| HS Code | 429693 |
| Material Type | Linear Low Density Polyethylene (LLDPE) |
| Comonomer | Butene-1 |
| Density | 0.925 g/cm³ |
| Melt Flow Rate 190c 2 16kg | 8 g/10 min |
| Melting Point | 124 °C |
| Vicat Softening Point | 95 °C |
| Tensile Stress At Yield | 13 MPa |
| Elongation At Break | >100 % |
| Tensile Modulus | 350 MPa |
| Flexural Modulus | 350 MPa |
| Shore D Hardness | 55 |
| Charpy Notched Impact 23c | 30 kJ/m² |
| Brittleness Temperature | -70 °C |
As an accredited INEOS LLDPE LL6808AA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | INEOS LLDPE LL6808AA is supplied as free-flowing pellets in 25 kg polyethylene bags, palletized and stretch-wrapped. |
| Container Loading (20′ FCL) | 20′ FCL loaded with INEOS LLDPE LL6808AA resin in 25kg bags, palletized, secured for safe transit. |
| Shipping | INEOS LLDPE LL6808AA is shipped as non-hazardous plastic granules in lined woven bags, bulk bags, or hopper trucks. Product should be kept dry, protected from direct sunlight, and stored below 50°C. Avoid dust accumulation and static ignition sources during handling and transport. |
| Storage | Store INEOS LLDPE LL6808AA in a cool, dry, well-ventilated area, away from direct sunlight, heat, and open flames. Keep containers tightly sealed to prevent moisture contamination. Avoid exposure to strong oxidizing agents. Maintain stable temperatures below 50°C, and follow good housekeeping practices to prevent dust accumulation and static discharge. |
| Shelf Life | Store in original, unopened packaging in a cool, dry place; shelf life is typically two years from date of manufacture. |
On a three-layer blown film line with a 350 mm die diameter, 2.0 mm die gap, and internal bubble cooling, INEOS LLDPE LL6808AA is directed to the core and outer layers of 80–120 µm form-fill-seal sack structures. The grade is specified within the 0.916–0.920 g/cm³ density range per ASTM D1505-18 and the 0.7–1.0 g/10 min melt flow rate range per ASTM D1238-20 at 190°C/2.16 kg, positioning it for high-toughness blown film rather than low-viscosity cast processes. A dry blend of 80 wt% LL6808AA, 20 wt% LDPE with a melt index of 0.3 g/10 min, and 3–5 wt% silica-based antiblock masterbatch is metered at the hopper. Barrel temperature zones are set at 180/185/190/195/200°C, die zones at 205°C, and melt temperature is maintained between 190°C and 215°C. Blow-up ratio is constrained to 2.0:1–2.8:1; operation at 2.8:1 without internal bubble cooling leads to frost line oscillation when frost line height drops below 600 mm. Dart drop impact is checked according to ASTM D1709-16a, with heavy-duty sack purchasers commonly setting minimum values of 600–900 g for 100–125 µm film depending on fill mass and drop cycle. Machine-direction tear resistance is evaluated per ASTM D1922-15, and puncture resistance is tested using a 1.5 mm hemispherical probe at 250 mm/min because no single universal ASTM puncture standard applies uniformly across all industrial sack formats. Output on a 90 mm grooved-feed extruder with an L/D of 30:1 is typically 320–380 kg/h at screw speeds of 100–120 rpm, with melt pressure between 300 bar and 420 bar; the throughput ceiling is set by bubble stability rather than plastication capacity. Gel count control is carried out by inline optical camera systems, with acceptable levels often specified as fewer than 10 particles larger than 200 µm per 1 m² for high-value petrochemical and fertilizer sacks. The end product is a filled and stacked sack used in resin pellet, fertilizer, and mineral logistics, with 125 µm film commonly selected for 25 kg fill weights and drop heights up to 1.2 m. For direct food-ingredient contact, compliance follows FDA 21 CFR 177.1520(c) 3.1a and 3.2a, and in the EU, Regulation (EU) No 10/2011 overall migration limits of 10 mg/dm² apply.
