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SABIC SUPEER mLLDPE 8118

    • Product Name: SABIC SUPEER mLLDPE 8118
    • 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 539539
    Product Name SABIC SUPEER mLLDPE 8118
    Polymer Type Metallocene Linear Low Density Polyethylene (mLLDPE)
    Catalyst Metallocene
    Comonomer 1-Butene
    Density 0.918 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 1.0 g/10 min
    Melt Flow Rate 190 C 21 6 Kg 20 g/10 min
    Melting Point 115 °C
    Vicat Softening Temperature 95 °C
    Tensile Strength At Yield 9 MPa
    Tensile Strength At Break 25 MPa
    Elongation At Break 600%
    Dart Drop Impact 250 g
    Elmendorf Tear Strength Md 200 g
    Elmendorf Tear Strength Td 400 g
    Haze 6%
    Gloss 45 80
    Seal Initiation Temperature 110 °C
    Coefficient Of Friction 0.2

    As an accredited SABIC SUPEER mLLDPE 8118 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged as SABIC SUPEER mLLDPE 8118 in 25 kg moisture-resistant polyethylene bags, supplied on pallets for convenient handling and storage.
    Container Loading (20′ FCL) Loaded into a 20-foot FCL container: SABIC SUPEER mLLDPE 8118 in palletized bags, dry, clean, and secured for ocean transport.
    Shipping Shipping description: SABIC SUPEER mLLDPE 8118, metallocene linear low-density polyethylene resin in pellet form; non-hazardous and not regulated for transport. Pack in moisture-resistant bags or octabins, keep dry and away from excessive heat, avoid contamination, and secure loads for truck or container shipment. No special dangerous goods documentation required.
    Storage Store SABIC SUPEER mLLDPE 8118 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep it in original, closed packaging to prevent moisture and contamination. Protect bags from punctures, tears, and excessive stacking pressure. Avoid prolonged UV exposure, control dust, and follow local regulations and the manufacturer’s storage guidance. Do not store near oxidizers or strong acids.
    Shelf Life SABIC SUPEER mLLDPE 8118 typically has a 24-month shelf life when kept in original packaging, cool, dry, and protected from sunlight.
    Application of SABIC SUPEER mLLDPE 8118

    SABIC SUPEER mLLDPE 8118 is an octene-1 metallocene linear low density polyethylene characterized by a nominal density of 0.918 g/cm³ per ISO 1183-1 and a melt flow rate of 1.0 g/10 min per ISO 1133-1:2022 at 190 °C and 2.16 kg load. The application environments that follow are restricted to conversion routes where the viscosity envelope and narrow comonomer distribution of this grade are routinely specified in blown film coextrusion. In each application, the polymer is treated as a formulation component rather than an isolated raw material, because the final processing window, regulatory status, and mechanical performance depend on the surrounding layer structure and additive package.

    How Does Sealant-Layer Rheology Affect Frozen-Food VFFS Line Speeds?

    In frozen-food vertical form-fill-seal (VFFS) packaging, the sealant layer of a coextruded blown film is evaluated through hot-tack and seal initiation performance rather than ambient tensile yield. The sealant layer is generally formulated with SABIC SUPEER mLLDPE 8118 at 60–80 wt% of the layer blend, while a fractional-MFI LDPE component at 20–40 wt% is introduced to raise bubble stability and reduce neck-in on dies in the 1.8–2.4 mm die-gap range. Compliance for EU retail packaging relies on Commission Regulation (EU) No 10/2011, with an overall migration limit of 10 mg/dm², and on U.S. direct-contact clearance under FDA 21 CFR 177.1520 for olefin polymers. Converters producing frozen-food formats under typical supermarket audits also require that the film substrate comply with current GMP requirements under Regulation (EC) No 2023/2006.

