Lyondellbasell Icorene 3560 Bue 5744 Polyethylene Linear Low Density

LyondellBasell Icorene 3560 BUE 5744 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3560 BUE 5744 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 515515
    Density 0.935 g/cm³
    Melt Flow Rate 0.90 g/10 min
    Tensile Strength At Yield 10.0 MPa
    Tensile Strength At Break 24.0 MPa
    Elongation At Break 800 %
    Tensile Modulus 0.300 GPa
    Flexural Modulus 0.400 GPa
    Izod Impact Strength Notched 0.500 J/cm
    Dart Drop Impact 200 g
    Elmendorf Tear Strength Md 300 g
    Elmendorf Tear Strength Td 500 g
    Vicat Softening Point 100 °C
    Melting Point 125 °C
    Haze 10 %
    Gloss 70 %

    As an accredited LyondellBasell Icorene 3560 BUE 5744 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 Supplied in 25 kg polyethylene-lined paper bags, 40 bags per 1,000 kg pallet; also available in 1,000 kg bulk bags.
    Container Loading (20′ FCL) 20′ FCL container loaded with LyondellBasell Icorene 3560 BUE 5744 Linear Low Density Polyethylene, secured on pallets for ocean transport.
    Shipping LyondellBasell Icorene 3560 BUE 5744 Polyethylene, Linear Low Density is a solid LLDPE resin shipped as pellets in 25-kg bags, octabins, or bulk containers. It is not classified as dangerous goods. Store cool and dry, away from ignition sources; protect from moisture, contamination, and UV exposure. Handle carefully.
    Storage Store in a cool, dry, well-ventilated warehouse in original, closed packaging. Keep off the floor, away from direct sunlight, heat, moisture, and ignition sources. Avoid strong oxidizers, contamination, and dust generation. Stack pallets securely to prevent deformation. Reseal partially used bags, ensure adequate ventilation and temperature control, and follow the SDS and local regulations.
    Shelf Life Typically 24 months when stored in original unopened packaging in a cool, dry, well-ventilated area; stable under normal conditions.
    Application of LyondellBasell Icorene 3560 BUE 5744 Polyethylene, Linear Low Density

    In the rotomoulding sector for agricultural pesticide and liquid fertilizer storage, Icorene 3560 BUE 5744 is charged as a UV-stabilized black LLDPE powder into closed steel or cast aluminium moulds, often on three-arm carousel machines with oven dwell times of 35–55 min for a nominal wall thickness of 8–12 mm. Compliance for static thermoplastic chemical storage tanks falls under EN 13575:2012, which requires hydrostatic pressure testing and environmental stress crack resistance evaluation after chemical immersion; where the finished vessel is fitted inside a steel cage and marked under ADR 2023 for dangerous goods, the intermediate bulk container must additionally meet UN 31A or UN 31B structural testing. The resin addition ratio for the mould charge is 100 parts Icorene 3560 BUE 5744, with clean in-house regrind from the same grade limited to 15 wt% in order to maintain a particle-size distribution within 150–425 µm and to avoid reducing the notched constant tensile load ESCR performance of the finished wall evaluated per ASTM D5397-20. Processing parameters are set around a biaxial rotation ratio of 4:1 on the primary arm and 1:1 on the secondary arm, an oven temperature of 260–280 °C, and a peak internal air temperature of 190–200 °C; forced-air cooling at 10–15 °C/min is used to control warpage in tank walls, but cooling rates above 18 °C/min have been associated with residual stress around rotationally moulded-in threaded bosses and subsequent stress cracking after 6–12 months of chemical exposure. Powder stored at relative humidity above 60% requires pre-drying at 70–80 °C for 2–4 h in a forced-air hopper dryer to prevent steam pinholes at the inner wall. Terminal products in this segment include 250 L to 10,000 L vertical tanks for liquid fertilizer and pesticide formulations, 1,000 L composite IBC liners marked under UN 31A, and 300 L to 1,500 L saddle-mounted orchard sprayer reservoirs.

