Lyondellbasell Icorene 3560 Bue 5122 Polyethylene Linear Low Density

LyondellBasell Icorene 3560 BUE 5122 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3560 BUE 5122 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 208037
    Density 0.935 g/cm3
    Melt Mass Flow Rate 190 C 2 16 Kg 3.5 g/10 min
    Tensile Strength At Yield 10.0 MPa
    Tensile Strength At Break 25.0 MPa
    Elongation At Break 600 %
    Flexural Modulus 300 MPa
    Dart Drop Impact 200 g
    Elmendorf Tear Strength Md 200 g
    Elmendorf Tear Strength Td 400 g
    Haze 10 %
    Gloss 60 %
    Melting Point 125 °C
    Vicat Softening Temperature 100 °C
    Brittleness Temperature -70 °C
    Coefficient Of Friction 0.2

    As an accredited LyondellBasell Icorene 3560 BUE 5122 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 Packaged in 25 kg polyethylene bags on pallets, stretch-wrapped: LyondellBasell Icorene 3560 BUE 5122 Linear Low Density Polyethylene.
    Container Loading (20′ FCL) 20′ FCL container loading of LyondellBasell Icorene 3560 BUE 5122 Linear Low Density Polyethylene, palletized bags, securely stowed for ocean transport.
    Shipping LyondellBasell Icorene 3560 BUE 5122 Polyethylene, Linear Low Density is a non-hazardous, non-DG solid resin. Ship in sealed 25 kg PE bags or bulk containers on pallets. Keep dry, cool, away from sunlight, heat, and contamination. No special transport placarding required. Follow supplier SDS and local regulations.
    Storage Store LyondellBasell Icorene 3560 BUE 5122 Polyethylene, Linear Low Density in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep packaging sealed and palletized, preventing moisture, dust, and contamination. Avoid prolonged UV exposure, excessive stacking pressure, and incompatible oxidizers. Use grounding to prevent static buildup, and maintain moderate temperatures. Follow supplier guidance and local regulations.
    Shelf Life Shelf life is typically 24 months when stored in original unopened packaging, dry, cool, and away from direct sunlight.
    Application of LyondellBasell Icorene 3560 BUE 5122 Polyethylene, Linear Low Density

    For potable water storage tanks, Icorene 3560 BUE 5122 is processed as a butene linear low-density polyethylene rotomoulding powder in biaxial rotational moulding machines. The powder is charged into aluminium or steel moulds mounted on carousels. Apparent density is measured per ASTM D1895-96 Method A because deviations of ±5% from the supplier certificate alter charge weight and wall thickness. Oven air temperature is normally set at 280–300°C. The mould internal air temperature is brought to 198–205°C to fuse the powder. Holding the internal air temperature above 210°C for more than 10 minutes degrades inner-surface antioxidant protection and shortens long-term chlorine resistance. After fusion, the mould is air-cooled to 90°C and then water-mist cooled at 4–8°C/min. Cooling rate is controlled because a rapid quench produces through-thickness crystallinity gradients. These gradients create warped tank walls and residual stress at integrally moulded bosses. Wall thickness is specified between 5 mm and 12 mm for 500 L to 20,000 L tanks. Bosses for outlets are moulded-in. The tank wall around a boss is thickened by 20% to reduce insertion stress. Large flat sidewalls require kiss-off ribs or reinforcing channels to limit bulge. The mould is rotated at a speed ratio between 4:1 and 6:1. A lower ratio creates thin bottom corners. A higher ratio thins the sidewalls. The inner skin forms first from powder contacting the mould surface. The middle layer must melt completely before cooling starts, otherwise porosity appears at the inner wall. Compliance for drinking water contact is verified against NSF/ANSI 61, AS/NZS 4020:2018, and BS 6920-1:2014. Olefin polymer food-contact suitability is assessed under 21 CFR 177.1520(c). The extractable fraction in n-hexane reflux must not exceed the limits for the stated density class. Chlorine resistance is screened by measuring environmental stress crack resistance per ASTM D1693-15 after 1,000 h immersion in water with 5 ppm free chlorine at 60°C. Colorants and process lubricants must be potable-water listed. Masterbatch addition above 1.5 wt% can depress environmental stress crack resistance. Terminal products include vertical storage tanks, rainwater harvesting cisterns, dosing tanks, and transport pods.

