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NOVA Chemicals Sclair VLDPE 10B

    • Product Name: NOVA Chemicals Sclair VLDPE 10B
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@sinochem-nanjing.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 558911
    Polymer Type Very Low Density Polyethylene (VLDPE)
    Comonomer Butene-1
    Density 0.911 g/cm³
    Melt Index 0.8 g/10 min (190°C/2.16 kg)
    Melt Flow Ratio 30
    Tensile Strength At Yield 8.0 MPa
    Tensile Strength At Break 20.0 MPa
    Elongation At Break 700%
    Flexural Modulus 200 MPa
    Vicat Softening Point 90 °C
    Melting Point 120 °C
    Brittleness Temperature -70 °C
    Hardness Shore D 45
    Dart Drop Impact 300 g
    Elmendorf Tear Strength Md 200 g
    Elmendorf Tear Strength Td 300 g
    Haze 10%
    Gloss 70%

    As an accredited NOVA Chemicals Sclair VLDPE 10B factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing NOVA Chemicals Sclair VLDPE 10B is packaged in 25 kg bags, typically 40 bags per pallet (1,000 kg net).
    Container Loading (20′ FCL) NOVA Chemicals Sclair VLDPE 10B loaded in a 20-foot FCL container, with bags/pallets secured for safe ocean transport.
    Shipping NOVA Chemicals Sclair VLDPE 10B is a non-hazardous very low density polyethylene resin supplied as solid pellets in bags or octabins. It is not classified as dangerous goods for transport and requires no UN number, hazard class, or special shipping label; store dry and avoid contamination.
    Storage Store NOVA Chemicals Sclair VLDPE 10B in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep containers tightly closed and protect from moisture, dust, and contamination. Avoid prolonged outdoor exposure. Use appropriate handling equipment and follow the manufacturer’s SDS and local regulations for safe storage and housekeeping.
    Shelf Life Shelf life is generally 24 months from manufacture when stored cool, dry, well-ventilated, and protected from sunlight in original packaging.
    Application of NOVA Chemicals Sclair VLDPE 10B

    Low Seal Initiation Temperature in Coextruded Food-Contact Sealant Webs Expands Line Speeds

    Coextruded three-layer films for vertical form-fill-seal (VFFS) packaging lines running at 120–160 bags/min require a sealant skin that reaches threshold seal strength before the jaw opens. A sealant layer formulated with 60–70 wt% Sclair VLDPE 10B and the balance a 1.0 dg/min metallocene LLDPE lowers the heat seal initiation range relative to a conventional 0.918 g/cm³ LLDPE control. The NOVA Chemicals grade carries a nominal density of 0.910 g/cm³ and a nominal melt index of 0.8 g/10 min tested per ASTM D1238 at 190 °C, 2.16 kg. The lower density fraction reduces the crystalline melting plateau at the seal interface, allowing the sealant to wet and entangle across the seal area under shorter dwell times. The structure is produced on a three-layer blown film line with extruder screw diameters of 50/60/50 mm and L/D ratios of 30:1; the die gap is set at 2.0 mm, the blow-up ratio is 2.2:1, and the frost line is maintained 350–400 mm above the die. The outer skins contain LDPE or HDPE for stiffness and thermal resistance, while the VLDPE 10B sealant layer is air-cooled on the inside. Finished seal strength is tested per ASTM F88 after a dwell time of 0.5 s and 98 °C jaw temperature; the measured seal strength must exceed 7 N/15 mm on a 25 µm total film. For food-contact compliance in the United States, the olefin polymer falls under 21 CFR 177.1520(c)(3.2); compliance with EU Regulation 10/2011 requires migration testing per EN 1186-1 and specific migration limits for additives. Operational boundary: At addition levels above 80 wt%, the sealant skin loses sufficient melt elasticity during bubble expansion, causing gauge variation greater than ±8% on automatic thickness profiling equipment. Published data for this specific configuration are limited; seal initiation temperature must be mapped against actual film gauge, dwell time, and additive package. Target end products are frozen vegetable pouches, snack flow-packs, and dry seasoning pouches.

    What Limits Puncture Propagation Resistance in High-Downgauge Stretch Wrap?

    In cast stretch film lines producing machine film below 12 µm, the transition from 35 µm downgauging has exposed the limits of standard metallocene LLDPE in the core layer. Adding 10–20 wt% Sclair VLDPE 10B into the core layer shifts puncture resistance from brittle crack propagation toward ductile deformation. The VLDPE fraction contributes lower crystallinity and reduces yield stress localization at the point of pallet-edge or fork contact. The cast line is configured with a 35:1 L/D barrier screw, a feedblock distributing 5–8% of total throughput to the cling skins, and a 45–50 °C chill roll with matte finish. Melt temperature at the die is maintained between 240–260 °C to dissolve gel nuclei from the VLDPE fraction without generating low molecular weight oxidation products. Cling force is measured on a 500 mm peel specimen per ASTM D5458; machine-direction elastic recovery and stress retention are recorded per ASTM D5459 at 200% elongation. Protrusion puncture resistance is measured per ASTM D5748 at 250 mm/min crosshead speed. The final film is a 20% pre-stretch machine film or hand film with 150–200% pre-stretch capability. Operational boundary: Addition of VLDPE 10B above 20 wt% in the core reduces machine-direction modulus below acceptable levels for A-grade loads and can increase cling skin transfer on the casting roll. Published converter data for Sclair VLDPE 10B in this exact downgauged structure are limited; the addition window is established on pilot line trials using the target chill roll surface and edge trim ratio.

