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TotalEnergies Lumicene Supertouch mLLDPE 18ST05

    • Product Name: TotalEnergies Lumicene Supertouch mLLDPE 18ST05
    • 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 794357
    Productname TotalEnergies Lumicene Supertouch mLLDPE 18ST05
    Polymertype Metallocene linear low density polyethylene (mLLDPE)
    Comonomer Hexene-1
    Density G Cm3 0.918
    Meltflowrate 190c 2 16kg G 10min 0.5
    Meltingtemperature C 116
    Vicatsofteningtemperature C 94
    Tensilemodulus Mpa 240
    Tensilestrengthatyield Mpa 10
    Tensilestrengthatbreak Mpa 35
    Elongationatbreak Percent 600
    Dartdropimpact G 1200
    Elmendorftearstrengthmd G 150
    Elmendorftearstrengthtd G 400
    Haze Percent 6
    Gloss45 Percent 80
    Sealinitiationtemperature C 90

    As an accredited TotalEnergies Lumicene Supertouch mLLDPE 18ST05 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing TotalEnergies Lumicene Supertouch mLLDPE 18ST05 is supplied in 25 kg moisture-resistant polyethylene bags, typically 55 bags (1,375 kg) per pallet.
    Container Loading (20′ FCL) Loaded in 20’ FCL container: TotalEnergies Lumicene Supertouch mLLDPE 18ST05 packed in 25 kg bags on pallets, securely stowed for sea transport.
    Shipping TotalEnergies Lumicene Supertouch mLLDPE 18ST05 is shipped as non-hazardous thermoplastic pellets, typically in moisture-resistant 25 kg bags on pallets, stretch-wrapped for protection. Use clean, dry transport at ambient temperature; avoid moisture, direct sunlight, contamination, and handling damage. Store closed in a dry, ventilated area.
    Storage Store TotalEnergies Lumicene Supertouch mLLDPE 18ST05 indoors in a cool, dry, well-ventilated area, protected from direct sunlight, heat, sparks, flames, moisture, and strong oxidizing agents. Keep original packaging sealed, clean, and off the ground to prevent contamination or mechanical damage. Avoid prolonged UV exposure, practice first-in/first-out rotation, and follow the manufacturer’s SDS and local regulations.
    Shelf Life Typically 24 months from production when stored unopened in dry conditions below 50°C, away from direct sunlight.
    Application of TotalEnergies Lumicene Supertouch mLLDPE 18ST05

    On five-layer cast stretch film lines used for pallet unitization, TotalEnergies Lumicene Supertouch mLLDPE 18ST05 is processed at nominal density 0.918 g/cm³ by ISO 1183-1 and melt flow rate 0.5 g/10 min by ISO 1133-1:2022 at 190 °C/2.16 kg. The low MFR requires die-zone melt temperature set points in the range of 245 °C to 265 °C on extrusion lines equipped with 90 mm 30:1 L/D grooved-feed extruders and positive-displacement melt pumps. Chill roll temperature is controlled between 18 °C and 25 °C; higher roll set points increase blocking tendency and degrade film haze consistency under ASTM D1003-21. Die gap is maintained at 0.6 mm to 0.8 mm, and melt pressure is held below 350 bar when line speed does not exceed 600 m/min. At film gauges below 12 µm, sharkskin is controlled with fluoropolymer process aid additions of 300 ppm to 800 ppm; the onset of melt fracture is gauge-dependent and occurs earlier than with C4-LLDPE grades having MFR of 1.0 g/10 min to 2.0 g/10 min. Pre-stretch ratios from 200% to 300% on rotary-arm wrappers expose the film to rapid strain hardening demands; 18ST05-containing structures tend to show high puncture and tear propagation resistance but lower strain hardening than LDPE-rich formulations. When gauge is reduced from 20 µm to 15 µm, converters validate performance with ASTM D5748-18 puncture tests and ISO 6383-2 Elmendorf tear tests at production-speed sampling intervals. Roll hardness is controlled by lay-on pressure settings matched to winder diameter; excessive nip pressure causes blocking in the core layer, particularly when the film is stored above 30 °C. This application is processing-critical because the combination of 0.5 g/10 min MFR, 0.918 g/cm³ density, and narrow metallocene composition distribution creates a narrow window between melt fracture, low-temperature gauge variation, and blocking.

    What Makes 18ST05 Suitable as a Sealant Web in Frozen Food Lamination?

