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SABIC LLDPE 220HT

    • Product Name: SABIC LLDPE 220HT
    • 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 390921
    Density 0.920 g/cm³
    Melt Flow Rate 2.2 g/10 min at 190°C, 2.16 kg
    Melting Temperature 123 °C
    Vicat Softening Temperature 93 °C
    Brittleness Temperature -70 °C
    Tensile Stress At Yield 11 MPa
    Tensile Strain At Yield 17 %
    Tensile Stress At Break 12 MPa
    Tensile Strain At Break 600 %
    Flexural Modulus 260 MPa
    Shore D Hardness 52
    Izod Impact Strength At 23 C No break

    As an accredited SABIC LLDPE 220HT factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing SABIC LLDPE 220HT is supplied in 25 kg polyethylene bags, palletized and stretch-wrapped, with clear product labeling for safe handling.
    Container Loading (20′ FCL) SABIC LLDPE 220HT is loaded into a 20′ FCL container, securely packed, ensuring safe transport and efficient use of space.
    Shipping SABIC LLDPE 220HT is a non-hazardous linear low-density polyethylene resin supplied in virgin pellet form. Ship in clean, dry containers or FIBC bags, protected from moisture, direct sunlight, and high temperatures. No dangerous goods restrictions apply, but avoid dust accumulation and ensure proper ventilation during handling.
    Storage Store SABIC LLDPE 220HT in a dry, clean, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep sealed in original packaging or suitable containers to prevent moisture pickup and contamination. Maintain moderate temperatures; avoid prolonged exposure to high heat, which can cause degradation or oxidation. No special storage restrictions are required under normal conditions.
    Shelf Life SABIC LLDPE 220HT has an indefinite shelf life when stored in sealed, dry conditions, away from direct sunlight and extreme temperatures.
    Application of SABIC LLDPE 220HT

    Film Bubble Oscillation in High-Stalk Heavy-Duty Sack Lines

    In heavy-duty industrial sack production, SABIC LLDPE 220HT is processed as a monolayer or as the outer skin of a coextruded structure on blown film lines equipped with internal bubble cooling and capacitance thickness gauging. The resin is characterized by a density of 0.922 g/cm³ and a melt flow rate of 2.0 g/10 min under ISO 1183 and ISO 1133-1; these values define the melt viscosity range that requires die temperatures between 205°C and 220°C. A typical 65 mm grooved-feed single-screw extruder with 30:1 L/D and barrier mixing geometry operates with a feed zone at 170–180°C, compression zone at 190–200°C, adapter at 205°C, and die zones at 210–220°C. The die gap is held at 2.0–2.2 mm, and the blow-up ratio is set at 3.0:1 to produce 50–80 µm final film for heavy-duty sacks. A high-stalk bubble configuration is used because 220HT, as a butene LLDPE with limited strain hardening, exhibits bubble hunting and MD gauge bands when the frost line is positioned below 7 die diameters from the die face. Moving the frost line from 5 to 9 die diameters is an effective corrective action for gauge variation on these lines; this change lowers the standard deviation of on-line capacitance gauging and improves dart impact reproducibility under ASTM D1709 Method A. The addition of 30 wt% LDPE increases long-chain branching in the melt, raises extensional viscosity, and stabilizes the bubble during transverse stretching. Tear resistance is measured under ASTM D1922, tensile properties under EN ISO 527-3, and the compound is qualified for shipping-sack use under warehouse handling protocols aligned with ASTM D3951. Slip and antiblock concentrates are limited to 0.5–1.5 wt% because higher silica loadings reduce cold-temperature dart impact and increase pinhole frequency at gusset folds. At shutdown, the 220HT melt should be purged with a lower-density LDPE grade above 200°C to prevent gel accumulation at the die lips; melt residence time above 220°C should not exceed 15 min.

    Test methodPropertyCondition
    ISO 1183Density23°C
    ISO 1133-1Melt flow rate190°C, 2.16 kg
    ASTM D1709Dart impact, Method A50 µm blown film
    ASTM D1922Elmendorf tearMD/TD
    ISO 527-3Tensile properties of film500 mm/min, 23°C

