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ExxonMobil Exceed mLLDPE 1018HA

    • Product Name: ExxonMobil Exceed mLLDPE 1018HA
    • 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 796504
    Product Name ExxonMobil Exceed mLLDPE 1018HA
    Polymer Type Metallocene Linear Low Density Polyethylene
    Catalyst Type Metallocene
    Comonomer Hexene-1
    Density 0.918 g/cm³
    Melt Index 1.0 g/10 min
    Peak Melting Temperature 118 °C
    Vicat Softening Temperature 95 °C
    Tensile Strength At Yield 8.3 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break 500 %
    Flexural Modulus 200 MPa
    Dart Drop Impact 200 g
    Elmendorf Tear Strength Md 200 g
    Elmendorf Tear Strength Td 300 g
    Haze 6 %
    Gloss 70 %

    As an accredited ExxonMobil Exceed mLLDPE 1018HA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing ExxonMobil Exceed mLLDPE 1018HA is supplied as pellets in 25 kg polyethylene bags, typically stacked on pallets for storage and transport.
    Container Loading (20′ FCL) ExxonMobil Exceed mLLDPE 1018HA metallocene polyethylene resin in palletized bags, securely loaded into a 20′ FCL container for ocean transport.
    Shipping ExxonMobil Exceed mLLDPE 1018HA is a non-hazardous polyethylene resin, typically shipped as pellets in 25 kg polyethylene bags stacked on stretch-wrapped pallets. Bulk truck or railcar delivery may be available. It is not classified as dangerous goods for transport. Store dry, away from heat, sunlight, and contamination.
    Storage Store ExxonMobil Exceed mLLDPE 1018HA in a clean, dry, well-ventilated area, preferably in sealed original bags or containers. Keep away from direct sunlight, heat sources, moisture, contamination, and incompatible materials. Maintain moderate, stable temperatures and avoid prolonged UV exposure. Stack pallets safely. Do not store outdoors. Use first-in, first-out stock rotation. Follow local regulations and supplier guidance.
    Shelf Life ExxonMobil Exceed mLLDPE 1018HA typically has a two-year shelf life when stored dry, cool, and in original packaging away from sunlight.
    Application of ExxonMobil Exceed mLLDPE 1018HA

    On a cast film line with a 1,500 mm wide coathanger die and 0.8 mm die gap, ExxonMobil Exceed mLLDPE 1018HA is processed as the primary skin layer in high-speed pallet wrap at nominal thicknesses of 12 µm to 25 µm. The resin's 0.918 g/cm³ density and 1.0 g/10 min melt flow index, determined per ASTM D1238 at 190°C/2.16 kg, permit draw-down at line speeds between 150 m/min and 300 m/min without the bubble instability encountered in blown-film conversion. Neck-in is managed by dry tumble blending 10–20 wt% of a fractional-melt LDPE with 0.25 g/10 min melt index into 1018HA before the material enters a 75-mm single-screw extruder with 33:1 L/D and a Maddock mixing section. Processing temperatures are set from 230°C at the feed throat to 255°C at the die, while the chill roll temperature is held between 18°C and 22°C to limit post-extrusion crystallinity. A 20 µm cast web tested per ASTM D882 at 500 mm/min typically records machine-direction elongation at break above 400% and cross-direction elongation above 600%; dart impact measured on 20 µm film per ASTM D1709 Method A commonly falls between 120 g and 200 g, with the lower bound observed when reclaim content exceeds 18 wt%. In stretch-wrapper trials, the cast film retains 90% of its initial load-holding force after 24 h at 5°C, though the specific value depends on pre-stretch ratio and gauge uniformity. The operational boundary is tied to moisture: when ambient relative humidity exceeds 60%, surface moisture on reclaim granules becomes a gel-generating contaminant at the die lip, and reclaim must be dried at 60°C for 2 h before blending. Terminal product is machine pallet wrap in which 1018HA provides puncture resistance and cling-layer compatibility within a seven-layer structure.

    Heat Seal and Hot Tack Thresholds Shift with Line Speed

    Vertical form-fill-seal line speeds above 80 cycles/min on a 10-head rotary jaw machine with 0.4 s dwell time shift the controlling seal parameter from ultimate seal strength to hot tack measured per ASTM F1921 Method A. Although published data for this specific resin is limited, production records from rotary jaw equipment place the peak hot tack of 1018HA near 105°C, with a practical sealing window of ±5°C when the acceptance threshold is 0.3 N/15 mm. Below 100°C the sealant layer fails cohesively and produces high leaker rates in frozen-food packs; above 115°C seal bead elongation transfers stress to the web and causes mis-tracking through the stripping station. The narrow processing window is widened by blending 80 wt% 1018HA with 20 wt% of a 0.25 g/10 min melt index LDPE in a gravimetric batch blender; the blend raises the hot tack plateau to ±8°C and shifts the peak by less than 2°C. The sealant layer is extruded from a 55-mm barrier screw with 28:1 L/D at 6–10 µm thickness as the inside layer of a three-layer structure: 12 µm sealant / 60 µm core / 30 µm print layer. The sealant layer complies with FDA 21 CFR 177.1520 for olefin polymer food contact. Finished 1-kg frozen vegetable pillow packs are inspected by burst testing at -20°C; seal strength after 24 h at that temperature is not less than 4 N/25 mm when tested per ASTM F88 at 300 mm/min. The limiting operational interaction is jaw temperature control: thermocouple drift of ±3°C across the 10 jaw pairs is sufficient to produce leaker rates above 0.5% unless the machine is calibrated at shift boundaries.

