Lyondellbasell Icorene 3546 Uv Grn 6414 Polyethylene Linear Low Density

LyondellBasell Icorene 3546 UV+ GRN 6414 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3546 UV+ GRN 6414 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 522287
    Product LyondellBasell Icorene 3546 UV+ GRN 6414 Polyethylene, Linear Low Density
    Polymertype Linear Low Density Polyethylene (LLDPE)
    Color Green
    Form Pellets
    Density 0.935 g/cm³
    Meltindex 3.5 g/10 min at 190°C/2.16 kg
    Tensilestrengthatyield 17 MPa
    Elongationatbreak 700%
    Flexuralmodulus 700 MPa
    Shoredhardness 55
    Vicatsofteningtemperature 110°C
    Meltingtemperature 125°C
    Environmentalstresscrackresistance >1000 h
    Uvstabilization Yes
    Processingmethod Rotational Molding

    As an accredited LyondellBasell Icorene 3546 UV+ GRN 6414 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 3546 UV+ GRN 6414 Linear Low Density Polyethylene packaged in 25 kg moisture-resistant bags, 1,000 kg per pallet.
    Container Loading (20′ FCL) 20′ FCL loading: LyondellBasell Icorene 3546 UV+ GRN 6414 Linear Low Density Polyethylene, palletized bags securely stowed for ocean transport.
    Shipping LyondellBasell Icorene 3546 UV+ GRN 6414 LLDPE is shipped as non-hazardous resin pellets, typically in 25 kg PE bags or octabins, palletized and stretch-wrapped. Transport in clean, dry trucks or containers; keep dry, away from heat, sunlight, and contamination. No special UN hazmat classification required.
    Storage Store LyondellBasell Icorene 3546 UV+ GRN 6414 LLDPE in a cool, dry, well-ventilated area using closed original bags or containers on pallets. Protect from direct sunlight, moisture, heat, ignition sources, and strong oxidizers. Keep clean and free from dust or contamination. Prevent spills and slipping. Use first-in, first-out rotation, and avoid excessive stacking or high temperatures.
    Shelf Life Shelf life is typically 24 months when stored in original unopened packaging in a cool, dry place, away from direct sunlight.
    Application of LyondellBasell Icorene 3546 UV+ GRN 6414 Polyethylene, Linear Low Density
    LyondellBasell Icorene 3546 UV+ GRN 6414 reaches the mold cavity as a dry, free-flowing linear low-density polyethylene powder. On a three-arm carousel rotational molding line with a shot weight of 120 kg per arm, the powder is conditioned at 18–25 °C before charging because cold powder extends the tack phase and creates thick corner radii. In agricultural chemical storage tanks of 10,000 L, the sidewall thickness is held at 8–12 mm and the rib-to-wall ratio is kept below 1.2:1 to avoid powder bridging during the first rotation. The shot weight is calculated as M = A × t × ρ × 1.03, where A is the mold cavity area, t is the target wall thickness, and ρ is the batch density from the certificate of analysis under ISO 1183-1:2019. The green pigment package designated 6414 and the UV+ stabilizer system are compounded into the powder; no additional liquid colorant or UV masterbatch is required for a single-layer tank. Exposure to surfactant formulations and low-molecular-weight esters creates stress-cracking conditions that are not predicted by short-term tensile data. The tank therefore requires a weld-line-free cavity and an environmental stress-crack resistance check on cut-out specimens under ASTM D1693-21, Condition B, in 10% Igepal CO-630 at 50 °C. If the tank is intended to store methyl ester-based adjuvants, a full-scale liner exposure of 90 days at 40 °C is performed using the actual formulation because the small-specimen ESCR test does not reproduce long-term leaching at the liquid-air interface. Regrind fraction is limited to 20 wt% for outdoor applications because the oxidative history of the regrind phase lowers the oxidation induction time measured by ISO 11357-6 at 200 °C. The parting line must be moved away from the bottom sump area; if the parting line crosses the lower sidewall, fusion integrity is checked on machined sections according to ISO 13953 to confirm ductile failure rather than brittle separation. Powder dry flow should remain above 30 s/100 g when measured by the funnel method of ASTM D1895 because lower dry flow produces thick-to-thin transitions across narrow ribs. The powder should be stored at 20–25 °C and below 60% relative humidity; if surface moisture exceeds 0.05 wt%, pre-dry with dehumidified air at 50 °C for 2 h because moisture can generate pinholes at the mold surface. Published data for this specific green pigmented configuration under concentrated agrochemical immersion is limited, so the tank manufacturer must qualify each end-use chemical package before starting commercial production.

