| HS Code | 212170 |
| Density Astm D1505 | 0.918 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg Astm D1238 | 18 g/10 min |
| Melt Flow Rate 190 C 21 6 Kg Astm D1238 | 180 g/10 min |
| Tensile Stress At Yield Iso 527 | 10 MPa |
| Tensile Stress At Break Iso 527 | 9 MPa |
| Tensile Strain At Break Iso 527 | 150 % |
| Flexural Modulus Iso 178 | 250 MPa |
| Izod Impact Strength Notched At 23 C Astm D256 | 20 kJ/m² |
| Vicat Softening Temperature Iso 306 A50 | 85 °C |
| Melting Point Dsc | 120 °C |
| Shore D Hardness Astm D2240 | 50 |
| Escr 10 Igepal Astm D1693 F0 | >1000 h |
As an accredited SABIC LLDPE 6118LE factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SABIC LLDPE 6118LE is supplied in 25 kg polyethylene bags, palletized and shrink-wrapped for safe handling and moisture protection. |
| Container Loading (20′ FCL) | 20′ FCL container loading of SABIC LLDPE 6118LE: 25-kg bags palletized, secured, export-ready for safe transport. |
| Shipping | SABIC LLDPE 6118LE is shipped as free-flowing pellets in 25 kg bags, shrink-wrapped pallets, or bulk containers. It is not classified as dangerous goods for transport. Keep dry, avoid direct sunlight and heat, and protect bags from damage during handling to preserve product quality. |
| Storage | Store SABIC LLDPE 6118LE in a clean, dry, well-ventilated area, away from direct sunlight, heat sources, and open flames. Keep in original sealed bags or containers to prevent moisture pickup and contamination. Avoid contact with oxidizing agents. Maintain moderate temperatures and protect packaging from physical damage. Rotate stock to ensure first-in, first-out usage. |
| Shelf Life | Shelf life is indefinite when stored in original packaging, protected from heat, moisture, and UV exposure. |
SABIC LLDPE 6118LE is a linear low-density polyethylene grade with a melt flow rate of 1.0 g/10 min at 190 °C/2.16 kg determined under ISO 1133-1:2022 and a nominal density of 0.918 g/cm³ measured under ISO 1183-1:2019. The grade is specified for blown film conversion where drawdown, dart impact retention, and seal integrity control downstream yield. The following profiles cover five verified application segments: frozen-food packaging film, agricultural silage and greenhouse covers, adhesive-laminated sealant webs, heavy-duty industrial liners, and e-commerce mailer films. Injection molding, blow molding, rotomolding, and pipe extrusion are outside the specified conversion window for this resin.
In frozen-food film conversion, SABIC LLDPE 6118LE is processed on grooved-feed barrier extruders with screw diameters of 45–75 mm and L/D ratios of 30:1; the melt temperature measured at the adaptor is controlled to 190–205 °C because higher thermal exposure accelerates gel formation and impairs optical homogeneity. Die gaps of 1.8–2.4 mm are retained across the circumference, and the bubble is stabilized in a high-stalk configuration with frost-line height between 6 and 8 die diameters. Blow-up ratio is maintained at 2.0:1–3.0:1, while layflat widths above 1,600 mm require internal bubble cooling to sustain outputs above 0.55 kg/h per cm die circumference. The formulation for frozen vegetable and bakery films uses 70–80 wt% 6118LE and 20–30 wt% high-pressure LDPE to raise melt extensibility; slip masterbatch addition is 0.5–1.5 wt% when film-to-film coefficient of friction must remain below 0.30, and synthetic silica anti-block is dosed at 0.1–0.4 wt% for roll windability. Downstream converting includes surface corona treatment at 38–42 mN/m and center-fold heat sealing at jaw set temperatures of 105–130 °C. Terminal products include frozen vegetable pouches, ice-cube bags, bakery over-wrap, and dry-food liners. Compliance for direct food contact under Regulation (EU) No 10/2011 requires overall migration not exceeding 10 mg/dm², while FDA 21 CFR 177.1520 classifies the olefin polymer by extractable fraction under the intended condition of use. Operational boundaries include avoiding melt temperatures above 250 °C and limiting residence time to less than 15 min at 200 °C; if resin granules are stored above 60% relative humidity, hopper drying at 70 °C for 4 h prevents moisture-generated pinholes. Die-lip buildup is managed by maintaining die temperature uniformity within ±3 °C.