    Downstream conversion occurs on multi-layer blown film lines fitted with internal bubble cooling and segmented air rings; melt temperatures are held at 180–210 °C, blow-up ratios are set between 2.0:1 and 3.0:1, and frost-line heights are commonly positioned at 6–10 die diameters. Die gap selection interacts with the shear-thinning behavior of the metallocene: narrower gaps below 1.8 mm can generate excessive melt pressure and surface melt fracture, while gaps above 2.4 mm can reduce the transverse direction orientation needed for freezer bag toughness. The low seal initiation temperature of the resin permits VFFS jaw settings between 115 °C and 145 °C at dwell times below 0.3 s, which is critical for high-speed pillow-bag lines running 80–120 bags/min. Seal strength is verified per ASTM F88, while impact and tear resistance are controlled by ASTM D1709-16a and ASTM D1922-15a respectively. End-product configurations include pillow pouches for individually quick-frozen vegetables, gusseted freezer bags, and HFFS pre-made side-seal bags; film is typically supplied in thicknesses from 25 µm to 80 µm.

    Within the heavy-duty industrial packaging sector, the octene-1 architecture of SABIC SUPEER mLLDPE 8118 is specified in the core layer of three-layer shipping-sack and FIBC inner-liner films, where the primary failure modes are puncture propagation and cold-drop impact. The addition ratio in the core layer is typically 20–35 wt% mLLDPE 8118, with the outer layers consisting of HDPE or broad-MWD LLDPE at 65–80 wt% to preserve creep resistance and stiffness. Coextrusion is performed on high-stalk blown film lines with die gaps of 2.5–3.2 mm, a blow-up ratio between 1.8:1 and 2.2:1, and melt temperatures not exceeding 220 °C to avoid gel formation. For FIBC inner liners, relevant standards include ISO 21898:2007 for flexible intermediate bulk containers, with specific stack-load and cyclic-load verification methods; for export sacks carrying hazardous materials, the outer woven polypropylene shell is evaluated under the UN Model Regulations Chapter 6.5 requirements, while the inner liner is specified as a contaminant barrier with a minimum film thickness of 40 µm. End-product formats include FIBC liners, gusseted valve sacks for polymer granules, and agricultural seed packaging.

    Heavy-duty three-layer liner film construction for mLLDPE 8118
    LayerFunctionmLLDPE 8118 contentVerification standard
    Outer skinCreep resistance and external abrasion control0–10 wt%ISO 527-3
    CorePuncture and tear propagation resistance20–35 wt%ASTM D1922-15a
    Inner sealProduct barrier and seal integrity10–20 wt%ASTM F88

    Tear propagation is assessed by ASTM D1922-15a in both machine and transverse directions; the mLLDPE component increases the low-temperature cornering resistance of the sack, which is verified by drop tests according to ISO 7965-2 for filled sacks. The processing limitation of this structure is the reduction in creep stiffness when the mLLDPE fraction exceeds 35 wt%, which can increase sack elongation under stacking; published data for this specific configuration is limited, so the upper blend boundary is generally determined by stack-load trials on the converter’s own line. Film thicknesses for these liners are commonly between 50 µm and 120 µm.

    Agricultural Silage Cover Film Impact Resistance Under Low-Temperature Tension

    Agricultural silage cover and greenhouse end-uses expose the film to long-duration tensile loading at low ambient temperatures, so the selection criteria center on slow-crack growth and dart impact retention after UV exposure. SABIC SUPEER mLLDPE 8118 is commonly blended into the surface layer at 30–50 wt% with a thermoplastic C4-LLDPE or LDPE carrier phase at 50–70 wt%, and a UV stabilizer masterbatch based on HALS plus carbon black or titanium dioxide is metered at 1.5–3.0 wt%. Compliance for silage films in the EU is verified against EN 13206:2017 for covering films, which specifies tensile elongation and durability requirements, while greenhouse films are evaluated under EN 13206 or dairy-specific agricultural standards and under the general requirements of REACH Regulation (EC) No 1907/2006 for monomer and additive content.

    Blown film extrusion for silage cover is carried out on three-layer lines with die gaps of 2.0–3.0 mm, blow-up ratios of 2.5:1 to 3.5:1, and bubble stabilizing internal cooling to maintain layer thickness tolerances of ±5%. Film thicknesses typically range from 100 µm to 200 µm; the mLLDPE component improves Elmendorf tear resistance in both directions, which is assessed by ASTM D1922-15a, and improves low-temperature drop impact tested by ASTM D1709-16a. End-product types include clamp-on silage cover sheets, bunker pit edge strips, and single-season greenhouse cladding; the operational boundary is that the resin does not provide sufficient UV stability on its own and must be compounded with a hindered amine stabilizer system before exposure beyond 12 months.