Low-temperature packaging produced from LL6808AA is built as a 40–60 µm monolayer or as a three-layer sealant web with an EVA or metallocene skin. The critical failure mode at -20°C is not tensile yield but crack propagation under impact; therefore dart drop values measured under standard ASTM D1709-16a conditioning at 23°C and 50% RH overestimate field performance. Frozen food converters typically condition specimens at -20°C for 48 h and then apply ASTM D1709-16a Method A; minimum impact values on 50 µm film are usually set at 180–250 g, although the standard condition is not -20°C and the deviation must be reported on the certificate of analysis. Heat seal initiation is measured per ASTM F88/F88M-21; the short-chain branching distribution of LL6808AA lowers seal initiation to roughly 95–105°C at 0.4 MPa dwell pressure and 0.5 s dwell on 40 µm film, 10–15°C below an equivalent LDPE. Hot tack strength per ASTM F1921-18 above 1.0 N/cm at 110°C is required for vertical form-fill-seal operations; below 100°C, seal strength is controlled by slow interdiffusion, and above 135°C, fibre tear of the web becomes the dominant failure locus. Gauge reduction below 35 µm increases pinhole formation at crease points after ice crystal flexing, particularly in IQF vegetable and shrimp bags. The structure is further limited by the requirement that sealant layers avoid migratory slip packages above 0.10 wt%, because higher erucamide or oleamide loadings reduce hot tack and can create organoleptic transfer in frozen prepared foods. Compliance for frozen food contact follows FDA 21 CFR 177.1520(c) 3.1a and 3.2a and EU Regulation (EU) No 10/2011, with overall migration below 10 mg/dm² under test conditions representing frozen storage. End products include frozen vegetable packs, IQF poultry pouches, and ice cream overwrap.
For 150 µm silage covers and greenhouse side sheeting exposed to high-UV agricultural environments, 100 wt% LL6808AA is dry-blended with 8–12 wt% of a polyethylene-based UV stabilizer masterbatch containing a hindered amine light stabilizer at 0.10–0.30 wt% active concentration and an o-hydroxybenzotriazole UV absorber at 0.05–0.15 wt% active concentration. The monolayer blown film line is configured with a 2.2–2.5 mm die gap, a blow-up ratio of 2.0:1–2.5:1, and a melt temperature of 200–220°C; the wider die gap is maintained because high UV masterbatch loadings reduce melt strength and narrow the stable bubble window. Frost line height is held between 700 mm and 1,200 mm to balance film optics against impact retention. Accelerated weathering is evaluated per ISO 4892-2:2013 Cycle 1 or ASTM G154-16 Cycle 1; agricultural film specifications under EN 13206:2017 generally require tensile elongation at break after artificial weathering to remain above 50% of the unexposed value, but published data for this specific formulation is limited and must be confirmed with a lot-specific weathering study. The concentration of UV additives is set by measured film thickness, not by total formulation weight; migration of HALS to the film surface can cause blocking at concentrations above 0.30 wt% active HALS, and EVA-based masterbatch carriers should be avoided at addition rates above 10 wt% because phase separation generates visible melt fracture lines. Silage covers produced from this formulation are intended for clamp silage piles and round bale wrapping; greenhouse side sheets are typically 150–200 µm and require anti-drip or anti-fog concentrates when used in enclosed high-humidity tunnels. Packaging waste compliance under EU Directive 94/62/EC imposes a combined heavy-metal limit of 100 mg/kg for lead, cadmium, mercury, and hexavalent chromium in the final agricultural film.
