Lyondellbasell Icorene 3546 Uv Whi 1101 Polyethylene Linear Low Density

LyondellBasell Icorene 3546 UV+ WHI 1101 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3546 UV+ WHI 1101 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 959367
    Polymer Type Polyethylene, Linear Low Density (LLDPE)
    Density 0.935 g/cm³
    Melt Mass Flow Rate Mfr 20 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 12 MPa
    Tensile Elongation At Break 600%
    Flexural Modulus 500 MPa
    Notched Izod Impact Strength 50 kJ/m²
    Shore D Hardness 50
    Vicat Softening Temperature 90 °C
    Heat Deflection Temperature At 0 46 Mpa 50 °C
    Melting Point 125 °C
    Linear Mold Shrinkage 0.020 cm/cm
    Uv Stabilization Yes
    Color White

    As an accredited LyondellBasell Icorene 3546 UV+ WHI 1101 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+ WHI 1101 is typically supplied in 25 kg polyethylene-lined bags, palletized and stretch-wrapped for industrial shipment.
    Container Loading (20′ FCL) 20′ FCL loading: LyondellBasell Icorene 3546 UV+ WHI 1101 Linear Low Density Polyethylene, palletized 25 kg bags, shrink-wrapped, secured for export.
    Shipping LyondellBasell Icorene 3546 UV+ WHI 1101 Polyethylene, Linear Low Density is shipped as solid pellets in 25 kg bags, jumbo bags, or bulk containers. Keep dry, cool, and clean; avoid direct sunlight, heat, and contamination. Non-hazardous under normal transport conditions. Protect packaging from damage and moisture during handling and storage.
    Storage Store LyondellBasell Icorene 3546 UV+ WHI 1101 LLDPE in a cool, dry, well-ventilated area. Keep original containers sealed and palletized off the floor. Protect from direct sunlight, heat, moisture, and contamination. Avoid ignition sources and strong oxidizers. Do not expose to prolonged UV radiation. Maintain good housekeeping to prevent dust buildup. Use stock first-in, first-out.
    Shelf Life Shelf life is typically 24 months when stored in original unopened packaging, dry, cool conditions, away from direct sunlight and excessive heat.
    Application of LyondellBasell Icorene 3546 UV+ WHI 1101 Polyethylene, Linear Low Density

    LyondellBasell Icorene 3546 UV+ WHI 1101 is processed as a dry-flow linear low density polyethylene powder for rotational moulding. The grade is supplied with a white pigmentation package and UV stabilisation, which shifts the heat-absorption behaviour of the powder during oven residence and changes the outdoor surface-retention profile relative to unpigmented LLDPE. Density for linear low density polyethylene is generally specified between 0.916 g/cm³ and 0.940 g/cm³ under ASTM D1505; grade-specific values for 3546 UV+ WHI 1101 should be taken from the certificate of analysis because post-reactor stabilisation and pigment addition influence final powder bulk properties. Melt flow rate should be determined under ASTM D1238 at 190 °C/2.16 kg or ISO 1133-1. Rotomoulding cycle design depends on peak internal air temperature rather than oven set point alone, particularly with a white pigmented grade, because surface reflectance delays heat transfer into the powder bed. Bulk density and pourability are evaluated under ASTM D1895, and particle size distribution is checked by ASTM D1921 or an equivalent sieve stack. The powder is not intended for injection moulding or blown film extrusion unless converted by an approved grinding and stabiliser masterbatch route.

    Rotational Moulding of White UV-Stabilised LLDPE for Agricultural Water and Chemical Storage Tanks

    Single-layer rotationally moulded tanks for agricultural water and liquid crop-care storage are produced from this grade on multi-station carousel machines or open-flame rock-and-roll units where vertical cylindrical geometry dominates. The biaxial rotation ratio is typically 4:1 primary axis to secondary axis, adjusted to achieve uniform wall thickness across sidewall and bottom transitions. Oven set-points range from 270 °C to 310 °C, with peak internal air temperature between 190 °C and 215 °C for LLDPE. White pigmentation in WHI 1101 reflects a portion of radiant heat, so cycle timers may require 5% to 12% additional oven dwell compared with unpigmented rotomoulding powders to reach full bubble dissolution. Cooling should begin with forced air, not water fog, to limit differential shrinkage at thin upper walls. Wall thickness is generally specified between 4.0 mm and 8.0 mm for vertical tanks in this segment; above 8.0 mm, longer cooling cycles are required to prevent internal voids.

