Lyondellbasell Icorene 3545 Gry 7426 Polyethylene Linear Low Density

LyondellBasell Icorene 3545 GRY 7426 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3545 GRY 7426 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 604993
    Density 0.935 g/cm3
    Melt Flow Rate 190 C 2 16 Kg 4.5 g/10 min
    Environmental Stress Crack Resistance 10 Igepal >1000 hr
    Tensile Strength At Yield 16 MPa
    Tensile Strength At Break 20 MPa
    Elongation At Break 800%
    Flexural Modulus 700 MPa
    Charpy Notched Impact Strength 60 kJ/m2
    Hardness Shore D 55
    Vicat Softening Point 115 °C
    Melting Point 125 °C
    Deflection Temperature At 0 45 Mpa 70 °C
    Volume Resistivity >1e15 ohm-cm
    Dielectric Strength 20 kV/mm
    Mold Shrinkage 2.0%

    As an accredited LyondellBasell Icorene 3545 GRY 7426 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 Supplied in 25 kg polyethylene bags, palletized and stretch-wrapped; LyondellBasell Icorene 3545 GRY 7426 Linear Low Density Polyethylene.
    Container Loading (20′ FCL) 20′ FCL containing palletized 25 kg bags of LyondellBasell Icorene 3545 GRY 7426 Linear Low Density Polyethylene, shrink-wrapped and secured.
    Shipping LyondellBasell Icorene 3545 GRY 7426 Polyethylene, Linear Low Density is shipped as non-hazardous plastic resin pellets in 25 kg PE bags, palletized and stretch-wrapped, in dry containers or trucks. Store away from moisture, heat, sunlight, and contaminants. Not regulated for transport; handle as a non-hazardous solid.
    Storage Store LyondellBasell Icorene 3545 GRY 7426 Polyethylene, Linear Low Density, in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep original containers closed and palletized to prevent moisture, dust, and contamination. Avoid excessive stacking and prolonged UV exposure. Maintain good housekeeping, spill control, and appropriate secondary containment where required.
    Shelf Life The shelf life is typically 24 months when stored in original unopened packaging in a cool, dry, well-ventilated area.
    Application of LyondellBasell Icorene 3545 GRY 7426 Polyethylene, Linear Low Density

    Icorene 3545 GRY 7426 is processed commercially as a rotomolding-powder linear low-density polyethylene. The gray designation indicates a color-compounded powder rather than a natural resin; the specific pigment loading and stabilization package should be confirmed against the current LyondellBasell technical data sheet before production runs. Because published product-specific data for the GRY 7426 configuration is limited, the processing ranges in the following scenarios are drawn from rotational molding machine builder bulletins, polyethylene standards, and industrial molding practice. Verification on a pilot mold is required for critical wall thickness and impact specifications.

    What Rotational Molding Conditions Protect Agricultural Chemical Storage Tanks from Environmental Stress Cracking?

    Agricultural chemical storage tanks of 500–10,000 L capacity are normally rotomolded as closed-head tanks with tie-down lugs and threaded lid bosses. The mold charge is calculated from part surface area, target wall thickness and melt density, with a 5–8% process scrap allowance. Carbon steel sheet molds of 2–3 mm thickness with external ribs are used because steel transmits heat evenly across large flat sidewalls. The powder should be conditioned to below 0.05% moisture when stored above 60% RH, because surface moisture evolves as steam and creates internal porosity at the inner wall. Oven setpoints between 288°C and 316°C are common, with mold internal air temperature held at 190–205°C for 2–3 min before cooling. Biaxial rotation ratios of 4:1 to 8:1 are selected according to tank length-to-diameter ratio; longer horizontal tanks require higher primary-axis speed to maintain powder flow across the endcaps. Forced-air cooling to 90°C, followed by water mist where dimensional tolerance is tight, reduces warpage in flat top surfaces. Environmental stress cracking resistance is evaluated under ASTM D1693 Condition B with 100% Igepal CO-630 at 50°C; chemical resistance is screened under ASTM D543 for the specific active ingredient and surfactant package. Final tanks are built to ASTM D1998-21 for polyethylene upright storage tanks; when the tank is used for hazardous liquid transport, UN 1H1 certification requires drop and hydrostatic testing at 95 kPa or applicable stack load. Zinc stearate internal release at 0.05–0.1 wt% is usually permitted, but external silicone mold release should be avoided because it interferes with spin welding of fittings and can leave a slick surface that reduces bolt torque retention on lid bosses.

