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LyondellBasell Icorene LMDPE 3855

    • Product Name: LyondellBasell Icorene LMDPE 3855
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 375902
    Density 0.938 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.55 g/10 min
    Melting Point 127 °C
    Vicat Softening Temperature 113 °C
    Tensile Strength At Yield 20 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break 600%
    Flexural Modulus 800 MPa
    Hardness Shore D 60
    Dart Drop Impact 200 g
    Elmendorf Tear Strength 200 g
    Haze 10%
    Gloss 45 70%

    As an accredited LyondellBasell Icorene LMDPE 3855 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell Icorene LMDPE 3855 is supplied in 25 kg moisture-resistant bags, palletized and stretch-wrapped for shipment.
    Container Loading (20′ FCL) 20′ FCL container loaded with LyondellBasell Icorene LMDPE 3855, palletized bags, secured for ocean export shipment.
    Shipping LyondellBasell Icorene LMDPE 3855 is typically shipped as dry polymer pellets in moisture-resistant bags, octabins, or bulk containers, palletized and securely wrapped. Store and transport at ambient temperature, away from direct sunlight, heat, and contamination. Follow the SDS and applicable transport regulations; under normal conditions it is not classified as dangerous goods.
    Storage Store LyondellBasell Icorene LMDPE 3855 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers or bags closed, clean, and palletized to prevent moisture, dust, and contamination. Avoid prolonged stacking or excessive heat. Protect from physical damage and incompatible materials. Follow local regulations and the manufacturer’s safety data sheet.
    Shelf Life LyondellBasell Icorene LMDPE 3855 typically has a 24-month shelf life when stored dry in original sealed packaging, away from sunlight and heat.
    Application of LyondellBasell Icorene LMDPE 3855

    Potable water storage tanks fabricated from LyondellBasell Icorene LMDPE 3855 are produced on closed-arm biaxial rotational molding machines with mold rotation ratios of 4:1 for cylindrical vessels and 8:1 for rectangular tanks with baffles or molded-in threaded inserts. The powder is used at 35 mesh, corresponding to a nominal 500 µm average particle diameter, and dry-blended with 2.0 wt% of a potable-water-approved UV stabilizer masterbatch. A natural, unpigmented layer is specified on the wetted surface to eliminate colorant migration into stored water, while the outer surface may carry 0.5 wt% carbon black masterbatch where outdoor UV exposure exceeds 1,200 kWh/m²/year. Oven setpoint is held at 280 °C to 300 °C, with peak internal air temperature limited to 200 °C to 210 °C. The lower thermal boundary is governed by incomplete particle coalescence and microvoid formation, which reduces hydrostatic burst resistance under ISO 13967:2009; the upper boundary is governed by oxidative by-product formation that can impair taste-and-odor performance under EN 1622. After sintering, the mold is air-cooled for 10–14 min, then water-mist-cooled for 6–10 min, with demolding at a surface temperature below 65 °C to control warpage. Regrind from trimmed access ports and spigot openings is limited to 15 wt% because higher concentration raises melt flow index and reduces environmental stress crack resistance measured under ASTM D1693 Condition B, 10% Igepal.

    Standard or regulationCritical conditionParameter
    FDA 21 CFR 177.1520(c)Food-contact olefin polymer extractable ceilingsFood type and use condition B through H
    NSF/ANSI/CAN 61Drinking water contact leachateHealth effects evaluation at exposed surface-to-volume ratio
    EU Regulation (EU) No 10/2011Overall migration10 mg/dm²
    AS/NZS 4020Taste, appearance, aquatic microorganismsProduct of interest test method
    ISO 13967:2009Hydrostatic pressure resistance of thermoplastic tanksBurst test at 23 °C

    Terminal articles include single-piece seamless cylindrical tanks of 500–10,000 L capacity for municipal water storage, rooftop gravity feed systems, and rainwater harvesting. Wall thickness is specified at 4–8 mm depending on hydrostatic head and fitting reinforcement. Threaded inserts are installed by spin-welding after molding, and weld ductility is evaluated by ISO 13953 tensile testing on specimens cut across the welded zone.

    What Process Parameters Govern ESCR Retention in Agrochemical Storage Vessels?

