDPE may be preferred. Differential scanning calorimetry at 10 K/min typically shows a melting peak at 124–128°C and a crystallization peak at 108–112°C. The heat of fusion of 140–160 J/g is lower than HDPE and corresponds to a crystallinity of roughly 50–55%. Thermogravimetric analysis in nitrogen often shows onset of decomposition above 400°C, but oxidative induction time at 200°C under oxygen is more relevant for rotational molding; stabilizer depletion before processing can reduce oxidative induction time below 20 min, increasing gel and pinhole formation. Published data for this specific grade’s oxidative induction time is limited. Batch-to-batch control during production-scale runs should include melt flow rate, density, and powder particle size distribution on each incoming lot. Rotomolding converters commonly reject lots with a melt flow rate deviation greater than ±0.5 g/10 min from the target because flow-to-thickness and bubble removal shift measurably. The pellet form is not standard for this product; if compounded, the powder morphology is lost and the material is no longer suitable for rotational molding without regrinding to the original particle size specification.
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