Lyondellbasell Icorene 3560 G Bwn 8412 Polyethylene Linear Low Density

LyondellBasell Icorene 3560 G BWN 8412 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3560 G BWN 8412 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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    VTB
    Specifications
    HS Code 712855
    Density 0.935 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 3.5 g/10 min
    Tensile Strength At Yield 14.5 MPa
    Tensile Strength At Break 20.0 MPa
    Elongation At Break 700%
    Flexural Modulus 480 MPa
    Vicat Softening Temperature 103 °C
    Brittleness Temperature -70 °C
    Shore D Hardness 50
    Melting Point 125 °C
    Thermal Expansion Coefficient 1.5E-4 1/°C
    Water Absorption <0.01%

    As an accredited LyondellBasell Icorene 3560 G BWN 8412 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 G BWN 8412 Linear Low Density Polyethylene is packaged in 25 kg bags, palletized and shrink-wrapped.
    Container Loading (20′ FCL) 20′ FCL container fully loaded with LyondellBasell Icorene 3560 G BWN 8412 linear low-density polyethylene bags, palletized/secured for ocean export.
    Shipping Non-hazardous LLDPE resin, not regulated for transport by DOT, IMDG, IATA, or ADR. Ship in original sealed bags, boxes, or octabins. Keep dry, cool, and away from direct sunlight and ignition sources. Provide SDS to carrier and follow local, national, and international regulations.
    Storage Store in a cool, dry, well-ventilated warehouse. Keep in tightly closed original bags/packaging, away from direct sunlight, heat, ignition sources, and moisture. Protect from dust, oils, and other contaminants. Maintain ambient temperature; avoid excessive stacking and pressure. Use FIFO stock rotation. Handle pallets carefully to prevent bag damage. Do not store outdoors or near oxidizers. Ensure clean, dry conditions.
    Shelf Life Store in cool, dry conditions; shelf life typically 24 months from manufacture in unopened original packaging, away from direct sunlight.
    Application of LyondellBasell Icorene 3560 G BWN 8412 Polyethylene, Linear Low Density

    Rotational moulding of chemical storage tanks from LyondellBasell Icorene 3560 G BWN 8412 begins with control of powder particle size and internal air temperature rather than a fixed oven dwell time. The nominal melt-flow rate is often found in the range of 3.5 g/10 min at 190 °C/2.16 kg under ISO 1133-1:2022, but the controlling process input is the ground powder distribution. After pulverizing, no more than 10 wt% is retained on a 500 µm sieve, and the fraction passing 106 µm is controlled at the mill because coarse particles remain as poorly fused inclusions in the inner wall while excessive fines migrate to the outer skin and produce microcracking at the bottom knuckle radius. In production on carousel machines with a 4:1 primary-to-secondary axis ratio, the oven set point is maintained between 280 °C and 300 °C, and the mould’s internal air temperature is driven to a peak of 190 °C to 205 °C. The lower bound is set by incomplete bubble dissolution in 3.0–4.5 mm sidewalls, while the upper bound is set by oxidative yellowing in thin corners and by volatile accumulation when regrind is present. A compatible polyethylene-based antioxidant or antioxidant-UV stabilizer masterbatch is dry-blended at 1.5–2.5 wt%; higher loadings reduce powder tack at the mould surface and extend gel time beyond the available heating window, resulting in pinholes at the parting line. If ambient relative humidity exceeds 60% and cold powder shows surface condensation, pre-drying at 50–60 °C for 2 h is applied as a boundary condition, not as a routine requirement. Mould release contamination is controlled because silicone-based external release agents can transfer to the powder and reduce melt adhesion at the inner fusion layer, producing delamination in the finished tank. Moulded 200 L vertical cylindrical tanks are checked for wall thickness distribution at the bottom knuckle radius, which is normally specified at 6.0–7.5 mm compared with 3.0–4.5 mm on the straight sidewall. Environmental stress-cracking resistance is tested under ASTM D1693 in 10% Igepal CO-630 at 50 °C, with failure before 500 h treated as a lot-rejection criterion, and low-temperature drop performance is assessed after conditioning at -20 °C using the tank manufacturer’s internal hydraulic or impact protocol. For European static chemical storage service, EN 13575 establishes design verification through a hydraulic pressure test at 1.1 times rated capacity and requires that the resin-chemical resistance list covers the stored substance. Terminal parts include 200 L dosing tanks, containment bunds, and acid-alkali vessels for agricultural and light industrial installations.

