Lyondellbasell Icorene 3546 Gry 7798 Polyethylene Linear Low Density

LyondellBasell Icorene 3546 GRY 7798 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3546 GRY 7798 Polyethylene, Linear Low Density
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 266872
    Polymer Type Linear Low Density Polyethylene (LLDPE)
    Color Grey 7798
    Density 0.935 g/cm3
    Melt Flow Rate 3.5 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 14.0 MPa
    Tensile Strength At Break 20.0 MPa
    Elongation At Break 800%
    Flexural Modulus 0.700 GPa
    Hardness Shore D 55
    Vicat Softening Point 115°C
    Brittleness Temperature -70°C
    Processing Method Rotational Molding

    As an accredited LyondellBasell Icorene 3546 GRY 7798 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 Typically supplied in 25 kg multiwall bags, 40 bags per pallet (1,000 kg net weight).
    Container Loading (20′ FCL) 20′ FCL loaded with LyondellBasell Icorene 3546 GRY 7798 Linear Low Density Polyethylene, palletized bags, shrink-wrapped and secured for ocean shipment.
    Shipping LyondellBasell Icorene 3546 GRY 7798 Polyethylene, Linear Low Density is a non-hazardous thermoplastic resin. Ship in original sealed 25 kg bags, octabins, or bulk trucks/containers. Keep dry, clean, and away from heat, sunlight, and contaminants. No special dangerous goods labeling required. Ambient transport.
    Storage Store LyondellBasell Icorene 3546 GRY 7798 Polyethylene, Linear Low Density in a cool, dry, well-ventilated area. Keep containers closed, off floors, away from direct sunlight, heat, ignition sources, moisture, and strong oxidizers. Prevent contamination and dust accumulation. Use appropriate PPE and follow the manufacturer’s SDS and local regulations. Store away from incompatible materials.
    Shelf Life Shelf life is typically 12 months when stored in a cool, dry, well-ventilated area in original unopened packaging away from sunlight.
    Application of LyondellBasell Icorene 3546 GRY 7798 Polyethylene, Linear Low Density

    LyondellBasell Icorene 3546 GRY 7798 is a pulverized linear low-density polyethylene rotational moulding feedstock; the grey colour formulation introduces carbon black or mixed metal oxide pigments that modify radiant heat absorption in the oven. In chemical containment service, the powder is charged directly into cast aluminium or fabricated carbon steel moulds and consolidated on carousel-type rotational moulding machines with biaxial rotation ratios typically between 3:1 and 5:1. Published grade-specific rheological and mechanical data for this exact grey-coloured configuration remain limited; consequently, first-run process validation must use test coupons taken from the intended mould rather than datasheet values for natural LLDPE. The densification window is governed by the peak internal air temperature, which for rotomoulded LLDPE normally falls between 190°C and 230°C. Oven air temperatures may be set from 260°C to 320°C depending on mould gauge and part wall thickness. Sustained internal air temperatures above 250°C accelerate thermo-oxidative chain scission and are a known cause of premature environmental stress crack resistance loss in the finished tank. A minimum wall thickness of 4 mm to 10 mm is generally required for upright storage tanks below 20,000 L fabricated under ASTM D1998-21. Particle size distribution controls sintering and bubble elimination; pulverized rotomoulding LLDPE typically shows a d50 between 150 µm and 250 µm and a maximum top size below 500 µm, though grade-specific sieve data should be verified by ISO 4610 air-jet sieving. Large particles above 500 µm that survive the oven dwell produce microporosity at mould corners and thin sections, and this porosity cannot be corrected by prolonging the cycle after the inner wall has sealed.

