| HS Code | 492565 |
| Polymer Type | Metallocene Linear Low Density Polyethylene (mLLDPE) |
| Density | 0.918 g/cm³ |
| Melt Index 190 C 2 16 Kg | 1.0 g/10 min |
| Peak Melting Temperature | 119 °C |
| Vicat Softening Temperature | 95 °C |
| Tensile Strength At Yield | 10 MPa |
| Tensile Strength At Break | 35 MPa |
| Elongation At Break | 600 % |
| 1 Secant Modulus | 200 MPa |
| Dart Impact Strength | 200 g |
| Elmendorf Tear Strength Md | 200 g |
| Elmendorf Tear Strength Td | 300 g |
| Haze | 8 % |
| Gloss 45 | 60 |
As an accredited ExxonMobil Exceed mLLDPE 2718QA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | ExxonMobil Exceed mLLDPE 2718QA is supplied in sealed 25 kg polyethylene bags, with 40 bags per 1,000 kg pallet. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): ExxonMobil Exceed mLLDPE 2718QA in palletized 25 kg bags, roughly 18–20 MT net, loaded dry and sealed. |
| Shipping | ExxonMobil Exceed mLLDPE 2718QA is shipped as non-hazardous metallocene polyethylene resin pellets, typically in 25 kg bags or octabins. Keep packages dry, cool, and protected from sunlight and heat. Use standard handling equipment; no special transport classification or hazard placards required. |
| Storage | Store ExxonMobil Exceed mLLDPE 2718QA in a clean, dry, well-ventilated area, away from direct sunlight, heat sources, moisture, and contaminants. Keep material in original sealed packaging on pallets, off the floor, and protect from prolonged UV exposure and strong odors. Maintain ambient storage conditions, practice first-in/first-out, and avoid damaging bags to prevent dust or water ingress. |
| Shelf Life | No specific shelf life is assigned; store resin pellets cool, dry, well-ventilated, away from sunlight/ignition; refer to supplier. |
ExxonMobil Exceed mLLDPE 2718QA is a hexene-based metallocene linear low-density polyethylene with a nominal density of 0.917 g/cm³ (ASTM D792-20) and a melt flow rate of 2.7 g/10 min (ASTM D1238-20, 190°C/2.16 kg). The following application profiles separate downstream processing sectors by equipment configuration, formulation ratio, and regulatory exposure.
High-speed rotary-ring pre-stretch machines consume cast pallet wrap at film draw speeds above 600 m/min and require a balance among unwind tension, cling force, and puncture resistance. In this application, Exceed mLLDPE 2718QA is blended at 70–85 wt% with 10–25 wt% LDPE or higher-MI LLDPE and 1–3 wt% polyisobutylene-based cling masterbatch, dosed into the cling layer rather than the back layer to control unwind noise. The film is produced on a multi-layer cast coextrusion line with a slot die gap of 0.5–0.9 mm, die exit melt temperatures held between 240°C and 260°C, and a polished chill roll surface controlled at 15–30°C. Layer distribution in five-layer lines commonly assigns 15–20 wt% of total throughput to the cling skin, 20–30 wt% to the release skin, and the remainder to core layers; edge trim is re-fed to the core at up to 20 wt% without measurable gel accumulation when melt filtering uses 60/100/120 mesh screen packs and die exit temperature remains below 260°C. Production-scale observation indicates that the narrow molecular weight distribution raises screw torque relative to Ziegler-Natta LLDPE; barrier screws with 30:1 L/D and drive power above 0.20 kW/(kg/h) are required to maintain throughput without screw-speed overshoot. Terminal products are machine-grade pre-stretched films at 12–23 µm, supplied on 250–500 mm web widths and applied at pre-stretch ratios of 200–300%. Compliance relies on ASTM D5458-19 for peel cling, ASTM D5748-19 for puncture, ASTM D882-18 for tensile properties, and REACH Regulation (EC) No 1907/2006 for substance registration.
