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ExxonMobil Enable mLLDPE 20-10CE

    • Product Name: ExxonMobil Enable mLLDPE 20-10CE
    • 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 124582
    Product Name ExxonMobil Enable mLLDPE 20-10CE
    Polymer Type Metallocene linear low density polyethylene (mLLDPE)
    Density 0.920 g/cm³
    Melt Index 190 C 2 16 Kg 1.0 g/10 min
    Melting Peak Temperature 116°C
    Vicat Softening Temperature 93°C
    Tensile Strength At Break Md 40 MPa
    Tensile Strength At Break Td 35 MPa
    Elongation At Break Md 500%
    Elongation At Break Td 600%
    1 Secant Modulus Md 130 MPa
    1 Secant Modulus Td 140 MPa
    Elmendorf Tear Strength Md 150 g
    Elmendorf Tear Strength Td 300 g
    Dart Drop Impact 120 g
    Haze 4%
    Gloss 45 80
    Coefficient Of Friction 0.2

    As an accredited ExxonMobil Enable mLLDPE 20-10CE factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing ExxonMobil Enable mLLDPE 20-10CE is packaged in 25 kg moisture-resistant polyethylene bags, with 55 bags per 1,375 kg pallet.
    Container Loading (20′ FCL) ExxonMobil Enable mLLDPE 20-10CE loaded in 20-foot FCL container, palletized 25 kg bags, securely stowed and restrained for ocean transport.
    Shipping ExxonMobil Enable mLLDPE 20-10CE is shipped as non-hazardous polymer pellets in 25 kg bags or 1,000 kg bulk bags, in dry containers or trucks at ambient conditions. It is not regulated for transport; keep dry, cool, ventilated, and protected from contamination and direct sunlight.
    Storage Store ExxonMobil Enable mLLDPE 20-10CE in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and moisture. Keep in original, sealed packaging and maintain stable stacking to prevent bag damage. Avoid prolonged UV exposure and contamination. Follow the supplier’s SDS and local regulations for safe handling and inventory rotation.
    Shelf Life ExxonMobil Enable mLLDPE 20-10CE typically has a recommended shelf life of 24 months from manufacture when stored dry in original packaging at ambient conditions.
    Application of ExxonMobil Enable mLLDPE 20-10CE

    In cast pallet unitization lines running chill roll temperatures between 18 °C and 30 °C, ExxonMobil Enable mLLDPE 20-10CE is introduced into the core layer of an A/B/A three-layer die at 70–90 wt%, with lower-molecular-weight LLDPE or LDPE in the skin layers at 10–30 wt% to stabilize edge pinning and control cling transfer. The resin’s nominal melt index of 1.0 g/10 min (ASTM D1238, 190 °C/2.16 kg) and density of 0.9200 g/cm³ (ASTM D1505) place it at the high-viscosity end of cast stretch formulations. A melt temperature of 240–265 °C at the die exit is therefore used on single-screw extrusion lines, with the lower bound set by motor-load rise in extruders shorter than 24:1 L/D and the upper bound set by oxidation gel formation when residence time exceeds 8 min above 280 °C. The processing window is narrow; a die gap below 0.5 mm raises melt pressure and shear heating, while a die gap above 0.8 mm promotes draw resonance and gauge variation.

    Formulation adjustments for high-cling machine wrap commonly place a polyisobutylene or EVA-based cling masterbatch in the skin layer at 0.5–2.0 wt%, while the core remains predominantly 20-10CE to preserve dart impact and puncture resistance. On production-scale cast lines, air gap is held between 40 mm and 120 mm, air knife pressure between 20 mbar and 60 mbar, and chill roll temperature between 18 °C and 30 °C; a polished chill roll improves film optics but reduces line speed if roll temperature is below 18 °C. Terminal machine stretch wrap exits at 10–23 µm, while hand wrap is produced at 15–35 µm, with pre-stretch ratios of 200–300% on powered wrappers. Compliance references include ASTM D4649-20 for selection and use, ASTM D5458-12 for cling force measurement, and ASTM D882-18 for tensile properties; where the wrap is used as a food-contact overwrap, 21 CFR 177.1520(c)3.1a applies to the olefin polymer, with antioxidant and processing aid levels recognized under 21 CFR 178.2010 for indirect additive use.