    Failure modes in chemical containment are dominated by environmental stress cracking rather than tensile overload. Storage of surfactants, wetting agents, mineral acids, or aliphatic hydrocarbons at continuous service temperatures above 40°C can reduce the stress crack resistance measured under ASTM D1693-21 Condition B. A practical control in tank design is to keep hoop stress below the long-term material limit; when no grade-specific ESCR data exist, the moulder specifies additional wall thickness in the bottom knuckle, outlet boss, and sidewall transition regions where biaxial orientation is insufficient. Field observations from rotational moulding shops indicate that uneven cooling at the mould parting line creates residual stress that accelerates ESCR at the waterline. A forced-air cooling segment followed by water mist at 1°C to 3°C per minute is commonly used for cylindrical containment vessels; cooling rates above 5°C/min on flat sidewalls increase warpage and create visible sink marks at internal bosses. Chemical compatibility is assessed through ASTM D543-21 immersion protocols, with coupons taken from flat-cut sections of tank wall rather than injection-moulded plaques because wall thickness and microvoids influence mass uptake. The material is not intended for prolonged exposure to strong oxidizers, aromatic solvents, or chlorinated hydrocarbons above 23°C; published immersion data for Icorene 3546 GRY 7798 in those media are limited.

    Control tests applied to rotomoulded LLDPE chemical tanks
    Control parameterStandard/methodApplication relevance
    Melt flow rate at 190°C/2.16 kgISO 1133-1:2022Indicates sinter flow and densification during oven dwell; low MFR can leave pinholes in narrow ribs.
    DensityISO 1183-1:2019Correlates with stiffness and ESCR balance in tank walls.
    Environmental stress crack resistanceASTM D1693-21 Condition BKey threshold for surfactant and chemical storage service.
    Tensile yield stress and elongationASTM D638-14Used to verify mechanical integrity of flat wall sections.
    Falling-weight impactASTM D5420-21Detects brittle failure at low temperatures in finished tank coupons.
    Chemical immersionASTM D543-21Evaluates mass change and dimensional shift after liquid exposure.

    Venting and mould release have a direct influence on pinhole formation. Vent tubes should be sized to prevent pressure buildup while minimizing gas leakage; if the vent is obstructed, gas generates porosity at the last point to seal. Semi-permanent mould release coatings based on silicone or PTFE reduce demoulding force but can create surface contamination; residual coating should be monitored by water-break-free inspection or adhesion pull-off. Internal air pressurization during cooling at 5 kPa to 15 kPa is sometimes applied to limit shrinkage and improve flatness; excessive pressure can blow open the parting line and produce flash. Surface moisture on the pulverized feedstock must also be controlled before charging. When storage relative humidity exceeds 60%, pre-drying at 60°C for 2 h using a dehumidified air drier is common practice to prevent steam-induced pinholes along mould parting lines. Lumps above 1 mm should be screened out before charging; agglomerated fines can produce hard particles that leave local blemishes and non-uniform pigmentation in the finished wall.

    What Changes When Grey Powder Is Rotomoulded into Large Agricultural Water Cisterns?

    In agricultural water storage, the service environment shifts from concentrated chemical exposure to long-term ultraviolet radiation and intermittent hydrostatic loading. Icorene 3546 GRY 7798 is processed into single-piece cisterns with capacities commonly above 1,000 L; large moulds may require wall thicknesses from 5 mm to 12 mm to resist hydrostatic pressure and soil settlement. The grey pigment system contains carbon black, which acts as a UV absorber and retards surface photo-oxidation. However, carbon black also increases infrared absorbance during the oven residence period. Moulders running large cisterns sometimes reduce peak internal air temperature by 3°C to 5°C compared with natural LLDPE to limit surface oxidation, but this adjustment is empirical and must be validated for each mould geometry. Outdoor weathering resistance is evaluated by ISO 4892-2:2021 xenon-arc exposure or ASTM G154-23 fluorescent UV cycling. Comparative weathering results are used to rank formulations; they do not predict absolute outdoor life without benchmark data from a known reference grade. A common acceptance criterion for rotomoulded agricultural tanks is retention of at least 50% of initial tensile elongation after 3,000 h of accelerated weathering, but published data for this specific grey grade are limited. Microbiological surface fouling in water tanks is not a polymer failure mechanism; however, rough inner surfaces from incomplete sintering can retain organic matter, and a smooth dense inner skin is achieved by controlling peak internal air temperature above 190°C.

