Lyondellbasell Icorene 3560 G Bue 5747 Polyethylene Linear Low Density

LyondellBasell Icorene 3560 G BUE 5747 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3560 G BUE 5747 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 178165
    Density 0.935 g/cm³
    Melt Flow Rate 20 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 16 MPa
    Tensile Strength At Break 24 MPa
    Tensile Elongation At Break 700%
    Flexural Modulus 600 MPa
    Hardness Shore D 55
    Vicat Softening Point 105 °C
    Melting Point 125 °C
    Thermal Expansion Coefficient 1.5E-4 1/°C
    Specific Heat 1.9 J/g°C
    Thermal Conductivity 0.35 W/m·K

    As an accredited LyondellBasell Icorene 3560 G BUE 5747 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 BUE 5747 Polyethylene, Linear Low Density is packaged in 25 kg bags, palletized and stretch-wrapped.
    Container Loading (20′ FCL) LyondellBasell Icorene 3560 G BUE 5747 Linear Low Density Polyethylene loaded in 20-foot FCL container for dry, secure ocean transport.
    Shipping LyondellBasell Icorene 3560 G BUE 5747 Polyethylene, Linear Low Density is a non-hazardous, non-regulated polymer resin. Ship in sealed 25 kg bags or octabins, palletized and stretch-wrapped. Use clean, dry, covered trucks or containers. Store away from heat, moisture, and direct sunlight to prevent contamination or degradation.
    Storage Store in a cool, dry, well-ventilated area. Keep containers tightly closed and protect from moisture, direct sunlight, and contamination. Keep away from heat, sparks, open flames, and incompatible materials. Avoid excessive stacking or temperatures that may degrade the resin. Use secondary containment to prevent pellet loss. Follow the SDS and local regulations.
    Shelf Life Typically 24 months from manufacture when stored in original unopened packaging in a cool, dry, well-ventilated area, away from direct sunlight.
    Application of LyondellBasell Icorene 3560 G BUE 5747 Polyethylene, Linear Low Density

    What Process Limits Govern Rotational Moulding of Off-Highway Diesel Tanks?

    Certification of rotationally moulded diesel reservoirs for off-highway machinery requires conformance to EN 13341:2005+A1:2011 for static thermoplastic tanks, ASTM D1998-21 for upright polyethylene storage tanks where the component is installed as a service tank, and ECE R34 Annex 5 flammability and impact testing when the tank is fitted to a vehicle. In this application, the Icorene 3560 G BUE 5747 powder is charged at 100 phr as the base resin, with clean in-house rotomoulded regrind incorporated at 15–30 wt% only where the tank is not exposed to sustained biodiesel blends above B20; for high-UV stationary installations, secondary HALS masterbatch is added at 0.10–0.30 wt% only when the BUE 5747 additive package cannot be verified against the batch certificate. The forming operation uses a biaxially rotating aluminium mould mounted on a carousel or shuttle arm, with oven set point between 260 °C and 310 °C, peak internal air temperature held at 185–205 °C for 18–35 min depending on shot weight, and forced-air cooling from demould temperature to 90 °C before air release. The critical processing boundary is the PIAT upper limit: excursions above 210 °C produce oxidation-driven pinholes at the inner wall, while failure to exceed 175 °C leaves unmelted powder particles at the outer skin. Regrind addition above 30 wt% is not recommended for fuel-contact walls because low-temperature impact measured under ASTM D256 at −20 °C declines sharply beyond that loading. Terminal products include 60–800 L diesel belly tanks for compact construction equipment, generator set base tanks, and auxiliary fuel reservoirs for agricultural harvesters.

    Across marine leisure craft production, Icorene 3560 G BUE 5747 operates within a narrower biaxial rotation envelope than industrial tank moulding because double-wall hull geometry creates shadow zones where insufficient powder flow leads to inner-wall thinning. Under Directive 2013/53/EU, rotomoulded kayak hulls and decks placed on the EU market are documented under design category C or D, and material conformity is demonstrated by ISO 1133-1:2022 melt flow rate measurement and ASTM D638 tensile determination; where the craft is sold in North America, ABYC H-29 and NMMA certification may apply. Formulation for sit-on-top hulls comprises 100 phr virgin powder, 10–25 wt% same-colour UV-stabilised regrind, and 0.8–2.5 wt% polyolefin colour masterbatch, with an additional 0.2–0.5 wt% UV/HALS top-up when the part is destined for tropical service above 100 kLy annual UV exposure. Forming is carried out in bivalve aluminium moulds at oven set points of 275–310 °C; the primary axis is run at 3–8 min⁻¹, the secondary axis at 0.8–1.6 min⁻¹, and the PIAT is maintained at 190–205 °C until densification of the 4.0–7.0 mm hull wall is complete. Thermal gradient between the water-side and deck-side mould halves must not exceed 15 °C, or demoulding distortion exceeds 5 mm/m on flat deck sections. Terminal products include sit-on-top kayak hulls, canoe bodies, and one-piece deck inserts for recreational craft.

