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PetroChina Daqing KunLun mLLDPE DQLV0810

    • Product Name: PetroChina Daqing KunLun mLLDPE DQLV0810
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 504373
    Polymer Type Metallocene linear low-density polyethylene (mLLDPE)
    Density 0.918 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.8 g/10 min
    Tensile Strength At Break ≥20 MPa
    Elongation At Break ≥500%
    Dart Impact Strength ≥800 g
    Haze ≤6%
    Gloss 45 ≥80
    Melting Point 118°C
    Vicat Softening Temperature ≥100°C
    Brittleness Temperature ≤-70°C
    Molecular Weight Distribution Narrow
    Comonomer 1-Hexene
    Catalyst Metallocene

    As an accredited PetroChina Daqing KunLun mLLDPE DQLV0810 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PetroChina Daqing KunLun mLLDPE DQLV0810 is supplied in 25 kg PP woven bags with moisture-barrier liners and labeled pallets.
    Container Loading (20′ FCL) PetroChina Daqing KunLun mLLDPE DQLV0810 in 25 kg bags, securely loaded into a 20′ FCL container for export shipment.
    Shipping PetroChina Daqing KunLun mLLDPE DQLV0810 is shipped as non-hazardous metallocene linear low-density polyethylene resin, not regulated for transport. It is supplied in moisture-barrier 25 kg bags or jumbo bags, palletized and shrink-wrapped, with product, grade, lot, and handling labels. Keep dry and avoid prolonged sunlight or heat.
    Storage Store PetroChina Daqing KunLun mLLDPE DQLV0810 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, moisture, and strong oxidizers. Keep in original sealed bags on pallets; avoid punctures, dust, and prolonged high temperatures. Protect from UV exposure and mechanical damage. Use first-in, first-out, keep containers closed and labeled, and follow local regulations.
    Shelf Life Typical shelf life is 24 months in unopened original packaging, stored dry, away from direct sunlight and heat.
    Application of PetroChina Daqing KunLun mLLDPE DQLV0810

    Modification of low-temperature sealant webs for quick-frozen food packaging with 10–30 wt% PetroChina Daqing KunLun mLLDPE DQLV0810 is carried out on three-layer air-cooled blown-film lines equipped with 30:1 L/D single-screw extruders and grooved feed sections. The resin is dosed into the sealant layer, while the core and outer layers remain Ziegler-Natta LLDPE or LLDPE/LDPE combinations; a common layer ratio is 1:2:1 or 1:1.5:1 with a total film gauge of 40–80 µm. On production lines, the die gap is maintained at 2.0–2.8 mm, the blow-up ratio is 2.5–3.2, and the frost line is kept 500–900 mm above the die face to stabilize bubble geometry. Corona discharge treatment to 42–46 mN/m is applied before lamination or printing. The metallocene architecture reduces heat-seal initiation temperature relative to conventional butene LLDPE by approximately 5–10 °C, and the sealant layer shows improved hot-tack strength under ASTM F1921 and seal strength under ASTM F88; however, published data for this exact grade in frozen food formulations is limited, so converter qualification trials should confirm these values for each film structure. Food-contact compliance is established under FDA 21 CFR 177.1520(c) for olefin polymers, EU Regulation 10/2011 with overall migration below 10 mg/dm², and China GB 4806.7-2016; specific migration limits for additives must be verified against the masterbatch and layer composition. The terminal formats include quick-frozen vegetable pouches, IQF seafood bags, frozen meat packaging, gusseted freezer bags, and pillow packs for ice cream or frozen confectionery—structures that require low-temperature seal integrity after exposure to -25 °C and repeated flexing.

    Which Sealant-Layer Variables Govern Hot-Tack Retention at High-Speed Vertical Form-Fill-Seal Output?