Because hand-applied stretch film is stretched manually, edge tear propagation governs roll performance more strongly than machine-direction ultimate tensile strength. Hand-grade formulas using Exceed mLLDPE 2718QA typically contain 65–85 wt% of the metallocene resin, 15–35 wt% LDPE or butene LLDPE to promote melt draw, and 2–4 wt% cling additive masterbatch to achieve sufficient peel cling on smooth, cold warehousing floors. The downstream process is cast coextrusion with edge-trim re-feed up to 15 wt%; extruder temperature profiles are set lower in the feed zone at 190–210°C and progressively increased to a die exit of 240–260°C. Chill-roll wrap angle and air-knife pressure are adjusted to suppress lateral gauge bands, a recurrent defect when entering the online pre-stretch unit at 250–400 m/min. Film haze below 2% (ASTM D1003-21) and clarity above 98% (ASTM D1746-15) are typical acceptance limits for retail packaging warehouses. The terminal product is a hand-grade stretch wrap roll of 15–20 µm, commonly on 300 mm cores, used for irregular pallet shapes and low-volume bundling. ASTM D5458-95(2019) peel cling values are specified by convertors in the 80–140 g/25 mm range, while ASTM D882-18 transverse-direction elongation at break is monitored to avoid film splits at the film edge.
Blown and cast coextruded flexible packaging structures use a thin heat-seal skin layer where Exceed mLLDPE 2718QA is incorporated at 80–100 wt%, optionally diluted with 10–20 wt% metallocene plastomer to reduce seal initiation by 3–5°C in higher-speed vertical form-fill-seal lines. The downstream process is cast-film coextrusion with the sealant layer contacting a chill roll to develop low haze below 3% (ASTM D1003-21) and high gloss above 80 GU at 60° (ASTM D2457-21). Seal initiation temperature is a process conflict: the dense tie-chain population of hexene mLLDPE increases hot-tack strength but can elevate seal initiation by 4–7°C compared with an equivalent butene LLDPE at equal density, forcing line operators to increase seal-bar setpoint or dwell time. Hot-tack force is evaluated per ASTM F1921-20, and the finished laminate must comply with FDA 21 CFR 177.1520 for olefin polymers and Commission Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm². Terminal products include dry-food pouches, frozen vegetable packs, and overwrap for paperboard trays. Published data for the exact seal-initiation window of Exceed 2718QA in retort configurations is limited; convertors should validate seal strengths on their own jaw geometry before line-speed increases.
| Scenario | Standard or regulation | Clause or test method | Measured parameter |
|---|---|---|---|
| Machine-grade pre-stretch film | ASTM D5748-19 | Method A | Puncture resistance |
| Machine-grade pre-stretch film | ASTM D5458-95(2019) | Peel cling | Cling force |
| Food-contact sealant web | FDA 21 CFR | 177.1520 | Olefin polymer clearance |
| Food-contact sealant web | EU Regulation | 10/2011 | Overall migration / SML |
| Surface-protective film | ASTM D1894-14 | COF | Static and dynamic friction |
| Non-food recycled-core film | Directive 94/62/EC | Heavy metals | Packaging waste compliance |
Surface-protective cast film for stainless steel coil, lacquered aluminium sheet, and polycarbonate board uses Exceed mLLDPE 2718QA at 85–100 wt% in the core and outer skin, with slip and antiblock additives incorporated at 0.2–0.8 wt% erucamide and 0.1–0.3 wt% synthetic silica or talc. Migration kinetics control the coefficient of friction: freshly cast film exhibits a static COF of 0.45–0.60, dropping to 0.15–0.25 after 24–72 h as the amide blooms to the surface, measured per ASTM D1894-14. The downstream process is a cast coextrusion line with one-side corona treatment at 38–42 mN/m surface tension on the layer later coated with pressure-sensitive adhesive. Production-scale field data show that erucamide loadings above 1 wt% create chill-roll plate-out and transfer marks, causing visible haze streaks on the protected sheet. Thickness tolerance across the web is maintained at ±1 µm on a 2,000 mm die width through automatic bolt adjustment. Terminal products are protective masking films from 30–70 µm, slit to sheet widths, and applied to automotive interior trim or appliance stainless steel panels. Compliance includes Directive 2011/65/EU (RoHS) for hazardous substances and REACH Regulation (EC) No 1907/2006 for migrating additives. The operational boundary is the coefficient of friction after aging; films stored at warehouse temperatures above 35°C may exhibit excessive bloom and adhesive transfer after 6 months.
