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Chevron Phillips Marlex mLLDPE D139

    • Product Name: Chevron Phillips Marlex mLLDPE D139
    • 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 293313
    Polymer Type Metallocene Linear Low Density Polyethylene (mLLDPE)
    Comonomer Hexene-1
    Catalyst Metallocene
    Density 0.918 g/cm³
    Melt Index 190 C 2 16 Kg 0.9 g/10 min
    Melting Point 119 °C
    Vicat Softening Point 94 °C
    Tensile Strength At Break Md 30 MPa
    Tensile Strength At Break Td 28 MPa
    Elongation At Break Md 500 %
    Elongation At Break Td 700 %
    Dart Drop Impact 250 g
    Elmendorf Tear Md 200 g
    Elmendorf Tear Td 300 g
    Haze 6 %
    Gloss 80 %

    As an accredited Chevron Phillips Marlex mLLDPE D139 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Chevron Phillips Marlex mLLDPE D139 is supplied in 25 kg moisture-resistant polyethylene bags, palletized for industrial handling.
    Container Loading (20′ FCL) Container Loading (20′ FCL): Chevron Phillips Marlex mLLDPE D139 in 25kg bags, palletized and securely loaded into one 20′ FCL.
    Shipping Chevron Phillips Marlex mLLDPE D139 is shipped as non-hazardous polyethylene resin pellets in 25 kg bags, palletized and stretch-wrapped, or in bulk trucks/railcars. It is not regulated as dangerous goods; keep dry and away from excessive heat. Follow the SDS and local shipping regulations.
    Storage Store Chevron Phillips Marlex mLLDPE D139 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers closed and protect from moisture and contamination. Avoid dust accumulation and keep away from strong oxidizers. Follow local regulations and the manufacturer’s SDS for specific storage requirements.
    Shelf Life Shelf life: typically 12 months from manufacture date when stored in original unopened packaging, protected from heat, sunlight, and moisture.
    Application of Chevron Phillips Marlex mLLDPE D139

    Marlex D139 is a metallocene-catalysed ethylene-hexene copolymer with a nominal density of 0.918 g/cm³ per ISO 1183-1:2019 and a melt flow rate of 1.0 g/10 min per ISO 1133-1:2022 at 190°C/2.16 kg. The narrow molecular-weight distribution and controlled short-chain branching distribution shift seal initiation below that of conventional Ziegler-Natta LLDPE of equivalent density, but they also reduce melt elasticity. This trade-off controls downstream processing decisions in every application segment.

    In primary food-contact blown film, D139 is processed as the main skin or core layer in three-layer coextruded structures. The line typically employs a grooved-feed extruder with 30:1 to 33:1 L/D, a barrier screw, and a die diameter from 200 mm to 400 mm. Melt temperature at the adapter is held between 193°C and 221°C, while die gap is set at 1.8 mm to 2.4 mm. Blow-up ratio is limited to 2.0:1 to 2.8:1 because the low melt strength of metallocene LLDPE produces bubble flutter at higher expansion. A monolayer line can run 100% D139, but for frost-line stability and die-lip cleanliness on lines without internal bubble cooling, converters blend 70-80 wt% D139 with 20-30 wt% LDPE. That blend sacrifices optical clarity; haze measured by ASTM D1003-21 may rise from 6% to 10% depending on LDPE grade and frost-line height. Food-contact compliance is governed by FDA 21 CFR 177.1520(c) for olefin polymers and by Commission Regulation (EU) No 10/2011, with overall migration held below 10 mg/dm² under the specified fatty-food simulant conditions. Sealant performance is assessed by ASTM F88/F88M-23 seal strength and ASTM F1921-18(2024) hot-tack; a 50 µm monolayer seal typically reaches the target 200 g/25 mm peel force at a lower bar temperature than an equivalent-density Ziegler-Natta LLDPE, while the narrow comonomer distribution prevents a broad sealing plateau. Reverse-printed BOPP or BOPET webs can be laminated to D139, but direct surface printing requires corona treatment at 38-42 mN/m; lower dyne levels produce ink adhesion failure on the metallocene-rich surface.

