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SABIC SUPEER mLLDPE 7118LE

    • Product Name: SABIC SUPEER mLLDPE 7118LE
    • 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 203029
    Polymer Type Metallocene Linear Low Density Polyethylene (mLLDPE)
    Density 0.918 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 1.0 g/10 min
    Comonomer 1-Hexene
    Catalyst Metallocene
    Melting Point 118 °C
    Vicat Softening Temperature 95 °C
    Tensile Strength At Yield Md 9 MPa
    Tensile Strength At Break Md 35 MPa
    Tensile Strength At Break Td 30 MPa
    Elongation At Break Md 500%
    Elongation At Break Td 700%
    Dart Drop Impact 200 g
    Elmendorf Tear Strength Md 120 g
    Elmendorf Tear Strength Td 300 g
    Haze 8%
    Gloss 45 70
    Heat Seal Initiation Temperature 95 °C

    As an accredited SABIC SUPEER mLLDPE 7118LE factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing SABIC SUPEER mLLDPE 7118LE is packaged in 25 kg moisture-resistant polyethylene bags for safe industrial storage and transport.
    Container Loading (20′ FCL) SABIC SUPEER mLLDPE 7118LE packed in 25 kg bags, palletized and loaded into a 20-foot FCL container for shipment.
    Shipping SABIC SUPEER mLLDPE 7118LE is typically supplied as free-flowing pellets in 25 kg PE bags or jumbo bags, palletized and stretch-wrapped. Ship in clean, dry containers, protected from moisture, heat, and direct sunlight; it is a non-hazardous polymer requiring no special dangerous-goods classification.
    Storage Store SABIC SUPEER mLLDPE 7118LE in a cool, dry, well-ventilated area away from direct sunlight, heat and ignition sources. Keep original containers/packaging closed and palletized to prevent moisture, dirt and UV exposure. Avoid prolonged outdoor storage and contact with incompatible chemicals. Observe local regulations and the manufacturer’s safety data sheet for specific handling and storage requirements.
    Shelf Life SABIC SUPEER mLLDPE 7118LE has a shelf life of 24 months when stored in original packaging, cool and dry, away from direct sunlight.
    Application of SABIC SUPEER mLLDPE 7118LE

    SABIC SUPEER mLLDPE 7118LE at nominal density 0.918 g/cm³ and melt flow rate 1.0 g/10 min measured under ISO 1133-1:2022 at 190 °C/2.16 kg is processed on high-speed vertical form-fill-seal lines through monolayer blown film dies. On 45–75 mm single-screw extruders with L/D 30:1 barrier screws and Maddock mixing sections, the melt temperature is held between 190 °C and 230 °C, the die gap is set from 0.8 mm to 1.6 mm, and the blow-up ratio is controlled at 2.0–2.8 to avoid transverse-direction tear resistance collapse while retaining bubble stability. A 100% 7118LE formulation is feasible only when the extruder drive is sized for 10–20% higher torque than an equivalent LDPE run; otherwise 15–25 wt% LDPE is blended to reduce melt pressure and stabilise the frost line. Antiblock masterbatch is added at 2–4 wt% and slip masterbatch at 0.5–1.5 wt%. Heat seal strength is checked under ASTM F88/F88M, puncture resistance under ASTM D5748, dart impact under ISO 7765-1, and haze under ISO 14782. Compliance for dairy, bakery, and snack packaging is established against FDA 21 CFR 177.1520(c) 3.2a and EU Regulation No 10/2011; high-fat food simulants require overall migration below 10 mg/dm².