    What Limits Peak Internal Air Temperature in Thin-Wall Agricultural Feed Troughs?

    For thin-wall agricultural water tanks and feed troughs moulded from the same grade, the critical process variable is not oven temperature but the time at which the inner wall reaches a peak internal air temperature sufficient to sinter the final layer without overheating the outer skin. Wall sections are frequently specified at 2.5–3.5 mm, which causes the mould inner surface to reach PIAT 15–30 s earlier than a thicker chemical tank under identical oven conditions. When a feed trough is moulded with an oval sidewall, the bottom radius can lag the straight panels long enough to create microvoid clustering at the transition line; the standard corrective action is to lower the oven set point by 10–20 °C and extend the rotation time rather than increase air velocity. For outdoor service, a dry blend of 1.5–2.0 wt% UV-stabilized polyethylene masterbatch is used, and where carbon black is required for long-term UV resistance, a 40% carbon black masterbatch is incorporated at 1.5 wt% to yield a net pigment loading near 0.6 wt%. Accelerated weathering is evaluated under ISO 4892-2 with a UVA-340 lamp cycle, and the commonly accepted acceptance boundary is a colour change no greater than 2.0 ΔE after 2000 h, though published data for this specific grade in thin-wall agricultural parts is limited and lot-specific verification is recommended. Food-contact status for feed and water troughs is drawn from FDA 21 CFR 177.1520(c) and, for the European market, EU 10/2011 overall migration limits of 10 mg/dm² under Simulant D2 and Simulant A conditions, with the caveat that any dry-blended colorant or UV package must independently meet the same compliance boundary. Terminal products include 300 L oval water troughs, mineral feeders, and farrowing pen partitions.

    Double-Walled Diesel Tanks Demand Kiss-Off Placement Before Cooling

    Double-walled fuel tanks and diesel day tanks moulded from Icorene 3560 G BWN 8412 introduce a structural requirement that is absent in single-skin tanks: the internal kiss-off columns must be fully fused to the inner wall before forced cooling begins, because the outer wall freezes first and pulls the inner wall away from the tool, leaving a cold-weld defect at the core. In this geometry, the useful oven period is shortened by the thermal mass of two skins and the air gap between them, so peak internal air temperature is typically held at the upper end of the 190–205 °C range and is monitored by a thermocouple inside the air cavity, not on the outer mould surface. The kiss-off fusion depth is specified as 40–50% of the combined wall thickness at the base, and the tool is designed with vent tubes of 4–6 mm internal diameter at the parting line to equalize pressure; blocked vents are a documented cause of blowholes at the upper corners of 350 L tanks. Compliance for static thermoplastic fuel storage is anchored to EN 13341, which requires leakage testing, drop testing at low temperature, and storage-lifetime verification for heating oils, kerosene, and diesel fuels. For urea solution or AdBlue service, material compatibility is assessed against ISO 22241-3, and the tank’s resin surface must not promote hydrolysis or extractable contamination above the limits specified for SCR systems. Published lot-specific data for double-walled fuel tank configurations is limited, so the moulder’s internal pressure test and parting-line inspection protocol remains mandatory. The final product range includes 350 L diesel day tanks, 1000 L static storage vessels, and double-wall containment tanks for light commercial refuelling skids.

    Material Handling Bins, Fish Totes, and Insulated Transport Boxes

    In double-wall insulated transport boxes and fish totes, the same linear low-density polyethylene grade is processed against a steel or cast aluminium mould with internal parting-line seals, and the mould is charged with sufficient powder to build two skins separated by a closed air layer or by a rigid foam core inserted after the first skin is formed. For fish totes intended for wet food contact, compliance is required under FDA 21 CFR 177.1520(c) and EU 10/2011, and because the inner wall is not machined after moulding, surface roughness and extractable residues are controlled by using clean reclaim streams and by limiting regrind to 20 wt%. The resin is generally processed at an oven set point 15–25 °C lower than that used for chemical tanks because foam-filled or double-wall moulds have a longer thermal lag and can develop hot spots at the junction of inner and outer walls. Part cooling is staged: forced air is applied first to solidify the outer skin, followed by internal air circulation through the vent openings to prevent sink marks on the load floor. Where a rigid polyurethane foam core is inserted, the foam exotherm must remain below 90 °C at the polyethylene interface to avoid local softening and dimensional distortion. Terminal products include 600–1000 L fish totes, insulated seafood boxes, and material handling bins for meat or dairy processing, where the part must retain dimensional stability after repeated hot-water washdown at 60–80 °C.

