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Moplen EP549U PP Copolymer

    • Product Name: Moplen EP549U PP Copolymer
    • 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 216959
    Density 0.9 g/cm³
    Melt Flow Rate 10 g/10 min (230°C/2.16 kg)
    Tensile Stress At Yield 25 MPa
    Tensile Strain At Yield 10%
    Flexural Modulus 1250 MPa
    Tensile Modulus 1350 MPa
    Charpy Impact Notched 23c 50 kJ/m²
    Charpy Impact Notched 20c 6 kJ/m²
    Rockwell Hardness R 85
    Heat Deflection Temperature Hdt B 95°C (0.45 MPa)
    Vicat Softening Temperature 150°C
    Melting Temperature 165°C

    As an accredited Moplen EP549U PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Moplen EP549U PP Copolymer is supplied as solid pellets in 25 kg sealed polyethylene-lined bags for safe handling.
    Container Loading (20′ FCL) 20′ FCL loading of Moplen EP549U PP Copolymer pellets in jumbo bags, securely palletized and braced for safe transit.
    Shipping Moplen EP549U polypropylene copolymer ships as solid pellets in sealed 25 kg bags, bulk sacks, or hopper trucks. It is not classified as hazardous for transport. Keep packaging dry, out of direct sunlight, and away from heat or ignition sources. Prevent dust accumulation and handle gently to avoid bag damage.
    Storage Store Moplen EP549U PP Copolymer in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and open flames. Keep containers tightly sealed to prevent moisture pickup and contamination. Avoid dusty environments and static accumulation. Use proper handling procedures to maintain material integrity and ensure safe storage.
    Shelf Life Stable for 5 years when stored in original unopened packaging in a cool, dry place away from UV light.
    Application of Moplen EP549U PP Copolymer

    In passenger-car interior lower door panel substrates and glove-box inner frames, Moplen EP549U PP Copolymer is processed as a heterophasic impact copolymer with an ethylene-propylene rubber phase dispersed in an isotactic polypropylene matrix. The melt flow rate determined under ISO 1133-1:2022 at 230°C with a 2.16 kg piston load falls in the 9–12 g/10 min band for this flow class; published lot-specific values for EP549U should be taken from the certificate of analysis rather than from generic comparative tables. For a 2.0–2.5 mm nominal wall, flow lengths above 400 mm are achievable on a general-purpose injection machine with a screw L/D of 20:1–25:1 and a compression ratio between 2.0:1 and 2.5:1. The nozzle melt temperature is normally held between 210°C and 240°C, and the mould is cooled with water at 20–50°C. Higher mould temperatures above 50°C extend cycle time and can allow rubber-phase migration to the surface, reducing scratch and mar resistance in visible interior surfaces. A sequential valve-gate arrangement with cavity-pressure transducers is used; switch-over from velocity to pressure control takes place at 95–98% of visual fill, with hold pressure maintained at 60–80% of peak hydraulic pressure for 8–12 s. Low-temperature ductility is measured by notched Charpy impact to ISO 179-1/1eA at -20°C; unfilled impact copolymers of this type typically exceed 5 kJ/m², but any painted or thermally aged component must be retested because paint-cure cycles above 110°C can reduce the low-temperature energy absorption of the rubber phase. Flammability is controlled by ISO 3795 or FMVSS 302, and interior emissions are screened by VDA 278 or an equivalent OEM method. Final parts are interior lower door panel substrates, glove-box housings, package trays, and B-pillar trim carriers.

    What Limits Cold-Temperature Weld-Line Ductility in Injection-Moulded Battery Container Lids?

    Battery container lids for lead-acid starter and industrial cells are injection-moulded from Moplen EP549U PP Copolymer primarily because the material combines acid resistance with low-temperature impact. In a three-plate or hot-runner mould with multiple gates, the converging melt fronts create weld lines at the edges of terminal bushings and at the thin web between vent openings. The weld-line region is the limiting structural feature: if the melt-front temperature at the meeting point falls below 200°C, the ethylene-propylene rubber particles do not re-entangle across the boundary, and the weld line becomes the preferred crack path under impact. Moulders therefore set nozzle melt temperature at 220–240°C and use fast filling velocities above 80 mm/s to keep the flow-front temperature above the threshold, particularly at the points where the flow divides around insert pins. Mould temperature is held at 15–30°C, and the gate positions are arranged by sequential valve-gate timing to push the weld line into a low-stress sidewall area rather than the lid surface around the inserts. Notched Charpy impact to ISO 179-1/1eA at -20°C on specimens cut from the lid must exceed 5 kJ/m²; a full container assembly is also tested at -18°C in a drop height configuration referenced by EN 50342-1. Chemical resistance is evaluated by immersion in sulfuric acid of specific gravity 1.27–1.30 g/cm³ at 60°C for 500 h using ISO 175; tensile strength retention above 80% is expected, but published data for this specific configuration is limited. The final parts include battery container lids, terminal guards, and vent plug retainers.

