Lyondellbasell Icorene 3545 Grn 6670 Polyethylene Linear Low Density

LyondellBasell Icorene 3545 GRN 6670 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3545 GRN 6670 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 607338
    Density 0.935 g/cm³
    Melt Flow Rate 4.5 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 17.2 MPa
    Tensile Strength At Break 17.2 MPa
    Elongation At Break 700%
    Flexural Modulus 0.800 GPa
    Hardness Shore D 55
    Vicat Softening Point 110 °C
    Brittleness Temperature < -70 °C
    Environmental Stress Crack Resistance >1000 hr
    Color Green
    Form Pellets
    Processing Method Rotational Molding
    Uv Stabilizer Yes

    As an accredited LyondellBasell Icorene 3545 GRN 6670 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 GRN 6670 is supplied in 25 kg bags, palletized and stretch-wrapped for industrial storage.
    Container Loading (20′ FCL) 20′ FCL container loaded with LyondellBasell Icorene 3545 GRN 6670 Polyethylene, Linear Low Density, palletized bags, stowed for ocean freight.
    Shipping LyondellBasell Icorene 3545 GRN 6670 Polyethylene, Linear Low Density is shipped as non-hazardous solid pellets, typically in moisture-resistant 25 kg bags or 1,000 kg jumbo bags, palletized and stretch-wrapped. Transport in clean, dry trucks or containers; avoid heat, moisture, contamination, and direct sunlight. No special UN hazard classification required.
    Storage Store LyondellBasell Icorene 3545 GRN 6670 Polyethylene, Linear Low Density in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original containers or bags tightly closed to prevent moisture, dust, and contamination. Do not smoke. Use proper grounding if handling bulk, maintain stable ambient temperature, avoid prolonged UV exposure, and follow supplier SDS recommendations.
    Shelf Life Store cool, dry, and sealed, away from UV; typical shelf life is 24 months under recommended storage conditions.
    Application of LyondellBasell Icorene 3545 GRN 6670 Polyethylene, Linear Low Density

    Rotomoulded saddle tanks and vertical storage units for agricultural crop-protection chemicals are produced from Icorene 3545 GRN 6670 because the linear-low-density backbone maintains an environmental stress-cracking response under dilute fertilizer and pesticide contact without the higher density penalty of high-density polyethylene. The green-compounded 6670 designation supplies integral colourant, but processors servicing row-crop sprayer original equipment manufacturers often tumble-blend the powder with 0.2–0.5 wt% of a hindered amine light stabilizer masterbatch and 0.1–0.3 wt% of a phosphite process stabilizer prior to mould charging; dry blending in a low-shear ribbon blender for 15–20 min prevents additive stratification in the powder hopper. Formulation variables are validated against ASTM D1693-15 condition B for environmental stress-cracking resistance and ASTM D638-14 Type IV tensile yield after 1,000 h of ISO 4892-2:2013 cycle 1 accelerated weathering. Hydrostatic tank integrity is evaluated under ASTM D1998-15 for upright polyethylene storage vessels, while sprayer-mounted units are assessed in accordance with the tank portion of ISO 16119-1:2013. Production on a 2.8 m swing-arm rotomoulding machine uses cast aluminium tooling preheated to 60–70 °C; the mould rotates at a 4:1 ratio with primary arm speed 2–4 rpm and secondary axis 0.5–1.0 rpm. For nominal wall thickness of 5–8 mm, oven setpoint is 280–295 °C and peak internal air temperature is held at 185–195 °C for 3–5 min. Experience on field-scale lines shows that a thermocouple inserted through the mould wall can lag the internal melt by 6–10 °C during the final ramp, so operators must calibrate peak internal air temperature against destructive wall-section analysis rather than relying solely on oven air temperature. Cooling is sequenced from forced air to water mist when the mould surface reaches 90 °C, with part removal below 60 °C; extracting above 65 °C distorts the sump flange, and over-chilling below 50 °C may cause mould-release cracking in thick sump walls. Terminal products include 1,000–15,000 L vertical storage tanks, 500–1,800 L saddle tanks for boom sprayers, induction rinse hoppers, chemical induction bowls, and secondary containment basins.

    Why Does Potable-Water Contact Certification Constrain Post-Consumer Recyclate Loading in Rotomoulded LLDPE?