    On high-speed stand-up pouch lamination lines, the sealant web is required to deliver low-temperature seal initiation without sacrificing interlayer adhesion after solventless lamination. SABIC SUPEER mLLDPE 8118 is introduced into the sealant layer at 75–90 wt% of the layer formulation, with the balance comprising either a low-crystallinity LDPE for lower sealing pressure or an antiblock/slip masterbatch at 1–2 wt% for coefficient-of-friction control. Indirect food contact and direct food contact status are documented under FDA 21 CFR 177.1520 and Commission Regulation (EU) No 10/2011, while lamination adhesives are evaluated separately under their own positive lists. Downstream conversion begins with blown film coextrusion at a die gap of 1.5–2.2 mm and a blow-up ratio of 2.0:1 to 2.5:1, followed by solventless or solvent-based lamination to PET, BOPP, or aluminium foil; the resulting laminate is converted on form-fill-seal machines with seal-bar temperatures between 125 °C and 155 °C and seal times of 0.2–0.4 s. End-product formats include stand-up pouches for dry snacks, pet food, and powdered beverages, with final laminate thickness between 70 µm and 140 µm.

    The boundary condition in this conversion route is adhesion to foil; 8118 is non-polar and does not produce direct aluminium adhesion without corona discharge or an adhesive tie layer. Slip-agent selection should avoid excessive primary amide loadings in the sealant layer because plate-out on the seal bar can reduce seal integrity; converters should verify hot-tack retention by ASTM F1921-20 or equivalent in-line seal testing. Published data for this specific configuration is limited to converter qualification runs.

    When Pallet Stretch Hood Film Demands Controlled Machine-Direction Tear Propagation

    In pallet stretch hood conversion, the film is blown in a multi-layer configuration and subsequently stretched over a pallet load by a dedicated hooding machine; the critical resin requirements are retained elasticity, puncture resistance, and machine-direction tear propagation control during hood application. SABIC SUPEER mLLDPE 8118 is specified in the core or tie layer at 25–40 wt% of the total structure, with C4-LLDPE or EVA-rich outer layers at 60–75 wt% to produce the surface cling and stretch force demanded by the hooding cycle. Industrial packaging compliance is typically limited to REACH Regulation (EC) No 1907/2006 and the RoHS directive 2011/65/EU when the packaging enters electrical/electronic supply chains; no direct food-contact documentation is required for this non-food logistics format.

    Processing is performed on three-layer blown film lines with die gaps of 2.0–2.8 mm and blow-up ratios between 2.5:1 and 3.5:1; melt temperatures are held at 190–220 °C. The resulting film is produced at thicknesses of 40–70 µm and tested for tensile elongation at break according to ISO 527-3:2018, with machine-direction Elmendorf tear resistance measured by ASTM D1922-15a as a direct indicator of resistance to crack propagation during the stretching sequence. End-product applications include hooded pallets for beverages, building materials, and chemical drums, where the tubular film is cut and sealed to a gusseted hood profile. The operational constraint is the balance between cling and elongation; a high mLLDPE fraction above 40 wt% can reduce surface tack to the point where pallet load retention fails in high-shrinkback hooding cycles, so layer distribution must be confirmed on the pallet unitization line.

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    Certification & Compliance
    More Introduction

    SABIC SUPEER mLLDPE 8118 is a metallocene-catalyzed linear low density polyethylene produced by SABIC for blown-film extrusion. The resin is supplied in pellet form and is distinguished from conventional Ziegler-Natta LLDPE by the single-site catalyst chemistry employed during polymerisation. Manufacturer-published nominal values list a density of 0.918 g/cm³ when tested in accordance with ISO 1183-1 and a melt flow rate of 1.0 g/10 min at 190 °C under a 2.16 kg load according to ISO 1133-1:2022. These values position the grade between lower-density metallocene sealants and higher-density structural film resins. The 0.918 g/cm³ density reduces seal initiation temperature relative to higher-density LLDPE, while the 1.0 g/10 min flow rate provides sufficient melt strength for bubble control on low-density polyethylene film lines. The grade is not a high-pressure LDPE replacement in applications that require high melt tension and high draw-down at large blow-up ratios. It is also not intended for injection moulding, rotational moulding, or profile extrusion, where the processing window and viscosity response are sufficiently different from blown-film operation.