    What Changes When Potable Water Contact Certification Is Required for Rotomoulded Storage Tanks?

    When the same linear low density polyethylene powder is specified for potable water storage, the certification burden shifts from chemical compatibility to finished-article extraction and surface cleanliness, and this alters both tooling and process discipline. The applicable standards are NSF/ANSI/CAN 61:2023 for North American municipal and residential water system components, AS/NZS 4020:2018 for Australian and New Zealand installations, and Regulation (EU) No 10/2011 with its associated migration testing for European Union food-contact materials, which is frequently cited in specifications for potable water tanks when no harmonised EU drinking water standard applies. The formulation addition ratio is restricted to 100 parts virgin Icorene 3560 BUE 5744; post-consumer regrind is excluded, and even same-grade regrind is held to 10 wt% maximum only when a documented lot-traceability programme demonstrates that no non-compliant scrap has entered the closed loop. On shuttle-type rotomoulding machines, the process uses polished stainless steel internal mould surfaces or electroless nickel plating, a peak internal air temperature of 195–205 °C, and a slow forced-air cooling ramp of 8–12 °C/min; no external mould release agents are applied to sealing surfaces because silicone or fatty acid release films can contribute water-extractable organic carbon and cause NSF/ANSI/CAN 61 tasting panel failure. The terminal product types are 500 L to 5,000 L above-ground rainwater harvesting tanks, 1,000 L emergency potable water pods for disaster response, and 2,000 L mobile water buffering tanks for vineyard and orchard irrigation distribution.

    Rotational moulders operating four-arm indexing machines in the food service supply chain use double-wall Icorene 3560 BUE 5744 shells to produce insulated transport boxes that carry temperature-sensitive fish, dairy, and meat products. Food-contact compliance is governed by FDA 21 CFR 177.1520 for olefin polymers and by Regulation (EU) No 10/2011 with specific migration limits, but the finished double-wall article also requires surface roughness control below 2.5 µm Ra on the inner cavity as verified by ISO 4287:1997 to prevent biofilm formation. The mould charge is 100 parts virgin powder for both inner and outer shells; after the two shells are demoulded, a rigid polyurethane foam core is injected between the walls at a density of 45–60 kg/m³, with foam density verified by ISO 845:2007 and adhesion achieved by mechanical anchoring rather than chemical bonding. The downstream production process rotomoulds the inner and outer shells separately on carousel machines, then assembles the double-wall cavity with internal spacers, and injects the polyurethane system at a metering pressure of 120–180 bar followed by a post-cure of 50–60 °C for 24 h; published data for foam-to-polyethylene adhesion under cyclic thermal shock for this specific BUE 5744 configuration is limited. Finished articles in this segment include 350 L to 1,000 L insulated fish tubs, 20 L to 80 L dairy sample transport boxes, and 600 L pharmaceutical cold-chain containers with a nominal shell wall thickness of 5–8 mm.

    When Single-Wall Secondary Containment Basins Are Molded as Polyethylene Structures

    In hazardous waste and oil storage operations, single-wall spill containment pallets and basins fabricated from UV-stabilized LLDPE powder are placed under regulatory obligations in the United States under EPA 40 CFR 264.175 for hazardous waste containment and under EPA 40 CFR 112.7(c) for oil pollution prevention; the structure must retain 110% of the volume of the largest container or 100% of the volume of the largest tank, whichever is larger. The mould charge is 100 parts Icorene 3560 BUE 5744 with 10–20 wt% clean in-house regrind permitted only in non-sump floor areas with a minimum wall thickness of 10 mm; the sump floor and forklift-bearing ribs are kept at 100% virgin material to avoid crack propagation from contaminated regrind particles. Plant observations show that regrind particles below 150 µm increase static charge and pinholing in rib roots, so screen classification is maintained before dry blending. Production uses heavy-plate fabricated steel moulds with removable rib inserts on a carousel rotomoulding machine, with a primary axis rotation of 8 rpm and secondary axis rotation of 2 rpm, oven temperature of 270–290 °C, peak internal air temperature of 195–205 °C, and a demoulding time delayed until the part surface reaches 60–70 °C to prevent rib deformation. Terminal products include two-drum and four-drum spill pallets with load ratings up to 1,200 kg, 600 L IBC containment basins, and modular chemical storage flooring tiles with interlocking ribs.

