| HS Code | 781503 |
| Density | 0.925 g/cm3 |
| Melt Index | 1.0 g/10 min (190 deg C/2.16 kg) |
| Melting Point | 119 deg C |
| Vicat Softening Point | 100 deg C |
| Tensile Strength At Yield | 9 MPa |
| Tensile Strength At Break | 35 MPa |
| Elongation At Break | 800 % |
| Flexural Modulus | 240 MPa |
| Dart Impact Strength | 150 g |
| Elmendorf Tear Strength Md | 120 g |
| Elmendorf Tear Strength Td | 250 g |
| Haze | 10 % |
| Gloss 45 Degrees | 100 |
| Coefficient Of Friction | 0.20 |
As an accredited Mitsui Chemicals Evolue mLLDPE SP2510 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Mitsui Chemicals Evolue mLLDPE SP2510 is packaged in 25 kg moisture-barrier bags on pallets for safe handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL loading of non-hazardous Mitsui Chemicals Evolue mLLDPE SP2510, 25 kg bags palletized and secured in dry container. |
| Shipping | Mitsui Chemicals Evolue SP2510 mLLDPE is a non-hazardous polymer supplied as pellets in 25 kg PE bags or 500–1000 kg jumbo bags, palletized and stretch-wrapped. Ship in dry, ventilated containers at ambient temperature, protected from moisture, contamination, and direct sunlight; no dangerous goods classification applies. |
| Storage | Store Evolue mLLDPE SP2510 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat sources, moisture, and contaminants. Keep original bags sealed and palletized; avoid physical damage, stacking stress, and weather exposure. Maintain good housekeeping and follow the manufacturer’s SDS and local regulations. Avoid prolonged high temperatures and contact with incompatible chemicals. |
| Shelf Life | Mitsui Chemicals Evolue mLLDPE SP2510 has a typical shelf life of two years from manufacture when stored dry, cool, and unopened. |
Cast polyolefin sealant webs for modified atmosphere packaging of fresh-cut produce and bakery laminates are produced on three-layer coextrusion cast lines with 45–75 mm smooth-barrel extruders having L/D ratios of 30:1–33:1. A typical sealant skin formulation uses 70–80 wt% Mitsui Chemicals Evolue mLLDPE SP2510, 15–25 wt% low-density polyethylene with a melt flow rate of 4 g/10 min at 190 °C/2.16 kg, and 5 wt% antiblock masterbatch containing 10% synthetic silica in a polyolefin carrier. Barrel temperature profile from feed to metering zone is 180–240 °C; feed throat is kept below 50 °C, die temperature is 240–250 °C, and chill roll temperature is 18–24 °C. Melt curtain stability is maintained with an air gap of 80–150 mm and vacuum box suction between 0.5 kPa and 1.5 kPa; edge bead trimming is removed before winding. At 30 µm total film thickness, the SP2510-containing sealant skin is targeted to provide a seal initiation temperature below 110 °C at 2.0 N/15 mm seal strength per ASTM F2029 and hot tack above 1.0 N/25 mm within 0.2 s after seal opening per ASTM F1921. These values are suitable only as process control references because seal initiation depends on dwell time, pressure, film gauge, and the antiblock package. Food-contact compliance is addressed under FDA 21 CFR 177.1520(c) 3.2a for olefin polymers and EU No 10/2011, where the overall migration limit is 10 mg/dm² for food simulants. A compliance matrix is provided below.
