Products

Lotrene LLDPE Q1018H

    • Product Name: Lotrene LLDPE Q1018H
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 237895
    Product Lotrene LLDPE Q1018H
    Polymer Type Linear Low Density Polyethylene (LLDPE)
    Comonomer Butene-1
    Density 0.918 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 1.0 g/10 min
    Melting Point Dsc 122 °C
    Vicat Softening Point 10 N 100 °C
    Brittleness Temperature < -80 °C
    Tensile Strength At Yield Md 12 MPa
    Tensile Strength At Yield Td 11 MPa
    Tensile Strength At Break Md 38 MPa
    Tensile Strength At Break Td 33 MPa
    Elongation At Break Md 450%
    Elongation At Break Td 650%
    Dart Drop Impact F50 120 g
    Haze 8%
    Gloss 60 50

    As an accredited Lotrene LLDPE Q1018H factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Lotrene LLDPE Q1018H is supplied in 25 kg polyethylene-coated paper bags, 40 bags per shrink-wrapped pallet, strapped for safe transport.
    Container Loading (20′ FCL) Container Loading (20′ FCL) for Lotrene LLDPE Q1018H ensures safe, efficient packing of polymer resin into a standard 20-foot container.
    Shipping Lotrene LLDPE Q1018H is a non-hazardous polyethylene resin supplied as free-flowing pellets. Ship in clean, dry containers or FIBC bags, protected from moisture and direct heat. No special transport classification required, but avoid excessive impact. Keep packaging sealed during transit and storage to preserve product quality.
    Storage Store Lotrene LLDPE Q1018H pellets in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep packaging sealed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and stacking damage. Maintain stable temperatures, and follow local regulations for polymer storage.
    Shelf Life Shelf life is typically 12 months from delivery if stored in original packaging in a cool, dry, shaded area.
    Application of Lotrene LLDPE Q1018H

    Lotrene LLDPE Q1018H is a butene-copolymer linear low-density polyethylene with a nominal density of 0.918 g/cm³ measured under ISO 1183-1:2019 and a melt flow rate of 1.0 g/10 min at 190 °C/2.16 kg under ISO 1133-1:2022. In heavy-duty shipping sack and FIBC liner film production, the resin is charged as the linear backbone component in a dry blend containing 70–80 wt% Q1018H and 20–30 wt% high-pressure LDPE with a melt index of 0.3–0.5 g/10 min. The blend is fed through a 90 mm single-screw extruder with an L/D of 30:1, a barrier feed section, and a Maddock mixing section; screen-pack configuration is commonly 20/40/60 mesh, and the die gap is maintained at 2.0 mm. Barrel-zone temperatures are held at 190–210 °C, adapter and die zones at 210 °C, blow-up ratio is controlled at 2.2:1 to 2.6:1, and frost line height is fixed at 6–8 die diameters with internal bubble cooling at a differential pressure of 15–25 Pa. The film is extruded at 80–120 µm and then edge-trimmed, wound, and converted into heavy-duty shipping sacks, FIBC liners, and 25 kg petrochemical product sacks. Slip and antiblock masterbatch are added at 1.0–2.0 wt% when the coefficient of friction must remain below 0.35 under ISO 8295, and fluoropolymer-based polymer processing aids are used at 0.03–0.05 wt% when melt fracture appears at high output rates above 180 kg/h.

    Qualification for FIBC liner conversion uses ISO 527-3:2018 for tensile strength and elongation, ASTM D1709-16a Method A for dart impact, and ASTM D1922 for Elmendorf tear. Because converted bulk bags may enter UN-certified dangerous-goods packaging, the finished sack system is tested under ISO 21898:2019 for FIBC classification, including stacking, drop, and tear-propagated failure modes; the Q1018H film contributes to the required mechanical envelope but is not the certifying component by itself. Additive masterbatches are verified under REACH 1907/2006, and antioxidant or processing-stabiliser chemistries are selected from the (EU) No 10/2011 positive list when the liner is supplied for indirect food contact. On production lines, a frost line drift exceeding ±100 mm on a 90 mm extruder has been observed to reduce dart impact at 60 µm by more than 15%; therefore the frost line height is locked to die-diameter ratio rather than to haul-off speed alone. If the film is downgauged below 55 µm, bubble instability increases unless internal bubble cooling pressure and air-ring geometry are rebalanced for the thinner web.

    What processing window preserves low-temperature ductility in frozen-food packaging film?