    What Limits the Use of UV-Stabilized LLDPE in Rainwater Harvesting Tanks?

    In above-ground rainwater harvesting, the dominant failure mode is not hoop stress but photooxidative embrittlement of the sun-facing wall. The green 6414 pigment absorbs a larger fraction of incident solar radiation than a white or natural LLDPE surface; this raises the maximum service temperature of the tank wall and shortens the time to surface microcracking under ISO 4892-2:2013, method A, with a black-standard temperature of 65 °C and a dry period of 102 min in a 120-min cycle. A vertical cylindrical tank of 5,000 L is therefore molded with a bottom-course wall thickness of 7–9 mm and a top-course wall thickness of 5–6 mm when the product is specified for a 10-year outdoor service in tropical latitudes. The oven peak internal air temperature is held at 200±5 °C; excursions above 210 °C consume the hindered amine stabilizer prematurely and reduce the retained tensile elongation after 2,000 h of UV exposure measured by ASTM G154-23, Cycle 1. The cooling phase is adjusted so that the mold surface temperature falls from 180 °C to 70 °C before demolding; forced-air cooling with no water mist is preferred because rapid quenching introduces residual stresses at the darker green surface. When potable water contact is claimed, the tank wall must be tested under NSF/ANSI 61, Section 4, and migration limits apply to the finished article, not only to the base polymer under FDA 21 CFR 177.1520(c). The processor should not add an external UV masterbatch unless the regrind content exceeds 20 wt%; above that threshold the stabilizer concentration in the recycled fraction is insufficient to protect the surface layer. Cleaning with sodium hypochlorite solution is limited to 100 mg/L free chlorine because higher concentrations attack the stabilizer package. The presence of algae or sediment in stored rainwater does not mechanically degrade the LLDPE wall but can promote biofilm adhesion; the cleaning protocol must therefore include mechanical brushing rather than aggressive oxidizing agents.
    Property or requirementMethod or conditionApplication link
    DensityISO 1183-1:2019 Method AShot-weight calculation and oven wetting time
    Melt mass-flow rateISO 1133-1:2022 at 190 °C / 2.16 kgIncoming powder lot control
    Powder dry flowASTM D1895 funnel methodRock-and-roll distribution in deep ribs
    Environmental stress-crack resistanceASTM D1693-21, Condition B, 10% Igepal CO-630, 50 °CChemical tank liners
    Tensile elongation at breakISO 527-2:2012, 23 °CThin-wall demolding and service strain
    Accelerated weatheringISO 4892-2:2013 Method AUV+ package and green pigment retention
    Impact punctureISO 6603-2 at −20 °CPlayground and cold-chain components
    Playground panels and outdoor furniture components molded from the same powder require a different validation path than tanks. The critical mechanical test is instrumented impact at sub-zero temperatures, because a green LLDPE part installed in northern Europe or Canada must survive a winter impact from a falling object without cracking. The part is conditioned for 40 h at −20 °C and tested by ISO 6603-2 with a 20 mm hemispherical striker; the acceptable failure mode is ductile puncture, not radial splitting. For a slide bed or climbing panel, the nominal wall thickness is specified at 6–8 mm, and the supporting ribs are molded at a rib-to-wall ratio of 1.0:1 to avoid sink marks on the visible surface. The rotational molding cycle is run on a shuttle machine with a mold swing diameter of 2.5 m and a biaxial rotation ratio of 4:1; the powder is charged at 20–25 °C, and the internal air temperature is raised to 190–200 °C before cooling. Regrind should not exceed 15 wt% for impact-critical parts because the weld-line region between virgin and recycled particles becomes more visible and can act as a crack initiation zone under repeated falling-sand impact. The UV+ stabilizer system is sufficient for the weathering exposure of outdoor playground equipment, but the green surface must be inspected after 1,000 h of accelerated weathering under ISO 4892-3:2016, Cycle 2, for chalking and color change. A colorimeter reading of ΔE greater than 3.0 after that interval indicates pigment degradation or additive migration; the root cause is usually an overheated mold surface rather than an understabilized resin. The part should be assembled with stainless steel fasteners and nylon washers to avoid galvanic cutting of the LLDPE around bolt holes; tightening torque is limited to 5 N·m for an M8 bolt without a metal insert. Published data for this specific compound in playground fall-height certification under EN 1176 is limited; the mechanical validation of the complete structure takes precedence over raw-material test values.

