Products

Sinopec Yangzi mPE-L mLLDPE mPE-L F184P

    • Product Name: Sinopec Yangzi mPE-L mLLDPE mPE-L F184P
    • 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 302343
    Density 0.918 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 4.0 g/10 min
    Melting Point 118 °C
    Vicat Softening Temperature 90 °C
    Tensile Strength At Break ≥20 MPa
    Elongation At Break ≥500%
    Dart Impact Strength ≥100 g
    Elmendorf Tear Strength Md ≥100 g
    Elmendorf Tear Strength Td ≥200 g
    Haze ≤6%
    Gloss 45 ≥80%
    Seal Initiation Temperature 95 °C
    Brittleness Temperature ≤-70 °C
    Molecular Weight Distribution Narrow

    As an accredited Sinopec Yangzi mPE-L mLLDPE mPE-L F184P factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Sinopec Yangzi mPE-L F184P mLLDPE is supplied in 25 kg polyethylene-lined woven bags, palletized and shrink-wrapped for shipment.
    Container Loading (20′ FCL) 20′ FCL loaded with 25 MT of Sinopec Yangzi mPE-L F184P in 25 kg bags, palletized, forklift-loaded, and securely sealed.
    Shipping Sinopec Yangzi mPE-L F184P mLLDPE ships as a non-hazardous polymer in 25 kg polyethylene-lined woven bags, palletized and shrink-wrapped. Transport and store in a cool, dry, ventilated area away from direct sunlight, moisture, heat, and contamination; avoid damaged packaging.
    Storage Store Sinopec Yangzi mPE-L mLLDPE mPE-L F184P in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep bags/containers closed, clean, and undamaged; palletize off the ground to prevent moisture uptake and contamination. Avoid prolonged high-temperature and UV exposure, and follow the SDS and local regulations.
    Shelf Life Store in a cool, dry, ventilated place away from direct sunlight; shelf life is typically 24 months in unopened original packaging.
    Application of Sinopec Yangzi mPE-L mLLDPE mPE-L F184P

    When 30 wt% mPE-L F184P Replaces Conventional C4-LLDPE in Frozen-Food Blown Film

    Frozen-food blown film operations using Sinopec Yangzi mPE-L F184P standardise the addition level at 20 wt% to 40 wt% of the total polyolefin feed, with the most frequently documented production formulation comprising 30 wt% F184P, 50 wt% low-density polyethylene, and 20 wt% Ziegler-Natta C4-LLDPE. Grade F184P is a metallocene-catalysed ethylene/α-olefin linear low-density polyethylene with a nominal melt flow index of 1.0 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg and a nominal density of 0.918 g/cm³ under ISO 1183-1. The blend is directed to frozen-food packaging because the Ziegler-Natta C4-LLDPE fraction supplies process stability, while the metallocene F184P phase raises low-temperature dart impact and seal toughness. Food-contact compliance is documented under FDA 21 CFR 177.1520(c) for olefin polymers and under EU Regulation (EU) No 10/2011 with overall migration limited to 10 mg/dm² for aqueous and fatty food simulants. The downstream production route is blown-film coextrusion on 55–75 mm single-screw extruders with L/D 30:1 barrier screws, low-pressure die heads, 1.8–2.4 mm die gaps, 2.0:1–2.8:1 blow-up ratio, and melt temperatures of 190–215 °C. On production-scale lines, the substitution of C4-LLDPE by F184P at 30 wt% routinely changes the screw pressure profile and raises melt pressure by a measurable increment because the metallocene phase has lower shear thinning than conventional linear-low resin; operators compensate by increasing rear-barrel set points by 10–15 °C or by reducing screw speed by 5–10%. At addition levels above 40 wt%, bubble instability and die-lip build-up become the process-limiting factors, particularly on unprotected single-lip air rings. Film property verification is anchored to ASTM D1709/A for dart impact, ISO 6383-2 for trouser tear, and ISO 527-3 for film tensile properties. Terminal finished product types include IQF frozen vegetable bags, frozen meat overwrap, ice cream pouches, and frozen seafood pillow packs where seal integrity at freezer temperatures is the primary acceptance criterion.

