Lyondellbasell Icorene 3545 Uv Gry 7816 Polyethylene Linear Low Density

LyondellBasell Icorene 3545 UV+ GRY 7816 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3545 UV+ GRY 7816 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 489878
    Polymer Type Linear Low Density Polyethylene
    Density 0.935 g/cc
    Melt Flow Rate 4.5 g/10 min
    Tensile Strength At Yield 10.0 MPa
    Tensile Strength At Break 15.0 MPa
    Elongation At Break 700 %
    Flexural Modulus 0.300 GPa
    Izod Impact Strength Notched 1.00 J/cm
    Vicat Softening Point 95.0 °C
    Brittleness Temperature -70.0 °C
    Thermal Expansion Coefficient 1.50E-4 1/°C
    Hardness Shore D 50
    Uv Stabilization Yes
    Color Gray

    As an accredited LyondellBasell Icorene 3545 UV+ GRY 7816 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 UV+ GRY 7816 is supplied in 25 kg polyethylene bags, palletized and stretch-wrapped for shipment.
    Container Loading (20′ FCL) 20′ FCL loading of LyondellBasell Icorene 3545 UV+ GRY 7816 Linear Low Density Polyethylene; palletized, secured, and stowed for transport.
    Shipping LyondellBasell Icorene 3545 UV+ GRY 7816 Polyethylene, Linear Low Density, ships as non-hazardous, free-flowing pellets in moisture-barrier bags or octabins on pallets. Keep dry, cool, and away from direct sunlight. Transport in covered trucks/containers; no special ventilation required. Follow local regulations, retain SDS/labels, and stack securely.
    Storage Store indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and ignition sources. Keep LyondellBasell Icorene 3545 UV+ GRY 7816 Polyethylene, Linear Low Density, in sealed, labeled original containers. Protect from moisture, dust, and static; stack securely, avoid prolonged UV exposure, and separate from strong oxidizers and acids. Follow the SDS. Use first-in, first-out rotation.
    Shelf Life Typically 24 months from manufacture when stored unopened in a cool, dry, well-ventilated area, away from direct sunlight and moisture.
    Application of LyondellBasell Icorene 3545 UV+ GRY 7816 Polyethylene, Linear Low Density

    Long-Term Dilute Pesticide Contact in Rotomoulded Chemical Vessels

    LyondellBasell Icorene 3545 UV+ GRY 7816, a linear low density polyethylene, is processed on carousel-type rotational moulding machines for agricultural crop-protection and fertiliser storage tanks. The grade is specified with a density of 0.938 g/cm³ by ISO 1183-1:2019 and a melt flow rate of 4.5 g/10 min by ISO 1133-1:2022 at 190 °C/2.16 kg. The compound is pre-coloured grey and UV-stabilised. No additional hindered amine light stabiliser masterbatch is required at the moulding machine. Clean in-house regrind from the same grade is permitted up to 10 wt% in the charge. Above 10 wt% regrind, low-temperature impact retention under ISO 179-1:2010 type 1 eA exhibits measurable batch-to-batch variation. The rotational moulding charge is pulverised to a 35 mesh nominal top size. Oven set-points are held at 275–290 °C. Peak internal air temperature for an 8–10 mm wall is controlled at 185–195 °C. Demoulding below 80 °C internal air temperature prevents post-mould warpage. For 500 L vessels, the heat cycle is typically 22–26 min. For 5,000 L vessels, the heat cycle extends to 38–45 min. The cooling phase is air-forced for 15–20 min, followed by water mist cooling. Too rapid water quenching below 60 °C has been associated with shrinkage variation across mould parting lines. The moulded density of the tank wall is checked by ISO 1183-1:2019 and should not fall below 0.930 g/cm³. Finished products include 500–5,000 L conical tanks, sump trays, and dosing vessels. Chemical compatibility is evaluated by immersion in 20 wt% ammonium nitrate and 5 wt% diammonium phosphate solutions at 40 °C for 30 days. The acceptance criterion is no leaching-induced cracking and less than 1.0 % mass change. The relevant product standard is EN 13575:2012 for thermoplastic tanks used for liquid chemicals above ground. Stress crack resistance is specified as greater than 1,000 h by ASTM D1693-15 Condition A, using a notched specimen in 10 % Igepal CO-630 at 50 °C. Each tank design must pass the hydrostatic pressure test at 1.1 times maximum service head as defined in EN 13575:2012 clause 6.3. Moulders should reject any lot with surface pitting deeper than 0.5 mm in the liquid-holding area. Pits act as stress concentrators and reduce the effective ESCR life of dilute pesticide contact surfaces.

