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Mitsui Chemicals Evolue mLLDPE SP3210

    • Product Name: Mitsui Chemicals Evolue mLLDPE SP3210
    • 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 520786
    Product Name Mitsui Chemicals Evolue mLLDPE SP3210
    Manufacturer Mitsui Chemicals
    Polymer Type Metallocene Linear Low Density Polyethylene (mLLDPE)
    Catalyst Type Metallocene
    Comonomer Hexene-1
    Density 0.921 g/cm³
    Melt Flow Rate 2.5 g/10 min at 190°C/2.16 kg
    Melting Point 118 °C
    Vicat Softening Point 95 °C
    Tensile Strength At Break 28 MPa
    Elongation At Break 700%
    Flexural Modulus 250 MPa
    Dart Impact Strength 130 g
    Haze 10%
    Gloss 70%
    Heat Seal Initiation Temperature 105 °C

    As an accredited Mitsui Chemicals Evolue mLLDPE SP3210 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Mitsui Chemicals Evolue mLLDPE SP3210 is supplied in 25 kg moisture-resistant paper bags, palletized at 1,000 kg per pallet.
    Container Loading (20′ FCL) Container Loading (20′ FCL): Mitsui Chemicals Evolue mLLDPE SP3210 in 25 kg bags, palletized, stretch-wrapped, and secured for ocean transport.
    Shipping Mitsui Chemicals Evolue mLLDPE SP3210 is shipped as solid polyethylene resin pellets, typically in 25 kg moisture-barrier bags or octabins on pallets. It is not classified as dangerous goods. Keep dry, away from direct sunlight and excessive heat; use standard covered freight and avoid package damage.
    Storage Store Mitsui Chemicals Evolue mLLDPE SP3210 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and oxidizing agents. Keep original bags sealed and palletized off the floor to prevent moisture pickup and contamination. Avoid prolonged high temperatures and UV exposure; use first-in, first-out stock rotation.
    Shelf Life Shelf life is approximately 24 months from manufacture when kept unopened in original packaging, dry, cool, ventilated conditions, away from sunlight.
    Application of Mitsui Chemicals Evolue mLLDPE SP3210

    On a 3-layer cast film line with a 2,500 mm die width and a 0.8 mm lip gap, Evolue SP3210 is processed as the core and outer cling layer for machine pallet wrap at 12–20 µm total thickness. The grade has a nominal density of 0.921 g/cm³ and a melt mass-flow rate of 2.1 g/10 min when measured per ISO 1133-1:2022 at 190°C and 2.16 kg. The line uses 90 mm, 75 mm, and 90 mm single-screw extruders with 30:1 L/D ratios, barrier screws, and screen pack sequences of 80/120/200 mesh. Melt temperatures are held at 221°C, 231°C, and 235°C in the three adaptors; the die is held at 235°C. Air gap is set at 110 mm, chill roll temperature at 18°C, and line speed at 420 m/min. The formulation is 90–95 wt% SP3210 with 5–10 wt% polyisobutylene cling masterbatch; no slip or antiblock is added in the cling layer because silica migration suppresses cling force within 48 h. Tensile properties are measured by ISO 527-3:2018 or ASTM D882-18, and cling force is measured by ASTM D5458-95. Melt curtain resonance becomes a process bottleneck above 480 m/min unless a vacuum box stabilizes the melt web; edge trim at 8–10% is reintroduced at no more than 15% of total throughput to prevent gel accumulation in the core layer. Terminal products include 12 µm hand wrap, 15 µm machine wrap, and 20 µm agricultural bale wrap when a UV stabilizer masterbatch is added. Die-lip build-up is controlled by maintaining the die exit temperature 5°C above the final adaptor setpoint and by scheduling die cleaning after 72 h of continuous running. Cling force drift outside 200–400 g/25 mm is corrected by adjusting the masterbatch feed ratio, and the cast sheet is corona-treated to 36–38 mN/m only on the non-cling surface to avoid reducing cling on the opposite face.