    Heavy-duty shipping sacks with a 25 kg fill weight often reject on dart impact variation when filled at −18 °C and dropped on a sharp corner. A three-layer blown film structure using a core layer of 20–25 wt% Sclair VLDPE 10B blended with a 0.918 g/cm³ C8-LLDPE and skins of 100% HDPE shifts failure from brittle shattering to ductile puncture. The core-layer single-screw extruder operates with a 30:1 L/D screw and a Maddock mixer; melt pressure at the screen pack is held below 420 bar to avoid excessive melt fracture of the VLDPE-rich melt. The die gap is set at 2.2 mm, the BUR at 2.4:1, and the layflat width at 750 mm. Dart impact is measured per ASTM D1709 Method A on the finished sack wall after conditioning for 40 h at −20 °C. Tear propagation is measured per ASTM D1922. The final sacks are printed flexographically and converted on a bottom-gusset line; the VLDPE-containing core reduces the incidence of side-seal splits during filling by 15–20% in plant trials, although that range varies with fill speed and sack dimensions. The grade is not recommended for outdoor storage beyond 12 months without UV stabilizer masterbatch; exposure to UV above 300 nm causes chain scission and loss of impact strength. REACH compliance is documented through a supplier SDS; the resin does not contain substances of very high concern above 0.1% w/w as declared. Quantitative public literature for Sclair VLDPE 10B in this exact multilayer heavy-duty sack is sparse, so converter qualification should use the actual gusset geometry, fill weight, and drop profile.

    When Frozen Food Film Must Retain Seal Integrity After −40 °C Storage and Abrasion

    For frozen dumpling and prepared vegetable films stored at −25 °C and handled in distribution at temperatures as low as −40 °C, a three-layer frozen-food film uses a sealant layer of 70 wt% Sclair VLDPE 10B, 20 wt% LDPE with 0.3 dg/min melt index, and 10 wt% silica antiblock masterbatch. The VLDPE 10B fraction lowers the amorphous-phase mobility transition enough to preserve impact strength at low temperature, provided the film is not over-oriented during blown film fabrication. The die gap is set at 1.8 mm, the BUR at 2.0:1, and the melt temperature at 210 °C. A high frost line of 450–500 mm is maintained to reduce frozen-in orientation and improve flex-crack resistance. Gelbo flex testing is performed per ASTM F392 at 500 cycles and −20 °C; acceptable films show no pinholes larger than 0.5 mm. Dart impact is measured per ASTM D1709 on the finished film after 24 h conditioning at −25 °C. Seal strength after a drop of oil or water on the sealant is measured per ASTM F88; the caulkability of the VLDPE-rich seal layer is what allows seal integrity through contamination. EU food-contact compliance requires overall migration below 10 mg/dm² per EN 1186-1. The final products are 250–500 g frozen food pouches, printed on the outer surface and back-sealed on a vertical form-fill-seal line. Operational boundary: The VLDPE 10B-rich sealant is not suitable as the print web without corona treatment to 38–42 mN/m, and even then adhesion to water-based inks is weaker than on LDPE. Published data for this specific grade in frozen food sealant layers at −40 °C are limited; low-temperature seal strength must be qualified on the target line because dwell time, jaw pressure, and fill temperature shift the failure mode.

    On liquid sachet filling lines, a sealant layer containing 50–60 wt% Sclair VLDPE 10B and 40–50 wt% LDPE is used for soy sauce, cream, and cosmetic sample packaging. The line runs a three-layer blown film die with internal bubble cooling and a 50 mm central extruder; the outer layer is a polyethylene-based print web, and the sealant layer is plasma-treated to 42 mN/m before lamination. Seal-through-contamination behavior is critical because the filling head leaves a fine aerosol of oil on the seal area. The VLDPE 10B fraction deforms at the seal interface at lower temperature than LDPE, filling irregular gaps caused by liquid residue. Seal strength is tested per ASTM F88 after intentionally contaminating the seal area with 2 µL of soybean oil; the failure mode must be seal peeling, not film peeling or transfer. In addition to 21 CFR 177.1520(c)(3.2), the structure must meet EU 10/2011 migration rules for fatty food simulant D2. The finished sachets range from 8 mL to 35 mL, produced on horizontal and vertical fill-seal machines at 80–120 cycles/min. Processing limitation: At line speeds above 120 cycles/min, seal dwell time drops below 0.3 s, and the VLDPE-rich sealant requires higher jaw temperature to compensate; if jaw temperature exceeds 135 °C, the outer printed layer tends to block, so the practical upper throughput is bounded by the barrier layer polymer choice.

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