    Tanks intended for potable water are evaluated under NSF/ANSI 61, but certification is a finished-tank requirement, not automatically conferred by the raw powder alone. Chemical storage tanks are commonly designed to meet ASTM D1998 even though the standard is more frequently applied to high-density polyethylene; the moulder should confirm that the lower modulus of LLDPE remains acceptable for the specified tank diameter and wall thickness. Environmental stress crack resistance is characterized by ASTM D1693 under condition A, and suppliers should provide batch-specific data because post-pigmentation can shift ESCR values relative to natural powder. Emulsifiable concentrate crop-care formulations can be more aggressive toward slow crack growth than simple inorganic fertiliser solutions. Moulded-in fittings and threaded inserts generate local stress concentrations; annealed or radiused insert bosses reduce cracking in concentrated crop-care products. Long-term outdoor colour retention is monitored using ASTM G154 and ASTM D2244, but the UV package should not be considered an unlimited weathering guarantee in highly alkaline irrigation environments.

    Application segmentCritical propertyTest method or design standardProduction-scale control point
    Agricultural water and chemical tanksESCR, wall thickness, potable-water complianceASTM D1693, ASTM D1998, NSF/ANSI 61PIAT 190 °C to 215 °C; forced-air cooling before demoulding
    Recreational hullsInstrumented impact, weatheringASTM D3763, ISO 6603-2, ASTM G154PIAT 200 °C to 220 °C; moisture below 0.1% before charging
    Telecommunication enclosuresLow-temperature ductility, colour retentionASTM D3763, ASTM D2244, ISO 75-2Local wall thickness not below 4.0 mm at bosses and latch recesses
    Marine buoyancy floatsUV ageing, oxidative stability, foam-fill integrityASTM G154, ISO 11357-6Continuous outer-skin layer; PIAT verified in hidden sections
    RV water and grey-water tanksStress cracking from cleaning agents, weldabilityASTM D1693, NSF/ANSI 61Mechanical abrasion before fitting welds; PIAT 190 °C to 210 °C

    Recreational kayak and canoe hulls are rotationally moulded from this white UV-stabilised LLDPE powder on shuttle or carousel machines equipped with aluminium or steel moulds. The material enters tight stern and bow contours as a dry powder; without sufficient peak internal air temperature, under-sintering creates microporosity along the waterline and decreases instrumented impact resistance measured by ISO 6603-2 or ASTM D3763. A peak internal air temperature of 200 °C to 220 °C is usually required for full densification, but white pigmentation slows radiant heat absorption and makes the time to reach that plateau longer than that of black or natural LLDPE. Mould surfaces that produce wall thickness below 3.0 mm at deck coamings are at risk of brittle puncture after long outdoor exposure. Because the grade contains UV stabilisation, surface cracking from weathering is assessed under ASTM G154 cycle 1 or ISO 4892-3, with flexural modulus modification tracked using ISO 178 or ASTM D790. Deep-draw areas may require increased powder charge, and tool designers typically maintain draft angles of 5° to 10° to reduce demoulding stress on the hull.

    Processors report that white hulls obscure visual sink marks better than unpigmented grades, but the same reflectance can mask insufficient sintering because the outer surface appears acceptable before the inner surface has fully densified. For this reason, oven time should not be shortened based on external gloss. The powder should be kept dry below 0.1% moisture before charging; damp powder produces steam pinholes when heated above 100 °C. Batch-to-batch powder bulk density is checked using ASTM D1895 to maintain consistent shot weight. There is no publicly available comparative data set for this grade in turbulent whitewater hulls; prototype validation under service-specific impact protocols remains necessary.