    UV Stabilized Powder in Playground Equipment Molds Without Post-Mold Painting

    Playground structures exposed to 8–12 years of solar radiation use the BUE 5744 black UV-stabilized variant because the carbon black dispersion and UV stabilization package are already incorporated into the polymer matrix, eliminating the need for post-mould painting or secondary UV coating. The applicable compliance standards are EN 1176-1:2017 for playground equipment safety in the European Union and ASTM F1487-21 for public playground equipment in the United States; entrapment, impact attenuation, and material durability test requirements are defined in those standards rather than by resin datasheet heat aging alone. The formulation addition ratio is 100 parts Icorene 3560 BUE 5744 powder; no separate UV masterbatch is added, and regrind from black UV-stabilized parts is limited to 20 wt% with a sieve retention of 100% passing 500 µm and 90% retained at 150 µm to maintain consistent particle flow through the mould charging port. The downstream process uses multi-cavity fabricated steel or cast aluminium moulds mounted on fixed-arm biaxial rotomoulding machines; peak internal air temperature is controlled at 190–200 °C, and a slow cooling stage at 5–8 °C/min is used for large slide shells with wall thicknesses of 10–14 mm to minimize sink marks on visible surfaces. Terminal product types include enclosed spiral slide tubes, tunnel climbers, step decks, and freestanding climbing boulders with a wall thickness of 8–15 mm and a documented UV exposure service envelope under ISO 4892-2:2013 and ASTM G154-21; exact test hours depend on wall thickness and are defined by the manufacturer’s certificate of analysis.

    For solar charge controller and remote telemetry enclosures that remain outdoors without painting or secondary sealing, Icorene 3560 BUE 5744 black LLDPE powder is charged into steel fabricated moulds. The relevant compliance standards are IEC 60529:2013 for ingress protection ratings up to IP66 on the enclosures, NEMA 250:2018 for Type 4X weatherproof service, and UL 94 HB flammability; this grade is not suitable where a V-0 rating is required. The polymer layer is charged at 100 parts of the grade; if regrind is used, it is held to 15 wt% and only from the same black UV-stabilized parts to avoid carbon black content drift and weld-line porosity around moulded-in stainless steel hinge inserts. Powder stored above 60% relative humidity is pre-dried at 70–80 °C for 2 h to avoid pinholes at moulded-in insert interfaces. Reported failures in outdoor enclosures often result from water ingress at moulded-in inserts when the cooling rate is accelerated beyond 12 °C/min; a post-mould thermal anneal at 80 °C for 30 min is used, but published data for this specific configuration is limited. The downstream process uses rotomoulding of steel fabricated moulds with moulded-in threaded brass or 316 stainless steel inserts, a peak internal air temperature of 190–200 °C, and a cooling rate of 10–12 °C/min; post-mould CNC trimming is used for gasket channels and display windows. Completed product types include 500 mm × 400 mm × 200 mm solar battery enclosures, 800 mm × 600 mm × 300 mm telemetry cabinets, and 300 mm diameter dome covers for water utility valve chambers.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3560 BUE 5744 Polyethylene, Linear Low Density is a rotational-molding powder in the Icorene family. The resin is produced by low-pressure ethylene–α-olefin copolymerization, giving a predominantly linear backbone with controlled short-chain branching. That architecture separates it from high-pressure low density polyethylene, which carries long-chain branching and is commonly supplied as pellets for extrusion or injection molding. The suffix BUE 5744 is an internal manufacturing and stabilization code; public documents define the product class rather than the full additive composition. Published data for this specific configuration is limited, and exact density, melt index, and particle-size distribution should be obtained from the manufacturer’s technical datasheet. The material is intended for biaxial rotational molding, where conduction heating through the mold wall and multi-axis rotation produce hollow articles.