    Cast-film sealant webs for laminated pouches and liquid sachets are run with F184P at 70 wt% to 85 wt% of the seal-layer feed, while the remaining 15–30 wt% is typically a low-density polyethylene grade selected to suppress draw resonance at high line speed. The sealant layer is produced by cast-film coextrusion through 0.5–0.8 mm die gaps on extruders of 65–90 mm barrel diameter with L/D 30:1–33:1, screen packs of 80/120/80 mesh, and melt temperatures in the 220–250 °C range. The air gap is kept between 15 mm and 25 mm, and the polished chill roll is controlled at 18–24 °C to stabilise the amorphous surface layer for low seal initiation. Compliance for food-contact sealant layers is handled under FDA 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011; converters must validate specific migration for the final laminate structure under EC 1935/2004 because the sealant layer is not evaluated in isolation. The addition of F184P at this level lowers seal initiation temperature relative to conventional LLDPE sealants, with laboratory comparison performed under ASTM F88 for seal strength and ASTM F1921 for hot-tack performance. At the process boundary, increasing F184P above 85 wt% in cast films without the LDPE modifier is associated with draw resonance on thin gauge structures below 25 µm and may require an increase in air-gap distance or a reduction in line speed by 10–15%. The terminal articles are stand-up pouches, liquid detergent sachets, retort-overwrap laminates, and microwaveable food pouches in which the cast sealant web is adhesive-laminated to polyester, aluminium foil, or biaxially oriented polypropylene.

    What Limits F184P Addition in Agricultural Silage and Greenhouse Cover Film?

    Agricultural silage and greenhouse cover film formulations exploit the puncture and tear resistance of F184P at addition ratios of 40 wt% to 60 wt% for greenhouse sheeting and 20 wt% to 35 wt% for silage bale wrap; the remainder is LDPE with a UV-stabiliser masterbatch based on hindered amine light stabilisers at 0.5–1.5 wt% letdown. The governing compliance standard for thermoplastic covering films used in agriculture is EN 13206:2017, which classifies film durability, tensile, tear, and impact characteristics; silage films are additionally assessed against farm-specific oxygen permeability limits and mechanical integrity checks after bale handling. Downstream production is blown-film extrusion on 65–85 mm extruders with internal bubble cooling, 2.3–2.5 mm die gaps, 2.5:1–3.0:1 blow-up ratio, and melt temperatures of 195–225 °C. The central process conflict is that F184P improves impact but the narrow molecular weight distribution of metallocene resin reduces bubble stability at high blow-up ratio; therefore, the LDPE fraction is not removed when the addition ratio is pushed toward 60 wt%. Field-scale observation on greenhouse film lines shows that when F184P addition exceeds 60 wt% at 3.0:1 blow-up ratio, the bubble begins to flap and the frost line becomes uneven, causing thickness variation outside the ±5% tolerance required by EN 13206:2017 classification. Verification of physical performance is anchored to ISO 7765-1 for puncture resistance, ISO 6383-2 for tear resistance, and ISO 527-3 for tensile properties. Terminal finished product types include greenhouse cover film in 150–200 µm thickness, low-tunnel cladding, silage bale wrap, and underlay agricultural film used in horticultural ground cover systems.