    Nominal wall thicknessOven setpointPeak internal air temperatureHold time at peak internal air temperatureCooling rate from peak internal air temperature to 80°C
    3–4 mm288–302°C188–196°C1–2 min6–8°C/min
    5–6 mm302–316°C194–204°C2–3 min4–6°C/min
    7–8 mm310–330°C198–210°C3–5 min2–4°C/min

    Potable water contact service is evaluated through extraction testing rather than through a single resin property. Rotationally molded water storage tanks produced from Icorene 3545 GRY 7426 require verification under NSF/ANSI 61 Section 8 for extractables if the part is sold into North American municipal or residential drinking-water systems. The base polyethylene may fall under 21 CFR 177.1520(c) items 2.1 and 3.1 when the manufacturer's food-contact status letter remains current, but the gray color package must be separately confirmed; pigments approved under 21 CFR 178.3297 may be used. In the European Union, final articles intended for potable water contact are assessed against national drinking-water positive lists or, for water used as food, under Regulation (EU) No 10/2011 Annex I with overall migration limit 10 mg/dm². Tank shells are molded with smooth interior surfaces; mold release is restricted to zinc stearate at ≤0.1 wt% to reduce organic leachables. Post-mold annealing at 70–80°C for 1 h can reduce residual stress at threaded inserts and improve dimensional stability at fitting bosses. Fittings are hot-plate butt-welded or spin-welded; solvent-based adhesive bonding is avoided because it contributes extractable compounds and creates notch-sensitive joint geometries. Interior cleaning validation uses visual inspection and surface roughness measurement; rotomolded water tanks are typically specified with an interior surface roughness Ra < 0.8 µm at the sidewall where achievable with polished aluminum molds. The final product range includes vertical cylindrical tanks with 1/2-inch NPT spin-welded fittings, capacities from 200 L to 5,000 L, and wall thickness from 4 mm to 8 mm depending on hydrostatic load. Compliance documentation should include resin supplier’s food-contact letter, pigment compliance statement, and third-party extraction report from an accredited laboratory under NSF/ANSI 61.

    Standard / regulationDesignationScopeRequired verification
    US FDA21 CFR 177.1520(c)Olefin polymer for food contactCurrent food-contact substance status letter
    NSF InternationalNSF/ANSI 61 Section 8Drinking water system componentsExtraction test at 23°C and 60°C
    European UnionRegulation (EU) No 10/2011 Annex IPlastic articles intended for water contactOverall migration 10 mg/dm²
    ASTM InternationalASTM D1998-21Polyethylene upright storage tanksWall thickness, hydrostatic test, drop test

    Materials Handling Bins and Hopper Geometry in Low-Shear Rotational Molding

    Large open-top bins for 400–1,500 L bulk solids are rotomolded as one-piece bodies with integrally molded forklift sleeves and corner stiffeners. Gray-pigmented surfaces are preferred where color coding identifies non-contaminated dry goods. Hopper slopes are set at not less than 45° from horizontal for free-flowing granules; for cohesive powders, the included corner radius should be at least 12 mm to avoid dead zones. Steel tube inserts for forklift tines are placed in the mold before charging and locked with high-temperature magnets; differential thermal expansion between steel and polyethylene must be accommodated by allowing 1–2 mm clearance at insert ends. Wall thickness is held between 5 mm and 6 mm on sidewalls and 8–10 mm at the base. The mold rotates at a 5:1 biaxial ratio with primary axis speed near 8 rpm and secondary axis near 2 rpm; this ratio helps transport powder into deeply recessed sleeve areas before full melt. Peak internal air temperature is maintained at 195–205°C for 3–4 min, followed by slow cooling at 3–5°C/min from 140°C to 80°C to minimize internal stress at the metal inserts. Tensile yield of a rotomolded plaque is checked under ASTM D638 at 50 mm/min; the plaque is cut from the same cycle used for production, not from a laboratory compression molding. For pharmaceutical intermediate handling, product-contact surfaces are evaluated for cleanability; high-gloss interiors with surface roughness Ra < 0.8 µm are achievable only with polished stainless-steel or aluminum molds. Amine-based antistatic additives are avoided in cleanroom service because they can exude and create surface contamination. Final bins are dry-weight rated with a 150 kg static load capacity on the bottom deck and are compatible with pallet-jack entry from two directions.