    Potable water tanks rotomoulded from Icorene 3545 GRN 6670 cannot automatically inherit drinking-water contact compliance from the resin datasheet; certification attaches to the finished rotomoulded article after formulation-specific extraction testing under NSF/ANSI/CAN 61 for North American installations or via migration testing under EN 12873-1:2014 when European Drinking Water Directive 98/83/EC conformity is required. This constraint limits post-consumer recyclate addition to 0–20 wt% in practice, with many high-regulatory-control producers retaining 100 % virgin Icorene 3545 GRN 6670 plus 0.2–0.4 wt% of a phenolic antioxidant and 0.1–0.3 wt% of an acid scavenger masterbatch to preserve low extractables. Stored powder should be kept above 10 °C and below 60 % relative humidity to avoid surface condensation, because moisture on the powder bed can produce surface pits in thick cylindrical walls. The process window for water tanks is shifted toward slower cooling rather than fast cycle time, because a 190–195 °C peak internal air temperature and forced-air cooling at 0.5–1.5 °C/min through the crystallisation region reduce residual shrinkage and flange warpage in capacities up to 10,000 L. Moulds are rotated at 3:1 or 4:1 ratio, oven setpoint is 270–300 °C, and wall thickness is held at 4–8 mm for cylindrical bodies; base corners are intentionally radiused to 25–50 mm to avoid stress concentration. Published data for this specific green-compounded moulding grade in 10,000 L potable-water tank certification is limited; tank manufacturers therefore qualify each tooling set by running extraction coupons from the actual mould surface and not from compression-moulded plaques. Terminal products include 500–10,000 L potable water storage tanks, loft tanks, emergency water reservoirs, and low-pressure process water vessels.

    For all-plastic intermediate bulk containers and process hoppers, the 31H1 certification path under UN recommendations for dangerous goods transport imposes a cold-conditioned drop test and stack-load test that are more severe than ordinary warehouse service. Icorene 3545 GRN 6670 is processed as a single-wall rotomoulded body with nominal wall thickness 6–10 mm; the mould is charged with 0.3–0.8 wt% of a UV-stabiliser masterbatch and 0.1–0.3 wt% of an internal mould-release additive, but filler or calcium carbonate is omitted because even 2.0 wt% rigid filler can lower environmental stress-cracking resistance under ASTM D1693-15 condition B. The moulding cycle uses an oven setpoint of 285–305 °C and a peak internal air temperature of 190–195 °C; after the sintering plateau, the mould is transferred to a cooling station where forced air reduces the outer surface to 80 °C before water fog is applied. Processors observe that an over-fast water quench across thick base ribs creates differential crystallinity between the rib root and the flat bottom, leading to stack-test creep at 40 °C in a 1,000 L intermediate bulk container loaded to 1.8 times the rated gross mass. Therefore, cooling in the base rib area is monitored with mould-mounted surface thermocouples; demoulding is inhibited until the rib surface is below 70 °C. Terminal product types include 1,000 L all-plastic 31H1 intermediate bulk containers, 1,250 L cylindrical liquid intermediate bulk containers, 500 L chemical tanks with integral pallet feet, and bulk solids hoppers with outlet cone sections.

    When Kayak Hull Mouldings Demand Post-Ageing Impact Thresholds Above 200 kJ/m²

    Kayak hulls and marine flotation bodies moulded from Icorene 3545 GRN 6670 are evaluated for post-ageing impact resistance rather than solely as-moulded impact because the green pigmented surface can mask micro-cracking that develops after 1,000 h of accelerated UV exposure. The formulation typically combines 0.3–0.6 wt% of a UVA/HALS masterbatch with 0.2–0.4 wt% of an antioxidant masterbatch; in natural-resin replacements, 0.5–1.5 wt% of a high-dispersion green colour concentrate is dry-blended, but the 6670 green compound eliminates that additional pigment dispersion step. Mechanical acceptance includes tensile yield strength and elongation at break under ASTM D638-14, as well as multiaxial puncture-impact testing under ISO 6603-2:2000 at 23 °C and -20 °C; impact retention after 1,000 h in ISO 4892-2:2013 cycle 1 is commonly specified at not less than 80 % of the as-moulded value, though published data for this specific green-compounded marine configuration is limited and must be confirmed on production coupons. Rotomoulding uses a 3.0 m canoe mould rotated at 4:1, oven temperature 260–280 °C, and peak internal air temperature 185–190 °C; the cooling phase is extended over 45–60 min to avoid hull-line warpage and to allow the mould surface to fall below 55 °C before demoulding. Terminal products include sit-on-top kayaks, canoe hulls, buoyancy floats, dock edge fenders, and rotomoulded hull covers.