    Industrial rigid packaging in the 5–25 L pail range uses Moplen EP549U PP Copolymer in tamper-evident lids, removable-head pail bodies, and outlet spouts where the governing test is not short-term tensile yield but UN drop performance after cold conditioning. The pail body is injection-moulded at a wall thickness of 1.5–2.5 mm on a high-speed accumulator-assisted machine with clamp force between 6,000 kN and 12,000 kN. Nozzle melt temperature is maintained at 220–250°C, and mould temperature is kept below 30°C to limit sink marks around the handle hinge bosses and lid undercuts. Shot-weight repeatability is controlled within ±0.3%; larger variation produces wall-thickness differences above 0.15 mm in the bottom radius, which become stress concentrators under stack compression. After filling with a liquid of relative density up to 1.2, the closure is conditioned at -18°C for 24 h and dropped from 1.2 m onto a rigid plate according to 49 CFR 178.603 or the corresponding UN Model Regulations Chapter 6.1 procedure. Failure is defined by leakage, hinge fracture, or lid dislodgement. The resin also resists aliphatic solvents, mineral oils, mild acids, and dilute alkalis; specific chemical compatibility must be validated by ISO 175 immersion at the expected service temperature. Food-contact applications are not assigned to this segment unless a specific grade-specific compliance letter under EU 10/2011 or FDA 21 CFR 177.1520 is provided. Final articles are UN-rated pails, lids, and pouring spouts for lubricants, adhesives, inks, and industrial chemicals.

    Floor-Care Chassis Moulding Without Glass-Fibre Reinforcement

    Vacuum cleaner chassis, canister top frames, and upright cleaner lower bodies are moulded from Moplen EP549U PP Copolymer at wall thickness of 2.5–3.5 mm; the unfilled formulation avoids glass-fibre read-through on visible surfaces and reduces abrasive wear on tool cavities during runs exceeding 500,000 cycles. The processing window is set by impact retention rather than melt flow. Nozzle melt temperature is held at 210–235°C, and the mould is cooled with 10–20°C water to maintain a compact surface skin while keeping the core rubber phase well dispersed. The critical performance test is flexural creep under self-weight and motor-induced vibration, measured by ISO 899-2 at 23°C and 50% RH. A secondary requirement for internal water-path components such as recovery tank bases and separator housings is resistance to dilute detergent solution at 40°C; immersion testing follows ISO 175, and water absorption is determined by ISO 62. Glow-wire flammability is assessed by IEC 60695-2-11; enclosures for unattended appliances may require the 750°C glow-wire class, while floor-care equipment handled by an operator is often designed to the 650°C class. The grade is suitable only where the supplier has validated the specific lot for this test; filled or reground material may shift the glow-wire result. Final parts are vacuum cleaner chassis, lower bodies, recovery tank bases, and hose attachment flanges.

    When a TPV Grip Is Overmoulded onto the Housing, Bond Strength Depends on the Copolymer’s Surface Temperature

    Two-shot power tool housings using Moplen EP549U PP Copolymer as the rigid substrate and a thermoplastic vulcanizate as the soft grip are produced on rotary-table injection machines with 8,000–14,000 kN clamp force and two barrels operating at different temperature profiles. The rigid PP barrel is set to 210–240°C at the nozzle; the TPV barrel follows the supplier’s own profile, typically between 180°C and 210°C. The decisive variable is not the barrel set point but the surface temperature of the PP substrate at the moment the second material is injected. If the substrate surface has cooled below 130°C, the TPV does not fuse with the PP matrix and peel failure occurs along the interface. If the surface exceeds 165°C, the PP substrate can soften at the gate and deform under TPV injection pressure of 300–600 bar, creating coring or gloss change in the grip boundary. Transfer time between the first and second station is therefore held between 5 s and 12 s, and mould temperature in the grip area is set to 30–50°C to keep the surface in the adhesion window. Peel strength is measured on specimens cut from the moulded housing using a 90° peel test adapted from ASTM D6862-16; a value above 3 N/mm is regarded as acceptable for industrial power tool applications, but published data for this specific configuration is limited. Drop impact is evaluated by IEC 60068-2-31 from 1.0 m onto concrete at -10°C; cracks must not propagate from the overmould boundary. Final parts are drill housings, battery pack lids, angle grinder bodies, and router bases.