    PropertyTest methodPublished nominal value
    Melt index (190 °C / 2.16 kg)ASTM D12381.0 g/10 min
    Density (23 °C)ASTM D15050.9200 g/cm³
    Peak melting temperatureASTM D3418123 °C

    What Limits Neck-In and Adhesion at Low Coating Weight in Extrusion Lamination with 20-10CE?

    Extrusion lamination lines running 20-10CE as the heat-seal layer on aluminum foil, oriented PET, or paperboard encounter two coupled constraints: melt tension is sufficient to support a 150–250 mm air gap at melt temperatures of 300–325 °C, but neck-in increases as coating weight drops below 15 g/m². A formulation using 70–100 wt% 20-10CE with 0–30 wt% of a high-MFR LDPE extrusion coating grade of 7–9 g/10 min moderates draw resonance; at 100 m/min line speed, a 100% 20-10CE melt can exhibit edge neck-in above 15 mm per side, while the LDPE-containing blend typically reduces this below 12 mm. Substrate pretreatments use corona discharge to 42–46 dyn/cm on PET or foil, and ozone dosing at 0.3–0.8 g/h/cm die width promotes polar adhesion to aluminum without a solvent-based primer. The extruder is typically a 30:1 L/D single-screw unit with a barrier screw and a gear pump to reduce surging at low coating thickness.

    Downstream, the coated web is slit into reel-fed form-fill-seal lamination stock. Terminal products include dried beverage sachets, condiment pouches, coffee stick packs, and moisture-barrier overwraps for pharmaceutical diagnostic devices. Compliance is governed by FDA 21 CFR 177.1520(c)3.1a for olefin polymers, EU Regulation 10/2011 with overall migration below 10 mg/dm², and ISO 1133-1:2022 for incoming melt flow verification. Operational boundaries are specific: melt temperature should not exceed 325 °C for more than 6 min residence time, and direct lamination to unprimed cellulosic substrates is not practiced because moisture release at the nip creates pinhole defects. For aluminum foil adhesion without ozone or chemical primer, published data for this specific configuration is limited.

    Frozen Food Sealant Layers in Three-Layer Cast Coextrusion

    For retail frozen vegetable and seafood packaging, 20-10CE is weighted at 60–80 wt% in the inner sealable layer of a three- or five-layer cast coextrusion, diluted with 20–40 wt% ethylene-octene plastomer to reduce seal initiation temperature to the 85–95 °C range without sacrificing dart impact. The outer and core layers may use higher-stiffness LLDPE or MDPE, but the sealant layer remains rich in 20-10CE to retain flex-crack resistance at freezer temperatures. Coextrusion die temperature is profiled from 220 °C to 250 °C, and the cast unit uses a 20 °C or colder chill roll to quench the film before edge trimming. The film thickness is typically 40–80 µm, with the sealant layer occupying 20–30% of total thickness to balance seal strength and cost.

    Seal strength is verified with ASTM F88/F88M-23, and low-temperature film brittleness can be screened with ASTM D1790-21 after conditioning at -40 °C. The relevant food-contact citations are 21 CFR 177.1520(c)3.1a and EU Regulation 10/2011; specific migration testing must cover the plastomer fraction and the slip/antiblock package if used above 1 wt%. Terminal finished goods produced from this sealant web include pillow pouches for frozen diced produce, semi-rigid carton liners for ice cream, and vacuum-sealed bags for frozen meat portions. The operational boundary is explicit: the sealant layer is not rated for retort cycles above 121 °C or for long-term continuous service above 70 °C, and published data for retort-adjacent low-temperature coextrusions using this exact grade are limited.

    Where a 80–150 µm cast liner is required for flexible intermediate bulk containers and drum inserts, 20-10CE is selected over conventional LLDPE because its hexene comonomer distribution maintains dart impact at high gauge without requiring an additional plastomer. Monolayer cast lines run the resin at 80–100 wt%, with 0–20 wt% LDPE for surface slip and 1–3 wt% slip/antiblock masterbatch to prevent blocking in stack-rolled liners. Melt temperature is held between 230 °C and 250 °C, die gap at 0.8–1.2 mm, and line speed between 50 m/min and 150 m/min; at thickness above 120 µm, a dual chill roll arrangement or post-cooling bath is used because residual heat in the wound roll otherwise causes roll blocking. End-use qualification for chemical powder inner liners commonly references the UN Model Regulations Chapter 6.1 performance tests for inner packagings, with side-seal strength and tear propagation tested per ASTM D882-18 and ASTM D1922-15.