    What Limits Low-Temperature Impact Resistance in Outdoor Telecommunication Enclosures?

    For outdoor telecommunication and electrical enclosures rotationally moulded from this LLDPE grade, service impact requirements at sub-zero temperatures set the primary processing constraint. The key limiting factor is wall thickness consistency at bosses and latch recesses, where local thinning below 4.0 mm reduces low-temperature ductility. The powder is processed in closed-cavity moulds on multi-arm carousels, and the peak internal air temperature is controlled between 195 °C and 215 °C. Insufficient internal air temperature leaves partly fused particles at the inner surface; this condition is detected by low ASTM D3763 instrumented impact energy and visible micro-porosity after cross-sectioning. UV exposure in rooftop or desert installations is assessed by ASTM G154, with colour shift measured by ASTM D2244, while heat deflection under load may be reported according to ISO 75-2; LLDPE exhibits lower modulus at elevated temperature than HDPE, so enclosures exposed to direct sun should not be designed as structural supports. Moulded-in inserts for lid hinges and latch strikes must be isolated from sharp thermal transitions, because differential shrinkage around metallic inserts generates tensile stress and may accelerate environmental stress cracking in the presence of condensation and road-salt aerosols.

    Tooling for this segment generally uses 2° to 4° draft angle on deep ribs and recessed pockets. Demoulding stress can concentrate at latch undercuts, so local wall section should be increased rather than relying on material toughness alone. If UL or telecom enclosure flammability classifications are required, the selected additive package must be verified in the final moulded wall because white pigment and UV stabilizer can alter ignition performance; publicly available confirmation for this grade with flame-retardant additive combinations is limited.

    Light industrial material-handling bins and hoppers are produced from this white UV-stabilised LLDPE powder where the dominant requirement is abrasion resistance during bulk-flow discharge and resistance to stress cracking from process washdown. The application is less impact-critical than recreational hulls; wall thickness can therefore remain between 3.5 mm and 5.0 mm, but the base corner must be radiussed to avoid fracture during fork tine handling. Dry-flow properties are measured with ASTM D1895 or an internal funnel test; no single specification applies across all rotomoulding powder producers. Hoppers are typically moulded with 2% to 4% draft angle and minimal internal undercuts. Welded polyethylene liners are not required, but drop-impact testing according to ASTM D5276 for filled containers should be included when parts are moved by forklift.

    When Closed-Cell Polyurethane Foam Filling Is Specified for Marine Floats

    In marine buoyancy parts, this white LLDPE grade is rotomoulded into floating buoys, flotation collars, and marine impact fenders because the polymer permits continuous closed-cell polyurethane foam filling and retains ductility after saltwater immersion. The white outer skin reduces solar heat build-up in exposed marine service, but it also changes the rotomoulding heat transfer: the oven dwell must be adjusted by measuring peak internal air temperature rather than relying on visual surface gloss. For marine floats, wall thickness is usually from 5.0 mm to 12.0 mm, and the mould is often aluminium with internal pressure testing specified by the end user after foam fill. The outer skin must be a single continuous layer; weld lines or under-sintered patches allow water intrusion into the foam and can cause freeze-thaw damage in northern harbours. UV stabilisation is verified by ASTM G154 exposure, while oxidative stability can be tracked using ISO 11357-6 oxidation induction time on material milled from the inner wall. Surface microcracking in high-UV marine environments is a known failure mode, and comparative weathering data for this grade under long-term South China Sea or Mediterranean conditions has not been published in open technical literature. Inserts for mooring eyes should be encapsulated with a raised boss profile to avoid stress concentration at the waterline.

    The foam filling operation introduces exothermic curing heat after the shell has cooled. Operators should delay demoulding and allow post-cure cooling of the polyurethane to avoid heat effects on the inner LLDPE wall. The white UV-stabilised skin also must be cleaned and flame-treated or mechanically abraded before structural adhesive or buoy marking attachment; untreated low-surface-energy polyethylene gives variable adhesion under marine conditions.

