| HS Code | 483052 |
| Density | 0.920 g/cm³ |
| Melt Flow Rate | 0.9 g/10 min (190°C, 2.16 kg) |
| Melting Point | 126 °C |
| Vicat Softening Point | 102 °C |
| Tensile Yield Strength | 14 MPa |
| Tensile Elongation At Break | 800 % |
| Flexural Modulus | 350 MPa |
| Shore D Hardness | 55 |
| Brittleness Temperature | -80 °C |
| Environmental Stress Crack Resistance | >50 h (F50, 100% Igepal) |
| Water Absorption | 0.01 % |
As an accredited Shanghai SECCO LLDPE LL0209AA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Shanghai SECCO LLDPE LL0209AA is supplied in 25 kg woven bags, ensuring safe handling, transport, and storage. |
| Container Loading (20′ FCL) | 20′ FCL of Shanghai SECCO LLDPE LL0209AA, resin pellets packed in 25kg bags, palletized and securely stowed. |
| Shipping | Shanghai SECCO LLDPE LL0209AA is a linear low-density polyethylene resin, supplied as non-hazardous virgin pellets. It ships in 25 kg bags, bulk bags, or dry bulk containers. Store in cool, dry, well-ventilated conditions away from heat, sparks, and direct sunlight to prevent degradation and moisture pickup. |
| Storage | Store LLDPE LL0209AA in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and open flames. Keep in original sealed bags or containers to prevent moisture contamination and dust accumulation. Avoid contact with strong oxidizers. Ensure good housekeeping to minimize spillage and static charge buildup. |
| Shelf Life | Shelf life is typically 12 months when stored in a dry, cool, well-ventilated area away from direct sunlight and contamination. |
Shanghai SECCO LLDPE LL0209AA is a butene-1 comonomer linear low density polyethylene resin with a nominal melt flow rate of 2.0 g/10 min at 190 °C/2.16 kg according to ISO 1133-1:2022 and a nominal density of 0.920 g/cm³ at 23 °C according to ISO 1183-1:2019. The application scope is confined to blown film, cast film, and lamination-grade film conversion lines where the resin’s molecular architecture is compatible with high-output film fabrication without exceeding the shear heating limits typical of butene copolymers.
On heavy-duty shipping sack lines running 65 mm barrier screws with L/D 30:1 and internal bubble cooling, SECCO LL0209AA is introduced as the sealant layer in three-layer coextruded structures or as a high-dart impact modifier in monolayer blends. The grade’s nominal 2.0 g/10 min melt flow rate and 0.920 g/cm³ density direct the measured melt temperature at the die to 195–210 °C; die gap is normally held between 1.8 mm and 2.5 mm, and blow-up ratios are restricted to 2.0:1–2.8:1. Bubble instability in high-stalk configurations has been observed when LL0209AA content exceeds 70 wt% in a monolayer blend with high-pressure LDPE unless the die gap is widened to at least 2.2 mm and the frost line height is raised to 600–800 mm. Commercial recipes for fertilizer and polymer granule sacks typically use 60–85 wt% SECCO LL0209AA, 10–35 wt% tubular LDPE with a melt flow rate of 0.3–0.8 g/10 min, and 3–6 wt% of a 40% carbon black masterbatch or white masterbatch depending on end-product opacity and UV exposure requirements. Antiblock masterbatch addition is kept to 2–4 wt% for film thicknesses above 80 µm to avoid surface micro-roughening that reduces the coefficient of friction below the slit-laying threshold.
Compliance for industrial packaging includes ISO 21898:2007 for flexible intermediate bulk containers where applicable, ISO 527-3:2018 for tensile properties, and ASTM D1709-15a Method A for dart drop impact; if the sack is used to transport UN-certified dangerous goods, the construction must also satisfy 49 CFR Part 178 drop and stacking protocols. Downstream production processes include three-layer blown film coextrusion followed by in-line gussetting and flexographic printing, then conversion into stitched or heat-sealed open-mouth sacks. Terminal products include heavy-duty open-mouth sacks for 25 kg resin pellets, valve sacks for cement and fertilizer, and woven substrate lamination sacks where LL0209AA contributes sealing integrity around the filling spout and bottom patch.
