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ExxonMobil Exceed mLLDPE 3518CB

    • Product Name: ExxonMobil Exceed mLLDPE 3518CB
    • 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 299725
    Product Name ExxonMobil Exceed mLLDPE 3518CB
    Polymer Type Metallocene Linear Low Density Polyethylene (mLLDPE)
    Comonomer Hexene-1
    Density 0.918 g/cm³
    Melt Index 3.5 g/10 min (190°C/2.16 kg)
    Peak Melting Temperature 119 °C
    Vicat Softening Temperature 95 °C
    Crystallization Temperature 103 °C
    Tensile Strength At Yield 10 MPa
    Tensile Strength At Break 28 MPa
    Elongation At Break 500%
    Flexural Modulus 200 MPa
    Shore D Hardness 50
    Dart Drop Impact 200 g
    Elmendorf Tear Strength Md 200 g
    Elmendorf Tear Strength Td 300 g
    Haze 1.5%
    Gloss 45 85%

    As an accredited ExxonMobil Exceed mLLDPE 3518CB factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in 25 kg moisture-resistant polyethylene bags, palletized and shrink-wrapped for safe handling and storage.
    Container Loading (20′ FCL) 20′ FCL container loaded with ExxonMobil Exceed mLLDPE 3518CB in 25 kg bags, palletized, stretch-wrapped, and securely stowed for export.
    Shipping ExxonMobil Exceed mLLDPE 3518CB is a solid metallocene linear low-density polyethylene resin supplied as pellets in bags or bulk containers. It is not classified as dangerous goods for transport. Keep dry, protect from heat and UV, and follow standard industrial hygiene practices.
    Storage Store ExxonMobil Exceed mLLDPE 3518CB in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and moisture. Keep containers closed and clearly labeled; avoid dust generation and contamination. Follow the supplier’s SDS and local regulations for safe handling and storage.
    Shelf Life Shelf life is 24 months from date of manufacture when stored in original packaging in a dry, cool, well-ventilated area.
    Application of ExxonMobil Exceed mLLDPE 3518CB

    At a melt index of 3.5 g/10 min measured per ASTM D1238 at 190 °C and 2.16 kg, and a density of 0.918 g/cm³ measured per ASTM D1505, ExxonMobil Exceed mLLDPE 3518CB is processed on a three-layer A/B/A cast stretch line with a die width of 2,200 mm and a maximum backing roll speed of 600 m/min. The core layer consists of 100 wt% 3518CB and occupies 60–70% of total web thickness. The cling layer is metered at 97.0–98.5 wt% 3518CB plus 1.5–3.0 wt% polyisobutylene tackifier masterbatch. The release layer is metered at 98.5–99.5 wt% 3518CB plus 0.5–1.5 wt% silica-based antiblock masterbatch. Barrel temperatures are set from 180 °C in the feed zone to 270 °C at the adapter; melt temperature at the die is held between 274 °C and 285 °C. The die gap is 0.45 mm to 0.65 mm. The air gap is 30 mm to 40 mm. Chill roll temperature is 18 °C to 24 °C. The finished film is slitted at 500 mm widths for machine wrap and 250 mm to 450 mm widths for hand wrap, with thickness from 12 µm to 35 µm. Compliance for the olefin polymer base in food contact is governed by 21 CFR 177.1520 and, for EU markets, Regulation (EU) No 10/2011; the tackifier and antiblock masterbatches require separate end-use migration evaluation. Pre-stretch on a powered carriage is set between 200% and 250%. Cling retention is measured with ASTM D5458; puncture propagation resistance is measured with ASTM D5748. At pre-stretch above 250% on 12 µm film, edge tear and transverse thickness variation increase unless the gauge control system maintains final film thickness tolerance within ±1.5% across the web.

    Why Does Chill Roll Release Limit Line Speed Below 450 m/min?