    Outdoor playground component manufacture imposes impact-attenuation and head-and-limb entrapment requirements that lead to low internal stresses and smooth radii, which in turn require sustained rotomoulding rather than injection moulding. EN 1176-1:2017 and ASTM F1487-21 require that accessible edges, protrusions, and entrapment openings be free from sharp internal ridges and cracking after impact; rotomoulded Icorene 3545 GRN 6670 panels are therefore produced with a single-wall shell and no internal weld lines. The formulation uses 0.2–0.5 wt% of a HALS masterbatch and 0.3–0.8 wt% of a UV absorber masterbatch; processors avoid slip agents above 0.1 wt% because surface bloom can increase the need for solvent wiping before post-moulding decoration. The moulding process for a tunnel section or slide run uses an oven setpoint of 280–300 °C and a peak internal air temperature of 180–190 °C; wall thickness is held between 5–12 mm, with the lower limit in non-load-bearing roof elements and the upper limit in slide bedways. Cooling is controlled so that textured surfaces are not quenched rapidly enough to create differential gloss bands; forced air is maintained until the mould surface falls below 85 °C, followed by water mist to 55 °C. Terminal products include slide bedways, crawl-tunnel sections, shade-panel inserts, activity panels, and balancing elements.

    Waste Container Bodies and Stress-Cracking Resistance in Hinge Boss Areas

    Two-wheeled and four-wheeled waste container bodies rotomoulded from Icorene 3545 GRN 6670 are qualified under EN 840-1:2020 for dimensions and designation and EN 840-5:2020 for performance and durability. In black municipal variants, carbon black is loaded at 2.0–2.5 wt% with 0.1–0.3 wt% of a HALS masterbatch; in green-coloured municipal schemes, the 6670 pigment package replaces that carbon black loading while still requiring separate UV stabilisation. A 2.4 m biaxial shuttle machine producing a 1,100 L body uses a 4:1 rotation ratio, oven setpoint 300–310 °C, and peak internal air temperature 190–195 °C; nominal wall thickness is 4–6 mm, but hinge bosses and axle locations may thicken to 12–15 mm. Internal air temperature must not exceed 200 °C in the boss region because oxidative embrittlement around steel hinge inserts is a known field failure mode. Extraction with the boss surface above 70 °C can produce ovality around inserts, so cooling is extended through forced air to 80 °C and water mist to 55 °C, with particular attention to the lower corner radii. Terminal product types include 120 L, 240 L, and 360 L two-wheeled bins, 660 L and 1,100 L four-wheeled containers, and recycling bank bodies.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3545 GRN 6670 is a linear low density polyethylene rotational moulding powder supplied with a green pigment package already incorporated. The base resin, Icorene 3545, belongs to the ethylene copolymer class used in low-shear rotational moulding; the suffix GRN 6670 denotes a specific green colour formulation rather than a separate masterbatch blend. Production-scale handling of this grade should proceed on the assumption that the material is a pulverised powder with a controlled particle-size distribution, because segregation of pigmented fines during pneumatic transfer can shift both colour consistency and wall-thickness distribution in deep-draw tools. Published data for the GRN 6670 variant is limited; the product should not be treated as interchangeable with natural Icorene 3545 without review of the lot-specific certificate of analysis and colour-match record.

    At incoming inspection, the base polymer is typically characterised by melt flow rate under ISO 1133-1 at 190 °C and 2.16 kg, density by ISO 1183-1 or ASTM D1505, and oxidative-induction time by ISO 11357-6. The green pigment package can shift melt flow rate by ±0.5 g/10 min relative to the natural base resin depending on pigment loading and carrier type, and density may be 0.003–0.010 g/cm³ higher. These shifts are measurable and justify qualification of incoming pigmented lots before moulding parameters are fixed. When ambient relative humidity exceeds 60%, surface moisture on the powder can produce porosity in thick sections; pre-drying in a desiccant hopper or heated air stream may be required for sensitive parts.

    What Rotational Moulding Variables Govern the Processing Window for Icorene 3545 GRN 6670?

