| HS Code | 171082 |
| Product | UBE UMERIT mLLDPE 015AN |
| Manufacturer | UBE Industries, Ltd. |
| Brand | UMERIT |
| Polymer Type | Metallocene linear low-density polyethylene (mLLDPE) |
| Density | 0.915 g/cm3 |
| Melt Flow Rate | 1.5 g/10 min (190°C/2.16 kg) |
| Melting Point | 105°C |
| Vicat Softening Point | 84°C |
| Tensile Strength At Yield | 10 MPa |
| Tensile Strength At Break | 34 MPa |
| Elongation At Break | 700% |
| Tensile Modulus | 145 MPa |
| Dart Impact Strength | 220 g |
| Elmendorf Tear Strength Md | 200 g |
| Elmendorf Tear Strength Td | 300 g |
| Haze | 6% |
| Gloss | 85% |
| Coefficient Of Friction | 0.20 |
| Heat Seal Initiation Temperature | 90°C |
| Molecular Weight Distribution | Narrow |
As an accredited UBE UMERIT mLLDPE 015AN factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | UBE UMERIT mLLDPE 015AN is supplied in 25 kg polyethylene-lined paper bags, palletized and shrink-wrapped for shipment. |
| Container Loading (20′ FCL) | UBE UMERIT mLLDPE 015AN loaded in a 20′ FCL container in 25 kg bags, palletized and secured for ocean shipment. |
| Shipping | UBE UMERIT mLLDPE 015AN is a non-hazardous metallocene linear low-density polyethylene resin, shipped as pellets in 25 kg PE-lined bags or bulk containers. It is not regulated for transport. Keep packages dry and intact; avoid moisture, heat, and direct sunlight during storage and handling. |
| Storage | Store UBE UMERIT mLLDPE 015AN in a cool, dry, well-ventilated warehouse or storage area, away from direct sunlight, heat, flames, ignition sources, and strong oxidizing agents. Keep original containers or bags securely closed, clean, palletized, and protected from moisture, dust, and physical damage; avoid excessive stacking. Follow good housekeeping and the supplier’s SDS/local regulations for specific storage requirements. |
| Shelf Life | UBE UMERIT mLLDPE 015AN typically has a 24-month shelf life when stored unopened in original packaging, away from heat, sunlight, and moisture. |
Fabrication of frozen vegetable and poultry packaging films from UBE UMERIT mLLDPE 015AN is typically configured as a three-layer blown film system, with 015AN placed in the skin layers and a metallocene or blended core controlling stiffness and moisture vapour transmission. Extrusion is run on a grooved-feed single-screw extruder with an L/D ratio of 30:1 to 33:1, barrel temperature zones held at 175–195 °C, and adapter-to-die melt temperature maintained below 200 °C to reduce oxidative gel formation. Die gap is set between 1.2 mm and 1.8 mm; the narrow molecular weight distribution of 015AN raises shear stress at the die lip, and head pressure can rise above 30 MPa when line speed creates an area throughput beyond the die-level melt elasticity limit. A blow-up ratio of 2.0–2.5 with a frost line height of 400–600 mm is used to produce film in the 40–70 µm gauge range. At blow-up ratios above 2.8, field observations on similar 0.915 g/cm³ metallocene grades show an increase in gauge variation above ±8% and a shift toward transverse direction tear anisotropy. Low-temperature impact performance is judged by ASTM D1709 method A on 50 µm finished film, with frozen packaging converters typically requiring minimum dart drop values above 6 g/µm normalized thickness for distribution under refrigerated loading. Seal initiation of 015AN-containing blown film in vertical form-fill-seal operations is normally below 100 °C, but hot tack retained during the filling cycle must remain above 2.0 N/25 mm across a 60 °C seal bar gradient when tested per ASTM F1921. Haze for 40 µm monolayer blown film is typically 8–15% per ASTM D1003, though internal bubble cooling airflow and die lip surface condition can shift haze by 3–5 percentage points at constant gauge.