    What Determines Hot Tack During 120 Cycles/min Vertical Form-Fill-Seal Operation?

    High-speed snack packaging lines require a sealant resin that maintains hot tack during jaw release and before the seal solidifies; SP3210 is placed in the sealant layer at 15–25% of the total film thickness, with a core layer of SP3210 or butene LLDPE at 50–70% and a skin layer of low-density polyethylene at 10–20%. The blown film line uses a die gap of 1.6–2.2 mm, blow-up ratio of 2.2–2.8:1, and frost line height of 500–700 mm. Melt temperature at the die is held at 210–225°C. Seal strength is measured by ASTM F88/F88M-21 at 0.3 MPa seal pressure and 0.5 s dwell; hot tack is measured by ASTM F1921-18 with 100 ms delay and 0.3 MPa sealing pressure. In VFFS operation at 120 cycles/min, the seal-bar setpoint is maintained at 105–125°C. Below 105°C the seal remains in peel mode and fails at the seal bar on powder-filled bags; above 135°C the sealant layer thins and edge weeps occur on 25 µm structures. Packaging trials show that film failure shifts from seal peel to film tear when the seal-bar temperature exceeds 125°C on 25 µm stock. The sealing layer is dry-blended with 1,000–1,500 ppm slip and 800–1,200 ppm antiblock to avoid blocking on the film roll while preserving seal integrity. Terminal products include salty snack bags, confectionery pouches, and powder sachets. Compliance is verified under EU 10/2011 with overall migration below 10 mg/dm² when tested in 10% ethanol and 3% acetic acid for 10 days at 40°C. The resin also falls under FDA 21 CFR 177.1520(c) 3.2a as an olefin polymer for food contact use.

    MeasurementStandardReporting unit
    Melt mass-flow rateISO 1133-1:2022g/10 min
    Seal strengthASTM F88/F88M-21N/15 mm
    Hot tackASTM F1921-18N/25 mm
    Dart impactASTM D1709-22g
    Elmendorf tearASTM D1922-15gf
    HazeASTM D1003-21%

    Drying is not required under normal storage at 20–25°C and 40–60% RH. At RH above 85%, surface condensation on cold pellets must be prevented by allowing the resin to reach 20°C before hopper loading. The film is produced with a frost line height stabilized at 600 mm for 25 µm total thickness; lowering the frost line below 400 mm increases dart impact but raises haze above 6% and reduces hot tack by permitting excessive crystallization before the seal jaw contacts the film. On a 65 mm extruder with 30:1 L/D, melt pressure at the screen pack is kept below 35 MPa; pressure excursions above 40 MPa require screen pack replacement because gel-induced die streaks appear within 20 min of sustained high pressure.

    Extrusion Lamination onto Biaxially Oriented Polypropylene and Aluminium Foil

    SP3210 is applied as a molten sealant web between a primed BOPP or PET print film and an aluminium foil or metallized polyester barrier layer. Typical coating weight is 12–20 g/m²; the extruder is a 120 mm single-screw with 33:1 L/D, a grooved feed section, and a T-die of 1.4 m width and 0.8 mm lip gap. Melt temperature at the die is held at 280–300°C to achieve adhesion to the primed substrate, and residence time in the adaptor is kept below 3 min to limit molecular scission. Air gap is set at 180–250 mm, and nip pressure is 3–5 N/mm across the chilled steel roll. Neat SP3210 shows neck-in of 60–80 mm at these settings; addition of 20–30 wt% LDPE reduces neck-in to 25–40 mm and improves draw-down stability. Substrate pretreatment uses primers based on polyethyleneimine or polyurethane applied at 0.3–0.5 g/m² dry coat weight. Ply adhesion is measured by ASTM F904-16; values below 2 N/15 mm are observed when foil is not primed, and values above 3 N/15 mm are achieved when primed. Terminal structures include BOPP/SP3210, PET/SP3210/foil, and PET/metallized-PET/SP3210 for dry food pouches, personal care sachets, and lidding films. The laminate is not suitable for retort processing above 121°C because sealant softening and pouch edge cracking occur under pressurized steam. Published data for this specific grade at 130°C retort conditions with olive oil simulant D2 is limited. The lamination bond must be checked after 24 h conditioning at 23°C and 50% RH because adhesion develops with cooling and crystallization; immediate peel testing after the nip gives false low values.

