Lyondellbasell Icorene 3545 Gry 7749 Polyethylene Linear Low Density

LyondellBasell Icorene 3545 GRY 7749 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3545 GRY 7749 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 143688
    Density 0.934 g/cm3
    Melt Index 190 C 2 16 Kg 4.0 g/10 min
    Tensile Strength At Yield 18 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break 800%
    Flexural Modulus 690 MPa
    Hardness Shore D 55
    Vicat Softening Point 113 °C
    Melting Point 125 °C
    Brittleness Temperature -70 °C
    Uv Stabilization Yes
    Color Gray

    As an accredited LyondellBasell Icorene 3545 GRY 7749 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 GRY 7749 LLDPE is supplied in 25 kg polyethylene bags, 40 bags per 1,000 kg stretch-wrapped pallet.
    Container Loading (20′ FCL) 20′ FCL: LyondellBasell Icorene 3545 GRY 7749 LLDPE loaded in 25 kg bags, palletized, shrink-wrapped, and secured for ocean transport.
    Shipping LyondellBasell Icorene 3545 GRY 7749 Polyethylene, Linear Low Density, is shipped as non-hazardous polymer resin in 25 kg bags or bulk containers. It is not regulated for transport by DOT, IMDG, or IATA; no UN number, hazard class, or marine pollutant. Keep closed, dry, and away from heat.
    Storage Store LyondellBasell Icorene 3545 GRY 7749 Polyethylene, Linear Low Density in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed, labeled, and protected from moisture, contamination, and strong oxidizers. Prevent dust buildup; use grounding/bonding for bulk handling. Stack securely to avoid falling. Follow local regulations and the manufacturer’s SDS.
    Shelf Life Shelf life is typically 24 months when stored unopened in a cool, dry place, away from direct sunlight and heat.
    Application of LyondellBasell Icorene 3545 GRY 7749 Polyethylene, Linear Low Density

    Atmospheric chemical storage vessels in the 1,500–10,000 L class are produced from Icorene 3545 GRY 7749 LLDPE powder in uniaxial shuttle or biaxial carousel rotational moulding machines. With a nominal density in the 0.930–0.940 g/cm³ range to ISO 1183-1:2019 and a rotomoulding-grade melt flow rate between 3.5–5.0 g/10 min to ISO 1133-1:2022, the grade is supplied as a grey-compounded powder and is typically charged without additional pigment when the moulded grey is acceptable, because post-added masterbatch above 0.5 wt% shifts the sintering window and can delay bubble removal at the inner wall. Mould charging mass is calculated from part surface area and a target nominal wall thickness of 6–25 mm; for a 3,500 L vertical cylindrical tank, a charge of 68–75 kg is common depending on parting-line flash allowance. The mould is heated in an oven at 280–310 °C with continuous biaxial rotation at a 4:1–4.5:1 major/minor speed ratio. Internal air temperature measured by a Rotolog-type probe is held at 190–205 °C for 8–12 min; peaks above 210 °C produce an oxidised inner surface with a measurable loss of notched Izod impact from above 40 kJ/m² to below 25 kJ/m² when tested to ISO 180/A. Cooling proceeds with forced air to 120 °C, then water mist to 60 °C, followed by demoulding. Rapid water cooling through the crystallisation window between 95 °C and 65 °C reduces spherulite size but can lock in differential shrinkage in corners; a wall thickness taper of ±1.5 mm across the knuckle radius is considered actionable for tanks intended for outdoor hydrocarbon storage. Compliance is anchored to ASTM D1998-21 for upright polyethylene storage tanks, with additional chemical immersion testing to ISO 175:2021 for the specific stored fluid at operating temperature. Concentrated acids and strong oxidising agents require a prior permeability review because polyethylene is not intrinsically resistant to chlorinated solvents above 35 °C. Final parts are fitted with moulded-in threaded inserts and baffle brackets; field failures on production lines most often appear at overcured parting lines rather than as bulk wall fracture.