In coextruded pouches for snacks, dry fruits, and frozen prepared foods, LL6808AA is commonly specified as the sealant layer at 20–30 wt% of total thickness in a three-layer construction with a core of HDPE or LLDPE-LDPE blend and an outer layer of HDPE or printable LDPE. Layer distribution in a 45 µm web is 15/70/15 or 20/60/20; the die gap is set at 1.8–2.0 mm and the blow-up ratio at 2.0:1–2.5:1. Seal initiation temperature is recorded as the temperature at which seal strength reaches 2.0 N/cm under 0.4 MPa pressure and 0.5 s dwell per ASTM F88/F88M-21; for this grade the initiation temperature is 95–105°C, which is 10–15°C lower than LDPE of the same melt index. Hot tack performance per ASTM F1921-18 is maintained above 1.0 N/cm between 100°C and 135°C; at temperatures above 135°C the seal fails by tearing of the film rather than interfacial peel, an undesirable failure mode in high-speed vertical form-fill-seal machines. Blending 20 wt% LDPE into the sealant layer raises seal initiation by 3–5°C but improves bubble stability and reduces blocking in wound rolls; adding more than 30 wt% LDPE eliminates the low-temperature sealing advantage. Slip and antiblock concentrates are limited to 0.05–0.10 wt% each in the sealant layer, because higher concentrations create seal contamination and reduce hot tack. The sealant web must comply with FDA 21 CFR 177.1520(c) 3.1a and 3.2a for food contact; for export to the EU, overall migration testing under Regulation (EU) No 10/2011 Annex III is carried out with simulant A, B, or D2 depending on the food type. The end product is a lamination-grade sealant web or a direct-print pouch substrate.
Where 25 µm bin liners are extruded on high-speed monolayer lines without internal bubble cooling, LL6808AA is added at 15–25 wt% to HDPE or LDPE to restore machine-direction tear resistance measured per ASTM D1922-15 and to widen the stable bubble window before frost line height adjustments become necessary.
Surface protection film based on LL6808AA is manufactured as a 40–60 µm blown web that is subsequently corona-treated to 38–42 mN/m per ASTM D2578 and coated with a solvent-based acrylic pressure-sensitive adhesive at a dry coating weight of 8–12 g/m². The film is applied to stainless steel, painted aluminium composite panels, and glass sheets during transport and installation. Peel adhesion is tested according to ASTM D3330-04(2018) after 24 h dwell at 23°C and 50% RH; values on stainless steel typically fall between 1.5 N/25 mm and 3.0 N/25 mm for clean removal, but adhesion increases with dwell time and substrate roughness. After 7 days at 40°C, peel strength can rise by 20–40% due to adhesive wet-out; removal after 6 months of outdoor exposure is not recommended because UV-induced oxidation of the acrylic adhesive can transfer residue to the substrate. The LL6808AA base film contributes controlled elongation at break and puncture resistance during slitting and application, but the film must be formulated without migratory slip packages above 0.05 wt% because migration to the treated surface before coating will reduce adhesive anchorage. Corona treatment must be applied in-line at 2.0–2.5 kW and 80–120 m/min; a surface energy below 36 mN/m causes adhesive delamination, while treatment above 44 mN/m can produce low-molecular-weight oxidized species that interfere with peel stability. Heavy metal limits in the final film follow EU Directive 94/62/EC with a combined limit of 100 mg/kg for lead, cadmium, mercury, and hexavalent chromium. The product is slit to widths of 50–1,500 mm and supplied on 3-inch paper cores.
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INEOS LLDPE LL6808AA is a butene-1 linear low-density polyethylene resin supplied as free-flowing pellets for blown-film conversion. The grade is compounded with a slip and antiblock additive package and is positioned for medium-duty packaging film, carrier bags, liners, overwrap, and industrial film structures where controlled surface slip, consistent bubble stability, and moderate optics are required. The nominal melt flow rate is 1.0 g/10 min at 190 °C under 2.16 kg load as determined by ASTM D1238; the nominal density is 0.918 g/cm³ according to ASTM D1505 and ISO 1183-1. The resin is produced by low-pressure gas-phase polymerization; short-chain branching introduced by the butene-1 comonomer reduces crystallinity relative to high-density polyethylene, lowering flexural stiffness and increasing dart impact energy absorption at equivalent gauge. The suffix “AA” identifies the standard slip and antiblock formulation; it is not a color, barrier, or clarity indicator. Exact additive concentrations, residual catalyst metals, and bulk density are lot-specific and are reported on the certificate of analysis.