    In marine buoyancy and floating dock pontoon construction, the grey compound enters service where saltwater immersion and continuous solar exposure act simultaneously. The one-piece shell is rotationally moulded with a wall thickness of 5–8 mm, then filled with closed-cell semi-rigid polyurethane foam of 28–32 kg/m³ apparent density. The foam fill raises reserve buoyancy. The polyethylene shell is not painted. The grey UV-stabilised skin provides weathering resistance under ISO 4892-2:2013 cycle 1, with chalking assessed by ISO 4628-6:2016. Low water absorption of linear low density polyethylene, typically below 0.01 % by ISO 62:2008, prevents salt uptake. External recycled polyethylene streams are excluded because mixed colourants and unknown stabiliser packages shift the low-temperature ductile-brittle transition under ISO 179-1:2010. Finished products include 200–1,500 mm diameter mooring buoys, floating dock end caps, and fish farm pen float collars. Cold-water impact resistance is inspected by a 9 kg drop weight at -20 °C using ISO 6603-2:2000. The shell must show ductile punch deformation without through-thickness crack. Each foam-filled assembly is subjected to a 24 h submersion leak test under 0.2 bar internal overpressure.

    What Changes When EN 1176 Impact Attenuation Is Applied to Rotomoulded Playground Components?

    Outdoor playground panels, tunnel sections, and slide shells made from Icorene 3545 UV+ GRY 7816 are designed against fall impact and long-term surface weathering. The grade's pre-coloured grey body is rotationally moulded at 6–10 mm nominal wall thickness. Tooling design must avoid sharp transitions at metal insert bosses. Stress concentrations at threaded inserts account for the majority of field failures. In production, the powder charge is compounded with no additional colourant. The GRY 7816 grey code is integral to the polymer matrix. Colour uniformity is checked by spectrophotometric measurement against the manufacturer's master standard at every 25th moulding cycle. Surface chalking is assessed after accelerated weathering under ISO 4892-2:2013 cycle 1. The requirement is no visible surface powder at 3,000 h. Mechanical validation follows EN 1176-1:2017 clause 4.2 for impact attenuation and ASTM F1487-21 for public-use playground equipment. Head injury criterion must not exceed 1,000 in the fall height test. The g-max value is kept below 200 g. Terminal products include 1.0–3.5 m slide segments, crawl tunnel sections, and shelter roof panels. The moulder must verify the grey polyolefin against EN 71-3:2019 migration of certain elements when the product is sold as a toy or accessible playground component. The UV-stabilised base polyethylene is olefinic. FDA 21 CFR 177.1520(c) covers the bulk polymer for food contact, but the grey pigment system requires separate verification for any food-contact claim. Field experience with threaded brass or steel inserts indicates that boss thickness should be at least 2.0 times the nominal wall thickness. Knurled inserts should not be inserted without thermal expansion relief. In rotomoulded slide shells, the critical zone is the transition from the sidewall to the base radius. Radius-to-thickness ratio below 5:1 may create a cold-flow region and reduce impact resistance. Published data for this specific configuration is limited. Moulders should therefore verify each tool geometry by drop-weight test at the design fall height and record the failure mode.

