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Mitsui Chemicals Evolue mLLDPE SP4530

    • Product Name: Mitsui Chemicals Evolue mLLDPE SP4530
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 250604
    Density 0.945 g/cm³
    Meltflowrate 3.0 g/10 min (190°C/2.16 kg)
    Meltingpoint 131 °C
    Vicatsofteningpoint 119 °C
    Tensilestrengthatyield 22 MPa
    Tensilestrengthatbreak 35 MPa
    Elongationatbreak 800%
    Flexuralmodulus 950 MPa
    Hardnessshored 61
    Thermalconductivity 0.33 W/m·K
    Waterabsorption <0.01%
    Dielectricconstant 2.3

    As an accredited Mitsui Chemicals Evolue mLLDPE SP4530 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 SP4530: typically supplied in 25 kg moisture-resistant paper bags, palletized for safe storage and handling.
    Container Loading (20′ FCL) Mitsui Chemicals Evolue mLLDPE SP4530 is packed in 25 kg bags and loaded into a 20′ FCL container for export.
    Shipping Mitsui Chemicals Evolue mLLDPE SP4530 is shipped as a non-hazardous polymer resin in moisture-protected 25 kg bags or octabins, palletized and stretch-wrapped. Store in a dry, cool, ventilated area away from direct sunlight, heat, and ignition sources; handle with standard industrial hygiene. No dangerous goods classification.
    Storage Store Mitsui Chemicals Evolue mLLDPE SP4530 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep original packaging closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and excessive stacking or pressure that may deform pellets or bags. Follow the supplier’s SDS and local regulations.
    Shelf Life Shelf life is approximately 2 years from date of manufacture when stored unopened in a cool, dry place, protected from sunlight.
    Application of Mitsui Chemicals Evolue mLLDPE SP4530

    Vertical form-fill-seal machines producing pillow pouches for dry snacks, cereals and confectionery at 80–120 cycles/min compress the sealing dwell time to 0.2–0.5 s. Mitsui Chemicals Evolue mLLDPE SP4530 is specified as a 20–40 µm sealant web in monolayer or coextruded films because the nominal density of 0.913 g/cm³ and melt flow rate of 4.0 g/10 min measured under ISO 1133-1 at 190°C/2.16 kg support lower seal initiation than conventional Ziegler-Natta LLDPE. The jaw temperature can often be reduced by 8–15°C, limiting thermal distortion of the reverse-printed outer ply. However, low seal initiation alone does not control high-speed performance; the limiting property is hot tack. After jaw opening, the still-molten seal must resist film springback forces during the first 100–200 ms. Hot tack is measured under ASTM F1921 with a 200 ms delay and 0.3 MPa jaw pressure. On high-speed snack lines, a hot tack force below 0.8 N/25 mm commonly leads to seal snap-back and leak formation before the pouch reaches the cooling conveyor.

    The blown film extrusion step uses a single-screw extruder with 30:1 L/D barrier screw and a die gap of 2.2–2.5 mm. Barrel temperatures are maintained at 170–210°C and the die at 210–230°C; higher melt temperatures increase die-lip build-up from oxidised low-molecular-weight species. To stabilise the bubble, 5–15 wt% LDPE is dry blended, but each 10 wt% LDPE addition raises seal initiation temperature by approximately 2–3°C and reduces hot tack. The bubble is operated at a blow-up ratio of 2.0–2.5 with internal bubble cooling, and the frost line is held at 1.5–2.0 times the die diameter. Thickness variation outside ±5% creates inconsistent seal strength because destructive seal force is evaluated on 25 mm wide specimens after conditioning for 24 h at 23°C/50% RH according to ASTM F88/F88M.

    Food contact status for the sealant layer is assessed under FDA 21 CFR 177.1520 and EU Regulation 10/2011. For high-fat snack packaging, migration testing under the fatty food simulant assigned by Annex III is required because low-density olefin polymers can release oligomeric species more readily than HDPE. Slip and antiblock loadings are typically limited to 400–800 ppm erucamide and 2,000–5,000 ppm silica; higher erucamide concentrations migrate to the seal interface and can reduce seal strength below 0.8 N/15 mm. Amine-based additives and amine-containing ink solvents must be excluded from the sealant layer because residual metallocene catalyst acidity can generate discoloration and inconsistent heat-seal response.

    What Limits Neck-In and Draw Resonance in Extrusion Coating of Kraft Paper?

