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Taisox LLDPE 3490

    • Product Name: Taisox LLDPE 3490
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 666188
    Product Name Taisox LLDPE 3490
    Material Type Linear Low Density Polyethylene
    Melt Flow Index 2.0 g/10min
    Density 0.920 g/cm³
    Melting Point 122 °C
    Vicat Softening Point 92 °C
    Tensile Strength At Yield 11 MPa
    Elongation At Break 800 %
    Tensile Modulus 320 MPa
    Dart Drop Impact Strength 150 g
    Haze 12 %
    Gloss 60

    As an accredited Taisox LLDPE 3490 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Taisox LLDPE 3490 is supplied as resin pellets in 25 kg net bags, palletized and shrink-wrapped for safe handling and storage.
    Container Loading (20′ FCL) Taisox LLDPE 3490 is loaded in a 20′ FCL as 25kg bags on pallets, shrink-wrapped and secured for safe transport.
    Shipping Taisox LLDPE 3490 ships as non-hazardous resin pellets in moisture-proof woven bags or bulk hoppers. Ensure dry, ventilated storage and avoid exposure to direct sunlight or high heat. Load securely, protect from punctures, and handle with standard conveying equipment to maintain product purity and flow.
    Storage Store Taisox LLDPE 3490 in a clean, dry, well-ventilated area, away from direct sunlight, heat sources, sparks, and open flames. Keep original sealed bags intact to prevent moisture, dust, or contamination. Maintain moderate temperatures and low humidity, avoid stacking excessively high, and follow first-in, first-out inventory rotation to preserve resin quality.
    Shelf Life Store in a cool, dry place away from sunlight. Shelf life is 12 months from production date.
    Application of Taisox LLDPE 3490

    In pallet-unitization cast-film production, Taisox LLDPE 3490 is screened against ASTM D5459 for machine-direction stretch retention and ASTM D5458 for cling force after the extrudate is quenched on a three-roll vertical chill-roll stack with roll temperatures between 22 °C and 30 °C; because the resin’s low crystallinity contributes to a broad hot-tack plateau, converters typically let down 10–25 wt% of Taisox LLDPE 3490 into a metallocene-catalyzed hexene LLDPE to shift the dart-impact/tear balance without narrowing the cast-film processing window below ±5 °C on die temperature. Compliance for non-food pallet wrap is usually governed by REACH (EC) No 1907/2006 Article 33 for SVHC disclosure and by Directive 94/62/EC Article 11 for the sum of lead, cadmium, mercury, and hexavalent chromium not exceeding 100 mg/kg in packaging, while food-contact stretch bundling film that may contact unpeeled produce falls under FDA 21 CFR 177.1520(c) paragraph 3.2a for olefin polymers and EU Regulation (EU) No 10/2011 Annex I with an overall migration limit of 10 mg/dm² as tested per EN 1186-1. The downstream production route on a dedicated cast-film line with a slot die of 0.8–1.0 mm die gap, a 30:1 L/D single-screw extruder with barrier mixing sections, and an air gap of 60–120 mm operates at melt temperatures of 240–260 °C; when the Taisox LLDPE 3490 fraction exceeds 25 wt%, measured machine-direction stretch retention may improve, but cling force decreases below 1.2 N/cm on ASTM D5458, which creates a hard upper addition limit for self-cling formulations. Published data for this specific formulation gradient are limited, so each converter must qualify the blend on the production line using the lot-specific certificate of analysis; cling-force variation above 0.4 N/cm between batches is observed when the cast-film line is restarted after a shutdown longer than 4 h. Terminal products from this application boundary are machine-grade stretch wrap with roll widths between 250 mm and 500 mm, hand wrap with nominal thickness from 12 µm to 23 µm, and bundling film for light industrial consolidation where load stability under 60 Hz vertical vibration is evaluated using ASTM D4169 truck-transport profiles.

    What Limits the Sealant Layer Loading of Taisox LLDPE 3490 in High-Speed Frozen-Food Form-Fill-Seal Webs?

