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UBE UMERIT mLLDPE 4040F

    • Product Name: UBE UMERIT mLLDPE 4040F
    • 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 196139
    Manufacturer UBE
    Product Name UMERIT mLLDPE 4040F
    Polymer Type Metallocene Linear Low Density Polyethylene (mLLDPE)
    Density 0.940 g/cm³
    Melt Flow Rate Mfr 4.0 g/10 min (190°C, 2.16 kg)
    Melting Point 125 °C
    Vicat Softening Point 107 °C
    Tensile Strength At Break 20 MPa
    Elongation At Break 800%
    Tensile Modulus 400 MPa
    Hardness Shore D 55
    Haze 1.5%
    Gloss 45 100%
    Dart Impact Strength 100 g
    Tear Strength Md 100 N/mm
    Tear Strength Td 120 N/mm
    Coefficient Of Friction 0.2

    As an accredited UBE UMERIT mLLDPE 4040F factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing UBE UMERIT mLLDPE 4040F is packaged in 25 kg moisture-resistant paper bags, palletized and shrink-wrapped for industrial shipment.
    Container Loading (20′ FCL) UBE UMERIT mLLDPE 4040F loaded in 25 kg bags into a 20-foot FCL container, palletized, dry, and securely stowed for export.
    Shipping UBE UMERIT mLLDPE 4040F is supplied as non-hazardous polyethylene resin pellets, packed in moisture-barrier bags or octabins on pallets. Ship in clean, dry containers at ambient temperature, protected from sunlight, heat, moisture, and contamination. Handle with care to avoid bag damage, in accordance with the SDS and applicable transport regulations.
    Storage Store UBE UMERIT mLLDPE 4040F in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and strong oxidizing agents. Keep original bags or containers closed, clean, dry, and palletized to prevent moisture pickup and contamination. Avoid prolonged outdoor exposure, excessive stacking, and damage; follow the manufacturer’s safety data sheet and local storage regulations. Use first-in, first-out stock rotation.
    Shelf Life Typically two years from manufacture when stored unopened in original packaging, below 40°C, away from direct sunlight and moisture.
    Application of UBE UMERIT mLLDPE 4040F

    On a three-layer blown film line equipped with 55/65/55 mm extruders and a 200 mm annular die, UMERIT 4040F is dry-blended into the inner and outer layers of heavy-duty industrial sack film at 20–35 wt% against a butene-based LLDPE carrier. This addition range is selected because supplier technical data for metallocene LLDPE-modified blown films demonstrate a 30–50% increase in dart drop impact relative to an unmodified butene-LLDPE control at equal thickness when tested under ASTM D1709-22 Method A; the exact movement depends on carrier resin melt index, die gap, and frost line height. The use of 4040F in the sealant side also lowers seal initiation temperature sufficiently to permit jaw temperatures of 115–125°C at line speeds of 40–55 m/min without leaker rates rising above 0.3% on multi-wall sack qualification runs. Compliance for non-food industrial packaging is governed by REACH (EC) No 1907/2006 SVHC restrictions and, where food additives are bagged, by FDA 21 CFR §177.1520(c) 3.2a and EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm². The film is produced via three-layer coextrusion with a blow-up ratio of 2.0:1–2.5:1, a die gap of 1.8–2.4 mm, and a frost line height set at 5–7 die diameters; the finished product is converted into gusseted or flat multi-wall sacks for 25–50 kg resin pellets, fertilizers, and mineral fillers. Field observation indicates that above 35 wt% 4040F, bubble stability becomes problematic on older lines without internal bubble cooling, and film blocking increases unless 500–1,000 ppm silica-based antiblock is included. This operational boundary is not a chemical incompatibility but a processing constraint arising from the resin’s narrow molecular weight distribution and the higher shear viscosity of metallocene LLDPE relative to an equivalent-melt-index traditional LLDPE.

    Why Does Seal Integrity Decline Below -25°C in Frozen Food Packaging?