    A core blend of 70 wt% 1018HA and 30 wt% of a 0.3 g/10 min melt index LDPE is pre-compounded in a corotating twin-screw extruder with 40:1 L/D and 50 mm screw diameter before being converted into 80 µm heavy-duty sack film. On a 250-mm diameter three-layer blown-film die with a dual-lip air ring, the core is coextruded with neat LDPE skins at a die gap of 2.3 mm, a blow-up ratio of 2.5:1, and a melt temperature of 205°C. Internal bubble cooling at 15°C air temperature is required when output exceeds 20 kg/h per 250 mm die diameter. If the LDPE fraction in the core exceeds 30 wt%, a 1–2 Hz frost line oscillation is observed on ultrasonic bubble diameter sensors, and corrective action is limited to reducing screw speed until output falls below 18 kg/h. Mechanical testing on 80 µm film per ASTM D882 gives machine-direction tensile yield strength near 11 MPa and cross-direction tensile yield strength near 11.5 MPa; Elmendorf tear resistance measured per ASTM D1922 is the limiting property in sack drop performance. Reported production data indicate that replacing the LDPE fraction with neat mLLDPE can reduce machine-direction tear by up to 20%, so the 70/30 blend is retained for tear performance and bubble stability. Melt temperatures above 230°C are avoided because gel formation from oxidative crosslinking accelerates. Terminal product is a 40-kg fertilizer sack film whose drop-test acceptance follows ISTA 1A procedures at 1.2 m.

    Can 1018HA Serve as an Extrusion Lamination Tie Layer on High-Speed Liquid Packaging Board?

    The use of 1018HA as an extrusion lamination tie layer on liquid packaging board is constrained by its 1.0 g/10 min melt flow index and relatively low melt strength, but it is technically workable when coextruded or blended with a high-pressure LDPE. On a laminator with a 1,200-mm flat die, 0.8 mm die gap, and three-roll stack, the melt temperature is set between 280°C and 300°C. A 70/30 wt% blend of 1018HA and a 0.7 g/10 min melt index LDPE is fed to a 90-mm extruder with 30:1 L/D and barrier screw to produce coating weights of 20–25 g/m² at line speeds from 120 m/min to 180 m/min. Neck-in at the die exit is held below 25 mm per side by the LDPE fraction and by maintaining an air gap between 100 mm and 150 mm. Adhesion to aluminum foil substrate is measured by T-peel at 180° angle; production records show peel strengths between 2.0 N/15 mm and 3.5 N/15 mm when the foil is preheated to 60°C by the laminator. The narrow molecular weight distribution of 1018HA reduces gel flecks compared with older Ziegler-Natta C8-LLDPE materials, but draw resonance appears above 180 m/min unless the LDPE content is raised to 40 wt%. Pinhole density in 20 g/m² coating is assessed by dye penetration per ASTM D3078; values below 0.5 defects/m² are achievable if melt temperature is held below 300°C. Pre-drying at 70°C for 3 h is required when ambient relative humidity exceeds 60% because hydrolytic degradation of reclaimed edge trim increases pinhole formation. Terminal product is a gable-top carton lamination layer in which 1018HA contributes low extractables under EU 10/2011 overall migration limit of 10 mg/dm² and heat-seal compatibility under FDA 21 CFR 176.170(c) for paperboard coatings.

    When 1018HA Is Let Down into Agricultural Silage Film with High Reclaim Content

    Agricultural silage wrap is processed on a three-layer blown-film line with a 300-mm die, 2.1 mm die gap, and an oscillating haul-off. A 45 µm film structure uses a core layer containing 50 wt% 1018HA, 30 wt% pelletized post-industrial LLDPE reclaim, and 20 wt% LDPE; the outer layers are neat LDPE or a 50/50 LDPE-1018HA blend depending on tack requirement. The melt temperature is limited to 210°C at the die to minimize oxidative degradation of the reclaim, and continuous screen filtration uses a 120/200 mesh screen pack to remove gel particles. The presence of reclaim above 30 wt% produces a measurable increase in dart impact variability; when tested per ASTM D1709 Method A on 45 µm film, the coefficient of variation rises from 5% to 18% as reclaim reaches 40 wt%. Puncture resistance is determined by ASTM D5748, and production records show that 45 µm silage wrap containing 50 wt% 1018HA retains a puncture energy above 0.5 J after 12 months outdoor exposure under UV stabilization with hindered amine light stabilizers. The operational constraint is pre-drying of reclaim at 70°C for 4 h when ambient relative humidity exceeds 60%; failure to dry produces hydrolysis-induced surface roughness and a reduction in film gloss measured by ASTM D523 at 60° incidence. Terminal product is a 750 mm wide agricultural bale wrap with UV stability sufficient for two-season outdoor storage.

