Lyondellbasell Icorene 3560 G Pin 4512 Polyethylene Linear Low Density

LyondellBasell Icorene 3560 G PIN 4512 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3560 G PIN 4512 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 707097
    Material Type Polyethylene, Linear Low Density (LLDPE)
    Density 0.935 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 3.5 g/10 min
    Melting Point 124 °C
    Vicat Softening Temperature 100 °C
    Tensile Strength At Yield 14 MPa
    Tensile Strength At Break 26 MPa
    Tensile Elongation At Break 800%
    Flexural Modulus 300 MPa
    Shore D Hardness 50
    Thermal Conductivity 0.33 W/m·K

    As an accredited LyondellBasell Icorene 3560 G PIN 4512 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 PIN 4512 LLDPE is supplied in 25 kg polyethylene bags, 40 bags per pallet (1,000 kg).
    Container Loading (20′ FCL) 20′ FCL container loading of LyondellBasell Icorene 3560 G PIN 4512 Linear Low Density Polyethylene, securely packed for ocean freight.
    Shipping LyondellBasell Icorene 3560 G PIN 4512 Polyethylene, Linear Low Density is shipped as non-hazardous, solid resin pellets in 25 kg bags, octabins, or bulk trucks/railcars. It is not regulated for transport. Store dry, away from direct sunlight, heat, and ignition sources. Handle per local regulations.
    Storage Store LyondellBasell Icorene 3560 G PIN 4512 Polyethylene, Linear Low Density in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original bags or containers closed, clean, and palletized to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and extreme temperatures. Rotate stock, use oldest first, and follow the manufacturer’s SDS and local regulations.
    Shelf Life No established shelf life; stable if stored sealed in a cool, dry, well-ventilated area away from heat and sunlight.
    Application of LyondellBasell Icorene 3560 G PIN 4512 Polyethylene, Linear Low Density

    Thermal Degradation Margins in Rotationally Moulded Double-Wall Chemical Tanks

    Rotational moulding of double-wall chemical storage tanks from LyondellBasell Icorene 3560 G PIN 4512 polyethylene, linear low density, is constrained by the interaction of powder bulk density, oven air temperature, and slow biaxial coalescence. The powder exhibits a typical apparent density of 0.35–0.42 g/cm³ per ISO 60, which dictates shot weight against internal cavity area. For a 250 L tank shell with a 6 mm nominal wall, the dry powder charge is 8.5–10.0 kg; for an outer containment basin with 10 mm nominal wall, the charge increases to 14–17 kg. The moulding line is typically a four-arm carousel with a 3.2 m swing and fabricated 5 mm carbon steel moulds. A rotation ratio of 4:1 with primary axis speed 6–8 min⁻¹ and secondary axis speed 1.5–2.0 min⁻¹ produces acceptable melt distribution. Peak internal air temperature of 185–190 °C is held for 18–25 min at an oven setpoint of 270–290 °C. If internal air exceeds 200 °C, oxidative induction time measured by ISO 11357-6 falls below 15 min, and sidewall impact energy measured by ISO 179-1/1eU at −20 °C may drop below 15 J. After heating, forced-air cooling at 0.8–1.2 °C/min is applied until demoulding at 65 °C; demoulding above 80 °C introduces flange warpage of 2–4 mm/m across the upper rim. The material is not specified for continuous immersion in chlorinated solvent service above 40 °C unless environmental stress-crack resistance is revalidated per ISO 22088-3; published data for this specific grade is limited under those conditions.

    Compliance for chemical storage service is anchored to ASTM D1998-21, which covers rotationally moulded polyethylene upright storage tanks and requires hydrostatic testing as defined by the specification. Food-contact secondary containment fabrication falls under FDA 21 CFR 177.1520(c) and EU Regulation (EC) No 10/2011, with an overall migration limit of 10 mg/dm² for plastic articles in contact with foodstuffs. Formulation adjustment uses 0.2–0.5 wt% HALS stabilizer masterbatch for outdoor weathering and 0.1–0.3 wt% antacid/processing stabilizer. Clean regrind is limited to 15 wt% because higher fractions narrow the processing window by 4–6 °C. Pigment masterbatch is added at 0.5–2.0 wt% only when the carrier resin melt-flow-rate is within 2.0–5.0 g/10 min per ISO 1133-1:2022; outside this range, unmelted pigment agglomerates produce surface pits under ×10 visual inspection. Terminal parts include vertical cylindrical tanks from 250 L to 5,000 L, secondary containment basins, dosing skid tanks, and conical-bottom process vessels.