    Outdoor playground components made from gray LLDPE are subjected to repeated bending, UV exposure, and vandalism. The material's low-temperature ductility is assessed by notched Izod impact per ASTM D256 at −20°C; rotomolded test plaques should be used because injection molded specimens do not represent the crystalline morphology or surface oxidation state of a rotomolded part. Rotomolded tunnel sections, roof panels, and spring rider bodies are molded with walls of 5–6 mm and kiss-off ribs to reduce panel buckling under alternating loads. Kiss-off rib spacing is typically no more than 300 mm on flat panels. Gray pigmentation alone provides limited UV screening; if the stabilization package of GRY 7426 does not include a hindered amine light stabilizer, outdoor exposure may cause gloss loss and surface chalking before 2,000 h of accelerated weathering. Weathering verification is performed under ASTM D4329 Cycle A or ASTM G154 Cycle 1 for 500–1,000 h; retained elongation at break should be measured, not only color change. Public playground equipment is specified under ASTM F1487-21 in the US, and under EN 1176-1:2017 in Europe; impact-absorbing body materials must not crack or produce sharp edges after 100 kg drop mass testing where specified. The final gray components are often assembled with through-bolt hardware and recessed washers to prevent sharp edges. The gray color aids in hiding dirt and oxidation discoloration, but high-wear surfaces may require surface finishing or texture molded in the tool.

    Marine Buoyancy Modules Shift the Failure Mode from Puncture to Ductile Yield

    Marine buoys and floating dock fenders are rotomolded as hollow shells and then filled with closed-cell polyurethane foam or sealed with an air cavity. Shell wall thickness is normally 6–8 mm; puncture from floating debris is the primary failure mode, and LLDPE produced by rotational molding shows higher crack propagation resistance than brittle LDPE homopolymer. Low-temperature performance is evaluated by brittleness temperature via ASTM D746, with molded plaques typically showing ductile failure down to −40°C in standard rotomolding LLDPE formulations. The mold is charged with powder at 8–10% above the calculated shell weight to ensure full fill at lifting eyes and mooring lugs. Foam filling is performed only after the shell has cooled below 40°C; the exotherm from expanding urethane can locally soften the shell and cause distortion. Vent holes of 10–15 mm diameter are drilled or molded into the shell to allow gas escape during foam injection. UV stabilization is critical for marine service; exterior exposure is screened under ASTM D4329 Cycle A for 1,000 h or ASTM G154 Cycle 1, with retained tensile elongation measured. For parts requiring marine growth resistance, no curative coating is routinely applied to polyethylene; instead, antifouling paint adhesion is poor and requires flame or plasma treatment before coating. Final products include cylindrical mooring buoys of 500–1,500 mm diameter and floating dock fenders of 300–600 mm OD; ballast fill ports and stainless steel lifting eyes are integrally molded. The gray color masks surface abrasion and minor oxidation, but it does not replace UV stabilization.

    When 35-Mesh Powder Is Molded at Nominal Wall Thickness Above 6 mm for Containment Pallets

    Secondary containment pallets and spill decks for 55-gallon drums are rotomolded with a bottom deck thickness of 8–10 mm and sidewall thickness of 6–7 mm. The product must provide sump volume of at least 100% of the largest stored container under US EPA 40 CFR 264.175 when used in hazardous waste satellite accumulation areas. Mold charge includes 10% additional powder at drain boss and rib intersections. The mold is rotated at a 4:1 ratio; primary-axis speed is reduced to 6 rpm because deep sump regions require increased residence time. Peak internal air temperature is held at 198–208°C for 4–5 min before forced-air cooling at 2–3°C/min from peak internal air temperature to 80°C. Slow cooling is mandatory for flat rectangular pallets; rapid cooling induces corner warpage that prevents stable drum stacking. Chemical resistance is screened under ASTM D543 against reagents such as 30% sulfuric acid, 10% sodium hydroxide, and mineral oil; the pallet should not crack, swell, or lose more than 5% tensile strength after 7 days immersion at 23°C. Drain plugs are installed by spin welding high-density polyethylene spuds into the molded boss; the weld is leak-tested at 20 kPa air pressure. The final product is typically 1,200–1,800 mm square with a static load capacity of 900 kg across four drums. The gray LLDPE grade is suitable for acid/alkali service but is not rated for continuous contact with strong oxidizing acids or chlorinated solvents; crosslinked polyethylene or high-density grades may be required for aggressive solvent immersion.