    Vertical form-fill-seal equipment running frozen vegetables, seafood, or prepared ice-glazed foods presents a sealing window in which 220HT film functions as the sealant web. The film is blown at 30–50 µm thickness with a 2.5:1 blow-up ratio and a 2.0 mm die gap to balance MD tear and TD elongation during bag-top folding. Food-contact compliance is supported by EU Regulation No 10/2011 and, for U.S. shipments, FDA 21 CFR 177.1520 when the grade is covered by the manufacturer’s food contact statement. Seal strength is tested under ASTM F88 on a 25.4 mm specimen at 300 mm/min; hot tack is measured on a J&B hot tack tester at 0.5 N/mm² seal pressure, 0.5 s dwell, and 200 mm/s peel speed. On high-speed vertical form-fill-seal lines cycling at 8–12 bags/min, seal jaws set below 115°C may produce ultimate seal strength below 4 N/15 mm on 40 µm film, causing burst pouches during drop loading; raising jaw temperature to 125–135°C restores a plateau above 6 N/15 mm. A melt blend of 10–20 wt% LDPE with 220HT widens the seal initiation window without eliminating the low-temperature dart impact required at -20°C; the trade-off is a small reduction in tensile modulus that is acceptable for gusseted pouches. The terminal product is a printed frozen food pouch with side gusset and back fin seal, typically 30–50 µm thick, qualified for impact testing under ISO 7765-1 at -20°C.

    Does Silage Film Puncture Resistance Depend More on Film Processing Than on Resin Density?

    For silage clamp covers and greenhouse tunnels, the puncture and tear performance of 220HT-based three-layer film is controlled as much by the frost line and blow-up ratio as by the resin density of 0.922 g/cm³. The outer skins are typically 60–80 wt% 220HT with 20–40 wt% LDPE or metallocene LLDPE, while the core carries a white-reflective or oxygen-barrier masterbatch. Ultraviolet stabilization is not provided by the neat 220HT resin; a HALS-based UV masterbatch is added at 2–4 wt%, and outdoor durability is assessed under ISO 4892-2 artificial weathering rather than by melt flow retention alone. Film thickness ranges from 150 µm for silage underlay to 200 µm for greenhouse covering. A 250 mm blown film die with 2.2 mm die gap, 2.8:1 BUR, and frost line fixed at 8–10 die diameters produces the expected isotropic tear balance. High frost line placement increases transverse orientation and improves Elmendorf tear under ASTM D1922 in the TD direction, but raising BUR beyond 3.2:1 can reduce machine-direction tear below the minimum required for silage bag insertion. The terminal product is a three-layer silage cover in which 220HT contributes adequate bubble stability at moderate BUR but does not match LDPE strain hardening. Converter trials on 65–90 mm three-layer lines remain the primary validation route. Published film property data for this exact UV-stabilized configuration is limited, particularly for tear after 12-month outdoor exposure.

    A three-layer coextrusion line running 50 µm T-shirt carrier bag film at 150 kg/h uses 220HT in the skin and core layers to increase dart impact and puncture resistance after transverse stretching at the bubble. The layer split is 10/80/10, with skins containing 80 wt% 220HT and 20 wt% LDPE, and the core carrying reclaimed trim at 10–20 wt% limited by gel accumulation in the screen changer and pressure rise across the melt filter. The die gap is 2.0 mm, the blow-up ratio is 3.5:1, and the frost line is kept at 6 die diameters to increase TD tear. Film property validation follows ISO 7765-1 for puncture and ASTM D1922 for tear; the controlling target for carrier bag conversion is a Dart impact of at least 100 g on 50 µm film and a TD tensile elongation above 600% under ISO 527-3. Silica antiblock is introduced at 0.5–1.0 wt% into the skins, and the static coefficient of friction is held below 0.35 under ASTM D1894 to maintain bag opening on wicket dispensers. The terminal product is a high-cycle T-shirt bag that withstands repeated top-load handling and carries printed retail branding.

    When 220HT Is Let Down to 65 wt% in Collation Shrink Bundling Film

    In collation shrink film for bottle and can bundling, 220HT is dry-blended or melt-compounded with LDPE at a letdown of 65 wt% to improve puncture resistance without raising the low-temperature seal initiation beyond the shrink tunnel’s hot-air profile. The film is produced as a 35–60 µm blown web on a 55 mm extruder with a 2.0 mm die gap and a 3.0:1 BUR, followed by high-stalk bubble cooling to preserve machine-direction shrinkage. Because butene LLDPE exhibits lower ultimate shrinkage than high-pressure LDPE, the converter must limit 220HT content to below 70 wt%; above this level, the residual shrink force under ISO 14616 falls below the force necessary to hold 6-pack bottle arrays during tunnel transit. The shrink tunnel is set to 160–180°C air temperature, and the web residence time is 3–5 s. Seal strength before shrinking is checked under ASTM F88, while tear after shrink is checked under ASTM D1922; the latter is critical because post-shrink cooling increases film brittleness. Equipment audits show that only blends containing long-chain-branched LDPE at 30–35 wt% maintain stable bubble geometry at 3.0:1 BUR. The terminal product is printed collation shrink bundling film for 6-pack or 12-pack beverage and canned food multipacks.