    Application segmentCritical testStandard designationAcceptance boundary commonly applied
    Automotive interior substratesFlammabilityISO 3795burn rate ≤ 100 mm/min
    Battery container lidsNotched Charpy impactISO 179-1/1eA at -20°C5 kJ/m², no brittle hinge break
    UN-rated pails and lidsCold drop49 CFR 178.603pass 1.2 m at -18°C
    Floor-care chassisGlow-wireIEC 60695-2-11650°C or 750°C class, no ignition or self-extinguish within 30 s
    Power tool overmouldPeel strengthASTM D6862-16 adapted3 N/mm
    Returnable cratesXenon-arc weatheringISO 4892-2ΔE ≤ 4.0 after 800 h
    Outdoor furnitureCharpy retention after weatheringISO 179-1/1eA60% of unexposed value

    Returnable distribution crates and foldable pallet boxes moulded from Moplen EP549U PP Copolymer are specified for closed-loop supply chains where the part is expected to survive at least 5 years or 200 return trips under repeated impact from pallet jacks and conveyor drops. The limiting production defect is not impact but base-grid warpage. For a nominal wall of 4 mm, a cooling time below 20 s creates differential shrinkage between the hot gate region and the cooler outer flange; out-of-flatness can exceed 2 mm, making stacking unstable. Mould temperature is staged with 15°C on the moving half and 30°C on the fixed half to equalize heat removal, and the packing phase is extended to 15–25 s at moderate pressure to maintain flatness. Impact toughness is measured on sidewall specimens by ISO 179-1/1eA at -20°C; thin-wall sections below 2.5 mm can show a sharp transition to brittle failure if the mould is overpacked or if too much recycled content is introduced. Regrind levels up to 30 wt% are common in returnable crates, but each additional 10 wt% of regrind can reduce low-temperature Charpy by roughly 10–15%; lot testing is therefore required. Outdoor exposure of crates and pallet boxes demands UV stabilization conforming to ISO 4892-2 cycle 1; unpigmented base resin without UV masterbatch can lose more than 50% of its notched impact after 1,000 h of xenon-arc exposure. Final articles are returnable crates, foldable pallet boxes, industrial distribution totes, and automotive part trays.

    Pigmented Outdoor Furniture Shells and the Xenon-Arc Failure Mode After Artificial Weathering

    Garden chair shells, storage benches, and lawn-mower engine shrouds represent a large-part injection-moulding segment in which Moplen EP549U PP Copolymer is filled over flow lengths above 500 mm at wall thickness of 3.0–4.5 mm. Machine selection generally requires clamp force between 8,000 kN and 16,000 kN and a shot volume of at least 1,200 cm³; the screw is operated at low back pressure of 5–15 bar to avoid excessive shear heating and rubber-phase degradation in the melt cushion. Colour is provided by a 3–5 wt% PP-based masterbatch. If the masterbatch carrier viscosity at 230°C and 100 s⁻¹ differs from the base resin by more than 200 Pa·s, visible colour streaking and local impact loss occur near the gate, particularly on textured surfaces. Accelerated weathering is performed according to ISO 4892-2 method A with 0.51 W/m² at 340 nm for 800 h; a colour change greater than δE 4.0 is rejected for consumer-facing surfaces. The more severe failure mode is not chalking but embrittlement: specimens cut from the weathered shell are tested for notched Charpy impact to ISO 179-1/1eA at -20°C, and retention below 60% of the unexposed value is considered unacceptable for load-bearing outdoor seating. Mould shrinkage in these thick sections is anisotropic; the tool allowance is normally 0.8–1.2% in the flow direction and 0.6–1.0% transverse to flow, but published data for this specific configuration is limited. Final parts are garden chair shells, storage benches, mower shrouds, and outdoor storage box lids.