    Cold-Chain and Material-Handling Containers Rely on Low-Temperature Ductility and Chemical Inertness of the Molded Wall

    When cold-chain containers and fish tubs are molded from Icorene 3546 UV+ GRN 6414, the dominant requirement shifts from UV stabilization to low-temperature impact ductility and chemical inertness. The containers are subjected to cold-room temperatures of −10 °C to 4 °C and repeated mechanical handling by forklift clamps. The LLDPE wall thickness is set at 10–12 mm on the base and 8–10 mm on the sidewalls to prevent clamp-through puncture. The material is not modified with a separate impact modifier because the base linear low-density structure already provides low-temperature ductility when the melt fusion is complete. Fusion is confirmed by a hammer impact test at −20 °C using ISO 6603-2; a specimen from the thickest base corner must show ductile deformation rather than a brittle shard. The mold is rotated at a ratio of 3:1 on a clamshell machine and the oven is set to a peak internal air temperature of 190–200 °C to avoid over-oxidizing the thin top rim. The green pigment is retained in the outer surface, but the food-contact side of the tub is produced from the same pigmented material; therefore the finished article must be checked for extractables under the intended food type rather than assuming compliance from the base polymer alone. The use of release agents is restricted to mold surface applications; silicone-based external release agents can be carried into the food-contact surface and must be removed by a validated washing cycle. Regrind is limited to 25 wt% for non-food outer layers and 10 wt% for food-contact surfaces when the recyclate traceability cannot be demonstrated. The container is stacked under load of 500 kg for 72 h at 23 °C; stack creep is measured by the deformation of the sidewall rib at the midpoint. A creep modulus value obtained by ISO 899-2 at 1,000 h is used to set the maximum stackable height, not the instantaneous flexural modulus from ISO 178. Published data for this specific pigmented compound in cold-chain service is limited; the end user should validate wash-down chemical exposure separately from the mechanical test.In salt-water buoyancy applications, the green 6414 shell is selected because the LLDPE grade can be molded as a closed float skin and then filled with closed-cell polyurethane foam. The shell wall is molded to a nominal thickness of 6–8 mm; the interior is filled after the LLDPE shell has fully cooled to below 50 °C. The foam-fill operation must be triggered within 24 h of demolding because surface moisture on stored shells interferes with adhesion of the foam skin. The grade is processed in a rock-and-roll machine with a single-axis rotation ratio of 8:1 and a shot weight calculated from the surface area and target thickness using a 3% scrap allowance. The green pigmented shell is tested under ISO 4892-2:2013, method A, for 2,000 h; the retained tensile elongation at break must be above 50% of the initial value, measured by ISO 527-2 at 23 °C. In salt water, the material is not subject to chloride-induced degradation, but a molded-in metal insert thread must be isolated with a polyethylene gasket; crevice corrosion of the insert can split the surrounding shell. The waterline zone is the first to lose gloss because the stabilizer package can migrate to the surface and be removed by wave action; therefore the part is tested by ISO 4892-3:2016, Cycle 2, with water spray. Copper-based antifouling additives should not be compounded into this UV-stabilized system because transition metals accelerate oxidative chain scission in the LLDPE wall. Published data for this specific green marine configuration under prolonged seawater immersion is limited; the fabricator must verify foam compatibility and shell adhesion on the actual production tool.

    When Buried Utility Enclosures Replace Sheet-Metal Pull Boxes in High-Moisture Trenches