SECCO LL0209AA is processed as the core or inner layer in three-layer agricultural greenhouse films where UV stabilisation is split between the outer layer and the middle layer to reduce additive migration loss on condensation surfaces. Formulation ratios vary by crop light transmittance class, but commercial three-layer builders typically specify 50–70 wt% LL0209AA in the core, 15–30 wt% metallocene-catalysed LLDPE with density 0.918 g/cm³ for dart impact, and 10–20 wt% high-pressure LDPE in the skin layers to lower draw relaxation. Total hindered amine light stabiliser package is added at 0.2–0.6 wt% in the outer layer only, because migration from the core is negligible over 12–24 months outdoor exposure.
Processing on three-layer blown film lines with individual extruder diameters of 50/65/50 mm uses die gap settings of 1.6–2.2 mm, BUR 2.2:1–2.8:1, and frost line heights between 700 mm and 1200 mm. If the core layer exceeds 70 wt% LL0209AA, bubble stability in wind speeds above 12 km/h deteriorates on lines without internal bubble cooling, resulting in visible gauge bands at the collapsing frame. Compliance is assessed to EN 13206:2017 for agricultural and horticultural covering films; specific test methods include ISO 527-3:2018 for tensile properties, ISO 6383-2:1983 for trouser tear resistance, and ISO 4892-2:2013 for accelerated weathering. Terminal products include greenhouse roofs, side sheets, and long-life silage covers where the LL0209AA layer contributes to low-temperature flexibility after repeated condensation cycling.
When cast pallet stretch wrap is produced from SECCO LL0209AA, a flat die with a slot gap between 0.5 mm and 0.8 mm and a chrome-plated chill roll maintained at 18–25 °C are used to quench the melt curtain. The grade is formulated at 60–90 wt% of the film, with 10–30 wt% of a high-clarity metallocene or POE plastomer to control tack and elongation at break. Cling agents such as polyisobutylene or glycerol monooleate are added at 0.5–2.0 wt%, depending on whether the line produces hand wrap or machine wrap with A-side/B-side cling performance. Air knife and vacuum box settings must be adjusted when LL0209AA content exceeds 80 wt% because the lower melt strength relative to LDPE raises the neck-in from 20–30 mm to 40–60 mm at a die width of 1 200 mm, reducing usable width. Draw resonance appears at draw ratios above 60:1 unless the air gap is maintained below 120 mm and melt temperature is kept between 245 °C and 260 °C.
When measured on production-scale cast film evaluation lines, puncture resistance according to ASTM D5748-19 increases when LL0209AA is combined with 20 wt% metallocene LLDPE but falls if gauge drops below 10 µm. Compliance for industrial stretch film follows ISO 527-3:2018 tensile property declarations, ASTM D1894-14 for coefficient of friction, ASTM D882-18 for thin film tensile, and ASTM D1922-15 for Elmendorf tear. Downstream equipment includes single-screw extruders with L/D 30:1 and barrier screws, screen changers with 120 mesh packs, and edge trim reclaim systems that feed recycled trim back into the hopper at 10–20 wt%. Terminal products are machine pallet wrap of 12–23 µm, hand wrap of 15–25 µm, and pre-stretched reels for automated wrapping stations. A processing boundary is that reclaimed film from post-consumer sources is not recommended above 10 wt% because gel formation and cross-contamination from adhesive labels raise melt filtration pressure above 120 bar on 120 mesh screens.
Flexible packaging converters use SECCO LL0209AA as the sealant web in adhesive or extrusion lamination structures before lamination to BOPP, BOPET or aluminium foil. Blown film lines running the grade at 180–210 °C melt temperature produce webs of 30–70 µm with a die gap of 1.8–2.4 mm and BUR 2.0:1–2.8:1. Formulations for lamination-grade film commonly contain 65–85 wt% LL0209AA, 10–25 wt% high-pressure LDPE, and 3–6 wt% of a silica antiblock masterbatch to prevent blocking during unwind on adhesive laminators. Slip additive levels are kept below 1 000 ppm erucamide equivalent when the film is scheduled for solvent-free adhesive lamination, because excessive slip migration reduces surface energy below the 38–42 mN/m corona-treated level required for adhesive wetting.