    When Rainwater Harvesting Tanks Require Non-Potable Outdoor Durability

    Above-ground rainwater retention and fire reserve tanks use the grey grade for the outer shell and lid where the service environment is non-potable and UV-exposed. Rotomoulding on shuttle-type machines with 3.0–4.5 m major axis requires a wall thickness of 7–12 mm for vertical tanks from 2,000 to 20,000 L. The charge is heated until internal air temperature reaches 190–200 °C. Soak time is 8–12 min per 10 mm wall. Tanks are demoulded at 70–80 °C. The UV+ stabiliser package eliminates the need for post-mould painting. Solvent-borne painting is not recommended. Adhesion to linear low density polyethylene is poor without corona or plasma treatment. If potable water use is intended, the grey pigment and the stabiliser system must be screened against AS/NZS 4020:2018 for taste, odour, and mutagenic potential. The bulk olefin polymer is covered by 21 CFR 177.1520(c), but the pre-coloured grey compound is not automatically cleared under that citation. Terminal products are vertical cylindrical tanks, slimline rainwater cells, and fire reserve tanks with moulded-in fittings. Hydrostatic burst testing is performed at 2.0 times the maximum working head for 1 h. The shell must not rupture or leak at the boss welds.

    Rotational moulding of highway delineator bases, water-filled barrier shells, and traffic sign feet uses the impact recovery and creep resistance of the grey linear low density polyethylene. Wall thickness ranges from 8 mm for sign bases to 15–20 mm for water ballast barrier segments. The low-speed impact scenario is evaluated by damage mode rather than by full containment. The shells must buckle or dent without releasing loose fragments. Production equipment includes carousel and rock-and-roll machines with gas-fired ovens. Charge weight is controlled to ±0.5 wt% of nominal shot mass. Wall thickness distribution is held within ±1.5 mm across the mould. The grey compound is not blended with external post-consumer polypropylene. Incompatible phases reduce impact strength under ISO 6603-2:2000. Finished products include 100–1,000 L water-filled barriers, 500 mm square sign bases, and 500–2,000 mm cylindrical delineator shafts. Weathering requirement follows ISO 4892-2:2013 cycle 1 with 2,000 h exposure. Tensile elongation at break must retain at least 60 % of the unexposed value when tested by ISO 527-2:2012 type 1B. Published data for this specific configuration is limited. Road authorities may require additional solar exposure panels under ISO 877-1:2009 Method A for site-specific validation.

    Industrial Waste Container Walls and Forklift Impact Zones

    Solid waste bins and pallet boxes in industrial yard applications are rotationally moulded from Icorene 3545 UV+ GRY 7816. The wall thickness in the base and forklift pockets is increased to 12–16 mm, while sidewalls are held at 6–8 mm. The melt flow rate of 4.5 g/10 min allows the compound to fill tight-radius corners on large flat-panel tools without excessive porosity. Clean in-house regrind from failure-free waste bin trim is added at a maximum ratio of 10 wt%. This maintains lot-to-lot low-temperature impact consistency. External recycled LLDPE is excluded. Uncontrolled carbon black and stabiliser residues shift the oxidative induction time measured by ISO 11357-6:2018. Terminal products include 120–1,100 L two-wheel and four-wheel bins, 1.5–3.0 m³ pallet boxes, and 30–100 L pharmaceutical waste containers. Smaller containers are tested by a top edge drop from 1.2 m at -18 °C. Larger bins are subjected to a 25 kg impact from a hemispherical striker at -20 °C under ISO 6603-2:2000. The design must withstand repeated fork truck insertion without cracking at the moulded fork pockets. Thermoformed insert plates made of the same grey LLDPE are sometimes used to reinforce the lower lip. Since the material is pre-coloured grey, post-mould regrind of rejected bins is re-pulverised and reintroduced in-house at up to 10 wt%. The compliance framework for hazardous waste packs may include UN 1H2 testing for solid waste packagings in accordance with ADR 2025 or 49 CFR 178.606, depending on destination. The base polymer is olefinic and falls under 21 CFR 177.1520(c). The grey pigment package requires separate audit for food or pharmaceutical contact.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3545 UV+ GRY 7816 Polyethylene, Linear Low Density is supplied as a precoloured rotational moulding powder. The designation separates the base polyolefin from the weathering additive package and the grey pigment code: Icorene 3545 identifies the LLDPE backbone, UV+ denotes the ultraviolet stabilization system, and GRY 7816 specifies the grey colourant. The material is intended for biaxial rotational moulding equipment in which powder is charged into a closed mould, rotated simultaneously about two perpendicular axes, and heated until the polymer particles sinter into a void-free layer. Under ISO 1043-1, the base resin is classified as PE-LLD.