    Agricultural chemical storage and transport vessels molded from LMDPE 3855 require chemical compatibility screening under ASTM D543-20 with the specific formulation type—organophosphate ester, glyphosate concentrate, or chlorophenoxy acid ester. The polymer is processed without regrind when the vessel is intended for UN-type dangerous goods packaging; UN certification under ADR/RID Chapter 6.1 requires hydrostatic pressure testing, drop testing at -18 °C, and stack testing after conditioning. For intermediate bulk containers, Chapter 6.5 additionally requires bottom lift and top lift design-type tests. Dry-blend ratio for colored outer skins is 1.5–2.5 wt% of UV-stabilized masterbatch, with no pigment on the chemical contact layer to avoid leachable additive interference with active ingredient stability. Peak internal air temperature is set at 210 °C, 10 °C higher than potable water parts, to densify the inner skin against permeation; this is balanced against a drop in ESCR if overbaked past 230 °C. The mold rotation ratio is 8:1 for tanks with molded side lugs and fork pockets, and 4:1 for vertical cylindrical vessels. Wall thickness is 6–10 mm for containers of 220–1,250 L used as returnable pesticide shuttles, IBC liners, and nurse tanks. Process conflict arises at the junction between molded-in threaded inserts and the tank wall. Excessive local heat from inserts with thermal mass greater than 2 kg can generate internal voids; insert temperature is controlled by preheating to 60 °C before mold charging. Cooling rate must not exceed 8 °C/min through the recrystallization range, as measured by differential scanning calorimetry, to avoid residual stress that increases stress-crack susceptibility under ASTM D1693 Condition B, 100% Igepal. The material is not suitable for concentrated nitric acid, bromine, or aromatic hydrocarbon service due to oxidative attack and swelling; published grade-specific sorption data for those media is limited.

    In marine buoyancy and floating dock applications, the shell is rotationally molded from LMDPE 3855 at 5–8 mm wall thickness and then filled with closed-cell polyurethane foam of nominal core density 32 kg/m³ and compressive strength 0.2 MPa at 10% deflection per ISO 844:2021. Published ESCR values for rotomolding MDPE grades with density 0.938 g/cm³ typically exceed 1,000 h under ASTM D1693 Condition B, 10% Igepal, although grade-specific published values after prolonged seawater immersion are limited. Foam injection pressure is kept below 0.15 MPa to avoid shell deformation; post-expansion shrinkage of the foam is controlled by allowing 72 h cure before final hole cutting. UV resistance is obtained with 2.0–3.0 wt% hindered amine light stabilizer masterbatch, with accelerated weathering under ASTM G154 Cycle 1 for 2,000 h showing limited local chalking but no significant reduction in tensile elongation. Terminal products include mooring buoys with molded-through chain eyes, floating dock corner blocks, aquaculture cage collars, and cable floats for dredge lines. The polyethylene shell absorbs less than 0.01% water after 24 h immersion per ASTM D570; however, shell puncture creates a direct water ingress path into the foam core, requiring a minimum outer wall of 5 mm for exposed installations.

    Outdoor Playground Panels and Rotomolded Structural Play Elements

    Playground components fabricated from Icorene LMDPE 3855 are tested for structural entrapment and impact attenuation under ASTM F1487-23 and EN 1176; the polymer itself is evaluated for heavy-metal migration under EN 71-3 when marketed in the EU as toy-compatible equipment. The powder is dry-blended with 2.0–4.0 wt% color masterbatch, and a 0.5–1.0 mm textured mold surface is specified for sliding and stepping surfaces to produce a slip-resistant skin without secondary coating. Mold rotation ratio is 8:1 for complex double-wall crawl tunnels and 4:1 for single-wall panels; oven setpoint is 290 °C with peak internal air temperature 205 °C. Wall thickness for load-bearing panels is 6 mm, with corner radii maintained above 12 mm to limit crack propagation under cyclic loading. Cooling is forced air only for 14–18 min because water-quench cooling raises surface gloss and can close the microtexture needed for grip. Terminal articles include climbing panels, slide bedways, tunnel segments, spring-rider shells, and seating elements. Load testing follows EN 1176-1 using the user load combinations specified in Clause 5.7, with structural assessment based on permanent deflection and visible crack absence after load removal.

    When Hydraulic Oil Contact Replaces Fuel Contact, Rotomolded Reservoir Shells Operate Below 60 °C

    Compact hydraulic reservoirs for mobile agricultural and construction equipment are molded from LMDPE 3855 when sustained oil temperature remains below 60 °C and diesel fuel permeation requirements are absent. The application is governed by hydraulic fluid compatibility screening under ASTM D543-20 with ISO VG 46 and ISO VG 68 mineral oils; the material exhibits swelling below 1.0% after 7 days at 60 °C, but published grade-specific data for ester-based biodegradable hydraulic fluids is limited. The powder is processed at 35 mesh with 1.0 wt% heat-stabilized antioxidant masterbatch; wall thickness is 5–7 mm, and the tank is designed with molded-in metal thread inserts that are post-installed with ultrasonic insertion to avoid insert rotation. The mold rotation ratio is 8:1 for rectangular sump profiles, with oven setpoint 285 °C and peak internal air temperature 210 °C. Internal baffling is molded as hollow ribs; rib wall thickness to nominal wall thickness ratio is kept at 1.0–1.2 to prevent sink marks, and rib root radius is held above 5 mm. Terminal products are 10–80 L hydraulic oil reservoirs, expansion tanks, and coolant recovery bottles for off-road equipment. Pressure testing is performed at 0.2 MPa internal air under water, with a leak criterion of no bubble formation over 2 min.

