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MOPLEN PP EP332L

    • Product Name: MOPLEN PP EP332L
    • 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 576299
    Material Polypropylene impact copolymer
    Brand MOPLEN
    Product PP EP332L
    Melt Flow Rate 230 C 2 16 Kg 6 g/10 min
    Density 0.9 g/cm³
    Tensile Stress At Yield 23 MPa
    Tensile Strain At Yield 9%
    Flexural Modulus 1100 MPa
    Charpy Notched Impact Strength 23 C 5 kJ/m²
    Charpy Notched Impact Strength 20 C 2.5 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 85°C
    Vicat Softening Temperature A50 150°C

    As an accredited MOPLEN PP EP332L factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing MOPLEN PP EP332L is a polypropylene copolymer resin. Packaging: 25 kg multilayer paper bags with polyethylene liner for moisture protection.
    Container Loading (20′ FCL) 20′ FCL container loading of MOPLEN PP EP332L polypropylene granules, packed in 25kg bags, palletized and secured for safe transport.
    Shipping MOPLEN PP EP332L (polypropylene impact copolymer) is shipped as non-hazardous plastic pellets in clean, dry containers. Keep away from moisture, excessive heat, and direct sunlight. No UN number required for general transport; standard handling prevents contamination and preserves material purity.
    Storage Store Moplen PP EP332L in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep in its original, unopened packaging to prevent moisture absorption and contamination. Avoid exposure to strong oxidizers. Maintain moderate temperatures and protect from prolonged UV radiation. Under proper storage conditions, product remains stable and retains its material properties for the expected shelf life.
    Shelf Life Shelf life of MOPLEN PP EP332L is typically 2 years from delivery when stored in original packaging under dry, cool conditions.
    Application of MOPLEN PP EP332L

    Shot-to-shot consistency in lower instrument panel carriers depends on holding pressure decay across the sprue and runner system. MOPLEN EP332L is a heterophasic polypropylene impact copolymer with a nominal melt flow rate of 7 g/10 min measured under ISO 1133-1:2022 at 230 °C and 2.16 kg. In automotive interior trim, the resin provides a balance between rigidity and low-temperature impact after moulding. The injection window for a 2.2–2.8 mm nominal wall lower trim panel starts at melt temperatures of 230–250 °C; maintaining mould temperature between 40 °C and 50 °C prevents an overly thick oriented skin. If the cavity surface falls below 40 °C, the frozen layer grows and the notched Charpy impact measured under ISO 179-1/1eA at 23 °C can drop by 15–20% relative to a 50 °C moulded reference. This cliff-edge is process-related and cannot be corrected by extending hold time alone. Tooling should therefore specify conformal cooling or higher water set points rather than increasing packing pressure. Hold pressure is typically set at 60–80% of the peak injection pressure, with screw back pressure between 0.5 MPa and 1.5 MPa to stabilize dosage. Residual stress can be checked by dimensional stability after 48 h at 23 °C and 50% RH following ISO 291. For interior trim, volatile organic compound emissions are measured using VDA 278; many OEM specifications require total VOC below 100 µg/g and fogging condensate below 2 mg under VDA 270 method B. Finished components include lower instrument panel retainers, door pocket shells, and seat side shields, where grained surfaces mask flow marks.

    What Limits the Use of EP332L in Thin-Wall Food Containers Below 0.8 mm?

    A melt flow rate of 7 g/10 min is not a high-flow thin-wall grade. At wall thicknesses below 0.8 mm, the flow-length ratio in a cold runner mould may not exceed 150:1 without elevated melt temperature and high injection velocity; at 2.0 mm wall, the flow-length ratio can approach 220:1 depending on gate geometry. Melt temperature should be pushed to the upper boundary of 240–250 °C, but residence time must remain below 4 min to limit yellowing and molecular weight degradation. Injection velocity is typically set between 200 mm/s and 500 mm/s, with holding pressure applied until gate freeze. The heterophasic structure gives higher haze than a clarified random PP; therefore EP332L is more appropriate for opaque reusable food storage containers, lunch box bases, and freezer-safe lids than for transparent delicatessen packaging. In food-contact applications, the base resin must comply with FDA 21 CFR 177.1520 for olefin polymers and, in the EU, Regulation (EU) No 10/2011 with overall migration below 10 mg/dm² under the prescribed simulant conditions. Reusable containers also require dishwasher resistance; warpage after 100 cycles in a residential dishwasher at 65–75 °C is evaluated by dimensional change under ISO 294-4. Moulders should not add post-industrial regrind above 20 wt% without repeating migration and impact testing, since recycled content can alter the extractable profile. The process conflict is that higher melt temperature improves thin-wall filling but increases oxidation risk; the exact set point must be validated by melt flow retention after moulding, with a target MFR shift of less than 10% from virgin pellet. Products include stackable freezer containers, insulated lunch box shells, and opaque microwave reheating containers.