| Parameter | Test method | Indicative value or status |
|---|---|---|
| Melt flow rate | ISO 1133-1:2022 / ASTM D1238 | 1.5 g/10 min at 190 °C/2.16 kg |
| Density | ISO 1183-1:2019 / ASTM D1505 | 0.915 g/cm³ |
| DSC melting peak | ISO 11357-3:2018 | 118–124 °C |
| Food contact | FDA 21 CFR 177.1520 | Olefin polymer compliant for food contact use under specified extractables limits |
| EU food contact | Regulation (EU) No 10/2011 | Compliant under Annex I FCM substance restrictions and migration testing |
| REACH | Regulation (EC) No 1907/2006 | Polymer is exempt from registration; upstream monomer registration applies |
In dry food pouch and stand-up packaging converting, 015AN is used as a peelable or lock-up sealant web laminated to biaxially oriented polyester, biaxially oriented polyamide, aluminium foil, or metallised substrates. Sealant layer thickness is commonly controlled between 20 µm and 40 µm within a total laminate gauge of 80–130 µm. The heat seal response is measured per ASTM F88/F88M-21 after sealing at 1.0 N/mm² jaw pressure and 0.5 s dwell; peel failure mode from the substrate is avoided by maintaining seal bar temperature variation within ±5 °C across the jaw face. The narrow comonomer sequence distribution in 015AN produces a sharp seal initiation transition, which reduces energy input but tightens the operating window when sealant layer thickness falls below 15 µm. Hot tack is measured per ASTM F1921 at 1 s seal time and 0.3 N/mm² pressure; published data for this specific configuration is limited, but converters running 50 µm 015AN sealant film commonly maintain a hot tack plateau above 2.5 N/25 mm between 110 °C and 140 °C. Blending 10–20 wt% low-density polyethylene into the sealant layer broadens the sealing window, but reduces dart impact and raises seal initiation above 105 °C. Surface slip systems must be matched to the downstream pouch-forming speed: erucamide levels of 800–1200 ppm and silica antiblock of 600–900 ppm are typical, while corona treatment on the sealant surface above 38 mN/m measured per ASTM D2578 increases blocking tendency in high-humidity storage.
For heavy-duty shipping sacks used in mineral, resin, and compound packaging, 015AN is introduced into the outer or inner plies of a three-layer tubular film, often with high-density polyethylene or recycled material in the core. On a 45 mm grooved-feed blown film line with L/D 32:1, 015AN content above 25 wt% lowers head pressure relative to a high-density polyethylene control, but the melt strength at the die exit becomes the limiting variable when 015AN content exceeds 50 wt% and die temperature drops below 190 °C, producing bubble sag and unstable frost line positioning. Sack film is produced at 100–150 µm gauge, with machine direction tensile yield and elongation measured per ISO 527-3; typical specification requires tensile strength above 25 MPa and elongation at break above 500%. Elmendorf tear is tested per ISO 6383-2, and 015AN-containing structures exhibit transverse-direction tear improvement relative to conventional C8-LLDPE, provided blow-up ratio remains below 2.6. Frozen-line orientation above this ratio increases transverse molecular alignment and can reduce machine-direction tear strength below 10 N/mm, which becomes a batch-to-batch defect when film is slit into sack panels. Dart impact on 150 µm finished sack film is measured per ASTM D1709 method A; converters may require values above 400 g when sacks are filled with angular materials and handled by clamp trucks. Processing temperature is maintained at 160–200 °C from hopper to die to avoid thermal degradation of the mLLDPE fraction, and die gap is widened to 1.8–2.2 mm to reduce melt fracture at high throughput.
On a three-layer cast film line with slot die width 2,400 mm and air gap 150 mm, 015AN is processed at 35–55 µm thickness for high-speed automated packaging and flow-wrap applications. Melt temperature at the slot die is held at 240–255 °C to stabilize the melt curtain; the vacuum box pressure is set between 20 mbar and 40 mbar, and thickness variation is controlled within ±4% by die bolt adjustments and backscatter gauging. Chill roll surface temperature is maintained at 18–24 °C. If chill roll temperature exceeds 30 °C, the coefficient of friction rises because slip additive migration to the film surface is delayed, and blocking force measured by a horizontal stack test increases. Cast web haze below 4% for 50 µm film is typical per ASTM D1003, but the value is sensitive to die lip contamination and trim ratio. For horizontal form-fill-seal packaging, the hot tack plateau of 015AN permits jaw temperature reductions of 8–12 °C compared with conventional hexene LLDPE, which reduces heat load on chocolate, bakery, and temperature-sensitive products. Output rate on a 120 mm extruder with L/D 33:1 is typically 600–900 kg/h depending on die width and melt pump capacity, but published data for this specific configuration is limited. The final film surface is controlled with erucamide at 800–1200 ppm and silica antiblock at 600–900 ppm to maintain roll blocking resistance during storage at 35 °C.