    In the fabrication of marine fender shells and floating buoyancy modules, Icorene 3560 G PIN 4512 is processed as a dry-blend rather than a melt-compounded formulation because long oven residence times for 8–15 mm walls create less additive degradation when concentrated masterbatch is introduced at the mould charging station. A typical formulation for a single-skin cylindrical dock fender includes 1.0–2.0 wt% of a HALS/UV masterbatch, 0.5–1.5 wt% of an endothermic chemical blowing agent for the foamed core, and 5–10 wt% of an LDPE grade with density 0.918–0.923 g/cm³ to reduce skin flexural modulus. The outer skin is moulded first to 4–6 mm, after which the foaming charge is introduced through a drop arm and the core expands to fill the remaining 8–12 mm cavity. Rock-and-roll machines are preferred over biaxial carousels for lengths above 1.5 m; the long axis rotates at 4–6 min⁻¹ and the rocking arc is ±45°. Oven setpoint is 255–270 °C, internal air target is 175–185 °C, and total cycle time is 35–50 min, followed by forced-air cooling at 0.6–1.0 °C/min to 50 °C before ejection. Demoulding above 60 °C causes foam cell collapse at the skin-core interface, reducing buoyancy by 3–5% after 24 h water immersion per ISO 2896. Marine components are evaluated for UV resistance under ISO 4892-3:2021 using 500 h fluorescent UVA-340 exposure; tensile elongation retention must exceed 80% relative to unexposed controls measured by ISO 527-2/1B. Environmental stress-crack resistance is assessed by ISO 22088-3 for fender service in saltwater; published data for this specific foamed configuration is limited, so suppliers qualify each lot with a 100 h notched constant-load immersion test in 3.5 wt% NaCl at 23 °C. Terminal parts include floating buoys, cylindrical ship fenders, dock bumpers, pontoon floats, and aquaculture collars.

    What Internal Air Temperature Ceiling Prevents Pinhole Formation in Thin-Walled Agricultural Feeding Troughs?

    The production of agricultural liquid-feed troughs and water tanks with wall thicknesses of 3.5–5.0 mm is more sensitive to internal air overshoot than to total heat input. In a clamshell machine with 1.8 m plate area, a 4 mm nominal wall trough is charged with 3.0–4.0 kg powder per cavity and heated at an oven setpoint of 255–265 °C. Internal air temperature is ramped to 170–175 °C over 14–18 min and held for 4–6 min. If internal air exceeds 180 °C during the stationary phase, tensile elongation at break drops from 800–900% to below 600% when tested per ISO 527-2/1B at 23 °C; this loss is accompanied by pinholes at the weld line and at sharp radii below 2 mm. Cooling uses 10–12 min forced air at 1.5–2.0 °C/min, followed by 3–5 min water mist. Demoulding below 45 °C is avoided because semi-crystalline shrinkage of 1.5–2.0% can lock the part onto the core. Formulation for food-contact troughs is restricted to additives listed in EU Regulation (EC) No 10/2011 Annex I/II; the total migration limit is 10 mg/dm². FDA 21 CFR 177.1520(c) applies for US dairy and poultry applications, and NSF/ANSI 61 is cited when troughs double as potable water reservoirs. The dry-blend comprises 0.2–0.5 wt% food-grade pigment masterbatch, 0.1–0.3 wt% process antioxidant, and 10 wt% clean regrind; no slip agent is used because total migration of excess fatty amide above 0.2 wt% can exceed 10 mg/dm² in fatty feed simulants. Terminal products include cattle water troughs, calf feeding troughs, pig farrowing pans, and 750 L horizontal agricultural water tanks.

    ApplicationNominal wall thicknessOven setpointInternal air ceilingCooling ratePrincipal process failure
    Double-wall chemical tank6–10 mm270–290 °C185–190 °C0.8–1.2 °C/minFlange warpage above 80 °C demould
    Marine fender8–15 mm255–270 °C175–185 °C0.6–1.0 °C/minFoam core collapse above 60 °C ejection
    Agricultural trough3.5–5.0 mm255–265 °C170–175 °C1.5–2.0 °C/minPinholes above 180 °C internal air
    Pharmaceutical bulk bin8 mm275–285 °C185–190 °C0.8–1.0 °C/minConductive carbon black embrittlement below 8 kJ/m²
    Road bollard foam core12 mm275–285 °C190–195 °CStagedRegrind-induced surface oxidation
    Outdoor recreational shell4.5–8.0 mm255–265 °C175–185 °C1.0–1.5 °C/minTalc-filled backing warpage above 190 °C

