Lyondellbasell Icorene 3545 Ore 3904 Polyethylene Linear Low Density

LyondellBasell Icorene 3545 ORE 3904 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3545 ORE 3904 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 494864
    Density 0.935 g/cm³
    Melt Flow Rate 4.5 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 12 MPa
    Tensile Strength At Break 25 MPa
    Elongation At Break 700%
    Flexural Modulus 400 MPa
    Vicat Softening Temperature 100 °C
    Melting Point 125 °C
    Shore Hardness D 55
    Notched Izod Impact Strength 80 J/m
    Water Absorption 0.01%
    Volume Resistivity 1e16 ohm·cm
    Dielectric Constant 2.3
    Thermal Expansion Coefficient 1.5e-4 /°C
    Oxygen Index 17%
    Color Orange

    As an accredited LyondellBasell Icorene 3545 ORE 3904 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 3545 ORE 3904 is supplied in 25 kg polyethylene bags, 40 bags per pallet (1,000 kg), stretch-wrapped for transport.
    Container Loading (20′ FCL) 20′ FCL container loaded with LyondellBasell Icorene 3545 ORE 3904 LLDPE; securely stowed and restrained for safe ocean transport.
    Shipping LyondellBasell Icorene 3545 ORE 3904 Polyethylene, Linear Low Density ships as a non-hazardous thermoplastic resin. Typical packaging includes 25 kg bags, bulk bags, octabins, or bulk trucks/railcars. Keep dry, cool, and contamination-free; avoid prolonged heat and direct sunlight. No special dangerous goods classification; follow local transport regulations.
    Storage Store LyondellBasell Icorene 3545 ORE 3904 Polyethylene, Linear Low Density in a cool, dry, well-ventilated area. Keep containers closed, off the floor, and away from direct sunlight, heat, sparks, flames, and strong oxidizers. Protect from moisture, dust, and contamination. Prevent static buildup and follow good housekeeping. Use appropriate PPE and comply with local regulations/SDS. Store in original packaging.
    Shelf Life Shelf life is 24 months from date of manufacture when stored in original packaging in a cool, dry, well-ventilated area.
    Application of LyondellBasell Icorene 3545 ORE 3904 Polyethylene, Linear Low Density

    In rotational moulding of vertical chemical storage tanks, LyondellBasell Icorene 3545 ORE 3904 is charged as a dry polyolefin powder with a published density of 0.934 g/cm³ and a melt flow rate of 5.0 g/10 min measured under ISO 1133-1:2022 at 190 °C and 2.16 kg. The application boundary is set by ASTM D1998-21 for polyethylene upright storage tanks; chemical resistance, containment integrity and material identification are further evaluated under ASTM D543-21 and ISO 11469:2016. In tank fabrication, the base powder is charged at 100 wt%, with pigmented masterbatch metered at 2–4 wt% and closed-loop regrind held at 10–25 wt%; regrind is accepted only when dry-flow testing remains within the processor’s validated range. On shuttle-type biaxial rotational moulding machines with a primary-to-secondary axis speed ratio of 4:1 and a 2.5 m swing diameter, the oven set point is maintained at 280–300 °C while peak internal air temperature is controlled to 190–205 °C. Below 185 °C, unmelted powder persists at the wall-core interface; above 215 °C, oxidative pitting occurs at high-shear corners. Cooling begins with forced air at a moulded-part cooling rate of 5–10 °C/min until the demoulding temperature reaches 75–85 °C, followed by intermittent water mist only after the crystalline skin has solidified. The resulting components are vertical cylindrical storage tanks, cone-bottom mixer tanks, secondary containment basins and chemical dosing unit housings.

    Application ScenarioPrimary Compliance StandardsCritical Test or Design Methods
    Chemical storage tanksASTM D1998-21, ASTM D543-21, ISO 11469:2016Hydrostatic tank testing; chemical immersion; wall thickness mapping
    Agricultural water and fertigation reservoirsEN 13575:2012, NSF/ANSI/CAN 61Above-ground tank design; potable water contact testing
    Marine flotation componentsASTM D1693-15e1 Condition B, ISO 4892-3:2016, RoHS Directive 2011/65/EUEnvironmental stress crack resistance; accelerated weathering; restricted substance verification
    Playground equipmentEN 71-3:2019+A1:2021, ASTM F1487-21Element migration limits; public playground impact performance
    Insulated food handling containersFDA 21 CFR 177.1520(c), EU 10/2011Overall migration testing; food contact material compliance
    Material handling pallets and dunnageISO 8611-1:2011, IEC 61340-5-1Pallet load testing; electrostatic protection verification

    What Restricts Regrind Percentage When Rotational Moulding Fertigation Reservoirs From Butene LLDPE?