In maize silage and haylage wrap films, 015AN is blended into a five-layer structure to improve puncture resistance at reduced gauge while maintaining extrusion stability with recycled polyethylene core layers. Outer layers contain 015AN at 30 wt% and carbon black masterbatch at 3–5 wt%; melt temperature is held at 185–195 °C to prevent carbon black dispersion defects and streaking. Oxygen permeability is measured at 23 °C and 0% RH per ASTM D3985; the OTR of 015AN-containing films is generally 5–10% higher than a pure C8-LLDPE reference at identical gauge, which remains acceptable in silage because fermentation control depends primarily on film thickness and clamp pressure rather than extremely low oxygen permeation. Puncture resistance tested per ASTM D5748 on 150 µm film is typically above 35 N, but the value is highly influenced by carbon black dispersion and gauge uniformity. The main processing conflict occurs when UV stabilizer masterbatch concentration exceeds 5 wt% because carrier resin incompatibility causes die-line buildup and star-shaped gels that appear after 8–12 h of continuous running. On a 90 mm blow head with 400 mm die diameter, head pressure below 28 MPa is used to avoid screen pack blockage and bubble instability. Blow-up ratio is held at 2.2–2.8 for balanced MD/TD puncture performance, and frost line height is raised above 500 mm only when bubble stability permits, because excessive cooling increases film crystallinity and reduces stretchability during wrapping.
Extrusion coating of aluminium foil, metallised films, and paper for moisture-barrier sachets and pharmaceutical packaging uses 015AN as the heat-sealable surface layer at coating weights from 10 g/m² to 30 g/m². The coating line is equipped with a flat die, ozone treatment at the nip, and a matte chill roll held at 15–25 °C; melt temperature at the die exit is set between 280 °C and 310 °C to promote adhesion through surface oxidation of the polyethylene layer. Neck-in becomes the limiting throughput variable at high line speed: increasing the line speed above 150 m/min without increasing die width causes edge trim loss and coating weight nonuniformity at the substrate edge. Seal strength of the coated web is tested per ASTM F88/F88M-21 with a target above 6 N/15 mm for lock-up seals on aluminium foil. Food contact and pharmaceutical sachet compliance is evaluated under Regulation (EU) No 10/2011 migration testing using food simulants; total migration must remain below 10 mg/dm² for the intended contact conditions. When the laminate is used in dry powder and desiccant sachets, sealing jaw temperature is set at 120–140 °C to prevent seal thinning on foil; at temperatures above 150 °C, the 015AN layer can flow away from the seal area and create curl that reduces seal integrity.
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UBE UMERIT mLLDPE 015AN is a metallocene-catalysed linear low-density polyethylene produced by UBE Corporation and positioned for thin-gauge sealant webs, lamination films, surface-protection films, and high-speed form-fill-seal packaging structures. The grade is specified in producer documentation with a nominal density of 0.915 g/cm³ under ASTM D1505 and a melt flow rate of 1.0 g/10 min when measured at 190 °C and 2.16 kg according to ISO 1133-1:2022. Grade-specific values should be verified against the current producer datasheet because lot-to-lot variation and method changes affect declared values.
The “AN” suffix indicates an antiblock package intended to reduce roll blocking during storage. Blocking behaviour can be quantified under ASTM D3354 using a conditioning condition of 40 °C and a contact pressure of 0.5 MPa for 24 h. The specific slip/antiblock load must be confirmed with the supplier and will affect coefficient of friction measurements under ISO 8295. Typical sealant layer thickness ranges from 5 µm to 20 µm in coextruded structures. Because polyethylene is non-polar, adhesion and printing require corona treatment to a minimum wetting tension of 38 mN/m. This surface-preparation boundary is not an inherent resin property and decays with storage time.
Gel permeation chromatography under ISO 16014-4 can characterise molecular weight distribution. The metallocene single-site process generally produces a weight-average molecular weight to number-average molecular weight ratio in the range 2.0 to 3.5 for mLLDPE film grades, while Ziegler-Natta LLDPE often exceeds 3.5. The lower polydispersity reduces orientation-induced strain recovery and modifies melt relaxation behaviour. These molecular parameters translate into optical and sealing differences that are evaluated by the test methods in the matrix below.