    High-speed vertical form-fill-seal (VFFS) operation demands a sealant layer formulated with 20–40 wt% DQLV0810 to widen the hot-tack plateau under short dwell times. The film is produced as a three-layer coextruded web, then printed and laminated or used as an unsupported inner web. The addition level is concentrated in the sealant side; the outer side may be an HDPE-rich layer for stiffness. Processing on VFFS lines with seal jaw dwell below 100 ms requires stable coefficient of friction in the range 0.25–0.35 to maintain film transport without slip-lip on forming tubes. Hot-tack testing under ASTM F1921 is performed at sealing temperatures 105–130 °C, with seal bar force 0.3–0.6 N/mm², to characterize the temperature window in which the seal remains intact before solidification. Heat seal strength is measured after cooling according to ASTM F88. The formulation reduces seal initiation by 5–10 °C compared with Ziegler-Natta LLDPE, but the exact shift depends on the core layer thickness and the presence of slip and antiblock additives. Compliance follows FDA 21 CFR 177.1520, EU Regulation 10/2011, and GB 9685-2016 only if the selected slip/antiblock masterbatch meets the positive-list restrictions. Terminal products include stand-up pouches for dry snacks, pillow packs for powders, gusseted pouches for frozen prepared meals, and VFFS packs for granular instant beverages.

    ApplicationPrimary compliance referenceTypical verification parameter
    Frozen food sealant webFDA 21 CFR 177.1520(c); EU 10/2011; GB 4806.7-2016Overall migration < 10 mg/dm²
    VFFS hot-tack filmFDA 21 CFR 177.1520; EU 10/2011; GB 9685-2016Seal strength ASTM F88; hot tack ASTM F1921
    Cast stretch filmREACH; RoHS 2011/65/EUCling ASTM D5458; puncture ASTM D5748
    Agricultural silage filmEN 13206:2017; REACHTear ASTM D1922; dart ASTM D1709 Method A
    Heavy-duty sack filmREACH; RoHS 2011/65/EUDrop ISO 7965-2
    Collation shrink filmEU 10/2011 where relevant; REACHTear ASTM D1922; tensile ISO 527-3

    When pallet unitization requires high elongation and consistent cling, the cast stretch film core layer is modified with 15–35 wt% DQLV0810, while the skin layers may contain 2–4 wt% low-molecular-weight cling additive or ethylene-vinyl acetate copolymer to achieve differential cling and slip. The process uses a multi-layer cast line with an annular or flat die, a chill roll temperature of 15–25 °C, and a die-to-chill roll distance below 25 mm to minimize neck-in and edge instability. Vacuum box or air knife pinning is adjusted during line acceleration to prevent air entrapment at speeds above 600 m/min. The mLLDPE in the core contributes to high elongation at break and puncture resistance but may reduce machine-direction tear; therefore, the core formulation often includes 5–10 wt% LLDPE or LDPE to retain processability. Tensile properties are tested under ISO 527-3 or ASTM D882, puncture resistance under ASTM D5748, and cling by ASTM D5458. Industrial stretch film is not a direct food-contact application unless separately evaluated under EU Regulation 10/2011 or FDA 21 CFR 177.1520; REACH registration and RoHS 2011/65/EU apply for heavy-metal and restricted-substance compliance. Terminal products include machine stretch film for high-speed automatic wrappers, power pre-stretch film for rotating ring wrappers, hand wrap, and vented pallet wrapping structures.

    When Agricultural Silage Bale Film Must Retain Tear Resistance After Field UV Exposure

    Agricultural silage bale wrap and clamp film using 20–35 wt% DQLV0810 in a three-layer structure is extruded on blown-film lines with die diameters from 200–400 mm and die gaps 1.6–2.4 mm. The black formulation contains carbon black masterbatch at 3–5 wt% and a hindered amine light stabilizer package at 0.4–0.8 wt% to withstand outdoor UV exposure for 12–24 months in temperate climates. Layer distribution is often 1:2:1, with the core carrying the carbon black and the skins modified with mLLDPE for puncture and tear. The bubble is run at a blow-up ratio of 2.5–3.5 to balance machine-direction and transverse-direction tear; frost line height is raised to 700–1100 mm to reduce film blocking on the reel. Tear resistance is tested according to ASTM D1922, tensile properties according to ISO 527-3, and dart impact using ASTM D1709 Method A. The agricultural film must meet EN 13206:2017 covering-film specifications and REACH restrictions; if the film is later used for direct fermentation wrap of feed crops, silage leachate contact falls outside food-contact frameworks and requires national regulations for agricultural plastics. Operational boundaries include avoiding carbon black masterbatches with oversized agglomerates above 20 µm when total film thickness is below 25 µm, because thick-black specks can initiate tear propagation. Terminal formats include round bale stretch film, large square bale wrap, clamp silage sheets, and silage bunker covers.