Non-food, high-clarity cast film used for garment bags, furniture overwrap, and temporary construction protection can be produced as an ABA structure in which the outer skins are Exceed mLLDPE 2718QA at 20–30 wt% per skin, and the core contains 40–60 wt% post-consumer recycled LLDPE. The recycled-core formulation is selected to retain optical clarity and low gel content in the skin while reducing total material carbon cost. The downstream process is a three-layer cast coextrusion line with dedicated edge-trim re-feed to the core extruder, which is equipped with a fine screen pack of 100/150/200 mesh to intercept gel particles. Melt temperatures at the die are held at 230–250°C; the skin extruder is run at 210–230°C to limit oxidation of recycled material migrating from the core. Terminal products are non-food bags and overwrap at 20–35 µm. Compliance follows REACH Regulation (EC) No 1907/2006 and, where the film enters European packaging waste streams, Directive 94/62/EC with a sum of lead, cadmium, mercury, and hexavalent chromium below 100 mg/kg. This application is not suitable for food contact under FDA 21 CFR 177.1520 unless recycled content is separated by a functional barrier validated by migration testing; published data for this specific configuration is limited.
Refrigerated red-meat display wrapping imposes simultaneous cold-seal, puncture, and optical clarity constraints that limit the resin slate to metallocene LLDPE grades with low gel counts. Exceed mLLDPE 2718QA is extruded at 90–100 wt%, with the balance being a process aid masterbatch at 0.3–0.8 wt% to reduce melt fracture at the slot die. The cast-film process runs with a die exit melt temperature of 240–260°C, a chill roll at 10–25°C, and a downstream aqueous bath or vacuum trim removal on lines exceeding 200 m/min. Terminal products are retail meat and poultry overwrap film at 8–15 µm, printed flexographically and folded into trays. The seal layer must pass FDA 21 CFR 177.1520 and EU Regulation No 10/2011; oxygen transmission measured by ASTM D3985-17 is controlled by film thickness rather than resin formulation. Operational limitations include the absence of a high-tack surface; cling is not an inherent property of Exceed 2718QA, so overwrap lines using cling dispensers may require an added cling masterbatch at 1–3 wt% with revalidation of food-contact compliance.
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ExxonMobil Exceed mLLDPE 2718QA is a metallocene linear low-density polyethylene resin for monolayer and coextruded film structures. The nominal density is 0.918 g/cm³ when determined by ASTM D1505 or ISO 1183-1, and the nominal melt index is 1.0 g/10 min when measured at 190°C/2.16 kg by ASTM D1238 or ISO 1133-1. Differential scanning calorimetry according to ASTM D3418 or ISO 11357-3 indicates a melting peak near 119°C. These values place the grade in the soft-tough film envelope used for packaging structures requiring low-temperature seal strength, tear resistance, and puncture resistance.
The resin is produced by single-site catalysis. The molecular weight distribution is narrower than that of conventional Ziegler-Natta linear low-density polyethylene, and the short-chain branching distribution is more homogeneous. This molecular architecture changes both the solid-state melting profile and the melt rheology. High-temperature gel permeation chromatography according to ISO 16014-4 can be used to verify the narrow distribution, while hexane extractables are evaluated by ISO 6427 or the applicable food contact specification.
The homogeneous branching distribution lowers the seal initiation temperature relative to Ziegler-Natta LLDPE of the same density because the crystal thickness distribution is narrower. Hot-tack strength is measured by ASTM F1921, and seal strength is measured by ASTM F88/F88M. In production comparisons, metallocene grades retain hot-tack over a wider temperature interval than similarly formulated LDPE sealant layers. The same architecture raises dart impact strength measured by ASTM D1709 and Elmendorf tear strength measured by ASTM D1922 at equivalent thickness. The trade-off is lower melt strength and less strain hardening than LDPE, so blown film bubble stability is managed by adjusting blow-up ratio, frost line height, and air ring conditions rather than by increasing melt temperature without limit.
At film extrusion shear rates, the narrow molecular weight distribution may produce elevated head pressure relative to LDPE of comparable melt index, depending on die gap and melt temperature. The pressure signal at the screen changer is therefore used as a process diagnostic. Capillary rheometry according to ISO 11443 or ASTM D3835 provides shear viscosity curves for equipment sizing. On blown film lines with screw length-to-diameter ratios of 24:1 to 30:1 and die gaps of 1.2 mm to 2.0 mm, stable operation is commonly established at blow-up ratios of 2.0:1 to 3.0:1. Melt temperatures are often set between 193°C and 221°C; operation above 240°C is not recommended for extended periods because the antioxidant package may deplete, generating oxidation products and possible odor. On cast film lines, the chill roll temperature is maintained between 15°C and 40°C to control quench rate and optical properties.