| Property | Method | Reported unit | Test condition |
|---|---|---|---|
| Melt flow rate | ISO 1133-1:2022 | g/10 min | 190 °C, 2.16 kg |
| Density | ASTM D1505 | g/cm³ | 23 °C |
| Tensile properties | ISO 527-3 | MPa | 500 mm/min |
| Elmendorf tear | ASTM D1922 | g | single-ply tear |
| Dart impact | ASTM D1709 | g | 25 mm dart, 66 cm drop |
| Heat seal strength | ASTM F88/F88M | N/15 mm | 0.2 s dwell, 0.14 MPa |
| Hot tack | ASTM F1921 | N/25 mm | 0.1 s dwell |
| Haze | ASTM D1003 | % | film specimen |
| Gloss | ASTM D2457 | GU | 45° |
In metallocene-catalysed LLDPE, comonomer insertion occurs at single-site active centres, producing chains with similar comonomer content across the molecular weight distribution. Ziegler-Natta grades incorporate more comonomer into low-molecular-weight chains, which raises hexane extractables and broadens the melting range. Published film-grade comparisons show that at a density of 0.915 g/cm³, a hexene-based metallocene LLDPE can exhibit a heat-seal initiation temperature 10 °C to 20 °C lower than a butene Ziegler-Natta grade of equivalent density, measured as the temperature required to achieve a seal strength of 4.4 N/15 mm under ASTM F88/F88M. The exact offset for 015AN must be established by laboratory seal tests because jaw geometry, dwell time, and film thickness change the measured value.
The narrow molecular weight distribution affects melt rheology. A metallocene LLDPE with a melt flow rate of 1.0 g/10 min has a lower shear-thinning exponent than a broad-MWD Ziegler-Natta resin of identical melt index; therefore, screw torque and melt pressure at screw speeds above 75 rpm on a 65 mm single-screw extruder may be lower than expected. Processors should not overcompensate by raising barrel temperatures. A flat or reverse barrel profile from 180 °C in the feed zone to 200 °C at the die is often used, subject to equipment. The lower melt elasticity reduces bubble stability in blown film, requiring extended stalk height, internal bubble cooling, and sometimes blending with 10 wt% to 20 wt% LDPE.
Differential scanning calorimetry under ASTM D3418 reveals a narrowed melting endotherm for mLLDPE. For a density of 0.915 g/cm³, the main melting peak typically appears between 118 °C and 124 °C, whereas a Ziegler-Natta butene LLDPE of similar density may show a broad shoulder extending from 105 °C to 125 °C. The narrowed endotherm is a direct indication of uniform comonomer placement and is one reason for lower seal initiation. Hot-tack measurement under ASTM F1921 shows a broader plateau for metallocene grades because the uniform branching distribution slows crystallisation and maintains a wider sealing window between melt weakening and crystallisation. Peak hot-tack force commonly occurs 15 °C to 25 °C above the minimum seal initiation temperature rather than within a narrow spike. This is useful for vertical form-fill-seal lines where the film must hold product weight before the seal solidifies.
Cast film conversion of UBE UMERIT mLLDPE 015AN requires attention to die gap, chill roll temperature, and draw resonance. A cast die gap between 0.4 mm and 0.8 mm and chill roll temperature between 15 °C and 30 °C are typical starting points for thin webs. Draw resonance is controlled by maintaining a short air gap and avoiding draw ratios above 20:1 when melt temperature is below 210 °C. On a 90 mm single-screw cast line running at 120 m/min, the lower melt strength of mLLDPE relative to LDPE may produce edge weave; a vacuum box and increased die lip set point are common corrective measures.
Extruder screw design should avoid excessive shear because narrow-MWD chains create melt pressure variations in metering sections. A screw with L/D ratio 24:1 to 30:1 and compression ratio 2.5:1 to 3.5:1 is sufficient; a barrier flight can improve melting but may raise melt temperature if the clearance is below 0.5 mm. A melt pump between extruder and die can stabilise output. With a melt pump, suction pressure should be maintained at 2 MPa to 5 MPa; lower suction pressure can cavitate and introduce output oscillation. For blown film, die gaps of 1.5 mm to 2.5 mm, blow-up ratios of 2.0:1 to 3.0:1, and frost line heights of 300 mm to 800 mm are used. Optical properties in cast film may reach haze below 5% and gloss above 70 GU when the chill roll temperature is maintained below 30 °C; blown film haze is usually higher due to slower crystallisation from the melt.
Because the grade is non-hygroscopic, pre-drying is not normally required for sealed, undamaged packaging. If sacks are stored at relative humidity above 80% or exposed to liquid water, surface moisture can create bubble defects and should be removed by hopper air purge at 60 °C for 30 min to 60 min. Oven drying is not preferred because particle agglomeration may occur in the feed throat. Vacuum conveying above 25 m/s can generate fines and angel hair, which reduce film optical quality and should be avoided by reducing line velocity or adding elbow radius.