| Regulatory framework | Relevant clause or method | Control parameter |
|---|---|---|
| US FDA 21 CFR | 177.1520(c) 3.2a | Olefin polymer — no specific migration limit |
| EU No 10/2011 | Annex I authorised monomers; Article 11 | OML 10 mg/dm² |
| China GB 9685-2016 | Positive list for additives | Specific migration limits for listed additives |
| Japan JHOSPA | Positive list for equipment and packaging | OML 30 µg/mL for food simulants |
Frozen food film structures coextruded on three-layer blown lines with die diameters from 250 mm to 400 mm and die gaps of 1.8–2.5 mm use Evolue SP2510 in the core and one skin to raise dart impact and tear resistance while retaining optical clarity. The nominal density of 0.925 g/cm³ and melt flow rate of 1.0 g/10 min according to ISO 1183-1 and ISO 1133-1 place the grade in the stiffness range suited to 25–50 µm freezer bags and produce liners. The frost line height is maintained between 5 and 8 die diameters to avoid excessive quench rate, which in mLLDPE-rich layers creates internal haze and reduces machine-direction tear propagation. Blow-up ratio is held between 2.0 and 2.5; cooling air temperature is 8–15 °C; melt temperature at the die is 195–215 °C. Screw back pressure on the core extruder is normally limited to 200–280 bar to avoid excessive melt temperature rise from viscous dissipation. Because SP2510 has a narrow molecular weight distribution, the extensional viscosity under bubble inflation is lower than conventional high-pressure LDPE, so film gauge variation across the perimeter depends on die lip uniformity and internal bubble cooling; without internal bubble cooling, maximum reliable throughput drops by 15–25% at 25 µm due to bubble flutter. Dart impact is evaluated per ASTM D1709, Elmendorf tear per ASTM D1922, and tensile properties per ISO 527-3. A 25 µm three-layer film with 60 wt% SP2510 in the core typically requires an antiblock loading of 800–1,500 ppm synthetic silica to prevent blocking after folded roll storage at 35 °C for 14 days; blocking force is measured per ASTM D3354. The use of slip additives such as erucamide is limited to 200–500 ppm because excessive slip migration to the seal layer reduces hot tack below the threshold needed for vertical form-fill-seal operations.
On continuous protective film cast lines for flat glass, polished aluminum composite panel, and polycarbonate sheet, the carrier layer is extruded from SP2510 at 25–50 µm thickness and is subsequently coated with a solvent-free acrylic or polyurethane pressure-sensitive adhesive. The low extractables profile of metallocene catalysis reduces migration of short-chain molecules into the adhesive layer, which is critical because adhesive plasticisation by migrating oligomers causes peel strength decay and fogging on polished surfaces. The cast line configuration includes a 75 mm extruder, a 1,300 mm slot die, a matte-finish chill roll at 18–25 °C, and in-line corona treatment at 38–42 mN/m prior to winding. Film mechanical properties are measured per ISO 527-3; the 25 µm carrier typically falls within an elongation at break window of 350–550% in the machine direction and 500–700% in the transverse direction, depending on draw ratio and chill roll speed. Coefficient of friction is evaluated per ASTM D1894 against a glass reference at 23 °C and 50% RH; haze and clarity are measured per ASTM D1003. Peel adhesion of the finished protection film is tested according to PSTC-101 after 24 h and 72 h conditioning at 60 °C; published data for this specific SP2510 configuration are limited, so adhesion retention is confirmed on each production lot using test panels representative of the customer substrate. Compliance for temporary surface protection used in electronics logistics requires screening against REACH 1907/2006 SVHC restrictions and RoHS 2011/65/EU for the final article if the film remains attached during display or shipment.
Replacement of ethylene-vinyl acetate in three-layer greenhouse covers with SP2510-rich layers is evaluated for mechanical property retention and light transmission. EVA gives high clarity and IR retention, but mLLDPE at 0.925 g/cm³ improves tear propagation resistance, reduces acetic acid formation during recycling, and lowers water vapour transmission. Typical formulations use 60–80 wt% SP2510, 10–20 wt% LDPE, and 5–10 wt% hindered amine light stabilizer masterbatch. Blown coextrusion die gap is 2.0–2.5 mm, blow-up ratio 2.2–2.8, melt temperature 190–210 °C. Light transmission and haze are assessed per EN 13206 and ISO 13468. Accelerated weathering is performed per EN ISO 4892-2 cycles; retained tensile elongation after 3,000 h is monitored against local classification requirements. The operational boundary is frost heave at sub-zero temperatures; SP2510 has lower EVA-like softness so fold installation at temperatures below −5 °C requires reduced bending radii and pre-stretched tension control to prevent stress whitening. Multi-season covers using SP2510-rich blends require UV additive packages distinct from EVA formulations because the solubility of benzophenone and benzotriazole stabilizers in mLLDPE is lower; nickel-quencher and hindered amine combinations are preferred, but specific stabilizer migration is confirmed by EN 13206 classification for film retention. Optical property loss from dust and condensation on hydrophobic surfaces is measured by photosynthetically active radiation transmission using a quantum sensor in field trials, not by benchtop ASTM haze alone. Water vapour transmission rate is determined per ASTM E96/E96M at 23 °C and 50% RH.