    Recreational vehicle water and grey-water tanks use a white UV-stabilised LLDPE rotomoulding powder for its balance of low-temperature impact and cleanability after field service. The tank body is produced as a one-piece hollow shell on a rock-and-roll machine, which allows long cylindrical or rectangular profiles with minimal parting-line leakage risk. Peak internal air temperature is held between 190 °C and 210 °C, and rotation speed is reduced for long rectangular tanks to maintain more uniform powder pick-up along corners. Wall thickness in this segment generally falls between 4.0 mm and 6.0 mm; baffled or flat-panel designs require stiffening ribs because LLDPE has a lower flexural modulus than high-density polyethylene. Potable-water certification is a finished-tank requirement under NSF/ANSI 61, and not all white UV packages automatically meet every clause; the moulder must request raw-material approval letters and test the final tank after insert moulding. Grey-water tanks require resistance to surfactant-induced stress cracking, which is assessed by ASTM D1693 after immersion in the intended cleaning agent. Drain fittings are welded by spin or fusion welding; surface pretreatment by mechanical abrasion improves fusion-bond strength because the white UV-stabilised skin contains pigment agglomerates that can reduce weld ductility.

    For diesel fuel service, conventional LLDPE rotomoulding grades are not regarded as high-barrier fuel-contact layers without additional fluorination or barrier treatment; published data for this configuration under continuous wet-dry diesel cycles is limited. The moulder should separately validate odour, swell, and stress-crack resistance under the specified tank wall thickness and closure system.

    For double-walled playground slides and outdoor climbing components, this white UV-stabilised LLDPE powder is rotationally moulded on multi-cavity wheel machines. The grade must satisfy finished-part impact and entrapment requirements under EN 1176 and ASTM F1487, which are assembly-level standards and are not addressed by raw-powder data. White pigmentation helps reduce surface temperature in direct sun and preserves colour stability, while the UV package contributes to impact retention after multi-year UV exposure. Moulders in this segment control wall thickness at slide rail edges to avoid brittle fracture; local thickness below 3.5 mm is usually avoided because it aligns with regions of high bending stress during use. If flame-retardant additives are mixed into the powder, processing windows narrow because the elevated oven temperatures needed for LLDPE can degrade halogenated or phosphorus systems; publicly available data for this grade in playground thermal-cycling tests is limited.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3546 UV+ WHI 1101 is classified as a linear low-density polyethylene (LLDPE) and is supplied in pre-compounded white rotational moulding powder form. The model designation carries three identifiers: the Icorene 3546 base resin code, the UV+ stabilisation marker, and the WHI 1101 white colourant code. Because this is a low-shear processing material, specifications for powder dry-flow, bulk density, and particle size distribution accompany the usual melt-state rheology. The grade is specified against ISO 1133-1:2022 for melt flow rate at 190°C under 2.16 kg, and against ISO 1183-1:2019 for density. Public datasheet values typical for this family place density near 0.940 g/cm³ and melt flow rate near 4.0 g/10 min; the certificate of analysis supersedes published typical values. The material is used in rotational moulding of outdoor tanks, agricultural hoppers, traffic barriers, insulated containers, and structural panels requiring a pre-compounded white surface and ultraviolet resistance. As an ethylene copolymer, the product carries short-chain branching along the main chain; the specific comonomer and catalyst architecture are generally not declared in abbreviated technical data, but they affect environmental stress-crack resistance and shear thinning. Specifiers should therefore treat comonomer type as a performance variable rather than an irrelevant background parameter.

    Representative datasheet properties for LyondellBasell Icorene 3546 UV+ WHI 1101
    PropertyMethodTypical value
    DensityISO 1183-1:20190.940 g/cm³
    Melt flow rateISO 1133-1:2022 (190°C, 2.16 kg)4.0 g/10 min
    Tensile stress at yieldISO 527-2:201214 MPa
    Tensile elongation at breakISO 527-2:2012>800%
    Flexural modulusISO 178:2019400 MPa
    Vicat softening temperatureISO 306:2022, A50105°C
    Brittleness temperatureASTM D746-20< -76°C

    The values above are representative only; they are not a specification schedule. For critical outdoor applications, property retention after weathering should be measured on finished parts because thickness, crystallinity level, and colourant dispersion alter the effective service lifetime.

