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MOPLEN PP EP548S

    • Product Name: MOPLEN PP EP548S
    • 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 808091
    Product MOPLEN PP EP548S
    Polymer Type Polypropylene Impact Copolymer
    Form Pellets
    Melt Flow Rate 8 g/10 min (230°C, 2.16 kg)
    Density 0.90 g/cm³
    Tensile Stress At Yield 20 MPa
    Elongation At Yield 6%
    Flexural Modulus 950 MPa
    Notched Izod Impact At 23 C 50 kJ/m²
    Notched Izod Impact At 20 C 6 kJ/m²
    Heat Deflection Temperature At 0 45 Mpa 80°C
    Heat Deflection Temperature At 1 8 Mpa 52°C
    Injection Molding Melt Temperature Range 190-230°C
    Mold Shrinkage 1.5%

    As an accredited MOPLEN PP EP548S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing MOPLEN PP EP548S polypropylene copolymer supplied in 25 kg multilayer paper bags, palletized and shrink-wrapped for safe transport.
    Container Loading (20′ FCL) 20′ FCL container loading of MOPLEN PP EP548S polypropylene pellets in 25kg bags, palletized and secured for safe transport.
    Shipping MOPLEN PP EP548S is a polypropylene copolymer supplied as free-flowing pellets. It ships as non-hazardous material in clean, dry containers or bulk bags. Protect from moisture, excessive heat, and direct sunlight during transit. Keep away from ignition sources and incompatible materials. Proper handling prevents contamination and maintains product quality.
    Storage Store MOPLEN PP EP548S in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid dust accumulation, as polypropylene dust may form explosive mixtures. Store in original, undamaged packaging, and keep separated from oxidizing agents.
    Shelf Life Shelf life is typically 12 months from delivery when stored in original, unopened packaging in a cool, dry place away from UV light.
    Application of MOPLEN PP EP548S

    In high-cavitation thin-wall injection moulding of freezer-to-microwave food containers, dairy portion cups, and tamper-evident deli lids with nominal wall sections between 0.45 mm and 1.20 mm, MOPLEN EP548S is processed at melt temperatures of 220 °C to 250 °C and mould temperatures of 10 °C to 30 °C to limit post-mould warpage while preserving drop impact resistance at −20 °C. The grade is a high-flow heterophasic ethylene-propylene copolymer; its melt flow behaviour under ISO 1133-1:2022 at 230 °C with 2.16 kg nominal load is used as a lot-release control rather than a direct predictor of thin-wall filling, because the dominant shear rates in sub-1.0 mm flow channels exceed the range of standard melt flow index testing. Final article conformity for food-contact service must be established under EU Regulation 10/2011, specifically the overall migration limit of 10 mg/dm² according to EN 1186-1, and under FDA 21 CFR 177.1520(c) for olefin polymers, with end-testing required for any added nucleating agent, antistatic package, or colour masterbatch. Production-scale failure modes observed on hot-runner, valve-gated stack moulds include gate blush on fast injection, hesitation lines across long flow paths, and sink marks at rib intersections when holding pressure decays before gate freeze; closed-loop transfer from velocity-controlled filling to pressure-controlled packing is configured on the basis of hydraulic pressure at the screw tip, not cavity pressure alone, to compensate for batch-to-batch melt flow variation. Typical tooling uses multi-cavity layouts with conical gate geometries and polished or textured cores to control release; ejection is assisted by air poppets or stripper plates when surface area exceeds 200 cm² and wall stock falls below 0.80 mm. Terminal articles in this sector include microwaveable polypropylene trays, cold-store dairy cups, and thin-wall lids where stack height and transport density force the minimum possible article mass.

    Application sectorReference standardTest methodCritical verification output
    Thin-wall food packagingEU Regulation 10/2011; FDA 21 CFR 177.1520(c)EN 1186-1; 21 CFR 177.1520Overall migration ≤ 10 mg/dm²; food-type and temperature restrictions
    Automotive interior trimFMVSS 302; ISO 3795Horizontal burning testBurn rate ≤ 100 mm/min for materials within occupant compartment
    Appliance housingsIEC 60335-1; RoHS 2011/65/EUIEC 60695-2-11Glow-wire ignition resistance and absence of restricted substances
    Dangerous goods pailsUN 1H2; ADR/RIDDrop test; stacking testNo leakage at specified drop height; stable stack for defined duration

    Thin-Gauge Automotive Interior Trim: Dimensional Control, Grain Retention, and Low-Temperature Ductility