    Washing machine base frames and dishwasher door inner panels subject PP impact copolymers to intermittent hot water contact, detergent exposure, and long-term creep under load. The base resin should be processed in a mould with clamp force calculated at 4–6 kN/cm² of projected area; for a 600 mm × 500 mm base frame, this corresponds to a press clamp force of 12,000–18,000 kN. Melt temperature is kept at 230–240 °C, and holding pressure is set to 30–40 MPa hydraulic for a 2.5 mm nominal wall. The key failure mode is not melt fracture but stress whitening at screw bosses and snap-fit reliefs. Boss outside diameter should be 2.0–2.5 times the screw nominal diameter, and wall thickness around the boss should not exceed 60% of the nominal wall to prevent sink and internal voids. Long-term electrical safety in household appliances is assessed under IEC 60335-1; the material must resist surface tracking and not deform at the 75 °C abnormal operation test. A relative thermal index for unfilled PP impact copolymers is typically in the 100–115 °C range under UL 746B; for EP332L the supplier CoA or UL yellow card should be consulted before using the part above 100 °C continuous service. If the moulder adds 1–2 wt% carbon black masterbatch for appearance, the effect on notched impact is generally small but can reduce weld-line strength at the gate area; weld-line tensile strength should be measured under ISO 527-2 at a line gate, with a minimum retention of 70% relative to the solid section. Finished parts include dishwasher door inner covers, washing machine base frames, and front-load washer pump brackets.

    Application segmentStandard / regulationTest conditionCommon acceptance lineMOPLEN EP332L status
    Automotive interior trimFMVSS 302 / ISO 3795Horizontal burn, 100 mm gauge lengthBurn rate ≤ 100 mm/minRequires lot-specific test; PP-HB expected
    Food-contact containersFDA 21 CFR 177.1520Monomer and extractables limits for olefin polymersComplies if base resin and additives are listedBase resin suitability subject to supplier CoA
    EU food-contact articlesRegulation (EU) No 10/2011Overall migration in food simulants≤ 10 mg/dm²Must be tested on final article
    Household appliancesIEC 60335-1Abnormal heat, tracking, mechanical enclosureNo ignition, no exposed live partsDesign-dependent; UL 746B RTI to be checked
    UN pailsUN Model Regulations / ADRStack load and drop test at -18 °CNo leakage after dropFinal article certification required
    Battery componentsUL 94Vertical burn at 1.5 mm if enclosureV-0 for high-voltage enclosure partsUnfilled EP332L typically HB only; not suitable unless independently rated

    When a 7 g/10 min Impact Copolymer Is Used for Industrial Pails and Returnable Crates

    A UN-rated pail moulded from EP332L must survive drop testing and stack loading without brittle failure. The grade is suitable for 20 L to 30 L open-head pails with wall thickness of 1.8–2.4 mm and base corner radius of 5–8 mm. The pail should be moulded with a central sprue or diaphragm gate; multi-gating on a pail side wall creates weld lines that reduce drop impact at -18 °C, a condition verified under ISO 6603-2 or a 1 m drop test at -18 °C for UN packaging. Stacking load is calculated by the top-rim hoop stress, not just wall compression; an I-section rim with ribs at 6–8 mm pitch increases top-load resistance. For returnable crates, the material allows a thinner grid base than homopolymer PP because the heterophasic phase absorbs impact energy during rough handling. Gate design for crates should place edge gates at 2–3 mm thickness, not below 1.8 mm, to avoid excessive shear heating. The melt temperature range of 225–250 °C is broader here because wall thickness is moderate; screw speed should be limited to 80–120 min⁻¹ to prevent shear-induced degradation of the rubber phase. Products include 25 L stackable pails, vegetable crates, and folding box pallets. Water contact and food use are not automatic; only lot-specific compliance with EU 10/2011 or FDA 21 CFR 177.1520 allows pails for raw food transportation.

