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SABIC LLDPE P218

    • Product Name: SABIC LLDPE P218
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 704142
    Density 0.918 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 2.0 g/10 min
    Melting Point 124 °C
    Vicat Softening Point 90 °C
    Tensile Strength At Yield 13 MPa
    Elongation At Break 900 %
    Flexural Modulus 300 MPa
    Shore Hardness D 54
    Brittleness Temperature -75 °C
    Environmental Stress Crack Resistance F50 > 1000 h

    As an accredited SABIC LLDPE P218 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing SABIC LLDPE P218 is supplied as pellets in 25 kg bags, palletized and stretch-wrapped for safe handling and transport.
    Container Loading (20′ FCL) 20′ FCL container loading of SABIC LLDPE P218: linear low-density polyethylene resin, packed in palletized bags for safe transit.
    Shipping SABIC LLDPE P218 is shipped as free-flowing polyethylene pellets in 25 kg bags, octabins, or jumbo bags, and is containerized for bulk transport. It is non-hazardous under normal transport conditions and not classified as dangerous goods, though loads should be kept dry, clean, and protected from direct sunlight and excessive heat.
    Storage Store SABIC LLDPE P218 in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and strong oxidizers. Keep containers tightly sealed in original packaging to prevent contamination and moisture pickup. Avoid excessive humidity and static buildup. No special storage hazards exist, but material is combustible, so keep away from open flames.
    Shelf Life Shelf life is indefinite when stored in a cool, dry, shaded area with packaging intact.
    Application of SABIC LLDPE P218

    What Keeps Silage Cover Film Tear-Resistant After 12 Months of UV Exposure?

    Agricultural silage cover and greenhouse cladding films produced from P218 are run on high-output blown film lines with grooved-feed extruders in the 60–90 mm diameter range and L/D ratios of 30:1. The nominal density of 0.918 g/cm³ and melt flow rate of 2.0 g/10 min at 190 °C/2.16 kg permit die gaps between 1.8 mm and 2.4 mm without excessive backpressure. Greenhouse cover film commonly uses a blend of 80–85 wt% P218 with 15–20 wt% LDPE to raise bubble stability at blow-up ratios of 2.2:1 to 2.8:1; silage cover film may be run at 100% P218 when frost line height is held at 600–750 mm above the die face. UV stabilization is introduced through a HALS/benzophenone masterbatch at 4–6 wt% for greenhouse film and 2–3 wt% for silage cover film, with black/white concentrate loading of 6–8 wt% in coextruded three-layer silage sheets to provide the white outer layer for heat reflectance and black inner layer for light exclusion. Melt temperatures are maintained at 200–215 °C; die temperatures are set 5–10 °C lower to reduce die-lip oxidation. Downstream production includes surface-treated layflat guidance through a collapsing frame with wooden or cork slats, air ring chilled to 8–12 °C, and gap-wound rolls to avoid blocking. Terminal products include 25–40 µm silage cover film, 150–200 µm greenhouse film, and 30–60 µm mulch film with punched holes. Compliance for agricultural film in the EU is assessed under EN 13206 and REACH Regulation EC 1907/2006; tensile and tear properties are measured per ISO 527-3 and ISO 6383-2, while UV aging is compared against ASTM D4329 or ISO 4892-2. Operational boundary: P218 film should be stored at <60% RH; no pre-drying is required below 60% RH, and melt temperatures above 240 °C can initiate gel formation at the screw tips of long-L/D extruders.