    A 75 mm single-screw blown-film line with internal bubble cooling producing heavy-duty industrial liners typically sets the F184P addition level between 30 wt% and 60 wt% in blends with LDPE and C4-LLDPE; the upper addition limit is dictated by melt strength rather than by film property loss. The dominant downstream process is thick-gauge blown-film extrusion on extruders of 75–90 mm barrel diameter with L/D 30:1–36:1, die gaps of 2.0–2.5 mm, blow-up ratio 2.2:1–2.8:1, and melt temperatures of 200–230 °C. The film is run at 100–250 µm for FIBC inner liners and octabin liners, where puncture and tear under static load are the acceptance criteria. Compliance for flexible intermediate bulk container liners is evaluated under ISO 21898:2004, and packaging-material heavy metal limits are verified under EU Directive 94/62/EC Annex II with total lead, cadmium, mercury, and chromium(VI) limited to 100 mg/kg. The processing limitation is bubble sag: at 200 µm thickness and 2.5:1 blow-up ratio, replacing more than 60 wt% of a high-pressure LDPE with F184P reduces bubble stiffness, increases frost-line movement, and forces a reduction in internal bubble cooling air velocity. To maintain output, the LDPE fraction is retained at 20–30 wt% as a melt-strength modifier. Physical verification uses ISO 7765-1 for puncture resistance, ISO 6383-2 for tear resistance, and ASTM D1709/A for impact. Terminal finished product types include FIBC inner liners, octabin liners, drum liners for viscous chemical products, and temporary protection sheeting for construction and equipment storage.

    Form-Fill-Seal Dry-Food Packaging: Seal Initiation, Hot Tack, and Migration Boundaries

    Vertical form-fill-seal and horizontal form-fill-seal dry-food packaging lines use F184P at 20 wt% to 40 wt% in monolayer blown-film structures and at 50 wt% to 80 wt% in coextruded sealant layers. The process window is set by the sealing jaw conditions: seal-bar temperatures of 115–135 °C, dwell times of 0.2–0.4 s, and jaw pressures of 2.0–3.0 bar on high-speed lines operating at 60–100 bags/min. F184P is incorporated because the metallocene resin gives a measurable lowering of seal initiation temperature and a wider hot-tack envelope than conventional LLDPE sealants. Compliance is documented under FDA 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011, with specific migration testing conducted on the sealed film under EC 1935/2004; the overall migration limit is 10 mg/dm². Laboratory synchronisation of line performance is performed with ASTM F88 for seal strength, ASTM F1921 for hot tack, and ISO 8295 for coefficient of friction. On high-speed VFFS equipment, the operational boundary is pellet surface condensation: at ambient relative humidity above 60%, surface moisture on pellets can cause feed-throat bridging, so dry-air hopper purging is required. Below 20 wt% F184P, the hot-tack advantage becomes marginal and seal failures increase on pillow packs with fine powder products. Above 40 wt% in monolayer film, the extruder backpressure rises sufficiently to reduce throughput and may require die-lip cleaning at intervals shorter than normal production cycles. Terminal finished product types include dry snack pillow packs, cereal liners, powdered beverage sachets, and spice pouches.

    Draw resonance, gel dispersion, and low-temperature flex-crack resistance are the controlling factors in logistics protective over-wrap and e-commerce mailer film produced with F184P. The formulation uses 30 wt% to 50 wt% F184P combined with LDPE and, where sustainability targets require, up to 25 wt% post-consumer recycled LDPE; the F184P fraction restores dart impact and tear after the recycled fraction degrades those properties. Compliance is governed by EU Directive 94/62/EC Annex II for packaging heavy metal limits at 100 mg/kg, REACH Annex XVII for restricted substances, and RoHS 2011/65/EU for electrical and electronic transport packaging where applicable. The downstream production process is blown-film coextrusion on 55–70 mm extruders with L/D 30:1, 1.8–2.2 mm die gaps, 2.3:1–2.7:1 blow-up ratio, and melt temperatures of 190–220 °C. The main process conflict is gel formation from the post-consumer recycled fraction: screen packs of 100/120/100 mesh are required, and pressure drop across the screen pack is monitored continuously to avoid gel breakthrough at the die lip. The addition of F184P above 50 wt% in this structure is not recommended because the narrow molecular weight distribution increases the draw resonance tendency on thin gauge versions below 40 µm. Flex-crack testing is anchored to ASTM F392 and dart impact to ASTM D1709/A. Terminal finished product types include e-commerce mailer outer layers, protective over-wrap for furniture, surface-protection film for appliances, and padded envelope outer shells.