    Marine flotation chambers are rotomoulded as closed double-wall structures with the annulus filled with closed-cell polyurethane foam after demoulding. The LLDPE skin must remain free of pinholes because foam injection into a partially densified inner wall creates exothermic pressure and can rupture thin sections below 3 mm. Icorene 3546 GRY 7798 powder flows into deep cavity features of foam-filled buoys when the rotation ratio is maintained near 4:1 major-to-minor axis, but no universal ratio applies to shallow flotation bodies; moulders tune the ratio to avoid bridging at the top pole. Wall thickness from 3 mm to 8 mm is typical for buoy skins, while high-impact areas around mooring eyes may require local thickening up to 12 mm. Low-temperature impact resistance is evaluated by Gardner falling-weight impact per ASTM D5420-21 or ISO 6603-2; brittle failures below -20°C are not expected in properly sintered LLDPE, but carbon black-pigmented grey grades can show a slight increase in notch sensitivity at very high pigment loadings. Published data for this exact colour grade in seawater immersion are limited. Water absorption after 24 h immersion per ASTM D570-22 typically gives a mass gain below 0.05% for unfilled LLDPE, though the grey formulation should be tested separately. Adhesion of rigid closed-cell foam to untreated LLDPE is primarily mechanical; mould release residues and incomplete densification at the inner surface reduce foam adhesion, while sanding or corona treatment of the inner cavity before foaming improves mechanical interlock. Outdoor buoy deployments require anti-fouling topcoats, but solvent-borne antifouling paints may contain aromatic solvents that soften the LLDPE surface; compatibility is tested by ASTM D543-21 immersion before production.

    When Diesel Fuel Contact Replaces Aqueous Service in Double-Walled Tanks

    In diesel fuel storage, the service environment imposes chemical sorption and permeation constraints that are absent in water tanks. Linear low-density polyethylene absorbs aliphatic hydrocarbons and swells; continuous contact with diesel at 23°C can reduce tensile modulus and creep resistance, although grade-specific data for Icorene 3546 GRY 7798 are limited. Double-walled diesel tanks are rotomoulded with an inner wall and an outer containment shell joined at the fill neck. The fill neck is a known failure location because the insert or gasket creates a sharp thermal gradient and local wall thinning. Processors therefore extend the oven dwell until the inner wall at the neck reaches a minimum peak internal air temperature of 210°C; below this temperature the polymer retains unmelted grain boundaries, creating a permeation path and a potential leak under vibration. A wall thickness of at least 6 mm is often specified for small diesel day tanks to reduce hydrocarbon permeation, but this thickness alone does not meet underground storage emission limits without surface fluorination or a barrier layer. Hydrocarbon permeation is evaluated in-house by gravimetric cup methods; published standard fuel permeation data for this exact grey grade are not widely available. Low-temperature impact integrity is verified by drop tests at -40°C following UN/ECE R34 or OEM-specific protocols. Field results indicate that bottom seams are the most sensitive because wall thickness at the seam typically decreases to between 70% and 85% of nominal. Ultrasonic thickness mapping across the bottom seam after demoulding is therefore used to establish process capability before batch production.

    Where polyethylene is used for hoppers and bulk solids discharge bins, the dominating design factor is abrasion resistance rather than chemical exposure. Icorene 3546 GRY 7798 is processed into seamless, one-piece bins with integrally moulded flanges; the absence of welded seams eliminates the crevice corrosion and crack initiation points observed in fabricated steel or welded thermoplastic containers. Abrasion resistance of linear low-density polyethylene is lower than that of UHMWPE, so a wear liner or replaceable pad is required for handling quartz sand, glass fines, or metal swarf. Dry-sand rubber wheel testing per ASTM G65 can be used for relative ranking, but grade-specific published mass loss values are limited. Wall thickness in hoppers typically ranges from 4 mm to 8 mm, with thicker sections near discharge openings. Rotomoulded LLDPE bins are rated for continuous use at temperatures below 60°C; hot product above 70°C can cause creep and wall distortion under fill head pressure. The grey colour reduces visible staining from dark mineral fines compared with unpigmented LLDPE, but this observation is aesthetic rather than a mechanical advantage.