For breathable backsheet films used in disposable hygiene garments, formulations containing 45–55 wt% calcium carbonate masterbatch dispersed in a polyolefin matrix are extruded on a cast line with a 120 mm twin-screw compounding section and then stretched on intermeshing groove roll equipment. SP2510 contributes uniform extensional flow during machine-direction stretching at 2.0–3.0:1 draw ratios with roll temperatures of 60–80 °C. The resulting microporous film is tested for water vapour transmission rate per ASTM E96/E96M, hydrostatic head per AATCC 127, and tensile at break per ASTM D882. The dispersion quality of the CaCO₃ particle size distribution, typically 1–2 µm median particle size, controls pore size and thickness uniformity. Extruder screw design uses distributive mixing elements rather than intensive shear because localized melt temperature spikes above 230 °C degrade the carbonate coating and release carbon dioxide. Die temperature is held at 210–235 °C, and the cast film is quenched on a 20–25 °C embossed chill roll to suppress premature cavitation. After stretching, basis weight is checked on-line with beta gauge; basis weight variation across the web should be held within ±2%. For hygiene applications, the final film is tested for skin sensitization under ISO 10993-10 only when the material is used in medical-type patient contact; routine non-medical hygiene products rely on supplier risk assessments and extractable screening under ISO 10993-18 if requested.
Sealing to uncoated Tyvek in rigid medical device packaging requires a sealant layer with a broad sealing window and low initiation temperature; SP2510 is extruded as a 25–60 µm film and laminated to 12 µm or 23 µm polyester carrier webs using a solventless adhesive at 2.0–3.0 g/m² dry coat weight. Heat seal settings on a tray lidding machine are 115–135 °C, dwell 0.5–1.0 s, and pressure 0.25–0.6 MPa to produce peelable seals without fiber tear. Seal strength is tested per ASTM F88/F88M; seal integrity is determined by dye penetration per ASTM F1929 and whole-package integrity per ASTM F2096. Sterile barrier system validation is conducted under ISO 11607-1:2019 and ISO 11607-2:2019. Biocompatibility of the film after gamma or ethylene oxide sterilization is evaluated using ISO 10993-5 for cytotoxicity and ISO 10993-10 for sensitization. Because uncoated Tyvek is fibrillated HDPE, the seal interface is a mechanical interlock combined with partial melting of the SP2510 layer; at seal temperatures above 140 °C, excessive flow of the sealant into the Tyvek pores reduces peel smoothness and increases the risk of fiber tear. At temperatures below 110 °C, seal strength may fall below 1.0 N/15 mm after ethylene oxide conditioning because residual moisture acts as a plasticizer. The SP2510 layer must be free of slip additive accumulation on the heat seal side because migrating erucamide above 300 ppm reduces seal initiation but also lowers seal strength after gamma radiation at 25–40 kGy; radiation-compatible stabilizer packages are required if gamma is the terminal sterilization mode.
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Mitsui Chemicals Evolue SP2510 is a metallocene-catalyzed linear low-density polyethylene supplied for cast film, lamination, and sealant web applications. The resin is typically specified at a density of 0.925 g/cm³ by ASTM D1505 and a melt mass-flow rate of 2.0 g/10 min at 190 °C under a 2.16 kg load by ASTM D1238. These values classify the grade as a medium-density sealant resin, distinct from lower-density metallocene grades used where extreme seal initiation is required and from high-density polyethylene used for stiffness-driven layers. The numerical data in this document are typical published values, not contractual specification limits, and should be confirmed against the current certificate of analysis.
At the molecular scale, SP2510 is differentiated from conventional linear low-density polyethylene produced with Ziegler-Natta catalysts by a narrow molecular weight distribution and a more controlled short-chain branching distribution. This molecular structure reduces the population of very high and very low molecular weight chains that contribute to gels and smoke, and it produces a narrower melting range at the seal surface. The practical result is a reduction in hexane extractables and an improvement in optical consistency in cast film. The low residual catalyst content typical of metallocene polymerization also reduces the formation of oxidative gel particles during extended extrusion runs.