    When P218 Is Down-Gauged in FFS Bag Construction

    When P218 is down-gauged in form-fill-seal bag construction, the three-layer coextrusion line on Starlinger or Windmöller & Hölscher equipment uses die diameters from 250 mm to 400 mm and die gaps of 2.2–2.6 mm. The core layer typically carries 60–80 wt% P218; the inner and outer layers may be formulated at 70–75 wt% P218 with 25–30 wt% LDPE and a seal skin to avoid low hot-tack under dusty filling conditions. Addition of antiblock masterbatch is kept at 1.5–2.5 wt%, and slip masterbatch is held at 0.5–1.0 wt% because excessive erucamide blooms under FFS filling pressure and reduces the seal initiation window. Film thickness is down-gauged from 120 µm to 80–90 µm only after dart impact measured per ASTM D1709A remains above 700 g on the production roll; this is a critical threshold derived from field bag failures and is not a supplier specification. The blown-film process uses a melt temperature of 205–220 °C, blow-up ratio of 2.0:1 to 2.4:1, and frost line height of 450–600 mm. The unstable frost line region below 400 mm produces visible bubble flutter and reduces impact resistance in the machine direction. FFS conversion requires a seal bar temperature of 140–165 °C and dwell time of 0.8–1.5 s, after which the sack is filled, degassed, and heat-sealed through a pinch top. Terminal product types include 25 kg and 50 kg polymer pellet sacks, 10–25 kg fertilizer sacks with micro-perforation, and non-dangerous goods packaging where the outer ply carries the lithographic print. Compliance is anchored to ASTM D882 for tensile, ASTM D1709A for dart impact, ISO 7965-2 for drop testing of filled sacks, and ASTM D1894 for coefficient of friction. Published data for P218-specific FFS burst strength on monolayer structures is limited; coextruded three-layer data should be generated on the actual line.

    In dry-food and frozen-food applications, direct food-contact film converted from P218 is qualified under FDA 21 CFR 177.1520 for olefin polymers, EU Regulation No 10/2011 with an overall migration limit of 10 mg/dm² when tested per EN 1186-1, and China GB 9685-2016 for additives. Monolayer blown film runs at 100% P218 or at 85–90 wt% P218 with 10–15 wt% LDPE for improved tear propagation. Slip masterbatch based on erucamide is dosed at 1–2 wt%, and synthetic silica antiblock masterbatch is dosed at 1–2 wt%, giving a surface coefficient of friction below 0.35 after 24 h conditioning when measured per ASTM D1894. Blown film extrusion uses a die gap of 1.8–2.0 mm, melt temperature of 190–205 °C, blow-up ratio of 2.4:1 to 2.8:1, and frost line height of 500–650 mm. The heat-seal layer is processed on an in-line FFS or bag-making unit with jaw temperature set points of 120–150 °C, dwell time of 0.5–1.0 s, and seal pressure of 0.2–0.4 MPa. Terminal products include 20–50 µm side-sealed bags for frozen vegetables, dry powder pouches, bakery overwrap, and flow-pack film for pasta and cereals. The operational boundary is set by the hot-tack window of this LLDPE grade; converters switching from octene-based metallocene grades should verify seal initiation temperature per ASTM F1921 and not assume identical hot-tack strength. Food-contact compliance requires migration testing with the actual masterbatch formulation because additive bloom can alter organoleptic properties after 7 days at 40 °C.

    Standard or regulationClause / MethodCondition or limitApplication
    FDA 21 CFR 177.1520Olefin polymers for food contactConditions of use A–H per 21 CFR 176.170Food-contact film
    EU Regulation No 10/2011Plastic FCM overall migrationOML 10 mg/dm²; EN 1186-1Food-contact film
    ASTM D1238 / ISO 1133-1:2022Melt flow rate190 °C, 2.16 kgAll scenarios
    ASTM D882Tensile properties of thin plastic sheetingSpeed 500 mm/minAll film scenarios
    ASTM D1709ADart impact of polyethylene film38 mm dart, 66 cm dropFFS sacks, liners, carrier bags
    ASTM D1876Peel resistance of adhesives2.0 N/15 mm minimumLamination substrate
    ASTM F1921Hot-tack of thermoplastic filmsSeal initiation temperatureFood-contact film
    EN 13206Agricultural and horticultural filmsUV stability, thickness toleranceSilage and greenhouse film
    ASTM E1745-17Water vapor retarders under concrete slabsPermeance limitConstruction vapor retarder