    Heavy-Duty Sack Sealant and Dart Impact Retention in Continuous Form-Fill-Process Granulate Packaging

    To improve dart impact retention in filled sacks, form-fill-seal sack production uses 15–30 wt% DQLV0810 in the sealant skin of a 3-layer coextruded heavy-duty sack film. The outer skin is typically HDPE or HDPE/LLDPE for stiffness, and the core may contain in-house trim. The film is blown on a high-output line with internal bubble cooling, oscillating haul-off, and a die gap of 1.8–2.6 mm, producing film thickness of 120–200 µm. Heat sealing on FFS equipment is performed with platen temperatures 130–160 °C and dwell 0.5–1.5 s; the mLLDPE skin creates a seal that withstands drop impact during transportation of filled sacks. Dart impact resistance is assessed under ASTM D1709 Method A, tensile properties under ISO 527-3 or ASTM D882, and filled-sack drop testing under ISO 7965-2. Industrial packaging systems are qualified according to converter quality controls under ISO 9001; REACH and RoHS 2011/65/EU apply to heavy-metal and restricted-substance compliance. Direct food contact is not intended unless the specific film passes EU 10/2011 or FDA 21 CFR 177.1520. Terminal product types include 25 kg polymer granulate sacks, fertilizer bags, mineral filler bags, cementitious dry mortar bags, and petrochemical resin packaging.

    For collation shrink film used in bottle multipacks, the blend is modified with 20–30 wt% DQLV0810 in the core or both skins to raise puncture resistance during tunnel shrink and maintain weld seal integrity after shrinking. The film is produced by high-stalk blown-film extrusion at a blow-up ratio of 3.0–3.5, followed by intentional orientation in both directions through hot-air bubble collapse and a secondary bubble process; the resulting film thickness is 45–70 µm. Shrink tunnels operate with air temperatures 160–200 °C, requiring seal strength retention and sufficient low-temperature impact after shrinking; ASTM D1922 and ISO 527-3 are used for tear and tensile verification. The formulation must be limited to 3–6 wt% silicone-free slip agent if the film is later corona-treated and printed, because excess slip can cause ink adhesion failure. Regulatory compliance involves EU Regulation 10/2011 only where direct contact with packaged beverage containers is not considered food contact; otherwise REACH and RoHS 2011/65/EU apply to packaging. Terminal products include shrink-wrapped multipacks of bottled water, canned goods, aseptic beverage carton multipacks, and insulated cup sets.

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    Certification & Compliance
    More Introduction

    PetroChina Daqing KunLun mLLDPE DQLV0810 is a metallocene-catalyzed linear low-density polyethylene supplied in pellet form for blown-film, cast-film, and extrusion-lamination conversion. Commercially published typical values for the grade place melt flow rate at 1.0 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg and nominal density at 0.918 g/cm³ under ISO 1183-1:2019. These two values position the resin in the high-toughness film-sealing segment; lot-specific release data on the certificate of analysis may vary within the producer’s control limits. Because polymerization uses a metallocene single-site catalyst, the short-chain branching distribution is more homogeneous than in conventional Ziegler-Natta linear-low-density polyethylene of similar density.

    What Limits the Processing Window for DQLV0810 in Monolayer Blown Film?

    On monolayer blown-film lines, the practical operating boundaries emerge from three interacting parameters: die gap, air-ring stability, and melt temperature. Metallocene LLDPE resins with a melt index near 1.0 g/10 min typically exhibit lower critical shear rates for sharkskin melt fracture than Ziegler-Natta grades at the same melt index. When DQLV0810 is run through a 40 mm to 65 mm single-screw extruder with a 24:1 to 30:1 L/D ratio and a LLDPE barrier screw, melt temperatures between 190 °C and 230 °C are common. A die gap of 1.5 mm to 2.2 mm is often specified for monolayer film; gaps below 1.2 mm increase the probability of melt fracture unless higher die temperatures or processing aids are applied. Frost-line height is typically maintained at 6 to 10 die diameters, depending on air-ring design and tower height. Blow-up ratios between 2.0:1 and 3.0:1 are used to orient the film in both directions; higher blow-up ratios raise transverse-direction tear resistance but can destabilize the bubble because of the resin’s narrow molecular weight distribution. Field observations from blown-film campaigns indicate that switching from a conventional Ziegler-Natta LLDPE of equivalent density to DQLV0810 can increase extruder head pressure by 10% to 20% at constant screw speed, which makes screen-changer pressure alarms and die-body pressure ratings the primary constraints rather than motor load. Pre-drying is not required for moisture removal because the resin is non-hygroscopic; however, pellet surfaces should be brought to ambient temperature before handling to avoid condensation at relative humidities above 60%.