    For vertical form-fill-seal packaging of frozen vegetables and IQF fruit, the sealant layer is usually a blend of 70–85 wt% Taisox LLDPE 3490 with 15–30 wt% LDPE having a melt index below 2.0 g/10 min, and the blend is coextruded against a core layer that may contain polyamide or EVOH; the addition ratio is constrained by hot-tack strength measured according to ASTM F1921, which must remain above 2.0 N/25 mm at sealing temperatures of 105–125 °C and dwell times below 40 ms. The applicable compliance framework is FDA 21 CFR 177.1520(c) paragraph 3.2a for all-olefin polymers, EU Regulation (EU) No 10/2011 with simulant D1 and D2 migration testing per EN 1186-3, and ISO 22000:2018 clause 8.3 for traceability of primary packaging inputs; if frozen-food packaging is printed or laminated, the finished structure must also satisfy EU 2023/2006 good manufacturing practice for food-contact materials. On blown-film lines with a 2.0–2.4 mm die gap, a die diameter of 250–400 mm, and a blow-up ratio of 2.0:1 to 2.8:1, the melt temperature is held at 185–210 °C to prevent excessive oxidation in the outer polyamide/EVOH core; using Taisox LLDPE 3490 below 70 wt% lowers dart impact below 7 g/µm as tested by ASTM D1709 method A, while using it above 85 wt% can reduce bubble stability on air-cooled lines when ambient temperature exceeds 30 °C and relative humidity exceeds 65%. Pre-drying of the polyamide or EVOH core at 70–80 °C for 4–6 h is required when raw-material storage relative humidity exceeds 60%, because moisture in the core layer produces pinholes and seal discontinuities at the FFS jaw. Terminal product types include iced-vegetable pouches of 250–1000 g fill weight, IQF berry pouches requiring -40 °C seal integrity after drop testing per ASTM D5276, and pillow packs for shredded cheese with print-web scuff resistance verified by ASTM D5264.

    Regulatory and test anchor matrix for non-food versus food-contact LLDPE 3490 applications
    RequirementStandard / regulationClause or test designationApplication boundary
    Olefin food-contact polymerFDA 21 CFR 177.1520(c)paragraph 3.2aFood-contact films and sealants
    Overall migration into simulantsEU Regulation (EU) No 10/2011Annex I, 10 mg/dm²Food-contact laminates
    Stretch wrap MD recoveryASTM D5459machine-direction stretch retentionPallet unitization film
    Stretch wrap clingASTM D5458peel clingPallet unitization film
    Dart impactASTM D1709method A / BIndustrial sacks, frozen-food film
    Hot tackASTM F1921seal strength after 40 ms dwellFFS sealant layers
    Seal strengthASTM F88flexible barrier materialsLiquid packaging laminates
    Packaging heavy metalsDirective 94/62/ECArticle 11, heavy metals 100 mg/kg sumAll packaging
    Agricultural covering filmEN 13206:2017mechanical and weathering classesSilage covers, greenhouse film

    Extrusion Lamination Sealant Layers for Liquid Packaging Laminates

    In liquid-packaging lamination, Taisox LLDPE 3490 is melt-extruded as a sealant tie layer between aluminium foil and paperboard or between oriented polyester and aluminium foil, with the addition ratio typically 100 wt% as a sealant layer or 20–40 wt% in a blend with LDPE when reduced neck-in is required; the material’s melt strength, measured indirectly as neck-in at 12 m/min line speed on a 280 °C melt, must be below 15 mm per edge to maintain uniform bond strength. Compliance is governed by FDA 21 CFR 177.1520(c) for the olefin sealant, EU Regulation (EU) No 10/2011 Annex II with overall migration per EN 1186-12, and EN 1186-5 for migration into simulant E when the laminate is used for fatty or dry food contact; when used in aseptic packages, the sealant layer must pass ISO 11607-1:2019 for sterile barrier system compatibility and ASTM F88 seal strength above 18 N/25 mm. The downstream production process is extrusion coating/lamination on a line with a 4.5–6.0 kg/h/cm die output rate, corona treater placed after the chill roll at 40–50 kW, and laminator nip pressure of 3–5 bar; melt temperature is set between 275 °C and 310 °C to oxidize the polyethylene surface sufficiently for adhesion to aluminium foil, and chill-roll temperature is maintained below 18 °C to limit backside web blocking. The addition of LDPE above 40 wt% reduces neck-in but also lowers heat-seal strength below 3 N/15 mm at 130 °C, making the blend unsuitable for aseptic packaging lines that demand high-integrity seals at short dwell times. Terminal products are 200–1000 mL aseptic drink packs, gable-top milk carton liners, and paper-based sachet laminates for cooking sauces that require a 3–4 N/15 mm heat-seal strength at 130 °C per ASTM F2029.