    Dry bulk handling bins for pharmaceutical and fine chemical secondary containment are rotationally moulded with an antistatic formulation in which conductive carbon black masterbatch is added at 6–10 wt% to achieve surface resistivity below 10^6 Ω per ASTM D257-14. The masterbatch is dry-tumbled with the powder immediately before charging because longer residence in a hopper causes carbon black segregation. A 25 kg shot for a 450 L straight-wall bin with 8 mm nominal wall is processed on a three-arm carousel; oven setpoint is 275–285 °C, internal air target is 185–190 °C, primary rotational speed is 5–7 min⁻¹, and secondary rotational speed is 1.5–2.0 min⁻¹. The heating cycle lasts 22–28 min; forced-air cooling at 0.8–1.0 °C/min to 55 °C is followed by ejection and post-mould trimming of the top rim with a 0.5 mm axial cut. Carbon black raises flexural modulus by 25–40% relative to unfilled material, measured by ISO 178, but reduces notched Charpy impact strength at −20 °C below 8 kJ/m²; therefore, bosses and corners require radii above 6 mm. The material complies with FDA 21 CFR 177.1520(c) for food-contact intermediates, USP ⟨661.1⟩ for plastic packaging components where the bin contacts packaged pharmaceutical materials, and ATEX 2014/34/EU when surface resistivity is below 10^6 Ω and resistance-to-ground below 10^8 Ω per IEC 61340-5-1. Terminal parts include powder transfer bins, tablet containment trays, bulk pharmaceutical hoppers, and aqueous secondary sump liners.

    When Road Bollard Foam Cores Are Moulded at 12 mm Nominal Wall

    When traffic bollards and flexible sign posts are rotationally moulded from Icorene 3560 G PIN 4512, the part is constructed as a 4–6 mm solid skin over a 8–12 mm foamed core. The solid outer layer is processed first, then the chemical blowing agent is added after the skin has sintered; this two-charge method prevents gas nucleation from disrupting the outer surface. The foaming agent is an endothermic sodium bicarbonate/citric acid system at 0.5–1.0 wt% of the core charge, combined with 2.0–3.0 wt% UV black masterbatch and 20 wt% clean regrind. A shuttle machine with a 2.4 m swing and cast aluminium mould is operated at oven 275–285 °C; internal air is raised to 190–195 °C for 18–22 min, then cooling is staged with 10 min forced air and 5 min water mist. Core density measured on cut samples is 0.45–0.60 g/cm³ versus 0.930–0.940 g/cm³ for the solid skin. At 15–25 wt% regrind, internal air setpoint is reduced by 4–6 °C because reprocessed antioxidant-depleted particles oxidize faster at the outer surface; failure to reduce setpoint produces yellowing and surface embrittlement after 5–7 min overshoot. Mechanical qualification for flexible bollards requires tensile yield stress above 12 MPa per ISO 527-2/1A, flexural modulus 200–350 MPa per ISO 178, and ultraviolet weathering per ISO 4892-3:2021 with 1000 h UVA-340 exposure retaining 80% tensile elongation. The product falls under EN 12767:2019 for passive safety support structures when installed in highway rights-of-way. Terminal products are car park bollards, delineator posts, sign base covers, and traffic-calming islands.

    Outdoor playground slides and roto-moulded kayak hulls manufactured from Icorene 3560 G PIN 4512 are produced in clamshell machines with multiple cavities and vented steel moulds to allow gas escape during fusion. The outer skin uses 1.0–2.5 wt% colour concentrate based on a carrier with melt flow rate 4–6 g/10 min per ISO 1133-1:2022; the backing layer is filled with 3–5 wt% fine talc masterbatch for scratch resistance and 1.0–2.0 wt% endothermic foaming agent to create a low-density core. Wall thickness ranges from 4.5–8.0 mm, with oven setpoint 255–265 °C and internal air target 175–185 °C. A rotational ratio of 3.5:1 is used because the elongated kayak geometry requires faster primary-axis distribution; primary speed is 7–9 min⁻¹ and secondary speed is 2.0–2.5 min⁻¹. Cycle time is 25–35 min; cooling is staged as 8 min fan air followed by 5 min water mist to 50 °C. Talc-filled backing increases melt viscosity and incomplete sintering occurs below 175 °C; above 190 °C, warpage of flat panel sections exceeds 2 mm/m measured by a three-point surface plate. Toy safety compliance is anchored to EN 71-3:2019+A1:2021 for migration of specific elements, ASTM F963 for US playground components, and ISO 8124-1 for mechanical hazards. Outdoor weathering is assessed by ISO 4892-3:2021 with 1000 h exposure; colour change measured by ASTM D2244 should not exceed ΔE 5. For kayak hulls, impact toughness is tested by ISO 179-1/1eU at −20 °C with minimum 20 kJ/m². Terminal products include playground slides, climbing panels, kayak hulls, paddleboard shells, and outdoor educational furniture.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3560 G PIN 4512 is classified as a linear low density polyethylene resin. The product designation separates the base resin grade, Icorene 3560 G, from the packaging or product identification number, PIN 4512. The material is supplied in natural resin form and is positioned for injection moulding, thin-wall packaging, caps and closures, and masterbatch carrier applications. The grade combines an upper-range LLDPE density with a melt mass-flow rate selected for fast cavity filling in multi-cavity tools. Product-specific values are established by the manufacturer under standardized test methods; Table 1 lists representative values reported for the natural grade. These values are not specification limits and must be confirmed against the lot-specific certificate of analysis.