    What Limits ESCR Retention in Trailed Agricultural Sprayer Tanks Exposed to Emulsifiable Concentrates?

    Trailed and tractor-mounted pesticide sprayer tanks of 600–4,000 L are rotomoulded in grey LLDPE because the colour masks chemical staining from copper-based fungicides and iron chelates. The tank wall is typically 7–10 mm at the cylindrical body, increasing to 12–15 mm at inlet lid bosses. The moulding sequence uses a 4:1 rotational ratio and an internal air temperature of 195–205 °C; the lower limit prevents incomplete powder sintering at baffle bosses, while the upper limit avoids inner-wall oxidative degradation. Environmental stress crack resistance is assessed to ASTM D1693-15 Condition A using 10% Igepal CO-630 at 50 °C. Semi-concentrated emulsifiable formulations and non-ionic surfactants can reduce time to failure because the ethylene-alpha-olefin comonomer distribution leaves amorphous tie-chain regions susceptible to stress cracking under moulded-in residual stress. The tank interior is not flame-treated; weld-line integrity at the mould parting line is controlled by limiting external release agent application to 2–4 µm dry film thickness. Post-mould machining of lid threads at a router feed of 1,200–1,800 mm/min produces a sealing surface that is then fitted with an EPDM gasket. If the end user requires a darker grey for additional opacity, carbon black masterbatch addition above 1.0 wt% increases low-shear viscosity and extends oven residence time by 3–5 min, which can push the inner wall past the degradation threshold at thin-wall regions. UV retention following outdoor weathering is evaluated by ISO 4892-2:2021 Method A; the grey pigment alone does not provide full UV stabilisation unless the stabiliser package is confirmed on the batch certificate. Final products include boom sprayer main tanks, induction hoppers and hand-lance tanks; the primary warranty failures observed in this sector are stress cracks radiating from the tank base insert and lid-ring pinch welds rather than uniform wall thinning.

    Marine float bodies for pontoon docks, buoyancy collars and aquaculture pen walkways are produced with wall thicknesses of 9–25 mm and then filled with closed-cell polyurethane foam of core density 35–45 kg/m³. The rotomoulding cycle is extended relative to unfilled tanks by 15–20% because large flat mould sides dissipate heat unevenly across the parting line. Oven temperature is held at 285–305 °C; the internal air temperature must exceed 190 °C for at least 10 min at the deepest mould concavity to prevent pinholing along the metallic insert seat. After demoulding, 316 stainless steel M8–M12 inserts are installed; tightening torque is limited to 8–12 N·m because the ductile LLDPE matrix deforms at the knurled interface. Water absorption of the moulded skin is tested to ASTM D570-22 for 24 h; values above 0.02% indicate through-wall porosity at corners. The grey compound reduces solar surface temperature compared with black rotomoulding grades but still undergoes surface oxidation after prolonged UV exposure; xenon arc testing to ISO 4892-2:2021 for 2,000 h is used to confirm that elongation at break remains above 100%. In saltwater immersion, the LLDPE phase is largely inert, but the foam core is protected only if the shell remains crack-free; therefore notched Izod impact at −20 °C to ISO 180/A is specified as a lot acceptance test. End products include modular dock floats, mooring buoys and aquaculture walkways. The absence of post-mould welding seams on rotomoulded floats removes a common leak path observed in blow-moulded alternatives.

