| HS Code | 714926 |
| Density | 0.918 g/cm³ |
| Melt Flow Rate | 1.0 g/10 min (190 °C, 2.16 kg) |
| Melting Point | 122 °C |
| Vicat Softening Point | 100 °C |
| Tensile Strength At Yield | 11 MPa |
| Tensile Strength At Break | 40 MPa |
| Elongation At Break | 500% |
| Flexural Modulus | 290 MPa |
| Hardness Shore D | 55 |
| Dart Drop Impact F50 | 130 g (25 µm film) |
| Haze | 12% (25 µm film) |
| Gloss 45 Deg | 45 (25 µm film) |
As an accredited SABIC LLDPE 118L factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SABIC LLDPE 118L is supplied as free-flowing pellets in 25 kg polyethylene bags, with 40 bags (1000 kg) per pallet. |
| Container Loading (20′ FCL) | SABIC LLDPE 118L packed in bags, palletized and loaded into a 20-foot full container load for safe transport. |
| Shipping | SABIC LLDPE 118L is a free-flowing linear low-density polyethylene resin supplied in 25 kg bags or octabins, palletized and stretch-wrapped. It ships in dry, ventilated containers or bulk trucks. Keep away from direct heat, moisture, and sunlight. This material is non-hazardous under normal transport regulations. |
| Storage | Store SABIC LLDPE 118L in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep in original sealed packaging to prevent moisture, dust, and contamination. Avoid prolonged UV exposure. No special storage conditions required, but maintain moderate temperatures and protect bags from damage. |
| Shelf Life | Shelf life is two years from delivery when stored in original, unopened packaging, in cool, dry conditions away from direct sunlight. |
SABIC LLDPE 118L is a butene-based linear low-density polyethylene with an ISO 1133-1:2022 melt mass-flow rate of 1.0 g/10 min at 190 °C/2.16 kg and an ISO 1183-1:2019 density of 918 kg/m³.
For heavy-duty industrial liner production, the resin is dry-blended with a high-pressure LDPE of 0.3–0.7 g/10 min melt mass-flow rate at 15–25 wt% to moderate melt extensibility and stabilize the bubble against gauge banding on oscillating haul-off assemblies. A typical starting recipe for 150–200 µm shipping sacks contains 78 wt% SABIC LLDPE 118L, 20 wt% LDPE, and 2 wt% white or carbon black masterbatch. Processing is carried out on a single-screw extruder with a 30:1 L/D ratio, a barrier screw fitted with a Maddock mixing section, and a 60/100/60 mesh screen pack. Barrel temperature zones from feed to metering are 170–185 °C, 190–205 °C, and 205–215 °C, with the adaptor and die maintained at 210–220 °C. A die gap of 1.8–2.5 mm is used with a blow-up ratio of 2.5:1–3.2:1 and a frost line height of 5–8 die diameters. Melt fracture onset is monitored visually as line speed increases; the exact threshold varies with die geometry and melt temperature, and published data for this specific configuration is limited. Because the resin is non-hygroscopic, pre-drying is not required unless pellets have been stored under high-condensation conditions; surface condensation can be cleared with a 60 °C hopper dryer for 30 min.
Finished film is slit into tube or sheet form and converted into valve sacks, open-mouth liners, and 25 kg drum liners. Mechanical acceptance testing is performed according to ASTM D1709-22 for dart drop impact, ASTM D1922-09(2019) for Elmendorf tear, and ISO 527-3:2018 for tensile properties. When used as FIBC liners, the film is evaluated against the end-user certificate for ISO 21898:2004 or equivalent packing group requirements; the 118L fraction contributes low-temperature puncture resistance but does not alone ensure the sift-proofness of the outer woven fabric. Seal failure in 35–50 µm edge fold areas is the dominant rejection mode on continuous bag converters, so weld seam strength must be verified on the converting line.
In three-layer greenhouse film coextrusion, SABIC LLDPE 118L is assigned to the central layer at 65–75 wt% of total formulation, with 15–25 wt% high-pressure LDPE and 5–10 wt% EVA containing 14–18% vinyl acetate. The EVA fraction improves the machine-direction tear balance and permits a more uniform surface distribution of anti-drip additives in the inner skin. UV durability is achieved with a hindered amine light stabilizer at 0.4–0.8 wt%, a benzophenone or hydroxyphenyl-triazine UV absorber at 0.2–0.4 wt%, and a phosphite/hindered phenol thermal stabilizer package at 0.15–0.25 wt%. Anti-drip agents based on polyglycerol esters are dosed at 1.0–1.5 wt% in the inside layer; infrared-retention fillers are added only where the cultivation programme specifies reduced night-time heat loss, and the resulting PAR transmission is verified by ISO 13468-1:2019 while haze is measured by ASTM D1003-21.