    On carousel, shuttle, and rock-and-roll machines, the conversion of Icorene 3545 GRN 6670 follows the conventional LLDPE powder densification sequence: powder coating, bubble dissolution, coalescence, and densification. The critical control variable is peak internal air temperature, not oven setpoint alone. For rotationally moulded LLDPE powders of this density class, production-scale carousels with arm speeds between 4 rpm and 12 rpm and a rotational ratio near 4:1 are typically started with a peak internal air temperature of 190–210 °C. A lower peak internal air temperature can leave unmelted particles at the inner surface, producing pinholes and reduced impact strength; a peak internal air temperature above 220 °C accelerates thermo-oxidative chain scission and shifts the green colour toward a yellower hue. The allowable window is therefore narrow enough that oven residence time should be adjusted in 2–4 min increments while recording peak internal air temperature with a calibrated infrared probe.

    Process variableStarting range for LLDPE rotomoulding powders of this classObserved failure mode outside window
    Peak internal air temperature190–210 °CBelow 180 °C: pinholes; above 220 °C: oxidation and colour shift
    Oven setpoint260–290 °CExcessive oven temperature with long dwell depletes stabiliser reserve
    Rotational ratio4:1Deviation changes wall-thickness distribution in deep-draw tools
    Demoulding temperature60–80 °CPremature demoulding increases warpage and dimensional spread

    Differential scanning calorimetry by ISO 11357-3 provides the actual melt peak and crystallinity of the coloured powder; oxidative-induction time by ISO 11357-6 indicates the residual stabiliser reserve for a given oven profile. In deep-draw parts with wall sections from 3 mm to 8 mm, the inner surface is the last to densify and the first to exhibit oxidation haze if oven dwell is excessive. Metallic and organic green pigments can affect nucleation and thermal conductivity; therefore, transfer of processing parameters from natural Icorene 3545 without empirical verification is not recommended. Cooling rate also affects dimensional stability: forced-air cooling to a demoulding temperature of 60–80 °C reduces warpage but may increase internal stress in thick sections. The moulder should establish a fixed cooling curve after measuring part shrinkage against tool dimensions.

    Mechanical assessment of Icorene 3545 GRN 6670 should be performed on specimens cut from rotationally moulded plaques, not compression-moulded plaques, because the low-shear process produces anisotropic morphology and residual stress that standard compression moulding does not reproduce. The following test matrix is the minimum set for incoming material qualification and moulded-part validation.

    PropertyStandardReason for inclusion
    Melt flow rateISO 1133-1Detects rheology shifts from green pigment concentrate
    DensityISO 1183-1Controls stiffness, ESCR, and shrinkage
    Tensile yield stressISO 527-2Verifies short-term load-bearing capacity
    Elongation at breakISO 527-2Confirms ductility retention after pigment addition
    Flexural modulusISO 178Relates to part rigidity and wall-thickness design
    ESCRASTM D1693Evaluates stress-cracking resistance in detergent or chemical service
    Vicat softening temperatureISO 306Indicates short-term heat resistance
    Oxidative-induction timeISO 11357-6Detects stabiliser depletion during processing

    Published representative values for the natural Icorene 3545 grade are commonly cited at a nominal density of 0.934 g/cm³ and a nominal melt flow rate of 5.0 g/10 min under 190 °C/2.16 kg. Tensile yield and flexural modulus in this density class are typically in the range of 16–20 MPa and 500–650 MPa, respectively, when tested on slow-cooled compression-moulded specimens. The GRN 6670 variant may exhibit slightly higher density and modulus and slightly lower stress-crack resistance than the natural resin because rigid pigment particles and carrier resins modify the amorphous tie-chain population. Published data for the specific green variant is limited; therefore, end-use validation should rely on actual moulded plaques tested under ISO 527-2, ISO 178, and ASTM D1693, with the environmental exposure condition stated on the test report.

    Thermal Oxidation and Colour Retention in Outdoor Service

    Outdoor exposure of green rotationally moulded parts requires separation between pigment screening and stabiliser performance. A green pigment package such as GRN 6670 may reduce ultraviolet penetration at the surface but can also increase surface temperature under solar load because darker green absorbs near-infrared radiation. Accelerated weathering is therefore specified by ISO 4892-2 or ASTM D2565 with the irradiance and black-panel temperature matched to the end-use climate. Colour change is measured by ISO 7724 or ASTM D2244; a ΔE value greater than 3 after accelerated exposure is generally visible under inspection lighting, although the acceptance limit is application-specific. Retention of mechanical properties after weathering should be confirmed by tensile and impact testing, not by colour alone.