    High-speed cast film made with 3518CB fails at the chill roll interface before the extruder becomes pressure-limited when the release surface is not managed. At line speeds above 450 m/min, the polymer melt exits the die at 270–285 °C and quenches within 40–60 ms. Chill roll release is governed by the static coefficient of friction between the film and the matte or polished roll, measured per ASTM D1894. A static COF above 0.45 increases the risk of blocking on the roll and micro-tearing in the cast web. A static COF below 0.15 causes slip and air entrapment between the web and the chill roll, reducing heat transfer. The resulting quench rate variation changes crystalline orientation in the machine direction and produces bands of low elongation at the slitting edge. The formulation uses 0.5–2.0 wt% of a silica-based antiblock masterbatch with a median particle size of 2–4 µm in the release layer. Chill roll temperature is controlled between 18 °C and 24 °C with a water-side ΔT of 2 °C across the roll face. Release layer thickness is maintained at 1.0–2.0 µm. Terminal products in this configuration are 23 µm machine stretch wrap and 15 µm hand wrap. Regulatory compliance for the base resin falls under 21 CFR 177.1520 and Regulation (EU) No 10/2011; the antiblock masterbatch must comply with the relevant additive positive list. A limitation is the need for periodic roll cleaning after 8–12 h of continuous operation when low molecular weight species migrate to the film surface and transfer to the chill roll.

    When 3518CB is coextruded as a heat-seal layer in form-fill-seal lamination, the sealant web is typically 10–15% of the total film thickness. The layer composition is 95–100 wt% 3518CB with 0–5 wt% slip and antiblock masterbatch, depending on slip requirements. The sealant layer is processed at a melt temperature of 255–270 °C without pre-drying at ambient humidity below 60% RH. The die gap is set at 0.60 mm and the line speed is maintained between 150 m/min and 250 m/min. Seal initiation temperature is measured per ASTM F88 on a 25 µm sealant layer after a 0.5 s dwell and 2.0 bar seal pressure; typical onset for standard mLLDPE cast films is between 85 °C and 95 °C, but converter-specific values must be confirmed because additive package and film thickness shift the curve. Hot tack force is measured per ASTM F1921 immediately after seal opening. The finished structure is used for dry food pouches, frozen vegetable bags, and milk powder sachets. Food contact compliance is established through 21 CFR 177.1520 for the polyolefin base and Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm² for the final laminated structure. If the sealant layer is corona-treated before lamination, the surface energy should not exceed 38–42 dyn/cm measured per ASTM D2578, because higher treatment levels accelerate oxidation byproducts that reduce hot tack uniformity.

    Screw Temperature Profiles and Gel Formation in 30:1 L/D Cast Lines

    Cast sheet lines running 3518CB with barrier screws of 30:1 L/D and compression ratio 2.5:1 exhibit pressure instability when the feed throat temperature exceeds 60 °C. The recommended barrel set profile begins at 180 °C in zone one, 210 °C in zone two, 240 °C in zone three, and 260 °C in the adapter. Melt temperature measured by an immersion thermocouple before the die is maintained between 265 °C and 275 °C. At melt temperatures above 285 °C, oxidative gel formation in the die lip region increases over a 4–6 h run, with gel counts detected by a 50 µm resolution camera system. A startup purge ratio of 70 wt% fractional melt LDPE and 30 wt% 3518CB is used to reduce die-lip polyethylene oxidation during line stops longer than 15 min. The die gap is 0.5 mm. The air gap is 25 mm. Chill roll temperature is 20 °C. Finished film produced under these conditions is used for surface protection tape and neutral backing films. Mechanical properties are tested per ASTM D882; density is verified per ISO 1183-1. The base resin is not hygroscopic, but pre-drying is required at relative humidity above 60% for 2 h at 70 °C to avoid surface splay on film edges. The limitation is that metallocene-catalysed 3518CB has a narrower shear-thinning window than Ziegler-Natta LLDPE; extruder screw speeds above 120 rpm on 45 mm screws can generate melt pressure above 350 bar, which accelerates screw wear and adds shear heat beyond the set profile. Industrial surface protection films in this segment are assessed under REACH Article 33 SVHC disclosure and RoHS Directive 2011/65/EU for lead, cadmium, mercury, hexavalent chromium, PBBs, and PBDEs.