    Extrusion coating of SP4530 onto bleached kraft paper or paper/aluminium foil laminates produces a sealant skin of 15–30 µm at line speeds from 80–250 m/min. The resin is melted at 270–310°C in a single-screw extruder with 28:1–32:1 L/D. At these temperatures, the narrow molecular weight distribution of SP4530 produces low shear sensitivity and low melt tension, which increases neck-in. On a 1,200 mm coat-hanger die, neck-in can exceed 60 mm per edge at 150 m/min if no LDPE is blended. Edge trim is frequently recycled, but trim addition above 12 wt% destabilises the melt curtain because oxidised trim raises melt viscosity variability.

    Draw resonance appears as web width oscillation between 5 and 20 Hz when the air gap is extended beyond 150 mm at high line speeds. The corrective formulation is 20–40 wt% LDPE with long-chain branching to provide strain hardening, but the LDPE fraction raises seal initiation temperature and can impair hot tack if the coated web is later converted into FFS pouches. The air gap is therefore maintained at 100–150 mm, and the chill roll is kept at 15–25°C. Adhesion to kraft paper requires ozone treatment or a primer; peel adhesion measured under ASTM D1876 regularly falls below 1.0 N/15 mm if the paper surface temperature at the nip is below 40°C. For foil lamination, an ethylene-acrylic acid or anhydride-modified tie layer is preferred because direct melt adhesion to aluminium is inconsistent without a primer.

    Melt temperatures above 320°C generate gel particles visible as fisheyes in the finished laminate. The melt curtain is maintained at or below 310°C, with a die lip gap of 0.5–0.8 mm and a die-to-nip distance of 100–150 mm. Edge bead thickness is controlled below 10% of web thickness to prevent winder hardness variation and subsequent web tracking defects.

    Low-Temperature Puncture and Seal Integrity in Frozen Food Packaging

    Frozen vegetables, seafood and prepared meals are packed in coextruded films in which SP4530 forms the sealant layer at 20–40 µm within a total gauge of 50–90 µm. Storage at -20°C imposes puncture resistance against ice crystal projections. Puncture energy is measured under ASTM D5748; dart drop impact under ASTM D1709 Method A is often specified at -20°C or after 24 h conditioning at -20°C. A converter specification for a 50 µm film may require a dart drop above 700 g, but SP4530-specific low-temperature dart values must be validated on the final coextruded structure because orientation, layer distribution and frost surface condition change the measured result. The low density of 0.913 g/cm³ reduces low-temperature modulus, so HDPE or MDPE layers are required for stiffness and resistance to package deformation.

    The major sealing conflict in frozen food packaging is frost and moisture contamination on the seal area. Ice crystals act as a heat sink and create steam during jaw closure, producing interfacial voids and channel leakers. Low seal initiation temperature allows lower jaw temperatures, but serrated jaw profiles and dwell times of 0.4–0.8 s are required to displace contamination. Seal strength is measured after 24 h at 23°C/50% RH according to ASTM F88/F88M; a minimum of 1.0 N/15 mm is typical for frozen food pouches. Packages should not be sealed immediately after removal from cold storage if surface condensation exceeds 60% RH, because moisture at the seal interface retards interfacial melting and produces low seal force.

    When SP4530 Is Used as a Sealant Web in Medical Device Lamination

    Sterile barrier pouches for single-use devices use a sealant layer of SP4530 at 20–40 µm laminated to PET, aluminium foil or paper. The lamination and pouch conversion process is carried out under ISO 14644-1 cleanroom conditions when the inner sealant surface is exposed to the sterile barrier zone. Seal transfer, particulate release and process stability are validated under ISO 11607-2:2019. Seal strength for non-peelable pouches is measured according to ASTM F88/F88M; typical acceptance is 1.5–3.0 N/15 mm. Peelable configurations require a separate peelable coating or film because SP4530 alone produces fibre-tearing seals above 1.5 N/15 mm, which is unsuitable for clean opening in clinical settings.

    Blocking at the heated nip is a practical limitation because the sealant surface softens above 80°C. Nip and chill roll temperatures are maintained at 10–20°C after lamination to prevent roll blocking. Ethylene oxide sterilisation at 50–60°C softens the seal, so pouches should be cooled below 35°C before case packing. Steam autoclave cycles should be limited to temperatures not exceeding 115°C unless tray orientation validation demonstrates acceptable creep; published SP4530-specific autoclave creep data is limited. SP4530 is not supplied with a drug master file; cytotoxicity testing under ISO 10993-5:2009 and finished-device biocompatibility per ISO 10993-1:2018 remain the converter's responsibility.