    Where Does D139 Fit in Heavy-Duty Sack Extrusion Without Sacrificing Output?

    On heavy-duty industrial liner and logistics packaging lines, the grade is extruded at film thicknesses from 125 µm to 250 µm on large blown film lines equipped with internal bubble cooling and dual-lip air rings. A screw diameter of 90 mm to 120 mm with an L/D of 30:1 is typical. Melt temperatures are kept in the 204°C to 232°C range. Output per die circumference is limited by bubble cooling rather than extruder capacity; with internal bubble cooling, specific output near 1.0 kg/h per mm die circumference is used as an upper boundary before bubble instability appears. Dart impact values measured by ISO 7765-1 Method A for a 200 µm monolayer film often fall between 800 g and 1,200 g for D139-rich structures, but converting to blends containing 15 wt% to 25 wt% LDPE lowers dart impact by 10-20% while improving bubble stability. Elmendorf tear is anisotropic; machine-direction tear per ISO 6383-2 is usually lower than transverse-direction tear, and for liner applications the minimum transverse-direction tear should be specified at 30 N/mm for manual handling. Reprocessed edge trim is introduced at up to 20 wt%, but each 10 wt% addition of regrind reduces puncture resistance measured by ASTM D5748 by approximately 5-15% depending on trim history and gel content. Terminal products include FIBC liners, shipping sack inserts, dunnage airbag films, and nonhazardous bulk powder liners. The grade is not automatically rated for UN dangerous-goods packaging; a filled-bag drop test and stack test under the specific UN 13M5 or 13H3 design type must be run on the finished sack before transport certification is assigned. Heavy inorganic fillers are avoided in this segment because calcium carbonate masterbatch above 8 wt% increases gel formation on the screw and reduces tear resistance below acceptable levels for filled bulk bags.

    Silage and greenhouse base films use D139 for the high dart impact and puncture resistance required by mechanical handling equipment. The resin itself has no meaningful UV resistance, so all outdoor service requires compounded light-stabiliser packages. A typical black silage film formulation contains 2.0-3.0 wt% carbon black masterbatch, 0.20 wt% hindered amine light stabiliser, and 0.10 wt% benzotriazole UV absorber. For white or three-layer silage covers, the outer white layer contains titanium dioxide at 5-8 wt% plus HALS, while the core can contain up to 30 wt% post-industrial reclaim if the reclaim is derived from unpigmented D139 film and screen-filtered through 100 µm melt filtration. The film is typically coextruded at 150 µm to 250 µm total thickness with a die gap of 2.2 mm to 2.8 mm and a blow-up ratio of 2.0:1 to 3.0:1. Frost-line height is kept low to maintain transverse orientation, which improves tear resistance when bales are wrapped. Adhesion to round-bale wrapping equipment is achieved by mechanical cling layers, not by D139 surface tack; if cling is required, a separate very-low-density polyolefin plastomer or EVA skin layer is used. Pesticide and silage additive contact is an operational boundary. Published data for the specific migration of silage inoculants and formic-acid-based additives into D139 film is limited; sacks and covers intended for prolonged direct contact with acidic silage leachate should be tested according to the additive supplier protocol because pH below 4.0 accelerates extraction of low-molecular-weight species and weakens heat-sealed seams after several months of outdoor storage.