    Underground Utility Vaults and Septic Tank Risers

    Buried vaults and risers are subject to external earth pressure, groundwater buoyancy, and internal hydrogen sulfide attack in sanitary applications. The rotomoulded LLDPE vault wall is designed for intermittent traffic loading when covered with a cast-iron frame; the wall thickness under the frame flange is increased to 10 mm or 12 mm to resist point loads. HDPE and LLDPE parts in buried service are evaluated for environmental stress cracking under ASTM D1693-21; the presence of wetting agents in septic effluent increases the stress crack potential at the riser-to-vault joint. Moulders often specify ESCR testing of rotomoulded coupons taken from the knuckle radius, not from flat tank bodies, because cooling rate differences alter crystallinity and residual stress. Carbon black-pigmented grey LLDPE absorbs infrared in the oven and can produce a more uniform crystalline structure if the cooling cycle maintains a steady rate below 3°C/min; rapid quenching at the mould surface has been reported to lower ESCR in flat panels by creating a less ordered boundary layer. These field observations are qualitative and do not replace standard batch testing. Structural acceptance is covered by local plumbing codes and ASTM D1998-21 as applicable to upright tanks and vault covers.

    Thermo-Oxidative Induction Time of Grey Rotomoulded Panels After Outdoor Weathering

    Outdoor enclosures, pump covers, and equipment housings are moulded with repeatable grey colour and require slow degradation under continuous sunlight. Oxidative stability is measured by oxidation induction time using differential scanning calorimetry per ISO 11357-6:2018. For outdoor applications, processors specify a minimum initial oxidation induction time at 210°C of 20 min to 60 min depending on the antioxidant package, but this value cannot guarantee service life because antioxidant consumption is nonlinear. In carbon black-pigmented LLDPE, the surface temperature under direct sunlight can reach 80°C in desert climates, accelerating antioxidant depletion. The grey colour of Icorene 3546 GRY 7798 moderates surface temperature compared with black but has lower UV absorption than full carbon black; published grade-specific weathering data are limited. A frequent processing issue in large flat enclosures is inner-surface bubble formation due to moisture from unpurged mould venting or insufficient pre-drying. The resulting pinholes are detected by visual inspection under internal pressurization at 10 kPa to 20 kPa; this non-destructive test reveals leaks that are not visible from the outer surface. Batch acceptance for outdoor enclosures is therefore based on oxidation induction time retention after accelerated weathering, not on initial tensile strength alone.

    Free Quote

    Competitive LyondellBasell Icorene 3546 GRY 7798 Polyethylene, Linear Low Density prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618005193850

    Email: sales8@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3546 GRY 7798 is a pre-compounded, gray-pigmented linear low-density polyethylene powder supplied for rotational moulding of hollow parts. The designation encodes the base resin grade, Icorene 3546, and a proprietary gray colour package, GRY 7798, in which the pigment is dispersed into the polymer matrix before delivery. The material is classified chemically as LLDPE and is supplied as a powder rather than pelletized resin because rotational moulding requires controlled particle size distribution for dry flow, bulk density, and particle coalescence under low-shear heating. The pre-coloured formulation removes the need for separate addition of liquid or powder colour at the moulding machine and is specified where consistent grey colour, lot-to-lot appearance control, and elimination of dry-colour streaking are required.

    Rotational moulding of Icorene 3546 GRY 7798 is directed at large hollow parts requiring wall thicknesses of 3–10 mm, including storage tanks, agricultural reservoirs, machinery housings, and transport containers. LLDPE is selected for these applications because the molecular structure resists slow crack growth in the presence of surfactants, fuels, and alkaline liquids; the grey colour is generally specified for soiling visibility or aesthetic requirements rather than as a structural performance additive.

    Because published data for the pre-coloured GRY 7798 variant are less complete than those for the natural 3546 base resin, the representative values in Table 1 are drawn from the Icorene 3546 base resin envelope and analogous LLDPE rotomoulding grades. They are not lot-specific release limits and must be superseded by the supplier’s certificate of analysis.