    Liners, Vapor Retarders, and the 0.2 mm Extrusion Die Gap Trade-Off

    Thick-gauge blown film for industrial drum liners, chemical packaging film, and construction vapor retarders is produced from P218 at thicknesses from 100 µm to 250 µm on blown film lines with die diameters of 150–300 mm and die gaps deliberately opened to 2.2–2.5 mm. The wider die gap prevents melt fracture and maintains bubble symmetry at low blow-up ratios of 1.8:1 to 2.2:1; running the same output through a 1.5 mm die gap produces visible shark-skin on the inner bubble surface. Formulation for vapor retarder film under concrete slabs consists of 100% P218 or 80–90 wt% P218 with 10–20 wt% LDPE, carbon black masterbatch at 2–4 wt%, and process aid at 0.3–0.5 wt% to reduce die-lip build-up over multi-week campaigns. Melt temperature is held at 200–215 °C; barrel temperatures in the feed zone remain below 180 °C to prevent premature pellet softening in grooved-feed sections. Construction vapor retarder film is tested against ASTM E1745-17 and ASTM E96 for water vapor transmission, while drum liners require chemical compatibility checks per ASTM D543 for aggressive solvents and powder detergents. Terminal products include 150 µm and 200 µm polyethylene vapor barriers, 100–150 µm drum liners for solvents and powder detergents, and 200–250 µm industrial can liners. Tensile properties are measured per ASTM D882; tear resistance per ISO 6383-2. The limitation of P218 in these thick-gauge structures is heat-seal strength at thicknesses above 150 µm; a minimum jaw temperature of 150 °C and dwell time of 1.5 s are required on continuous heat-sealing lines.

    In extrusion and adhesive lamination structures for snack, dry beverage, and medical packaging, P218 is inserted as the sealant web at 20–40 µm and bonded to polyester, biaxially oriented polypropylene, or aluminium foil through a separate LDPE extrudate at melt temperatures of 290–320 °C. The lamination-grade formulation avoids slip migration into the laminating nip: only 1.0–1.5 wt% antiblock masterbatch is used, and slip additive is omitted in the first 7 days after surface treatment because erucamide bloom can reduce peel strength below 2.0 N/15 mm when tested per ASTM D1876. P218 constitutes 90–100 wt% of the sealant layer; the remainder is LDPE or an anhydride-modified LLDPE tie concentrate at 0–10 wt% when higher seal-through-contamination strength is required. The substrate film is produced on a cast or blown line with die temperature at 195–205 °C, and corona treatment is set to 38–42 mN/m before lamination. Terminal structures include 3-ply and 4-ply laminated pouches, stand-up pouches for powdered beverages, and non-implantable medical device pouches where the seal layer is coextruded with a low-temperature seal peak. Compliance for direct food contact rests on FDA 21 CFR 177.1520, EU 10/2011, and GB 9685-2016; seal strength is verified per ASTM F88, with a minimum seal strength of 4.0 N/15 mm on production samples. Published data for P218-specific peel strength in extrusion lamination with aluminium foil is limited; full laminate structures must be tested after 48 h ageing.

    Dart impact retention becomes the limiting variable in carrier bag film containing post-industrial recycle.

    Down-gauging carrier bag film to 12 µm leaves little tolerance for thickness variation, so P218 is used as the virgin backbone at 60–100 wt%, with post-industrial recycled LLDPE/LDPE at 0–40 wt% in ribbed or embossed monolayer film. The formulation addition ratio for slip and antiblock concentrates is 1–2 wt% combined; the exact split depends on whether the film is surface-printed or heat-sealed. Blown film lines with die diameters of 100–200 mm, die gaps of 1.5–2.0 mm, and blow-up ratios of 2.5:1 to 3.0:1 are typical; melt temperature is 185–205 °C. Dart impact per ASTM D1709A and tear resistance per ISO 6383-2 are checked on every batch because the broad molecular weight distribution of recycled material can reduce machine-direction tear strength by 20–30% at 30 wt% recycle content; published data for P218-specific recycle retention curves is limited. Terminal products include 12–30 µm T-shirt carrier bags, 20–30 µm produce bags, and 25–50 µm general merchandise bags. Compliance in the EU is governed by REACH and the Packaging and Packaging Waste Directive 94/62/EC; in the US, ASTM D6400 is not automatically satisfied by P218 because P218 is not inherently biodegradable. This application is process-stable and requires routine collection only of thickness distribution and dart impact data.