    Agricultural silage-wrap conversion with Taisox LLDPE 3490 is run as a dry-blend operation: 92–97 wt% of the resin is mixed with 5–8 wt% of a 10% UV-stabilizer masterbatch and 0.5–1.5 wt% of a slip/anti-block masterbatch, and the addition ratio is adjusted according to film thickness because a 25 µm film exposed to 18 months of direct sunlight must retain at least 50% of its original elongation at break when tested by ISO 527-3 after 1,500 h accelerated weathering per ISO 4892-2 cycle 1. The industry compliance standard for such covers is EN 13206:2017, which specifies thickness classes, optical properties, and mechanical performance for thermoplastic covering films used in agriculture and horticulture; in the European Union, the resin is supplied under REACH (EC) No 1907/2006, and any silage wrap containing more than 0.1 wt% SVHC must be disclosed under Article 33, while food-contact use for silage that may contact animal feed is not directly covered by FDA 21 CFR 177.1520 unless the film is used as an indirect food-contact article in a packing operation. The downstream production line is a monolayer blown-film extruder with a 2.0 mm die gap, die diameter of 350–500 mm, blow-up ratio of 2.5:1 to 3.5:1, and dual-lip air ring maintaining frost-line height at 400–650 mm; melt temperature is controlled at 190–210 °C, which is low enough to avoid thermal degradation of the UV/HALS masterbatch but high enough to prevent melt fracture at line speeds above 60 m/min. Terminal products include 25–45 µm silage covers, 1.2–1.6 m wide silage bags, and greenhouse side sheets with 150–200 µm thickness where the film is folded by a rotary die and sealed by a continuous hot-wedge sealer at 180–200 °C.

    Taisox 3490 as a Backbone Resin in Heavy-Duty Industrial Sack Film

    For industrial sacks that carry 25–50 kg of polymer resin, cement, or chemicals, Taisox LLDPE 3490 is blended with high-density polyethylene at 70–85 wt% to the LLDPE component and 15–30 wt% HDPE, with the exact ratio set by falling dart impact requirements of ASTM D1709 method A or B and tear resistance per ISO 6383-2; below 70 wt% LLDPE, the film’s penetration energy at -20 °C falls below the minimum specified for clean-room packaging lines, while above 85 wt% LLDPE, Elmendorf tear in the transverse direction increases but the film loses secant modulus below 150 MPa. The regulatory basis for such non-food packaging is REACH (EC) No 1907/2006 Annex XVII restrictions on cadmium and lead in packaging, with Article 33 SVHC disclosure, and Directive 94/62/EC Article 11 for the sum of heavy metals not exceeding 100 mg/kg; if the sack liner is used for indirect food-contact resin packaging, the olefin polymer must meet FDA 21 CFR 177.1520(c) paragraph 3.2a. The production equipment is a high-output blown-film line with a 200–350 mm die, 2.0–2.4 mm die gap, internal bubble cooling, and a blow-up ratio of 2.0:1 to 2.5:1; melt temperature is held at 200–230 °C and output is typically 150–250 kg/h, with a frost-line height of 600–900 mm to avoid strain hardening that would increase TD shrinkage. Terminal products include 25–50 kg valve sacks for polymer pellets, FIBC liners with 80–150 µm wall thickness, and heavy-duty liners for chemicals requiring a 1,500 N/50 mm tensile strength minimum per ISO 527-3.

    If Taisox LLDPE 3490 Is Used as the Sealant Skin in High-Speed Coextruded Lamination Film, Post-Corona Decay Must Be Accounted For

    Coextruded lamination film for detergent or dry-food pouches frequently uses Taisox LLDPE 3490 as the sealant skin at 20–30 wt% of the total film structure, with the core layer consisting of a polypropylene or high-density polyethylene at 40–50 wt% and a tie layer at 10–15 wt%; the major process limitation is the decay of corona treatment, because the surface energy of the sealant layer drops below 38 dynes/cm over 48 h after online treatment at 2.0 kW, making offline lamination or printing unreliable. Compliance for this structure is EU Regulation (EU) No 10/2011 for food contact when dry-food pouches are involved, with migration testing in simulant E per EN 1186-5, and FDA 21 CFR 177.1520(c) for the polyethylene sealant; the outer layer, if printed, is covered by EU 2023/2006 for food-contact printing inks and ISO 22000:2018 clause 8.2.4 for hazard analysis of the laminate structure. The production process is a three-layer coextrusion blown-film line with die gap 2.0 mm, die diameter 300 mm, and blow-up ratio 2.5:1; melt temperatures are separately controlled at 180–190 °C for the sealant skin and 210–230 °C for the PP/HDPE core, and the bubble is collapsed through a secondary nip after 2–3 s residence time; corona treatment is applied at 1.5–2.5 kW immediately after the primary nip, and the film must be laminated or printed within 24–48 h. Terminal products include dry-food pouch laminates of 50–80 µm, detergent bag laminates requiring 12 N/25 mm peel strength per ASTM F904, and frozen-food lamination film where the sealant layer must reach 2.5 N/25 mm hot tack at 120 °C per ASTM F1921.