    Lamination converters select the grade for the inner sealant web when an adhesive lamination structure is built as PET or OPP / adhesive / mLLDPE. The seal initiation temperature is characterized by ASTM F1921-18 hot tack and seal strength is measured by ASTM F88/F88M-21 at 200 mm/min; the narrower melting distribution of the metallocene resin shifts the sealing plateau to a lower temperature than C4-LLDPE webs of equivalent density. On solventless laminators running 1,200 m/min, the low gel count reduces optical defects in transparent structures, but the sealant web must be corona treated to 42 dyn/cm to 46 dyn/cm, measured by DIN 53364 or ASTM D2578-17, before adhesive application. The resulting composite is used for frozen food such as IQF vegetables, seafood, and ready-to-bake dough, where seal integrity below −25 °C is evaluated by drop impact tests at line audit intervals. Sealant layer thickness in such structures typically ranges from 25 µm to 60 µm, with 18ST05 comprising 60 wt% to 100 wt% of that layer. Food-contact status is supported by EU Regulation (EC) No 1935/2004, EU Regulation (EU) No 10/2011 Annex I, and FDA 21 CFR §177.1520(c) for olefin polymers under applicable conditions of use; individual conversion conditions still require a supplier compliance letter because printing inks, adhesives, and coating systems are outside the resin supplier’s control. Because the mLLDPE has a lower crystallinity level relative to 0.920+ g/cm³ copolymers, the sealant web follows package contours with a lower secant modulus, characterized by ISO 527-3 on 100 mm/min crosshead speed. Film blocking after slitting is managed by anti-block masterbatch dosing into the sealant layer at levels determined by rewind tension; excessive dosing above 4 wt% can lower seal strength below process capability limits.

    When 18ST05 Replaces C4-LLDPE in Heavy-Duty Sack Blown Film

    On heavy-duty form-fill-seal sack lines producing 25 kg to 50 kg industrial packaging, replacing a conventional C4-LLDPE with 18ST05 requires adjustment of both blend ratio and blown film line parameters. The resin is typically introduced at 20 wt% to 40 wt% in the middle layer of a three-layer A/B/A structure, with outer layers containing LDPE or HDPE to maintain bubble stability. Die gaps are set between 1.6 mm and 2.2 mm, blow-up ratio is held between 2.0 and 2.5, and frost line height is raised by 1 to 2 die diameters relative to C4-LLDPE to reduce bubble oscillation. The film is tested for dart impact using ASTM D1709-22 method A and Elmendorf tear using ISO 6383-2; the low MFR of 0.5 g/10 min increases melt pressure on 75 mm 30:1 L/D grooved-feed extruders, where screen packs of 20/40/60 mesh are common. End-use performance in heavy-duty sacks is assessed by drop testing of filled sacks according to ISO 7965-1:2022, with ten-drop staircase methods used on production floors to determine safe fill weights for granulate, fertilizer, and construction additives. The resin’s narrow comonomer distribution improves puncture robustness against irregular fill particles, but the absence of long-chain branching reduces bubble stability unless die temperatures remain above 210 °C. Pre-drying is not required below 50% storage relative humidity; if outdoor silo condensation occurs, a desiccant hopper dryer set to 60 °C to 70 °C with a −20 °C dew point for 2 hours is used to prevent surface moisture defects. These line modifications are considered deep-dive control points because the processing window is narrower than for conventional LLDPE, and gauge uniformity at 150 µm total thickness is checked continuously by beta scanning systems.

    Agricultural silage films coextruded on three-layer blown lines use 18ST05 as a puncture-resistant core layer in white/black and transparent barrier structures. The line setup generally includes a die diameter of 250 mm to 400 mm, die gap of 1.8 mm to 2.5 mm, blow-up ratio of 2.0 to 3.0, and total film thickness of 100 µm to 180 µm; UV stabiliser masterbatch is metered into the outer layers at rates determined by exposure period and regional solar intensity. The film’s suitability for silage covering is based on the balance between puncture resistance and tear propagation, measured with ISO 6383-2 and ASTM D5748-18 after UV ageing according to ISO 4892-2, because field failures occur when solar degradation reduces tear resistance before silage removal. Published data for this specific 18ST05 configuration is limited, so converters run side-by-side outdoor exposure trials before replacing conventional C4-LLDPE or EVA blends. The low MFR requires higher barrel temperatures in the core extruder, but the metallocene resin allows reduction in core layer gauge from 40 µm to 30 µm in some structures without a measured loss in dart impact. Film blocking during roll storage is managed by adding anti-block masterbatch at 2 wt% to 4 wt% into the outer layers and quarantining rolls under covered storage at 20 °C to 30 °C.