    What Limits Melt Processing Stability in Narrow-Distribution mLLDPE Film Lines?

    The combination of a narrow molecular weight distribution and uniform short-chain branching alters both shear viscosity and extensional behaviour. In shear flow, 8118 exhibits a higher viscosity at the apparent shear rates encountered in a blown-film die than high-pressure LDPE of similar melt index. The polymer is less shear-thinning because long-chain branching is minimal. Consequently, extruder head pressure is commonly 15 % to 25 % higher than that of Ziegler-Natta C4-LLDPE at equal output and equal die gap. The exact pressure differential is line-specific because it depends on screw speed, barrel temperature profile, die size, and melt temperature. Apparent shear rate at the die lip can be estimated with γ̇ = 6Q/(πD h²), where Q is volumetric melt flow rate, D is die diameter, and h is die gap. For an annular die of 250 mm diameter and 2.0 mm gap at a volumetric flow rate of 37 cm³/s, the apparent wall shear rate is approximately 70.7 s⁻¹. If the die gap is reduced to 1.0 mm at constant output, the apparent shear rate rises to approximately 283 s⁻¹. This fourfold increase can move the melt past the critical shear stress for sharkskin melt fracture on polished dies. The calculation uses melt density, not solid-state density; at 200 °C, polyethylene melt density is approximately 0.75 g/cm³.

    On production-scale blown-film lines, bubble stability is governed by the strain hardening of the melt. Metallocene LLDPE lacks the long-chain branching of high-pressure LDPE and therefore exhibits lower strain hardening and lower melt tension. Processors typically set blow-up ratio between 2.0:1 and 2.5:1 and keep the frost line height at 1.5 to 2.0 die diameters when running 8118, but these values are starting points rather than universal specifications. Internal bubble cooling raises output and stabilises the bubble by removing heat from inside the bubble; it is often specified on lines built for metallocene LLDPE. Melt temperature exiting the die is typically held at 195 °C to 205 °C, but higher temperatures can reduce bubble stability if the melt film sags before crystallisation.

    Die gap selection interacts with film optics and mechanical properties. A die gap of 1.4 mm to 2.0 mm is typical for 0.918 g/cm³ metallocene film resins because it reduces shear heating and improves bubble stability. Many older LDPE lines have die gaps of 0.8 mm to 1.2 mm; these lines may be converted to 8118, but the user should expect higher extruder pressure and may require a fluoropolymer processing aid at 0.02 % to 0.08 % by weight to delay melt fracture. Processing aid levels above 0.10 % are not generally required and may cause die lip deposit formation. The use of a barrier screw with L/D ratio 25:1 to 30:1 and a spiral mandrel die with a moderately polished land surface reduces the incidence of melt fracture and improves film thickness uniformity. Lot-to-lot melt flow rate variation is controlled within manufacturer specification, but the narrow molecular weight distribution means small changes in melt index can shift die pressure more than similar changes in broad-distribution LLDPE.

    In performance comparisons against conventional C4-LLDPE, the metallocene catalyst system changes the distribution of comonomer along the chain. Ziegler-Natta C4-LLDPE with the same bulk density of 0.918 g/cm³ carries a higher fraction of short chains that remain in the amorphous phase and contribute to extractables and lower hot-tack. 8118 places the α-olefin more uniformly along the high-molecular-weight fraction, which increases tie-molecule concentration and enhances dart impact strength per unit thickness. The practical consequence is that film can be downgauged by 10 % to 20 % in some heavy-duty sack applications while retaining dart impact resistance, but the exact downgauging ratio must be confirmed by running the intended film structure on the target line. Published data for this specific configuration is limited when the film structure includes regrind or high levels of anti-block masterbatch, because additive particles alter tear resistance and optics independently of the metallocene base resin.