    When Demoulding Occurs Before the Inner Wall Reaches 60°C

    Insulated pallet boxes and cold-chain logistics totes for non-food temperature-sensitive payloads are rotomoulded as double-wall shells with 6–9 mm outer and inner skins and a 35–45 kg/m³ polyurethane core. The demoulding threshold is set by residual crystallinity: if the inner wall is removed from the tool below 60 °C, interior panel sink can reach 2–4 mm across a 1.2 m face. Forced-air cooling from 190 °C internal air temperature to 60 °C should proceed at 3–6 °C/min; water mist before the wall reaches 90 °C is avoided because rapid cooling across the crystallisation window can generate internal voids at the foam interface. The moulded shell is evaluated for stack load to ASTM D642-20 and for environmental stress crack resistance to ASTM D1693-15 Condition B after cleaning with quaternary ammonium disinfectant at 800 ppm. If food contact is required for the final payload, the grey grade must be tested against EU 10/2011 and FDA 21 CFR 177.1520; published data for this specific grey-pigmented Icorene configuration is limited, and a certificate of food-contact compliance should not be assumed from the natural LLDPE base alone. End products include pharmaceutical bulk totes, tissue sample transfer boxes and industrial ice-pack shipper shells. Moulded-in side walls with draft angles of 2–3° reduce vertical ejection force to below 1.5 kN; higher draft angles thin the upper wall beyond design tolerance.

    Outdoor Telemetry Cabinet Housings and Water Filtration Vessel Liners

    Rotomoulded outdoor enclosures for remote telemetry, water filtration vessels and dosing skid covers are built with 8–14 mm walls and integrated hinge bosses. The material is selected for UV exposure and chemical cleaning resistance; however, the LLDPE has no inherent flame retardancy and is rated only UL 94 HB, which excludes it from indoor electrical enclosure applications requiring V-2 or better. Sealing is achieved by post-mould CNC machining of a flat gasket groove, tested to IEC 60529 for IP65 with an EPDM seal compressed 0.8–1.2 mm. In water treatment vessels, exposure to 10 ppm free chlorine at 60 °C for 1,000 h followed by tensile testing to ASTM D638-22 is used to detect oxidative chain scission; elongation at break retention above 70% of the non-aged value is the acceptance limit. Any use in potable water contact requires a separate NSF/ANSI 61 evaluation of the grey pigment and stabiliser package because the LLDPE base resin alone does not confer automatic compliance. Moulded-in stainless-steel hinge plates are inserted at the charging stage; insert pull-out strength is verified to 10–15 N/mm² of interfacial surface area. The final products include field-mounted telecommunication cabinets, filter vessel housings and pump station covers, where warpage of the open side is controlled by demoulding only after the rim is below 55 °C. Batch-to-batch variation in pigment dispersion around the rim sealing area has been observed on production-scale machines as a ±0.3 mm surface flatness deviation, which is corrected by reducing the demoulding temperature or increasing mould release agent uniformity.

    Playground components and rotomoulded recreational accessories such as crawl tunnels, slide hoods, balance-beam shells and sandpit liners use Icorene 3545 GRY 7749 for its ductile impact behaviour at low temperature and grey moulded-in colour retention. These parts are designed to EN 1176-1:2023 for structural shell geometry; the polymer shell itself is not the energy-absorbing impact surface unless backed by foam or a resilient underlay. Wall thickness is maintained at 6–12 mm, with a minimum corner radius of 5 mm to limit stress concentration during high-rate impact; notched Izod impact at −20 °C to ISO 180/A is specified because playground equipment can be installed in alpine environments. UV retention is confirmed by ISO 4892-2:2021 for 3,000 h accelerated weathering; chalking of the grey surface is permitted only to the extent that it does not reduce the tensile elongation at break below 300%. The product is not suitable for indoor trampoline park features where flame-retardant polyurethane foam laminates are required under EN 13501-1 class B-s1,d0, because the LLDPE shell cannot achieve that classification without a fire-retardant coating that would compromise weld adhesion. Rotational moulding allows integrally moulded handles, hiding seams and attachment bosses; CNC trimming is limited to access ports where a 3 mm corner radius is retained. End products include outdoor playground tunnels, slide covers, sandbox shells and balance path segments. Field failure in recreational applications is most often linked to repeated UV exposure combined with mechanical abrasion at entry edges; design practice therefore adds 1.5–2 mm extra wall thickness at rim edges, which is not subtracted from the main wall thickness calculation.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3545 GRY 7749 is identified as a linear low-density polyethylene supplied in rotomolding powder form with a pre-compounded grey color package. The grade is based on an ethylene-alpha-olefin copolymer and is intended for rotational molding of hollow parts in which a balance of low-temperature impact, environmental stress-crack resistance and moderate flexural rigidity is required. The numerical designation 3545 separates the base resin melt flow and density from adjacent grades in the Icorene portfolio; GRY 7749 denotes the pigment formulation and does not define the polymer backbone. Typical application fields include storage tanks, agricultural and industrial containers, outdoor equipment housings, playground structures and general-purpose technical parts produced on biaxial rotational molding machines. The product is supplied as a pulverized powder rather than pellets, with particle size distribution controlled to support dry-flow and uniform wall thickness in clam shell, rock-and-roll and shuttle-type machines. Owing to the pigmented configuration, UV exposure and food-contact suitability require end-use validation under the relevant regulatory and weathering standards, including ISO 4892-2 for accelerated weathering and the applicable sections of 21 CFR 177.1520 only when confirmed by a grade-specific compliance letter.