    Food-grade liner versions fall under 21 CFR 177.1520(c)3.1a and EU Regulation 10/2011; for dry ingredients in Europe, overall migration must remain below 10 mg/dm². Produced articles include FIBC and drum liners for mineral fillers, dry-flowable foods, and non-hazardous chemical salts. Observable production bottlenecks include edge trim waste rates of 8–12% at start-up on cast lines, and screw torque-limited output when melt temperature is kept below 250 °C. At ambient temperature below 10 °C, the liner becomes stiffer to unfold, but the hexene comonomer provides less stiffness increase than equivalent density butene-based LLDPE.

    When Silage Bale Wrap Requires Controlled Cling and Weathering Stability Without Sacrificing Tear Resistance

    Agricultural bale wrapping lines apply 20-10CE at 96–98 wt% with a UV masterbatch at 1–3 wt% and a cling additive at 1–2 wt%; the film is cast at 25 µm nominal thickness and stretched at ratios of 60–100% on round bales. The cast line runs a melt temperature of 240–260 °C, and the chill roll is maintained at 25–30 °C to preserve cling while minimizing blocking in the finished roll. EN 14932:2018 is the controlling European standard for thermoplastic stretch films for wrapping bales, and it sets requirements for elongation, width retention, and cling performance after artificial weathering under EN ISO 4892-3 exposure conditions.

    For outdoor storage of silage, haylage, and chopped forage, the film must resist punctures from stem ends and maintain oxygen exclusion for 9–12 months; film using 20-10CE is selected for the combination of tear propagation and retained stretch at low temperatures. If the film is used in contact with animal feed only, compliance focuses on EU Regulation 10/2011 migration limits and REACH Regulation (EC) No 1907/2006 SVHC restrictions; no direct food-contact approval is required for silage wrap unless the wrapped bales are later used as animal feed packaging. The terminal article is a 750 mm wide roll of pre-stretched agricultural film for round and square bale wrappers. A documented failure mode on farm-scale wrappers is width recovery loss at film temperatures below 5 °C, which is mitigated by storing rolls above 10 °C before use.

    Protective Film for Glass and Coated Metal: Adhesion Control Without Solvent-Based Coatings

    At appliance and architectural glass converters, coextruded cast protective film uses 20-10CE in the core and back layer at 60–80 wt%, while the skin layer is modified with 20–40 wt% EVA or POE to achieve peel adhesion to stainless steel, coated aluminum, glass, or ceramic surfaces. The process is a three-layer cast line with a 0.5–0.8 mm die gap, melt temperatures of 220–245 °C, and a textured or matte chill roll to control unwind behavior. Thickness ranges from 40 µm to 80 µm, and peel adhesion is measured by ASTM D3330/D3330M-04(2018) after 24 h contact on the target substrate. To avoid blocking, the back layer may include 0.5–1.5 wt% silica-based antiblock.

    Terminal protective articles include masking films for refrigerator door panels, stainless steel kitchen appliance surfaces, architectural glass, and anodized aluminum profiles. Compliance for electronics or appliance supply chains may require EU 2011/65/EU RoHS declarations for restricted substances and REACH Regulation (EC) No 1907/2006 SVHC below 0.1 wt% at article level. Food-contact status can be claimed under 21 CFR 177.1520(c)3.1a only for the polyolefin layer, not for the adhesive modifier unless separate supportive data are supplied. The operational boundary: adhesion increases as the film remains on a substrate above 40 °C or under UV exposure, and removal after 6 months of outdoor weathering may leave residue if the adhesive layer is not UV-stabilized.