    Frozen-food packaging webs based on Q1018H are formulated with 80–85 wt% Q1018H, 15–20 wt% high-pressure LDPE, and 1.5–2.0 wt% synthetic silica-based antiblock masterbatch. The film is produced on a three-layer blown-film line using a 70 mm core extruder and 50 mm skin-layer extruders, with a die gap of 1.6 mm, a blow-up ratio of 2.5:1, and melt temperatures of 195–205 °C. Gauge is typically 40–80 µm, and the web is converted on servo-driven side-weld or bottom-seal bag machines. The butene short-chain branching of Q1018H is exploited for sub-zero toughness rather than high-temperature stiffness; the film retains flexibility and puncture resistance after conditioning at -20 °C, although published data for Q1018H finished-pouch burst at this temperature is limited and processors usually set in-process control limits by testing film immediately after the nip and again after 24 h of chill storage.

    Direct food-contact validation is based on FDA 21 CFR 177.1520 for olefin polymers, with end-use migration testing under conditions of use A through H described in 21 CFR 176.170(c). For EU-bound articles, the finished package must demonstrate an overall migration below 10 mg/dm² under (EU) No 10/2011, and each slip or antiblock additive is checked against the specific migration limits in Annex II of the regulation. The film is not intended for retort or hot-fill service above 60 °C; the vicat softening point of a butene LLDPE with a density of 0.918 g/cm³ typically lies near 90–96 °C, and sustained thermal load during filling or sealing can distort the seal interface. Terminal products include bags for IQF vegetables, frozen poultry, seafood, and ice-cream multipacks.

    Where a 180 µm three-layer greenhouse cover is extruded on a 120 mm, L/D 28:1 three-layer blown-film line, Q1018H is assigned to the core layer at 50–60 wt% of total film weight, with the outer layer consisting of 25–30 wt% UV-stabilised LDPE and the inner layer composed of 10–15 wt% anti-fog LDPE/EVA blend. The UV-stabiliser package is delivered as a HALS/UV-absorber masterbatch at 6–8 wt% of the outer layer, while the inner layer carries a nonionic anti-fog masterbatch at 1.5–2.5 wt% of the inner layer. The die gap is 2.0 mm, blow-up ratio is 2.8:1, frost line height is maintained at 1.0–1.2 m with a dual-lip air ring and internal bubble cooling, and output is typically 300–350 kg/h on the 120 mm line. The Q1018H core contributes puncture resistance during hail exposure and high elongation at break in the machine direction, which is relevant when the film is stretched over tunnel arches; the outer LDPE layer carries UV protection, and the inner anti-fog layer controls interfacial condensation during diurnal temperature cycling.

    The covering film is assessed under EN 13206:2017 for greenhouse films, with artificial weathering performed under ISO 4892-2 cycle 2 for 9,000 h. Tensile properties before and after ageing are measured under ISO 527-3:2018, and the commonly applied acceptance criterion is retained tensile strength above 50% after the xenon-arc exposure period. In high-irradiation zones, field replacement intervals are typically 12–18 months; when retained tensile strength falls below the 50% threshold, the film is removed before micro-tear propagation compromises the tunnel structure. Finished product types include greenhouse covers, low tunnel covers, and dairy silage covers.

    When a 250 µm damp-proof membrane must survive installation over coarse aggregate

    Construction damp-proof membranes based on Q1018H are formulated with 94–97 wt% Q1018H, 2–3 wt% carbon black masterbatch, 0.5–1.0 wt% fluoropolymer-based processing aid, and 0.3–0.5 wt% phenolic/phosphite antioxidant. The film is blown on a 90 mm extruder with a die gap of 2.2 mm and a blow-up ratio limited to 2.0:1, which reduces bubble-neck instability at high gauge. Thickness is controlled between 125–250 µm, and flat widths up to 6 m are produced for underslab applications; the thick-web output rate is deliberately reduced to 120–150 kg/h to maintain bubble cooling and gauge uniformity. The membrane is converted as sheet rolls with 3-inch cores and slit edges, and the film is laid over a sand blinding layer or over compacted hardcore with a lap distance of 150 mm.

    Regulatory compliance under the Construction Products Regulation is established by CE marking under EN 13967:2012 for flexible sheets for waterproofing. Tensile properties are tested under ISO 527-3:2018, water vapour resistance under EN 1931:2014, and puncture resistance as an index property under ASTM D4833-07. The operational boundary is thickness-related: when the membrane is installed directly over angular aggregate larger than 20 mm, the probability of puncture increases, and specifiers commonly require a minimum gauge of 250 µm unless a sand blinding layer is placed underneath. Finished products include damp-proof course membranes, underslab vapour barriers, and temporary weather-protection sheets.