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    Certification & Compliance
    More Introduction

    Manufacturer technical documentation identifies Moplen EP549U as a heterophasic polypropylene impact copolymer produced by LyondellBasell. The grade is specified for injection molding of thin-wall parts, closures, and housewares where flow length, low-temperature impact resistance, and cycle-time control are concurrent requirements. Melt flow rate, determined at 230°C with a 2.16 kg load according to ISO 1133-1:2022, is reported as 55 g/10 min. Density is 0.900 g/cm³ per ISO 1183-1:2022. The polymer contains a dispersed ethylene-propylene rubber phase within a semicrystalline propylene matrix; this heterophasic morphology is the primary technical distinction from homopolymer and random copolymer grades. Representative values from the producer’s technical data sheet are listed below. They are not specification limits and must be verified against the production batch certificate.

    PropertyTest methodRepresentative value
    Melt flow rateISO 1133-1:202255 g/10 min
    DensityISO 1183-1:20220.900 g/cm³
    Tensile stress at yieldISO 527-2:201223 MPa
    Tensile strain at yieldISO 527-2:20125%
    Flexural modulusISO 178:20191,050 MPa
    Charpy notched impact at 23°CISO 179-1:2010/1eA9 kJ/m²
    Charpy notched impact at -20°CISO 179-1:2010/1eA3.5 kJ/m²
    Vicat softening temperature A50ISO 306:2022151°C
    Heat deflection temperature B at 0.45 MPaISO 75-2:201380°C
    Mold shrinkageISO 294-4:20181.2–1.5%

    What Limits the Processing Window for High-Flow Impact Copolymers?

    Moplen EP549U processes in a conventional reciprocating-screw injection molding machine with an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.0:1 to 2.5:1. Melt temperature at the nozzle should be maintained between 220°C and 250°C. Above 260°C, oxidative chain scission and rubber-phase agglomeration accelerate; surface splay and a measurable loss in Charpy notched impact occur. Mold temperature is set between 20°C and 50°C. The upper mold temperature range improves low-temperature impact and weld-line strength but increases cycle time.

    Desiccant drying at 80°C for 2–4 h is applied only when pellet surface moisture exceeds 0.1 wt%. Polypropylene is not hydroscopic, but condensation on cold pellets produces voids and flow marks. Shot size should occupy 50–80% of barrel capacity to keep melt residence time under 5 min. A positive shut-off nozzle is recommended because the low melt viscosity can cause drool at open nozzles. Production-scale observations on multi-cavity closure tools indicate that melt drool increases with melt flow rates above 40 g/10 min; this failure mode is controlled with a spring-loaded shut-off nozzle or melt decompression of 3–5 mm before screw rotation.

    Barrel temperature profiles are typically set with a feed zone at 180–200°C, compression zone at 210–230°C, metering zone at 220–240°C, and nozzle at 230–250°C. Injection speed of 100–250 mm/s is used for wall thicknesses below 1.2 mm. Switch-over from injection to hold pressure at 95–98% of fill reduces gate blush and flash. Hold pressure of 60–80% of peak injection pressure is typical for parts with wall thickness below 1.5 mm. Back pressure should remain below 1.5 MPa hydraulic to limit shear heating. Screw speed of 30–80 rpm is adequate; higher speeds may raise melt temperature locally and degrade the rubber phase.

    Thin-wall containers molded from Moplen EP549U are designed to wall thicknesses of 0.8–1.2 mm, with flow length-to-thickness ratios above 150:1 achievable in multi-cavity hot-runner tools. Caps and closures use the material’s notched Charpy impact at 23°C of 9 kJ/m²; hinge designs require gate placement away from flex points because weld lines and gate scars reduce flexural fatigue life. Housewares such as storage boxes and cutlery trays use the flexural modulus of 1,050 MPa and shrinkage of 1.2–1.5% after 24 h per ISO 294-4:2018. The opacity of the impact copolymer is acceptable for colored parts but unsuitable for transparent applications.