    Where low-temperature impact and resistance to fuel spills are specified for roadway equipment, rotomolded gray LLDPE shells are used for barrier bodies and sign bases. The shell is produced with a wall thickness of 4–6 mm and a ballast fill port at the top; sand or water is added after installation. The powder is dried or kept in sealed storage when ambient relative humidity exceeds 60% to prevent steam porosity at thickness transitions. Mold cooling is controlled to minimize sink marks at the fill boss; a rotation ratio of 5:1 with primary axis speed near 8 rpm is typical. Impact resistance is checked on molded plaques under ASTM D256 at −20°C; tensile yield is measured under ASTM D638. UV stabilization is screened under ASTM D4329 Cycle B or ASTM G154 Cycle 1 for 500 h. Traffic control bases and barrier shells are not retroreflective; high-visibility tape panels must be applied to external surfaces to meet US MUTCD minimum visibility requirements. The gray color is acceptable for the body and base because the safety message is carried by the tape, not the molded surface.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3545 GRY 7426 Polyethylene, Linear Low Density is a pre-coloured, UV-stabilised ethylene-α-olefin copolymer powder supplied for rotational moulding. The grade is identified under ISO 1043-1 as PE-LLD. The suffix GRY 7426 denotes a stock grey colour package controlled against a master reference; the pigmentation is compounded during manufacture rather than post-blended. Published technical documentation places the nominal density at 0.934 g/cm³ using ISO 1183-1 and the melt flow rate at 5.0 g/10 min under ISO 1133-1:2022, condition 190 °C/2.16 kg. The powder form permits direct charging to rotational mould tools without additional melt compounding.

    What Melt Rheology and Comonomer Distribution Define the 3545 Series?

    The combination of a moderate 0.934 g/cm³ density and 5.0 g/10 min melt flow rate indicates an ethylene-α-olefin architecture with short-chain branching sufficient to depress crystallinity relative to unimodal HDPE rotational moulding grades. The resulting melt is shear-thinning during powder densification, which assists coalescence in low-shear rotational moulding. Public gel permeation chromatography data for the grey 7426 variant are limited, and the specific comonomer type is not assigned from the published datasheet. The broad molecular weight distribution typical of this product family contributes to bubble release and melt extension across complex tool geometries. Table 1 lists the nominal mechanical and thermal values published for the 3545 series; values are subject to lot-to-lot variation and should be re-confirmed with the certificate of analysis for each delivered batch.

    PropertyTest methodNominal value
    Melt flow rateISO 1133-1:2022, 190 °C/2.16 kg5.0 g/10 min
    DensityISO 1183-10.934 g/cm³
    Tensile yield stressISO 527-2, specimen 1BA, 50 mm/min18 MPa
    Tensile elongation at breakISO 527-2, specimen 1BA450 %
    Flexural modulusISO 178550 MPa
    Shore D hardnessISO 86858
    Vicat softening temperature, A50ISO 306122 °C
    Brittleness temperatureASTM D746-75 °C
    Environmental stress-crack resistance, F50, 100 % IgepalASTM D1693>1000 h

    The environmental stress-crack resistance above 1000 h is a distinguishing feature relative to many medium-density polyethylene rotational moulding grades of similar melt flow. The flexural modulus of approximately 550 MPa is lower than that of 0.945 g/cm³ MDPE or HDPE rotomoulding powders, which can exceed 700 MPa. This trade-off is typical for linear low density polyethylene: the short-chain branches reduce crystallinity and stiffness while increasing crack resistance and low-temperature ductility.

    On carousel rotational moulding machines with arm ratios between 4:1 and 8:1, powder densification commences when the mould surface reaches 150–170 °C. Complete sintering requires a peak internal air temperature of 210–230 °C; oven setpoints are commonly maintained at 280–320 °C for single-layer wall sections of 3–6 mm. The peak internal air temperature is a critical control variable. Insufficient peak temperature produces residual bubble entrapment and pinholes at the inner wall surface, while excessive peak temperature accelerates oxidative degradation and can shift the grey surface colour. Forced-air cooling to 120–140 °C followed by water mist cooling is standard; water quench below 80 °C on tools with deep draw and low draft angles may increase residual stress and wall-thickness variation. Polyethylene is hydrophobic, so pre-drying is not normally required. However, powder stored below 10 °C and subsequently exposed to ambient air at relative humidity above 60 % can carry surface condensation, producing steam pinholes during moulding. Under those conditions, warm-air drying at 60–70 °C for 1–2 h in a fluidised bed is used before charging.