    When Frozen-Food Pouches Require Puncture Resistance at −25°C After Quenching

    Frozen vegetable and seafood pouches at 40–60 µm total thickness are produced as blown film using SP3210 at 80–85 wt%, LDPE at 10–15 wt%, and a slip/antiblock masterbatch at 3–5 wt%. The melt temperature is deliberately reduced to 195–205°C to limit additive degradation and to preserve low-temperature impact strength; this reduces output by 10–15% compared with standard polyethylene processing temperatures. Die gap is 1.8–2.2 mm, blow-up ratio is 2.0–2.4:1, and frost line height is 400–600 mm. After extrusion, the film is conditioned at −25°C for 48 h before testing. Dart impact is measured by ASTM D1709-22, Elmendorf tear by ASTM D1922-15, and seal strength by ASTM F88/F88M-21 on samples sealed at 105°C, 0.3 MPa, and 0.5 s dwell. Film failure at subzero storage occurs mainly by dart puncture adjacent to seal corners in VFFS pillow packs; increasing SP3210 content from 60 wt% to 85 wt% shifts failure from seal peel to film stretch under impact. Terminal products include 40 µm frozen vegetable pillow packs, 55 µm shrimp pouch stock, and 60 µm ice cream bag-in-box liners. Compliance with EU 10/2011 requires overall migration below 10 mg/dm² when tested in 10% ethanol and 3% acetic acid simulants for 10 days at 40°C. Compliance with FDA 21 CFR 177.1520(c) 3.2a applies when the film is used as an olefin polymer under the limitations specified in that section. At low melt temperature, barrel zone setpoints must be profiled to avoid unmelted pellets reaching the screen pack; a 75 mm extruder with 28:1 L/D uses zone temperatures of 160°C, 175°C, 185°C, 195°C, and 200°C, with measured melt temperature at 198°C before the die.

    Converter trials with SP3210 in a 75 µm mono-layer cast extrusion web for heavy-duty liquid packaging show that the resin can replace conventional octene LLDPE at 100% in the sealant ply when the substrate is corona-treated to 42–44 mN/m. The cast film line uses a 90 mm extruder with 30:1 L/D, a 0.7 mm die gap, 150 mm air gap, and 20°C chill roll. Melt temperature is set at 235°C. The film is then laminated to BOPP or PET at 12–15 g/m² coating weight. Water vapor transmission rate is measured by ASTM F1249-20 at 38°C and 90% RH; oxygen transmission is measured by ASTM D3985-17. Terminal products include 5–20 L bag-in-box liners for edible oil and dairy concentrates. The seal is tested after filling at 4°C to simulate cold-chain distribution. Seal failures occur when the seal bar temperature drops below 110°C because crystallinity at the seal interface remains too high; raising dwell time from 100 ms to 150 ms compensates only if sealing pressure is at least 0.25 MPa. Published comparative data for SP3210 against a standard C8 LLDPE in this specific liquid-packaging configuration is limited. The cast web must be wound with taper tension from 20 N to 10 N across the roll width to prevent blocking, and slitting must use razor blades maintained at 0.3 mm protrusion to avoid micro-tearing at the edges.