    Low-voltage battery carrier and busbar insulation components in electric vehicle modules are often specified in mineral-filled flame-retardant PP. EP332L is an unfilled heterophasic grade without a halogenated flame-retardant system, so it should not be used for high-voltage module enclosures requiring UL 94 V-0 at 1.5 mm unless independent testing confirms a V-0 rating. The application space is therefore limited to non-flame-facing parts such as low-voltage cable clips, thermal management line brackets, and protective edge strips. These components still require pre-drying when the resin has been exposed to ambient relative humidity above 60%; a dehumidifying hopper dryer at 80 °C for 2–4 h prevents surface splay on textured surfaces. The recommended melt temperature is 220–240 °C, and the mould temperature can be lowered to 20–30 °C because the parts are small and impact loading is minimal. For cable clips, the snap arm should be designed with a deflection of less than 3 mm, because the flexural modulus of an unfilled impact copolymer is lower than that of a talc-filled PP; the mating geometry must avoid permanent deformation during insertion. Short-term heat resistance is adequate up to 90 °C, but creep at 105 °C is a known boundary for continuous load. Products include battery management system wire retainers, cooling line brackets, and module edge protectors.

    Garden Furniture, UV Aging, and the Case Against Unfilled Heterophasic PP

    Outdoor furniture shells made from EP332L require an additional UV stabilizer concentrate if the part is exposed to more than 500 h of accelerated weathering under ASTM G154 Cycle 1. Without 0.2–0.5 wt% hindered amine light stabilizer masterbatch or 2–3 wt% carbon black, surface chalking begins within 12–24 months in high-UV exposure, and flexural modulus retention under ISO 178 can fall below 70% after 2,000 h in xenon-arc testing. The injection moulding process for garden chair shells uses a 2.5–3.5 mm wall and a large fan gate; melt temperature is kept at 230–250 °C to minimize internal stress. The main failure is not UV alone but the combination of frozen-in stress and UV-induced chain scission at the gate area, leading to cracking after outdoor summer-winter cycling. Gate area radius should be at least 10 mm, and secondary ribs should not intersect at acute angles. If a fire-retardant garden furniture specification requires EN 1021-1 or EN 1021-2, unfilled EP332L is generally not suitable without a flame-retardant masterbatch; adding such a masterbatch lowers impact and complicates weathering performance. Products include stackable garden chairs, table leg covers, and park bench slats where a black or dark color hides weathering defects. Published data for this specific outdoor configuration in EP332L is limited, so the selection should be validated by a 12-month Florida or Arizona exposure trial before series production.

    Large-diameter over-caps for non-carbonated products are a narrow but viable downstream segment. The melt flow rate of 7 g/10 min is far below the 25–35 g/10 min grades used in high-cavity beverage closure moulds, so cavitation must be reduced and cycle time extended by 10–20% relative to a high-flow random copolymer. A two-plate cold runner with edge gates at 1.5–2.0 mm is used; melt temperature is 230–250 °C, and mould temperature is 20–30 °C. The tamper-evident band hinge is the primary failure location, because the heterophasic rubber phase reduces hinge fatigue resistance compared with homopolymer closures; the hinge should be designed with a thickness of 0.35–0.45 mm and no sharp gate vestige. Sealing liners for food applications must comply with FDA 21 CFR 177.1520 and EU 10/2011; the closure itself must be tested for overall migration if it is in direct contact with food, not just the liner. Products include large peanut butter jar over-caps, cosmetic jar lids, and detergent over-caps where the lower melt flow rate helps control flash on wide-diameter threads.

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    Certification & Compliance
    More Introduction

    MOPLEN PP EP332L, produced by LyondellBasell, is a heterophasic polypropylene impact copolymer supplied in pellet form for injection moulding. The grade consists of a continuous semi-crystalline polypropylene matrix and a dispersed ethylene-propylene rubber phase. This reactor-generated morphology changes the mechanical response of the moulded part relative to a polypropylene homopolymer: stiffness is reduced, but resistance to crack initiation at 0°C and −20°C is substantially higher. Typical conversion equipment includes reciprocating-screw injection moulding machines with three-zone screws having L/D ratios of 20:1 to 24:1 and compression ratios of 2.0:1 to 2.8:1. The melt mass-flow rate is controlled to a medium-flow band, with typical values near 8 g/10 min measured under ISO 1133-1:2022 at 230°C and 2.16 kg. Density is controlled near 0.900 g/cm³ when tested by ISO 1183-1:2019.