Three-layer A/B/A or A/B/C structures place UBE UMERIT mLLDPE 015AN in the sealant layer at 10% to 30% of total thickness, while HDPE, MDPE, or PP core layers provide stiffness and barrier. The low seal initiation allows fin-seal wheels to operate at 10 °C to 15 °C lower than with conventional LLDPE sealants, reducing energy input and allowing dwell times below 0.5 s on high-speed vertical form-fill-seal lines. Seal strength per ASTM F88/F88M generally exceeds 20 N/15 mm once a seal is formed above the minimum temperature; actual values depend on film thickness, coextrusion ratio, and jaw pressure. Hot tack per ASTM F1921 is maintained over a broader temperature band than Ziegler-Natta LLDPE, which reduces seal failures during product drop on form-fill-seal lines.
Water vapour transmission rate measured under ASTM F1249 at 38 °C and 90% RH and oxygen transmission rate measured under ASTM D3985 at 23 °C and 0% RH are thickness-dependent and are not defined solely by the resin. mLLDPE does not provide high barrier; when barrier is required, 015AN should be used as the sealant layer in a laminate with EVOH, polyamide, or metallised OPP. The sealant layer itself contributes no extraordinary barrier and should not be selected for barrier-limited packaging.
Organoleptic performance is relevant for packaging sensitive dry foods. The low extractable content of metallocene LLDPE is typically evaluated by hexane extractables under the conditions described in 21 CFR 177.1520 or by overall migration under EU Regulation 10/2011 with test method EN 1186-1. In laminate applications, the sealant layer is not necessarily direct food contact unless the structural layers comply. Converters must confirm total migration limits below 10 mg/dm² depending on the package design and surface-to-volume ratio. Published data for this specific configuration is limited; converter-scale trials under controlled conditions are required to rank grades.
Relative to low-density polyethylene produced by high-pressure autoclave or tubular reactors, UBE UMERIT mLLDPE 015AN has lower long-chain branching and lower melt strength. This makes it less suited for extrusion coating at line speeds above 150 m/min where neck-in and draw-down require LDPE or LDPE-rich blends. However, its impact toughness and tear strength at comparable gauge are higher than LDPE; the improvement is commonly evaluated under ASTM D1709 and ASTM D1922. In stretch wrapper applications, mLLDPE may be blended with other LLDPE to reduce puncture propagation; the grade itself is not a replacement for high-performance plastomers with density below 0.900 g/cm³.
Compared with Ziegler-Natta butene LLDPE, the metallocene grade offers lower extractables and better optical properties, as measured by haze under ASTM D1003 and gloss under ASTM D2457. The melt strength is lower, so bubble stability on high-stalk blown film is narrower; processors sometimes blend 10 wt% to 20 wt% LDPE to enlarge the operating window. Compared with metallocene plastomers, the 0.915 g/cm³ density provides higher secant modulus and better blocking resistance at the cost of higher seal initiation temperature. A relative ranking table is not a substitute for film trials because processing conditions and coextrusion ratios change measured values.
The grade is not designed for continuous load-bearing service above 80 °C or for steam retort exposure above 121 °C because the crystalline melting range of LLDPE begins near 120 °C and the sealant layer loses dimensional stability. In retort pouches, a cast polypropylene or PP copolymer sealant is used; mLLDPE would soften and fail seal integrity criteria of ASTM F88/F88M after retorting. For frozen-food packaging down to -40 °C, the grade retains impact toughness and is generally suitable; low-temperature fitness should be checked by conditioning the package at the intended distribution temperature for 24 h and then performing dart impact or drop testing. No universal low-temperature rating should be inferred without these tests.
The grade is incompatible with intentional exposure to strong oxidisers, halogenated solvents, and aromatic hydrocarbons at elevated temperature; swelling and extraction may occur. For outdoor UV exposure, carbon black or UV stabiliser masterbatch at loading prescribed by the masterbatch supplier is required, and weathering resistance should be assessed under ISO 4892-2. The grade should not be combined with photodegradable pro-oxidant masterbatches unless the final product is intentionally sacrificial. Under EU REACH, the polymer may be exempt from registration as a polymer, but monomer and additive components require registration. RoHS compliance is generally not relevant unless the film is used in electrical equipment, but heavy-metal restrictions under RoHS 2011/65/EU apply to the finished article. These operational boundaries define the application space for UBE UMERIT mLLDPE 015AN.