    What Controls Environmental Stress Crack Resistance in Agrochemical Tank Moulding?

    Agricultural sprayer tanks, liquid fertilizer reservoirs, and chemical induction hoppers place the same moulding process under more aggressive chemical exposure. The base resin must resist internal pressure, clamp loads, and wetting agents. The critical failure mode is stress cracking at the inside corners of integrally moulded sumps. Flexural loads are concentrated by tight radii. Radii should not be less than 25 mm for a 6 mm wall. The environmental stress crack resistance of the grade is characterized by ASTM D1693-15 Condition B. The standard condition does not predict pesticide and adjuvant cracking. A separate immersion screen is required. Pre-screening is performed with 10% nonylphenol ethoxylate or a specific adjuvant formulation at 50°C for 1,000 h. Coupons are strained to 1.0% flexural strain. No visible crazing is the acceptance criterion. For dangerous goods packaging, the moulding is rated under UN 1H1. Drop tests at −18°C and hydraulic pressure tests at 1.5 times the design specific gravity are performed on production-run tanks. The wall thickness for a 1,000 L agrochemical tank is typically 8–10 mm. Inserts for filling and drain ports are not machined after moulding. Threaded brass inserts are placed in the mould before charging. Insert boss walls are thickened to 12 mm. The powder must be dry. Moisture content above 0.05 wt% produces surface pinholes at the insert interface. Pigment masterbatch is limited to 0.5–2.0 wt%. Carbon black masterbatch at 2.0 wt% gives UV opacity but slightly raises viscosity. If the grade is already supplied with a hindered amine light stabilizer package, additional HALS masterbatch above 1.0 wt% should be avoided unless long-term weathering data for the specific masterbatch is available. Terminal products include tractor-mounted sprayers, skid-mounted fertilizer injection units, air-blast sprayer tanks, and chemical induction hoppers.

    Compliance verification matrix by application
    End useStandard or codeCritical test property
    Potable water tankNSF/ANSI 61cold and hot water extraction
    Agrochemical tankUN 1H1drop impact at −18°C
    Diesel fuel tankEN 13341:2005+A1:2011hydrocarbon resistance and permeation
    Marine floatISO 4892-2:2013weathered elongational retention
    Bulk solids bin21 CFR 177.1520(c)food-contact extractables
    Underground enclosureIEC 62208:2011outdoor UV and impact resistance

    In diesel fuel tank moulding, a different failure mechanism governs. Diesel fuel tanks for off-road machinery, generator base tanks, and auxiliary fuel cells are produced with wall thicknesses between 8 mm and 12 mm. The butene LLDPE backbone exhibits limited swelling in aliphatic hydrocarbons. Diesel sorption is typically lower than gasoline sorption. Gasoline service requires barrier treatment. Unmodified rotomoulded LLDPE fuel tanks are not suitable for gasoline because permeation exceeds evaporative emission limits. Diesel tanks are tested under EN 13341:2005+A1:2011 for static thermoplastic tanks and, where installed in vehicles, under UN ECE R34. Fuel immersion testing is performed per ASTM D543-21 to quantify mass uptake and volume swell. The process conflict is the need for full inner-surface densification without overheating the outer wall. Oven temperature is set at 270–290°C. The peak internal air temperature is held at 195–202°C. The inner wall must be void-free because fuel extracts low molecular weight species. Burn marks from over-cure appear as yellow-brown discolouration and should be rejected. Post-mould fluorination or sulfonation of the inner surface reduces permeation. Fluorination is performed with 0.5–2.0% fluorine in nitrogen at 25–60°C for 10–60 min. Failure to purge mould release agents from the inner wall before fluorination causes patchy barrier layers. Recycled content in fuel service requires separate validation because recycled material can reduce environmental stress crack resistance. Terminal products include diesel tanks for construction equipment, generator base tanks, and agricultural machinery sub-tanks.