| Standard/regulation | Clause | Requirement |
|---|---|---|
| Regulation (EU) No 10/2011 | Article 12, Annex I | Overall migration limit 10 mg/dm²; specific migration limits for listed monomers and additives |
| FDA 21 CFR 177.1520 | Section (c) and (d) | Olefin polymer compliance by extractable fraction or end-test depending on condition of use |
| EC No 2023/2006 | Annex, GMP requirements | Traceability, contamination control, and batch documentation |
| EN 1186-2 | Total immersion test | Overall migration testing for films; simulant selection based on food type |
Silage cover formulations based on 6118LE require UV stabilization against long-term solar exposure because the base resin does not contain a sufficient hindered-amine light stabilizer package for multi-year agricultural service. The polymer phase is kept at 90–100 wt% 6118LE, with up to 10 wt% metallocene LLDPE or LDPE for tack adjustment in clamp applications; HALS active dosage is 0.25–0.60 wt% in the finished film, supplied as a 10% UV masterbatch at 2.5–6.0 wt%. White or black pigment masterbatch is incorporated at 6–12 wt% to block transmission below 400 nm, and anti-drip agents are dosed at 0.5–1.0 wt% for greenhouse side sheets. Processing uses low-stalk blown film lines with die gaps of 2.0–2.6 mm, blow-up ratios of 2.5:1–3.5:1, and final thickness between 120 and 200 µm for silage clamp covers. Frost-line height is lowered to 3–5 die diameters to reduce film haze; output rates are limited by bubble cooling capacity because thick gauges above 150 µm retain heat at the nip. Terminal products include silage clamp side sheets, greenhouse anti-drip films, and low-tunnel perforated covers. Compliance for silage films references EN 13207:2018 for elongation retention after weathering and EN 13206:2017 for greenhouse covering films; pesticide contact with sulphur-containing agrochemicals can consume phenolic antioxidants, so end-use exposure trials are required before multi-season warranty claims. Operational boundary: direct contact with chlorinated water or fumigant vapours containing methyl bromide is not recommended; published data for this specific grade under those exposure conditions is limited.
A sealant web produced from 6118LE is deposited as a blown film at 25–40 µm and subsequently adhesive-laminated to PET or BOPP at a solvent-free adhesive coat weight of 2–4 g/m². The polymer fraction of the sealant layer contains 80–95 wt% 6118LE and 5–20 wt% metallocene plastomer to depress seal initiation to 80–95 °C; anti-block of 0.1–0.3 wt% is added only when the film is wound under high-humidity roll storage. The blown film process uses die gaps of 1.6–2.0 mm, BUR of 2.0:1–2.5:1, and melt temperatures of 180–200 °C to limit low-molecular-weight extractables. Lamination curing is conducted at 35–40 °C for 24–48 h, after which the sealant web is slit and pouch-making is performed at 40–60 cycles/min on vertical form-fill-seal lines. Terminal product types include dry-food stand-up pouches, snack pillow pouches, and non-food detergent refill packs where seal integrity under drop tests is specified. Compliance under Regulation (EU) No 10/2011 applies when the adhesive is separated from food by the sealant web; migration testing is carried out on the finished laminate using EN 1186-2 total immersion or cell methods. The operational limit of 6118LE in this structure is its melt flow rate of 1.0 g/10 min: if direct extrusion coating is attempted without a high-MFR LDPE coextrudate, die pressure becomes unstable above 150 m/min line speed and pinholing occurs. Published data for solvent-free lamination pot life with this specific sealant film is limited; adhesive viscosity doubling times should be verified against the adhesive manufacturer’s batch data.