    Collation Shrink Film Edge Seal Behaviour

    Collation shrink lines using 18ST05 in outer layers are set to a die gap of 1.0 mm to 1.6 mm and a blow-up ratio of 2.5 to 3.5 to create orientation balance for shrink sleeves around bottled water or canned goods. The resin’s 0.918 g/cm³ density produces a lower shrink force than higher-density LLDPE, so the edge seal on a packaging machine must be re-optimized with jaw temperature settings between 140 °C and 170 °C, depending on film thickness and line speed. Seal strength is checked with ASTM F88/F88M-21 at 200 mm/min, while shrink percentage is controlled by oil bath immersion conditions described in ISO 14616:2016 for polyethylene shrink films. On high-speed lines beyond 40 cycles/min, the low MFR influences seal dwell time; if the hot-wire seal contact time is too short, cold peel occurs at the overlap edge. A common structure is 20 µm to 30 µm three-layer film with 18ST05 in the outer layers and an LDPE-rich core. Optical properties after orientation are influenced by die lip cleanliness and chill temperature; haze is measured in accordance with ASTM D1003-21 and tracked from the extruder to the inspector rewinder. This configuration is shallower than cast stretch processing, but the shrink edge seal remains a critical control point because intermittent jaw temperature drift above 170 °C causes seal burn-through on thin outer layers.

    Application areaCritical test methodRegulatory or technical reference
    Cast stretch film puncture and tearASTM D5748-18, ISO 6383-2, ISO 1133-1:2022Pallet unitization film guidance; converter internal gauge verification
    Lamination sealant webASTM F1921-18, ASTM F88/F88M-21, DIN 53364EU (EC) No 1935/2004, EU (EU) No 10/2011, FDA 21 CFR §177.1520(c)
    Heavy-duty sack filmASTM D1709-22, ISO 7965-1:2022, ISO 6383-2Industrial packaging drop test staircase protocol
    Agricultural silage filmISO 4892-2, ASTM D5748-18, ISO 6383-2Outdoor exposure trial reporting; UV stabiliser masterbatch documentation
    Collation shrink filmISO 14616:2016, ASTM D1003-21, ASTM F88/F88M-21Polyethylene shrink film classification
    Bag-in-box film sealingASTM F88/F88M-21, ASTM D5276-19, ASTM D1693-21Food-contact packaging limitations for non-retort use

    Dielectric welding compatibility in bag-in-box film is process-defined.

    Bag-in-box converters replacing EVA or C4-LLDPE with 18ST05 in the inner sealing layer encounter different dielectric welding behaviour because the nonpolar polyolefin has a low dielectric loss factor. Radio-frequency welding is therefore not an acceptable sealing method; heat-seal and ultrasonic welding are preferred. Ultrasonic welding equipment with 20 kHz or 35 kHz horns and anvil gap set to 0.05 mm to 0.15 mm produces consistent fitment weld strengths when the film thickness is 80 µm to 120 µm and the sealant layer is at least 30 µm thick. Seal strength is validated according to ASTM F88/F88M-21, and drop testing of filled bags is conducted using ASTM D5276-19. The low density of 0.918 g/cm³ supports stress-crack resistance in liquid fill, but environmental stress cracking in aggressive liquids must be evaluated via ASTM D1693-21 bent strip testing with the specific fill fluid at service temperature. The grade is not suited for retort applications above 100 °C; continuous-use temperature for LLDPE in food-contact service is below 100 °C under many EU and FDA conditions of use. Published data for 18ST05 in bag-in-box applications is limited, so converters must perform migration testing under Commission Regulation (EU) No 10/2011 for specific food simulants and time-temperature conditions. This limitation is stated to prevent misuse in hot-fill or retort formats where seal creep and film softening occur before the end of shelf life.

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    Certification & Compliance
    More Introduction

    TotalEnergies Lumicene Supertouch mLLDPE 18ST05 is a metallocene-catalysed linear low-density polyethylene with a nominal density of 0.918 g/cm³ determined according to ISO 1183-1 and a nominal melt flow rate of 0.5 g/10 min at 190 °C under a 2.16 kg load determined according to ISO 1133-1:2022. Manufacturer documentation identifies hexene-1 as the comonomer; this C6 chemistry separates the grade from butene-based C4 Ziegler-Natta LLDPE of similar density because the higher alpha-olefin comonomer and the single-site catalyst produce a more homogeneous short-chain branching distribution. The resulting molecular architecture narrows the molecular weight distribution, lowers the weight fraction of high-melting low-comonomer material, and reduces extractable species after film conversion. Unlike conventional LLDPE grades with broad molecular weight distributions, 18ST05 is intended for blown film structures where lower seal initiation temperature, lower haze, and higher dart impact resistance are required without an increase in film gauge. The grade is supplied as free-flowing pellets without a heavy slip or antiblock package, allowing the film converter to select the required surface-additive masterbatch according to end-use coefficient of friction, blocking behaviour, and food-contact requirements. Typical end uses include industrial stretch hood, heavy-duty sacks, lamination film, agricultural film, frozen-food packaging, and multi-layer film where the metallocene resin is used as a toughening component in core or skin layers.