    In heavy-duty block-bottom sack extrusion, 7118LE is introduced at 60–80 wt% alongside 10–25 wt% LDPE and 5–15 wt% carbon-black or colour masterbatch to increase slow puncture resistance and reduce film thickness without sacrificing package integrity. Production on 90 mm grooved-feed extruders with L/D 30:1 and 350–500 mm rotating dies requires melt temperatures no higher than 215 °C; excursions above this threshold generate oxidative gels that appear as pinholes in 150–250 μm sack film. The downgauged webs are tested under ISO 527-3 for tensile yield and elongation at break, ISO 6383-2 for Elmendorf tear, and ISO 7765-1 Method A for dart impact. Finished FIBC liners and chemical sacks are qualified under ISO 21898 for UV stability and physical handling; packaging waste compliance is screened against EU Directive 94/62/EC heavy-metal limits. Blown film towers must be equipped with high-capacity internal bubble cooling because 7118LE retains heat longer than C4-LLDPE and may block in collapsing frames when line speeds exceed 60 m/min on thick-gauge webs.

    Pallet Unitization Mechanics and Stretch Hood Recovery Thresholds

    Stretch hood film produced from 7118LE is pre-stretched 60–80% on pallet hood machines with rotary and vertical simultaneous stretching cycles; the critical film property is retained load after elongation rather than ambient yield strength. The blend for pallet hoods typically contains 70–80 wt% 7118LE, 10–20 wt% LDPE, and 5–10 wt% high-molecular-weight HDPE to raise strain hardening and prevent localised necking at high stretch ratios. Extrusion uses 1.2–2.4 m layflat width dies with 1.2–2.2 mm die gaps, blow-up ratios between 3.0 and 4.0, and melt temperatures of 195–220 °C. The film must be tested under ISO 527-3 for elongation at break, ASTM D5748 for puncture resistance after pre-stretching, and a stress-relaxation procedure for retained load. Under EU Directive 94/62/EC, the film is also screened for lead, cadmium, mercury and hexavalent chromium totals not exceeding 100 ppm combined. End-product hoods are converted for cement bag pallets, PET bottle pallets, and white goods distribution; field failures are most commonly tied to uneven gauge distribution caused by poor oscillating haul-off calibration rather than resin deficiency.

    Assigning 7118LE to the sealant layer of a seven-layer blown film structure for modified atmosphere packaging requires a layer thickness of 15–30 μm against polyamide or EVOH core layers. The coextrusion line is configured with separate extruders per layer; the sealant extruder operates at 210–240 °C while the barrier extruder is kept within its own melt temperature window, and the multi-layer die is maintained at 220–240 °C to prevent interfacial flow instabilities. The sealant formulation is 80–100 wt% 7118LE with 5–15 wt% anti-block masterbatch and, where high-speed vertical packaging demands consistent hot tack, 200–500 ppm of a fluoropolymer processing aid to reduce die lip oxidation. Seal strength is measured under ASTM F88/F88M, hot tack under ASTM F1921, and oxygen transmission through the finished laminate under ASTM D3985. Food-contact status is demonstrated under FDA 21 CFR 177.1520(c) 3.2a and EU Regulation No 10/2011 with specific migration testing in 95% ethanol and 3% acetic acid simulants. The end products include vacuum pouches for fresh red meat, cheese, and MAP flowpacks; seal initiation below 105 °C is targeted for high-speed vertical baggers.

    What Limits UV Stabilization Loadings in 7118LE-Based Silage Cover Film?

    Long-term silage cover film demands an absorption and hindered amine stabilisation package that does not create localised gel formation during extended blown film runs. In 7118LE-based silage webs, the resin fraction is 80–90 wt%, LDPE is 5–10 wt%, and a UV masterbatch containing HALS and titanium dioxide is added at 5–10 wt%; exceeding 10 wt% UV masterbatch has been observed to increase screw pressure fluctuation and reduce melt fracture control, especially on 70 mm extruders without grooved barrel cooling. Film thickness is 120–250 μm, die gap is 1.6–2.5 mm, blow-up ratio is 2.0–2.8, and melt temperature is limited to 190–210 °C to protect the HALS package from volatilisation. Accelerated weathering is conducted under ISO 4892-2, film tensile after ageing under ISO 527-3, tear propagation under ISO 6383-2, and product classification under EN 13206 for agricultural covering films. The converted products are silage bunker covers and anaerobic fermentation sheets for chopped maize and grass; outdoor exposure beyond 12 months typically shifts failure mode from tensile loss to surface crazing in unpigmented film, which is why white or titanium dioxide-pigmented layers are used in exposed northern European storage.