    What processing parameters require validation before rotomolding Icorene 3560 BUE 5744?

    Rotomolding is governed by peak internal air temperature, heating time, and cooling rate. For LLDPE systems, peak internal air temperature typically falls within 180–220 °C, while oven air temperature may range from 260 °C to 340 °C depending on mold gauge, part mass, and pigmentation. The lower melting point of LLDPE relative to HDPE permits fusion at a lower internal air temperature, but organic pigments and UV stabilizer packages can shift the optimum upward. Thermocouple or infrared internal air measurement is preferred over dwell-time control because heat transfer varies with mold thermal conductivity, wall thickness, and oven airflow. On multi-axis carousel machines with aluminum tooling, a medium-wall storage tank often reaches a peak internal air temperature of 200 °C before forced-air cooling. This is not a universal recipe; tooling design and machine calibration must determine the final profile.

    Cooling rate affects part flatness and residual stress. Slow ambient cooling reduces warpage but extends cycle time and may produce low-crystallinity skins. Rapid water-mist cooling increases productivity and can refine surface smoothness; however, it can also freeze a tensile skin and reduce impact in large flat panels. Differential cooling of steel inserts and aluminum molds is a common source of part distortion. The cooling segment should therefore be profiled with the same rigor as heating.

    Mechanical property benchmarks and standard test alignment

    Density and melt flow are first-order indicators for material handling and warpage. Density is measured by ASTM D792/ISO 1183-1:2019; melt index is measured at 190 °C with 2.16 kg load by ASTM D1238-20/ISO 1133-1:2022. Table 1 compares class-typical values for unpigmented, untreated rotational-molding LLDPE, HDPE, and high-pressure LDPE. These are not grade-specific certification values for Icorene 3560 BUE 5744.

    Property Test standard LLDPE rotomolding typical HDPE rotomolding typical LDPE typical
    Density ASTM D792/ISO 1183-1:2019 0.920–0.940 g/cm³ 0.940–0.965 g/cm³ 0.915–0.935 g/cm³
    Melt index ASTM D1238-20/ISO 1133-1:2022 2.0–6.0 g/10 min 3.0–9.0 g/10 min 3.0–10 g/10 min
    Tensile yield strength ASTM D638-14/ISO 527-2:2012 10–20 MPa 20–30 MPa 8–12 MPa
    Flexural modulus ASTM D790-17/ISO 178:2019 200–450 MPa 700–1,200 MPa 100–250 MPa
    Environmental stress-crack resistance ASTM D1693-15 >1,000 h 50–500 h 1–100 h

    The comparative ranges are drawn from general rotational-molding grade datasheets. They demonstrate the differentiation between LLDPE and other polyolefins, but they do not replace supplier certification for Icorene 3560 BUE 5744.

    On production-scale biaxial rotational molding machines, powder dry-flow and static charge control determine wall distribution inside deep cavities. LLDPE powders are not hygroscopic, but cool molds stored in humid bays can accumulate condensation; free water on the mold surface produces steam porosity and pinholes. Powder storage should be maintained below 40 °C and protected from UV exposure to minimize particle agglomeration and surface oxidation. Pre-drying is rarely required unless visible moisture is present or the powder has been stored in high-humidity conditions above 60 % RH. Static charge from pneumatic transfer can cause powder to cling to mold corners; grounded transfer lines and anti-static mold primers reduce this effect.

    Rotational molding equipment with a shot weight above 10 kg often uses drop boxes or internal air injection to control wall thickness. Mold release compounds must be selected for compatibility with polyolefins. Silicone-based external mold release agents can reduce surface energy and complicate post-molding adhesion or painting. No abrasive fillers are normally used in natural LLDPE rotomolding unless specified for wear applications.