Extrusion uses a three-layer blown film die of 200–350 mm diameter, a blow-up ratio of 2.2:1–2.8:1, and internal bubble cooling with a layflat width tolerance of ±3%. Melt temperatures in the 118L-rich core are maintained at 195–215 °C; die temperatures above 220 °C can deactivate certain UV stabilizer systems and should be avoided unless the stabilizer supplier confirms volatility limits. Films exposed to sulfur fumigation or halogenated crop protection products require a chemical resistance check; the active stabilizer package must be selected for acidic decomposition products because not all HALS types retain performance in elemental sulfur-rich greenhouse atmospheres. Finished greenhouse film is tested under EN 13206:2017 and accelerated weathering per ISO 4892-2:2013. End products include three-season tunnel covers, low tunnels, and side-roll greenhouse curtains.
In vertical form-fill-seal lines for frozen food, a three-layer A/B/C film uses SABIC LLDPE 118L in the sealant layer at 30–40% of a 60–80 µm total structure. The sealant layer is blended with 10–20 wt% of a metallocene plastomer or very-low-density polyethylene with a density of 0.902 g/cm³ to lower seal initiation temperature to 85–95 °C while retaining low-temperature ductility. The outer layers are formulated with 20–30 wt% 118L and 70–80 wt% LDPE or HDPE depending on stiffness, printability, and coefficient of friction requirements. Extrusion is carried out on a 55–75 mm three-layer blown film line with 24:1–30:1 L/D screws, a die gap of 1.5–2.2 mm, a blow-up ratio of 2.0:1–2.8:1, and melt temperatures of 190–210 °C. The print skin is corona-treated to 38–42 mN/m according to ASTM D2578-17; the sealant side remains untreated to avoid blocking and to preserve seal strength. Puncture resistance at freezer temperatures is measured by ASTM D3420-21 at −18 °C, and tensile properties by ISO 527-3:2018.
Seal performance is evaluated on a laboratory heat sealer with 0.5 N/mm² jaw pressure, 0.5 s dwell, and a 5 mm flat jaw; hot-tack testing follows ASTM F1921-20. The butene-based linear fraction provides a seal plateau between 95 °C and 125 °C; above 130 °C the seal interface may shift into viscous flow, so faster form-fill-seal lines should lower jaw temperature rather than increase dwell to avoid edge thinning. Food contact compliance is not a resin-only property: the converter must review the SABIC product stewardship statement, the anti-fog or slip masterbatch, and the final structure under Regulation (EU) No 10/2011 and 21 CFR 177.1520 for olefin polymers. End products include frozen vegetable pouches, seafood bags, and ice-cream pillow packs.
| Application Sector | Governing Standards or Regulations | Critical Test Designations | Typical Thickness |
|---|---|---|---|
| Heavy-duty liners and shipping sacks | ISO 21898:2004, ASTM D1709-22, ASTM D1922-09(2019) | ISO 527-3:2018 | 150–200 µm |
| Greenhouse covers | EN 13206:2017, ISO 4892-2:2013 | ISO 13468-1:2019, ASTM D1003-21 | 150–200 µm |
| Frozen food sealant webs | Regulation (EU) No 10/2011, 21 CFR 177.1520 | ASTM F1921-20, ASTM D3420-21 | 60–80 µm |
| Below-slab vapour retarders | ASTM E1745-17, ASTM D4397-16 | ASTM D882-18, ASTM E96/E96M-22 | 150–300 µm |
| Collation shrink film | ASTM D2732-20 | ASTM D1922-09(2019), ASTM D1003-21 | 40–80 µm |
| Refuse sacks and bin liners | EN 13592:2017 | ASTM D1709-22, ASTM D1922-09(2019) | 40–120 µm |
For below-slab vapour control, the governing specification is ASTM E1745-17. Formulations for 150–300 µm film include 85–95 wt% SABIC LLDPE 118L, 5–15 wt% reprocessed polyethylene film of known density and melt index, and 2–3 wt% carbon black masterbatch for UV shielding during storage and installation. Blown film extrusion uses a 90–120 mm die, internal bubble cooling, and a segmented air ring with automatic gauge control; flat width is typically 1.5–3.0 m, with layflat variation held at ±4% or better. Barrel and die temperatures are set to achieve a melt temperature of 190–210 °C, and the die gap is 1.8–2.5 mm. Winding is performed on 76 mm cores with taper tension to prevent blocking and telescoping in 50–100 m roll lengths.