The two published nominal properties establish a material class but do not fully define converter behavior. Density is the primary crystallinity control; at 0.918 g/cm³, the resin places in the low-density film range, producing a sealant-like melting profile and lower yield stress than a nominal 0.935 g/cm³ medium-density polyethylene. Melt flow rate at 1.0 g/10 min indicates moderate shear viscosity and sufficient melt strength for bubble diameters up to the die’s rated blow-up capacity. However, lot-to-lot variation in molecular weight distribution, pellet geometry, and additive dispersion can move extrusion pressure and heat-seal response even when density and melt flow rate remain within certificate limits. A complete processing definition therefore requires converter-level measurements of melt pressure at fixed screw speed, extruder amperage, frost-line position, and film gauge variation.
| Property | Nominal value | Test method / condition |
|---|---|---|
| Melt flow rate | 1.0 g/10 min | ASTM D1238, 190 °C, 2.16 kg; ISO 1133-1:2022 |
| Density | 0.918 g/cm³ | ASTM D1505; ISO 1183-1 |
| Base comonomer | Butene-1 copolymer | Manufacturer technical data sheet |
| Additive package | Slip and antiblock | Product suffix “AA”; certificate-of-analysis concentration |
On blown-film lines, INEOS LLDPE LL6808AA is processed on single-screw extruders with 24:1 to 30:1 L/D ratios and barrier or Maddock mixing sections. Die gaps of 1.5 mm to 2.5 mm are used, with blow-up ratios between 2.0:1 and 3.0:1. Barrel profiles generally rise from 160 °C near the feed throat to 190 °C at the die; melt temperature is maintained from 190 °C to 230 °C. Exceeding 240 °C risks oxidative chain scission and additive degradation, especially at high residence times in large-diameter dies. Because linear low-density polyethylene has a narrower molecular weight distribution and higher shear viscosity at low shear rates than branched LDPE of similar melt index, extruder drive amperage and die pressure are higher. A dual-lip air ring with internal bubble cooling is preferred when output exceeds 150 kg/h on dies larger than 300 mm; otherwise, bubble instability may appear as vertical diameter oscillation or draw resonance. The resin is not hygroscopic, and pre-drying is not normally required. If pellets have been stored in an unheated warehouse and exposed to condensation, dry-air purging at 60 °C for 1 h removes surface moisture without altering the additive package. Screen packs of 60/80/100 mesh are typical for general film; finer packs increase melt pressure without measurable optical improvement.
The slip additive in the “AA” package is migratory; after pellet extrusion, the additive blooms to the film surface over a period of hours to days. This bloom reduces film-to-film coefficient of friction and blocking force, but it can also alter the heat-seal response. In polyethylene films, seal initiation temperatures for a 0.918 g/cm³ butene LLDPE are commonly reported between 95 °C and 115 °C on laboratory heat-seal equipment, yet the additive package may shift the measured initiation upward by 2 °C to 5 °C if sealing occurs after full bloom. Converters should establish the seal window on production jaws using ASTM F88 for seal strength and ASTM F2029 for heat sealability; laboratory-generated values from untreated cast film are not directly transferable. Hot tack response is additionally important in vertical form-fill-seal operations and should be measured separately according to ASTM F1921. For lamination and print, migratory slip reduces surface energy; corona treatment to 38 mN/m or higher, measured by ASTM D2578, is commonly required before solventless lamination or UV ink application. Avoid amine-based antifog masterbatches at high loadings where surface competition with slip bloom may produce non-uniform coefficient of friction; no incompatibility with standard hydrocarbon food-contact additives is indicated.