    What rheological profile governs filling behaviour in thin-wall tools?

    The melt exhibits shear-thinning behaviour across the shear-rate range encountered in injection moulding. Capillary rheometry at 230°C with apparent shear rates from 100 s-1 to 10,000 s-1 is required for reliable mould-filling simulation; the melt mass-flow rate alone is a single point and does not describe pressure drop in a thin-wall tool. A Bagley correction and Rabinowitsch correction are applied to convert apparent viscosity to true shear viscosity. Pressure-dependent viscosity data should be generated up to 50 MPa because polypropylene viscosity rises with hydrostatic pressure; without pressure dependence, simulation can under-predict injection pressure in long flow lengths.

    On a production injection moulding machine, the nozzle melt temperature should be maintained between 220°C and 250°C. Rear-zone barrel settings are normally 20°C to 30°C lower than the nozzle to stabilise pellet feed and prevent bridging. Mould surface temperature should be held between 20°C and 50°C. Lower mould temperatures reduce cycle time but freeze the skin rapidly and can increase sink-mark visibility and frozen-in orientation. Pre-drying is not required for moisture control under normal indoor storage below 60 % relative humidity. If pellets are stored below 10°C and transferred into a warmer moulding shop, condensation may form; a hot-air hopper dryer at 80°C for 2 h is recommended. Back pressure between 2 bar and 8 bar hydraulic improves melt homogeneity but excessive back pressure raises melt temperature and can degrade the rubber phase. Screw rotation should produce a plasticating time slightly longer than the cooling time; cushion control should maintain 3 mm to 6 mm of molten material ahead of the screw tip.

    For moulding machines, clamp force should be selected from projected part area and cavity pressure. A cavity pressure of 30 MPa to 50 MPa at the end of filling is typical for polypropylene impact copolymers; required clamp force is calculated by multiplying cavity pressure by projected area. Machines with clamp force between 1,500 kN and 4,000 kN are common for multi-cavity tools producing articles of 100 cm² to 500 cm² projected area. Insufficient clamp force causes flash, especially at melt temperatures near the upper limit of 250°C.

    Low-temperature impact response and crystallisation rate in heterophasic PP

    The ethylene-propylene rubber phase has a glass transition below −50°C, whereas the amorphous fraction of the polypropylene matrix has a glass transition near 0°C. Impact resistance at −20°C therefore depends on the rubber domain size, the interparticle distance, and the thickness of the brittle matrix ligaments between rubber domains. In reactor-grade impact copolymers such as MOPLEN PP EP332L, the rubber phase is generated during polymerisation and is typically finer and more uniform than post-reactor melt compounding of homopolymer with an external elastomer. However, the moulder cannot independently vary rubber content after polymerisation.

    Thermal history during injection moulding alters the ductile-to-brittle transition. High back pressure and long residence times can coalesce rubber domains and reduce the number of effective stress concentrators, lowering notched impact strength. Insufficient mixing leaves rubber agglomerates that behave as macroscopic defects. The processing window is therefore not defined solely by barrel temperature; screw speed, back pressure, and residence time are equally critical.

    Charpy notched impact specimens should be prepared according to ISO 179-1:2010. For sub-zero testing, specimens are conditioned in a liquid bath for 30 min and tested within 5 s of removal to limit thermal drift. Standard plaque tests do not fully represent production parts because cooling rate and mould temperature can shift the ductile-to-brittle transition by 5°C to 10°C.

    If the moulding line uses cold-runner tools with restricted gate dimensions

    Gate geometry directly influences impact retention. For wall thicknesses of 2 mm to 3 mm, edge gates with land lengths of 0.5 mm to 1.0 mm and gate diameters of 0.8 mm to 1.5 mm are typical. Pinpoint gates below 0.5 mm produce high shear rates; local shear heating can degrade the rubber phase and generate delamination or reduced notched impact strength at the gate. If a restricted gate is unavoidable, filling speed should be reduced and holding pressure increased to promote gate seal. Hot-runner valve gates should be sized at least 1.2 mm for balanced filling.