Blending with LDPE is used on blown film lines to increase melt strength. The blend ratio is optimized against bubble stability and final film optics; addition of LDPE may reduce dart impact and increase haze if the blend is not optimized. Haze is measured by ASTM D1003, and 45° gloss is measured by ASTM D2457.
Pre-drying in a desiccant hopper at 50°C to 80°C for 2 h to 4 h is recommended only when storage humidity exceeds 60% RH. Surface moisture on pellets can introduce fish eyes and bubble defects. Equipment and silo design should use the supplier's bulk density data; typical polyethylene pellet bulk density lies between 0.53 g/cm³ and 0.56 g/cm³, but lot-specific values should be confirmed before sizing conveying lines.
In three-layer or five-layer structures, 2718QA may serve as the sealant skin because its low seal initiation temperature allows reduced jaw temperature on form-fill-seal machines. It is coextruded with tie resins and polyamide or EVOH barrier layers; the melt processing temperatures of the complete structure must remain below the barrier polymer's degradation threshold while maintaining interlayer adhesion. Seal strength is measured on finished film by ASTM F88/F88M; hot-tack is measured by ASTM F1921. The resin itself does not confer food contact approval on the final package; migration testing according to EU 10/2011 or FDA 21 CFR 177.1520 must be completed on the final article.
| Property | Nominal value | Test method |
|---|---|---|
| Density | 0.918 g/cm³ | ASTM D1505 / ISO 1183-1 |
| Melt index | 1.0 g/10 min | ASTM D1238 / ISO 1133-1 at 190°C/2.16 kg |
| Melting peak temperature | 119°C | ASTM D3418 / ISO 11357-3 |
| Regulatory reference | Test method or condition |
|---|---|
| FDA 21 CFR 177.1520(c) 3.1a | Olefin polymers for food contact; final article compliance required |
| EU 10/2011 | Overall migration limit 10 mg/dm² by EN 1186-1, depending on food simulant and contact conditions |
| REACH EC 1907/2006 | SVHC screening at 0.1% w/w |
| RoHS 2011/65/EU | Heavy metal screening by IEC 62321 |
Mechanical properties of film made from 2718QA are not fixed resin constants. Tensile properties are evaluated by ASTM D882 or ISO 527-3, dart impact by ASTM D1709, Elmendorf tear by ASTM D1922, puncture resistance by ASTM D5748, and low-temperature impact by ASTM D1743 as applicable. Because gauge, draw ratio, frost line height, and layer distribution influence these values, the certificate of analysis for the specific lot should be reviewed for density and melt index, and converter validation on production equipment is required to establish final film performance. Published data for certain application-specific configurations is limited.
The additive package in 2718QA includes antioxidants and processing stabilizers intended for film extrusion. Oxidative induction time can be evaluated by ISO 11357-6 to verify stabilizer retention after processing. The upper melt temperature should be limited to 240°C for extended residence time. The resin should not be combined with incompatible acid- or amine-based additives unless the additive supplier confirms compatibility with the polyolefin stabilization system. Contact with strong oxidizing agents, aromatic hydrocarbons, or chlorinated solvents at elevated temperatures can plasticize or degrade the surface and requires chemical compatibility review.
Relative to LDPE, 2718QA provides higher dart impact and Elmendorf tear resistance at equal film gauge; however, LDPE may provide greater melt strength and easier bubble stability. Relative to Ziegler-Natta LLDPE at identical melt index and density, 2718QA typically gives lower seal initiation temperature and lower hexane-extractable content. Compared with higher-density metallocene grades near 0.926 g/cm³, the 0.918 g/cm³ density reduces modulus but improves impact and tear balance. Compared with lower-density plastomers near 0.912 g/cm³, it provides higher modulus and better thermal resistance. Tensile modulus is measured by ASTM D882; seal initiation is evaluated by gradient heat seal testing according to ASTM F2029. No single resin property predicts all film performance outcomes.
In a production-scale form-fill-seal application, pellets are conveyed to the extruder hopper, melted, and formed into film. Process records should include melt temperature, die pressure, screw speed, and output against the lot certificate of analysis. If film gauge variation exceeds the control limit, automatic air ring control and internal bubble cooling can be used to stabilize the bubble; the frost line position is controlled with infrared sensors. No additional processing step is required beyond standard pellet drying when high-humidity storage has occurred.