    Stretch Hood Film Bubble Stability and Puncture Retention Data

    Blown stretch hood film for pallet unitization is extruded from 1018HA at a blow-up ratio of 2.0:1 to 2.2:1 and a die gap of 2.0 mm, conditions that reduce the bubble sag associated with the resin's narrow molecular weight distribution. A coextruded structure places 60 wt% 1018HA in the core and 40 wt% LDPE in the skins. The melt temperature is maintained at 200°C to 210°C, and the frost line height is kept below 3 die diameters to preserve transverse direction tear resistance. Film at 120 µm thickness is tested for elastic recovery after 200% strain per ASTM D5459; recovery values below 75% are rejected because pallet load retention falls below the requirement for long-haul transport. Puncture retention measured by ASTM D5748 on 120 µm film shows that 1018HA in the core maintains puncture energy above 0.8 J after 30 days of warehouse aging at 35°C. When the film is stretched to 80–100% pre-stretch on a stretch hood machine, the 1018HA-containing core reduces snap-back variability between pallet cornerboards. Processing is limited by the same moisture rule applied to other 1018HA film operations: below 60% relative humidity no pre-drying is required, but above 60% relative humidity recycled edge trim must be dried at 65°C for 2 h before re-introduction. Terminal product is a pallet unitization hood with a nominal 120 µm thickness and a load-holding service range from -20°C to 40°C.

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    Certification & Compliance
    More Introduction

    ExxonMobil Exceed mLLDPE 1018HA is a metallocene-catalyzed ethylene-hexene copolymer supplied as a pelletized blown-film resin. The nominal density is 0.918 g/cm³ determined under ASTM D1505, and the nominal melt index is 1.0 g/10 min at 190 °C under a 2.16 kg load according to ASTM D1238. The grade designation follows the Exceed naming convention in which the first two digits indicate nominal density and the second two indicate nominal melt index. The suffix HA identifies a specific additive and slip/antiblock package rather than a change in the base resin composition. All values are supplier-typical lot-average data, not specification limits, and shipment documentation should be used for lot-specific control limits.

    Because 1018HA is manufactured with a single-site metallocene catalyst and a hexene comonomer, the short-chain branch distribution is more uniform than that of a conventional Ziegler-Natta butene-based LLDPE. The molecular weight distribution is also narrower. These structural differences alter the balance among dart impact strength, tear propagation resistance, optical haze, and seal initiation temperature. Table 1 summarizes primary resin-level properties published for the grade. Film-level values such as dart impact, Elmendorf tear, haze, and gloss are excluded because published data for a single fabrication configuration is limited; they are strongly controlled by die gap, blow-up ratio, frost line height, cooling-air geometry, and film thickness. Converter trials are required for film property qualification.

    Typical resin-level values published for ExxonMobil Exceed mLLDPE 1018HA
    Property Test method Unit Typical value
    Nominal density ASTM D1505 g/cm³ 0.918
    Melt index at 190 °C, 2.16 kg ASTM D1238 g/10 min 1.0
    Peak melting temperature ASTM D3418 °C 118
    Vicat softening temperature ASTM D1525 °C 105

    What Limits Bubble Stability in High-Speed mLLDPE Extrusion?

    Compared with high-pressure LDPE, Exceed 1018HA exhibits lower melt strength and reduced shear thinning. This produces a narrower stable bubble window and greater sensitivity to frost line height variation on monolayer and coextruded blown-film lines. Equipment configurations that manage these limits include dual-lip air rings, internal bubble cooling, and screen packs sized to increase back pressure and homogenize melt delivery. Barrier screws with L/D ratios of 24:1 or greater, often with Maddock mixing sections, are used to limit melt-temperature nonuniformity.

    Melt temperatures are typically held between 190 °C and 220 °C for mLLDPE blown film. Die gaps are often set between 1.5 mm and 2.5 mm, with blow-up ratios from 2.0:1 to 3.0:1. These ranges are line-specific and must be adjusted for collapsing-frame geometry, tower height, and output-rate targets. Excessive die gap or melt temperature increases molecular orientation and can reduce dart impact strength measured under ASTM D1709. Die-lip deposit and melt fracture are controlled with fluoropolymer polymer-processing aids at addition levels typically reported in the 200–800 ppm range. The extruder should be purged with LDPE before and after processing because a narrow-MWD mLLDPE may leave a tight skin layer on screw and barrel surfaces.