    Corona-treated 220HT blown film enters the lamination stage at a wetting tension of 38–42 mN/m under ASTM D2578 and is subsequently laminated to BOPP, PET, or metallized substrates using a solventless polyurethane adhesive. The application is primarily in dry-food and powder packaging, where the 220HT web functions as the inner sealing layer in a two-ply or three-ply laminate. The blown inner web is produced at 25–40 µm thickness with a 2.5:1 BUR and a 2.0 mm die gap; lower BUR is preferred because the laminate requires higher machine-direction stiffness to resist crease cracking on the form-fill-seal line. Peel strength is measured under ASTM D1876 after 24 h adhesive cure and after a 72 h aged condition at 40°C; the minimum acceptable T-peel is typically 2.5 N/15 mm in dry-food lamination. Coefficient of friction after corona treatment is maintained below 0.30 static under ASTM D1894, and the sealant layer is qualified for migration under EU Regulation No 10/2011 and FDA 21 CFR 177.1520 where the laminate is intended for food contact. The terminal product is a stand-up pouch or gusseted pouch for dehydrated soups, pet food, and seasoning mixes, with 220HT selected for seal integrity after repeated flexing rather than for optical properties.

    ApplicationPrimary qualification methodKey condition or limit
    Heavy-duty sacksASTM D1709Dart impact, Method A, 50–80 µm
    Frozen food pouchesASTM F88Seal strength, 300 mm/min
    Silage coversISO 4892-2Accelerated weathering
    Carrier bagsISO 7765-1Puncture resistance
    Collation shrinkISO 14616Shrink force/temperature
    Dry-food laminationASTM D1876T-peel adhesion
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    Certification & Compliance
    More Introduction

    On high-output blown film towers and cast film lines, SABIC LLDPE 220HT is classified as a butene-based linear low density polyethylene supplied in pellet form. The nominal melt mass-flow rate is 2.0 g/10 min when determined at 190 °C under a 2.16 kg load in accordance with ISO 1133-1:2022. The nominal density is 0.922 g/cm³ when determined by ISO 1183-1:2019. These two values are the principal incoming resin specification checkpoints; film-level mechanical and optical data are line-dependent and are not intrinsic resin specifications.

    The grade is directed at monolayer and coextruded packaging structures, including carrier film, overwrap, tissue bundling, and light food packaging below 100 µm thickness. It is also evaluated as a sealant layer in coextruded films where the line requires a balance of low gel count, moderate hot-tack, and optical clarity. Film property measurements for tensile behaviour follow ASTM D882, dart impact follows ASTM D1709A, Elmendorf tear follows ASTM D1922, haze follows ASTM D1003, and gloss follows ASTM D2457. Published single-point data for this grade are generally limited to nominal resin properties unless converter-generated film data are available from a defined line.

    Food-contact suitability is evaluated under 21 CFR 177.1520 for olefin polymers in the United States and under Commission Regulation (EU) No 10/2011 in the European Union, with overall migration limit of 10 mg/dm². The resin is not classified as hazardous under REACH Regulation (EC) No 1907/2006; no Candidate List substance is intentionally added. RoHS assessment under Directive 2011/65/EU is generally not required for packaging film, but can be evaluated for electrical and electronic applications.

    Regulatory and compliance checklist
    FrameworkDesignationApplicability
    U.S. food contact21 CFR 177.1520Olefin polymers; end-use limitations apply
    EU food contactCommission Regulation (EU) No 10/2011Overall migration limit 10 mg/dm²; specific migration verification required
    REACHRegulation (EC) No 1907/2006No intentionally added SVHC
    RoHSDirective 2011/65/EUOutside packaging scope unless electrically active article

    How Does the Melt Flow Ratio Constrain Die Pressure and Throughput?

    The MFR of 2.0 g/10 min indicates higher average chain mobility than a 1.0 g/10 min butene LLDPE of equivalent density. On a 65 mm barrier screw with L/D 30:1, the lower melt viscosity reduces discharge pressure and permits accelerated screw speed before the drive reaches current limit. The trade-off is lower melt strength in the bubble; the linear molecular structure does not generate the strain-hardening observed in high-pressure LDPE under extensional flow.

    At a die setpoint of 215 °C, viscosity is sufficiently low to allow thin film drawing, but barrel residence time should not be increased to compensate for unmelted resin. The stable operating window is typically defined by melt temperature between 195 °C and 220 °C. Below 195 °C, sharkskin or melt fracture may appear because the die exit stress exceeds the critical slip stress of the polymer; above 220 °C, oxidative by-products may accumulate on the die lip and form gel defects. Sharkskin in linear LLDPE is a viscoelastic instability controlled by the slip between the polymer and the die lip. Reducing extruder speed below the critical shear rate of the die or raising the die temperature will eliminate the defect. The operational boundary is set by the die geometry and the critical shear stress of the resin, not by MFR alone.