    The dominant failure mode in frozen food packaging is not tensile rupture but channel leakers along the seal at temperatures below -25°C due to sealant layer stiffening. UMERIT 4040F is introduced into the sealant layer of coextruded blown film at 15–25 wt% with a low-density carrier resin, while the core and outer layers retain a butene-LLDPE or LDPE-rich formulation. The addition ratio is bounded by hot-tack performance under ASTM F1921-18 Method B and seal strength under ASTM F2029-16; at 20 wt%, processor qualification data show a plateau in hot-tack force between 110°C and 130°C, which supports sealing through residual frost and surface moisture on vertical form-fill-seal lines. Compliance for direct food contact requires FDA 21 CFR §177.1520(c) 3.2a, EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm², and EC 1935/2004 Article 3 for organoleptic neutrality. Downstream processing uses two-layer or three-layer blown film extrusion with a 1.8–2.0 mm die gap, a blow-up ratio of 2.5:1–3.0:1, and melt temperatures no higher than 195–210°C to prevent sealant layer degradation; internal bubble cooling is used to stabilize the bubble because 4040F reduces melt elasticity. Finished product types include IQF vegetable and seafood bags, frozen meat pouches, and ice cream overwrap films, all in the 40–80 µm range. A processing boundary is observed below -30°C: coextruded films with less than 15 wt% 4040F lose seal impact integrity unless seal geometry is widened or the sealant layer is thickened.

    Where horizontal form-fill-seal lines exceed 60 cycles/min, the sealant web must deliver consistent slip, low seal initiation, and high hot-tack without sacrificing stiffness, and UMERIT 4040F is dry-blended into the middle and sealant layers of coextruded liquid pouch structures at 25–40 wt%. The film structure typically uses a surface layer of a butene-LLDPE or LDPE for external abuse resistance and a sealant layer containing 4040F; the dry blend avoids the added heat history of compound-pellet conversion and preserves the resin’s narrow molecular weight distribution. Seal strength is verified under ASTM F88/F88M-21, coefficient of friction under ASTM D1894-24, and flex-crack resistance under ASTM F392/F392M-23; a production benchmark for such pouches is a seal strength above 10 N/25 mm at 130°C jaw temperature, though published data for this specific configuration is limited and must be confirmed on line. The applicable compliance set includes FDA 21 CFR §177.1520(c) 3.2a and EU Regulation (EU) No 10/2011 for food-contact bag-in-box inner liners, while detergent and non-food chemical pouches follow REACH (EC) No 1907/2006 and may require additional compatibility testing under ASTM D543-20. Converters run this film on three-layer blown film equipment with a die gap of 1.6–2.0 mm, a blow-up ratio of 2.0:1–2.5:1, and barrel temperatures from 175°C to 215°C; the finished products are flexible liquid detergent pouches, bag-in-box liners for dairy and edible oils, and industrial fluid liners.

    Agricultural Silage and Greenhouse Film: Haze, UV, and Tear Propagation

    Agricultural silage covers and greenhouse cladding require a blend in which metallocene LLDPE contributes tear propagation resistance and low-temperature flexibility without increasing haze beyond the crop’s light transmission requirements. UMERIT 4040F is incorporated at 10–20 wt% into an EVA/LDPE carrier blend; this ratio is kept below 20 wt% because higher loadings reduce the efficiency of UV stabilizer packages and increase film stiffness at the expense of folding behavior on field wrapping machines. Tear propagation resistance is tested under ISO 6383-2:1983, light transmission and haze under ASTM D1003-21, and accelerated weathering under ISO 4892-2:2013; the film must retain at least 50% of original elongation after 3,000 hours of xenon-arc exposure for multi-season greenhouse use, though the specific stabilizer system, not the base resin, controls that retention. Compliance is framed by REACH (EC) No 1907/2006 for the stabilizer package and, for silage films in the EU, by national specifications such as UNI 9298:2009 where required in Italian markets. Production occurs on three-layer blown film lines with a 250 mm annular die, a die gap of 1.8–2.2 mm, a blow-up ratio of 2.5:1, and a frost line height adjusted to balance bubble expansion and quench-induced haze. Finished products include 150–200 µm silage covers, bale wrap films, and 180 µm greenhouse cladding. An operational boundary applies in tropical high-UV environments: the film must be checked for gel formation after 500 hours of continuous extrusion because metallocene resins with narrow molecular weight distribution are less forgiving of temperature overshoot in the metering zone.