    The limiting factor in agricultural tank production is not melt flow but dry-flow loss and low-temperature impact reduction when regrind content exceeds 20 wt%. EN 13575:2012 governs rotationally moulded thermoplastic tanks for above-ground chemical storage, and NSF/ANSI/CAN 61 is applied when the reservoir is specified for potable water contact. For UV-opacity in long-duration outdoor service, carbon black masterbatch at 40% pigment loading is added at 2.0–2.5 wt%; regrind is capped at ≤20 wt%, and no slip aid is added because surface migration from slip additives reduces weld-line integrity. Closed-shell moulds for 2,000–20,000 L reservoirs are processed in carousel rotational moulding stations with oven residence times of 18–25 min; peak internal air temperature is held at 190–200 °C and wall thickness is maintained at 5–8 mm for hydrostatic loading. Terminal parts are sprayer tanks, fertigation reservoirs, mixing hoppers and potable water holding tanks.

    For marine flotation components, continuous brackish-water immersion and cyclic flexural loading make environmental stress crack resistance and post-moulding impact retention more decisive than short-term tensile strength. ASTM D1693-15e1 Condition B test data is used as the acceptance gate; ISO 4892-3:2016 is applied for UV weathering validation, and RoHS Directive 2011/65/EU Annex II is used for restricted substance verification. The shell formulation consists of 100 wt% base powder, 0.5–1.0 wt% high-molecular-mass HALS masterbatch and 2–3 wt% carbon black masterbatch; regrind is limited to 10–15 wt% because foam-filled buoy hulls require consistent wall density. Double-wall buoy shells are rotationally moulded, cooled below 60 °C, then filled with a two-component closed-cell polyurethane foam core at foam density 40–60 kg/m³; the exotherm is controlled below 85 °C to prevent inner wall softening. Published data for product-specific marine certification of this exact grade is limited; flotation devices must be project-tested for buoyancy retention and weathering. Terminal parts are aquaculture float collars, pontoon floats and navigation buoy hulls.

    Playground Rotomoulded Shells and the Influence of Polyurethane Foam Core Injection on Low-Temperature Impact

    The rotational moulding of slide shells, tunnel sections and climbing panels uses a cadmium-free organic pigment masterbatch at 3–5 wt%; regrind is added at 10–18 wt%, with the melt flow rate verified after each 500 kg of regrind incorporation under ISO 1133-1:2022. EN 71-3:2019+A1:2021 migration limits and ASTM F1487-21 public playground impact performance define the compliance envelope. Shell wall thickness is held at 3.5–5.0 mm before foam injection; a two-component polyurethane foam core is injected at 50–70 kg/m³ after the rotationally moulded shell has cooled to 55–65 °C. Moulds are run on three-axis rotational equipment with a secondary-axis reversal to distribute pigment and reduce knit-line visual defects. Terminal products are slide shells, crawl tunnels, climbing panels and modular play pods.

    ScenarioBase Polymer LoadingMasterbatch and RegrindKey Process Parameter
    Chemical storage tanks100 wt%2–4 wt% pigment; 10–25 wt% regrindPIAT 190–205 °C; forced-air cooling 5–10 °C/min
    Agricultural water tanks100 wt%2.0–2.5 wt% carbon black MB; ≤20 wt% regrindOven residence 18–25 min; PIAT 190–200 °C
    Marine flotation components100 wt%0.5–1.0 wt% HALS MB; 2–3 wt% carbon black MB; 10–15 wt% regrindFoam core 40–60 kg/m³; exotherm ≤85 °C
    Playground equipment100 wt%3–5 wt% organic pigment; 10–18 wt% regrindShell 3.5–5.0 mm; PU foam 50–70 kg/m³
    Food handling containers100 wt% neat2–4 wt% migration-tested MB or none; ≤25 wt% same-grade regrindInner wall ≥2.0 mm; foam fully encapsulated
    Material handling pallets100 wt%1–3 wt% antistatic MB; 2–4 wt% colour MB; ≤20 wt% regrindTwin-sheet or single-shot rotomoulding