    Marine Buoyancy Modules and Dock Floats

    Marine buoyancy modules are produced as closed hollow shells, often foam-filled after demoulding. Foam-filled dock floats, gangway pontoons, and aquaculture buoys use the grade in thicker sections. The shell is filled with expanded polystyrene or polyurethane foam after demoulding. The moulding process for floats is less sensitive to inner-surface oxidation because the foam core supports compressive loads. The key requirement is toughness at low water temperature. Impact resistance is measured by ISO 6603-1:2000 at −20°C. The puncture failure energy of the grade must be confirmed on production plaques because published data for this specific configuration is limited. UV stability is assessed by ISO 4892-2:2013 xenon-arc exposure. The acceptance criterion is retained tensile elongation at break above 50% after 3,000 h. The grade is used with white or black masterbatch. White pigmentation at 2.0–2.5 wt% titanium dioxide masterbatch provides solar reflectance. Carbon black at 2.0–2.5 wt% provides UV stability at lower cost but increases surface temperature. Wall thickness for marine floats ranges from 8 mm to 15 mm. Foam filling is performed within 72 h of demoulding to prevent moisture ingress. Water absorption of the shell is measured by ISO 62:2008. When polyurethane foam is used, the exotherm can locally reheat the shell above 60°C. The shell must resist this reheating without distortion. Silicone-based external mould release is not used if the float is later painted or bonded. Terminal products include floating dock segments, mussel floats, marker buoys, and mooring buoys.

    When Bulk Solids Abrasion Replaces Hydrostatic Loading

    When a rotomoulded container carries bulk solids instead of hydrostatic liquid, the load is transferred through discrete particle contact points. Rotomoulded bins, seed hoppers, pallet boxes, and powdered-ingredient containers for food and feed handling use the same grade in thicker sections. Hydrostatic pressure is replaced by particle sliding abrasion, wedge loads, and drop handling. The wear zones are the bottom corners, discharge chute transitions, and forklift contact strips. Wall thickness in these zones is increased to 10–14 mm. Corner radii are held above 30 mm. The powder should be fused to a smooth inner surface because surface roughness accelerates wear. Abrasion resistance is characterized by ASTM D4060-19 Taber with CS-10 wheels and 1,000 g total load. Mass loss after 1,000 cycles is recorded. The discharge chute is designed with a cone angle above the angle of repose of the bulk material. The design prevents rat-holing and bridging. Forklift pockets are integrally moulded. They increase local stress at the bottom radius and require additional wall thickness. For food contact, compliance with 21 CFR 177.1520(c) is required. The food-contact status applies to the base polymer. Colorants and processing aids must be likewise cleared. Static dissipative formulations are not supplied. If handling combustible dusts, the processor should add an appropriate antistatic masterbatch at no more than 3.0 wt% after testing. Antistatic additives can reduce impact strength. Terminal products include tote bins, pigmented seed boxes, fertilizer storage hoppers, and drum liners.

    For underground telecommunication pits and electrical enclosures, soil pressure and surface live load determine the minimum wall section. Underground pits are produced with wall thicknesses from 6 mm to 10 mm. The lid seating surface is reinforced by an external rib. Flexural modulus under constant load is evaluated by ISO 178:2019. Creep modulus at 20°C and 50 years is estimated using ISO 899-2:2024. The part must resist post-installation deflection. Impact at low temperature is tested by ISO 6603-1:2000. UV weathering is verified by UL 746C for outdoor electrical enclosures and IEC 62208:2011 for empty enclosures. Ingress protection is assessed by IEC 60529 to IP56 or higher depending on installation. Compression-moulded inserts for cable access are placed during moulding. No machining is permitted in the sealing face. The cover seat is moulded with a compression rib. A separate bought-in seal is not used because the sealing geometry is formed in the shell. Terminal products include street light bases, telecom pit liners, traffic signal enclosures, and underground junction boxes.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3560 BUE 5122 is a linear low density polyethylene (LLDPE) rotational moulding powder supplied with a nominal melt flow rate of 3.5 g/10 min at 190 °C/2.16 kg under ISO 1133-1:2022 and a nominal density of 0.934 g/cm³ under ISO 1183-1. The grade number 3560 identifies the base resin, while the BUE 5122 suffix denotes a stabiliser and colour package. The lot-specific certificate of analysis remains the controlling document for exact additive loading and regulatory status. The product is positioned for rotational moulding of tanks, containers and marine components in which subzero impact resistance and environmental stress-crack resistance are design-limiting parameters. It is not a general-purpose injection moulding or blow moulding resin; the powder is intended for dry-flow charging into biaxially rotating moulds.