    When Stretch Hood Formulations Exceed 30 wt% mLLDPE

    The decision to push UMERIT 4040F content beyond 30 wt% in stretch hood film creates a measurable trade-off between puncture resistance and bubble stability on three-layer blown film lines. At 20–30 wt%, the resin raises machine-direction tear resistance under ISO 6383-1:2015 and dart drop impact under ASTM D1709-22 Method A while retaining enough melt strength for a blow-up ratio of 2.5:1–3.0:1. Above 30 wt%, the narrow molecular weight distribution of metallocene LLDPE reduces extensional viscosity, leading to bubble fluttering and gauge variation greater than ±8% unless the line is equipped with internal bubble cooling, a high-pressure dual-lip air ring, and automatic gauge control with die-bolt mapping on a 250–300 mm die. Processors running 35 wt% 4040F typically reduce die gap to 1.6–1.8 mm and set melt temperature at 185–205°C to increase shear heating and stabilize the frost line at 6–8 die diameters. The addition ratio is validated by puncture resistance under ASTM D5748-19, elongation at break under ISO 527-3:2018, and cling performance under ASTM D5458-95(2020) for wrap retention. Compliance for transit packaging is based on REACH (EC) No 1907/2006 and, where recycled content is incorporated, on ISO 14021:2016 for environmental claims. The end product is stretch hood film in the 80–120 µm range used to secure palletized building materials, paper rolls, and appliance cartons. The operational boundary is explicit: without internal bubble cooling, 4040F loadings above 30 wt% cause unacceptable bubble instability, and cling additives may migrate to the film surface within 48 hours if masterbatch dosing exceeds 2 wt%.

    Chemical Pouch Sealant Webs Under Biaxial Orientation Stress

    Laminated and coextruded pouches for detergents, agrochemical precursors, and mineral-based cleaning powders subject the sealant web to biaxial stress during pouch collapse and drop loading. UMERIT 4040F is placed in the sealant layer at 25–40 wt% with a butene-LLDPE or MDPE carrier to improve environmental stress crack resistance under ASTM D1693-21 Condition B and low-temperature puncture under ASTM D5748-19. The upper limit of 40 wt% is set by the loss of interlayer adhesion in blown-film coextrusion when the outer HDPE skin and the mLLDPE-rich sealant layer have a melt index disparity greater than 1.5 g/10 min under ISO 1133-1:2022. The sealant web is produced as a three-layer blown film with a 1.8 mm die gap, a blow-up ratio of 2.0:1–2.2:1, and a melt temperature of 190–210°C, then laminated to PET or oriented nylon via a solventless adhesive. Compliance is governed by FDA 21 CFR §177.1520(c) 3.2a where indirect food additive exposure is involved, EU Regulation (EU) No 10/2011, and REACH (EC) No 1907/2006; compatibility with the specific chemical fill is validated under ASTM D543-20 for weight change and ASTM F1249-20 for moisture vapor transmission rate. Finished products are stand-up pouches for liquid detergents, powder chemical sachets, and agrochemical packaging with barrier laminations. A critical operational boundary is chemical exposure: continuous contact with concentrated oxidizing acids above 60°C is outside the recommended service window for polyethylene sealant webs, regardless of mLLDPE content.

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    Certification & Compliance
    More Introduction

    UBE UMERIT mLLDPE 4040F is a metallocene-catalysed linear low-density polyethylene supplied for film conversion, extrusion coating, and sealant layers. The grade is identified by a nominal melt mass-flow rate of 4.0 g/10 min measured at 190 °C under a 2.16 kg load per ISO 1133-1, and a nominal density of 0.904 g/cm³ at 23 °C per ISO 1183-1. The metallocene catalyst platform produces a narrow molecular weight distribution and controlled short-chain branching distribution. These structural features differentiate the product from conventional Ziegler-Natta LLDPE grades in seal initiation, haze, impact, and extractables behaviour.

    Typical published values for the neat resin are provided below. These values are not specification limits and do not replace the certificate of analysis for a specific production lot.

    Typical published property values for UBE UMERIT mLLDPE 4040F
    PropertyTest methodTypical value
    Melt mass-flow rateISO 1133-14.0 g/10 min
    DensityISO 1183-10.904 g/cm³

    At equal melt flow rate, a conventional butene-based Ziegler-Natta LLDPE with a density of 0.918–0.920 g/cm³ possesses a broader molecular weight distribution than 4040F. The narrower distribution of the metallocene resin reduces the high-molecular-weight species that raise seal initiation temperature and haze. The trade-off is a lower degree of shear thinning; melt pressure at high screw speed may therefore be higher than that of a Ziegler-Natta LLDPE with the same ISO 1133-1 value. Seal initiation is measured per ASTM F2029, hot tack per ASTM F1921, and haze per ASTM D1003. Dart impact, where reported, is measured per ASTM D1709. Published data for this specific configuration is limited to typical film trial conditions, and a converter must run confirmatory trials on the target line.

    What Limits the Stable Melt Curtain During High-Speed Cast Film Extrusion?

    On cast film lines, the narrow molecular weight distribution of 4040F reduces the shear-thinning response. At a die shear rate above 100–500 s⁻¹, sharkskin surface melt fracture may appear at the die exit. The exact onset is not a single resin property; it depends on die gap, die land length, melt temperature, and the presence of fluoropolymer processing aids. Die lip fouling is controlled by maintaining the die-lip temperature 10–20 °C above the melt temperature and by purging at startup with a commercial polymer processing aid masterbatch or a zinc stearate purge compound.