    Adhesive-lamination sealant web for liquid-packaging laminates

    Q1018H is converted as a blown-film sealant web that is adhesive-laminated to oriented polyester or biaxially oriented polypropylene print webs. The film formulation is 80–85 wt% Q1018H, 15–20 wt% high-pressure LDPE, and 1.0–1.5 wt% slip/antiblock masterbatch; film thickness is 30–60 µm, and the corona-treated surface is adjusted to 38–42 mN/m before lamination. Blown-film processing uses a die gap of 1.8 mm and a blow-up ratio of 2.2:1, with controlled winding tension to avoid blocking during storage. In lamination, a solventless polyurethane adhesive is applied at 2.0–2.5 g/m² through a multi-roller coater, the nip is held at 65–75 °C, and the laminate is cured for 48 h at 35–40 °C before slitting or pouch conversion.

    Food-contact laminates using this sealant web are evaluated under FDA 21 CFR 177.1520 for the olefin polymer layer and 21 CFR 175.105 for the laminating adhesive. EU compliance follows (EU) No 10/2011, with overall migration below 10 mg/dm² and specific migration limits checked for each adhesive and additive component; because the adhesive is not fully polymerised until the cure cycle is complete, packages are not filled with aggressive liquids before the 48 h cure window expires. Seal strength of the converted pouch is tested under ASTM F88/F88M-21. The sealant web is not recommended for retort processing at 121 °C, and published data for Q1018H steam-retort performance in this structure is limited; end-use sealing windows and seal-strength retention should be validated on the specific lamination line. Terminal products include non-retort liquid sachets, bag-in-box outer liners, and stand-up pouches for liquid packaging.

    Application scenarioStandard or regulationProperty or test condition
    Heavy-duty FIBC linerASTM D1709-16aDart impact, Method A
    Frozen-food packagingFDA 21 CFR 177.1520Olefin polymer food-contact clearance
    Agricultural greenhouse filmEN 13206:2017Thermoplastic covering film performance
    Construction damp-proof membraneEN 13967:2012Flexible sheet waterproofing characteristics
    Adhesive-lamination sealant webASTM F88/F88M-21Seal strength of flexible barrier materials
    Free Quote

    Competitive Lotrene LLDPE Q1018H prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615365186327

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Lotrene LLDPE Q1018H is a butene-1 linear low-density polyethylene blown-film extrusion resin supplied by QAPCO. The polymer is produced in a gas-phase process and sold as a pelletised grade containing an antioxidant/processing stabiliser system and a slip/antiblock additive package. Its nominal melt mass-flow rate is 1.0 g/10 min measured at 190 °C under 2.16 kg load according to ISO 1133-1:2022 or ASTM D1238-20. The nominal density is 0.918 g/cm³ at 23 °C according to ISO 1183-1:2019 or ASTM D1505-18. These base specifications place the grade in the general-purpose film window for low-to-medium gauge applications in which low seal initiation and toughness are required without the cost of a hexene- or octene-based resin.

    The product is used in blown-film structures for carrier bags, industrial liners, heavy-duty sacks, agricultural film, lamination film, and coextruded films. The H suffix indicates a formulated additive package that reduces blocking and lowers coefficient of friction after film winding. This distinguishes the grade from unformulated C4-LLDPE variants that require converter-added slip/antiblock masterbatch. Additive bloom requires 24 h to 72 h after film production to reach near-equilibrium, which affects subsequent print and lamination adhesion.

    Nominal Specification Values and the Standards That Anchor Them

    PropertyTest methodNominal value
    Melt mass-flow rate (190 °C, 2.16 kg)ISO 1133-1:2022 / ASTM D1238-201.0 g/10 min
    Density (23 °C)ISO 1183-1:2019 / ASTM D1505-180.918 g/cm³
    Comonomer typeProducer specificationButene-1 (C4)
    Melting peak temperature (DSC)ISO 11357-3121–124 °C
    AdditivesProducer formulationAntioxidant, slip, antiblock

    Published film mechanical data for this specific grade under every possible line configuration are limited. The following values should therefore be treated as class-typical ranges for a 0.918 g/cm³ C4-LLDPE with a 1.0 g/10 min melt index. For a 30 µm blown film produced at a 2.5:1 blow-up ratio, the producer-documented range of tensile yield strength is typically 10 to 12 MPa in both MD and TD under ISO 527-3. Dart drop impact F50 under ASTM D1709A is generally between 80 g and 120 g; Elmendorf tear under ASTM D1922 is usually higher in TD than MD. These values shift with die gap, frost-line height, gauge, and additive concentration. A certificate of analysis from the lot should be requested for critical outlets.

    How Does Q1018H Perform on Blown Film Extrusion Lines?