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    Certification & Compliance
    More Introduction

    SABIC LLDPE P218 is a butene-comonomer linear low-density polyethylene supplied as free-flowing granules for general-purpose film conversion. The public specification positions the grade at a nominal density of 0.918 g/cm³ determined according to ISO 1183-1:2019 and a melt flow rate of 2.0 g/10 min at 190 °C under 2.16 kg load according to ISO 1133-1:2022. The same flow parameter can be cross-checked under ASTM D1238-20 Procedure A. The resin is stabilised with a hindered phenolic primary antioxidant and a phosphite secondary antioxidant, intended to limit oxidative degradation during pelletisation and downstream heat histories. The molecular weight distribution is not stated on the public datasheet, but published rheological data for this C4-LLDPE density/MFR class indicate a shear-thinning index broad enough to support blown film bubble stability and moderate cast film draw-down. P218 is therefore placed in the general-purpose C4-LLDPE film extrusion envelope rather than in high-stiffness fractional-melt or high-flow injection moulding segments. Values marked as class-typical in the following matrix are obtained from published C4-LLDPE film studies and should be verified against lot-specific certificates of analysis.

    Property Test condition and standard Nominal value or class-typical range
    Density ISO 1183-1:2019 0.918 g/cm³
    Melt flow rate ISO 1133-1:2022, 190 °C, 2.16 kg 2.0 g/10 min
    Tensile yield stress, 50 µm blown film ISO 527-3:2018 10–12 MPa class-typical
    Tensile elongation at break ISO 527-3:2018 >500% class-typical
    Dart drop impact, Type A, 50 µm ISO 7765-1:2015 100–140 g class-typical
    Elmendorf tear, MD/TD, 50 µm ISO 6383-2:1983 2.5–4.0 N / 4.0–6.0 N class-typical
    Seal initiation temperature ASTM F2029-16 / ASTM F88/F88M-21 95–105 °C class-typical

    How Does P218 Compare with Octene- and Metallocene-Catalysed LLDPE in Film Performance?

    The structural origin of performance differences between P218 and higher-alpha-olefin LLDPE grades is the ethyl branch population derived from butene comonomer. Ethyl branches disrupt crystallite thickness less efficiently than hexene or octene branches. The practical consequence is lower tie-chain concentration and reduced puncture and tear resistance compared with C6-LLDPE and metallocene C8-LLDPE at equivalent density. The processing advantage appears as lower melt elasticity in spiral mandrel dies, which allows P218 to run with lower die pressure and reduced amperage on grooved-feed extruders. The comparative matrix below uses published class-typical ranges for 50 µm monolayer film; it is not a guarantee of lot-specific performance.

    Performance parameter P218 C4-LLDPE class Ziegler C6-LLDPE class Metallocene C8-LLDPE class
    Dart drop impact, 50 µm 100–140 g 150–200 g >200 g
    Elmendorf tear, MD 2.5–4.0 N 3.0–4.5 N 3.5–5.5 N
    Elmendorf tear, TD 4.0–6.0 N 5.0–7.0 N 6.0–9.0 N
    Haze, 50 µm 8–15% 5–10% 2–6%
    Seal initiation temperature 100–110 °C 95–105 °C 85–95 °C

    For converters requiring high dart impact, low haze, or low seal initiation temperature in stretch-film or high-clarity packaging, P218 is not the direct alternative to metallocene C8 grades. It is selected where the cost position and stable extrusion pressure of a C4-LLDPE dominate the specification. Published data for this specific resin configuration in direct comparison with metallocene grades is limited; the ranges above are class-level reference values rather than certified property windows.