    When Insulated Food Handling Containers Require Migration Compliance Under FDA 21 CFR 177.1520 and EU 10/2011

    The double-wall container is rotationally moulded using neat powder at 100 wt% for direct food contact surfaces; pigmented masterbatch at 2–4 wt% is accepted only when the supplier provides migration data under FDA 21 CFR 177.1520(c) and EU 10/2011, including the overall migration limit of 10 mg/dm². Regrind is limited to ≤25 wt% and must originate from the same food-contact grade and same production cell to prevent cross-contact with non-food formulations. The inner wall is maintained at 2.0 mm minimum thickness, the outer shell is rotationally moulded in a closed aluminium mould, and the cavity is filled with polyurethane foam that is completely encapsulated so that foam components do not contact food. Terminal parts are insulated fish tubs, dairy boxes, food bulk containers and cold-chain transport bins.

    Where closed-loop material handling requires washable, non-toxic dunnage with low warpage, Icorene 3545 ORE 3904 is formed into rotationally moulded pallets and separator sheets. ISO 8611-1:2011 pallet load testing and IEC 61340-5-1 electrostatic protection are applied when antistatic surfaces are specified. The base powder is charged at 100 wt%, with antistatic masterbatch at 1–3 wt%, colour masterbatch at 2–4 wt% and regrind at ≤20 wt%; the mixture is fed through a dry-flow hopper to a twin-sheet thermoforming or single-shot rotational moulding cell. The resulting items are industrial pallets, dunnage trays, separator sheets and insulated transport bases.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3545 ORE 3904 Polyethylene, Linear Low Density is identified as a grade designation within the Icorene series of ethylene-α-olefin copolymers. The suffix “ORE 3904” denotes a grade-specific formulation or stabilisation package, and public technical literature for this exact configuration is limited. Therefore, engineering values used for tool design, part qualification, or regulatory assessment should be taken from the current LyondellBasell product data sheet and the batch certificate of analysis rather than from generic LLDPE nominal values. The material class falls within the linear low density polyethylene density range of 0.918 to 0.940 g/cm3. The grade is commonly discussed in rotomoulding powder contexts, but the physical form, intended conversion process, and stabilisation package for the ORE 3904 variant must be confirmed with the supplier before specifying silo storage, feeding, grinding, or drying equipment.

    Specification Profile and Required Test Standards

    The specification framework for an LLDPE rotomoulding powder is built around melt mass-flow rate, density, environmental stress cracking resistance, low-temperature ductility, tensile properties, and powder particle size distribution. Melt mass-flow rate is reported at 190°C under a 2.16 kg load using ASTM D1238 or ISO 1133-1; this value controls whether the powder can flow into deep ribs, narrow cavity sections, and moulded-in inserts before the melt temperature reaches the oxidation limit. Density is measured by ASTM D1505 or ISO 1183-1. Environmental stress cracking resistance is commonly tested under ASTM D1693, Condition B, in 100% Igepal at 50°C. Low-temperature brittleness is assessed by ASTM D746 or ISO 974. Tensile yield strength and elongation at break are evaluated by ASTM D638 or ISO 527-2, and flexural modulus by ASTM D790 or ISO 178.

    Specification property Reference test method Typical reported parameter
    Melt mass-flow rate ASTM D1238 at 190°C/2.16 kg; ISO 1133-1 g/10 min
    Density ASTM D1505; ISO 1183-1 g/cm3
    Environmental stress cracking resistance ASTM D1693, Condition B h to F50 or % failure
    Low-temperature brittleness ASTM D746; ISO 974 °C
    Tensile elongation at break ASTM D638; ISO 527-2 %
    Flexural modulus ASTM D790; ISO 178 MPa
    Powder bulk density ASTM D1895 g/cm3 or kg/m3
    Particle size distribution ASTM D1921 sieve analysis % retained or passing

    On a production-scale shuttle arm or carousel rotational moulding line, the powder is charged into a heated mould and formed into a hollow shell by sequential melting and consolidation. Wall thickness distribution is controlled by powder dry flow, peak internal air temperature, mould surface temperature, and cooling rate. Fines below 100 µm can reduce bulk density and increase electrostatic adhesion to the mould surface, while coarse particles above 500 µm may remain unmelted in corners, ribs, and kiss-off regions. The sieve fraction between 35 mesh (500 µm) and 100 mesh (150 µm) is commonly monitored because it influences both powder flow and particle coalescence. Published data for this specific Icorene configuration is limited; an incoming-inspection plan should therefore include ASTM D1921 sieve analysis and ASTM D1895 bulk density on every lot, with acceptance limits derived from the supplier’s certificate of analysis and the moulder’s historical process capability.