    Cast Film Die Buildup and Low-Temperature Seal Response

    In cast film and extrusion coating lines, D139 is run at higher melt temperatures than blown film, generally 238°C to 260°C, to reduce melt viscosity and improve web uniformity. The flat die is set with a lip gap of 0.5 mm to 0.8 mm for films under 50 µm. Chill-roll temperature is maintained at 18°C to 24°C; higher roll temperatures decrease haze but reduce the cooling rate and can generate blocking in wound rolls. Neck-in and draw resonance are limiting factors because the metallocene resin has less strain-hardening than LDPE. To suppress draw resonance in monolayer cast film, converters either use a vacuum box and air knife at 2-4 bar air pressure or blend 10-20 wt% LDPE into D139. Die-lip deposit formation is observed at the edge bead when melt temperature exceeds 265°C for more than 6 h continuous running; the deposit is typically oxidised low-molecular-weight polyethylene, and it produces edge-thickness variability and film breaks. For sealant layers in cast coextruded polypropylene or polyethylene structures, D139 is used as the skin layer at 10-20% of total thickness. Hot tack strength measured by ASTM F1921-18(2024) remains usable over a sealing bar temperature window of 90°C to 140°C; outside this range, failure mode transitions from cohesive peel to interfacial delamination. Terminal products include flow-wrap overwrap, medical device pouch film, and non-food lamination sealant webs. The grade is not intended for direct cast extrusion onto aluminium foil without an anhydride-grafted polyethylene tie layer because D139 has no polar functionality and will not survive foil-failure delamination tests.

    Lamination and flexible-packaging sealant webs convert D139 at coat weights between 15 g/m² and 40 g/m² in tandem extrusion lamination. The resin is melted in a 90 mm extruder at 260°C to 285°C and deposited through a slot die onto primed BOPET, BOPP, or aluminium foil. Because D139 is nonpolar, the substrate must be primed with a waterborne polyethylenimine or polyurethane primer at 0.05-0.10 g/m² dry coat, or a tie resin must be coextruded between the sealant and foil. Delamination strength measured by ASTM F904-16 on a D139-to-foil structure without primer is typically below 0.5 N/15 mm; with a maleic-anhydride-grafted polyethylene tie layer, values above 5 N/15 mm are obtained. The low seal initiation temperature of D139 allows high-speed vertical form-fill-seal packaging lines to reduce dwell time at the fin-seal bar, but chill-roll release must be controlled because the metallocene surface becomes tacky at cast-roll temperatures above 30°C. Terminal products include stand-up pouch sealant webs, sachet inner layers, and medical packaging tray lidding. The grade is not suitable for retort pouch construction; sustained exposure at 121°C for 30 min exceeds the softening range and causes seal creep and channel leaks in the finished pouch. For hot-fill packaging up to 85°C, seal strength retention is acceptable only if the sealant layer is supported by a polyester or nylon outer web.

    When Frozen Food Packaging Demands Ductility Below -20°C

    Low-temperature ductility is one of the main reasons D139 is specified for frozen food overwrap and bag-in-box liners. The film is converted at 40 µm to 80 µm on blown film lines with a blow-up ratio of 2.5:1 to 3.0:1 and an air-ring temperature of 8°C to 12°C. The rapid quench freezes in the narrow crystallite size distribution that gives metallocene LLDPE its toughness at sub-zero conditions. Dart impact measured at -20°C by ISO 7765-1 Method A remains above 300 g for a 60 µm monolayer, while the same film at room temperature exceeds 1,000 g. Tensile elongation at break in the transverse direction is tested by ISO 527-3 at -10°C; values below 250% can indicate excessive orientation or frost-line height. The film is often corona-treated to 40-42 mN/m on the inner surface for print or lamination; on the outer surface treatment is avoided to prevent blocking during cold storage. Terminal products include frozen vegetable bags, ice cream overwrap, fish block liners, and meat barrier laminates. If D139 is used in direct contact with fatty frozen foods, EU Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520 apply; the converter must verify overall migration under frozen-fatty-food simulant conditions, which are less severe than hot-fill simulants but still require batch documentation. The operational boundary is temperature. Continuous service below -30°C is possible, but repeated flexing at -40°C can induce pinholes at film creases if the gauge is under 50 µm; for such service, gauges above 70 µm or lamination to orientated polyamide is specified.

