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Braskem Pluris 4303 Blown Film Extrusion Linear Low Density Polyethylene

    • Product Name: Braskem Pluris 4303 Blown Film Extrusion Linear Low Density Polyethylene
    • 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 141182
    Polymer Type Linear Low Density Polyethylene (LLDPE)
    Melt Index 190 C 2 16 Kg 0.8 g/10 min
    Density 0.924 g/cm³
    Melting Point 124 °C
    Vicat Softening Point 100 °C
    Tensile Strength At Yield 10 MPa
    Tensile Strength At Break 25 MPa
    Elongation At Break 750%
    Dart Drop Impact 120 g
    Elmendorf Tear Strength Md 250 g
    Elmendorf Tear Strength Td 400 g
    Haze 12%
    Gloss 45 55
    Coefficient Of Friction 0.2
    Blocking 20 g

    As an accredited Braskem Pluris 4303 Blown Film Extrusion Linear Low Density Polyethylene factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

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    Application of Braskem Pluris 4303 Blown Film Extrusion Linear Low Density Polyethylene

    In the vertical form-fill-seal (VFFS) packaging of dry granular foods and frozen vegetables, Pluris 4303 is converted into monolayer blown film with the base resin fraction maintained between 95 wt% and 98 wt%, the remaining fraction split among high-melt-strength LDPE, antiblock, slip, and processing aid masterbatches. The grade is a butene-based linear low density polyethylene with nominal density 0.918 g/cm³ and melt flow index 1.0 g/10 min at 190°C/2.16 kg per ISO 1133-1:2022. The formulation addition ratio comprises 2.0 wt% to 4.0 wt% LDPE for bubble stability, 0.10 wt% to 0.30 wt% silica antiblock, 0.05 wt% to 0.12 wt% erucamide slip, and optional fluoropolymer processing aid at 0.10 wt% to 0.30 wt% when melt fracture appears on narrow die gaps. Industry compliance for the final film is evaluated under FDA 21 CFR 177.1520(c) olefin polymer provisions, Commission Regulation (EU) No 10/2011 with overall migration below 10 mg/dm², and Good Manufacturing Practice Regulation (EC) No 2023/2006. Downstream processing uses air-cooled blown film lines with die diameters of 250 mm to 400 mm, die gap 1.8 mm to 2.4 mm, blow-up ratio 2.5:1 to 3.0:1, melt temperature 195°C to 215°C, and frost line height 6 to 8 die diameters. On a 300 mm die at 120 kg/h output, bubble flutter is observed when the LDPE fraction drops below 2.0 wt%, while exceeding 4.0 wt% LDPE reduces dart impact at 60 µm below 90 g per ASTM D1709-16a Method A. The terminal product set includes pillow pouches, gusseted bags, and stand-up pouch inner liners for cereals, frozen peas, and pre-portioned rice, with seal initiation between 95°C and 105°C and hot tack force above 1.8 N/25 mm at 110°C per ASTM F1921-12.

    What Limits Drawdown on High-Versatility Liquid Packaging Lines Using Butene-LLDPE Sealant Webs?

    Sealant webs laminated to BOPP or PET in solventless flexible packaging are produced from Pluris 4303 as a monolayer blown film at 20 µm to 35 µm. The process operates with a die gap above 2.0 mm, blow-up ratio 2.0:1 to 2.5:1, melt temperature 190°C to 205°C, and frost line height 5 to 7 die diameters to preserve low haze. Draw resonance and pinhole formation initiate above 80 m/min unless a high-melt-strength LDPE fraction of 3.0 wt% to 5.0 wt% is added. The additive package comprises 0.15 wt% to 0.25 wt% natural silica antiblock and 0.08 wt% to 0.12 wt% erucamide. Slip loadings above 0.15 wt% generate laminate bond decay below 2.0 N/15 mm after 72 h cure per ASTM F904-16, because slip migration blocks secondary urethane crosslinking in solventless adhesives. In-line corona discharge treatment to 42 dyn/cm to 46 dyn/cm is applied immediately before rewinding; surface energy decays by 6 to 10 dyn/cm within 30 days under 23°C/50% RH storage. Regulatory compliance requires EU Regulation (EU) No 10/2011 Annex III migration screening, FDA 21 CFR 177.1520(c), (EC) No 2023/2006, and REACH SVHC verification under Regulation (EC) No 1907/2006. Terminal webs are used as the inner sealant layer in pouches for liquid detergent sachets, oil sachets, and coffee bricks. For aggressive surfactant packaging, environmental stress crack resistance screening under ASTM D1693-15 Method B is recommended; published data for this specific configuration is limited, and converters should qualify each final laminate under the target filling head temperature and product chemistry.