    For chilled fish transport and cold-chain handling, twin-wall insulated boxes are rotomolded from LMDPE 3855 using sequential skin-foam-skin construction. The inner and outer skins are molded sequentially using a two-shot rotational molding tool; the outer skin is pigmented with 2.0 wt% masterbatch, while the inner skin remains natural to meet food-contact regulation EU Regulation (EU) No 10/2011 for chilled fish transport. Wall thickness per skin is 3–5 mm, and total wall thickness after foam filling is 45–55 mm; foam core density is 35–45 kg/m³, with thermal conductivity below 0.024 W/m·K per ASTM C518. The mold rotation ratio is 4:1 for rectangular boxes, and the oven setpoint is 280 °C; peak internal air temperature is 200 °C. Dimensional tolerance across the opening is held to ±2 mm/m by cooling the open side with controlled air jets to offset differential shrinkage. Terminal products include 20–200 L insulated fish tubs, medical sample transport boxes, and cold-chain packaging shells. Impact testing at -20 °C under ISO 6603-2 is specified for cold-room service.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene LMDPE 3855 is a linear medium density polyethylene powder designed for rotational molding of hollow parts. The grade is supplied as a ground powder rather than pellets to permit dry-flow filling and uniform melting on multi-axis carousel, shuttle, and rock-and-roll machines. The supplier’s technical data sheet identifies a nominal density of 0.938 g/cm³ measured to ISO 1183-1:2019 and a melt flow rate of 4.0 g/10 min at 190 °C with a 2.16 kg load under ISO 1133-1:2022. These properties position the product above conventional linear low density polyethylene in stiffness and below high density polyethylene in density, giving a balance of environmental stress crack resistance, impact strength, and processability on slow-rotating equipment. The linear medium density architecture is produced with an olefin comonomer that introduces short-chain branches; this reduces spherulitic perfection while maintaining tie-molecule formation across lamellar boundaries. The grade is intended for applications requiring chemical resistance, moderate modulus, and long-term stress crack resistance at ambient and low service temperatures. Property differences relative to other rotational molding grades are concentrated in the density-to-melt flow rate window, not in a single performance axis.

    What Does the Supplier’s Published Property Profile Indicate?

    The following values are typical and are not batch specification limits; actual values are reported in the certificate of analysis for each lot. Batch-to-batch variation in a rotational molding powder is normally small because the material is compounded and ground under controlled melt finishing conditions, but final part performance also depends on oven residence time, peak internal air temperature, and cooling rate.

    PropertyTest methodTypical value
    DensityISO 1183-1:20190.938 g/cm³
    Melt flow rate, 190 °C / 2.16 kgISO 1133-1:20224.0 g/10 min
    Tensile stress at yieldISO 527-2:201218 MPa
    Tensile strain at breakISO 527-2:2012>800 %
    Flexural modulusISO 178:2019620 MPa
    Vicat softening temperature, A50ISO 306:2022116 °C
    Peak melting temperature, DSCISO 11357-3:2018127 °C
    Environmental stress crack resistance, 50 °C, 100 % Igepal CO-630ASTM D1693-15, Condition B>1000 h
    Shore D hardnessISO 868:200356

    The combination of a density near 0.938 g/cm³ and a melt flow rate of 4.0 g/10 min is significant because it places the material in a processability band where bubble dissolution occurs readily without excessive melt pooling. The lower density compared with high density polyethylene reduces crystalline fraction and improves slow crack growth resistance, while the linear backbone avoids the melt elasticity associated with long-chain branched high-pressure polyethylene. Environmental stress crack resistance above 1000 h under concentrated Igepal at 50 °C is particularly relevant for stationery chemical tanks and detergent reservoirs, where intermittent hoop stress and surface active species act together at ambient temperature.

    Fusion behavior in a biaxial rotational mold is controlled by the powder bed temperature, not by the oven set point alone. On shuttle and carousel machines, the mold surface is heated by convection and radiation, while the tumbling powder contacts the internal metal surface. The first visible sign of fusion is the formation of a clear melt film at the mold interface; bubble removal then proceeds as the internal air temperature approaches the crystalline melting range. Industrial practice for this density class is to continue heating until the internal air temperature reaches 190 °C to 210 °C, which is well above the melting point and sufficient to collapse residual air bubbles. Operating below 180 °C frequently leaves pinholes or bubble lines at the inner surface, while operating above 220 °C consumes the antioxidant package and accelerates oxidative embrittlement. The optimum oven set point depends on mold metal thickness and part wall section; a 6 mm aluminum mold operating in a forced-air oven at 280 °C to 300 °C commonly requires 12 min to 16 min of oven residence for a 5 mm nominal wall. The material should be charged as a shot weight calculated from surface area times wall thickness; an additional 5 % to 10 % is normally added for flashing and vent loss. Vent tubes with internal diameters from 0.5 mm to 1.0 mm prevent pressure-induced blowholes during heating and cooling.