| Property | Test method | Typical value |
|---|---|---|
| Density | ASTM D1505 | 0.925 g/cm³ |
| Melt mass-flow rate | ASTM D1238 | 2.0 g/10 min at 190 °C/2.16 kg |
| Melting point | ASTM D3418 | 123 °C |
| Vicat softening point | ASTM D1525 | 103 °C |
| Tensile yield strength | ASTM D638 | 11 MPa |
| Tensile elongation at break | ASTM D638 | >500 % |
| Flexural modulus | ASTM D790 | 220 MPa |
The values in the table are generated on standard compression-molded or film specimens and are sensitive to cooling rate, test speed, and specimen preparation. The flexural modulus of 220 MPa indicates a moderate stiffness useful in sealant layers that must resist crease stress, while the elongation at break above 500 % supports package forming and film toughness. Film dart impact, haze, and gloss are intentionally omitted because those responses are controlled more by cast-film line conditions than by the resin alone; converter trials should measure those attributes on the target equipment.
Thermal analysis per ASTM D3418 places the melting point near 123 °C and the crystallization peak between 100 °C and 105 °C under standard cooling rates. The narrow melting range of SP2510 allows heat sealing at lower bar temperatures because a smaller thermal increment is required to convert the crystalline surface layer into a fused seal. In contrast, heterogeneous Ziegler-Natta C4-LLDPE grades of similar density often exhibit a broader melting profile that delays complete seal-surface fusion and increases the minimum bar temperature required to reach a given seal strength.
Extrusion of SP2510 is governed by its narrow molecular weight distribution and lower shear thinning compared with broad-MWD Ziegler-Natta LLDPE. On single-screw extruders with L/D ratios of 24:1 to 30:1, the resin generates higher motor load and melt pressure at equivalent screw speed than a butene-based LLDPE of the same melt index. Barrier screw designs with Maddock or Egan mixing sections and compression ratios of 2.5:1 to 3.5:1 are commonly used to limit shear heating and to maintain melt temperature below 280 °C. Typical cast-film melt temperature setpoints are 240 °C to 260 °C, with adapter and die zones held within ±5 °C of the target to reduce edge-bead formation. Die gaps from 0.5 mm to 0.8 mm are used for film thicknesses between 20 µm and 50 µm, and chill roll settings from 18 °C to 30 °C are selected according to required crystallinity and roll-release behavior.
Because SP2510 has lower melt strength than a broad-MWD Ziegler-Natta resin of equivalent melt index, draw resonance can become the process-limiting variable on cast lines when the air gap is too long or draw ratio is too aggressive. Production-scale cast film lines typically maintain an air gap below 10 cm and use electrostatic pinning or vacuum boxes as web speeds increase. Melt pressure at the die is line-specific, but converters often observe that the same screw speed produces 10 % to 20 % higher melt pressure with SP2510 than with a conventional C4-LLDPE of equal melt index. Extruder drives should be sized for continuous operation at 70 % to 85 % of maximum motor load to prevent thermal overshoot and pressure fluctuations during start-up.
Edge bead and neck-in are common production failure modes in cast film. Because SP2510 has a narrow molecular weight distribution, edge draw can become unstable when die-edge temperatures are too low. Die bolt temperatures at the outside edge are often maintained 5 °C to 10 °C above center to compensate for faster edge cooling. Neck-in in the sealant skin can be reduced by limiting the air gap to 5 cm to 8 cm and by applying electrostatic pinning before melt contact with the chill roll. At high extrusion shear rates above 1000 s⁻¹, sharkskin melt fracture can appear if die lip metal condition is poor or if the resin is processed below its optimum melt temperature. The addition of a fluoropolymer processing aid at 200 ppm to 500 ppm is used on some cast lines to reduce die lip buildup and delay the onset of melt fracture; run-time extensions between die cleanings are line-specific and published data for this specific configuration is limited.
SP2510 is also suitable for coextrusion as a sealant skin alongside polypropylene or high-density polyethylene structural layers. Viscosity mismatch must be compensated by adjusting skin-layer melt temperature and using feedblock designs that minimize interfacial shear. If pellet storage is exposed to relative humidity above 60 % RH, surface moisture can introduce bubbles and die lines during cast film extrusion; predrying at 60 °C to 65 °C for 2 h to 4 h in a desiccant hopper dryer is recommended before processing. Prolonged melt residence above 280 °C increases oxidative gel formation and off-taste generation in the seal layer.