    Buried utility enclosures and underground valve boxes are molded from this LLDPE grade when the trench environment is permanently damp and soil pH is acidic. The enclosure wall thickness is specified at 9–12 mm for load-bearing lids and 6–8 mm for the sidewalls; the load-bearing surface is reinforced with corrugated ribs of 15 mm depth to resist backfill loads. The part is molded in a carousel machine with a biaxial rotation ratio of 4:1; the internal air temperature is controlled to 195–205 °C because the deep rib pattern requires a longer oven dwell than a flat tank wall. The green 6414 pigment provides a visible underground safety color, but the UV+ stabilizer package is not the primary durability requirement in buried service. The critical performance criteria are soil-induced stress cracking and creep under constant backfill. A representative sidewall sample is checked under ASTM D1693-21, and the stress-cracking agent is selected according to the site-specific soil chemistry rather than a single laboratory surrogate. The enclosure lid is proof-loaded with a hydraulic press to 22.5 kN in a 300 mm square test frame; the deflection is recorded after 10 min, and no crack may appear in the rib root. The rib root is radiused to at least 3 mm to prevent notch concentration from the machining of the tool surface. Where the box is installed below the water table, the seam between the body and lid is fitted with an EPDM gasket and the insert threads are molded from stainless steel to avoid cast iron failure; the LLDPE itself is resistant to soil acid but not to repeated lateral strain from expansive clay. The sidewall is designed with a safety factor of 2.0 against the maximum expected vertical soil pressure, and the long-term deflection is compared with the creep modulus from ISO 899-2 rather than a short-term bending modulus. Published data for this specific pigmented configuration under combined soil load and groundwater immersion is limited; the utility authority should conduct a site-specific burial trial before specifying the material in large-diameter vaults.
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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3546 UV+ GRN 6414 is a linear low-density polyethylene powder produced for biaxial rotational molding of hollow parts. The grade is pre-stabilized and pre-compounded with a green 6414 color package, placing it outside the natural LLDPE powder category. Supplier typical property documentation reports a density of 0.934 g/cm³ measured by ISO 1183-1 and a melt flow index of 4.0 g/10 min at 190 °C under 2.16 kg load in ISO 1133-1. The resin is used in outdoor chemical storage, agricultural tanks, playground enclosures, marine flotation devices, and industrial covers. The principal difference from unpigmented Icorene grades is the elimination of dry-blended masterbatch at the molding machine and the associated color segregation; the principal difference from HDPE rotomolding grades is a lower flexural modulus and higher environmental stress-crack resistance.

    Why Does a Pre-Colored UV+ Grade Reduce Rotomolding Pigmentation Variance?

    When natural rotomolding powder is dry-blended with a granular pigment masterbatch at the hopper, the two components have different bulk densities, particle sizes, and flow behaviors. Vacuum conveying, auger feed, and mold rotation can stratify the mixture before the powder reaches the heated mold wall. The result is color streaking, local pigment agglomeration, and shot-to-shot ΔE variation that is often measured with a spectrophotometer against the CIELAB L*a*b* reference. In contrast, the 3546 UV+ GRN 6414 grade is compounded under high-shear twin-screw mixing before grinding, which wets pigment particles with polyethylene and stabilizes the colorant distribution in the final powder. On carousel machines running multiple aluminum molds from a common hopper, the pre-compounded grade reduces the manual weigh-up error and segregation that occur when operators add 2–3 wt% masterbatch to natural powder. The incorporated pigment also affects infrared absorption during oven heating; green colorants can reflect a different fraction of the incident IR spectrum than natural powder or carbon black, so the grade and final wall thickness should be temperature-profiled together.

    The mechanical design envelope for this LLDPE grade includes tensile yield strength near 18 MPa per ISO 527-2/1A, elongation at break above 700%, and flexural modulus in the range of 550–750 MPa per ISO 178. The environmental stress-crack resistance under ASTM D1693 condition B, 10% Igepal CO-630 at 50 °C, is typically reported above 1,000 h for the base resin family; actual values for green-compounded powder should be confirmed by lot certificate. Low-temperature resistance is commonly assessed by impact testing on rotomolded plaques rather than by neat resin tests, because cooling rate, wall thickness, and internal stress dominate field performance. Published data for the specific GRN 6414 configuration at sub-−20 °C service is limited; final-part testing under ISO 179-1 Charpy or equivalent is required before use in cold-climate structural parts.

    Powder Morphology, Sieve Retention, and Machine Feed Consistency

    Rotational molding powder is characterized by dry-flow time, bulk density, and particle-size distribution, not simply by melt flow index. The Icorene 3546 family is typically supplied as a ground powder with a 35-mesh profile; sieve analysis per ASTM D1921 is used to control the fraction retained on 500 µm, 250 µm, and 150 µm screens. Fines below 150 µm can create dust during mold charging and tend to melt prematurely, producing small pits on the outer surface. Oversized particles above 500 µm may not fully coalesce in short oven residence times and can leave pinholes at the inner surface. Dry-flow values below 35 s/100 g by ASTM D1895 Method A are typical for clean feed through 25-kg bag dumping stations and flexible screw conveyors. The bulk density of this type of rotomolding powder is commonly between 0.38 g/cm³ and 0.42 g/cm³; a lower bulk density changes the shot weight that fills a given mold volume, and processors should recalculate fill ratios whenever the powder source changes.