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    Certification & Compliance
    More Introduction

    Chevron Phillips Marlex mLLDPE D139 is a hexene-based metallocene linear low-density polyethylene supplied as pelletized resin for blown-film, lamination, and coextruded sealing-layer applications. The grade is characterized by a nominal melt index of 1.0 g/10 min at 190 °C/2.16 kg and a nominal density of 0.918 g/cm³. The metallocene single-site catalyst system produces a narrow molecular weight distribution and controlled short-chain branching, which differentiate the material from conventional Ziegler-Natta LLDPE grades by reducing low-molecular-weight extractables and providing lower seal initiation, improved hot-tack strength, and higher optical clarity. The resin is used in food-contact packaging, high-clarity laminates, stand-up pouches, heavy-duty sacks, and industrial wrapping where the converting operation requires a balance of heat-seal response, dart impact, and tear resistance.

    The neat resin is not formulated with slip or antiblock additives, permitting the converter to select surface-modifying masterbatches according to the specific film line and end-use requirement. That feature also shifts the coefficient-of-friction control burden to downstream formulation and winding practice. The product is not supplied as a direct cast-film replacement for high-flow grades with melt index above 2.0 g/10 min; its molecular architecture is oriented toward blown-film processing where bubble stability and seal performance drive equipment selection.

    Typical Physical Property Matrix Under ASTM D1505 and D882

    Representative values from product technical literature are provided in the following table. These values are typical material characterization data and are not intended as sales specifications; film properties vary with gauge, blow-up ratio, frost-line height, and additive package.

    PropertyTypical ValueTest Method
    Melt index1.0 g/10 minASTM D1238
    Density0.918 g/cm³ASTM D1505
    DSC melting temperature117 °CASTM D3418
    Vicat softening temperature94 °CASTM D1525
    Tensile yield strength, MD10.3 MPaASTM D882
    Tensile yield strength, TD10.5 MPaASTM D882
    Elongation at break, MD500%ASTM D882
    Elongation at break, TD620%ASTM D882
    Dart drop impact, F50800 gASTM D1709A
    Elmendorf tear, MD170 gASTM D1922
    Elmendorf tear, TD350 gASTM D1922
    Haze8%ASTM D1003
    Gloss at 45°80ASTM D2457

    Film property measurements are typically obtained on conditioned blown film at a defined gauge, often 25 µm to 50 µm. Direct comparison between data sheets requires confirmation of gauge and processing history because tensile, tear, and impact values shift with orientation and cooling rate. The narrow molecular weight distribution of D139 causes a more abrupt melting transition than conventional broad-distribution LLDPE, which is reflected in the DSC melting endotherm and in heat-seal behavior.

    On blown-film extrusion lines, the reduced shear-thinning response of metallocene LLDPE relative to autoclave LDPE changes the extrusion energy profile. Melt temperatures at the die are commonly controlled between 204 °C and 232 °C; lower temperatures improve bubble strength but increase the risk of sharkskin surface defects when shear stress at the die lip approaches approximately 0.14 MPa. Increasing the die gap to 2.0 mm and maintaining die land temperature above 215 °C reduces the incidence of surface melt fracture. Bubble stability is typically optimized at blow-up ratios of 1.8:1 to 2.5:1, with frost-line height set at 5–8 die diameters. A dual-lip air ring supplied with chilled air at 8–12 °C improves cooling symmetry and reduces gauge bands. On a 75 mm grooved-feed extruder with 30:1 L/D and a barrier screw, stable production is commonly reported in the 150–200 kg/h range; above this output, bubble oscillation may appear unless the air ring is changed to a high-pressure configuration with improved venturi flow. Pre-drying is generally unnecessary at ambient relative humidity below 60%, but moisture-contaminated regrind should be dried before reclaim to avoid surface depressions and gel-related visual defects.

    When Hexene-Based mLLDPE Replaces C4-LLDPE in High-Hot-Tack Sealant Layers

    In vertical form-fill-seal and horizontal form-fill-seal packaging, D139 is evaluated as a sealant-web replacement for C4 Ziegler-Natta LLDPE because of differences in seal initiation and hot-tack strength. The seal initiation temperature, measured at a seal force of 2.0 N/25 mm under ASTM F88, is commonly 10–15 °C lower than that of a comparable 0.918 g/cm³ C4 ZN grade. That reduction permits faster cycling and shorter seal-bar dwell on rotary or reciprocating sealing jaws. Hot-tack strength does not decay as sharply above the melting point; the material maintains a force plateau above 2.5 N/25 mm through the 110–130 °C seal-bar window on rotary sealing equipment. The controlled comonomer placement reduces low-molecular-weight fractions that can migrate to the sealing surface and create weak tear points after package filling.