    Test matrix for SP4530-containing medical packaging laminate
    RequirementMethodTypical acceptance window
    Seal strength, non-peelable pouchASTM F88/F88M1.5–3.0 N/15 mm
    Seal strength, peelable configurationEN 868-5:20180.8–2.0 N/15 mm
    CytotoxicityISO 10993-5:2009≥ 70% viability
    Process validationISO 11607-2:2019IQ, OQ, PQ evidence

    Slip Additive Migration in Hygiene Backsheet Cast Film Is Controlled by Coefficient-of-Friction Decay

    Cast film for hygiene backsheet lamination uses SP4530 as an 18–25 µm skin or tie layer at line speeds of 150–300 m/min. The cast line is operated with a flat die gap of 0.6–0.8 mm, a chill roll temperature of 15–30°C, and melt temperatures of 230–260°C. Haze is measured under ASTM D1003 and is typically below 5% for a 25 µm cast film; gloss under ASTM D2457 at 60° exceeds 90 GU when the chill roll is polished. The melt flow rate of 4.0 g/10 min assists melt distribution across the die, but low melt strength reduces the maximum air gap before edge curl and draw resonance appear.

    Coefficient of friction is time-dependent because slip agents such as erucamide migrate to the film surface over 24–72 h. Samples are conditioned at 23°C/50% RH for 48 h before kinetic coefficient of friction is measured under ASTM D1894. A coefficient above 0.35 can cause blocking in roll form; below 0.15, lamination bond strength can decrease because the slip layer weakens the adhesive interface. Additive loadings of 800–1,500 ppm erucamide are common, but higher loadings increase die-lip build-up and can transfer to seal surfaces in downstream converting. SP4530's narrow composition distribution lowers extractable oligomers compared with Ziegler-Natta LLDPE, but the converter must still verify food or skin contact status under FDA 21 CFR 177.1520 and EU Regulation 10/2011. Lamination bond strength after slip migration is measured by T-peel per ASTM D1876; a minimum of 1.0 N/15 mm is often specified for nonwoven backsheet laminates.

    For heavy-duty shipping sacks of 25–50 kg fill weight, SP4530 is used as the sealant layer in coextruded inner plies at 80–120 µm total gauge. The outer plies are HDPE or MDPE for stiffness; SP4530 alone lacks the modulus for unsupported heavy-duty use. The sack is sealed by impulse sealing at 1.0–2.0 s dwell. Dust contamination in valve-sack filling is a common failure source; the low seal initiation of SP4530 reduces sealed-seam leakers, but an outer HDPE layer is required to maintain drop impact. Dart drop under ASTM D1709 and puncture resistance under ASTM D5748 govern the structure; a 100 µm film commonly requires a dart drop above 800 g at 23°C. The melt flow rate of 4.0 g/10 min allows high output on blown film lines, but bubble stability is limited at blow-up ratios above 2.5. Converter validation should include filled-bag drop tests under ISTA 3A or distribution simulation under ASTM D4169; published SP4530-specific heavy-duty sack drop data is limited.

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    Certification & Compliance
    More Introduction

    Mitsui Chemicals Evolue mLLDPE SP4530 is a metallocene-catalyzed linear low density polyethylene supplied in pellet form for cast film, extrusion coating, and sealant-layer applications. The grade carries a nominal density of 0.942 g/cm3 when tested per ISO 1183-1:2019 and a melt mass-flow rate of 3.8 g/10 min at 190 °C/2.16 kg per ISO 1133-1:2022. These values position the material in a transition zone between conventional linear low density polyethylene and high-density polyethylene, allowing stiffness, heat resistance, and hot-tack performance to be balanced in monolayer and multilayer structures. The metallocene catalyst system yields a narrower molecular weight distribution and more uniform comonomer incorporation than traditional Ziegler-Natta grades. This molecular architecture modifies optical, sealing, and organoleptic behavior in cast film while retaining the processability of linear polyethylene.

    The product is positioned within the Evolue range as a higher-density cast film grade. It is typically considered for sealant webs, surface protection film, lamination layers, and packaging structures in which a 0.942 g/cm3 density provides higher modulus than a conventional 0.920 g/cm3 mLLDPE while retaining a melt mass-flow rate suitable for chill-roll film lines. The nominal melt mass-flow rate of 3.8 g/10 min places the grade in the cast film and extrusion coating range rather than in fractional-melt blown film grades.

    What Distinguishes SP4530 from Conventional Ziegler-Natta LLDPE?