    Blown film extrusion on a three-layer line with internal bubble cooling is commonly started with a die gap of 1.2 mm to 2.0 mm, blow-up ratio of 2.0:1 to 2.5:1, and frost line height between 500 mm and 800 mm. Internal bubble cooling air temperature is maintained at 10 °C to 18 °C. Higher blow-up ratios improve transverse direction impact but worsen bubble stability; lower frost line decreases crystallinity and raises clarity while lowering dart impact in some gauge ranges. Melt temperature should not exceed 230 °C for prolonged residence times. Above that threshold, carbonyl group concentration increases and gel particles may be detected by ISO 18553 optical inspection.

    On a 90 mm grooved-feed extruder running above 120 rpm, die lip deposit and melt fracture are the main extrusion failure modes. A processing aid masterbatch at 0.3 wt% to 0.8 wt% is used to reduce die lip build-up, but the specific additive must be food-contact compliant if the film is intended for packaging. Corona treatment before printing or lamination is adjusted to a surface tension of 38 mN/m to 42 mN/m; untreated film usually measures 31 mN/m to 34 mN/m depending on additive bloom and storage time.

    Cast film production of SABIC LLDPE 220HT is performed on flat die lines with chill roll temperatures of 15 °C to 30 °C and air gap controlled between 10 mm and 30 mm. The lower melt strength relative to LDPE permits high line speed, but die swell and edge neck-in should be monitored. For extrusion lamination, melt temperature is often increased to 230 °C to enhance adhesion to substrates such as paper and aluminium foil; at this temperature residence time must be minimized to avoid oxidative gel formation.

    When Hot-Tack Windows Narrow in Vertical Form-Fill-Seal Operations

    Vertical form-fill-seal lines impose an immediate load on the seal after jaw release. Hot-tack force is measured by ASTM F1921, while seal strength after cooling is measured by ASTM F88. The seal initiation temperature is a film-structure property rather than a resin property, because layer thickness, seal bar pressure, dwell time, and cooling delay shift the curve.

    SABIC LLDPE 220HT is used as a sealant web in coextruded structures for dry food and light product packaging. The butene-based short-chain branching can narrow the hot-tack plateau when compared with octene-based LLDPE at equivalent density and MFR. On high-speed lines with dwell below 40 ms, the upper temperature limit is governed by seal-through and film distortion, while the lower limit is governed by incomplete interface fusion. Converters must generate their own hot-tack curve using the target film structure; published data for this specific configuration is limited.

    Oxidative Stability, Re-Grind Limits, and Additive Interactions

    Edge trim and start-up reclaim can be reintroduced at 10 wt% to 20 wt% in monolayer film. Higher reclaim fractions may raise haze and reduce dart impact. Re-grind must be free of degraded gel and should not contain mixed polyolefins or acid-modified tie resins. The antioxidant system is formulated for standard LLDPE extrusion temperatures; prolonged exposure to air at melt temperatures above 220 °C will consume the stabilizer package prematurely.

    Combination with amine-based slip or antistatic masterbatches should be evaluated through thermal-oxidative stability tests because amine species can interfere with phenolic stabilizer cycling. If titanium dioxide or carbon black masterbatches are added, film gel counts and dispersion rating should be confirmed by ISO 18553. The grade is not hygroscopic, but surface moisture on cold pellets stored at relative humidity above 60% can create steam-induced microbubbles when introduced directly into a hot feed throat. Hopper drying at 55 °C for 2 h is a standard corrective action for condensation on cold pellets entering a warm extrusion floor.

    Relative to an octene-based LLDPE of identical density and MFR, the butene-based 220HT has shorter side branches and generally develops lower slow puncture resistance and a narrower hot-tack plateau under identical film processing. The difference can be measured by ASTM D5748 for puncture and by ASTM F1921 for hot-tack. In high-abuse applications or where seal performance near 90 °C is critical, octene-based or metallocene LLDPE may be required.

    Compared with a general-purpose butene LLDPE of 1.0 g/10 min MFR and 0.922 g/cm³ density, 220HT lowers melt pressure and permits higher screw speed at the same barrel setpoint. The trade-off is reduced bubble stability at blow-up ratios above 3.0:1. Adding 5 wt% to 15 wt% high-pressure LDPE restores bubble stability and improves transverse direction tear, but may reduce optical clarity slightly.

    Against metallocene LLDPE of similar MFR, 220HT generally presents a broader molecular weight distribution and lower extrusion pressure, while metallocene grades provide higher dart impact, improved hot-tack, and better ESCR. Selection between these classes should be based on film data generated on the target production line because the differences are magnified in film below 25 µm thickness.

    Production validation should include gel count measurement by ISO 18553, film haze by ASTM D1003, and dart drop impact by ASTM D1709A after the line reaches steady state. Values obtained on a high-output line with internal bubble cooling may differ from laboratory cast film data.

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