    At the low shear rates encountered in rotational molding—typically below 10 s⁻¹—the melt viscosity of LLDPE is shear-rate-sensitive but not as temperature-sensitive as that of HDPE. The zero-shear viscosity of a 4.0 g/10 min LLDPE at 190 °C is commonly in the range of 2 × 10⁴ Pa·s to 5 × 10⁴ Pa·s, which is high enough to allow the powder to densify and sinter before flow fills the mold. In thick sections, trapped air bubbles must escape through the melt; bubble removal is governed by melt viscosity, surface tension, and mold surface temperature. The green pigment particles can act as nucleating sites or as local viscosity modifiers, so bubble-entrapment behavior should be established using sectioned plaques.

    On shuttle and carousel rotational molding machines, the recommended mold surface temperature is between 260 °C and 320 °C. The peak internal air temperature for LLDPE of this density is typically maintained between 190 °C and 210 °C; falling below 190 °C can leave partially coalesced particles and lower ESCR, while exceeding 230 °C for extended periods accelerates thermo-oxidative degradation and may darken the green color. Cooling must be controlled because LLDPE crystallization continues below 80 °C; forced-air cooling followed by water mist is common, but rapid quenching of thick sections can increase amorphous orientation and distort large flat panels. The biaxial rotation ratio is set by mold geometry; ratios of 4:1 primary to secondary are a starting point on shuttle machines, but rock-and-roll machines for long tanks may use a single-axis rock with approximately 30° to 45° swing. Rotational molding tooling is typically fabricated from cast aluminum or stainless steel. Aluminum molds provide higher heat transfer and shorter cycle times but are more prone to surface wear from filled or abrasive powders; 3546 UV+ GRN 6414 is unfilled, so tool wear is not a primary concern. Mold release agents based on silicone or PTFE should be applied to thin cross-sections sparingly, because excessive release agent can be entrapped at the inner surface and reduce weld-line strength.

    When ESCR and Low-Temperature Impact Govern Tank Design over Density

    For outdoor liquid storage, rotomolding engineers often choose a lower-density LLDPE because slow crack growth resistance is more important than the higher stiffness of an HDPE grade. Icorene 3546 UV+ GRN 6414 has a density below 0.940 g/cm³; the lower crystallinity leaves a larger fraction of amorphous tie molecules between lamellae. Under constant hoop stress in a filled tank, the tie-molecule network resists crack opening at stress concentrations such as weld lines, insert bosses, and the liquid fill line. This behavior is measured by ASTM D1693 and by ISO 22088-3 bent-strip methods, and for long-term hydrostatic design by ISO 9080 regression of pipe-grade data. The trade-off is reduced flexural modulus relative to HDPE: the same sidewall deflects more under head pressure, so tank walls are often thickened by 10–20% or reinforced with rotationally molded ribs. The low-temperature impact of the finished part is a function of section thickness and mold surface finish; brittle transitions are evaluated by impact testing at −20 °C and −40 °C on samples cut from the actual moldings, not solely on compression-molded plaques.

    Outdoor service degrades polyolefins through free-radical oxidation initiated by ultraviolet radiation, leading to surface chalking, loss of gloss, and tensile elongation loss. The UV+ package in Icorene 3546 contains a hindered amine light stabilizer and a UV absorber, dispersed during pellet production to survive the grinding step. Accelerated weathering per ISO 4892-2 cycle 1, with a 0.51 W/m² irradiance at 340 nm and black panel temperature of 65 °C, is used to compare stabilized grades against unstabilized controls. Unstabilized LLDPE can lose more than 50% of its original elongation within 3,000 h of xenon-arc exposure; stabilized rotomolding grades are expected to retain the majority of their elongation over the same interval, although actual retention depends on wall thickness, cooling rate, and pigment loading. The green pigment can elevate surface temperature under solar exposure by absorbing visible and near-infrared radiation, so the service temperature at the exposed surface is somewhat higher than for white or natural parts. Published data for GRN 6414 after 5,000 h of xenon-arc exposure is limited; requesting supplier weathering curves is advisable before specifying a multi-year outdoor service interval.