    Substituting 3518CB into conventional LLDPE blown-film formulations at 70–85 wt% creates a bubble with lower melt strength than a Ziegler-Natta LLDPE. A typical blend is 80 wt% 3518CB and 20 wt% LDPE with melt index 0.25 g/10 min per ASTM D1238 to restore bubble stability. The blown-film line uses a 250 mm die, die gap 1.2 mm, blow-up ratio 2.5:1, and melt temperature 195–210 °C. Frost line height is maintained at 350–450 mm above the die face. Final film thickness is 40–70 µm. Blending is done by gravimetric feeders at the feed throat; no pre-compounding is required when the LDPE is added at 20 wt% or less. The film is printed and converted into frozen vegetable pouches and freezer bags. Cold-temperature impact is measured by ASTM D1709 Method A after conditioning at −20 °C for 24 h. Tear resistance is measured by ASTM D1922 in the machine direction after conditioning at 23 °C and 50% RH. Food contact compliance is governed by 21 CFR 177.1520 and Regulation (EU) No 10/2011; migration testing for the printed film is required for the finished package. The limitation is that lower blow-up ratios below 2.0:1 increase machine-direction tear strength but reduce transverse-direction impact resistance, so the optimum for frozen food is 2.5:1 to 3.0:1.

    If 3518CB Replaces Conventional LLDPE in Heavy-Duty Industrial Liners

    A three-layer blown-film structure for 100–150 µm industrial liners can replace 60–70 wt% of a conventional Ziegler-Natta LLDPE with 3518CB while retaining the remaining 30–40 wt% as fractional-melt LDPE. The blend is processed on a 1,200 mm die with die gap 1.5 mm, blow-up ratio 3.0:1, and melt temperature 200–215 °C. A carbon black masterbatch is added at 2–4 wt% only in the outer layers for UV resistance; the core remains unpigmented to preserve dart impact resistance. Dart impact is tested per ASTM D1709 Method B after conditioning at 23 °C and 50% RH. Elmendorf tear is tested per ASTM D1922. The finished liners are used for construction debris, mineral fillers, and bulk resin packaging. Compliance is limited to industrial packaging; the carbon black masterbatch must meet REACH and RoHS Directive 2011/65/EU restrictions. The operational boundary is that addition of recycled post-industrial LLDPE above 15 wt% increases gel defects and lowers puncture propagation resistance beyond acceptable limits unless a 100 µm continuous melt filter is installed before the die.

    Surface Protection Films Demand a Tighter Melt Temperature Band Than Standard Cast Film

    For extruded surface protection film, 3518CB is cast as a 30–60 µm backing web with an adhesive layer coextruded through a two- or three-layer feedblock. The backing layer is 90–95 wt% 3518CB; the remainder is a slip masterbatch. The adhesive layer is a hydrogenated styrenic block copolymer or acrylic formulation at 5–10 wt% of the total structure. Melt temperature in the backing layer is held between 265 °C and 275 °C, narrower than standard cast film because higher temperatures increase low molecular weight extractables that migrate into the adhesive and reduce peel adhesion. The die gap is 0.40 mm. The air gap is 20 mm. Chill roll is polished to Ra 0.02–0.05 µm and maintained at 15–20 °C. Thickness uniformity is monitored by a beta gauge and held within ±1.0% of nominal. The finished film is slit to 1,000–1,500 mm rolls and used for temporary protection of stainless steel, coated metal, and laminated panels. Peel adhesion is measured per ASTM D3330. The backing film tensile strength and elongation are measured per ASTM D882. Regulatory compliance is based on REACH, RoHS 3 Directive (EU) 2015/863 amending Annex II of Directive 2011/65/EU, and the absence of phthalates listed in Entry 51 of Annex XVII to REACH when the adhesive is formulated. The limitation is that reels stored above 35 °C show adhesive transfer to the backing due to micro-migration of oligomers from the mLLDPE surface.