    MOPLEN EP548S is processed into pillar covers, door panel inserts, seat side shields, and rear quarter trim panels where the requirement is a balance between low-temperature impact resistance and grain retention on visible surfaces. The material is injected at melt temperatures of 230 °C to 250 °C and mould temperatures of 15 °C to 35 °C; sequential valve gating is preferred for long-flow trim parts because it actively controls flow-front advancement and moves weld lines to structurally non-critical zones. Clamp tonnage is selected based on projected area, typically 3.0 kN/cm² to 5.0 kN/cm², but textured surfaces demand additional packing pressure to replicate grain uniformly and to prevent gloss variation along the flow path. Automotive interior conformity is evaluated under FMVSS 302 and ISO 3795 for horizontal burn rate, with a maximum burn rate of 100 mm/min commonly applied to occupant-compartment materials; volatile organic compound and fogging behaviour are measured under VDA 277 and VDA 278 when the trim part is specified by European OEM standards, and REACH Regulation (EC) No 1907/2006 SVHC screening applies to the compounded article. Low-temperature performance is characterised by notched Charpy impact according to ISO 179-1/1eA at −30 °C and instrumented puncture according to ISO 6603-2 at −20 °C; the specific acceptance values must be taken from the converter’s lot protocol because colour masterbatch, regrind level, and cooling rate shift the ductile-brittle transition. Typical failure modes observed on production lines include tiger-stripe flow marks, grain shadowing near the gate, and brittle weld lines at boss features when the flow-front temperature falls below the crystallisation onset temperature. Drying is normally not required for sealed material handling, but storage at relative humidity above 60% can introduce surface moisture that produces splay in hot-runner systems; pre-drying at 80 °C for 2 h to 4 h is applied when such conditions are detected.

    What Processing Limits Protect Puncture Resistance in Refrigerator Liners and Appliance Housings Below −20 °C?

    Large-area appliance components such as refrigerator door bins, ice-maker covers, and washing machine detergent dispenser housings use EP548S where the final article must survive occasional low-temperature impact without brittle fracture. The injection moulding window is constrained at the lower melt-temperature boundary by incomplete replication of textured surfaces and at the upper boundary by oxidative degradation of the ethylene-propylene rubber phase; melt-residence time above 250 °C should be limited to 10 min or less, and barrel temperature profiles are graduated from hopper 200 °C to nozzle 250 °C. Mould temperatures in the range 15 °C to 35 °C are used to balance cycle time against the development of oriented skin layers that affect low-temperature puncture energy measured under ISO 6603-2. Equipment with clamp force from 500 t to 1200 t is common for refrigerator liner parts; the injection machine should provide closed-loop pack control because post-mould shrinkage in thick bosses and reinforcing ribs leads to sink marks when the holding phase is terminated before gate freeze. Regulatory compliance for appliance housings is assessed under IEC 60335-1 for electrical safety and RoHS 2011/65/EU for restricted substances; where the end-use standard requires resistance to glow wire, the test is performed under IEC 60695-2-11 and the acceptance temperature is defined by the appliance manufacturer. The operational boundary of unfilled EP548S is reached when continuous exposure to strong oxidisers, aromatic hydrocarbons, or chlorinated cleaning agents occurs; environmental stress cracking may follow from lipid absorption, and prolonged exposure above 70 °C can accelerate post-crystallisation shrinkage. Terminal articles include refrigerator door bins, freezer drawer fronts, and injection-moulded housings for small domestic appliances where the combination of flow length, impact resistance, and surface quality determines material selection.

    When EP548S Replaces Standard Copolymer in Hinged Closure Systems

    Hinged closures for condiments, personal-care products, and household chemicals are moulded with integrally moulded hinges in the thickness range 0.25 mm to 0.45 mm; the hinge web must fill without jetting and must be oriented by immediate shear across the hinge line to resist premature flexural failure. MOPLEN EP548S is processed at melt temperatures of 230 °C to 250 °C and mould temperatures of 10 °C to 25 °C, with injection velocities set to produce a flow-front velocity that prevents hesitation at the hinge restriction; the pack profile then seals the hinge before the cooling gate freezes. Closure performance is evaluated using application-specific tests, including strip torque, resealing torque after repeated opening, and hinge flex endurance under ASTM D2063-12 or equivalent closure torque test protocols; published data for the exact hinge life of EP548S in a specific closure design is limited and must be generated on the production tool. Food-contact closures are subject to the same migration framework as thin-wall packaging, with overall migration tested under EU Regulation 10/2011 and FDA 21 CFR 177.1520(c). The operational boundary for carbonated soft drink carbonation is typically below 4.0 volumes CO₂ for polypropylene closures; above that, HDPE or PET closures are generally preferred due to creep and stress cracking in the thread root. Terminal articles include snap-top lids, disc-top caps, and dispensing closures where the polypropylene hinge replaces acetal or polyethylene closure systems.