    Barrel zone settings from 180 °C to 240 °C on a 30:1 L/D single-screw extruder are used to balance melting and viscosity. A reverse temperature profile, in which the feed zone is 10–20 °C cooler than the metering zone, is commonly applied to avoid screw slip and reduce melt temperature. The screw should include a barrier flight section and low-shear mixing elements. High-shear dispersive mixers can generate excessive melt temperature and promote gel formation in metallocene LLDPE, particularly if a previous high-density polyethylene has not been fully purged.

    In a three-layer A/B/C cast film where 4040F is placed in the sealant layer, the sealing window is evaluated under ASTM F2029 using a dwell time of 1.0 s and a sealing pressure of 0.3 MPa across a temperature ladder from 80 °C to 140 °C. Seal strength after cooling is measured per ASTM F88 with a crosshead speed of 300 mm/min. The seal initiation temperature is not an intrinsic resin constant; it shifts with film thickness, backing layer stiffness, and seal bar geometry. Values obtained on a 25 µm monolayer film are therefore not transferable to a 50 µm coextruded lamination without revalidation.

    Extrusion Coating Draw Resonance and Neck-In After LDPE Replacement

    Substitution of autoclave LDPE with 4040F in extrusion coating alters elongational behaviour. Long-chain branching in LDPE provides strain hardening; 4040F has lower melt strength and can exhibit draw resonance at coating speeds above 200 m/min. The converter controls neck-in by reducing the air gap to 150–200 mm, selecting a die gap of 0.5–0.6 mm, and adjusting the melt curtain trajectory through the die bolt settings. Published data for coating-grade mLLDPE with a similar melt flow rate indicates melt temperatures of 280–310 °C are used on extrusion coating lines; converters must verify against the resin certificate of analysis and avoid exceeding the recommended upper temperature to prevent oxidative degradation.

    Melt curtain stability is monitored under stroboscopic lighting to detect draw resonance before it propagates into coating weight variation. The lower extensional viscosity of 4040F relative to LDPE may also reduce edge purging tension; edge bead trim systems must be set to remove the full neck-in region to avoid transfer roll contamination.

    Food-Contact Status Requires Final Article Migration Testing.

    Neat resin compliance with FDA 21 CFR 177.1520 for olefin polymers may be stated by the manufacturer, but this does not cover the final packaging article. Converters must test overall migration under EU Regulation (EU) No 10/2011 using food simulants assigned to the intended food type. For fatty foods, simulant D2 or 95% ethanol is used; for aqueous foods, simulants A, B, or C are used according to the food category. The overall migration limit is 10 mg/dm² for plastic materials, or 60 mg/kg for certain high-surface-area applications. Specific migration of additives and residual catalyst components must also be assessed if the final structure incorporates printing inks, adhesives, or tie resins.

    Because polyethylene is not hygroscopic, predrying is not normally required. However, condensation on pellet surfaces at relative humidity above 60% can introduce surface moisture into the feed throat and produce film bubbles at the die. Silos or hoppers should be maintained 5–15 °C above ambient to prevent condensation. Bags should be closed after sampling, and the resin should not be stored near strong odorants such as amines, esters, or solvent-based inks because polyethylene sorbs volatile organic compounds and can develop organoleptic defects.

    Purging and blending rules are governed by density and viscosity mismatches.

    Before switching from a higher-density HDPE to 4040F, the extruder is purged with a lower-viscosity polyethylene or a dedicated purge compound. Melt pressure and torque are monitored until stable values are reached. Blending 4040F with conventional Ziegler-Natta LLDPE broadens the molecular weight distribution, but the seal initiation temperature does not shift linearly with blend ratio. Converter-generated sealing data is required to validate any blend ratio. Processing with a blend above the converter-validated percentage may reduce the benefit of the metallocene architecture without producing a proportionate cost advantage. A density drift of ±0.002 g/cm³ is detectable in infrared thickness gauges and can alter seal performance in multilayer films.

    In five-layer coextrusions designed for modified atmosphere packaging, 4040F is positioned as the sealant skin. Interfacial adhesion is evaluated by ASTM D1876 T-peel testing after film production. The target value is not universal; the package integrity protocol defines the minimum seal strength after 48 h of ageing at 23 °C and 50% relative humidity. Cohesive failure in the tie resin is preferred over adhesive failure at the 4040F/tie interface. This failure mode indicates that the sealant layer has not become the limiting interface in the converted package.

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