    How Does the Grade Behave Under Rotational Moulding Oven Conditions?

    Rotational moulding is a low-shear process; the powder is charged into a closed mould, rotated biaxially, and heated until the polymer densifies and fuses into a bubble-free wall. The melt flow rate of 4.0 g/10 min supports powder flow and gas venting in moderate wall sections, while density near 0.940 g/cm³ balances stiffness and impact. Oven set temperatures for LLDPE powders in this melt flow range are commonly 280–310°C, but the more meaningful control is peak internal air temperature. Operators typically target 180–200°C internal air temperature; prolonged excursions above 220°C increase the risk of oxidative yellowing in white pigmented materials and reduce retained elongation. Because the white colourant alters infrared absorption and reflection, oven calibration should be performed with the actual WHI 1101 powder rather than a natural or black reference grade. Insufficient heating produces incomplete fusion and pinholes; excessive heating can generate carbonyl species and reduce ultraviolet stability. The cooling phase must also be controlled. Rapid cooling with forced air or mist lowers crystallinity and preserves ductility but increases warpage on asymmetric parts. Slow cooling in the mould raises crystallinity and flexural modulus but can reduce low-temperature impact. A uniform cooling ramp through 90–120°C is therefore often maintained until the part can be demoulded without distortion.

    Two-machine carousel and shuttle lines may require different shot-weight to oven-time ratios; a fixed oven temperature cannot be transferred between machines without re-qualification of wall-thickness distribution. The powder particle-size distribution, bulk density, and compacted density should be monitored because these variables influence cavity fill and bubble removal more directly than capillary rheology in a low-shear service environment.

    The UV+ package in Icorene 3546 UV+ WHI 1101 is supplied as a pre-compounded stabiliser system rather than a diluent letdown masterbatch. WHI 1101 denotes a white colourant package, generally based on rutile titanium dioxide dispersed in the polymer matrix. Titanium dioxide scatters ultraviolet wavelengths and contributes opacity, but it does not fully replace the organic light-stabiliser system; both components interact to reduce photochemical chain scission at the moulded surface. Accelerated weathering of rotomoulded parts is normally specified by ISO 4892-2:2013 or ISO 4892-3:2016, with evaluation of colour change and retained tensile elongation. Retained elongation after weathering is a more sensitive indicator of polymer degradation than change in mass or gloss, because ethylene-based materials tend to embrittle by molecular weight reduction before gross mass loss occurs. Published data for this specific configuration is limited in the public domain, so outdoor service life should be validated through site-specific exposure or a comparative weathering programme using a control HDPE of known field performance. Additive compatibility must be checked before any secondary masterbatch is introduced: pro-oxidant additives, unsaturated carrier resins, and certain acid-modified adhesion promoters can antagonise the hindered amine stabiliser package and reduce weathering retention. The use of nitrogen blanketing during compounding and low-shear processing minimises thermal history, but the rotomoulder retains control over final melt quality.

    Compared with a non-UV LLDPE of equal melt flow rate and density, the UV+ grade is not distinguishable by short-term yield stress; the operational difference appears in retained mechanical integrity after outdoor exposure.

    When a Specification Requires Substitution Comparisons Against HDPE and Unmodified LLDPE