    Films conditioned at −40 °C before filling on frozen-food bagging machines rely on 7118LE for dart impact retention and seal integrity through cold-chain distribution. The formulation is 70–90 wt% 7118LE with 10–20 wt% LDPE to reduce film-to-film blocking, and 0.5–1.5 wt% slip masterbatch to maintain coefficient of friction under ISO 8295. Extrusion on a 50–80 mm single-screw blown film line uses melt temperatures of 190–210 °C, die gap 1.2–1.8 mm, and frost line height 4–8 die diameters to maximise impact strength without excessive orientation. Dart impact after conditioning is tested under ISO 7765-1 Method A, low-temperature tensile under ISO 527-3, and seal strength under ASTM F88/F88M; hot tack under ASTM F1921 determines the maximum bagging speed. Food-contact requirements are verified against FDA 21 CFR 177.1520(c) 3.2a, EU Regulation No 10/2011, and EC Regulation No 1935/2004 for materials intended to come into contact with frozen vegetables, seafood, and ice cream. Converted products include side-seal pouches and bottom-gusset bags for deep-freeze applications; seal settings must be re-validated whenever the LDPE fraction is changed because seal initiation increases disproportionately above 20 wt% LDPE addition.

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    Certification & Compliance
    More Introduction

    SABIC SUPEER mLLDPE 7118LE is a single-site metallocene linear low-density polyethylene (mLLDPE) grade in the SABIC SUPEER portfolio. The grade is specified for blown film and cast film applications that require controlled seal initiation, high hot-tack strength, and low gel levels. Nominal density is 0.918 g/cm³ as measured by ASTM D1505, and nominal melt flow rate is 1.0 g/10 min at 190 °C and 2.16 kg load per ASTM D1238 or ISO 1133-1:2022. These values are supplier technical datasheet nominal values and are not release limits. The product is used in multilayer food packaging, frozen food films, high-clarity overwrap, heavy-duty packaging, and sealant webs in lamination structures. Because it is produced using metallocene catalysis, the grade has a narrower molecular weight distribution and more uniform intermolecular comonomer distribution than conventional Ziegler-Natta C4-LLDPE. That molecular architecture changes crystallisation, optical, and seal behaviour relative to conventional linear low-density polyethylene grades of the same density and melt index.

    Published nominal property matrix for SABIC SUPEER mLLDPE 7118LE
    PropertyTest methodNominal value
    DensityASTM D15050.918 g/cm³
    Melt flow rateASTM D1238, 190 °C/2.16 kg1.0 g/10 min
    Peak melting temperature, differential scanning calorimetryASTM D3418121–124 °C

    Why does 7118LE require die-gap adjustment on blown film lines?

    On single-screw extruders with 24:1 to 30:1 L/D barrier screws, the melt temperature should be held between 190 °C and 230 °C. The grade exhibits less shear thinning than conventional LLDPE, so pressure peaks in spiral mandrel dies occur earlier than with Ziegler-Natta C4 grades of equivalent melt index. Die gaps below 1.5 mm are associated with sharkskin onset under typical blown film shear rates; a die gap of 1.8–2.5 mm is recommended for production. Blow-up ratio is typically kept between 2.0:1 and 3.0:1, with frost line height at 1–3 die diameters. If sustained head pressure exceeds 35 MPa, the die gap, melt temperature, or screen-pack configuration should be revised. Polymer processing aids may be required on narrow-gap lines. No forced pre-drying is required for resin stored at 20–25 °C and 50–60% RH; surface moisture from cold storage must be allowed to evaporate before extrusion.