    Playground and outdoor leisure components are moulded from the same powder when the specification prioritizes low-temperature ductility and ultraviolet resistance over chemical compatibility. On shuttle machines with a 4:1 or 8:1 rotational ratio, the oven cycle is extended by 10–15 min compared with thin-wall feed troughs because the parts commonly include enclosed hollow profiles, slide runouts, and mounting bosses with varying wall stock from 4 mm to 12 mm. A dry-blended UV package at 1.0–2.0 wt% is standard, and impact performance is verified by an instrumented puncture test under ISO 6603-2 at -20 °C, with the failure mode required to be ductile rather than shattering. Compliance for installed play equipment in the European market is evaluated against the mechanical and entrapment criteria of EN 1176, while raw material chemical safety is confirmed through REACH Annex XVII restrictions and the supplier’s food-contact or toy-contact statements where applicable. The terminal article range includes rotational-moulded activity panels, tunnel sections, kayak hulls for recreational use, and outdoor seating shells; published grade-specific data for kayak hull fatigue under repeated flexural loading is limited, so part-level validation remains with the moulder’s own cyclic load protocol.

    When In-Plant Regrind Exceeds 30 wt% in Non-Food Mouldings

    Non-food mouldings such as waste bins, cable covers, and industrial floor plates can accept in-plant regrind of the same grade, but the blend crosses a property cliff-edge when regrind exceeds 30 wt%. At 15–30 wt% regrind, the primary losses are measured as a reduction in ASTM D1693 environmental stress-cracking resistance and an increase in microporosity at the inner fusion layer, while low-temperature ductility under ISO 6603-2 remains acceptable for most industrial parts. Above 30 wt%, the fraction of particles that have been through one or more additional grinding cycles becomes significant; these particles have lower bulk density and a larger specific surface area, and they sinter earlier in the oven cycle, trapping air and creating pinhole clustering at the lowest point of the mould. The corrective processing change is not a simple temperature reduction, because virgin powder still requires the full upper PIAT for complete bubble dissolution; instead, the blend is sieved to 35 mesh and remixed in a low-shear paddle blender for 20 min to minimize segregation, and the rotomoulder may reduce the regrind level to 20 wt% in parts with wall thickness below 4 mm. Compliance for waste bins and cable covers is typically limited to internal impact and UV requirements rather than food or fuel standards; however, the moulder must still ensure that a mixed-color regrind stream does not violate RoHS substance restrictions when the product enters electrical or electronic equipment housings. Final products include 240 L wheeled waste bins, outdoor cable joint pits, and anti-slip industrial floor plates.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3560 G BWN 8412 is a linear low-density polyethylene rotational molding powder in which the Icorene designation identifies the manufacturer’s rotational molding product family, the 3560 G alphanumeric string denotes the base resin generation and melt-flow target, and the BWN 8412 suffix specifies a black weathering-stabilized additive and color package. The grade is specified for single-layer and multilayer hollow components requiring a controlled balance of stiffness, notched impact strength, and outdoor ultraviolet stabilization. It is supplied as a free-flowing powder rather than pellets, because the powder form allows the material to sinter directly against the heated mold wall without extrusion or grinding before charging. Typical production applications include agricultural chemical sprayer tanks, marine fenders, automotive wheel arches, insulated fish boxes, pedal boats, and material-handling bins. The powder is dry-charged into cast aluminum, fabricated steel, or CNC-machined steel molds on biaxial, shuttle, carousel, and rock-and-roll rotational molding machines. Because the base polymer is a thermoplastic linear low-density polyethylene rather than a crosslinkable high-density polyethylene, the material remains reprocessable after service; regrind from trimmed openings, pinch-off flash, and rejected parts can be reintroduced into the shot weight if the recyclate fraction and particle size distribution are controlled. Published data for this specific configuration is limited; release values should be confirmed against the current certificate of analysis and the manufacturer’s current technical bulletin.