    Heavy-Duty Sack Extrusion and Creep Resistance Under Stacked Storage

    Industrial sacks for resin pellets, fertilizers, and building additives are extruded from Pluris 4303 at basis weights of 100 µm to 180 µm on blown film dies of 350 mm to 500 mm. The compound is blended with 2.0 wt% to 3.0 wt% carbon black-loaded LLDPE masterbatch for UV stabilization in outdoor storage, and 0.5 wt% to 1.0 wt% fluoropolymer processing aid to reduce melt fracture when die gap is narrowed to 1.8 mm. Process settings include die gap 1.8 mm to 2.4 mm, blow-up ratio 2.0:1 to 2.5:1, melt temperature 200°C to 225°C, and gusseted layflat widths of 400 mm to 600 mm. On production lines crossing 60 m/min, bubble wandering increases thickness variation beyond ±8% and decreases drop impact by 15% to 20%. Mechanical acceptance for non-hazardous bulk goods uses tensile properties per ISO 527-3:2018, dart impact per ASTM D1709-16a, and Elmendorf tear per ASTM D1922-15. When the sack is intended for dangerous goods, UN Model Regulations Chapter 6.5 drop testing at 1.2 m and stacking at 3 m require closure integrity and tear propagation verification; published data for this exact formulation under UN certification is limited. Terminal product types include pinch bottom valve sacks, form-fill-seal pouches on tubular lines, and liner bags for flexible intermediate bulk containers.

    In silage bale wrap production, Pluris 4303 serves as the base polyolefin at 88 wt% to 94 wt%, combined with 0.5 wt% to 1.2 wt% hindered amine light stabilizer masterbatch, 0.2 wt% to 0.5 wt% phenolic/phosphite antioxidant, and 0.5 wt% to 1.5 wt% titanium dioxide or 2.0 wt% to 3.0 wt% carbon black masterbatch depending on UV protection and aesthetic requirements. Cling is developed via 1.0 wt% to 3.0 wt% polyisobutylene masterbatch applied to one surface through an extrusion or surface application step. The blown film line runs a die gap of 1.8 mm to 2.2 mm, blow-up ratio 2.7:1 to 3.2:1, melt temperature 190°C to 210°C, and layflat width 500 mm to 750 mm on towers with frost line height 8 to 12 die diameters. At high blow-up ratio conditions, bubble instability can elevate thickness variation to ±10%, requiring internal bubble cooling set between 10°C and 18°C. For silage bale wrap, EN 14932:2018 specifies tensile elongation at break above 300% in machine direction and above 350% in transverse direction, tear resistance, and UV durability after 12 months outdoor exposure. REACH Annex XVII and Regulation (EC) No 1907/2006 apply to EU market access; the final film is not considered food contact. Terminal product is a 25 µm to 40 µm pre-stretched or conventional silage bale wrap supplied in rolls of 1000 m to 1500 m.

    When Coextruded with EVA and mLLDPE for Frozen Food Surface Gloss

    Three-layer coextruded films for frozen meat, seafood, and ice cream packaging use Pluris 4303 in the core layer at 55 wt% to 65 wt%, while the sealant layer contains 70 wt% to 80 wt% mLLDPE and 20 wt% to 30 wt% EVA, and the outer skin contains 60 wt% to 70 wt% Pluris 4303 with high-clarity mLLDPE. Antiblock addition is 0.10 wt% to 0.20 wt% in the skin only, slip addition 0.05 wt% to 0.10 wt% in the skin only, and process aid 0.10 wt% to 0.20 wt% in the core to manage shear heating. The production line uses a 5-layer die, die gap 1.8 mm, blow-up ratio 2.2:1 to 2.8:1, melt temperature 200°C to 220°C, and a dual-lip air ring with internal bubble cooling set at 8°C to 12°C to stabilize the bubble and raise cooling capacity. For frozen food contact, the finished film must meet FDA 21 CFR 177.1520(c), EU Regulation (EU) No 10/2011 overall migration below 10 mg/dm², and (EC) No 2023/2006. Terminal films of 40 µm to 80 µm are converted into vacuum pouches, tubular ice cream bags, and lidding film with seal initiation 90°C to 100°C. Monolayer Pluris 4303 film has insufficient gloss for high-gloss frozen food displays; the coextruded skin is required because butene-LLDPE gloss at 60° typically falls to 45% to 55%. Published data for this exact coextruded configuration under low-temperature puncture testing ASTM D3763-18 is limited.

    In stretch hood film for pallet unitization, Pluris 4303 is compounded at 80 wt% to 90 wt% with 10 wt% to 20 wt% mLLDPE or high-melt-strength LDPE to raise melt elasticity and with 0.2 wt% to 0.5 wt% UV stabilizer masterbatch for outdoor warehouse exposure. The formulation is processed on large blown film dies of 300 mm to 500 mm, die gap 2.0 mm to 2.5 mm, blow-up ratio 2.2:1 to 2.8:1, melt temperature 200°C to 215°C, and internal bubble cooling set at 12°C to 20°C to stabilize the bubble below the frost line. The process bottleneck is melt pressure buildup at outputs above 200 kg/h, where fluoropolymer processing aid at 0.10 wt% to 0.20 wt% is added to reduce screw amperage and eliminate sharkskin. Mechanical property acceptance follows ISO 527-3:2018 for tensile properties, ASTM D882-18 for secant modulus, and puncture resistance via ASTM D5748-19; load stability for European transport is assessed under EUMOS 40509:2020. Terminal product types are stretch hood films of 60 µm to 100 µm and layflat widths 1.2 m to 2.0 m, used on automatic stretch hood machines to secure pallets of beverages, building materials, and bagged chemicals. Published data for Pluris 4303 under EUMOS 40509:2020 is limited, and converter qualification should include full pallet stability testing under the target wrapping machine.

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