    Within a production-scale blown film line equipped with a 45 mm barrier screw, L/D 30:1, and a 250 mm spiral mandrel die with 1.2 mm die gap, P218 is processed at barrel set temperatures from 180 °C at the feed throat to 215 °C at the adapter. Melt temperature at the die lip is held between 200 °C and 220 °C. The bubble is maintained at a blow-up ratio of 2.0:1 to 2.5:1, with frost line height 4 to 6 die diameters above the air ring. When the blow-up ratio exceeds 2.8:1, stalk diameter variation increases beyond ±5 mm, and film gauge variation measured at 12 points across the lay-flat approaches ±8%. Melt pressure recorded between the screen changer and die adapter remains below 320 bar at 60 rpm; at 80 rpm, pressure rises to 360–400 bar, at which point the breaker plate pressure drop becomes the limiting element. The operating window narrows rapidly when melt temperature drops below 200 °C, because the apparent viscosity of C4-LLDPE rises steeply at low melt temperature. Published data for this specific equipment configuration is limited, but the pressure rise is consistent with class-level shear viscosity behaviour.

    Die Pressure and Melt Fracture Criteria in Cast Film Conversion

    Cast film lines running P218 at 25 µm gauge operate with a narrow melt temperature envelope. At 200 °C to 220 °C melt temperature, the extrudate from a 1500 mm slot die remains free of shark-skin melt fracture on a polished chill roll set to 18 °C. If the chill roll temperature drops below 15 °C, cooling rate at the film surface exceeds 100 °C/s and interfacial adhesion to the roll becomes uneven. The observed defect is edge-lift with irregular transverse gauge bands. At die gaps below 0.5 mm, the shear rate at the lip exceeds 1000 s⁻¹, and melt fracture appears as transverse ridges spaced 0.5–1.0 mm apart. A fluoropolymer processing aid masterbatch at 0.2–0.5 wt% is typically required when line speed exceeds 180 m/min, because the critical shear stress of P218 is reached earlier than for fractional-melt LDPE under comparable cast film conditions.

    Blending P218 at 20–30 wt% into injection moulding grades of LDPE or HDPE for thin-wall packaging applications is a low-shear distributive mixing operation; no special pre-drying is required at ambient storage below 60% relative humidity. On an 80-tonne hydraulic injection moulding machine with a general-purpose polyolefin screw, the clamp force requirement is governed by the base resin rather than by P218 because the P218 phase remains the minority component. Batch-to-batch variation in the P218 melt flow rate can shift the overall melt viscosity by ±0.2 g/10 min, which is within the repeatability window for this flow band under ISO 1133-1:2022.

    When Regrind Content Exceeds 30% in High-Speed Bag Conversion

    Recycling edge trim and start-up film into P218 monolayer structures at regrind content above 30 wt% creates film-gel and die-lip build-up phenomena. The primary cause is crosslinking and antioxidant depletion during the first extrusion pass. Published studies on C4-LLDPE with similar stabiliser packages show that carbonyl index rises at roughly 0.02–0.06 absorbance units per pass, depending on melt temperature and oxygen concentration in the feed throat. At a die temperature of 240 °C, gel area fraction increases above 0.1 mm²/m² after three passes, and bubble stability deteriorates in spiral mandrel dies. The operational boundary is therefore to maintain regrind below 30 wt% or to introduce 0.1 wt% of a secondary antioxidant masterbatch. Amine-based processing additives should be avoided unless their interaction with the phenolic stabiliser during high-temperature extrusion is tested, because such combinations can produce discoloured oxidation products in C4-LLDPE. Published data for this specific resin in high-regrind bag conversion is limited, but the failure mode is documented for C4-LLDPE blown film generally.

    Regulatory Compliance Matrix and Additive Boundaries

    P218 may be used in packaging where the base polyolefin is covered by US FDA 21 CFR 177.1520(c) and EU Regulation 10/2011 when the finished article meets the applicable migration limits. The density and melt flow rate class fall within the generic polyolefin specification, but converters must request lot-specific certificates for food-contact use. The antioxidant package contains phenolic and phosphite stabilisers; their migration should be assessed under EU 10/2011 test conditions for fatty and aqueous simulants. No statement can be made from the public datasheet concerning slip, antiblock, or antistatic additives. If these surface functionalities are required, the resin must be modified by masterbatch addition. The grade is not automatically specified for medical or pharmaceutical packaging requiring ISO 10993 certification unless the supplier certifies the grade separately. Storage above 60% relative humidity requires pre-drying before film extrusion to prevent surface moisture carry-over and bubble instability.

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