    The oxidative-induction time of the moulded inner surface is a practical screening parameter after processing. When OIT at 190 °C or 210 °C falls below the control value established on the raw powder, the part has consumed a portion of the stabiliser package during the moulding cycle. For long-term outdoor tanks, hoppers, or agricultural equipment, qualification by ISO 4892-2 at a defined irradiance and cycle is required; no universal service life can be claimed from resin datasheet values. The green colour in GRN 6670 should be evaluated in combination with the intended stabiliser package, and any change of pigment source from the original formulation requires re-qualification because impurity profiles in pigments can reduce oxidative-induction time without altering colour significantly.

    At ambient relative humidity below 60%, pre-drying is not normally required for this class of LLDPE rotational moulding powder. Above that threshold, moisture adsorbed on the powder surface can volatilise during the moulding cycle and create internal bubbles that weaken the part. A frequent production-floor observation with pre-coloured powders is colour streaking in deep ribs when the powder is conveyed through long drop lines that allow fines segregation. The moulding service should therefore sample the powder after transfer for particle-size distribution by ISO 4610 or ASTM D1921 to confirm that the d50 value remains within the supplier’s control range. If the green pigment is present as a separate free-flowing component rather than fully compounded, segregation can also produce local variation in melt flow rate and surface gloss.

    Regrind of Icorene 3545 GRN 6670 can be re-introduced into the moulding charge, but the colour balance shifts unless the regrind fraction is controlled and recorded. Particle-size distribution of reclaimed powder differs from virgin powder because of attrition and partial melting at the tool surface. A maximum regrind addition of 20–30% is commonly used in production for non-critical parts; critical parts with tight colour tolerance require validation of the exact regrind ratio before release. The pigment package does not provide electrical conductivity, flame retardancy, or chemical compatibility; those properties must be addressed by separate additive systems or design controls and verified by the relevant IEC, UL, or DIN standards.

    When Crosslinked Polyethylene or HDPE Would Be Selected Instead of Icorene 3545 GRN 6670

    For applications requiring stiffness and creep resistance, an HDPE rotational moulding powder with a density above 0.945 g/cm³ may be substituted, but the trade-off is reduced low-temperature impact strength and higher melt viscosity. Icorene 3545 GRN 6670 occupies a lower-density LLDPE position that provides higher elongation and lower warpage in complex parts than many HDPE rotomoulding grades. For chemical tanks requiring maximum ESCR performance, a single-sided crosslinked polyethylene or a high-density ESCR grade may outperform this LLDPE in hot chlorinated-water service, particularly where failures occur at sharp corners or weld-line regions. Crosslinked polyethylene requires different processing equipment and cannot be reground and re-moulded, whereas Icorene 3545 GRN 6670 remains thermoplastic and can be reground within the limits of the moulding plant’s colour-control plan.

    Compared with conventional LDPE rotational moulding powders, the linear low density structure of Icorene 3545 provides higher tensile yield and flexural modulus at equivalent density because short-chain branches create a more regular crystalline network. Compared with metallocene-catalysed LLDPE rotational moulding grades, the 3545 designation may exhibit different peak melting temperature and organoleptic behaviour; selection for food-contact or potable-water service requires confirmation against 21 CFR 177.1520 and REACH obligations for the finished part. The pre-coloured green package does not automatically confer UV stabilisation, chemical resistance, or impact modification; those performance properties must be validated under the intended service conditions using the standards applicable to the final fabricated part.

    On production-scale carousel machines, a recurring processing boundary is the interaction between the green pigment package and the narrow peak internal air temperature window. When cycle time is shortened to increase throughput, the inner surface may remain under-densified even though the exterior colour appears acceptable. This failure mode is detected by cutting a representative part and inspecting the inner surface for pinholes, unmelted powder, or glossy oxidation bands. If the part passes visual inspection, mechanical validation should still include tensile elongation and impact tests on specimens taken from the thickest and thinnest sections, because wall-thickness-dependent cooling history determines local crystallinity and residual stress. The absence of published lot-specific data for the GRN 6670 variant makes such part-level validation the controlling method for release to production.

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