    PropertyTest methodRepresentative range for 3546 base resin
    Melt flow rate, 190 °C/2.16 kgISO 1133-1:20224.0–5.0 g/10 min
    DensityISO 1183-1:20190.934–0.936 g/cm³
    Tensile yield strengthISO 527-2:201216–19 MPa
    Tensile elongation at breakISO 527-2:2012>400 %
    Flexural modulusISO 178:2019600–750 MPa
    Vicat softening temperature, A50ISO 306:2022110–118 °C
    Environmental stress cracking resistance, F50, 100 % Igepal CO-630ASTM D1693-21>500 h

    How Does the 3546 Base Resin Differ from Film-Grade LLDPE?

    Although both materials are classified as linear low density polyethylene, the 3546 base resin is formulated for pressure-free sintering in a rotating mould, whereas film-grade LLDPE is designed for high-shear blown-film extrusion. Film-grade LLDPE typically exhibits a melt flow rate below 2.0 g/10 min for bubble stability and tear resistance; rotomoulding grades such as 3546 operate in the 3–6 g/10 min range to permit particle coalescence without extruder-induced compaction. The molecular architecture of rotomoulding LLDPE is adjusted to limit long-chain branching and reduce terminal unsaturation, which slows crystallization and extends the window for bubble release before solidification. The 3546 grade is delivered as rotomoulding powder with a controlled particle size envelope and not as film pellets; a pelletized film resin cannot be substituted without grinding to a rotomoulding-specific top size near 500 µm and controlled fines below 150 µm. The additive package also differs: film antioxidants and slip agents are selected for continuous extrusion stability, while rotomoulding stabilizers are selected for longer oven residency times and multiple cycles of heating and cooling.

    Peak Internal Air Temperature and Cooling Rate Define the Processing Window

    On a carousel or shuttle-type biaxial rotational moulding machine operating at a 4:1 primary-to-secondary speed ratio, oven settings for LLDPE rotomoulding powder are commonly maintained between 280 °C and 320 °C. The controlling variable is the peak internal air temperature inside the mould cavity. For the 3546 base resin, a PIAT of 190–205 °C is typical for acceptable densification. If PIAT remains below 175 °C, the melt viscosity is too high for complete particle coalescence; the result may include pinholes, microvoids, weld-line porosity, and tensile elongation below the value reported in Table 1. If PIAT exceeds 215 °C, oxidative degradation of the polyethylene backbone and antioxidant depletion can occur, and the grey pigment dispersion may shift toward yellow as the polymer matrix degrades. In a carousel rotomoulding line with multiple arms, batch-to-batch PIAT drift of 5–10 °C can occur after a tool change because the steel or aluminium mould mass alters the heat sink. A thermocouple inserted into the mould cavity or an infrared pyrometer aimed at the inner surface should be used to reset oven residence time, not simply the oven setpoint.

    Cooling should be staged: forced-air cooling through the crystallization plateau at 100–110 °C at 0.5–1.5 K/min limits spherulite growth and shrinkage, while water mist or fine water spray is applied only after the part surface drops below 90 °C. Demoulding before the part core reaches 70 °C can increase warpage because the flexural modulus of the semi-crystalline matrix remains below the level needed to resist ejector and handling stresses. Mould dimensions must also compensate for LLDPE rotomoulding shrinkage, which typically ranges from 1.5–2.5 % depending on wall thickness, cooling rate, and pigment content. On aluminium moulds, grey pigment build-up can increase demoulding force; external mould release may be required for wall thicknesses below 3 mm or deep undercuts.

    Dry flow of rotomoulding powders is commonly measured by ASTM D1895-21 with a funnel orifice of 10 mm. A typical rotomoulding LLDPE powder flows through a 10 mm orifice in 25–35 s/100 g; this range supports uniform filling of complex mould channels. Powder bulk density for LLDPE rotomoulding grades is generally 0.35–0.45 g/cm³, and a lower bulk density can increase mould fill time but may improve air release. Fines below 150 µm should be controlled because they can become airborne, increase dust explosion risk, and cause surface bubbles when the powder bed sinters unevenly.