    A Comparative Table for Stiffness, Stress-Crack Resistance, and UV Stability

    The table below compares the general property envelope of Icorene 3546 UV+ GRN 6414 with a natural LLDPE rotomolding powder and an HDPE rotomolding grade. The values are typical ranges and should not be read as specification limits.

    PropertyIcorene 3546 UV+ GRN 6414Natural LLDPE rotomolding powderHDPE rotomolding grade
    Density (ISO 1183-1)0.934 g/cm³0.932–0.938 g/cm³0.945–0.955 g/cm³
    Melt flow index (190 °C/2.16 kg, ISO 1133-1)4.0 g/10 min3.5–4.5 g/10 min5–7 g/10 min
    Flexural modulus (ISO 178)600 MPa550–700 MPa900–1,200 MPa
    ESCR (ASTM D1693, condition B)>1,000 h>1,000 h10–100 h
    UV stabilizationPre-compounded UV+ packageNoneOptional package
    Pigment integrationPre-compounded green 6414NoneOften dry-blended

    The practical difference in rotational molding is that the precolored grade removes a manual compounding step and its attendant lot-to-lot drift, while the HDPE alternative gains stiffness at the cost of ESCR and low-temperature ductility. MDPE grades occupy an intermediate position with density near 0.940 g/cm³ to 0.945 g/cm³, but their processability window is often narrower because the higher crystallinity can produce more shrinkage and warpage in asymmetric molds. Crosslinkable PE grades offer higher heat distortion and creep resistance, but they cannot be reground and reprocessed as readily as a linear low-density grade.

    Regulatory Status When the Finished Article Contacts Food or Potable Water

    The base polyethylene is typically manufactured to meet FDA 21 CFR 177.1520 for olefin polymers, but that clearance applies to the base polymer and specified end-use extractive conditions, not automatically to a green pigmented finished article. The UV stabilizer and pigment package must be evaluated under the relevant national or regional food-contact framework. For European Union food contact, plastic materials and articles must comply with Regulation (EU) 10/2011, including overall migration limits of 10 mg/dm², and the pigment must be listed or authorized. For drinking-water components in North America, NSF/ANSI 61 certification is article-specific and depends on formulation, surface-to-volume ratio, and exposure temperature. The grade is therefore more commonly specified for non-food outdoor chemical storage and agricultural tanks than for direct potable-water contact. Metal release and heavy-metal restrictions under REACH and RoHS Directive 2011/65/EU can be addressed by supplier declarations, but these are not substitutes for article-level compliance testing.

    Regulatory areaTest or basisApplicability to finished article
    EU RoHS 2011/65/EUHeavy metal content in homogeneous materialApplicable; supplier statement required
    EU REACH EC 1907/2006SVHC candidate list, Article 33 communicationApplicable if SVHC present above 0.1 wt%
    US FDA 21 CFR 177.1520Olefin polymers, extractives under 21 CFR 176.170(c)Base resin only; pigment not automatically covered
    US ASTM D3350PE cell classification systemUsed for material identification, not compliance
    EU food contact Regulation (EU) 10/2011Overall migration limit 10 mg/dm²Article-specific; green formulation must be verified

    Field applications for Icorene 3546 UV+ GRN 6414 include rotationally molded agricultural sprayer tanks, water storage tanks, outdoor playground components, marine buoys, road barriers, and machinery covers. The green color serves as a visual designation for chemical compatibility or asset ownership without secondary painting; polyethylene surfaces require flame, corona, or plasma treatment before coating, so precompounded color avoids that process step. Agricultural chemical contact can induce environmental stress cracking even at low concentrations because surfactants and emulsifiers act as ESC agents. Tanks used for glyphosate, paraquat, or ester-based formulations should be tested under ASTM D2561 or by internal pressurization after contact with the formulation. The high ESCR of LLDPE is advantageous, but the rotational molder must ensure complete fusion of weld lines; any undercured region becomes a preferential crack-initiation site. Wall-thickness mapping of rotomolded tanks with ultrasonic gauges is often specified at 18–25 points to verify minimum wall thickness before the tank enters service. Processors should not expose the grade to strong oxidizing acids, aromatic solvents, or low-boiling hydrocarbons at elevated temperature without chemical resistance data for the exact fluid, concentration, and service temperature. Cold-climate installations below −20 °C require final-part impact testing because weld-line quality, wall-thickness distribution, and UV history override neat resin ductility. Dimensional stability after demolding is improved by cooling fixtures for large flat panels, especially when the green pigment raises the surface temperature during outdoor storage.

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