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    Certification & Compliance
    More Introduction

    ExxonMobil Exceed mLLDPE 3518CB is a metallocene-catalysed linear low density polyethylene intended for high-output cast film extrusion. The resin is an ethylene-hexene copolymer supplied in pellet form. Typical values in ExxonMobil product documentation list density at 0.918 g/cm³ under ASTM D1505 and melt index at 3.5 g/10 min under ASTM D1238 with 190 °C/2.16 kg loading. Peak melting temperature is reported as 119 °C by ASTM D3418, and Vicat softening temperature is reported as 100 °C by ASTM D1525. The grade is typically processed without pre-drying unless storage in relative humidity above 60 % has produced visible surface condensation on the pellets.

    Resin PropertyTypical ValueTest Method
    Density0.918 g/cm³ASTM D1505
    Melt index3.5 g/10 minASTM D1238, 190 °C/2.16 kg
    Peak melting temperature119 °CASTM D3418
    Vicat softening temperature100 °CASTM D1525

    The values in the table are typical and are not lot-level specification limits. Certificates of analysis should be consulted for batch-specific tolerances.

    What Processing Boundaries Are Observed on High-Speed Cast Film Lines?

    On cast film equipment, the 3.5 g/10 min melt index reduces extruder head pressure relative to a 1.0 g/10 min mLLDPE at equal throughput. The reduction is observed on single-screw extruders with 90 mm to 120 mm barrel diameters and 30:1 L/D barrier screws. The exact pressure differential is line-specific and depends on screw geometry, screen-pack condition, melt temperature, and throughput. In production practice, melt temperatures are commonly maintained between 240 °C and 280 °C. Operation below 230 °C may generate surface melt fracture and elevated screw torque, while operation above 290 °C increases gel formation risk, odour development, and die lip deposit accumulation on long campaigns.

    Rheologically, the narrow molecular weight distribution of metallocene LLDPE produces lower melt strength than a broad-molecular-weight Ziegler-Natta LLDPE at equivalent density. Capillary rheometry under ASTM D3835 at 190 °C and 230 °C is used to characterise the shear viscosity curve for lot acceptance or process diagnosis. Because the material shows less shear-thinning than broad-distribution LLDPE, increasing screw speed does not reduce viscosity as rapidly as it does for conventional butene-based LLDPE. Gear-pump-equipped cast lines stabilise die pressure and damp pressure pulsations that would otherwise create transverse gauge variation.

    Draw resonance can appear when the draw ratio exceeds approximately 20:1. Thickness oscillation in the machine direction is controlled with a vacuum box or electrostatic edge pinning at the die-to-roll air gap. The air gap is normally set between 25 mm and 75 mm, and chill-roll temperature is held between 15 °C and 30 °C. Larger air gaps allow greater stress relaxation but increase neck-in; smaller air gaps reduce neck-in but can trap air between the melt curtain and the chill roll. Die gaps for cast film typically range from 0.5 mm to 1.0 mm. A narrower die gap improves gauge uniformity at high draw but raises die pressure and may increase die lip fouling.

    For this grade, high-speed cast film lines operating at 300 m/min to 600 m/min are common. Published data for this specific configuration above 600 m/min is limited. Above that rate, air gap turbulence, edge bead formation, and winding quality require line-specific validation. The edge pinning system must maintain curtain contact at the die lip; otherwise edge beads form and downstream web handling deteriorates.

    Screen packs are selected to protect the die from contamination. Increasing mesh count raises backpressure and can reduce output by an amount controlled by filtration area. Barrier screws with Maddock mixers are generally used; high-shear screws can generate excessive melt temperature in the rear compression section before the resin reaches the die. Processors report lower backpressure at equivalent throughput relative to low-melt-index mLLDPE, but the pressure difference has not been standardised across screw designs.

    Mechanical performance in cast film is strongly affected by film gauge and quenching. In 25 µm cast film, tensile properties are commonly evaluated by ASTM D882. Dart impact resistance is assessed by ASTM D1709, and Elmendorf tear resistance by ASTM D1922. The grade is used in stretch wrap, industrial overwrap, lamination film, and packaging structures where good puncture resistance and drawability are required. The base resin is non-polar; printing, laminating, or metallising requires corona treatment to a minimum surface wetting tension of 38 mN/m measured by ISO 8296. The treatment level decays with time and must be checked in-line before secondary conversion.