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    Certification & Compliance
    More Introduction

    ExxonMobil Enable mLLDPE 20-10CE is a metallocene-catalyzed ethylene-hexene copolymer supplied as pelletized linear low-density polyethylene for cast film extrusion. The grade designation encodes nominal resin parameters: the numeral 20 denotes a nominal density of 0.920 g/cm³, and 10 denotes a nominal melt index of 1.0 g/10 min determined at 190 °C with a 2.16 kg load according to ASTM D1238 and ISO 1133-1:2022. Density is determined by ASTM D1505 / ISO 1183-1:2019. The CE suffix identifies cast extrusion grade positioning; the resin is processed on high-throughput cast film lines producing overwrap, stretch, lamination, and produce packaging. Because the metallocene catalyst system yields a narrow molecular weight distribution and a more uniform comonomer distribution than conventional Ziegler-Natta LLDPE, the product is differentiated by reduced gel-related optical defects, lower seal initiation temperature, and a different shear-thinning response in the melt. Published datasheets present typical values rather than specification limits; lot-specific certificate of analysis values are controlled by the supplier.

    The molecular architecture of 20-10CE is the primary point of difference from conventional linear low-density polyethylene. In a metallocene-catalyzed hexene copolymer, the comonomer is inserted more uniformly across the molecular weight distribution. This reduces the fraction of high-density, low-comonomer chains that crystallize rapidly and produce haze and high seal initiation. As a consequence, the resin exhibits a lower seal initiation temperature at the same average density. The absence of long-chain branching, by contrast, separates the grade from high-pressure LDPE and changes melt elasticity. This architectural difference is relevant to cast film processing because it lowers the first normal stress difference and reduces shear thinning; it also increases the high-shear viscosity relative to a broad-MWD LLDPE of the same melt index.

    What Bulk Resin Properties Govern Feed and Melt Handling?

    Bulk material handling is governed by pellet geometry, bulk density, and melt index. The melt index of 1.0 g/10 min places 20-10CE in the medium-viscosity range for cast film; at 190 °C and 2.16 kg load this value is lower than high-flow coating grades but higher than fractional-melt film grades. Density of 0.920 g/cm³ is determined by ASTM D1505-18 or ISO 1183-1:2019 on compression-molded plaques. At this density, the amorphous fraction reduces film stiffness relative to medium-density grades but does not suppress the crystallization front enough to hinder chill roll release.

    Thermal analysis by differential scanning calorimetry according to ISO 11357-3:2018 typically shows a peak melting point near 121 °C for metallocene hexene copolymers of this density class. A Vicat softening point near 108 °C by ASTM D1525-17 is used as a comparative value for heat resistance, not as a continuous-use temperature. Bulk density of pelletized LLDPE of this form typically ranges from 0.48 g/cm³ to 0.60 g/cm³; silo and hopper mass-flow design should be based on measured lot values. The resin does not absorb equilibrium moisture; predrying is not required unless surface condensation occurs after cold storage, in which case 60–70 °C for 2–4 h is generally sufficient. Extended storage above 50 °C or direct sunlight may increase pellet blocking and should be avoided.

    On production-scale cast lines with single-screw extruders of 60–150 mm diameter and 24:1–33:1 L/D, the narrow molecular weight distribution of mLLDPE can produce die pressure 10–20% higher than a broad-MWD Ziegler-Natta LLDPE of the same melt index at equal mass throughput. Barrier screws with a Maddock section reduce melt temperature gradients and improve output consistency; a screen pack with 400–800 µm mesh and a breaker plate is usually installed for gel and contaminant protection.

    For cast film extrusion, 20-10CE is processed with a flat die, vacuum box or air knife, and polished chill rolls. Melt temperature profile from feed to die is typically maintained between 230 °C and 270 °C, with die gap settings of 0.5–1.0 mm used to accommodate the low melt strength of linear polyethylene. Chill roll temperatures of 15–35 °C set film crystallinity and minimize optical haze. Draw ratio between die exit and chill roll commonly falls between 10:1 and 40:1; draw resonance can appear when draw ratio and air gap are not optimized. Vacuum box geometry and reduced air gap are preferred over polymer modification for stabilizing the melt curtain. Unlike LDPE, the resin has limited extensional strain hardening; this limitation is managed by machine configuration rather than by raising melt temperature excessively, because thermal oxidation at die lips increases gel and edge trim. Neck-in at the die edge is larger for linear resins than for LDPE; deckle width and edge trim must be adjusted accordingly. In coextrusion structures, 20-10CE is generally located in core or sealant layers; skin layers of LDPE or polypropylene modify stiffness, optics, and sealing behavior.