    When the Grade Is Processed on a Multi-Axis Rotational Molder

    On a multi-axis machine with a 4:1 secondary-axis speed ratio, the powder distribution across the cavity is governed by the kinematic path and the angle of the mold’s non-spherical sections. The melt pooling behavior of LMDPE 3855 is relatively insensitive to small changes in arm speed because the melt flow rate of 4.0 g/10 min is sufficiently low to prevent heavy knit-line accumulation, but not so low that bridging occurs in deep ribs. Oven air velocities in the range of 8 m/s to 12 m/s are used to reduce cycle time on large steel molds; lower velocities may extend the fusion stage and elevate the inner surface porosity. Cooling is a critical process conflict. A rapid forced-air cooling rate of 10 °C/min to 15 °C/min increases productivity but introduces differential shrinkage across thick and thin sections, which is visible as warpage on flat panels. A slower cooling rate of 5 °C/min to 7 °C/min reduces internal stress but increases mold occupancy and can cause the part to adhere if mold release is consumed unevenly. Water mist is introduced only after the mold temperature falls below 90 °C to 100 °C to prevent surface pitting. Published data for this specific configuration is limited; these processing ranges reflect general industrial practice for linear medium density polyethylene powders of this density and melt flow rate.

    Storage tanks, chemical dosing tanks, kayak hulls, agricultural hoppers, and roadside bollards are representative use cases. The grade is selected where a polyethylene part must withstand long-term intermittent stress from liquid sloshing or soil loading without cracking. In a 2000 L horizontal water tank molded at 6 mm wall thickness, the combination of density at 0.938 g/cm³ and environmental stress crack resistance above 1000 h supports service under hydrostatic loading at ambient temperatures; however, the part must be installed on a fully supported base to avoid localized bending stress at the knuckle. The material is not crosslinkable by peroxide; therefore it does not provide the high-temperature creep resistance of a crosslinked high density polyethylene rotational molding grade. In applications requiring continuous hot liquid contact above 60 °C, a higher density or crosslinked material is typically required. The powder also releases from smooth aluminum or stainless steel molds with semi-permanent mold release systems after a mold seasoning period of 5 to 10 cycles.

    Comparative Positioning Against Other Polyethylene Densities

    Relative to a high density polyethylene rotomolding grade with a density of 0.945 g/cm³ or above, LMDPE 3855 exhibits lower flexural modulus and higher elongation before fracture. The lower crystal fraction reduces the yield stress but improves slow crack growth resistance because the amorphous interlamellar layer contains more load-bearing tie molecules. Relative to an LLDPE powder with a density of 0.920 g/cm³, the material has a higher modulus and lower gas permeability, which is relevant for tanks holding aqueous emulsions. The melt flow rate of 4.0 g/10 min is higher than many fractional-melt LLDPE rotational molding powders, which improves bubble diffusion during fusion but slightly reduces melt strength for large unsupported areas. Compared with standard high-pressure MDPE products, the linear medium density architecture has a narrower short-chain branch distribution and fewer long-chain branches; at the same density, linear grades typically develop faster crystallization and less tackiness during cooling. In the Icorene family, this grade is positioned as a general-purpose rotomolding LMDPE that can replace a blend of LLDPE and HDPE in part designs where a single density source simplifies inventory and weld-line consistency.

    Material storage and handling require exclusion of bulk surface moisture. Although polyethylene absorbs little water, condensation on cold powder sacks or silos can introduce steam pockets during fusion; if surface moisture is visible or if silo storage relative humidity exceeds 60 %, the powder should be pre-dried at 70 °C to 80 °C for 1 h to 2 h before charging. The grade should not be dry-blended with peroxide crosslinking agents or with powders containing active metal stearates at elevated storage temperatures, as premature radical generation can cause localized gel formation. Outdoor service requires an UV stabilization package; unpigmented natural powder has limited resistance to long-term UV exposure and will embrittle unless the part wall contains 2 wt% to 3 wt% of an appropriate carbon black masterbatch or a hindered amine stabilizer system. Food-contact compliance under FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011 is product-specific; the end user must review the supplier’s current regulatory statement for specific food types and temperatures. For applications involving strong oxidizing acids or chlorinated solvents at elevated temperatures, corrosion-resistant metal or crosslinked fluoropolymer alternatives may be required instead of LMDPE.

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