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    Certification & Compliance
    More Introduction

    Mitsui Chemicals Evolue mLLDPE SP3210 is a metallocene linear low-density polyethylene produced by single-site catalyst polymerization. The resin is supplied as an ethylene-α-olefin copolymer with a nominal melt mass-flow rate of 2.1 g/10 min at 190 °C under 2.16 kg load per ISO 1133-1:2022, and a nominal density of 0.921 g/cm³ at 23 °C per ISO 1183-1:2019. It is intended for cast film, monolayer and coextruded sealant webs, lamination film, and general-purpose flexible packaging. The grade is not a drop-in substitute for autoclave LDPE on high-speed extrusion coating lines because the metallocene architecture lacks long-chain branching; shear-thinning response is less pronounced, and extruder head pressure is higher at equivalent output. In cast film, SP3210 is used at thicknesses from 20 µm to 80 µm, where low seal initiation temperature, low extractables, and optical clarity are required. The resin is also used as a sealant layer in laminated pouches, overwrap, and flow-wrap structures because its uniform short-chain branching distribution supports rapid interfacial fusion at seal bar temperatures below 110 °C.

    Nominal Melt Rheology and Physical Property Data for SP3210

    The representative values in this section are consolidated from supplier technical data for film-grade evaluations. Cast film tensile and impact data are thickness-dependent; unless otherwise stated, values correspond to 40 µm film produced on a chill-roll cast line with a 0.8 mm die gap and melt temperature of 250 °C. These values should not be interpreted as batch release limits. The narrow molecular weight distribution associated with single-site catalysis reduces melt fracture and improves gloss; however, it also lowers melt extensibility relative to LDPE, which must be managed through die gap and air gap selection. The polydispersity index for this grade is typical of metallocene LLDPE, generally below 3.0.

    PropertyTypical valueTest method
    Melt mass-flow rate, 190 °C/2.16 kg2.1 g/10 minISO 1133-1:2022
    Density, 23 °C0.921 g/cm³ISO 1183-1:2019
    Tensile stress at yield, MD/TD11.0 / 10.5 MPaISO 527-3
    Tensile strain at break, MD/TD620 / 780 %ISO 527-3
    Elmendorf tear strength, MD/TD14 / 22 NISO 6383-2
    Dart impact strength, F50130 gASTM D1709
    Haze6.5 %ASTM D1003
    Gloss at 60°105ASTM D2457
    Vicat softening point103 °CISO 306
    Peak melting temperature115 °CISO 11357-3

    Typical usage scenarios include monolayer cast wrap at 25 µm for bakery or confectionery packaging, three-layer coextruded sealant webs with a core layer of LDPE or HDPE, and extrusion coating of paper or aluminium foil. In monolayer cast film, the resin is run at 240–250 °C and provides a seal initiation temperature below 110 °C on vertical form-fill-seal lines. In three-layer structures, SP3210 is placed in the skin layer at 10–20 µm; the core may be a Ziegler-Natta LLDPE or recycled material at 20–30 µm. For lamination film, a 20 µm SP3210 layer can be adhesive laminated to PET or BOPP; the low seal initiation and low oligomer content reduce seal bar contamination. In extrusion coating, SP3210 is dry-blended with LDPE in ratios from 50:50 to 80:20; however, above 80 wt% SP3210, neck-in increases and edge trim waste rises. Melt temperature for coating is maintained at 260–270 °C to improve adhesion to aluminium foil, and a corona discharge unit is operated at 2.0–3.0 kW for 10–15 m/min treatment speed to achieve surface energy above 38 mN/m. Published adhesion data for this specific configuration are limited; users typically run a pilot trial to determine optimal air gap and melt temperature for the target substrate.

    On cast film lines, SP3210 is processed at melt temperatures between 240 °C and 260 °C. The die and adapter temperatures are typically set 10–15 °C above the melt temperature to prevent flow marks and die-lip deposit formation. On a 90 mm single-screw extruder with a barrier screw and 30:1 L/D, outputs up to 350 kg/h are generally attainable; higher outputs require a 120 mm extruder or a twin-screw side feeder. The die gap is set at 0.7–0.9 mm, and the air gap is maintained at 100–150 mm to limit web flapping and edge curl. Chill roll temperature is controlled at 18–22 °C; higher chill roll temperatures above 30 °C increase blocking tendency and reduce film flatness. Electrostatic pinning is applied across the full die width because the melt has limited long-chain branching and neck-in is greater than LDPE. When SP3210 is coextruded with LDPE or HDPE layers, the melt curtain can be stabilized by blending 10–20 wt% LDPE with a melt mass-flow rate of 4.0 g/10 min and density of 0.919 g/cm³. This blend reduces neck-in and edge bead without shifting seal initiation above 110 °C. Operators should monitor die-lip deposit formation; the narrow molecular weight distribution can produce flow marks at die temperatures below 220 °C, so die temperatures should be maintained above 240 °C.