    Processability is defined by the melt index and the narrow short-chain branching distribution produced by the butene-1 comonomer. On a 65 mm 30:1 L/D grooved-feed extruder feeding a 200 mm spiral die with a 1.2 mm die gap, the melt-temperature window is 185 °C to 230 °C. The lower boundary is set by unstable screw pressure and high melt viscosity; the upper boundary is set by gel formation, oxidative chain scission, and odour. Output is controlled by die pressure, although the low density of the resin results in lower die pressure than an HDPE or higher-density LLDPE of the same melt index. High-output lines with die gaps below 0.8 mm may develop melt fracture unless melt temperature is raised or a polymer processing aid is added.

    Bubble stability is acceptable over a blow-up ratio range of 2.0:1 to 3.0:1. Frost-line height should be maintained between 4 and 8 die diameters for balanced MD/TD orientation. At the low end, film can carry excessive quench stress; at the high end, TD tear improves while MD tear and dart impact fall. On production lines with internal bubble cooling, cooling air volume should be adjusted before increasing line speed to avoid film blocking on the collapsing frame. The resin is not optimised for cast-film extrusion, although limited cast use is possible on lines with a gear pump and a sharp lip profile.

    Pre-drying is not routinely required when pellet storage is below 40 °C and RH 60%. If bags have been exposed to RH > 70%, a dehumidified hopper dryer at 60 °C for 2 h is recommended. Do not exceed melt temperature 280 °C. Avoid purging with acidic or ionomer residues; a fractional-melt LDPE or MDPE purge is preferred to reduce retained butene-1 volatiles and shorten changeovers.

    When Q1018H Replaces Hexene- or Octene-Based LLDPE in Film Structures

    Substitution of Q1018H for a C6/C8 LLDPE of equivalent 1.0 g/10 min melt index and 0.918 g/cm³ density reduces film toughness. Under ASTM D1709A, dart drop impact F50 for 25 µm film is typically 15% to 30% lower because butene branches generate a lower tie-molecule concentration than hexene or octene branches at the same comonomer content. Machine-direction Elmendorf tear under ASTM D1922 is usually 10% to 25% lower. Haze under ASTM D1003 is higher, and gloss under ASTM D2457 is lower. Therefore the grade is not recommended for frozen-food packaging, high-puncture silage film, high-performance stretch hood film, or ultra-thin gauge films where a C6/C8 LLDPE specification is mandatory.

    The processing advantage is bubble stability at lower melt temperature and a wider die-gap window. Because the C4 grade has a lower extensional viscosity plateau than many C6/C8 resins, it typically tolerates higher stalk height and less sophisticated air-ring control on older blown-film lines. When a converter evaluates replacement, comparative trials should be run at constant thickness, BUR, and frost-line height. Dart impact and tear should be measured using ASTM D1709A and ASTM D1922.

    The table below summarises directional performance differences when Q1018H is used in place of a C6/C8 LLDPE of the same density and melt index.

    Directional performance differences versus C6/C8 LLDPE of equal density and melt index
    Performance propertyTest methodDirectional change for Q1018H
    Dart drop impact F50ASTM D1709ALower
    Elmendorf tear strength, MDASTM D1922Lower
    Elmendorf tear strength, TDASTM D1922Moderately lower
    HazeASTM D1003Higher
    GlossASTM D2457Lower
    Bubble stability at low melt temperatureProduction line observationWider
    Screw pressure at equal outputProduction line observationComparable to slightly lower
    Seal initiation temperatureASTM F88Comparable

    Compared with high-pressure LDPE of the same 0.918 g/cm³ density, Q1018H requires more attention to bubble control because its linear backbone lacks the strain-hardening characteristics of LDPE. Blends of Q1018H with 10% to 30% LDPE are common on older lines to widen bubble stability and improve melt extensibility. In such blends, tensile yield and puncture strength remain above LDPE-only film under ISO 527-3 and ASTM D5748.

    Compared with a metallocene C4-LLDPE of similar melt index, Q1018H has a broader molecular weight distribution. Processability on older extruders is generally easier, but optical properties and toughness are lower. Haze measurements under ASTM D1003 will be higher; dart impact under ASTM D1709A will be lower. These trade-offs are important for clear garment bags or high-clarity overwrap.

    Food-contact evaluations for this olefin polymer are typically based on 21 CFR 177.1520 and EU Regulation No 10/2011; the producer’s declaration should be obtained before use in direct food contact. Migration limits depend on film thickness, additive package, and extraction conditions. The material is not intended for medical applications or steam autoclave use; film distortion begins near 95 °C.

    Store in a dry, UV-protected area below 40 °C. Use within 12 months of delivery for bagged resin. Opened bags should be resealed to prevent moisture and dust contamination. Rotation of inventory is standard, but do not mix bags from different lots without re-testing slip and antiblock bloom, because surface properties may vary in the first 72 h after processing.

    Top