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    Certification & Compliance
    More Introduction

    Sinopec Yangzi mPE-L mLLDPE mPE-L F184P is a metallocene-catalysed linear low-density polyethylene film resin designated by a nominal density of 0.918 g/cm³ in accordance with ISO 1183-1:2019 and a melt flow rate of 4.0 g/10 min at 190 °C/2.16 kg in accordance with ISO 1133-1:2022. The resin is supplied in pellet form and is positioned for cast film, stretch film, lamination film, and selected blown film structures where high throughput, low seal initiation temperature, and film uniformity outweigh the need for maximum melt strength. Compared with conventional Ziegler-Natta LLDPE of equivalent density, F184P yields a narrower molecular weight distribution, a more uniform comonomer distribution, and a reduced low-molecular-weight fraction. These molecular features improve optical clarity, heat-seal initiation, and dart impact consistency while lowering melt elasticity and elongational viscosity, which requires converter adjustment of melt temperature, air gap, and edge pinning on cast film lines.

    On a production-scale cast film line using a 90 mm single-screw extruder with L/D 30:1 and a barrier screw, the resin is typically processed at melt temperatures from 240 °C to 260 °C, with die temperatures held near the upper limit to reduce edge tear. Chill roll temperatures between 18 °C and 24 °C are common for film thicknesses of 15 μm to 50 μm. Because F184P has a narrow molecular weight distribution, melt curtain stability is strongly influenced by air gap. Production lines generally operate with an air gap not exceeding 100 mm and use electrostatic edge pinning or an adjustable vacuum knife to suppress neck-in and melt resonance. Published product-specific data for every equipment configuration is limited, but the processing corridor described here is consistent with class-typical metallocene LLDPE behaviour on cast film equipment.

    What Structural Difference Separates F184P from Ziegler-Natta LLDPE Grades?

    F184P is produced with a single-site metallocene catalyst. The polymer has a polydispersity index commonly found in the range 2.0–3.0, whereas conventional Ziegler-Natta butene LLDPE grades typically fall between 3.5 and 5.0. The low-molecular-weight tail is smaller, which reduces hexane extractables, odour contribution, and die-lip build-up. The high-molecular-weight tail is also smaller, which lowers melt strength and reduces bubble stability on high-stalk blown film lines. Comonomer insertion is more random than in conventional LLDPE, suppressing the formation of long crystallisable ethylene sequences that scatter light. At 50 μm film thickness, haze values for this metallocene class are therefore lower than those of a Ziegler-Natta LLDPE of similar density, and dart impact per unit thickness is improved. The advantage is not universal: on high-stalk blown film towers the lower melt elasticity of F184P may cause bubble flutter and gauge variation unless the resin is blended with LDPE at 10–20 wt%.

    Cast Film Die Build-Up and Extractable Fractions in Food Packaging Structures

    Die build-up and plate-out are governed by the low-molecular-weight fraction and by the additive package. For F184P, the metallocene catalyst system reduces the concentration of low-molecular-weight oligomers, so the n-hexane extractable fraction under FDA 21 CFR 177.1520 extraction conditions is lower than that of conventional Ziegler-Natta LLDPE. Converters running 20 μm monolayer and multilayer films for fresh produce, bakery, and frozen food packaging report less frequent die-lip cleaning cycles when compared with Ziegler-Natta LLDPE at the same melt temperature. For organoleptic-sensitive applications, laboratory panels using DIN 10955:2004 for odour and taste transfer test film samples; the resin is generally suitable for indirect food contact when the fabricated article meets Regulation (EU) No 10/2011 Annex I migration limits. The specific migration limit for total non-volatile extractives should be confirmed because downstream additives, printing inks, and lamination adhesives can dominate the final compliance profile.