    Talc-Filled Compounding Through Twin-Screw Dispersion and Vacuum Devolatilisation

    EP548S is used as a high-flow base resin for talc-filled compounds intended for semi-structural automotive interior carriers and appliance sub-frames; the high melt flow assists pigment and filler wet-out but reduces the shear heating margin in high-torque extruders, requiring careful temperature control. Compounding is performed on co-rotating twin-screw extruders with L/D between 32 and 44, gravimetric feeding of the resin in the main feed throat, and downstream side-feeding of talc after the polymer melting zone; vacuum devolatilisation is applied at −0.08 MPa to −0.09 MPa to remove low-molecular-weight volatiles and moisture before strand pelletising. Screw configuration for a 20 wt% talc loading typically includes two or three kneading blocks downstream of the side feeder, with distributive mixing elements rather than intense neutral kneading blocks to avoid excessive temperature rise and degradation of the rubber phase; melt temperatures are held between 190 °C and 220 °C, and specific mechanical energy input is monitored continuously to detect filler agglomeration. Tensile properties are verified after injection moulding according to ISO 527-2, flexural modulus according to ISO 178, Charpy impact according to ISO 179-1/1eA, and density according to ISO 1183-1; the quality gate for dispersion includes a pressure-rise test through a screen pack installed before the die, because undispersed talc agglomerates cause screen pressure spikes and surface defects in finished mouldings. Operational limitations include the incompatibility of unsaturated or amine-functional additives with peroxides used in some grafting processes, and the need to avoid direct adding of high-moisture talc without vented side-feed, as hydrolysis accelerates polypropylene chain scission. Terminal articles produced from such compounds include automotive airbag housings, glove-box structural inserts, and washing machine outer tub carriers where the combination of stiffness, heat resistance, and low-temperature impact is controlled by the ratio of EP548S to mineral filler.

    For stackable industrial crates, distribution pails, and agricultural logistics trays with wall thickness from 1.8 mm to 4.0 mm, MOPLEN EP548S is processed at melt temperatures of 220 °C to 240 °C and mould temperatures of 10 °C to 25 °C; the thicker sections shift cycle time toward cooling rather than filling, so mould temperature uniformity and conformal cooling layout control total cycle more than melt temperature reduction alone. In pail designs intended for dangerous goods transport, the article must satisfy UN 1H2 drop test and stacking requirements under ADR/RID or IMDG, and the handle boss areas are the critical weld-line locations; processing parameters are adjusted to position weld lines away from the bail ear and to increase local pressure by sequenced valve gating or overflow wells. Batch-to-batch variation in melt flow affects fill pressure and sink mark formation at the handle lug; therefore, process alarm limits on fill time and hydraulic pack pressure are set from a validated normal distribution of at least 20 consecutive production lots. Environmental stress cracking in service can occur when the pail contains fatty acids, esters, or aromatic solvents; liquid immersion screening under ISO 22088-3 is recommended when the final article moves beyond aqueous or dry-goods applications. Terminal articles in this application sector include 20 L injection-moulded pails, ventilated fruit crates, collapsible distribution boxes, and stacking trays used in automated warehouses.

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    Certification & Compliance
    More Introduction

    Supplied as spherical pellets for injection moulding, MOPLEN PP EP548S is a heterophasic propylene-ethylene impact copolymer produced by LyondellBasell. In the ISO 19069-1:2015 classification system for polypropylene materials, the grade is positioned in the impact-copolymer category, identified by an ethylene-propylene rubber phase dispersed in a polypropylene matrix. The nominal melt mass-flow rate measured at 230 °C with a 2.16 kg load is 11 g/10 min under ISO 1133-1:2022, and the density is 0.900 g/cm³ under ISO 1183-1:2019. The rubber-phase content contributes to a property envelope that differs from unfilled polypropylene homopolymers; the matrix provides stiffness and thermal resistance, while the dispersed ethylene-propylene phase improves energy absorption during impact loading. Mechanical property values are generated from injection-moulded test specimens prepared according to ISO 19069-2:2016 and conditioned at 23 °C and 50 % relative humidity according to ISO 291:2008. The grade is intended for medium-flow injection moulding where a balance of ambient-temperature ductility and processing ease is required. Typical downstream equipment includes conventional reciprocating-screw injection moulding machines with L/D ratios between 20:1 and 24:1; no specialized plastication unit is required. The product is supplied without a chemical blowing agent, and the pellet form is compatible with central material-handling systems, provided the conveying air dew point is maintained below 5 °C to limit surface condensation.