    Specification Profile and Lot-Release Testing

    Commercial control of Icorene 3560 G BWN 8412 is based on rheological, density, mechanical, thermal, and environmental stress-cracking resistance determinations. Melt flow rate is measured according to ISO 1133-1:2022 at 190°C/2.16 kg; values for this class of rotational molding powder are typically controlled in the 3.0–4.0 g/10 min band, although the certificate of analysis governs each lot. Density is determined by ISO 1183-1:2019 and normally falls between 0.933 g/cm³ and 0.937 g/cm³. Tensile yield strength and elongation at break are measured according to ISO 527-2:2012; flexural modulus according to ISO 178:2019; Charpy notched impact at 23°C and −20°C according to ISO 179-1:2020; Vicat softening temperature A50 according to ISO 306:2022; and environmental stress-cracking resistance according to ASTM D1693-15, Condition B. For black weathering grades, accelerated ultraviolet exposure is often evaluated through ISO 4892-3:2016, Method A, with retained elongation after exposure serving as the primary acceptance criterion. The powder is further characterized by dry flow, bulk density, and particle size distribution; these are not cosmetic parameters but determine whether the powder will sinter uniformly into undercuts, ribs, and narrow kiss-off features. A powder with a mean particle size between 250 μm and 500 μm and a controlled fines fraction below 10% is generally required to maintain homogeneous wall thickness; a drop in loose bulk density below 0.330 g/cm³ may indicate moisture pickup or particle agglomeration and should trigger sieve analysis before production release. Published data for this specific configuration is limited.

    Property Test method Class-typical window or behavior
    Melt flow rate ISO 1133-1:2022 3.0–4.0 g/10 min at 190°C/2.16 kg; CoA governs
    Density ISO 1183-1:2019 0.933–0.937 g/cm³
    Tensile yield strength ISO 527-2:2012 14–18 MPa
    Elongation at break ISO 527-2:2012 >350%
    Flexural modulus ISO 178:2019 450–600 MPa
    Charpy notched impact, 23°C ISO 179-1:2020 >30 kJ/m²
    Charpy notched impact, −20°C ISO 179-1:2020 >10 kJ/m²
    Vicat softening temperature A50 ISO 306:2022 108–116°C
    ESCR, F50 ASTM D1693-15 >1000 h
    Accelerated UV retention ISO 4892-3:2016 >2000 h to 50% retained elongation for black 8412 package

    When Peak Internal Air Temperature Overshoot Exceeds the Degradation Threshold

    On carriage-type shuttle machines with fabricated steel molds heated by forced convection, the powder layer initially fuses when the internal air temperature reaches approximately 150–170°C. Densification continues between 180°C and 210°C; at this stage the molded wall must remain under positive internal air pressure until the melt has flowed into the corners of the cavity. If a black 8412 powder is substituted for a natural rotational molding powder without lowering the oven set point, the mold wall absorbs radiant heat more rapidly, and an unchanged oven cycle can push the peak internal air temperature beyond 230°C. At that upper boundary, the black polyethylene surface can exhibit microvoid formation, gloss loss, and additive bloom, particularly in wall sections thicker than 8 mm. A biaxial rotation ratio of 4:1 is common for simple rectangular molds; however, undercuts and deep draw features require fixed angular offsets and a lower minor-axis speed to prevent powder pooling in concave ribs. On a multi-arm carousel with an open-flame oven, the effective heating rate for black powder can be several degrees per minute higher than for natural powder at the same oven temperature; therefore, oven set points should be revalidated after any color change. Wall-thickness-dependent cycle recipes are normally established by mold trials, not by melt-flow alone. The cooling phase is equally process-sensitive: black parts retain heat longer than natural parts, so the demolding temperature should be kept below 70°C for flatness-critical parts. Directed cooling air should be applied across the thickest wall region, and the mold should not be opened while the part is above 85°C if warpage control is critical. Batch-to-batch variance in particle size distribution can occur when powder is transported from a cold warehouse to a warm molding shop; condensation on bag walls can increase wall adhesion and reduce dry flow. The powder should be conditioned at the molding shop temperature for 24–48 hours before charging.

    What Distinguishes This Grade From Butene-Comonomer and High-Density Rotational Molding Polyethylenes?