Class A, B, and C vapour retarder performance under ASTM E1745-17 is verified through tensile strength per ASTM D882-18, puncture resistance per ASTM D1709-22, and water vapor permeance per ASTM E96/E96M-22. A Class A retarder under this standard is specified at 0.1 perm or less; because 118L is a butene-based LLDPE, the verified permeance depends on thickness, draw-down ratio, and the quality of the recycled fraction. Sealing, overlap, and installation details follow ASTM D4397-16 for polyethylene sheeting. Operational boundary: the film is not a chemical-resistant membrane; contact with hydrocarbon-based form-release agents, solvents, or aggressive ground gases requires a barrier layer evaluation outside the scope of standard polyethylene sheeting. End products include under-slab vapour retarder, crawl-space ground cover, and temporary building enclosure film.
When double-bubble collation shrink lines process SABIC LLDPE 118L, the formulation incorporates 20–40 wt% 118L into an LDPE-rich structure to raise Elmendorf tear and maintain shrink-force consistency. The primary tube is extruded at 190–205 °C through a 50–70 mm extruder with a 24:1–30:1 L/D and a die gap of 1.2–1.8 mm; the tube is quenched below 35 °C, reheated to 105–115 °C, and stretched in the machine direction 3.5:1–5.0:1 and transverse direction 3.0:1–4.5:1 in a double-bubble tower. Web handling requires air turners and adjustable spreader bars to avoid edge fold-over. The orientation window narrows when the 118L fraction exceeds 40 wt% because the linear butene chains increase melt elasticity; melt fracture appears as a regular chevron pattern on the second bubble and is managed by lowering draw rate or raising reheat zone temperature by 2–5 °C. Shrink measurements are performed after 120 °C immersion according to ASTM D2732-20; tear is measured per ASTM D1922-09(2019); haze is measured per ASTM D1003-21.
The addition of 118L alters the transverse direction shrink-force balance, so the air ring and secondary bubble blower settings are trimmed to maintain an MD/TD shrink ratio acceptable for the bottle pack geometry. At 30 wt% 118L, the film typically retains sufficient optical clarity for printed multipack sleeves; above 35 wt%, haze may rise and require evaluation under ASTM D1003-21. Food contact structures are assessed under Regulation (EU) No 10/2011 and 21 CFR 177.1520 with the final additive package. End products include 6×1.5 L water bottle collation packs, canned food tray overwrap, and carbonated soft drink multipacks. Operational limit: at 118L fractions above 40 wt%, transverse shrink force decreases and can create register drift on high-speed packaging lines; published data for this specific configuration is limited, so line trials are required.
In refuse sack extrusion with post-consumer recycle, the formulation contains 50–70 wt% SABIC LLDPE 118L, 20–40 wt% recycled polyethylene film scrap, and 0–10 wt% LDPE for bubble support. The recycled fraction is melt-filtered through a continuous screen changer with 120–200 µm aperture screens, because low-melt-index butene LLDPE combined with unpurified PCR can produce pressure excursions and elevated gel counts. Film thickness ranges from 40 µm for lightweight bin liners to 120 µm for wheelie-bin refuse sacks. Extrusion uses a 65–80 mm extruder with a 25:1–30:1 L/D, a die gap of 2.0–2.5 mm, a blow-up ratio of 2.8:1–3.5:1, and a melt temperature of 195–210 °C. Gauge variation is controlled by an internal bubble cooling system; modern lines hold layflat variation to ±5% or better on 800–1200 mm flat widths.
Finished sacks are tested according to EN 13592:2017 for household refuse sacks, with dart drop impact per ASTM D1709-22 and Elmendorf tear per ASTM D1922-09(2019). The 118L fraction maintains low-temperature dart impact for outdoor collection at −20 °C; the recycled fraction shifts rheology unpredictably if it contains degraded LDPE, so each lot is sampled for MFR under ISO 1133-1:2022 before blending. Operational boundary: PCR streams containing paper labels, adhesives, or nylon strapping should be melt-filtered to 80 µm or lower to avoid screen blockage; silicon-based anti-block masterbatch in the reclaimed film can reduce surface tension during corona treatment. End products include 35 L household refuse sacks, 120 L trash bags, and 240 L wheelie-bin liners.