    Which standardised property values define the specification envelope?

    The specification envelope is established using ISO methods rather than single-point vendor specifications. Test specimens are injection-moulded in accordance with ISO 19069-2:2016, and the values in Table 1 represent typical mid-range data from supplier technical literature. These are not batch-level release limits; purchasers should obtain the current certificate of analysis for the specific lot.

    Property Method Typical Value
    Melt mass-flow rate at 230 °C / 2.16 kg ISO 1133-1:2022 11 g/10 min
    Density ISO 1183-1:2019 0.900 g/cm³
    Tensile modulus ISO 527-2:2012 1100 MPa
    Tensile stress at yield ISO 527-2:2012 23 MPa
    Tensile strain at yield ISO 527-2:2012 6 %
    Charpy notched impact strength at 23 °C, Type 1 specimen, edgewise ISO 179-1/1eA:2010 25 kJ/m²
    Charpy notched impact strength at -20 °C ISO 179-1/1eA:2010 5 kJ/m²
    Vicat softening temperature, A50 ISO 306:2013 152 °C
    Heat deflection temperature, 0.45 MPa flatwise ISO 75-2/B:2013 90 °C

    Tensile modulus is determined at a test speed of 1 mm/min until 0.25 % strain, after which the crosshead speed is increased to 50 mm/min according to ISO 527-2:2012. The Charpy notched impact test uses a Type 1 specimen with a 0.25 mm A-notch; the edgewise orientation is identified by the 1eA designation. Low-temperature impact at -20 °C is substantially lower than the ambient-temperature value, a known limitation of impact-copolymer systems where the rubber phase approaches its glass transition. Users designing for cold storage or outdoor winter conditions should specify additional post-moulding impact testing at the minimum service temperature of the application.

    Processing Behaviour on Reciprocating-Screw Injection Moulding Lines

    Drying is not systematically required for MOPLEN PP EP548S. Polypropylene is not hygroscopic, and moisture uptake under normal indoor storage is below 0.05 % by weight. If pellet exposure to condensation or relative humidity above 60 % occurs, surface moisture can generate splay defects on moulded parts; hopper drying at 80 °C for 2 h is sufficient to remove surface water. The melt temperature measured at the nozzle should be maintained between 200 °C and 250 °C, with 230 °C as the usual set point for screw-recovered melt. At melt temperatures below 200 °C, the increased viscosity can produce short shots in thin-wall sections; above 280 °C, thermal oxidative degradation may cause yellowing and a loss of notched impact strength. The barrel temperature profile should be reverse or flat, with the feed zone set 20–30 °C below the nozzle temperature to prevent bridging in the feed throat. A general-purpose polyolefin screw with an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.5:1 to 3:1 provides adequate homogenization. Back pressure should be held between 0.5 MPa and 1.0 MPa hydraulic, or 5–10 bar; excessive back pressure increases residence time and may shift the melt flow rate upward through chain scission. Injection speed should be selected according to cavity thickness: for wall sections of 1.5 mm to 3.0 mm, fill velocities of 100–200 mm/s are typical, while thick sections above 4 mm require lower velocities to avoid jetting and internal weld lines. Mould temperature from 20 °C to 50 °C is acceptable; higher mould temperatures up to 60 °C improve surface replication but increase cooling time and shrinkage anisotropy. A melt cushion of 2–5 mm is recommended after pack to maintain gate freeze control and reduce sink marks. Check-ring wear on older injection units can reduce cushion consistency and lower part-to-part Charpy impact repeatability; inspection intervals of 500 000 cycles are used on high-volume packaging lines. Published data for specific clamp-force optimizations on this grade are limited, but the clamp force is sized on projected area for cavity pressures of 35 MPa to 50 MPa in rigid crates and technical components.

    High-impact crates, rigid packaging, housewares, toys, and technical components are injection-moulded from MOPLEN PP EP548S where the specification requires ductile failure at ambient temperature and moderate stiffness sufficient to resist stacking loads. The notched Charpy value of 25 kJ/m² at 23 °C under ISO 179-1/1eA:2010 provides a reproducible measure of crack-initiation resistance, but component performance must be validated by application-specific tests. Stacking containers are routinely evaluated by top-load compression tests conducted at 10 mm/min crosshead displacement with load retention for 24 h at 23 °C; published data for this specific configuration is limited, and prototype validation on the filled container is required. For cold-chain crates, the -20 °C Charpy value of 5 kJ/m² indicates a reduction in impact energy absorption at low temperature, so rib radii and wall thicknesses should be increased at stress-concentration points. The grade can be processed with conventional hot-runner systems; gate geometries with a minimum orifice diameter of 0.8 mm reduce shear heating and preserve impact-copolymer morphology. Weld lines are inherent in multi-gate injection moulding and represent the most common failure sites under impact loading. Mould-filling simulation using a two-domain moldflow model should be performed for parts with weld lines in load-bearing regions; the simulation should use the 11 g/10 min MFR and 0.900 g/cm³ density as input. Colour change and regrind handling on production lines are standard; regrind addition up to 20 % by weight is typical, but higher fractions may reduce low-temperature Charpy impact due to repeated shear history and rubber-phase coalescence. When regrind exceeds 30 %, impact retention should be confirmed by ISO 179-1/1eA testing on moulded parts.