    The same narrow molecular weight distribution that improves sealing behavior lowers melt strength in monolayer blown-film operations. On older low-pressure air-ring lines, substitution of D139 for a conventional C4 LLDPE may produce bubble instability unless a blending component is introduced. A typical correction is the addition of 5–10 wt% LDPE with melt index of 0.25 g/10 min to restore bubble geometry without eliminating the seal advantage. Published data for specific three-layer sealant-layer thicknesses below 20 µm in high-speed vertical fill lines are limited; seal-bar pressure, dwell time, and jaw temperature profiling on the target machine remain necessary for process qualification.

    Dart impact strength measured at 25 µm on conditioned film according to ASTM D1709A is generally reported in the 700–900 g range for D139, whereas a conventional C4 ZN LLDPE at equivalent density may fall below 150 g. The difference arises from hexene comonomer incorporation and reduced molecular weight polydispersity, which distribute load more uniformly across the film structure. Elmendorf tear in the transverse direction is typically above 300 g, and film haze per ASTM D1003 is below 10%. Gloss measured at 45° according to ASTM D2457 commonly exceeds 70, allowing lamination-grade optical clarity without additional processing aids. Puncture resistance per ASTM D5748 shows energy-to-break values approximately 30–50% higher than conventional C4 LLDPE at equivalent gauge. These differences are material-specific and depend on extrusion conditions, particularly drawdown ratio and frost-line cooling.

    What Limits Downstream Conversion in High-Clarity Lamination Structures?

    In extrusion lamination and adhesive lamination, D139 is employed as a sealant or print-receiving web where low gel count and optical uniformity are required. The grade’s low extractable profile improves lamination bond retention after autoclaving and reduces surface haze in multilayer polyethylene-based pouches. Because the neat resin does not contain slip or antiblock, roll blocking can occur during storage of wound master rolls if winding tension is high and storage temperature exceeds 30 °C. Corona treatment levels of 38–42 mN/m are typical for lamination downstream; treatment above that range can generate oxidized low-molecular-weight species that reduce heat-seal strength in the final packaging structure.

    The resin is not recommended for cast-film lines operating below 190 °C melt temperature, because surface haze and melt fracture defects may become visible at low melt temperature and high draw ratio. On tandem extrusion-lamination equipment with a 90 mm extruder and AC motor load remaining below 85%, line speeds up to 120 m/min are commonly attainable with 20 µm coating thickness. Published data for configurations using water-quench cast-film dies are limited; validation of gloss, haze, and adhesion under the specific line configuration is required before production release.

    For food-contact use, compliance is evaluated under 21 CFR 177.1520(c) and the applicable European plastics regulation, including Regulation (EU) No 10/2011, provided that the final article meets the overall migration limit for the intended food simulant. The resin is not classified as hazardous under GHS and does not contain intentionally added heavy metals subject to RoHS Directive 2011/65/EU. The grade is not intended for medical implant or pharmaceutical primary packaging applications. If high-temperature retort conditions above 121 °C are specified, the material may not retain adequate seal strength after retorting, and validation under the specific retort profile is required.

    In frozen-food packaging, low-temperature dart impact and seal integrity after temperature cycling are the principal performance criteria. On a high-speed vertical form-fill-seal line running at 60 cycles/min, D139-based sealant webs have shown stable seal strength after filling at −25 °C, but direct conversion data for multi-layer lamination with oriented polyester or biaxially oriented polypropylene outer webs are product-specific. The material’s narrow melting range makes seal-bar temperature control more critical than with broad-distribution LLDPE; a temperature deviation of ±5 °C at the sealing jaw can shift seal strength and cause film pull-out in drop-impact testing. Process windows should therefore be established on the specific packaging machine using the exact film structure and gauge.

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