    Parameter mPE-L F184P class Conventional ZN-LLDPE reference Test basis
    Density 0.918 g/cm³ 0.918 g/cm³ ISO 1183-1:2019
    Melt flow rate 4.0 g/10 min 1.0–2.0 g/10 min 190 °C/2.16 kg, ISO 1133-1:2022
    Polydispersity index 2.0–3.0 3.5–5.0 GPC with polystyrene or PE standards
    Melt strength lower higher Rheotens elongational viscosity test
    Chill roll temperature 18–24 °C 15–22 °C Production cast film line
    Recommended air gap <100 mm 80–120 mm Cast film with edge pinning

    When Heat-Seal Initiation and Hot-Tack Force Become Critical on Vertical Form-Fill-Seal Lines

    Vertical form-fill-seal packaging operations demand a narrow heat-seal temperature window and rapid hot-tack development. The melting peak of F184P is normally observed between 118 °C and 122 °C by differential scanning calorimetry at 10 K/min under ISO 11357-3:2018. The reduction in low-molecular-weight species permits a lower seal initiation temperature than that of conventional Ziegler-Natta LLDPE. On pilot VFFS jaw sealers with 0.5 s dwell, seal strength at 120 °C often exceeds 4 N/25 mm when measured by ASTM F88/F88M-21. These values are class-typical for 50 μm cast film and must be verified on the actual film structure, because lamination layers, antiblock additives, and corona treatment shift seal response.

    Cast stretch film made from F184P or from a skin layer containing F184P can be pre-stretched up to 200–250% on power pre-stretch units. Tensile elongation at break under ISO 527-3:2018 is typically above 500% for 0.918 g/cm³ metallocene LLDPE of this melt flow class. Compared with an octene-based metallocene plastomer of density 0.902 g/cm³, F184P has a higher melting point and higher stiffness, which allows faster packaging-machine line speeds where dimensional stability at ambient temperature is required. Compared with a low-density polyethylene homopolymer, F184P gives lower melt elasticity and should not be expected to reproduce the neck-in and draw-down behaviour of autoclave LDPE in extrusion coating. For lamination film, corona treatment is used to raise surface tension above 38 mN/m; treatment decays over time, so inline treatment immediately before winding is preferred.

    Processing Boundaries and Additive Incompatibility Limits

    F184P is not a high-melt-strength resin. On single-screw blown film lines with high stalk length and without internal bubble cooling, the film may show gauge variation and bubble flutter when F184P constitutes more than 30 wt% of the dry blend unless LDPE is added at 10–20 wt%. The resin does not require predrying under normal ambient storage conditions because the olefin matrix has negligible moisture affinity; however, surface condensation from cold warehouse transfer can create gels or optical defects when ambient relative humidity remains above 60% for extended periods. Avoid mixing with pro-degradant transition-metal stearates if the end product needs a service life beyond 12 months. During extrusion, melt temperatures above 280 °C should be avoided because polyethylene degradation accelerates and may form carbonyl species detectable by infrared spectroscopy near 1715 cm⁻¹. A 200-mesh screen pack is typical for capturing crosslinked gel particles; screen pressure increase above 80 bar signals polymer degradation or contaminant accumulation and requires equipment inspection.

    Property or compliance parameter Designation or test method Condition
    Melt flow rate ISO 1133-1:2022 190 °C, 2.16 kg
    Density ISO 1183-1:2019 Method A
    Melting point ISO 11357-3:2018 10 K/min
    Tensile properties ISO 527-3:2018 50 μm cast film
    Dart impact ASTM D1709-22 50 μm film
    Haze ASTM D1003-21 50 μm film
    EU food contact Regulation (EU) No 10/2011 Annex I Migration testing
    US food contact FDA 21 CFR 177.1520 Olefin polymers
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