    Unlike Ziegler-Natta linear-low-density polyethylene, which produces a heterogeneous distribution of inter- and intramolecular comonomer placement, DQLV0810 is synthesized with a single-site metallocene catalyst. This changes the solid-state morphology and the melt-extensional behaviour. In gel permeation chromatography of metallocene LLDPE resins, published polydispersity indices are commonly in the range of 2.0 to 3.0, whereas conventional LLDPE grades often fall between 3.5 and 5.0 when measured by ISO 16014; for DQLV0810, the producer’s open datasheet may not report a lot-specific molecular weight distribution, and published GPC values for this specific configuration are limited. The homogeneous branching distribution reduces the concentration of low-molecular-weight, high-comonomer fractions that plasticize the amorphous phase and increase extractables. As a result, blown film from DQLV0810 can be sealed at a lower temperature than a Ziegler-Natta LLDPE of the same nominal density because the crystalline melting distribution is narrower and the surface of the seal layer reaches the softening point more uniformly. This effect is not unique to DQLV0810 but is characteristic of metallocene LLDPE chemistry.

    Compared with high-pressure low-density polyethylene, DQLV0810 has fewer long-chain branches and lower melt strength in elongational flow, which limits its use as a pure high-stalk resin but improves draw-down in cast film. Compared with metallocene LLDPE grades at density 0.912 g/cm³, the 0.918 g/cm³ nominal density lowers dart impact slightly but raises secant modulus measured by ASTM D882; compared with 0.924 g/cm³ metallocene grades, it provides lower seal initiation and better puncture resistance, but lower stiffness. These differences make the grade a mid-range sealing-layer resin rather than a high-modulus or ultra-low-temperature sealant.

    Mechanical, Optical, and Seal Performance Parameters for 40 µm Film

    Film property data for metallocene LLDPE are sensitive to gauge, draw-down ratio, and cooling rate; therefore, comparisons should be made only when specimen preparation is stated. For 40 µm monolayer blown film produced under a 2.5:1 blow-up ratio and a frost-line height of 8 die diameters, published property ranges for mLLDPE of 1.0 MI / 0.918 g/cm³ include dart impact values measured by ASTM D1709A that exceed those of a Ziegler-Natta LLDPE of the same density by approximately 30% to 60%, Elmendorf tear strengths by ASTM D1922 that may be higher in the machine direction but lower in the transverse direction depending on blow-up ratio, and haze by ASTM D1003 that is commonly 30% to 50% lower. Seal initiation temperature, defined as the point at which a seal strength of 4.4 N/15 mm is reached on a laboratory heat sealer, is typically 8 °C to 12 °C lower for metallocene LLDPE than for conventional LLDPE at the same density. Because these are cross-resin comparisons rather than DQLV0810-specific certificates, lot-specific tensile yield, elongation at break, and puncture resistance should be obtained from the producer’s technical data sheet. Published data for DQLV0810-specific mechanical values under all film fabrication conditions is limited.

    Property Test method Comparative observation
    Melt flow rate ISO 1133-1:2022 DQLV0810 nominal 1.0 g/10 min; conventional Ziegler-Natta LLDPE of equal melt index also 1.0 g/10 min
    Density ISO 1183-1:2019 DQLV0810 nominal 0.918 g/cm³; conventional LLDPE equivalent
    Dart impact ASTM D1709A mLLDPE higher by 30% to 60% at 40 µm; no single published DQLV0810 absolute
    Elmendorf tear MD/TD ASTM D1922 Machine direction often higher; transverse direction depends on blow-up ratio
    Seal initiation 4.4 N/15 mm criterion mLLDPE lower by 8 °C to 12 °C versus conventional LLDPE of equal density
    Haze ASTM D1003 mLLDPE lower by 30% to 50% in published cross-resin comparisons
    Hexane extractables 21 CFR 177.1520 related extraction Metallocene grades typically lower extractable fraction than Ziegler-Natta LLDPE of equal density