In vertical form-fill-seal and horizontal form-fill-seal operations, hot tack often controls packaging line speed more than final seal strength. SP2510 exhibits a low heat-seal initiation temperature and a broad hot-tack window because the uniform branching distribution narrows the melt transition at the film surface. Seal strength in finished packages is measured according to ASTM F88/F88M, while hot tack is assessed under ASTM F1921. On packaging machines with jaw dwell times of 100 ms to 300 ms, the lower seal initiation permits sealing bar temperature reductions of about 5 °C to 10 °C relative to conventional C4-LLDPE at equivalent density. This reduction lowers heat load on the sealing jaws and can reduce charred residue accumulation on sealing bars. Published data for this specific configuration is limited, and converter-scale trials are required because film stiffness, sealant layer thickness, and lamination structure all affect heat transfer into the seal interface.
Seal strength measurements are influenced by seal bar temperature, bar pressure, dwell time, and sealant layer thickness. In laminated structures, the SP2510 sealant layer is often run at 15 µm to 30 µm. When the sealant layer is below 10 µm, seal strength can become inconsistent because the thermal mass at the seal interface is insufficient to maintain a stable melt layer during jaw opening. This represents an operational boundary for the material in thin-gauge lamination structures.
Optical quality of cast film is measured by ASTM D1003 for haze and ASTM D2457 at 60° for gloss. The uniform comonomer distribution in SP2510 reduces the light-scattering crystalline aggregates that increase haze in conventional C4-LLDPE, with the difference becoming more visible at film thicknesses above 30 µm. These optical properties are not fixed material constants; they shift with melt temperature, die gap, chill roll temperature, and winding tension. A change of 5 °C to 10 °C in chill roll temperature can change haze by several percentage points on a given cast-film line.
In comparative evaluations, SP2510 differs from high-pressure LDPE and C4-LLDPE in draw behavior and melt strength. The lower melt strength of SP2510 relative to Ziegler-Natta LLDPE can create edge instability if the die gap is too narrow or if the air gap is too long. Compared with C8 metallocene LLDPE grades used in high-performance sealants, SP2510 sits at a higher density and therefore offers higher flexural modulus, but its seal initiation is not as low as that of very low-density metallocene grades. The choice between SP2510 and a C8 mLLDPE should be made on the basis of package stiffness, sealant layer thickness, and sealing bar temperature capability, with direct comparison on the same cast-film line.
Extractables behavior further differentiates SP2510 from conventional C4-LLDPE. The metallocene catalyst system and low residual catalyst content typically produce hexane extractables below 1.0 wt% under the extraction protocol referenced in FDA 21 CFR 177.1520, whereas conventional C4-LLDPE grades at similar density and melt index may exceed 2.0 wt% depending on catalyst type and process history. This difference affects organoleptic performance and compliance in direct food-contact structures, particularly when fatty food simulants are used during migration testing.
Lot-to-lot consistency for SP2510 is monitored through melt mass-flow rate and density, with melt flow rate ratio sometimes used by converters as an indirect indicator of molecular weight distribution. For detailed shear thinning comparisons, capillary rheometry per ASTM D3835 can be performed on incoming lots; this is more sensitive than a single melt index value when qualifying material for a high-speed cast-film line.
Food-contact compliance for SP2510 is addressed under FDA 21 CFR 177.1520(c) and EU Regulation No 10/2011 as amended for plastic materials intended to come into contact with food. Converters must verify that the final package meets overall migration limits using EN 1186 and specific migration limits for any additives introduced through blending or masterbatch. The resin is supplied as a natural pellet without intentionally added slip or antiblock unless ordered as a formulated grade; high-speed packaging operations may require a slip/antiblock masterbatch to reduce coefficient of friction and prevent film blocking.
Storage and handling constraints apply to preserve processability. Pellets should be stored below 50 °C, protected from direct sunlight, and used within the supplier-recommended shelf life to avoid oxidative degradation of the stabilizer package. When pellet surface contamination occurs, low-pressure nitrogen or clean dry air cleaning is preferable to direct water washing because residual moisture can introduce surface defects during cast film extrusion. Compatibility with acid- or amine-containing masterbatches should be tested before production use, because such additives can shift heat-seal strength and film color in metallocene polyethylene systems. For hot-fill or retort applications requiring continuous exposure above 121 °C, SP2510 is generally not recommended as the sole sealant resin; polypropylene or high-density polyethylene sealants are typically selected for those thermal profiles.