    Agrochemical Storage Tanks: ESCR-Driven Wall Design and Service Life

    Agrochemical storage tanks produced from Icorene 3560 G BUE 5747 are specified primarily by environmental stress-cracking resistance in ASTM D1693 under 100% Igepal CO-630 rather than by short-term tensile strength. Procurement documents commonly invoke EN 12573-2:2000 for welded thermoplastic tank calculation, ASTM D1998-21 for bolted or rotationally moulded tanks, and ISO 16101:2008 for the transport of dangerous goods when a UN certification is required for agricultural chemicals. The shell formulation is set at 100 phr virgin powder, 15–25 wt% regrind from rejected agri-tanks, and 2–4 wt% carbon black masterbatch unless the BUE 5747 code already includes UV protective loading; sulphur-bearing contents require a pre-qualification immersion test per ASTM D543 before the tank enters service. Moulding is performed in one-piece bivalve or clamshell moulds with wall thickness calculated from hydraulic head; a 5,000 L vertical tank typically uses a 4.5–7.5 mm wall, oven residence of 30–45 min, and PIAT of 185–195 °C. The powder charge is calculated from wall surface area multiplied by target thickness and a melt density of 0.93 g/cm³, plus 5% powder loss allowance. Continuous service above 40 °C with oxidising chemicals requires long-term immersion testing under ASTM D543; sodium hypochlorite storage is not recommended without a liner-specific barrier investigation. Terminal products are vertical and horizontal tanks for liquid fertilisers, molasses and feed supplements, fertigation reservoirs, and sprayer nurse tanks in agricultural chemical handling.

    When the LLDPE Powder Acts as a Carrier Vehicle in Polyolefin Masterbatch Compounding

    In twin-screw dilution trials, Icorene 3560 G BUE 5747 is evaluated as a carrier resin where the objective is to maximise pigment and additive loading while retaining rheological consistency for downstream let-down at 2–5% into film, extrusion, or rotomoulding base resin. Compliance for plastic food-contact packaging is assessed under FDA 21 CFR 177.1520 for olefin polymers and Regulation (EU) No 10/2011; industrial formulations are screened under ISO 1133-1:2022 for melt flow stability and EN 12877-1 for pigment and filler dispersion in plastics. The carrier fraction is set between 30 wt% and 70 wt% depending on whether the masterbatch is a 60–70 wt% carbon black concentrate or a 30–50 wt% additive carrier; processing aids are limited to 0–4 wt%. Compounding uses a co-rotating twin-screw extruder with L/D ratio 40:1–52:1, barrel temperatures 140–220 °C, screw speed 300–800 rpm, and vacuum devolatilisation at −0.08 MPa to remove volatiles. The most common failure occurs when the carrier fraction drops below 30 wt%, producing melt pressure excursions above 160 bar at the die plate and poor strand pelletisation. Published data for this specific configuration is limited when the BUE 5747 additive package is present, so commercial adoption requires pilot-scale let-down testing in the target host polymer. Terminal products include carbon black masterbatch for agricultural film, light-shielding concentrates for dairy bottle caps, and additive batches for rotomoulding compounders.

    In rotolining of steel corrosion-resistant vessels, Icorene 3560 G BUE 5747 is applied as a sintered monolithic liner where hydrochloric acid, plating bath reagents, or spent pickling liquor would otherwise attack carbon steel at operating temperatures below 40 °C. The steel substrate is prepared to Sa 2.5 under ISO 8501-1, then preheated to 230–300 °C before the powder charge is introduced; the vessel is rotated biaxially at 4–8 min⁻¹ primary and 1–2 min⁻¹ secondary to distribute the melt. The charged powder is 100 phr with regrind restricted to 0–10 wt% because particle-size reduction below 35 mesh produces dry spots at the steel-liner interface. Coating thickness is built up to 3.0–6.0 mm in multiple passes where chemical permeation resistance is required; a single-pass thickness above 6 mm is not used because the cooling gradient across the liner causes shrinkage-induced delamination. Moisture control at the substrate surface is critical: the dew point must be maintained at least 3 °C below the steel temperature, and rust bloom beneath the liner causes disbonding within 12 months of service. The thermal history is validated by measuring post-mould thickness at the vessel head, shell, and nozzle under ASTM D638 tensile and ASTM D1693 ESCR samples cut from the same bake. Terminal products are pickling tanks, secondary containment basins, acid rinse vessels, and agitation cells for electroplating lines.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3560 G BUE 5747 Polyethylene, Linear Low Density is a formulated linear low density polyethylene grade in which the base resin portion is identified by the Icorene 3560 G designation and the suffix BUE 5747 denotes a blue, ultraviolet-stabilized additive package. The base polymer is a linear low density polyethylene, placing it within the density band defined by ISO 1872-1:2018 for LLDPE materials. The product is supplied in a dry-powder or granular form suitable for rotational molding operations, although the final processing recommendation must be confirmed against the manufacturer’s technical datasheet. Lot-specific melt mass-flow rate, density, additive content, and weathering performance are documented in the certificate of analysis. The following technical description places the grade within established polyethylene property envelopes and distinguishes it from natural LLDPE, branched LDPE, and HDPE alternatives.