    The pre-coloured GRY 7798 powder introduces a pigment effect that is absent from the natural 3546 compound. Inorganic grey pigments can act as nucleating agents and shift the crystallization peak by 1–4 °C relative to natural LLDPE, which may require a 2–5 °C reduction in mould cavity temperature to maintain the same undercutting or shrinkage. Because the pigment is already dispersed, high-shear dry blending that can break particles and generate fines is not required. Regrind from grey parts should be segregated from natural or white powder, and rework ratios above 30 wt% should be validated by measurement of tensile elongation and impact energy because regrind particle shape and bulk density differ from virgin powder.

    When Post-Moulding Assembly Requires Adhesive Bonding or Welding

    Low surface energy limits adhesive wetting on Icorene 3546 GRY 7798. Untreated polyethylene generally has a surface energy of 30–32 mN/m; adhesive bonding requires pretreatment by flame, corona discharge, or air plasma to raise surface energy above 40–44 mN/m. Without pretreatment, pressure-sensitive and structural adhesives may fail adhesively at the interface. Hot plate welding of LLDPE rotomoulded parts is typically conducted at a plate temperature of 180–210 °C and weld pressure of 0.05–0.15 MPa; plate temperatures above 230 °C can produce oxidative weld-line degradation. For ultrasonic welding of grey-pigmented material, the pigment can raise acoustic attenuation compared with natural LLDPE, and welding speeds may need to be reduced by 10–20 % to achieve equivalent joint strength. Published process data for this specific grey pre-compound are limited; production-scale validation is required because geometry, wall thickness, and moulding residual stress can alter joint strength more than the pigment alone.

    Table 2 compares the product envelope with two alternative rotomoulding chemistries used for similar hollow parts.

    AttributeIcorene 3546 GRY 7798 LLDPEHDPE rotomoulding gradeCrosslinkable PE rotomoulding grade
    Density range0.934–0.936 g/cm³0.940–0.955 g/cm³0.925–0.945 g/cm³
    Flexural modulus600–750 MPa900–1400 MPa500–900 MPa
    ESCR, ASTM D1693-21>500 h50–150 h>500 h
    Regrind useThermoplastic regrind acceptableThermoplastic regrind acceptableThermoset behaviour limits regrind to filler or low-percentage rework
    Cure stepNoneNonePeroxide cure required above 150 °C
    Colour controlPre-compounded grayNatural or dry colourNatural or dry colour

    The comparative values are typical of commercial rotomoulding grades; lot-specific values for the named product must be confirmed by the supplier.

    Regulatory Status and Food-Contact Constraints

    The uncoloured LLDPE base resin generally falls under the olefin polymer clearances in FDA 21 CFR 177.1520(c) 3.2a, provided that end-use conditions comply with the extraction limits in that section. The grey pigment package in GRY 7798 is not automatically covered by the base-polymer clearance and must be verified separately for direct food-contact use. For European supply, the material safety data sheet and REACH registration are the controlling documents; rotomoulding-grade LLDPE powders are typically not classified as dangerous substances, but the colour concentrate may contain trace inorganic metals. RoHS Directive 2011/65/EU compliance for lead, cadmium, mercury, hexavalent chromium, PBB, and PBDE should be confirmed for the homogeneous material, with lead and cadmium restricted to 1000 ppm and 100 ppm, respectively. Published compliance data for the pre-coloured GRY 7798 configuration are limited; a written supplier statement is required before use in regulated packaging, potable water, or children’s products.

    Storage and handling impose additional boundaries. The powder should be kept in sealed containers at 20–30 °C and below 60 % relative humidity. Although LLDPE is hydrophobic, surface condensation on cold powder can introduce moisture that forms steam pinholes during heating. The powder should not be stored in direct sunlight or near oxidizing agents, and sustained storage above 60 °C may deplete antioxidants and shift the melt flow rate. Electrostatic grounding and explosion-rated vacuum systems should be used during powder transfer. Regrind from trimmed parts may be reused, but its particle size distribution, bulk density, and colour uniformity differ from virgin powder; unscreened regrind above 30 wt% can reduce dry flow and increase surface roughness. Mixing GRY 7798 with natural or white powder is not recommended for parts requiring exact colour and opacity, because incomplete dispersion will appear as streaks or mottling rather than as discrete defects detectable by ordinary mechanical testing.

    Top