    Rheological and density data are measured under controlled laboratory conditions. Melt mass-flow rate is determined by ISO 1133-1 at 190 °C with a 2.16 kg load, while density is assessed by ISO 1183-1 Method A. The grade is positioned near a nominal density of 0.935 g/cm³, with melt flow rate typically controlled in the range 3.5–4.5 g/10 min. The combination of low density and moderate melt flow rate promotes sintering without the excessive sag associated with high-flow grades. Powder particle size distribution also influences process behaviour: the product is normally screened through 35 mesh (500 µm) openings, with the fines fraction below 150 µm improving particle coalescence while potentially reducing bulk density and increasing static adhesion in low-humidity conditions. Dry flow properties should be verified according to ISO 6186 or equivalent hopper-flow test methods before long production runs.

    What Processing Envelope Governs Rotational Moulding with Icorene 3545 UV+ GRY 7816?

    On shuttle and carousel machines with forced-air oven circulation, mould wall temperature and internal air temperature are the primary process variables. The powder bed adjacent to the mould surface begins to sinter when the internal air temperature reaches approximately 120–135 °C. Complete densification of a 5 mm wall section is normally achieved at a peak internal air temperature of 200–220 °C. A practical production window of ±5 °C around the established peak air temperature is maintained because the material shows a distinct cliff-edge in appearance and performance outside this band. Exceeding 240 °C for extended dwell initiates oxidative degradation, visible as yellowing, surface embrittlement, or a rough inner surface. Falling below 190 °C produces incomplete sintering, retained powder morphology, and pin-holing. Oven set points are typically 260–315 °C, with dwell time adjusted for part mass, mould material, and wall section. Aluminium moulds with 8–10 mm wall thickness reach the target internal air temperature faster than steel moulds, and thermocouple validation through the mould wall is required on production-scale equipment.

    Cooling rate after demoulding or in-mould cooling alters crystallite size, shrinkage, and dimensional stability. Forced-air cooling produces higher crystallinity and greater shrinkage; water mist cooling accelerates cycle time but increases the risk of warpage in asymmetric parts. Dimensional evaluations are conditioned at 23 ± 2 °C and 50 ± 5 % relative humidity according to ISO 291. Mould shrinkage is measured on prototype plaques, and the value depends on wall thickness, cooling rate, and the proportion of regrind. Because the grey pigment can absorb radiant energy differently from natural grades, oven dwell time should be re-established whenever the same mould is run in natural and grey formulations.

    Mechanical Response After Rotomoulding and Slow Cooling

    Mechanical testing is performed on rotomoulded plaques rather than injection-moulded specimens because skin orientation, porosity distribution, and residual thermal history differ. Tensile yield stress and elongation at break are evaluated under ISO 527-2; flexural modulus is determined by ISO 178. The linear low density backbone provides a lower flexural modulus than high density polyethylene at comparable density, while retaining higher impact resistance at sub-zero temperatures. Impact resistance for rotomoulded parts is commonly assessed by the Association of Rotational Molders low-temperature dart impact method or ASTM D3763; the actual values depend on wall thickness, cooling rate, and the proportion of recycled in-house material. Quantitative lot-specific minimum values for ARM impact and environmental stress-crack resistance hours are retained in the supplier’s certificate of analysis. Published data for this specific grey configuration is limited, so qualification should be carried out on prototype parts.