    Substitution decisions are driven by the interaction among flexural modulus, environmental stress-crack resistance, and low-temperature ductility. In comparison with a rotational moulding high-density polyethylene of density 0.945–0.955 g/cm³, this LLDPE grade typically exhibits lower flexural modulus and lower Vicat softening point but higher ESCR and greater ductile draw before rupture. In comparison with an unmodified LLDPE of approximately 0.940 g/cm³ density and 4.0 g/10 min melt flow rate, the principal difference is not short-term tensile strength but ultraviolet and colour stability. The grade is not designed to replace high-modulus HDPE in applications requiring stacking rigidity above 120°C, nor to replace very-low-density polyolefins in extreme sub-zero puncture where plastomer-rich blends may outperform. When a designer considers switching from an HDPE rotomoulding grade to the Icorene 3546 UV+ WHI 1101 material, the part thickness should be re-evaluated because flexural modulus differences can alter buckling and load-bearing performance under identical wall sections. Conversely, a change from this grade to HDPE for enhanced stiffness may sacrifice environmental stress-crack resistance in detergent tanks, agricultural chemical service, or cyclic pressure applications.

    Environmental stress-crack resistance is usually measured according to ASTM D1693-21, condition B, 10% Igepal CO-630; long-term chemical resistance should be confirmed in the actual fluid, not assumed from single-point ESCR data.

    Production-scale issues with white UV-stabilised LLDPE rotational moulding powders are often traced to powder handling rather than melt viscosity. In low-humidity environments, electrostatic fines can adhere to mould surfaces and create deposition irregularities. In high-humidity environments, surface moisture can promote agglomeration and bridging in feed hoppers. If the moulded surface shows pinholes, the first variables to examine are venting and oven time rather than melt index; pinhole formation in LLDPE is frequently a bubble-removal problem. Separation of the white pigment during dry flow is uncommon when the material is supplied as a pre-compounded powder, but segregation can occur if the moulder dry-blends regrind or additional pigments. The regrind addition level should be limited by lot-traceable validation; typical practice permits addition of clean in-house regrind, but high regrind ratios can reduce weatherability and shift lot-to-lot colour. Drying is generally unnecessary below 60% RH; above this threshold, surface moisture can be removed at 70–80°C for 1–2 h. Temperatures above 100°C are to be avoided because powder particles can fuse and destroy flowability before the mould is charged.

    On twin-screw compounding lines used upstream, the pre-compounded additive package is incorporated before grinding; the rotomoulder receives no pelletized resin unless a custom size-reduction step is required. Chilled milling helps preserve the stabiliser package by limiting frictional heat.

    Compliance Documentation and Lot-Release Requirements

    Qualification of incoming lots should require a certificate of analysis reporting melt flow rate, density, colour, and particle-size distribution. The material safety data sheet and product safety bulletin are maintained under REACH Regulation (EC) No 1907/2006. Restrictions on hazardous substances for electrical and electronic equipment applications are evaluated under RoHS Directive 2011/65/EU; however, final component compliance depends on all ingredients, regrind, and processing aids. If food-contact service is proposed, migration testing under European Commission Regulation (EU) No 10/2011 or relevant FDA 21 CFR sections is not automatic and must be confirmed against the specific supplier formulation. Internal quality systems at the production site are generally certified to ISO 9001:2015; resin designation may follow ISO 17855-1:2018 and ASTM D4976. Lot acceptance should not rely on a general resin certificate; it should include the actual lot-specific melt flow rate within the agreed control window and a retained plaque for weathering comparison.

    Standards and documentation referenced in qualification
    Standard / DocumentRole
    ISO 1133-1:2022Melt flow rate at 190°C, 2.16 kg
    ISO 1183-1:2019Density by immersion or gas pycnometer
    ISO 527-2:2012Tensile yield stress and elongation at break
    ISO 178:2019Flexural modulus
    ISO 306:2022Vicat softening temperature A50
    ASTM D746-20Low-temperature brittleness temperature
    ASTM D1693-21Environmental stress-crack resistance
    ISO 4892-2:2013Accelerated weathering, xenon-arc, if specified
    ISO 4892-3:2016Accelerated weathering, fluorescent UV, if specified

    Quality issues that occur after lot qualification are often process-induced rather than resin-induced; when a weather-resistant part fails early, the investigation should not only retest melt flow rate but also section the part for thickness distribution, pigment dispersion, porosity, and evidence of under-fusion. Infrared oxidation mapping and gel content measurements can distinguish between molecular damage from processing and insufficient stabiliser dispersion.

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