    The 0.5 g/10 min melt flow rate is at the low-MFR end of the blown film process window and should not be treated as a drop-in replacement for 1.0 g/10 min or 2.0 g/10 min LLDPE. On blown film extruders with grooved-feed barrels and L/D ratios of 25:1 to 30:1, the melt temperature at the adapter is usually held between 190 °C and 230 °C. Sustained adapter temperatures above 240 °C are generally unnecessary and may initiate oxidative gel formation, die-lip build-up, and discolouration. Starting conditions for high-stalk film generally include a die gap of 1.2 mm to 2.0 mm and a blow-up ratio between 2.0:1 and 3.0:1. Frost line height must be established on the target line because quench rate controls molecular orientation and the balance between machine-direction and transverse-direction tensile properties. The narrow molecular weight distribution reduces melt strength at low shear; blending 10 wt% to 20 wt% of LDPE with a melt index of 0.3 g/10 min to 2.0 g/10 min is a standard melt-strength and bubble-stability adjustment. Fluoropolymer processing aid masterbatches are used at 200 ppm to 500 ppm where sharkskin, die-lip build-up, or melt fracture occurs, but the exact dosage should be validated against the complete additive formulation and film specification.

    On multi-layer spiral mandrel coextrusion lines, the viscosity of 18ST05 must be matched against the adjacent LDPE, tie-resin, EVOH, or polyamide layers. Interfacial instability can appear as wavy or grainy film when the polyolefin and barrier-layer melt viscosities differ excessively. For barrier structures, the polyethylene layers are typically run at 190 °C to 220 °C while the barrier layer is processed according to its own thermal degradation limit; the melt temperature difference between adjacent streams is normally kept within 10 °C to 15 °C at the die entry. Published data for the specific pairing of 18ST05 with EVOH or polyamide in commercial barrier film is limited; converters should use coextrusion rheology trials and melt viscometry to define the optimum layer ratio and temperature programme.

    Because 18ST05 is supplied without a heavy slip or antiblock package, surface additives must be chosen against end-use requirements. Erucamide slip at 500 ppm to 1500 ppm and synthetic silica antiblock at 2000 ppm to 6000 ppm are typical starting concentrations in masterbatch form. Excessive antiblock reduces haze and dart impact; excessive slip can interfere with print adhesion and heat-seal strength. Migration of fatty amide slip to the film surface is time- and temperature-dependent and should be measured by coefficient of friction according to ASTM D1894 after maturation at 23 °C for at least 48 h. The lower crystalline fraction of mLLDPE can accelerate surface bloom relative to higher-density polyethylene; therefore packaging, lamination, and printing trials should be timed to reflect the final storage and transport history of the finished film.

    Mechanical property balance is controlled more by film orientation and processing than by pellet properties alone. A higher blow-up ratio, typically 2.5:1 to 3.0:1, increases transverse-direction tensile strength and tear resistance while reducing machine-direction orientation. Lower frost line height increases machine-direction tensile strength and modulus but can reduce dart impact and increase haze. For heavy-duty sack and stretch-hood structures, converters often select a blow-up ratio near 2.5:1 to approach balanced tear resistance; the optimum must be confirmed with tensile tests according to ISO 527-3 and Elmendorf tear tests according to ASTM D1922. Published data for 18ST05 in all gauge and line combinations is limited; the relationships described are standard blown film processing responses rather than product-specific curves.

    How Does Narrow Molecular Weight Distribution Alter Seal and Puncture Performance?

    The most measurable performance changes appear in heat-seal and impact testing. Because the metallocene catalyst incorporates hexene-1 more uniformly along the polyethylene backbone than a heterogeneous Ziegler-Natta C4 system, 18ST05 contains fewer high-melting, low-comonomer fractions that delay seal initiation and reduce interlayer adhesion. Heat-seal initiation temperature is determined by producing seals under controlled jaw temperature, pressure, and dwell time, followed by peel testing according to ASTM F88/F88M. Converter trials have recorded seal initiation reductions of 5 °C to 10 °C relative to a conventional C4 Ziegler-Natta LLDPE of equivalent 0.918 g/cm³ density and 0.5 g/10 min melt flow rate, although the absolute value is sensitive to film thickness, additive bloom, seal bar condition, and dwell time. Dart drop impact measured by ISO 7765-1 on 50 µm blown film is directionally higher because the homogeneous branching distribution limits large crystalline domains that act as stress-concentration sites. Haze measured by ASTM D1003 and gloss measured by ASTM D2457 also improve relative to conventional C4 grades, but the magnitude is influenced by die gap, frost line height, and external cooling air temperature.