    Compared with a low-density polyethylene, the linear low-density backbone provides a higher tensile yield and improved environmental stress-cracking resistance at equal wall thickness because the short-chain branches disrupt large crystalline lamellae less than long-chain branching. When compared with a 0.942–0.950 g/cm³ high-density polyethylene rotational molding grade, Icorene 3560 G BWN 8412 has lower flexural modulus and lower heat-distortion resistance but higher notched impact strength and better low-temperature impact retention. This trade-off is significant in crosslinkable high-density polyethylene grades: those materials provide higher upper-use temperature and chemical resistance but require a post-mold cure and cannot be reprocessed as virginlike recyclate. The Icorene grade remains thermoplastic and can be reground directly on the shop floor. Compared with an octene-comonomer linear low-density polyethylene at equal density and melt index, a butene-comonomer grade may show a lower balance of dart impact and environmental stress-cracking resistance; the 3560 G designation does not independently identify comonomer type, so the current datasheet should be consulted for comonomer and molecular architecture. Compared with a metallocene-catalyzed linear low-density polyethylene rotational molding grade of similar density, a conventional Ziegler-Natta grade may have broader comonomer distribution and lower dart impact; the catalyst type for 3560 G is not identified in this document and should be confirmed before selecting the grade for impact-critical parts. The BWN 8412 suffix differentiates this grade from natural or non-weathering black rotational molding powders; if the article is not exposed outdoors, this additive package may be unnecessary, and a non-stabilized grade may be used to reduce cost and eliminate a potential source of UV stabilizer migration under long-term liquid contact.

    Property or attribute Icorene 3560 G class LLDPE HDPE rotational molding Crosslinkable HDPE
    Density, ISO 1183-1:2019 0.933–0.937 g/cm³ 0.942–0.950 g/cm³ 0.940–0.950 g/cm³
    Melt flow, ISO 1133-1:2022 3.0–4.0 g/10 min 5–8 g/10 min typical Not applicable after cure
    Flexural modulus, ISO 178:2019 450–600 MPa 800–1200 MPa 700–1000 MPa
    Low-temperature impact, ISO 179-1:2020 High Moderate High after cure
    Reprocessability Yes, thermoplastic Yes, thermoplastic No, thermoset after crosslink
    Weathering option Black 8412 UV package Natural or UV package Varies

    The BWN 8412 Designation Is Not a Separate Base Resin

    The BWN suffix should not be interpreted as a separate polymer or a melt-flow grade. It is a manufacturer-specific color and stabilization system applied to the base powder. The alphanumeric sequence 8412 is the manufacturer-specific formulation and packaging code; it is not a density or melt-flow specification. The carbon black loading in such grades is typically controlled in the 1.5–2.5% by weight range, because sufficient carbon black dispersion is required to meet weathering criteria but excessive carbon black can reduce notched impact strength and increase melt viscosity at the sintering surface. Procurement should require the full designation rather than only Icorene 3560 G, because the black stabilization package changes heat absorption, cooling rate, and surface appearance relative to the natural base resin. The infrared heat absorption of black powder is higher; black powder reaches the sintering wall temperature more quickly in the radiative portion of oven heating but cools more slowly in the cooling chamber. In multilayer rotational molding, black 8412 powder may be used as the outer weather-exposed skin with a natural or foamed core; interfacial adhesion must be verified through peel or shear testing because the skin layer may reach its flow plateau earlier than the core.

    Before a molded tank or fender is specified for continuous contact with agricultural chemicals, the complete article should be subjected to immersion testing of the actual molded wall under the intended chemical concentration, temperature, and service stress. Chemical tank applications require evaluation of the base polyethylene under 21 CFR 177.1520 only if the specific additives and pigments are also cleared; the black weathering package may not be suitable for direct food contact unless the full formulation is covered by a current Food and Drug Administration food-contact notification or equivalent positive list. For outdoor tanks and marine parts, oxidative induction time by ISO 11357-6:2018 may be specified on the finished part; black 8412 packages should show an oxidative induction time above 20 min at 200°C on the finished part, but published data for this specific configuration is limited. If bags are left open at relative humidity above 60%, moisture regain can occur, and drying at 80°C for 2–4 hours should be considered before processing. The material should not be stored in direct sunlight for prolonged periods before processing because the stabilizer package can be consumed prematurely, leaving less antioxidant reserve for the intended service life.

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