    Process audits on rotomolding lines identify three recurrent failure modes for LLDPE: undercure porosity at thick bosses, oxidative embrittlement at the inner surface due to prolonged high-temperature exposure, and warpage from asymmetric cooling. Undercure porosity appears as microvoids at the junction of mold inserts because powder stagnates in low-movement zones. Oxidative embrittlement occurs when the part remains above 180 °C for excessive time in the presence of air, consuming antioxidant stabilizers. Warpage is managed by balancing cooling on both mold faces, especially for flat panels longer than 1 m. These process limitations are generic to LLDPE rotational molding; grade-specific behavior of Icorene 3560 BUE 5744 must be validated by trial.

    When low-temperature impact toughness and environmental stress-crack resistance determine service life

    LLDPE is selected over HDPE when the part must withstand impact at sub-zero temperatures and resist environmental stress cracking in contact with detergents, alcohols, or agricultural chemicals. In notched constant-strain testing according to ASTM D1693-15, unpigmented LLDPE rotational-molding grades frequently exceed 1,000 h in a wetting agent, whereas HDPE grades may fail below 500 h at comparable density. The ESCR advantage arises from short-chain branching distribution and molecular weight; the branches decrease density and crystallinity while pinning tie molecules at amorphous-region boundaries.

    The ESCR test method uses a 10 % solution of nonylphenoxy poly(ethyleneoxy) ethanol at 50 °C for condition B, while condition A uses 100 % agent at 50 °C. A stress-crack inhibitor additive can alter this response, so the chosen stabilization package in BUE 5744 must be considered.

    Low-temperature impact is evaluated with notched Charpy per ISO 179-1:2010 or notched Izod per ASTM D256. A useful comparison point is the ductile-to-brittle transition; LLDPE generally retains ductile behavior below -30 °C, but this depends on comonomer type and molecular architecture. For rotomolded kayaks, marine buoys, and agricultural tanks, this low-temperature ductility reduces seasonal field failures. Published data for this specific configuration is limited; end users should obtain a grade-specific datasheet before specifying impact requirements in a tender.

    Regulatory documentation must be verified before food-contact or potable-water service.

    Unfilled olefin polymers may comply with 21 CFR 177.1520 if the polymer meets the specified density and extraction limits. The regulation permits certain ethylene copolymers in contact with food under prescribed conditions; compliance is established by testing the finished article for extractables, not solely by resin grade. Converters should obtain a manufacturer’s regulatory statement that references the exact grade and any approved monomers. Potable water components require testing against NSF/ANSI 61 or applicable national standards; the resin alone does not certify the finished fitting or tank.

    Regulatory area Reference Verification requirement
    US food contact 21 CFR 177.1520 Manufacturer compliance letter; finished article extraction testing
    EU food contact EU 10/2011 Overall migration testing per EN 1186 series
    EU REACH EC 1907/2006 Safety Data Sheet and registration status
    RoHS 2011/65/EU Confirmation of no restricted additives or pigments

    For rotationally molded water storage tanks, wall thickness is commonly specified from 3 mm to 12 mm, depending on tank volume and hydrostatic pressure. Large tanks may require internal baffles and additional inserts, which influence the powder flow path and demolding. Shrinkage is anisotropic because cooling occurs from the outer mold surface; linear mold shrinkage for LLDPE is generally 1.5 % to 3 % but must be confirmed on the actual tool. After demolding, parts should be conditioned at ambient temperature before dimensional inspection because continued crystallization can change dimensions by up to several tenths of a percent over 24 h.

    The performance difference between Icorene 3560 BUE 5744 and a pelletized HDPE is most evident in large flat sidewalls. HDPE offers higher bending stiffness and better hot-water resistance but is more prone to stress-cracking at baffle inserts and along weld lines. In contrast, this LLDPE grade can accept greater deflection without brittle fracture, provided the part is fully fused and not overcooled. No single property can substitute for prototype testing on the intended rotational molding machine.

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