    When Seal Initiation and Optical Haze Function as Film Grade Screening Criteria

    Where low seal initiation temperature and high gloss are critical, mLLDPE 20-10CE is screened against ZN-LLDPE and high-pressure LDPE using cast film samples at 25 µm thickness. Seal initiation is measured according to ASTM F88 with dwell time and pressure typical of packaging lines; the uniform hexene incorporation of the metallocene grade shifts the onset of seal strength development to temperatures roughly 5–12 °C below those required by Ziegler-Natta LLDPE of the same density. Optical haze is measured according to ASTM D1003, and gloss at 45° according to ASTM D2457. Lower catalyst residues and a controlled crystallization front reduce surface roughness and permit thinner film structures without sacrificing dart impact, measured according to ASTM D1709. Comparative film data for this grade are available from the supplier’s technical datasheet without specification-limit force; published data for this specific configuration is limited where film line and chill roll variables are not reported.

    Film propertyStandardEnable 20-10CEZN-LLDPELDPE
    DensityASTM D1505 / ISO 1183-10.920 g/cm³0.918–0.922 g/cm³0.918–0.922 g/cm³
    Melt indexASTM D1238 / ISO 1133-11.0 g/10 min0.8–1.2 g/10 min0.8–2.0 g/10 min
    Seal initiationASTM F8895–105 °C105–115 °C110–120 °C
    Haze, 25 µm cast filmASTM D10032–4%4–8%6–12%
    Dart impact F50, 25 µmASTM D1709500–800 g300–600 g100–300 g

    The values in the table are representative screening ranges for cast film in the density class, not specification limits. Differential scanning calorimetry under ISO 11357-3:2018 often shows a narrower melting range for mLLDPE than for ZN-LLDPE, which lowers heat-seal initiation but also reduces the melt processing window at low temperatures. For high-temperature sealing applications, the seal plateau and hot-tack measured by ASTM F1921 should be evaluated because ultimate seal strength can be governed by skin layer and seal bar pressure.

    Process Boundary Variables in Cast Extrusion of mLLDPE 20-10CE

    The primary process boundaries are melt temperature, shear rate, air gap, and cooling rate. Melt temperatures above 280 °C can accelerate oxidative gel formation at the die lip, resulting in die-lip buildup and film defects that are visible as arrowhead gels. Sustained operation above 300 °C is not recommended for this linear polyethylene. At the lower boundary, melt temperatures below 220 °C may produce incomplete melting of high-molecular-weight fractions and pressure pulsation. Incompatibility with amine-based antifog or antistatic masterbatches is not generally documented, but additives that release polar volatiles at cast film temperatures should be evaluated for die deposit interaction; fluoropolymer processing aids may reduce die lip buildup when used up to 0.05–0.10 wt% by extruder barrel output. If the resin is blended with LDPE to increase melt strength, addition levels below 20 wt% are typical because higher LDPE fractions raise seal initiation and haze.

    Extruder pressure response is affected by the narrow molecular weight distribution. At a constant screw speed, the melt pressure is generally higher than for a broad-MWD ZN-LLDPE at the same output, and motor load may increase. Screw cooling and feed-throat temperature control should be set to prevent pellet bridging at the feed section. A grooved-feed extruder can be used, but excessive pressure generation should be avoided by adjusting screw speed and screen pack. Die lip gap should not be increased beyond 1.0 mm solely to reduce pressure, because edge beading and gauge variability can increase. If optical haze rises at high output, chill roll temperature and contact pressure should be checked before polymer parameters are assigned as the cause.

    Compliance with olefin polymer food-contact regulations is governed by 21 CFR 177.1520 for the base polyethylene and by European Regulation EU 10/2011 for migration. End-use migration testing is the responsibility of the converter. The product is not a drop-in substitute for high-pressure LDPE on all cast lines because of lower melt strength and different extruder pressure response. Compared with ZN-LLDPE, the metallocene resin generally yields lower seal initiation, reduced haze, and improved dart impact at comparable density, but may require more attention to melt pressure and draw resonance. Compared with LDPE, 20-10CE gives higher dart impact and lower seal initiation, but LDPE typically provides better drawdown stability and higher neck-in resistance. These differences are controlled through screw design, die gap, air gap, and chill roll temperature rather than through melt index adjustment alone. Published data for this specific configuration is limited where the final film structure is a coextrusion with skin layers or where masterbatch addition exceeds 5 wt%.

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