    Representative physical property data reported for Icorene 3560 G PIN 4512
    PropertyTest methodRepresentative value
    DensityASTM D1505 / ISO 1183-10.935 g/cm³
    Melt mass-flow rateASTM D1238 / ISO 1133-1:20226.0 g/10 min at 190 °C/2.16 kg
    Tensile strength at yieldASTM D638-14 / ISO 527-218 MPa
    Elongation at breakASTM D638-14 / ISO 527-2>800%
    Flexural modulusASTM D790 / ISO 178620 MPa
    Vicat softening pointASTM D1525 / ISO 306 A50121 °C
    Shore D hardnessASTM D2240 / ISO 86855

    What separates a 3560 G injection-moulding LLDPE from high-pressure LDPE and butene-based LLDPE?

    The principal difference operates at the molecular scale. High-pressure low density polyethylene contains both short-chain and long-chain branches, which reduce crystallinity and impart elevated melt strength. Linear low density polyethylene produced by low-pressure copolymerization of ethylene with an alpha-olefin has short-chain branches but no long-chain branching. This linear architecture increases tensile strength, puncture resistance, and environmental stress-cracking resistance at equivalent density and melt flow, but reduces melt strength and can narrow the processing window in extrusion blow moulding. For injection moulding, the lower melt strength is less restrictive than the gains in toughness and environmental stress-cracking resistance.

    Grade-specific differences are driven by density and melt mass-flow rate. The 0.935 g/cm³ density of Icorene 3560 G places it above film-grade LLDPE resins, which are often positioned near 0.918 g/cm³. The higher density raises flexural modulus and heat resistance while retaining linear polyethylene toughness. The 6.0 g/10 min melt mass-flow rate at 190 °C/2.16 kg is selected for injection moulding; film grades with melt indices of 0.5–1.0 g/10 min offer higher melt strength for blown-film bubble stability but require excessive injection pressure and longer fill times in thin-wall tools.

    Comonomer type introduces another distinction. In LLDPE, butene, hexene, and octene grades differ in short-chain branch length. A hexene-based LLDPE typically improves tie-molecule formation and raises dart impact and tear resistance relative to a butene copolymer at the same density and melt index. If the 3560 G is a conventional Ziegler-Natta LLDPE, its comonomer distribution is broader than metallocene-catalyzed grades, which affects sealing, toughness, and organoleptic behaviour. The manufacturer’s technical data sheet must be consulted to confirm the comonomer and catalyst package, because both are proprietary and affect additive selection and odour and taste performance.

    Compared with HDPE grades of density 0.952 g/cm³, the 0.935 g/cm³ density reduces flexural modulus and heat deflection temperature but increases environmental stress-cracking resistance and low-temperature impact. Compared with high-flow LDPE grades, tensile yield and puncture resistance are higher, but melt flow is more shear-sensitive and screw torque may be higher at equivalent melt index.

    On a 50 mm reciprocating-screw injection moulding machine with a 20:1 L/D screw and a compression ratio of 2.5:1, the material is processed at melt temperatures of 200–240 °C. Mould surface temperatures of 20–50 °C are typical for thin-wall packaging; the upper end of this range improves weld-line strength and surface gloss but adds cycle time. Because linear low density polyethylene is not hygroscopic, pre-drying is not a routine requirement. Condensation on cold resin transferred into a humid production hall can cause splay; if this occurs, pre-drying at 70–80 °C for 2 h is applied.