Because the grade is used on single-screw extruders with limiting barrels, melt-pressure monitoring at the breaker plate is the most direct lot-to-lot diagnostic. A melt-pressure increase of 10% or more at fixed screw speed and barrel setpoint, or a corresponding drop in motor amperage, indicates partial screen blockage, additive agglomeration, or cross-contamination with a higher-viscosity resin. The film gauge profile may remain acceptable during the early stages of blockage; melt-pressure drift therefore precedes visible gauge variability. When the pressure rise exceeds 20%, screen-pack replacement is recommended before die-head temperature or screw speed is changed, because increasing barrel temperature to reduce pressure can accelerate additive degradation and shift the slip bloom profile. On production-scale lines, lot changes should be documented with melt pressure, extruder output in kg/h, and film gauge distribution from a scanning frame. Published data for this specific configuration is limited, but the general relationship between pressure drop and screen blockage is well established in blown-film practice.
Film properties derived from LL6808AA are not intrinsic resin constants; they emerge from film gauge, blow-up ratio, frost-line height, and thermal history. The appropriate test methods for converted film are ASTM D882 for tensile strength and elongation, ASTM D1922 for Elmendorf tear, ASTM D1709 for dart impact, ASTM D1003 for haze, and ASTM D2457 for 60° gloss. Because blown film is anisotropic, machine-direction tensile yield and break strength will differ from transverse-direction values; at 25 µm, the orientation effect is stronger than at 50 µm. Butene-based LLDPE of this density typically shows lower Elmendorf tear than hexene-based LLDPE at equal density and melt flow rate; the difference is attributed to lower tie-molecule concentration and limited strain-induced crystallization. Dart impact, by contrast, may be adequate for medium-duty packaging because the comonomer distribution and additive package are designed to preserve bubble stability without sacrificing low-temperature ductility. Direct comparison with other products should be made only on film produced on the same die, at the same blow-up ratio, and at the same gauge; otherwise, differences are confounded by orientation and cooling rate.
| Response | Test method | Routine qualification interval |
|---|---|---|
| Tensile strength and elongation | ASTM D882 | Each lot on 25 µm or product gauge |
| Elmendorf tear | ASTM D1922 | Each lot or process change |
| Dart impact | ASTM D1709 | Each lot; F50 reporting |
| Haze | ASTM D1003 | Each lot |
| Gloss | ASTM D2457 | Each lot |
| Kinetic coefficient of friction | ASTM D1894 | After 72 h bloom |
| Blocking force | ASTM D3354 | After 24 h at 60 °C as agreed |
| Seal strength | ASTM F88 | Seal temperature curve |
| Heat sealability | ASTM F2029 | On production jaws |
Relative to hexene-based LLDPE grades, LL6808AA trades some intrinsic tear and dart impact for a controlled surface additive system and predictable film-to-film slip in high-speed form-fill-seal conversion. The product should not be directly substituted where maximum Elmendorf tear in frozen-food packaging below −25 °C is the primary specification; in such applications, a hexene or metallocene grade may be required. Compared with non-additivated butene LLDPE film grades, the “AA” additive package reduces blocking and stabilizes coefficient of friction after 24 h to 72 h of bloom, but sacrifices some adhesion and seal-initiation margin. In blends with LDPE, addition of LL6808AA at 20 wt% or less usually increases dart impact and tensile strength without overloading the extruder; at levels above 30 wt%, the linear resin’s higher melt viscosity should be checked against motor torque, die pressure rating, and air-ring cooling capacity. Food-contact suitability must be confirmed against FDA 21 CFR 177.1520 and current European Union Regulation (EU) No 10/2011 positive-list conditions for the specific additive package; the manufacturer’s regulatory documentation states the covered use conditions and migration limits. For converters running vertical form-fill-seal equipment, pouch seal strength after filler contamination and through creases should be qualified using ASTM F88; published data for this specific configuration is limited.