| Application segment | Die gap | Blow-up ratio | Melt temperature | Frost-line height |
|---|---|---|---|---|
| Frozen-food film | 1.8–2.4 mm | 2.0:1–3.0:1 | 190–205 °C | 6–8 die diameters |
| Silage and greenhouse cover | 2.0–2.6 mm | 2.5:1–3.5:1 | 180–200 °C | 3–5 die diameters |
| Adhesive-laminated sealant web | 1.6–2.0 mm | 2.0:1–2.5:1 | 180–200 °C | 5–7 die diameters |
| Heavy-duty industrial liner | 2.0–2.4 mm | 1.8:1–2.5:1 | 190–210 °C | 5–8 die diameters |
| E-commerce mailer film | 1.6–2.0 mm | 2.0:1–2.8:1 | 180–200 °C | 5–7 die diameters |
Where drum liners and FIBC inner plies are extruded from 6118LE, the resin is blended with high-density polyethylene to control creep and film stiffness at cargo temperatures above 40 °C. The recommended polyolefin fraction is 60–75 wt% 6118LE and 25–40 wt% HDPE; a fluoroelastomer processing aid at 0–400 ppm is used only after melt fracture occurs at screw speeds exceeding 80 rpm, and carbon black masterbatch is added at 2–4 wt% if UV resistance is needed for outdoor storage. Film extrusion takes place on 65–90 mm grooved-feed lines with die gaps of 2.0–2.4 mm, BUR of 1.8:1–2.5:1, and melt temperatures of 190–210 °C. Frost-line height is fixed at 5–8 die diameters, and internal bubble cooling is used above 120 µm gauge to maintain dart impact targets of ≥ 800 g at 100 µm under ISO 7765-1/ASTM D1709; converter trials report that HDPE addition beyond 40 wt% reduces dart impact rapidly and should be avoided for cold-climate stacking. Terminal products include FIBC inner liners for hygroscopic chemical powders, drum liners for non-oxidizing liquids, and heavy-gauge box liners. Compliance for FIBC packaging under ISO 21898:2004 is package-level, not resin-level; UN dangerous goods certification requires testing of the complete bag and liner. The liner is not suitable for direct contact with strong oxidizing agents above 50 °C or with aromatic hydrocarbon fills above 40 °C; published data for this specific configuration is limited, and fill compatibility tests must be conducted before shipment.
The addition of recycled LLDPE to 6118LE in e-commerce mailer film is controlled at 15–30 wt% to retain puncture propagation resistance; the prime 6118LE fraction is 70–85 wt%, and black or coloured masterbatch is dosed at 2–6 wt%. Three-layer coextrusion is used rather than monolayer to place recycled content in the core layer and maintain outer-surface ink adhesion. Die gaps are 1.6–2.0 mm; blow-up ratios are held at 2.0:1–2.8:1; film thickness is 60–100 µm after layflat winding. Corona treatment at 36–40 mN/m is applied to the print face, and flexographic or water-based ink adhesion is tested with tape pull under ISO 2409 or equivalent cross-cut method; delamination is not acceptable beyond 5% of the cut area. Converting includes side-gusset or bottom-seal pouch formation and self-seal adhesive strip application, with seal bar temperatures of 110–135 °C. Terminal products include non-food e-commerce mailers, apparel shipping bags, and protective over-pack for books. Compliance under Directive 94/62/EC requires the sum of lead, cadmium, mercury, and hexavalent chromium not to exceed 100 mg/kg in packaging; REACH candidate list screening is required when post-consumer recyclate is used. Operational limits: batch-to-batch gel counts increase with recycled content above 30 wt%; a melt screen with aperture of 80–120 µm is required upstream of the die. This film is not intended for food contact because post-consumer recyclate is not food-grade, and no statement of food-contact compliance should be made.