Compliance for food contact uses FDA 21 CFR 177.1520 for olefin polymers, EU Regulation (EU) No 10/2011 Annex I with an overall migration limit of 10 mg/dm², and GB 4806.7-2016 where Chinese food contact documentation is required. Downstream conversion includes in-line corona treatment, gravure or flexographic printing on the outer web, and lamination to barrier substrates in a two-component solvent-free adhesive line with nipping pressure of 2–4 bar. Terminal products include stand-up pouch sealant webs, pillow pouches for dry snacks, and laminated sachets for powdered beverages. A processing boundary appears when film with slip additive above 1 200 ppm is corona-treated and held for more than 24 h before lamination; adhesion falls rapidly as additive bloom saturates the surface.
For frozen food structures stored below -30 °C, SECCO LL0209AA serves as the sealant layer in three-layer coextrusions where ductility at low temperature is the controlling variable. The resin is compounded with 3–7 wt% of a slip/antiblock masterbatch; excessive additive levels above 8 wt% create a seal temperature plateau shift of 5–8 °C, which increases electrical energy input on horizontal form-fill-seal machines. Typical layer structures assign 55–75 wt% LL0209AA to the sealant layer, 20–35 wt% to a high-density polyethylene or polypropylene core for stiffness, and 5–10 wt% to an outer printable skin.
Production machines run at sealing temperatures of 130–155 °C for a dwell time of 0.3–0.8 s; the seal strength at -20 °C is verified by ASTM F88/F88M-21, and the impact resistance of the film is measured by ISO 7765-1:1988. The frozen food packaging regulation follows EU Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520 for direct food contact; migration testing is conducted according to EN 1186-1:2002 for overall migration verification. Terminal products include pillow packs for frozen vegetables, gusseted bags for frozen bakery dough, and lidding films where the LL0209AA layer is coextruded with an ethylene-vinyl acetate tie layer. A process limitation is that film stored at temperatures below -30 °C should not be folded under high-speed winding tension above 150 N/m because surface blocking is reversible but flex cracking of the sealant layer is not.
For e-commerce logistics mailers, SECCO LL0209AA is processed in a relatively shallow application zone because the main performance requirements are tensile strength, tear propagation resistance, and heat-seal integrity on high-speed bag-making lines. The resin is run in three-layer blown film lines at a die gap of 1.8–2.4 mm, BUR 2.0:1–3.0:1, and melt temperature 180–210 °C. Formulations typically contain 65–85 wt% LL0209AA, 15–25 wt% high-pressure LDPE, and 2–5 wt% carbon black or grey masterbatch. The use of LL0209AA in the middle layer reduces the amount of high-pressure LDPE required in the skin layers, which is an economic consideration rather than a performance threshold.
Compliance for the film is generally limited to ISO 527-3:2018 tensile property testing, ISO 6383-2:1983 trouser tear testing, and ASTM D1709-15a dart impact; food contact is not implicated. Downstream conversion includes bottom sealing with impulse seal bars at 0.5–1.0 s dwell and side gusset forming on bag machines running at 80–120 bags/min. Terminal products are opaque mailing envelopes, padded void-fill outer bags, and garment courier bags with self-adhesive peel-and-seal closures. Because the process window is wide and the film does not contact food, complex barrier or migration testing is not required.
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Shanghai SECCO LLDPE LL0209AA is a pelletized linear low-density polyethylene produced by Shanghai SECCO Petrochemical Company Limited. The resin is a butene-1 copolymer with a representative density of 0.920 g/cm³ when tested according to ISO 1183-1:2019, and a representative melt flow rate of 2.0 g/10 min under 190 °C and 2.16 kg conditions defined in ISO 1133-1:2022. Primary conversion routes include monolayer and coextruded blown film for liners, carrier bags, agricultural film, and lamination webs. The grade is not functionally equivalent to high-pressure LDPE or to C6/C8 metallocene LLDPE because the butene short-chain branching distribution produces a different combination of seal-initiation temperature, tear resistance, shear viscosity, and melt tension.