    Typical blown film extrusion parameters for 7118LE
    ParameterTypical rangeUnit
    Melt temperature190–230°C
    Die gap1.8–2.5mm
    Blow-up ratio2.0:1–3.0:1dimensionless
    Frost line height1–3 die diametersdimensionless

    Seal performance is a primary reason for specifying 7118LE. In heat-seal testing performed according to ASTM F1921, the grade produces measurable hot tack at lower platen temperatures than a comparative Ziegler-Natta C4-LLDPE of equal density and melt index; the offset is generally reported in the range of 5–12 °C, depending on film thickness and dwell time. Seal strength per ASTM F88 increases steadily once the seal initiation temperature is exceeded. The lower and sharper melting endotherm measured by differential scanning calorimetry per ASTM D3418 produces a controlled sealing window; the absence of high-melting fractions reduces the risk of unsealed spots through powdered product on vertical form-fill-seal lines. At 25 µm gauge, haze values below 5% and gloss values above 60 are typical for this density class; published film-property data for the specific grade may vary with die configuration and film gauge.

    When 7118LE replaces Ziegler-Natta C4-LLDPE in multilayer blown film structures

    The substitution is not fully drop-in without process adjustments. In a 7-layer blown film line with a 400 mm annular die and 2.0 mm die gap, haul-off tension may need to be reduced by 10–15% because the metallocene-grade film retains more orientation at the frost line and can exhibit bubble instability when tension is too high. Feed-section temperatures are sometimes lowered by 5–10 °C to avoid premature pellet sticking on the grooved feed bushing. The comparative difference between 7118LE and a conventional C4-LLDPE lies in the molecular weight distribution and comonomer distribution. Ziegler-Natta products contain a broader distribution of chains, including high-melting fractions that contribute to seal initiation and haze, whereas 7118LE contains less of these fractions. The result is improved dart impact per ASTM D1709A, improved optical properties per ASTM D1003 and ASTM D2457, and lower seal initiation per ASTM F1921. However, machine-direction Elmendorf tear per ASTM D1922 can be lower than some C6-LLDPE grades, and this must be managed through blow-up ratio and gauge distribution.

    Food-contact compliance is covered by the resin manufacturer under FDA 21 CFR 177.1520 for olefin polymers, and the grade may be evaluated according to European Union Regulation (EU) No 10/2011 for plastic materials intended for food contact. The limits of use are defined by the manufacturing certificate for each production lot. In industrial practice, 7118LE is not recommended as the outer layer for applications requiring high coefficient of friction control without external slip or antiblock masterbatch. The resin has limited resistance to highly aromatic solvents and strong oxidising acids, consistent with polyolefin chemistry; prolonged contact with these media causes softening, swelling, or oxidative embrittlement. Processing above 250 °C is not recommended because thermal-oxidative degradation may generate gel particles and low-molecular-weight extractables. Where regrind is permitted by end-use specifications, addition is usually limited to 20% by weight to maintain optical and seal consistency; published data for high-regrind configurations in this specific grade is limited.

    High-speed form-fill-seal sealant performance boundaries

    On high-speed vertical form-fill-seal lines, the sealant layer is exposed to short dwell times of 0.2–0.5 s and jaw pressures of 20–40 N/cm². Under these conditions, 7118LE benefits from low seal initiation temperature and a narrow melting range; hot tack is maintained when the sealing interface is contaminated with fine product dust because the polymer can flow and fuse at lower temperatures. However, at line speeds above 80 cycles/min, the seal window may become too narrow for packaging machines with large temperature overshoot. The sealing layer thickness should be verified at the minimum dwell time for the specific filling operation using ASTM F88 for seal strength and ASTM F1921 for hot tack. The grade may be coextruded with polyamide or EVOH; tie layers are not required for direct adhesion to these materials in many structures, but adhesion values depend on oxidation level and die gap. Published data for this specific configuration is limited.

    Extrusion lamination and coating are boundary operations for 7118LE. The resin has lower melt strength than LDPE and is not recommended as the sole coating layer on high-speed extrusion lamination lines where neck-in and draw resonance are controlling defects. If 7118LE is used as a coextruded sealant skin in a coating structure, the coating weight should be at least 15 g/m² and the air gap should be minimised within the limits of the coating line to reduce oxidative degradation and edge instability. The grade's advantage in these structures is limited to the sealant interface; structural layers should be selected from LDPE, PP, or tie-resin grades with adequate melt strength. Published grade-specific data for high-speed coating conditions is limited.

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