    What Limits Rotational Moulding Cycle Efficiency in Icorene 3545 ORE 3904?

    Cycle efficiency is bounded by the temperature interval between particle coalescence and oxidative degradation. For LLDPE rotomoulding powders, oven set temperatures are commonly held between 260°C and 310°C, while the internal air temperature in the mould is raised to 190°C to 210°C. The upper limit is determined by oxidation-induced rheological shifts, discolouration, and pinhole formation; the lower limit is set by incomplete wetting at knit lines, corners, and inserts. Complex aluminium or steel tools may require internal air temperature control within ±5°C to avoid underflow at the parting line or excessive shrinkage in thick bosses. Cooling must be sequenced so that release occurs below the recrystallisation range, but not so rapidly that warpage exceeds drawing tolerance. Because published data for this exact configuration is limited, the oven profile and cooling ramp must be established on the actual moulding machine using an internal air probe and mould surface thermocouple rather than relying on class-level datasheet values.

    Polyethylene is not hygroscopic in the manner of polyamide or thermoplastic polyester, but condensation on cold powder can introduce steam marks and pinholes during melting. In high-humidity storage, powder should be allowed to reach ambient temperature before silo discharge, and hopper temperature should be maintained above the dew point. Regrind from post-industrial parts may be added only after verifying melt flow rate and sieve distribution. Regrind additions above 20 wt% can increase pinhole density and reduce environmental stress cracking resistance unless the regrind is screened to remove fines and thermally damaged particles, and unless the blend is re-qualified by ASTM D1238 and ASTM D1921.

    When Icorene 3545 ORE 3904 Is Compared with High-Pressure LDPE and HDPE

    Unlike high-pressure LDPE, which contains long-chain branching, linear low density polyethylene has a predominantly linear backbone with short-chain branches introduced by α-olefin comonomer. At equivalent melt flow rate and density, LLDPE typically provides higher tensile strength, puncture resistance, and environmental stress cracking resistance than LDPE, but lower melt strength during thermoforming and blow moulding. Compared with HDPE, LLDPE has lower flexural modulus, lower Vicat softening temperature, and higher low-temperature impact toughness. These differences arise from lower crystallinity and from the distribution of short-chain branches. The comparison below shows class-level values and is not a substitute for the official Icorene 3545 ORE 3904 datasheet.

    Material class Density range Typical flexural modulus ESCR tendency Melt strength
    High-pressure LDPE 0.910–0.930 g/cm3 150–350 MPa lower than LLDPE higher than LLDPE
    Linear low density polyethylene 0.918–0.940 g/cm3 350–800 MPa high moderate
    High-density polyethylene 0.941–0.965 g/cm3 900–1,500 MPa moderate low to moderate

    For outdoor hollow parts such as storage tanks, agricultural reservoirs, and industrial containment shells, the ORE 3904 suffix may indicate a stabiliser package selected for ultraviolet resistance. Stabilisation is not a permanent property; it is consumed by UV exposure, heat, and extraction. Parts intended for prolonged outdoor service must be tested under the proposed exposure conditions. Compliance statements for food-contact or potable-water service must be obtained in writing from LyondellBasell. Typical polyethylene grades are evaluated under FDA 21 CFR 177.1520, EU Regulation No 10/2011, REACH, and RoHS, but coverage for this exact grade should not be inferred from similarity to other LLDPE grades. Published data for this specific configuration is limited; therefore, mould-flow simulation, stacking calculations, and failure-mode analysis should use the production-lot certificate of analysis rather than generic class values. The operational boundary in prolonged outdoor service is set by stabiliser depletion rate, not by initial tensile property, and long-term heat ageing or accelerated weathering data is required for service-life prediction.

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