    Does the 5.0 g/10 min Melt Flow Rate Limit Sintering in Thin-Wall Rotational Molding?

    The melt flow rate of the base resin is reported at 5.0 g/10 min when determined at 190°C and 2.16 kg according to ISO 1133-1:2022. This value places the material in the moderate-flow segment for rotomolding LLDPE and sets specific constraints on bubble removal and particle coalescence. Rotational molding relies on near-zero shear sintering of the powder against a heated mold surface; therefore melt flow rate alone is not a complete predictor of processability. Dry-flow, bulk density and particle size distribution are equally significant. For this grade, the powder form is controlled by sieving methods such as ASTM D1921 or equivalent optical particle analysis; typical rotomolding distributions retain a median particle size near 250–350 μm with a fraction below 150 μm limited to reduce fines generation. Bulk density is commonly measured by ISO 60 or ASTM D1895, and production-grade rotomolding powders generally fall between 0.35 g/cm³ and 0.45 g/cm³. A narrow particle-size distribution with adequate fines aids corner filling in complex tooling, but excessive fines can trap air and create pinholes. In the presence of relative humidity above 60%, moisture adsorption on powder surfaces may increase surface defects; pre-conditioning or dry-air storage is therefore required before processing.

    For mechanical design, the unpigmented base resin exhibits a density of 0.934 g/cm³ by ISO 1183-1 and a flexural modulus near 600 MPa by ISO 178. The combination of moderate density and short-chain branching yields a part that is less rigid than a high-density polyethylene rotomolding grade but offers improved crack resistance under repeated loading. Table 1 summarizes indicative physical and mechanical values for the base resin. The presence of the GRY 7749 colorant may shift density and tensile values slightly; published data for this specific pigmented configuration is limited, and property comparisons should be based on molded specimens, not powder values alone.

    Indicative characteristics for Icorene 3545 base resin
    PropertyTypical valueTest method
    Density0.934 g/cm³ISO 1183-1
    Melt flow rate at 190°C/2.16 kg5.0 g/10 minISO 1133-1:2022
    Tensile yield strength17 MPaISO 527-2
    Flexural modulus600 MPaISO 178
    Elongation at break400%ISO 527-2
    ESCR, 50°C / 100% Igepal>1000 hASTM D1693, Condition B

    The environmental stress-crack resistance value of >1000 h by ASTM D1693, Condition B, 50°C / 100% Igepal, is a key differentiator for chemical tanks and detergent reservoirs. The elongation-at-break value near 400% by ISO 527-2 indicates ductile behavior at ambient temperature; this ductility persists at low temperatures where the material is commonly assessed by falling-weight impact tests, but the exact low-temperature impact energy depends on part wall thickness, cooling rate and pigment dispersion. The GRY 7749 grey formulation can improve long-term outdoor appearance retention compared with natural unpigmented powder when exposed to UV light, but weathering resistance is controlled by the stabilizer package and cannot be inferred from color alone. For outdoor parts, validation according to ISO 4892-2 and ISO 4892-3 is required.