    Directional comparison based on industrial blown film trials; values are not specification limits.

    Property or behaviour Test method Conventional C4 Ziegler-Natta LLDPE reference 18ST05 directional response
    Molecular weight distribution GPC/SEC Broad Narrow
    Seal initiation temperature ASTM F88/F88M Reference Lower 5 °C to 10 °C
    Dart drop impact, 50 µm film ISO 7765-1 Reference 20–50% higher, process-dependent
    Haze, 50 µm film ASTM D1003 Reference 20–40% lower, gauge-dependent
    Melt pressure at equal screw speed Extruder pressure transducer Reference 10–20% higher on grooved-feed L/D 30 machines

    The directional ranges in the table should not be used for incoming inspection or product release. Actual differences depend on screw design, melt temperature profile, die gap, blow-up ratio, frost line height, cooling air velocity, and additive masterbatch composition. A converter should generate a multi-point property map on the target line before changing film formulations or downgauging.

    When 18ST05 Is Substituted for a Higher-MFR Cast-Film Grade

    Replacement of a cast-film grade with 0.5 g/10 min 18ST05 is not a direct equipment change. Cast stretch-film lines are usually optimised for resins with melt flow rates between 2.0 g/10 min and 4.0 g/10 min, which allow lower melt temperatures, lower backpressure, and higher line speed. The higher viscosity of 18ST05 increases extruder motor load and melt pressure at constant screw speed. To reduce viscosity, processors may raise barrel and die temperatures toward 250 °C; this approaches the thermal oxidation threshold of polyethylene when residence time is long or melt temperatures are uneven. Published data for 18ST05 in high-speed cast stretch film at commercial throughput is limited. Injection-moulding applications are also outside the practical viscosity window; most injection-moulding LLDPE and mLLDPE grades require melt flow rates above 10 g/10 min to fill thin sections at acceptable pressure drop. The product is therefore assigned to blown film processes, and cast-film substitution should proceed only after a narrow-window trial with independent melt pressure and melt temperature monitoring.

    For incoming inspection and finished film qualification, the following test designations are referenced. The table does not imply that the pellet is automatically compliant with food-contact regulations; finished articles must be evaluated under the intended use conditions because migration of additives and any post-manufacturing contaminants is article-dependent.

    Assessment area Standard or regulation Application in qualification
    Density ISO 1183-1 Incoming resin identity
    Melt flow rate ISO 1133-1:2022 Incoming resin identity
    Dart drop impact ISO 7765-1 Film toughness
    Elmendorf tear ASTM D1922 Machine-direction and transverse-direction tear resistance
    Haze ASTM D1003 Optical quality
    Gloss ASTM D2457 Optical quality
    Seal strength ASTM F88/F88M Heat-seal performance
    Puncture resistance ASTM D5748 Puncture and stretch-hood performance
    Coefficient of friction ASTM D1894 Slip and packaging behaviour
    Olefin polymer food-contact status FDA 21 CFR 177.1520(c) Base resin condition; article-dependent
    EU food-contact migration Regulation (EU) No 10/2011 Finished-article compliance testing

    Polyethylene pellets do not require drying under normal enclosed storage. Condensation, not hygroscopic absorption, is the relevant moisture failure mode: when cold pellets are moved from an uninsulated silo into a production hall with a dew point above the pellet surface temperature, surface moisture can form and generate bubble defects or slip issues at film blowing. Under such conditions the pellets should be tempered in sealed containers until the pellet temperature is above the ambient dew point. Extended hot-air drying above 80 °C is not recommended and can accelerate oxidative degradation despite the presence of phenolic and phosphite antioxidant packages. Reclaim film containing 18ST05 is usually incorporated into scrapless edge-trim and start-up waste at addition levels up to 20 wt%; higher rework fractions may increase gel count and reduce dart impact because of oxidative chain scission and crosslinking during multiple heat histories. The grade should not be stored in direct sunlight or in the presence of open flame, and standard polyolefin housekeeping procedures apply to dust and pellet leakage.

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