    Why Does Catalyst Architecture Control Seal Initiation Temperature in Cast Sealant Webs?

    Single-site metallocene catalysis provides a narrow molecular weight distribution and uniform intermolecular comonomer composition. In cast film sealant layers, seal initiation temperature is governed by the melting of low-crystallinity fractions. For SP3210, the uniform short-chain branching distribution concentrates melting in a narrow temperature window near 105–115 °C, which allows interfacial fusion at seal bar temperatures below 110 °C. In contrast, Ziegler-Natta LLDPE has a broader branching distribution; its low-crystallinity fraction melts earlier, but a high-melting fraction delays seal strength development. The homogeneous comonomer distribution also reduces high-molecular-weight, low-branch molecules that would otherwise increase extractables. In laboratory heat-seal testing, the grade develops 2.0 N/15 mm seal strength at a lower temperature than a conventional butene LLDPE of equivalent density when measured with 0.5 s dwell and 0.2 MPa jaw pressure according to ASTM F2029. Hot tack strength, measured according to ASTM F1921, is also typically higher at 110–120 °C because crystallization after seal jaw release is more uniform. Seal curves generated on a laboratory heat-seal machine show that SP3210 in 40 µm monolayer film reaches a plateau seal strength near 120 °C. Published data for specific film structures are limited; seal performance must be verified on the target packaging line because film gauge, chill roll cooling, and coextruded layer structure alter interfacial temperature history.

    When SP3210 replaces a conventional Ziegler-Natta butene LLDPE of similar density in a 40 µm three-layer cast film, the optical haze generally drops from approximately 12–15% to 6–8%, and gloss at 60° increases from around 70 to above 100. The difference arises from reduced surface roughness and fewer high-molecular-weight species that scatter light. The optical improvement is not solely due to density. The single-site catalyst reduces the concentration of high-molecular-weight, high-crystallinity chains that form surface protrusions during film solidification. The same replacement reduces hexane extractables and improves organoleptic performance in food packaging. In extrusion coating, SP3210 does not match the neck-in performance of LDPE because the absence of long-chain branching reduces strain-hardening. A blend of 70 wt% SP3210 and 30 wt% LDPE is typical for coating paper or aluminium foil at line speeds below 200 m/min; the LDPE component imparts draw-down and edge stability, while SP3210 contributes low seal initiation and toughness. Compared with higher-density mLLDPE grades, SP3210 has lower modulus and lower seal initiation temperature; compared with lower-density mLLDPE grades, it gives lower water vapor transmission rate and higher stiffness. The density of 0.921 g/cm³ places it between a 0.915 g/cm³ easy-seal resin and a 0.927 g/cm³ stiff structural resin.

    Within the broader Evolue metallocene range, SP3210 is differentiated by its balance of melt flow and density. Lower-melt-flow grades are used in thicker gauge cast film where higher melt strength is required; higher-melt-flow grades are used for thin-gauge extrusion coating. SP3210 occupies the intermediate cast film window, with a density of 0.921 g/cm³ that provides moisture barrier without excessive stiffness. The grade is not a very-low-density metallocene resin in the 0.900–0.910 g/cm³ range, and it is not a high-stiffness grade in the 0.927–0.930 g/cm³ range. Its selection is therefore driven by sealant-layer performance and cast film draw, rather than by monolayer structural modulus. Current certificates of analysis should be obtained for lot-specific melt flow and density before film conversion.