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SABIC LLDPE 118L is a butene-comonomer linear low-density polyethylene resin supplied in pellet form for blown film extrusion. The nominal density is 0.918 g/cm³ when tested according to ISO 1183-1:2019, and the melt mass-flow rate is 1.0 g/10 min at 190 °C under 2.16 kg dead load according to ISO 1133-1:2022. The grade is used in thin-gauge primary packaging, industrial liners, collation shrink films, carrier films, and agricultural stretch-wrap where a converter requires a defined balance between dart impact strength, tear propagation resistance, and bubble stability. The base polymer architecture is an ethylene-butene copolymer with a short-chain branching distribution that yields lower melt elasticity than high-pressure LDPE and a broader molecular weight distribution than a metallocene-catalysed LLDPE of the same density. Compared with SABIC LLDPE 118N and 118W grades, the 118L designation is differentiated primarily by the slip and antiblock additive package rather than by nominal density or melt flow rate; converters must verify the batch certificate for the actual coefficient of friction and blocking force because additive levels are formulation-specific and not defined by grade number alone.
At the molecular level, the resin is a semicrystalline ethylene-butene copolymer with a broad lamellar thickness distribution. Differential scanning calorimetry of butene LLDPE of this density typically records a peak melting temperature between 120 °C and 125 °C at a heating rate of 10 K/min according to ISO 11357-3:2018. The cooling exotherm peak under the same standard lies between 104 °C and 110 °C. These values are matrix-level indicators rather than direct process settings; they influence the minimum heat-seal temperature and the frost line position. Batch-to-batch variance in melt flow rate is normally specified as ±0.1 g/10 min around the nominal value, and density variation is typically controlled within ±0.002 g/cm³. Such shifts may not be visible in routine film production but become relevant when the film is sealed through a narrow temperature window. A positive density drift of 0.002 g/cm³ can reduce dart impact and increase stiffness enough to alter film handling on vertical form-fill-seal machines.
Processors running blown film lines equipped with single-screw extruders of 25:1 to 30:1 L/D ratio generally set the barrel temperature profile from 180 °C at the feed section to 210 °C at the metering section, with adapter and die temperatures between 190 °C and 210 °C. The melt temperature measured at the die lip is commonly held at 200 °C to 220 °C, although the exact setpoint depends on die diameter, output rate, and ambient line cooling. At a melt mass-flow rate of 1.0 g/10 min, the grade has a higher viscosity under shear than a 2.0 g/10 min LLDPE; therefore maximum extruder throughput may be limited by drive motor amperage before melt-pressure limits are reached on high-output lines. Melt-pressure variation at the screen changer should be monitored: a progressive increase exceeding 10 MPa above the start-of-run value with a 150 mesh or finer screen pack indicates gel or additive plate-out accumulation. Because the grade is stabilised for multiple extrusion passes, gel count in film thinner than 30 µm should be measured with an online laser gel counter if the film is destined for high-printability applications.
On high-speed lines running 25 µm to 50 µm film, bubble stability with this density/MFR combination is maintained within a blow-up ratio of 2.0:1 to 3.0:1 and a frost line height of 600 mm to 900 mm when the die gap is set at 1.2 mm to 2.0 mm. A wider die gap increases residence time and may reduce melt fracture, but it also lowers melt orientation and can reduce machine-direction tear resistance. The internal bubble pressure should be adjusted so that the frost line is stable within a vertical band of ±50 mm; oscillation beyond this range is commonly caused by irregular air-ring flow or incompletely melted pellets. For a spiral mandrel die with a 200 mm diameter and 12 feed ports, output uniformity of ±5% in film thickness across the web is an achievable target when the die temperature is held within ±3 °C. Converters using internal bubble cooling can increase throughput by 15% to 25% relative to external air-ring cooling, but the colder internal air also increases the effective melt cooling rate and may lower dart drop impact if frost line height is not reset.
Pre-drying of SABIC LLDPE 118L is not normally required when the pellets are stored in undamaged bags at ambient conditions below 60% RH. If surface moisture is present, a dehumidified hopper dryer at 60 °C for 2 h is applied; temperatures above 80 °C are avoided because pellet surface tack may develop and restrict hopper discharge. Return-air dew point should be held below −20 °C when drying is installed in humid plants.
Seal performance of film produced from SABIC LLDPE 118L is evaluated using heat-seal strength tests conducted according to ASTM F88/F88M-23 after a dwell time of 0.5 s and a sealing pressure of 0.27 MPa. The seal initiation temperature for a 25 µm blown film is typically between 95 °C and 110 °C, although published data for this specific configuration is limited, and the exact value shifts with film density, gauge, and thermal history. Once sealed, the film retains adequate hot-tack strength only when the seal-bar dwell is completed before crystallisation at the seal interface proceeds; interruptions longer than 1.0 s between sealing and cooling can reduce hot-tack performance on form-fill-seal machines running above 60 cycles/min.