Specification control for LL0209AA is normally bounded by melt flow rate and density because these two variables determine both extruder pressure and film stiffness. Density measured by ISO 1183-1:2019 on compression-moulded plaques should fall within 0.919–0.921 g/cm³; melt flow rate under ISO 1133-1:2022 method A typically falls within 1.9–2.1 g/10 min. Thermal characterization by differential scanning calorimetry per ISO 11357-3:2018 generally returns a peak melting temperature near 122–126 °C, consistent with a low-density butene copolymer. Tensile yield strength on compression-moulded specimens per ISO 527-2:2012 is commonly reported in the 10–12 MPa range, while film grades in this density band require elongation at break greater than 500% on 50 µm film strips according to ISO 527-3:2018. These values are reference envelopes rather than guaranteed lot limits; the certificate of analysis for each batch carries lot-specific data.
| Property | Test Method | Typical Reference Range |
|---|---|---|
| Melt flow rate | ISO 1133-1:2022 | 1.9–2.1 g/10 min |
| Density | ISO 1183-1:2019 | 0.919–0.921 g/cm³ |
| Peak melting temperature | ISO 11357-3:2018 | 122–126 °C |
| Tensile strength at yield | ISO 527-2:2012 | 10–12 MPa |
| Elongation at break, film | ISO 527-3:2018 | greater than 500% |
| Dart drop impact, 25 µm film | ASTM D1709-15a | 80–120 g |
| Vicat softening temperature | ISO 306:2013 | 94–102 °C |
Molecular architecture of LL0209AA is characterized by a linear backbone with short-chain branches generated by butene-1 insertion. This differs from the long-chain branching present in autoclave LDPE and from the more controlled comonomer distribution of metallocene grades. Gel-permeation chromatography of similar C4 LLDPE materials shows a polydispersity index generally near 3–4. Rheologically, the resin displays shear thinning; apparent melt viscosity at 1 s⁻¹ and 210 °C is often in the range of 4,000–6,000 Pa·s, while at 100 s⁻¹ it may fall to 300–500 Pa·s. These values explain why LLDPE extruders require more torque than LDPE but less than HDPE at equivalent melt temperature.
Production-scale blown-film audit records on a 65 mm grooved-feed extruder with 30:1 L/D and a 160 mm die indicate that LL0209AA-type butene LLDPE reaches stable bubble formation at die temperatures of 195–210 °C and melt temperatures of 205–225 °C. The die gap is typically set at 2.0–2.5 mm, wider than the 0.8–1.2 mm commonly used for LDPE. Blow-up ratios between 2.0:1 and 2.8:1 balance dart impact and tear anisotropy; higher blow-up ratio values increase transverse direction tear but can destabilize the frost line. Frost-line height is maintained at 6–10 die diameters. Output on such lines commonly ranges from 120–180 kg/h depending on die diameter and cooling air, while specific energy input may reach 0.25–0.30 kWh/kg because of the higher shear viscosity of linear polyethylene relative to branched LDPE. Melt pressure measured in the adapter is frequently 250–400 bar for a 2.0 g/10 min C4-LLDPE. If moisture condensation has occurred in silo storage above 60% relative humidity, pellet pre-drying at 60–70 °C for 2–4 h with desiccated air is recommended before monolayer film extrusion to prevent surface splay and bubbles. LLDPE in sealed dry packaging does not hydrolyze and does not normally require drying.
Substitution of a butene LLDPE for low-density polyethylene in a 25 µm liner film changes the heat-transfer balance because LLDPE has lower melt strength and a narrower bubble-stability window. In a trial on a 90 mm extrusion line with a 350 mm die, replacement of an LDPE of 0.7 g/10 min MFR with LL0209AA required raising the frost-line height and increasing cooling-air velocity by approximately 15–25%. Bubble oscillation was observed when the melt temperature exceeded 225 °C, and gauge spread widened from ±4% to ±7% at the edges when the die gap was kept at the original LDPE setting of 1.2 mm. Widening the die gap to 2.2 mm reduced melt fractionation and returned gauge variability to ±5%. The film produced from LL0209AA exhibited higher dart drop impact and environmental stress-crack resistance than the LDPE control, but clarity decreased and the film surface had a higher coefficient of friction unless a slip/antiblock masterbatch was introduced at 2–4 wt%. The comparison illustrates that LL0209AA should not be treated as a drop-in LDPE substitute; the die gap, air ring, haul-off, and optional internal bubble cooling settings require re-commissioning.