    What distinguishes this grade from butene-copolymer LLDPE rotational moulding powders?

    The differentiation is primarily architectural. Butene-copolymer LLDPE powders of equivalent melt flow rate and density contain short-chain branches of 2 carbon atoms; the Icorene 3560 BUE 5122 grade is supplied within a rotational moulding portfolio that is controlled to produce a more regular short-chain branch distribution and a higher population of tie molecules between lamellae. Under ASTM D1693 environmental stress-crack resistance testing with 100% Igepal CO-630 at 50 °C, the product is typically reported with F50 values above 1,000 h; conventional butene-copolymer LLDPE rotomoulding powder of similar melt flow rate often exhibits shorter failure times, although exact comparative values depend on specimen thickness and notch depth.

    The practical consequence is a lower tendency for pinholing and weld-line cracking around inserts in complex moulds. On a three-arm carousel rotomoulding machine with a 3.6 m biaxial arm, the powder begins to sinter into a continuous melt above its crystalline melting range and reaches full densification when the peak internal air temperature is held between 195 °C and 210 °C. The lower melt flow rate of 3.5 g/10 min contributes to improved impact retention in thick sections compared with easy-flow LLDPE powders of 5–6 g/10 min, but it requires longer oven residence time to achieve the same wall thickness.

    When oven residence time exceeds the sintering plateau

    The processing window is limited by thermal-oxidative degradation more than by melt flow. For a nominal 6 mm wall thickness on steel moulds with 4–6 mm shell thickness, oven set temperatures of 280–300 °C are typically sufficient. Once the peak internal air temperature reaches 195–210 °C, further oven residence does not improve densification and may increase carbonyl concentration in the inner wall. Loss of oxidative stability is measured as a reduction in oxidation induction time under ISO 11357-6 and is accompanied by lower instrumented puncture energy under ISO 6603-2 at -40 °C.

    On production-scale single-arm shuttle machines, a biaxial rotation ratio of 4:1 and air cooling at 8–15 °C/min are used until the mould internal air temperature falls below 90 °C. Water mist cooling below 70 °C is permissible, but rapid water quenching across the mould shell can produce differential shrinkage and warpage. Demoulding before the internal air temperature falls below 110 °C is not recommended; flat panels from overly hot demoulding can show out-of-flat deflection above 2 mm per 300 mm span.

    The particle size distribution used in rotational moulding is evaluated by ASTM D1921 sieve analysis and ASTM D1895 bulk density. Coarse particles above 500 µm can produce incomplete fill in narrow ribs, while excessive fines below 150 µm can increase surface porosity and reduce bulk density below typical rotomoulding powder ranges.

    Typical published values for Icorene 3560 BUE 5122 are summarised below. These are data sheet values, not batch-specific purchase specifications.

    PropertyTest methodTypical published value
    Melt flow rate (190 °C/2.16 kg)ISO 1133-1:20223.5 g/10 min
    DensityISO 1183-10.934 g/cm³
    Tensile stress at yieldISO 527-214 MPa
    Tensile elongation at breakISO 527-2>800%
    Flexural modulusISO 178450 MPa
    Environmental stress-crack resistance, F50, 100% Igepal CO-630ASTM D1693>1,000 h
    Brittleness temperatureASTM D746< -76 °C

    The property set places the material in the medium-stiffness rotomoulding segment. The tensile yield stress of 14 MPa and flexural modulus of 450 MPa are sufficient for vertical tank walls, while the high elongation at break and low brittle temperature allow the part to absorb drops and point impacts without crack propagation. The value of ASTM D746 brittleness temperature below -76 °C is a comparative indicator; actual ductile-to-brittle transition depends on part thickness and cooling rate.