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    Certification & Compliance
    More Introduction

    Taisox LLDPE 3490 is a linear low-density polyethylene resin supplied for blown-film extrusion and lamination webs. The grade’s primary lot-release values are a density of 0.918 g/cm³ and a melt mass-flow rate of 1.0 g/10 min at 190 °C/2.16 kg under ISO 1133-1:2022. These values place the material below the 0.925 g/cm³ conventional LLDPE/HDPE boundary and in the flow range used for general packaging films. Because the backbone is predominantly linear and carries short-chain branches, the resin exhibits lower melt elasticity than high-pressure LDPE of the same melt flow rate but higher solid-state tensile and tear resistance.

    The comonomer used in this grade is generally identified in commercial documentation as 1-butene. Converters requiring hexene or octene LLDPE should confirm the specific comonomer on the certificate of analysis, because comonomer type affects seal initiation temperature and tear balance in oriented films. Observed converting operations use the grade for bag-in-box liners, collation shrink film, garment packaging, and agricultural films. In these applications, the resin is selected for a combination of melt flow stability and toughness; specific regulatory or performance requirements are determined by the end-use standard, not by the resin data alone.

    What nominal property set is declared for lot release and film conversion?

    Table 1 lists the primary resin specification values. Film-level mechanical properties are dependent on gauge, blow-up ratio, and frost line height, and therefore are not treated as fixed resin lot-release limits.

    PropertyTest methodNominal valueUnit
    DensityISO 1183-1:20190.918g/cm³
    Melt mass-flow rateISO 1133-1:2022, condition D1.0g/10 min
    Melting peak by differential scanning calorimetryISO 11357-3:2018122°C

    The melting peak value is class-typical for an LLDPE of this density and should be confirmed against the specific production lot. Published dart impact, Elmendorf tear, and haze data for Taisox LLDPE 3490 are conversion-dependent; direct comparison between suppliers requires identical film gauge and process geometry.

    Film processing on 45 mm to 75 mm grooved-feed extruders

    Grooved-feed single-screw extruders with screw L/D ratios from 24:1 to 30:1 are used for this grade. A barrel profile of 170 °C, 180 °C, 185 °C, and 190 °C from feed throat to metering section, with die zones at 190 °C to 200 °C, keeps melt temperature between 185 °C and 195 °C. Operation below 170 °C risks unmelt solids and fisheyes; operation above 200 °C increases gel formation and lowers bubble stability. A die temperature variation of ±5 °C around the set point is sufficient to produce gauge bands in high-stalk tubular film.

    Die gap settings between 1.2 mm and 2.0 mm are standard. The smaller die gap reduces shear residence time and melt fracture for LLDPE, while the larger gap is used when LDPE blends are added to increase melt tension. Blow-up ratios of 2.0:1 to 3.0:1 and frost line heights of 4 to 8 die diameters are typical starting conditions.

    The lower melt strength of this resin relative to high-pressure LDPE creates a gauge-stability conflict. Increasing melt temperature from 180 °C to 190 °C lowers head pressure but reduces bubble tension; decreasing melt temperature from 190 °C to 180 °C improves bubble support at the expense of higher torque and back pressure. On a 55 mm grooved-feed extruder running at 80 kg/h, the latter adjustment often raises back pressure by 20 bar to 30 bar. Sustained back pressure above 350 bar should trigger screen pack inspection, because higher pressure increases shear heating and may initiate melt fracture at the die lip.

    Blending with high-pressure LDPE is a standard bubble-stability modification. Addition of 15 wt% LDPE to Taisox LLDPE 3490 raises low-shear melt tension sufficiently for high-stalk film without a large loss in tensile properties. At 30 wt% LDPE, the blend begins to shift seal initiation and stiffness toward LDPE behaviour. Recycled film concentrates containing high-density polyethylene should be controlled because a 1 wt% HDPE contamination can shift blend density upward by approximately 0.002 g/cm³, altering gauge and stiffness.