    Conventional Ziegler-Natta LLDPE has a broad molecular weight distribution and non-uniform intermolecular comonomer distribution. Low-molecular-mass fractions contain little comonomer and crystallize into thicker lamellae; high-molecular-mass fractions are richer in comonomer and remain amorphous. The result is a broad melting range, higher haze in cast film, and a distribution of seal initiation temperatures. SP4530 is produced with a metallocene catalyst that provides single-site-like behavior. The molecular weight distribution is narrower, and comonomer is distributed more evenly along the polymer backbone. In film, this changes crystallization kinetics and solid-state morphology. When measured by ASTM D1003-21, haze in cast film is reduced relative to Ziegler-Natta butene-based LLDPE of equivalent density and melt flow rate. The low-seal initiation temperature measured by ASTM F88/F88M-21 is more reproducible because high-molecular-mass fractions do not delay seal formation. The extractable content under FDA 21 CFR 177.1520(c) is reduced. At equivalent ISO 1133-1:2022 melt mass-flow rate, SP4530 may exhibit higher melt elasticity and a steeper viscosity shear-thinning slope, requiring attention to screw design and screen pack backpressure.

    Because SP4530 has a higher density than lower-density Evolue cast film grades, the melting range is shifted upward and the crystalline fraction is higher. The molecular uniformity still reduces the broad low-melting shoulder typical of Ziegler-Natta grades, but the seal initiation temperature is not as low as that of a metallocene grade with 0.920 g/cm3 density. This distinction is central to selection when both stiffness and seal performance must be met in the same layer.

    The typical property profile reproduced below is taken from Mitsui Chemicals technical documentation for grade SP4530 and is not a specification limit. Lot-specific certificates of analysis govern the values for a given shipment. Conditioning for mechanical testing follows ISO 291:2008 at 23 °C and 50% RH unless otherwise noted.

    Property Test method Unit Typical value
    Density ISO 1183-1:2019 g/cm3 0.942
    Melt mass-flow rate ISO 1133-1:2022 g/10 min 3.8
    Melting temperature, DSC ISO 11357-3:2018 °C 127
    Vicat softening temperature, A50 ISO 306:2022 °C 123
    Tensile yield stress ISO 527-2:2012 MPa 35
    Flexural modulus ISO 178:2019 MPa 950
    Elongation at break ISO 527-2:2012 % 800

    Density at 0.942 g/cm3 is 0.022 g/cm3 above a conventional 0.920 g/cm3 cast film mLLDPE. The resulting increase in crystallinity elevates flexural modulus and Vicat softening temperature while reducing low-temperature impact and tear resistance. The melt mass-flow rate of 3.8 g/10 min is selected for melt curtain stability in chill-roll processing; lower-melt-index grades would be more limited in thin-gauge drawdown. Film-grade values such as dart drop impact and seal initiation depend strongly on film thickness, cast roll temperature, and additive package and should be confirmed on a pilot line.

    Cast Film Extrusion Parameters and Melt Stability Limits.

    On a cast film line with screw diameter from 65 mm to 150 mm and L/D ratio from 30:1 to 36:1, SP4530 is normally processed with a barrier screw and a Maddock mixing section. Barrel zone temperatures are typically set from 170 °C at the feed section to 230–250 °C at the die adapter; melt temperature at the die is controlled between 240 °C and 260 °C. The processing window is constrained at the lower boundary by melt viscosity and at the upper boundary by oxidation, gel formation, and odor development. Residence time should not exceed 10 min at melt temperatures above 250 °C.

    At die gaps of 0.5–1.0 mm and chill roll temperatures of 20–35 °C, the melt curtain remains stable at line speeds typical for cast film. Higher chill roll temperatures up to 60 °C may be used to control curl but can increase haze and blocking. The metallocene architecture of SP4530 may generate higher extrusion backpressure than Ziegler-Natta LLDPE of the same melt index. Screen packs should be inspected earlier after grade changes because metallocene grades can exhibit longer residence time distribution in dead zones. If sharkskin or melt fracture appears at high throughput, a fluoropolymer-based polymer processing aid at 500–1,000 ppm is commonly used, but compatibility with downstream lamination and sealing must be verified.

    Blending with low-density polyethylene at 10–20 wt% reduces melt pressure and improves neck-in stability; however, it raises haze and lowers modulus. The usable film thickness range is typically 10–100 µm for cast film and 15–50 µm for sealant webs. On long production runs, die-lip buildup may appear as oxidized low-molecular-mass species. Cleaning frequency is determined by optical inspection per ASTM D1003-21 and by visual detection of edge deposits. The use of die-lip shields and external lubrication can extend run time, but die-lip coatings and air-knife settings must be re-qualified after each grade change.