    When EP548S Replaces Homopolymer Grades in Thin-Walled Packaging

    Comparisons between MOPLEN PP EP548S and unfilled polypropylene homopolymers are governed by differences in phase morphology, melt flow, and stiffness. A general-purpose injection moulding homopolymer with a similar 12 g/10 min MFR typically shows a tensile modulus in the range 1450 MPa to 1700 MPa under ISO 527-2:2012, while EP548S shows a lower tensile modulus near 1100 MPa. The trade-off is impact resistance: homopolymer notched Charpy values at 23 °C are generally below 5 kJ/m², while EP548S is typically 25 kJ/m². For thin-walled packaging with wall thickness below 0.8 mm, the lower viscosity of high-flow homopolymers or controlled-rheology impact copolymers in the 25–40 g/10 min range is preferred; EP548S at 11 g/10 min may fail to fill long flow paths at practical injection pressures below 120 MPa. When replacing a homopolymer with EP548S in an existing mould, the lower modulus reduces bending stiffness by approximately 20–30 % for identical part geometry; rib thickness or rib count must be adjusted. Conversely, the improved Charpy impact often permits thinner wall sections for impact-critical housings, but this must be verified by instrumented drop-weight tests at the part level. Compared with random copolymers, EP548S is opaque rather than transparent and provides substantially higher low-temperature ductility; random copolymers used for clear housewares display better optical clarity but lower notched impact at -20 °C. The Vicat softening temperature of 152 °C under ISO 306/A50 is slightly below values for homopolymers, which typically fall between 150 °C and 160 °C; stacking containers exposed to hot wash cycles above 80 °C require creep testing under load. For applications in contact with fatty foods, end-use compliance must be confirmed under FDA 21 CFR 177.1520 and the relevant European food-contact regulation; the grade may be supplied with a food-contact statement, but migration testing on the finished article remains the responsibility of the converter.

    Compliance testing for high-volume packaging lines requires documented evidence from the resin supplier. Table 2 summarises the principal regulatory references applicable to polypropylene impact-copolymer grades supplied in the European market.

    Requirement Reference Status
    European chemical regulation REACH (EC) No 1907/2006 Supplier declaration available
    Restriction of hazardous substances RoHS Directive 2011/65/EU, Pb <1000 mg/kg, Cd <100 mg/kg, Hg <1000 mg/kg, Cr(VI) <1000 mg/kg, PBB/PBDE <1000 mg/kg Compliant as supplied
    Food-contact base polymer FDA 21 CFR 177.1520 Meets olefin polymer requirements, subject to conditions of use
    Specimen preparation ISO 19069-2:2016 Used for mechanical property data
    Test specimen conditioning ISO 291:2008 23 °C / 50 % RH

    Material datasheets and supplier compliance statements are not substitutes for end-item certification. Converters must verify that colour concentrates, processing aids, and regrind additions do not alter the regulatory profile. For food-contact applications, the final article must comply with overall migration limits under the applicable European regulation, such as 10 mg/dm² of food-contact surface area for general food contact under Commission Regulation (EU) No 10/2011.

    Incoming quality control on production lines often verifies melt mass-flow rate, density, and moisture content. Melt flow rate is checked at 230 °C with 2.16 kg according to ISO 1133-1:2022; lots within ±1.5 g/10 min of the nominal value are typically accepted for injection moulding. Density is measured by displacement in water or ethanol according to ISO 1183-1:2019. Pellet moisture is determined by Karl Fischer coulometry at 160 °C; values above 0.10 % may indicate surface condensation and require drying. Ash content by ISO 3451-1:2019 should remain below 0.05 % unless a specific nucleation package is declared. The colour of the base resin is natural, and lightness values can vary between production sites due to catalyst residues; colour-critical parts should use masterbatch at 2–4 % addition. For outdoor UV-stabilized parts, a UV masterbatch or a grade with hindered amine light stabilizers should be selected; EP548S as supplied is not formulated for prolonged unprotected UV exposure.

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