    When downgauging below 20 µm in high-stalk tubular film

    Below 20 µm, the property differences between this LLDPE and a high-pressure LDPE of identical 1.0 g/10 min MFR become more pronounced. Tensile strength and Elmendorf tear of the LLDPE-rich film normally exceed those of the LDPE film at the same gauge, but haze may be higher unless a clarity additive package is used. Measurements are performed under ASTM D882-18 for tensile properties and ASTM D1922-21 for Elmendorf tear. Dart impact is measured under ASTM D1709-22, Method A, with a 25.4 mm dart and a 660 mm drop height. These tests should be run on conditioned film at 23 °C ± 2 °C and 50 % ± 5 % relative humidity.

    At thicknesses below 12 µm, the linear backbone of the resin reduces melt elasticity further; converters often use 70 wt% Taisox LLDPE 3490 / 30 wt% LDPE blends to maintain bubble stability. In such blends, the LDPE fraction dominates bubble tension and seal initiation, while the LLDPE fraction maintains tensile and puncture resistance. The exact optimum blend ratio depends on the frost line height and die diameter, and must be determined by a designed experiment on the production line.

    Compared with metallocene-catalysed LLDPE of equivalent density, Taisox LLDPE 3490 exhibits a broader molecular weight distribution and lower melt fracture sensitivity at high screw speed. The lower gloss and higher haze of conventional LLDPE are accepted in many industrial films because the processing window is wider. A metallocene grade may require tighter die gap and lower screw speed to avoid sharkskin; a conventional grade such as Taisox LLDPE 3490 is less sensitive to die lip buildup but may retain higher melt elasticity than LDPE. Published film haze and gloss data for this specific grade are limited; converting trials are required for high-clarity packaging.

    In lamination film, seal initiation temperature and hot tack are assessed because the web must seal at high speed after corona treatment. Hot tack is measured under ASTM F1921-20. Corona treatment at 38 mN/m to 42 mN/m is typical for print adhesion on this grade. The lower melting range of a 0.918 g/cm³ LLDPE permits seal initiation in the class-typical range of 90 °C to 100 °C in monolayer films, but the exact value depends on film gauge, additive package, and sealing pressure. Production-scale trials on the intended packaging machine are required before specification.

    Against a high-density polyethylene film resin with a density of 0.945 g/cm³ to 0.955 g/cm³, Taisox LLDPE 3490 has lower modulus and higher stress-crack resistance. HDPE film provides greater moisture barrier and stiffness, but its tear resistance and dart impact are generally lower at equivalent gauge. The choice between the two families is therefore governed by the package’s moisture-vapour transmission requirement, measured under ASTM F1249-20 or ISO 15106-2:2017, and by the required seal-through-contamination performance on high-speed form-fill-seal lines.

    Food-contact verification and resin compliance boundaries

    Food-contact converters must evaluate the finished article, not the resin alone. The base olefin polymer is typically evaluated against U.S. FDA 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011. For EU food-contact articles, overall migration must not exceed 10 mg/dm², with the test conducted under the intended time and temperature conditions. If the converter adds recycled film, non-compliant masterbatch, or processing aids, the compliance status of the final article changes.

    RequirementReferenceTypical acceptance criterion
    U.S. FDA21 CFR 177.1520(c)Olefin polymer, extraction limits
    EU food contactRegulation (EU) No 10/2011Overall migration ≤ 10 mg/dm²
    REACH SVHCRegulation (EC) No 1907/2006SVHC ≤ 0.1 wt% per article
    RoHS restricted substancesDirective 2011/65/EUPb ≤ 1000 mg/kg; Cd ≤ 100 mg/kg

    The resin supplier’s food-contact statement does not transfer automatically to the converted film; the converter controls final composition and process residues. Under REACH, the polymer is generally exempt from registration, but monomer and additive components must be registered where required. Under RoHS Directive 2011/65/EU, lead, cadmium, mercury, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers are controlled at the homogeneous material level with maximum concentration values of 1000 mg/kg for lead and 100 mg/kg for cadmium.

    Controlling moisture and additive migration in long silo residence

    Pre-drying is not normally required for this resin. At relative humidity above 60 %, condensed moisture on pellet surfaces can create steam defects in film; hopper drying at 60 °C for 4 h is sufficient to remove surface moisture. Silo residence times beyond 6 months may increase additive migration and oxidative degradation, particularly if the silo is not purged with dry air. Avoid direct UV exposure and contact with copper-based piping components, which accelerate thermo-oxidative degradation.

    The resin should not be processed with additives that release free radical initiators at melt temperatures above 200 °C, because uncontrolled crosslinking can increase gel levels. In compounding operations, high-shear dispersion of concentrate masterbatches should be performed within the extruder’s recommended torque range and with melt temperature below 220 °C.

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