    Environmental stress-crack resistance is characterized by ASTM D1693, condition B, in 10 % Igepal CO-630 at 50 °C. The material is selected for detergent and fuel tanks that require resistance to stress cracking under hoop stress and intermittent thermal cycling. Chemical exposure is assessed under ISO 175 at 23 °C for 7 days. The grade resists continuous contact with aqueous solutions of inorganic acids, alkalis, and many detergent formulations. Strong oxidizing acids, chlorinated solvents, and aromatic hydrocarbons extract low-molecular-weight fractions and cause swelling; these service conditions require prototype testing before specification.

    When Outdoor Exposure and Colour Retention Are Assessed

    UV+ denotes a stabilizer package intended for exterior service. Accelerated weathering is commonly run under ISO 4892-2 xenon arc conditions with daylight filters and a black standard temperature of 65 ± 3 °C. The grey 7816 pigmentation contributes opacity and reduces visible chalking from surface oxidation; however, it does not convert the polyethylene into a high-temperature polymer. Colour change is measured under ISO 7724 or ASTM D2244. Acceptable ΔE values vary by application; for this specific grey formulation, supplier lot certificates and outdoor exposure trials are required for quantitative service life claims. Parts that operate under continuous UV exposure in hot climates may experience surface microcracking before bulk mechanical failure if the stabilizer package is depleted by prolonged heat oxidation.

    Compared with unpigmented Icorene 3545, the GRY 7816 precolour introduces a minor reduction in tensile strength and a slight shift in shrinkage due to pigment nucleation. Rotational moulders often report that dark grey parts require longer heating because lighter colours and natural grades reflect more infrared radiation. The exact oven time must be established with the same mould geometry and shot weight. Compared with a similar-density HDPE rotational moulding grade, Icorene 3545 UV+ GRY 7816 exhibits higher impact and environmental stress-crack resistance but lower bending stiffness. It is therefore used for large outdoor tanks, agricultural storage, and equipment housings where low-temperature toughness and chemical resistance are more important than load-bearing rigidity.

    Comparative Position Among Polyethylene Rotomoulding Grades

    The table below compares the general property classes relevant to material substitution decisions. Values are indicative and must not replace supplier-certified lot data.

    Property-class comparison framework for rotomoulding grade selection
    Property classIcorene 3545 UV+ GRY 7816Unfilled HDPE rotomouldingConventional butene LLDPE
    Density by ISO 1183-10.935 g/cm³ nominal0.940–0.950 g/cm³0.930–0.940 g/cm³
    Low-temperature impactHigher than HDPELowerModerate to high
    Flexural stiffnessModerateHigherModerate
    ESCR by ASTM D1693HighModerateModerate to high

    Powder storage at relative humidity above 60 % can introduce surface moisture that appears as microporosity or surface roughness during sintering. A pre-drying step of 70 °C for 1–2 h in a dehumidified air hopper is recommended when ambient humidity exceeds that threshold. Regrind additions above 20 % of shot weight may reduce impact and shift colour, depending on grind quality and thermal history. The precoloured grey grade should not be dry blended with other colour concentrates without a compatibility check because different carrier resins can create unmelted agglomerates on the inner surface.

    Regulatory status for food-contact use is assessed under FDA 21 CFR 177.1520 for olefin polymers, with the specific pigment package requiring separate evaluation. European Union food-contact compliance is evaluated under EU Regulation 10/2011; the grey pigment and UV stabilizers must be listed or covered by national approvals. The grade is supplied in accordance with European REACH registration obligations, and the absence of lead, cadmium, mercury, and hexavalent chromium is verified under IEC 62321 or equivalent RoHS test protocols. Melt mass-flow rate and density certifications are normally reported on the supplier certificate of analysis according to ISO 1133-1 and ISO 1183-1.

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