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SABIC LLDPE 6118LE is a pelletized linear low-density polyethylene copolymer supplied primarily for blown film extrusion. The nominal density is 0.918 g/cm³ when measured in accordance with ISO 1183-1, and the nominal melt mass-flow rate is 1.0 g/10 min at 190°C/2.16 kg when measured in accordance with ISO 1133-1:2022. The grade is classified as a fractional-melt-index LLDPE for film thicknesses from 20 µm to 80 µm. It is supplied as a stabilized pellet; the exact additive package, including slip and antiblock loadings, is defined in the product specification and certificate of analysis rather than in generic technical literature.
For preliminary grade selection, the following coordinate values are used as typical values, not release specifications.
| Property | Test method | Typical value |
|---|---|---|
| Density | ISO 1183-1 | 0.918 g/cm³ |
| Melt mass-flow rate, 190°C/2.16 kg | ISO 1133-1:2022 | 1.0 g/10 min |
| Melting temperature, DSC second heat | ISO 11357-3 | 121–123°C |
| Vicat softening temperature, A50 | ISO 306 | 94–96°C |
Blown film lines processing 6118LE commonly use single-screw extruders with grooved-feed sections, screw diameters of 45–75 mm, and length-to-diameter ratios between 24:1 and 30:1. Barrel temperatures are set from 170°C to 210°C, with adapter and die zones maintained at 190–225°C. A die gap of 1.5–2.5 mm and a blow-up ratio of 2.0:1–3.0:1 are standard start-up settings for film gauges from 25 µm to 50 µm. Because the melt flow index is 1.0 g/10 min, head pressure increases more rapidly than with higher-flow LLDPE grades. Barrier screws with dispersive mixing sections are therefore preferred to limit melt-temperature overshoot to below 230°C. Head pressures above 350–400 bar are not recommended because shear heating can initiate localized gel formation and generate off-odour in the melt film. The resin does not normally require pre-drying when stored in sealed hoppers below 60% relative humidity. Condensation on cold pellets entering the feed throat is a common source of bubble instability and surface haze, particularly during humid plant conditions.
On production-scale blown film lines, the most frequent processing defect observed with fractional-melt-index LLDPE of this density range is unstable neck height and layflat width variation caused by incorrect internal bubble cooling air volume. The condition can appear as a repetitive 2–5% deviation in layflat width and is corrected by adjusting cooling air volume rather than melt temperature. Melt fracture may occur when the die gap is below 1.2 mm and the melt temperature is below 180°C. Raising the die temperature to 210–220°C and maintaining a die gap of 1.5–2.0 mm typically reduces the defect. Screen packs with mesh sizes from 100 µm to 250 µm are used to protect the die and build backpressure for mixing; screen plugging rates increase when the resin is blended with high-slip masterbatch. An inline screen pressure monitor is required to signal change-outs before gel tears appear in the film.
The technical function of 6118LE arises from the combination of 0.918 g/cm³ density and 1.0 g/10 min melt mass-flow rate. This positions the grade for moderate stiffness and toughness without the excessive melt pressure of lower-flow resins. Density contributes to water-vapour transmission rate values typical of linear low-density film measured by ASTM F1249; oxygen permeability is measured by ASTM D3985. Film stiffness is determined by secant modulus according to ISO 527-3. End-use film performance is controlled by dart impact resistance under ASTM D1709 and propagation tear resistance under ASTM D1922. The grade is used in unoriented heavy-duty liners, carrier bags, industrial wraps, agricultural film, and lamination base webs. In applications where seal-through-contamination and hot tack are controlling requirements, a metallocene-catalyzed LLDPE or a hot-tack-modified blend is usually more suitable; hot tack is tested by ASTM F1921 and seal strength by ASTM F88.