    Property and test method SABIC SUPEER mLLDPE 8118 Conventional C4-LLDPE High-pressure LDPE
    Density ISO 1183-1 0.918 g/cm³ 0.918 g/cm³ to 0.920 g/cm³ typical 0.918 g/cm³ to 0.924 g/cm³ typical film grades
    Melt flow rate ISO 1133-1:2022 at 190 °C/2.16 kg 1.0 g/10 min 0.9 g/10 min to 1.1 g/10 min available 0.2 g/10 min to 0.5 g/10 min typical
    Dart impact ISO 7765-1/A Higher than C4-LLDPE at equal gauge; film-line dependent Moderate Lower at equal gauge
    Elmendorf tear ISO 6383-2 Machine/transverse tear balance is gauge and blow-up ratio dependent Directional tear balance may favour machine direction to a lesser degree Typically lower transverse tear strength
    Seal initiation temperature Lower than C4-LLDPE of equal density Higher Higher
    Haze ISO 14782 Lower than C4-LLDPE typical; final value depends on cooling rate Higher Variable, often higher than metallocene LLDPE

    End-use applications for 8118 involve packaging films where seal integrity, optics, and impact toughness are required. The grade is used in multi-layer coextruded films as an outer or sealant web. Its lower seal initiation temperature allows heat-seal temperatures to be reduced on form-fill-seal machines, which may increase cycle speed when other packaging components tolerate the lower set point. Seal strength tests are commonly performed in accordance with ASTM F88, while hot-tack measurements follow ASTM F1921. The resin is also used in heavy-duty bags, frozen food packaging, liquid packaging inner layers, and lamination film. In frozen food packaging, the combination of low-temperature dart impact resistance and seal integrity at freezer temperatures is the primary design criterion. Low-temperature impact testing is usually carried out with ISO 7765-1/A after conditioning at -40 °C or at the intended storage temperature, because room-temperature impact data do not predict behaviour in frozen food distribution. Published data for 8118 under frozen conditions are limited.

    In five-layer or seven-layer coextruded structures, 8118 can serve as a sealant layer with a thickness of 10 µm to 25 µm within a total film gauge of 50 µm to 120 µm. The layer ratio must be validated because the low seal initiation temperature can allow the outer layer to remain cooler, but if the outer layer is still below its softening point, the seal jaw may not transfer enough heat through the film cross-section. When 8118 is blended with high-pressure LDPE for bubble stability, the addition of LDPE usually lowers dart impact and raises haze. The optimum balance is often 10 % to 30 % LDPE, but line-specific trials are needed. Conversely, adding 8118 to high-pressure LDPE improves seal initiation and dart impact but reduces melt tension.

    Regulatory Compliance Matrix for Food-Contact and Non-Food Film

    Compliance is additive-package-specific and lot-specific. The following table summarises commonly requested regulatory instruments for metallocene LLDPE film resins. A product-specific statement from SABIC is required before use in food-contact or medical packaging, because migration limits depend on the complete final film structure and converting conditions.

    Regulatory instrument Typical scope Verification for 8118
    FDA 21 CFR 177.1520(c) Olefin polymers for food contact, subject to density and extraction limits Manufacturer letter required for specific grade and additive package
    EU Regulation (EU) No 10/2011 Plastics intended for food contact, including overall and specific migration limits Compliance determined by migration testing of final article
    REACH Regulation (EC) No 1907/2006 SVHC screening and restrictions in the EU Grade-specific declaration required
    RoHS Directive 2011/65/EU Restricted hazardous substances in electrical and electronic equipment Polyethylene grades are generally outside direct scope; customer-specific certification applies

    Operational boundaries for 8118 include melt temperature limits and blending boundaries. The grade should not be processed above 220 °C for extended residence times, because oxidative degradation may generate gels and discoloration. Barrel temperatures are usually set between 180 °C and 200 °C in the feed and metering zones, with die temperature held at 195 °C to 205 °C. Pre-drying is not generally required for pellets stored below 60 % relative humidity. If condensation is visible on the pellets, a hopper dryer at 60 °C to 70 °C for 1 h to 2 h is applied by some converters, but the practise is less common for polyethylene than for hygroscopic polymers. The product should not be assumed to be a universal replacement for all conventional LLDPE applications. Similar density and melt flow rate do not guarantee equivalent bubble stability, screw output, or seal-bar set-point behaviour. Selection must be based on a measured seal-temperature, dart impact, and melt-pressure comparison on the target production line.

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