    In cast-film and extrusion-lamination operations, DQLV0810 is processed at melt temperatures between 230 °C and 275 °C. The narrower molecular weight distribution reduces draw resonance amplitude compared with broader-distribution LLDPE at the same line speed, but neck-in behaviour is a function of both resin elasticity and air-gap length. On cast-film lines using a 0.5 mm to 0.8 mm die gap and air-knife-assisted pinning, line speeds above 150 m/min can be achieved if the extruder is sized for the output; published data for this specific configuration is limited. Because mLLDPE does not contain high levels of low-molecular-weight waxes, it is used in sealant layers of multilayer films where low seal initiation and reduced seal contamination are required. It is not supplied as a single solution for high-stiffness applications, because the density of 0.918 g/cm³ produces lower secant modulus than high-density polyethylene or polypropylene. Slip and antiblock additives are typically introduced via masterbatch at 0.5 wt% to 2.0 wt% to control coefficient of friction measured by ASTM D1894 and blocking behaviour at the unwind.

    When DQLV0810 Replaces Conventional LLDPE in High-Stalk Blown Film Lines

    In high-stalk extrusion lines running conventional LLDPE at a given die, a direct substitution of DQLV0810 requires evaluation of bubble stability and frost-line morphology. Because metallocene LLDPE has lower melt strength in some elongational regimes than low-density polyethylene but a more uniform extensional flow than Ziegler-Natta LLDPE, the stalk height may need to be adjusted to prevent bubble instability. Processors have reported that high-stalk lines optimized for LDPE-rich blends may exhibit unstable free-surface deformation when mLLDPE exceeds 70 wt% in the blend, unless air-ring adjustment or die-temperature profiling is applied. For DQLV0810 in high-stalk monolayer structures, a die gap of 2.0 mm or above and a blow-up ratio below 2.5:1 are common starting conditions. On a 90 mm extruder with a 30:1 L/D barrier screw, processing at melt temperatures of 200 °C to 220 °C and a screen pack of 60/80/100 mesh can control initial pressure, but the melt pressure at the die entrance should not exceed the die manufacturer’s maximum rating. Adding a polymer processing aid at 200 ppm to 600 ppm may be required to delay sharkskin at high output rates; fluorine-based processing aids are common, but their loading should be kept below the supplier’s maximum to avoid surface plate-out.

    Food-contact compliance for DQLV0810 is not a single-property declaration. The resin is an olefin polymer within the scope of 21 CFR 177.1520 when used in the United States, but the specific paragraph and end-use restrictions depend on the extraction test results and the food type. For European Union applications, compliance with Regulation (EU) No 10/2011 requires overall migration testing according to EN 1186 series and specific migration testing where applicable. REACH registration under EC No 1907/2006 applies to substances imported or manufactured in the EU; the producer’s safety data sheet should state the registration status for the grade. RoHS Directive 2011/65/EU Annex II restrictions are relevant only if the final article falls within an electrical and electronic equipment category. DQLV0810 should not be blended with pro-oxidant additives if the film is intended for food-contact use, because degradation products may violate migration limits. Avoid storage exceeding 40 °C and direct sunlight, which can increase odor and discoloration through thermo-oxidative degradation.

    Compliance reference Applicability Verification
    21 CFR 177.1520 Olefin polymer clearances for food-contact use in the United States Producer declaration and extraction testing per cited paragraph
    Regulation (EU) No 10/2011 Plastic food-contact materials in the European Union Overall migration via EN 1186 series; specific migration where applicable
    EC No 1907/2006 REACH registration and safe use information Safety data sheet and registration status
    2011/65/EU RoHS restricted substances in electrical and electronic equipment Article-category dependent; not a resin-level universal declaration

    Heavy-duty packaging, frozen food films, and form-fill-seal structures are conversion areas where the lower seal initiation temperature of DQLV0810 is used to reduce heat-seal dwell time on vertical form-fill-seal machines. In vertical form-fill-seal packaging, a decrease in seal initiation of 8 °C to 12 °C relative to a Ziegler-Natta LLDPE of equal density can allow a reduction in sealing-bar setpoint or an increase in cycle speed, provided the seal-bar pressure and dwell time are characterized. On rotary fill-seal equipment, the resin’s narrow melting distribution reduces the occurrence of stringing and seal contamination compared with broader-distribution LLDPE, but screw speed and back pressure should be adjusted to avoid overheating. These operational benefits are contingent on the additive package, film gauge, and lamination structure; the producer’s technical service bulletin should be consulted for the specific DQLV0810 lot. Published data for this specific configuration is limited.

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