    When SP3210 Is Run Without LDPE Blending on High-Speed Cast Film Lines

    Without LDPE, SP3210 shows higher extruder pressure than a comparable autoclave LDPE melt index because the metallocene resin has less shear thinning. The effect is measurable on a 90 mm extruder at 200 kg/h: head pressure can be 15–25% higher, and melt curtain instability increases below 40 µm gauge. Edge weave and draw resonance become more severe at line speeds above 150 m/min. Neck-in on an extrusion coating die is greater than LDPE; industrial practice therefore adds 20–30 wt% LDPE to SP3210 for coating structures. In cast film, the addition of LDPE also improves web tracking and reduces blocking on the chill roll, but levels above 30 wt% begin to raise seal initiation temperature and reduce puncture resistance. The selection of LDPE grade should be based on a melt index near 3.0–4.0 g/10 min and a density between 0.918 g/cm³ and 0.920 g/cm³. Lower-density LDPE reduces stiffness, while higher-density LDPE increases haze. When high clarity is required, a metallocene LDPE or a second mLLDPE grade may be used as the coextrusion partner.

    Die-lip deposit formation is commonly observed when SP3210 is run at melt temperatures above 270 °C for extended periods, particularly on cast film lines without melt filtration. The deposit consists of oxidized oligomers and can be mitigated by lowering the adapter temperature 5–10 °C, increasing the die gap to 0.9 mm, or adding a fluoropolymer processing aid at 200–400 ppm. If a processing aid is added, the specific grade must comply with FDA 21 CFR 177.1520 or EU 10/2011 for food contact. On cast film lines with a 20/40/60/80 mesh screen pack, pressure should remain below 35 MPa. A melt pump is recommended downstream of the extruder to stabilize output and reduce surge-induced thickness variation to less than ±2%. Extrusion coating of paper and aluminium foil with SP3210 requires careful control of the air gap. Air gaps below 100 mm increase thermal degradation of the substrate and reduce adhesion; air gaps above 200 mm increase neck-in and reduce web edge stability. The use of a back-up roll with a shore hardness of 80–90 A and a surface temperature below 30 °C improves coating thickness uniformity.

    Compliance documentation for SP3210 states that the base resin meets the requirements of FDA 21 CFR 177.1520 for olefin polymers used in contact with food, subject to limitations on use levels and additive package. Supplier declarations typically reference EU Regulation (EU) No 10/2011, including overall migration limits of 10 mg/dm² for food contact applications, and REACH registration under EC 1907/2006. The resin is supplied without anti-block or slip additives in the base grade; specific masterbatch formulations must be evaluated for organoleptic and migration contributions. For pharmaceutical blister packaging, users should verify absence of zinc stearate or erucamide interactions with the seal lacquer. SP3210 is not suitable for high-temperature retort structures requiring sustained exposure above 121 °C; it is intended for hot-fill, pasteurization, or dry food packaging where seal temperatures do not exceed 100–110 °C.

    Storage, Moisture, and Thermal Stability Boundaries

    Predrying is not required for SP3210 under normal ambient storage if pellets remain dry. Condensation from cold silo transfer or high humidity above 60% RH can introduce surface moisture that causes splay in cast film. In such cases, a hopper dryer at 60 °C for 2 h is sufficient. The resin should be extruded with melt temperatures below 280 °C; prolonged residence time above 290 °C promotes oxidative gel formation and carbonized specks. To limit degradation, use a screw with low compression ratio of 2.5:1–3.0:1 and avoid dead spots in the adapter. SP3210 is incompatible with high levels of certain phthalate plasticizers and with strongly acidic or amine-based processing aids that can accelerate catalyst residue hydrolysis or form odor-active compounds. For monolayer food packaging, no more than 15 wt% recycled content should be added unless the specific recycled stream is tested under EU 10/2011 migration protocols. Regrind from SP3210 cast edges can be reintroduced at levels up to 20 wt% if the regrind is free of dust, contamination, and oxidized gels. Higher regrind levels can reduce gloss and increase gel count. A dedusting unit or vacuum loading system with filtration below 250 µm is recommended to prevent fines from accumulating in the hopper.

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