After the film is wound, surface slip is measured as the kinetic coefficient of friction according to ISO 8295:1995 or ASTM D1894-24. The slip additive migrates to the film surface at a rate controlled by storage temperature and additive loading; near-room-temperature conditioning for 24 h to 48 h after extrusion may be required before the final coefficient of friction is reached. Storage below 15 °C slows this migration, and film tested immediately after winding can show higher friction than film aged for 7 days at 23 °C. Blocking force, measured according to ASTM D3354-23, is dependent on both the antiblock particle concentration and the film surface topography generated by the die and frost line. Converters must not assume that the coefficient of friction of 118L is identical to that of 118W or 118N; the selection among these grades is based on the target slip and blocking behaviour for the packaging line.
For specification comparison, the minimum test-method set used in converter batch acceptance includes the standards listed below.
| Property | Test method | Typical evaluation condition |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 | 190 °C, 2.16 kg |
| Density | ISO 1183-1:2019 | 23 °C immersion |
| Tensile stress at yield | ISO 527-3:2018 | 500 mm/min, 25 µm film |
| Elongation at break | ISO 527-3:2018 | 500 mm/min, 25 µm film |
| Dart drop impact | ASTM D1709-24 Method A | 25 µm film, F50 |
| Elmendorf tear | ISO 6383-2:1983 | 25 µm film, MD/TD |
| Coefficient of friction | ISO 8295:1995 | 23 °C, 50% RH |
| Blocking force | ASTM D3354-23 | 50 °C, 7 days stacked |
| US food-contact status | 21 CFR 177.1520 | Olefin polymer clearance |
| EU food-contact status | EU 10/2011 | Overall migration limit |
In a direct substitution trial on a vertical form-fill-seal packaging line with a 75 mm wide heat-seal jaw and a dwell time of 0.4 s, the butene-based 118L grade may show lower hot-tack strength and lower dart impact resistance than a metallocene LLDPE of identical density because the metallocene resin possesses a narrower short-chain branching distribution and a higher tie-molecule concentration in the amorphous phase. The practical consequence is a higher incidence of seal failure during product drop-through and a higher puncture failure rate on sharp-edged product geometries. Where film haul-off speed exceeds 40 m/min, the broader molecular weight distribution of 118L can improve bubble stability and reduce melt-pressure fluctuation compared with a typical mLLDPE, but this benefit does not compensate for the lower mechanical abuse resistance. The substitution should therefore be based on a comparison of finite seal strength after 0.5 s and dart drop impact measured to ASTM D1709-24 Method A on 25 µm film, rather than on density and MFR alone.
Where the 118L designation is selected for a low-to-medium slip surface, 118W is used when a higher slip additive loading is required, and 118N is used where a natural, no-slip surface is needed. The differing additive packages do not materially alter the melt flow rate or density, but they affect film friction, print adhesion, and heat-seal strength when slip additive migrates into the seal interface. For lamination or extrusion coating, the absence of such additives in 118N may provide better anchorage; published data for this specific configuration is limited, so adhesion testing according to ASTM F904-22 is required.
Compared with a high-pressure LDPE of 0.918 g/cm³ density and 1.0 g/10 min MFR, SABIC LLDPE 118L exhibits lower melt elasticity and lower melt strength, so bubble neck-in and draw resonance are less stabilised without a 10% to 15% LDPE blend addition. In contrast, when a 1-octene or 1-hexene LLDPE is replaced by 118L, the butene comonomer produces a lower degree of short-chain branching uniformity and therefore lower puncture resistance, lower dart impact, and lower Elmendorf tear resistance at equivalent thickness. These differences are measured under ASTM D5748-24 for puncture, ASTM D1709-24 for dart drop, and ISO 6383-2:1983 for Elmendorf tear. Against a hexene or octene LLDPE of identical density and MFR, 118L generally shows a lower intrinsic dart impact at equivalent blow-up ratio and a lower slow-crack growth resistance, but it retains a lower melt temperature and generally easier processability on older extruders. The differences arise because butene forms shorter branches than hexene or octene, which results in a broader distribution of lamellar thickness and fewer tie chains spanning the amorphous phase.
Because the stabiliser package is designed for blown film extrusion, the material is not recommended for rotomoulding or injection moulding without verification; the long residence times in rotomoulding ovens can deplete stabilisers and promote oxidative embrittlement. Avoid blending with polypropylene above 5 wt% without compatibiliser, because the incompatible boundary layers reduce tear strength and can increase gel-like defects in thin film. Melt temperature above 240 °C is not advised for extended periods because the butene LLDPE backbone can undergo chain scission and form volatile oxidation products detectable as odour in downstream packaging. When regrind is reintroduced, the addition rate should not exceed 20% unless the converter has validated gas chromatographic odour panels and film gel counts on the actual line configuration.