    Residence time is the principal thermal boundary. At melt temperatures above 220 °C, the antioxidant package is consumed progressively. If the melt remains in the barrel for 8–10 min during an interruption, chain scission lowers molecular weight and can produce gel defects. The standard corrective procedure is to reduce barrel setpoints to 180–190 °C during stoppages longer than 5 min and to purge with a lower-viscosity LDPE or a commercial purging compound before restart. On hot-runner moulds, valve gates control drool at 6.0 g/10 min; open hot sprues are more likely to drool if manifold temperatures exceed 230 °C.

    In compounding, a 40:1 L/D co-rotating twin-screw extruder with side feeding is suitable for masterbatch dilution and filler incorporation. Screw torque rises sharply when high-aspect-ratio mineral fillers exceed 2–5 wt%. Die-plate melt temperature should not exceed 230–240 °C to avoid additive degradation. Underwater pelletizing with water temperatures of 35–50 °C produces uniform pellets, but residual surface moisture must be removed by spin drying before packaging.

    Failure modes observed in closure moulding and dimensional stability

    Closure and thin-wall moulding faults associated with this density and flow class include gate blush, weld-line weakness, flash on worn tools, and anisotropic shrinkage. Gate blush is controlled by reducing injection speed or enlarging the gate diameter; excessive speed reduction increases viscosity and can cause short shots. Weld-line strength in multi-cavity closure tools responds to mould temperature. Raising the mould surface to 40–50 °C improves weld-line strength but can lengthen cycle time by 5–10%. Flash formation is not controlled solely by clamp force; for a high-flow LLDPE, clamp force should exceed 3–5 kN/cm² of projected area depending on wall thickness and flow length.

    Dimensional stability is governed by post-mould crystallization and molecular orientation. Shrinkage parallel to flow can differ from transverse shrinkage; typical mould shrinkage for 0.935 g/cm³ LLDPE injection-moulding grades is in the 1.5–2.5% range, but tool-specific measurement is required. Published shrinkage values are not transferable across different gate and cooling layouts.

    When Food-Contact Compliance Is Specified, Specific Migration Limits and Extraction Protocols Apply

    Food-contact use requires confirmation that the grade and its additive package comply with FDA 21 CFR 177.1520 for olefin polymers or with EU Regulation (EU) No 10/2011. FDA 21 CFR 177.1520 covers polyethylene under specified use conditions, and finished-article extraction testing is required. Under EU Regulation (EU) No 10/2011, the overall migration limit for plastic food-contact materials is 10 mg/dm², verified according to EN 1186-1 and related parts. Specific migration limits for additives and monomers apply from the positive list in the regulation. A resin should not be considered food-contact compliant unless a lot-specific manufacturer declaration and finished-article migration test data are available.

    Compliance checklist matrix for LLDPE packaging and articles
    Regulation / StandardRelevant requirementTypical verification method
    FDA 21 CFR 177.1520Olefin polymer food-contact use conditionsEnd-use extraction testing
    EU Regulation (EU) No 10/2011Overall migration limit 10 mg/dm²EN 1186-1 / EN 1186-14
    EU Directive 94/62/ECSum of Pb, Cd, Hg, Cr(VI) 100 mg/kgEN 14582
    RoHS Directive 2011/65/EUPb, Hg, Cr(VI), PBB, PBDE 1000 mg/kg; Cd 100 mg/kgIEC 62321

    Under REACH Regulation (EC) No 1907/2006, polyethylene polymers are exempt from registration as polymers under Article 2(9), but monomers and additives remain subject to registration. For packaging under EU Directive 94/62/EC, the sum of lead, cadmium, mercury, and hexavalent chromium must not exceed 100 mg/kg by weight of the packaging material. For electrical and electronic equipment under RoHS Directive 2011/65/EU, homogeneous material levels are restricted to 1000 mg/kg for lead, mercury, hexavalent chromium, PBB and PBDE, and 100 mg/kg for cadmium; compliance depends on the absence of heavy-metal pigments and restricted flame retardants.

    Reported conversion applications for this density and flow class include thin-wall disposable food containers, caps and closures, housewares, and masterbatch carrier resins. In closures, the material is selected against HDPE where environmental stress-cracking resistance under ASTM D1693 is the dominant failure mode. A 0.935 g/cm³ LLDPE can withstand stress-cracking conditions that would embrittle an equivalent-MFR HDPE, with the trade-off of lower flexural modulus and lower heat deflection. In thin-wall packaging, the 6.0 g/10 min melt flow permits reduced wall thickness without short shots in multi-cavity tools, provided that the tool is designed for fast-flowing LLDPE rather than low-flow LDPE. The grade should not be used in continuous service above 60–70 °C under load, in outdoor exposure without UV stabilization, or in contact with strong oxidizing acids and chlorinated solvents.

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