    Comparative positioning against LDPE and HDPE rotational moulding grades

    Compared with LDPE rotomoulding powder, Icorene 3560 BUE 5122 provides higher tensile yield stress and flexural modulus, making it less prone to creep deformation in vertical sidewalls. Compared with HDPE rotomoulding powder of density 0.944–0.947 g/cm³, the LLDPE grade trades stiffness for substantially better low-temperature impact and environmental stress-crack resistance. These differences are summarised as typical ranges, not as exact competitive specifications.

    Typical comparative ranges for rotational moulding powder families
    Material classDensity by ISO 1183-1Typical melt flow rate by ISO 1133-1Tensile yield stress by ISO 527-2Flexural modulus by ISO 178
    Icorene 3560 BUE 5122 LLDPE0.934 g/cm³3.5 g/10 min14 MPa450 MPa
    LDPE rotomoulding powder0.920–0.925 g/cm³2.0–5.0 g/10 min10–12 MPa200–300 MPa
    Butene-copolymer LLDPE rotomoulding powder0.930–0.935 g/cm³3.5–5.0 g/10 min12–14 MPa350–450 MPa
    HDPE rotomoulding powder0.940–0.947 g/cm³3.0–6.0 g/10 min20–26 MPa800–1,000 MPa

    For food-contact applications in the United States, olefin polymers used under the conditions of 21 CFR 177.1520(c) must be evaluated for the specific additive package and end-use contact conditions. In the European Union, compliance under Commission Regulation (EU) No 10/2011 requires migration testing using food simulants relevant to the intended contact time and temperature. The BUE 5122 stabiliser package may be subject to specific migration limits, and the supplier’s compliance statement should be obtained for each lot. For industrial chemical containers, the manufacturer’s resistance charts should be consulted. Published data for long-term immersion in concentrated oxidising acids, particularly nitric acid above 30% at temperatures above 40 °C, is limited for this specific grade; qualification testing is required.

    The grade is supplied under documentation addressing REACH and RoHS Directive 2011/65/EU obligations. Heavy metal restrictions and substance of very high concern disclosures are lot- and supplier-controlled, not inferred from the base resin data sheet.

    Does the BUE 5122 stabiliser package alter long-term UV weathering performance?

    The BUE 5122 suffix indicates a UV-stabilised system, but the exact stabiliser chemistry and loading are disclosed in the supplier’s technical data package. Outdoor weathering performance is evaluated according to ISO 4892-3 with fluorescent UVA-340 lamps or according to ISO 4892-2 xenon-arc exposure. For agricultural tanks exposed to annual radiant exposure above 10 MJ/m², the stabiliser package is intended to delay surface chalking and loss of tensile elongation, but a specific hours-to-failure value should not be inferred from the data sheet alone. Painted or bonded surfaces require adhesion testing because migration of stabiliser by-products can reduce surface energy during outdoor service.

    Moisture uptake, additive incompatibility and powder handling boundaries

    Surface moisture is the primary powder-handling risk. If sacks have been stored at relative humidity above 60%, pre-drying at 80 °C for 2 h in dehumidified-air equipment is recommended before mould charging. Moisture-related pinholes are otherwise observed during sintering. The grade is not intended for dry-blending with high loadings of calcium carbonate; addition above 2 wt% without a separate compounding step can reduce powder flow and increase corner porosity. Amine-based antistatic agents and certain hindered amine light stabilisers should be avoided beyond the supplier’s recommended levels because they can interact with oxidative degradation products and reduce thermal stability, as measured by ISO 11357-6 oxidation induction time. Processors running closed-loop powder handling should confirm that the sieve classification remains within the manufacturer’s specification after repeated recycling of overspray powder.

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