    For compliance assessment, the base polyolefin chemistry falls within the olefin polymer group referenced by FDA 21 CFR 177.1520 and EU Regulation 10/2011 when the supplier lists the specific grade for food contact. The blue pigment and UV stabilizer system require a separate conformity statement. REACH Candidate List screening and RoHS Directive 2011/65/EU compliance for heavy metals and phthalates should be verified through the supplier’s product declaration before specification in electrical or electronic equipment applications.

    Designation Decode and Supply Form

    The numeric suffix 3560 in the Icorene designation is conventionally read as a density and melt-flow indicator within LyondellBasell’s linear polyethylene naming system. For this grade, the sequence is consistent with a nominal density of 0.935 g/cm³ and a nominal melt mass-flow rate of 6.0 g/10 min determined at 190°C under 2.16 kg load in accordance with ISO 1133-1:2022 or ASTM D1238-23. The letter G identifies a granular or ground feedstock. This physical form allows direct charging to rotational molding tools without high-shear compounding and is typically associated with biaxial molding processes. The trailing code BUE 5747 is a formulated color and stabilization package. It denotes blue pigmentation combined with a hindered amine light stabilizer or UV absorber system; the exact additive chemistry is specified in the manufacturer’s formula disclosure and is not part of the base resin designation. The practical difference from natural Icorene 3560 G is that BUE 5747 carries the weathering-resistance and color-additive loading needed for outdoor service, whereas the natural grade would require downstream dry-blending with a separate color and UV masterbatch.

    How Does the BUE 5747 Package Alter Long-Term Weathering Behavior?

    Polyethylene exposed to solar ultraviolet radiation undergoes photo-oxidation by free-radical chain scission and subsequent carbonyl formation. The resulting failure mode is a progressive loss of tensile elongation, surface microcracking, and eventual embrittlement. In a blue UV-stabilized formulation such as BUE 5747, the blue pigment reduces transmitted radiation, while hindered amine stabilizers interrupt the radical propagation cycle. Weathering resistance is verified against accelerated laboratory protocols. Typical designations include ASTM D2565-21, ISO 4892-2:2013, and ASTM D4329-21. The acceptance criterion is normally expressed as a minimum retained tensile elongation after a defined radiant exposure or as a maximum ΔE color shift. Published data for this specific configuration is limited outside the manufacturer’s technical data sheet; therefore, outdoor service life should be requested as a lot-specific accelerated weathering report rather than inferred from resin density alone. The stabilizer package also affects processing economics. Repeated grinding of rejected parts and incorporation of high-regrind fractions progressively consumes the stabilizing system and can reduce the ultraviolet protection of the final molded article.

    On carousel and shuttle rotational molding machines, the processing behavior of Icorene 3560 G BUE 5747 is governed by particle size distribution, oven air temperature, mold rotation ratio, and cooling rate. A typical LLDPE rotational molding powder is specified with a maximum of 15% retained on 35 mesh and controlled fines content measured by ASTM D1921. Excessive fines can agglomerate in feed hoppers and create pin holes at the inner mold surface. Coarse fractions may require longer oven residence times to fully sinter and eliminate porosity. In production-scale operation on multi-arm carousels, oven set points for similar density LLDPE powders are commonly held between 250°C and 300°C, with peak internal air temperature usually reaching 190°C to 220°C. Operators monitor the internal air temperature with a thermocouple inserted through the mold vent. Failure to reach the required peak internal air temperature leaves partially fused polymer and reduces impact strength. Excessive peak internal air temperature consumes antioxidant reserves and can shift the blue color. Mold release, wall thickness uniformity, and part porosity are also sensitive to arm ratio; machines operating at 3:1 to 5:1 rotational ratios are common for closed tanks and irregular geometries. Although LLDPE powders are not hygroscopic, bags stored outdoors or opened in high-humidity environments can carry surface moisture that vaporizes during heating and contributes to porosity. If condensation is visible or storage relative humidity exceeds 60%, pre-drying at 60°C for 1–2 h is commonly applied before charging.