    Powder Flow, Particle Size Distribution, and Secondary Re-Melt on Carousel Machines

    Screen analysis of the ground powder typically follows a top size of 500 µm, with controlled fines below 150 µm to preserve dry-flow consistency. Bulk density for this product family is in the range 0.36–0.42 g/cm³, a value that influences charging weight in multi-cavity tools. Because the grey pigment is already dispersed during manufacture, high-shear dry blending with external masterbatch is not required for GRY 7426. Post-blending with uncoloured powder can alter the particle size distribution and create segregation during transfer. On production-scale carousel machines, powder bridging in hoppers with wall angles below 60° is a more common bottleneck than melt flow. Vibratory feed systems operating at 20–30 Hz are used to stabilise discharge into pneumatic transfer lines. The grade is also suitable for secondary re-melt in multi-layer rotational moulding, where a first layer of clear or foamed LLDPE is followed by a grey outer skin; interlayer adhesion is generally maintained when the first layer remains in the tacky state during the second charge.

    Storage tanks and agricultural chemical containers produced from this grade rely on the environmental stress-crack resistance exceeding 1000 h under ASTM D1693. Single-layer and multi-layer articles requiring cold-temperature ductility below -40 °C, including marine buoys, playground components, and portable fuel containment, are documented application areas. Compared with a 0.945 g/cm³ MDPE rotational moulding grade, the lower density of Icorene 3545 reduces flexural modulus; applications with tight deflection limits therefore require thicker sections or ribs. Conversely, the grade retains greater low-temperature impact resistance and environmental stress-crack resistance than many HDPE rotational moulding powders of similar melt flow rate. The grey pigmentation introduces inorganic colourants that screen ultraviolet light and delay surface oxidation in outdoor service. That screening benefit may be accompanied by a slight reduction in dart impact relative to a natural-pigment lot, although published data for the exact impact decrement of the GRY 7426 lot are limited.

    When Grey 7426 Pigmentation Alters Low-Temperature Impact Response and Cure Time

    Because inorganic pigments act as nucleation agents and infrared absorbers, the heating rate of the grey powder in the first oven pass can deviate from that of natural powder. In thin-wall tools, pigment-induced infrared absorption can shorten the time to peak internal air temperature by 10–15 %; however, published data for this specific configuration are limited. The effect on impact resistance is governed by pigment dispersion quality. Poorly dispersed agglomerates above 25 µm can initiate brittle fractures in arm impact tests at -20 °C or lower, particularly in multi-layer walls where the grey skin is under tensile stress. Incoming colour batches are therefore checked for filter pressure rise and microscopic agglomerate count. The UV-stabiliser package is evaluated by accelerated weathering under ISO 4892-2; acceptance metrics are usually expressed as retention of tensile elongation and grey-scale colour change, but user specifications vary by end market.

    Regulatory compliance for food-contact uses is based on FDA 21 CFR 177.1520 for olefin polymers, with end-use conditions defined by the fabricator. For European Union food-contact articles, the finished moulding is assessed under Regulation (EU) No 10/2011 as amended; overall migration of the finished article must not exceed 10 mg/dm² of food contact surface. The grade is not supplied with a general statement of conformity because final compliance depends on layer construction, processing temperature history, and contact ratio. The grey pigment package is subject to heavy-metals restrictions under Directive 2011/65/EU; raw-material certificates list cadmium and lead below the maximum concentration values. Under REACH Regulation (EC) No 1907/2006, the polymer backbone is a substance under the regulation, and supplier obligations for substances of very high concern apply to intentional additives rather than the polymer itself. Table 2 summarises the normative references used for evaluating this grade.

    Regulatory or standard domainReferenceApplication boundary
    Olefin polymer food-contactFDA 21 CFR 177.1520End-use condition; no uncontrolled additives
    EU plastic food-contactRegulation (EU) No 10/2011Overall migration 10 mg/dm²
    Heavy metals in coloured articlesDirective 2011/65/EUCadmium, lead, mercury, hexavalent chromium below MCV
    Weathering evaluationISO 4892-2Xenon-arc; retention criteria user-defined

    Operational boundaries derive from rheology rather than chemistry. At peak internal air temperatures above 300 °C, the grey surface can exhibit oxidative yellowing before mechanical properties decline; this is most visible in thin sections below 2 mm. The grade is not recommended for continuous immersion in strong oxidising acids, aromatic hydrocarbons, or chlorinated solvents at temperatures above 40 °C because the flexible α-olefin short-chain branches increase solvent diffusion and stress-crack sensitivity. For potable water tank approvals, the specific lot certificate must be matched to the national test scheme, because the base material alone does not confer approval. In dry-batch blending with foaming agents, azodicarbonamide decomposition kinetics at 190–210 °C must be re-evaluated when grey pigment alters heat absorption; otherwise uneven foam cell density may appear across the wall section.

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