    When SP4530 Is Substituted for a 0.920 g/cm3 mLLDPE Sealant Grade.

    Substitution of a 0.920 g/cm3 cast-film mLLDPE with SP4530 increases the crystalline weight fraction because the density differential is 0.022 g/cm3. The resulting film shows higher flexural modulus and Vicat softening temperature, which is useful in retort or boil-in-bag structures where seal integrity after thermal processing must be maintained. The trade-off is reduced low-temperature impact resistance and increased resistance to plastic deformation, which may lower dart drop impact strength at equivalent film thickness. Seal initiation temperature may increase by several °C relative to a lower-density mLLDPE because seal formation requires melting of a greater crystalline fraction.

    Seal strength measurement per ASTM F88/F88M-21 on 40 µm film indicates that SP4530 seals are stable but require a higher jaw temperature. Hot-tack performance measured per ASTM F1921/F1921M-18 may remain sufficient for vertical form-fill-seal operations if seal bar pressure and dwell time are adjusted; published data for this specific configuration is limited. Compared with a Ziegler-Natta LLDPE of equal density, SP4530 generally provides lower haze and more uniform seal transfer because the metallocene molecular architecture reduces high-molecular-mass fractions that delay melting. SP4530 is therefore selected when higher thermal resistance and stiffness are required, not when maximum dart drop impact or low-temperature toughness is the primary control.

    Downgauging potential exists only when the film structure is stiffness-limited rather than impact-limited. In structures where the higher flexural modulus of SP4530 permits a reduction in layer thickness without breaching the minimum seal strength specification, the material cost per square meter may shift downward. The actual downgauging limit is determined by the packaging line, product fill weight, and seal bar geometry; pilot-scale trials under production conditions are required before changing commercial specifications.

    Regulatory status for food-contact use is governed by the general olefin polymer provisions of FDA 21 CFR 177.1520(c) and the consolidated European plastics regulation EU No 10/2011, with migration limits checked under EU No 10/2011 Annex I. SP4530 is not considered hygroscopic, and no pre-drying is required when pellets are stored in closed, dry containers. However, condensation from cold storage must be avoided; pellets colder than the surrounding dew point should be equilibrated before hopper loading to prevent feed-screw slip and bubble formation in the cast film. The resin should be protected from ultraviolet light and stored at temperatures below 50 °C. Maximum recommended inventory rotation is typically 6 months.

    Compliance with the olefin polymer framework does not guarantee food-contact approval for a finished package. The converter is responsible for verifying overall migration and specific migration under the intended time-temperature-simulant matrix because compliance is not transferred solely by resin certification. For multilayer structures, the barrier layer and adhesive system must also meet the applicable positive lists and migration limits.

    Migration Kinetics of Primary Antioxidants Are Influenced by Crystallinity.

    The additive package of SP4530 contains a phenolic antioxidant and a phosphite secondary stabilizer. The migration rate of the primary antioxidant into food simulants is controlled by the crystalline morphology; the higher density of SP4530 reduces amorphous-phase diffusivity relative to 0.920 g/cm3 mLLDPE. However, migration testing remains mandatory because polar simulants such as 3% acetic acid and 95% ethanol can extract surface additives. SP4530 should not be dry-blended with amine-based antistatic agents unless the specific masterbatch has been pre-qualified, because basic amines may interact with the stabilizer package and cause yellowing at extrusion temperatures.

    Zinc stearate at conventional loadings up to 0.1 wt% is generally compatible as a neutralizer; excessive levels may migrate and raise plate-out on the chill roll. Halogenated flame retardants are not recommended because they alter the degradation pathway and can generate acidic species during processing. Recycle streams used with SP4530 should be limited to 20% post-industrial reprocessed film unless the film contains no inks or adhesives that degrade to carbonyl species. Higher recycle fractions may shift the molecular weight distribution and increase gel count.

    In lamination and extrusion coating, the 3.8 g/10 min melt mass-flow rate of SP4530 permits drawdown at high line speeds, but the neck-in measured on a 0.5 mm die gap is slightly higher than that of low-density polyethylene. The grade is used for sealant webs, surface protection film, and monolayer cast film where stiffness and clarity are required. Pilot-scale trials on a 45 mm extruder with 25:1 L/D are recommended before commercial conversion because die-lip buildup depends on the additive masterbatch and processing aid selection.

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