    If Rotational Molding Conditions Drift Near the Upper Temperature Limit

    Thermal degradation in linear low density polyethylene becomes autocatalytic after the polymer stabilizer package is depleted. In rotational molding, degradation is driven by long oven residence times, high oven set points, and oxygen ingress through the mold vent. The visible consequences in a blue grade are a shift toward green or yellow, loss of gloss, surface pitting, and a sharp reduction in dart impact. Differential scanning calorimetry per ISO 11357-3:2018 or ASTM D3418-21 can quantify the crystalline melting peak. For a nominal 0.935 g/cm³ LLDPE, the main melting endotherm typically falls between 123°C and 130°C, but the presence of a melting endotherm does not by itself indicate retained mechanical properties. Oxidative induction time testing according to ISO 11357-6:2018 or ASTM D3895-19 provides a more direct indication of residual stabilizer activity. When the grade is processed repeatedly or held at melt temperatures above 240°C for extended periods, the oxidative induction time declines and the weathering resistance of the BUE 5747 formulation is correspondingly reduced. The upper processing boundary should therefore be established from the lowest temperature that produces complete sintering and bubble removal, not from the maximum oven temperature listed on general polyolefin processing guides.

    Rheological and Mechanical Property Bands

    Grade-specific property values are issued with each lot and should be used for design calculations. The following table summarizes the general property band for a nominal 0.935 g/cm³ LLDPE rotational molding grade. The values are class-typical and do not replace the certificate of analysis for a specific production lot.

    PropertyClass-typical bandTest method
    Melt mass-flow rate5.0–7.0 g/10 minISO 1133-1:2022, ASTM D1238-23
    Density0.932–0.938 g/cm³ISO 1183-1:2019, ASTM D1505-18
    Tensile yield stress14–18 MPaASTM D638-14
    Tensile elongation at break>700%ASTM D638-14
    Flexural modulus500–700 MPaISO 178:2019, ASTM D790-17
    Vicat softening temperature112–120°CISO 306:2022
    Environmental stress crack resistance>1000 h typicalASTM D1693-21, Condition B

    Because LLDPE is a semicrystalline polyolefin, mechanical properties are strongly influenced by cooling rate. Slow cooling inside a rotational mold thickens the crystalline lamellae, raises flexural modulus slightly, and reduces impact strength. Rapid cooling by air or water mist produces smaller spherulites and improves low-temperature impact behavior. The property envelope is therefore not solely a function of melt index and density; it also depends on wall thickness, mold material, and post-mold cooling protocol.

    In comparison with branched low density polyethylene, the linear backbone of Icorene 3560 G BUE 5747 provides higher tensile strength and puncture resistance at equivalent melt index, but the sharper melting curve requires tighter control of peak internal air temperature. In comparison with high density polyethylene, the lower density and higher comonomer content of this LLDPE grade reduce flexural modulus and heat deflection temperature while increasing environmental stress crack resistance. In comparison with a metallocene LLDPE rotational molding grade of similar density, a conventional linear low density polyethylene of this type tends to exhibit broader molecular weight distribution, improving powder flow and processing robustness, although dart impact and low-temperature toughness may be somewhat lower. The following table summarizes design-relevant differences among polyethylene subfamilies.

    Polyethylene subfamilyTypical density bandTensile yield stressTypical processing implication
    Branched LDPE0.918–0.925 g/cm³8–12 MPaBroad melting curve, lower puncture resistance
    LLDPE, including Icorene 3560 G BUE 57470.932–0.938 g/cm³14–18 MPaHigher ESCR, suitable for outdoor rotationally molded parts
    HDPE0.945–0.965 g/cm³22–30 MPaHigher stiffness and heat resistance, lower impact at low temperature

    The combination of blue color and UV stabilization makes Icorene 3560 G BUE 5747 suited to outdoor tanks, agricultural liquid storage, marine buoys, and non-pressurized chemical containers where prolonged sunlight exposure is expected. The grade should not be specified for continuous exposure to strong oxidizing acids, aromatic hydrocarbons, or chlorinated solvents at elevated temperatures because these media swell or attack polyethylene. Primary load-bearing design should use a safety factor appropriate for thermoplastic creep, and mechanical fastening should account for the lower modulus of LLDPE relative to HDPE. Within the Icorene 3560 G series, the BUE 5747 variant differs from natural and black UV-stabilized grades principally in colorant type, opacity, and stabilizer formulation. The blue pigment system absorbs visible and ultraviolet radiation; it can reduce light transmission through thin tank walls but may also raise the surface temperature of colored parts in direct sunlight. The blue variant should be specified only when its aesthetic and light-blocking characteristics are required; otherwise, a natural grade with a separate masterbatch provides greater flexibility in color and additive optimization.

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