Regulatory status rests on the olefin-polymer base, which falls under FDA 21 CFR 177.1520 and EU Regulation No 10/2011 when the finished article satisfies the relevant overall migration and specific migration limits. The grade is not delivered as a medical-grade material; ISO 10993 biocompatibility is not implied. Electrical and electronics applications must be evaluated under RoHS Directive 2011/65/EU; REACH obligations under Regulation (EC) No 1907/2006 remain with the article producer. The resin should not be blended with reprocessed material containing barrier-layer polyamide or EVOH residues unless compatibilization and dispersion are engineered into the reclaim stream. Extended melt exposure above 280°C causes oxidative chain scission, gel counts, and odour. Purge with a subsequent fractional-melt-index LLDPE or LDPE is recommended after shutdown.
| Domain | Reference | Scope |
|---|---|---|
| Food contact, United States | FDA 21 CFR 177.1520 | Olefin polymers for food packaging |
| Food contact, European Union | EU No 10/2011 | Overall migration and specific migration limits |
| Dart impact resistance | ASTM D1709 | Falling dart impact of film |
| Elmendorf tear resistance | ASTM D1922 | Propagation tear resistance |
| Haze | ASTM D1003 | Optical clarity of film |
| Gloss | ASTM D2457 | Specular gloss at 60° |
Substitution is not direct one-to-one replacement. A conventional butene-comonomer LLDPE with 0.918 g/cm³ density and 1.0 g/10 min melt index typically shows lower dart impact resistance and lower machine-direction tear than a hexene-LLDPE of equivalent density and melt flow, with differences quantified using ASTM D1709 and ASTM D1922. Optical haze measured by ASTM D1003 may be higher than metallocene grades at the same 25 µm gauge. However, 6118LE can provide more stable bubble formation at high blow-up ratios because the lower melt flow increases melt strength, and it may permit downgauging in lower-abuse packaging. When replacing another grade, the same die gap and temperature profile should be retained first, and only backpressure and takeoff speed adjusted. Published data for this specific substitution configuration is limited; a plant trial at 2.5:1 blow-up ratio and 25–40 µm gauge is the only reliable method for validation.
In blown film coextrusion used for food pouches, 6118LE frequently serves as a core layer in a three-layer A/B/C structure. Skin layers may be metallocene LLDPE for seal initiation and low extractables, or LDPE for optics. The core layer gauge fraction can be 40–60% of a total 50–70 µm structure. Layer thickness is monitored using beta gauges and should be maintained within ±3% of target; excessive core-layer variation affects seal strength consistency under ASTM F88. Slip migration from the skins into the core, or from core to skins, can alter the coefficient of friction measured by ISO 8295. If a high-slip masterbatch is added to the core, fogging and plate-out can develop on the collapsing frame. Converters seeking low coefficient of friction without visible plate-out should evaluate migrating slip systems in the skin layers only. Process data from die lip to winder must be trended to maintain web tension; abrupt tension changes can introduce gauge bands that are not visible until the roll is unwound.
The choice of screw geometry directly affects the conversion of 1.0 g/10 min LLDPE. Barrier screws with compression ratios from 2.5:1 to 3.5:1 and a Maddock-style mixing section provide sufficient shear to homogenize the melt and disperse additives, but the design can generate excessive shear heating if backpressure exceeds 350–400 bar. Melt temperature should be measured at the die entry with an immersion probe; the difference between barrel setpoint and actual melt temperature is commonly 5–15°C under normal shearing. On high-output lines, grooved-feed extruders operating at 150–250 kg/h require cooling on the feed zone to prevent premature pellet compression. Failure to control feed-zone temperature can create torque spikes and reduce output stability. The resin is not suited to adiabatic screw designs intended for high-speed polypropylene film extrusion because the LLDPE melting curve and melt-viscosity profile differ.
For converters running cast film lines, process limits differ from blown film. Cast film processing can use melt temperatures from 200°C to 240°C, but the risk of surface oxidation increases above 250°C. Chill-roll temperatures are typically maintained at 15–25°C to control crystallinity and film blocking. In cast film, 6118LE should be compared with higher-flow LLDPE grades below 0.918 g/cm³ density when driven by throughput requirements. Where draw resonance is observed, increasing the melt temperature within the stated range or reducing the air gap can improve melt-curtain stability.