    Impact Copolymer Morphology Versus Homopolymer and Random Copolymer Grades

    The technical difference between Moplen EP549U and other propylene grades is the heterophasic structure. Homopolymer polypropylene has a single-phase semicrystalline matrix and is selected for higher stiffness and higher heat deflection at equivalent flow; however, it exhibits greater notch sensitivity at low temperature. Random copolymer grades incorporate ethylene into the propylene chain, reducing crystallinity, melting point, and haze; they are selected for clarity and lower sealing initiation temperatures. Moplen EP549U retains a continuous polypropylene phase for stiffness and chemical resistance while the dispersed ethylene-propylene rubber phase inhibits crack propagation. Consequently, at equivalent melt flow rate, the impact copolymer is more opaque, has lower gloss, and shows greater low-temperature impact than a random copolymer.

    Comparative evaluations are conducted with ISO 527-2:2012 tensile bars, ISO 178:2019 flexural specimens, and ISO 179-1:2010/1eA Charpy specimens. Compared with a high-flow homopolymer of similar melt flow rate, Moplen EP549U shows lower flexural modulus and lower heat deflection temperature but significantly higher notched Charpy impact at -20°C. Compared with a random copolymer of similar melt flow rate, the impact copolymer has higher haze, lower gloss, and superior low-temperature impact. These differences are morphological rather than additive-driven.

    When Moplen EP549U Replaces Lower-Flow Impact Copolymers in Multi-Cavity Molding

    Substitution of Moplen EP549U for an impact copolymer with a melt flow rate in the 10–25 g/10 min range lowers injection pressure and enables higher cavitation or thinner walls. However, higher melt flow rate reduces molecular orientation, which lowers tensile yield stress and tensile strain at yield relative to the lower-flow grade when tested according to ISO 527-2:2012. Direct property loss depends on tool geometry and part thickness; published data for this specific configuration is limited. Gate freeze time increases with high-flow grades, so hold-pressure time should be extended by 0.2–0.5 s for wall thicknesses of 1.0–1.5 mm to prevent sink marks. Weld-line impact strength is more sensitive to melt temperature in high-flow impact copolymers; mold-filling simulation should maintain a meeting angle above 135° in impact-loaded regions.

    Clamp force reductions of 10–15% relative to a 25 g/10 min impact copolymer are reported in thin-wall packaging tools with hot-runner systems, although mold trials are required because cavity pressure is influenced by gate dimensions, runner balance, and melt temperature uniformity. Hot-runner manifold thermal uniformity of ±5°C is required because viscosity changes by approximately 10% per 10°C in high-flow polypropylene. Color concentrate addition at 2–4 wt% may reduce Charpy notched impact by 5–10%; converters should qualify impact after color let-down.

    Regulatory Conformance Requires End-Use Temperature and Food Simulant Verification

    Food-contact compliance claims for Moplen EP549U depend on the final article’s end-use temperature and food simulant. Under EU No 10/2011, overall migration must not exceed 10 mg/dm² in the applicable simulant; for aqueous, acidic, and alcoholic foods at temperatures up to 70°C, the grade may be specified after converter migration testing. FDA 21 CFR 177.1520 covers olefin polymers used in contact with food, subject to conditions of use and end-testing. REACH and RoHS obligations are addressed in the safety data sheet; no SVHC above 0.1% w/w is declared for the current formulation. The grade is not intended for implantable medical devices, pharmaceutical packaging requiring USP Class VI, or continuous use with chlorinated water above 60°C unless oxidative stabilizer performance is validated for the specific application.

    Regulation/StandardTest/ClauseBoundary condition
    EU No 10/2011Overall migration10 mg/dm²; simulant-specific
    FDA 21 CFR 177.1520Olefin polymerConditions of use A–H
    REACH (EC) 1907/2006SVHC declarationNo SVHC above 0.1% w/w
    RoHS 2011/65/EUPb, Cd, Hg, Cr(VI), PBB, PBDEBelow directive thresholds

    Post-industrial regrind from Moplen EP549U can be reintroduced at up to 20 wt% in non-food-contact applications without re-stabilization, provided the regrind is dried to 0.1 wt% moisture and is free of contamination. For food-contact articles, regrind content is governed by food-contact legislation and the end-use condition. The natural grade is not UV-stabilized; exterior applications require a UV stabilizer masterbatch with an oxidative stabilizer package validated by accelerated weathering per ISO 4892-2:2013. The material is incompatible with strong oxidizing acids, aromatic hydrocarbons, and chlorinated hydrocarbons at elevated temperatures; swelling and stress cracking may occur. Continuous service in chlorinated water above 60°C is not recommended unless validated. Published data for this specific configuration is limited.

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