    Cling performance in stretch wrap is controlled by tackifier masterbatch and slip additives rather than by the base resin alone. The grade can be used in the cling layer, core layer, or both, depending on the formulation. Coefficient of friction is evaluated by ASTM D1894. Additive dosage is determined by masterbatch active content, final film gauge, and unwind behaviour on powered stretch wrappers. The base resin is not formulated as a ready-to-use cling layer without converter-side modification unless the converter has validated the final structure.

    Comparative Differentiation Against Conventional Ziegler-Natta LLDPE and Other Cast-Film mLLDPE Grades

    Exceed mLLDPE 3518CB differs from conventional Ziegler-Natta butene-copolymer LLDPE primarily in molecular architecture and comonomer type. The hexene comonomer and metallocene catalysis provide a more uniform short-chain branching distribution. As a result, seal initiation temperature measured by ASTM F1921 is lower, and puncture resistance at equivalent gauge is higher when tested by ASTM D5748 or equivalent. Haze measured by ASTM D1003 and gloss measured by ASTM D2457 are typically improved at equivalent film gauge. The trade-off is lower melt strength and greater draw resonance sensitivity.

    Processing or Film AttributeExceed mLLDPE 3518CBConventional Ziegler-Natta Butene LLDPE
    Short-chain branching distributionNarrowBroader
    Melt strengthLowerHigher
    Puncture resistance at equivalent gaugeHigherLower
    Seal initiation temperatureLowerHigher
    Clarity and glossHigherLower

    Within the Exceed family, the 3.5 g/10 min melt index positions this grade for cast film. Lower melt index variants of similar density are typically directed to blown film where bubble stability requires higher melt strength. Higher melt index cast grades can deliver higher flow for thin-gauge coating but may sacrifice toughness and tear resistance. The density of 0.918 g/cm³ provides a balance between stiffness, tear, and cling. Lower density variants reduce modulus and increase softness; higher density variants increase stiffness and reduce gas permeability. Selection among these grades should be based on final film property targets and the specific cast line configuration.

    If Food-Contact and Regulatory Conformity Are Required

    Food-contact use is addressed through supplier documentation referencing FDA 21 CFR 177.1520 for olefin polymers and EU Regulation 10/2011 for plastic materials intended to come into contact with food. Overall migration testing is performed under the conditions prescribed in EU Regulation 10/2011, with a general migration limit of 10 mg/dm². Converters must verify that additives, processing aids, and regrind streams do not alter the regulatory status of the final article. Compliance with REACH Regulation 1907/2006 is based on supplier declarations for monomers and additives; the polymer itself is exempt from registration as a polymer under REACH.

    RoHS Directive 2011/65/EU restrictions for lead, mercury, cadmium, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers are addressed through supplier declarations. The resin is supplied without intentionally added heavy metals. The product is not intended for medical implantation or long-term implant use; USP Class VI data should not be assumed without application-specific testing.

    Outdoor service requires the addition of a UV stabiliser masterbatch. Weathering resistance must be tested under ISO 4892-2 or ASTM G154 according to end-use exposure. Continuous operation at elevated temperature above 70 °C may reduce load-bearing capacity and creep resistance; mechanical testing at service temperature is required for load-bearing articles.

    Converters should validate the effect of regrind addition on film appearance and physical properties. Trim content above 20 % may raise gel counts and increase the risk of black specks if the trim is contaminated with labels, edge debris, or incompatible film scrap. If bags are opened in an uncontrolled warehouse at relative humidity above 60 %, surface condensation may form on pellets. In that case, drying by dry-air conveying or hopper drying is recommended before extrusion. The resin is not inherently antimicrobial, antistatic, or UV-stable; those performance properties must be introduced by functional masterbatches selected for the final film structure.

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