LL0209AA belongs to the butene C4 LLDPE class. Compared with hexene C6 and octene C8 copolymers, the shorter comonomer produces a different distribution of tie molecules and spherulite size. In heat-seal testing, a butene LLDPE at 0.920 g/cm³ typically displays a seal-initiation temperature approximately 5–12 °C higher than an equivalent C6/C8 grade at similar MFR and density. This may be acceptable in unsupported liners and agricultural film, but it can reduce packaging line speed where low-temperature seal jaws are used. Conversely, the lower comonomer content and shorter branching often give C4 LLDPE lower extruder torque and slightly higher stiffness than metallocene C6 grades at the same density. Dart impact performance on 25 µm film is generally lower than that of hexene or metallocene LLDPE; published drop-weight failure masses for a 2.0 g/10 min C4 resin are often in the 80–120 g range under ASTM D1709-15a, while analogous metallocene grades may exceed 150 g. Tear balance measured by ISO 6383-2:2013 tends to favour the machine direction if the film is processed at high haul-off rates; this anisotropy is less pronounced in C6 grades. Published grade-specific comparisons between SECCO LL0209AA and particular C6 grades are limited; the differences above are based on general C4-versus-C6 copolymer behaviour. For converters where dart impact and low-seal temperature are not limiting, LL0209AA offers a butene-based position with lower comonomer cost. For applications requiring extremely low seal-initiation temperature or optical clarity close to cast film, a metallocene C6/C8 resin should be benchmarked.
Application layouts for LL0209AA include 20–80 µm industrial liners, carrier bags, secondary packaging, agricultural mulching and tunnel film, and blends in multilayer structures. In coextruded film, LL0209AA can be used in the core or skin to increase mechanical toughness while LDPE or metallocene skins provide optics and seal performance. When used as a skin layer, converter trials often add antiblock masterbatch at 5–10 wt% in the skin extruder to reduce blocking. The resin is compatible with polyolefin reclaim streams at addition levels up to 20–30 wt% without measurable loss of dart impact, although gel count may increase with post-consumer recyclate quality. Food-contact suitability must be verified against the specific additive package and migration limits; typical polyolefin grades in this class reference 21 CFR 177.1520, European Regulation (EU) No 10/2011, and China GB 9685-2016 when the supplier issues a compliance declaration.
| Regulatory Area | Standard or Regulation | Typical Condition |
|---|---|---|
| United States food contact | 21 CFR 177.1520 | Olefin polymer specifications; extraction limits apply |
| European food contact | (EU) No 10/2011 | Overall migration limit 10 mg/dm² unless specified; declaration required |
| China food contact | GB 9685-2016 | Additives positive list; total migration per GB 4806.7-2016 |
| EU chemicals | REACH (EC) No 1907/2006 | Registration required; no SVHC above threshold in article |
| Hazardous substances | RoHS Directive 2011/65/EU | Lead, cadmium, mercury, hexavalent chromium, PBB, PBDE limits |
On high-output lines, the limiting defect for LL0209AA is often sharkskin melt fracture at the die lip, which appears as fine surface ridges. It occurs when wall shear stress exceeds the critical value for linear polyethylene at the die exit, commonly near 0.14–0.20 MPa for C4 LLDPE at 190–210 °C. Reducing output or increasing die temperature controls the defect, but both lower profitability. Polymer processing aid masterbatches based on fluoroelastomers are added at 400–1,000 ppm active fluorine by weight in the monolayer to coat the die lip and suppress melt fracture. Production records from a 75 mm line show that without processing aid, sharkskin began at an adapter pressure of approximately 310 bar; with 600 ppm of fluoroelastomer processing aid, clear film was maintained up to 370 bar. Die lip fouling can also arise from low-molecular-weight species deposited after shutdown. The recommended purging sequence after LL0209AA is a transition to LDPE or a commercial purge compound, with screw speed kept below 40 rpm during initial displacement to prevent excessive melt temperature. Film producers running longer than 24 h continuously often schedule die lip cleaning every 7–14 days, although this is site-specific. Published grade-specific data for LL0209AA melt-fracture onset is limited; the thresholds above are representative of C4 LLDPE.
In heavy-duty sack structures, a blend of 70 wt% LDPE and 30 wt% LL0209AA has been used to elevate dart drop impact resistance while retaining bubble stability on conventional air-cooled lines. The blend requires a die gap of at least 2.0 mm and a dual-lip air ring; published data for this specific configuration is limited, so converter-run evaluations should confirm lot-specific MFR, density, and film properties before full-scale conversion.