    When additional bubble stiffness is required, converters may blend 1018HA with LDPE or HDPE. LDPE addition from 5 wt% to 20 wt% increases melt strength and widens the bubble window but raises haze and dilutes dart impact. HDPE addition increases film modulus and moisture-barrier contribution but can reduce Elmendorf tear strength under ASTM D1922. Blend acceptance should be based on dart impact, tear resistance, seal strength, and bubble stability measurements rather than melt index alone.

    Coextruded sealant webs and monolayer form-fill-seal structures use 1018HA where a reduction in seal initiation temperature relative to conventional C4 LLDPE is required. Heat seal strength is measured under ASTM F88, and hot tack is measured under ASTM F1921. The absolute seal initiation temperature is not fixed by resin density alone; seal-bar pressure, dwell time, film thickness, and coextruded layer distribution shift the measured response on commercial heat sealers. Converter trials on the target jaw configuration are therefore required for package qualification.

    Film applications include monolayer produce packaging, frozen-food bags, carrier films, industrial liners, heavy-duty sacks, and agricultural greenhouse covers. Relevant film test methods include ASTM D1709 for free-falling dart impact, ASTM D1922 for Elmendorf tear, ASTM D882 for tensile strength and elongation, ASTM D1003 for haze, and ASTM D2457 for gloss. High-stalk and low-stalk bubble configurations produce different molecular orientation, and the resulting machine-direction versus transverse-direction tear balance must be optimized on the actual production line.

    Comparative Film Property Profile Against Conventional C4 LLDPE and LDPE

    At equal density and melt index, Exceed 1018HA typically provides higher dart impact strength and puncture resistance than a conventional Ziegler-Natta butene LLDPE. The improvement arises from higher tie-molecule density generated by hexene comonomer and more uniform short-chain branching. Optical performance under ASTM D1003 and ASTM D2457 is generally better than that of a C4 LLDPE of similar melt index because the reduced crystalline spherulite size lowers haze and raises gloss. The exact difference depends on film gauge, cooling rate, and the selected additive package.

    Compared with high-pressure LDPE, 1018HA offers higher tensile strength, higher puncture resistance, and a lower sealing threshold, but lower melt strength and reduced shear thinning. This inverse relationship means that LDPE is usually added as a minority component to 1018HA, rather than the reverse, when bubble stability is marginal. Within the Exceed family, 1018HA occupies the 0.918 g/cm³ and 1.0 g/10 min position. Lower-density mLLDPE grades reduce seal initiation and increase impact and clarity but decrease film modulus and melt strength. Higher-density grades increase stiffness and barrier contribution but require higher seal temperatures and may reduce dart impact.

    The primary operational boundaries for 1018HA are thermal and rheological. Melt temperatures above 260 °C should be avoided for extended residence times to limit thermo-oxidative degradation, gel formation, and subsequent visual defects. The resin is not intended for injection molding, blow molding, or rotomolding where higher melt strength or different crystallization behavior is required. If surface condensation is present due to storage at RH > 60%, hopper drying at 70–80 °C for 2–4 hours is used to prevent surface defects, although routine polyolefin processing does not normally require drying.

    When Food-Contact Compliance Requires Migration and Composition Documentation

    Polyethylene resins intended for food packaging are evaluated under FDA 21 CFR 177.1520 for olefin polymers, provided the final article meets use conditions and thickness limitations. For EU applications, Regulation (EU) No 10/2011 as amended establishes an overall migration limit of 10 mg/dm² for food contact surface area, with a 60 mg/kg limit applicable in specific infant-food simulant cases. Specific migration limits apply to individual additives and decomposition products, and the final package must be tested as a finished article.

    Representative compliance framework for ExxonMobil Exceed mLLDPE 1018HA
    Framework Standard or regulation Application boundary
    US food contact FDA 21 CFR 177.1520 Olefin polymers for food contact; final article compliance required
    EU food contact Regulation (EU) No 10/2011 Overall migration limit 10 mg/dm²
    REACH Regulation (EC) No 1907/2006 Substance registration and communication obligations
    RoHS Directive 2011/65/EU Electrical and electronic equipment; restricted heavy-metal thresholds

    End-use fitness for food contact cannot be inferred from resin data alone. Converters must validate organoleptic performance, extraction behavior, seal integrity, and film toughness on the specific coextrusion line and package geometry. Batch-to-batch variation should be tracked using melt index, density, film dart impact, and seal strength control charts. These measurements are the only reliable basis for release of production tonnage because published data for a specific fabrication configuration is limited and cannot substitute for production-scale validation.

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