    If the Peak Internal Air Temperature Falls Below 190°C or Rises Above 230°C, Which Failure Modes Emerge?

    In rotational molding, the critical processing window is defined less by the oven setpoint than by the peak internal air temperature reached inside the hollow tool. For Icorene 3545-class LLDPE, the practical PIAT window is approximately 190°C to 220°C. If PIAT remains below 190°C, particle sintering may be incomplete. Incompletely coalesced powder leaves spherical voids at the inner surface, lowers tensile strength and produces a rough internal finish; impact failure often initiates at these residual particle boundaries. If PIAT exceeds 230°C, oxidative degradation accelerates. The carbonyl index measured by infrared spectroscopy increases, and the internal surface may yellow or brown; flexural modulus and impact strength decline non-linearly. On production-scale biaxial machines, a deviation of +10°C in oven air temperature can raise PIAT by 5–8°C, moving a part near the upper limit of the window into degradation. The use of internal air temperature probes and infrared mold sensors is therefore essential. Mold release coatings based on silicone or PTFE must be applied within the supplier’s recommended film thickness, because excess release agent can migrate into the LLDPE surface and reduce paint adhesion or weld-line strength. Cooling rate also influences warpage and shrinkage. Parts demolded at temperatures above 70°C can distort during post-mold cooling; forced-air cooling with rotation continued through the crystallization range reduces dimensional variation. The grade’s moderate melt flow rate makes it less tolerant of short sintering cycles than a 6.5–8.0 g/10 min rotomolding LLDPE, but the trade-off is a higher ESCR plateau after proper curing.

    Compared with a conventional LDPE homopolymer rotomolding powder, Icorene 3545 has a linear backbone with short-chain branches rather than a highly branched architecture. The density of 0.934 g/cm³ and the α-olefin comonomer yield higher tensile yield strength and greater environmental stress-crack resistance than many LDPE grades of equivalent melt flow. Compared with an HDPE rotomolding powder of 0.945 g/cm³ or higher, the lower density and lower flexural modulus reduce stiffness and allow more deformation before fracture; this behavior is preferable in tanks subject to soil movement or impact. When evaluated against a hexene- or octene-based LLDPE rotomolding resin, a butene-based grade such as this one generally shows lower low-temperature toughness and lower ESCR at equivalent density and melt flow. The selection therefore depends on whether the part is regulated by ASTM D1998 for tanks or by impact classifications under ISO 179-1/ISO 179-2. The GRY 7749 pre-colored form differs from natural powder combined with a masterbatch by eliminating on-site pigment weighing and reducing lot-to-lot color variation, but it limits the molder’s ability to adjust color strength and may require a dedicated cleaning procedure when switching to light-colored parts. Published data for this specific configuration is limited for chemical resistance to aggressive oxidizing agents; validation using the intended chemical mixture and ASTM D543 is required.

    Quality control for rotomolding powder typically includes lot-by-lot verification of melt flow rate, density, particle size distribution, bulk density and colorimetric coordinates. The base resin is supplied with a certificate of analysis; the pigmented grade should be stored in sealed containers away from direct sunlight and moisture. Processing environments with RH above 60% require pre-drying or controlled storage because surface water can generate bubbles. For occupational hygiene, airborne dust from handling polyethylene powder should be controlled; the powder is combustible as a dust cloud, and equipment should be grounded to avoid electrostatic discharge. Regulatory compliance must be confirmed for the final article rather than the raw material alone. The base polyolefin may meet the olefin polymer requirements of 21 CFR 177.1520 for food-contact use, but the grey colorant package must be covered by a separate suitability confirmation. European Union end-use compliance is assessed under REACH and RoHS Directive 2011/65/EU; these obligations apply to the final compounded article and its handling supply chain. For outdoor weathering, direct correlation between accelerated xenon-arc testing by ISO 4892-2 and field performance in the target climate must be established before final part sign-off.

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