    Holding pressure is typically 60 % to 80 % of peak injection pressure. Holding time must exceed the gate freeze time, which is determined by plotting part weight against increasing holding time until the weight plateau. Premature release of holding pressure causes sink marks and microvoids, particularly above ribs and bosses. For a 2 mm-wall part with a flow length of 200 mm, injection pressure at the nozzle commonly falls between 60 MPa and 90 MPa; peak hydraulic pressure should remain within the machine manufacturer’s rated clamp.

    In multi-cavity tools, melt filling imbalance produces density variation and warpage. Runner balancing should be verified with short-shot studies at 90 % of full fill rather than by cavity weight alone. For hot-runner systems, nozzle tip temperatures should not exceed 250°C to avoid rubber-phase degradation at dead spots.

    Cooling circuit design controls warpage in impact copolymer parts. Mould temperature differences across the part should be kept below 10°C. When wall thickness changes from 1 mm to 4 mm in the same part, the thin section freezes first and transfers residual stress to the thick section; a mould temperature near 40°C and a post-moulding jig may be required for dimensional stability. Dimensional checks should be performed after 24 h conditioning at 23°C because post-ejection crystallisation and moisture equilibration shift dimensions. Mould shrinkage for this class of impact copolymer is typically 1.2 % to 1.6 % in the flow direction; transverse shrinkage may be slightly higher.

    Weld-line strength is governed by molecular interdiffusion across the flow-front interface. At melt temperatures within the recommended range, weld-line tensile strength retention of 60 % to 80 % relative to non-weld-line specimens is typical. Weld-line impact retention falls sharply when melt temperature drops below 220°C. Vents should be placed at the end of fill and at weld-line intersections to prevent gas entrapment.

    Colour concentrates based on low-MFR polypropylene carriers are preferred. Masterbatch addition levels should not exceed 4 wt% unless mould-filling and shrinkage behaviour are verified. Titanium dioxide-based white masterbatch at 2 wt% can raise flexural modulus slightly while reducing elongation; carbon black at 1 wt% does not provide full weathering stability and should be combined with hindered amine light stabilisers for outdoor use.

    Relative to a polypropylene homopolymer with the same melt mass-flow rate, MOPLEN PP EP332L has lower tensile modulus, lower yield stress, and substantially higher resistance to crack propagation at 0°C and −20°C. Compared with a random copolymer used for clarity, EP332L is translucent to opaque and offers higher low-temperature impact strength. Compared with high-flow impact copolymers used for thin-wall packaging, EP332L has lower MFR and is less suitable for wall sections below 0.8 mm but more suitable for thick-wall industrial parts with slow cooling. Substitution decisions should be confirmed on production tooling and not based solely on standard specimen results; published data for this specific configuration is limited.

    When switching from other polymers on the same line, the barrel should be purged with a dedicated polypropylene purge compound before moulding MOPLEN PP EP332L. Residual polyamide or polyester forms immiscible inclusions that reduce impact performance. Regrind from the same grade may be used at addition levels up to 20 wt% when the regrind is dry and free of oil; higher fractions shift the melt mass-flow rate and reduce low-temperature impact because of repeated thermal history.

    Chemical resistance is typical of olefin polymers. The grade resists polar solvents, dilute acids, and aqueous salt solutions at temperatures up to 60°C; it is not recommended for continuous contact with oxidising acids, aromatic hydrocarbons, or chlorinated solvents. Environmental stress-cracking resistance should be evaluated by exposure to the actual service fluid under load, using a fixed strain jig and notched specimens according to ISO 22088-3. Outdoor weathering without stabilisation is not recommended; long-term UV exposure causes chain scission and surface cracking.

    For food-contact applications, polypropylene is evaluated under FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011. Migration limits depend on the final article formulation, including pigments and processing aids. Under EC No 1907/2006 (REACH), substances of very high concern are not expected above 0.1 % w/w. Under Directive 2011/65/EU (RoHS), restricted substances in the polymer matrix are below thresholds when no restricted pigments or additives are introduced.

    Regulatory domainStandard or regulationAssessment basis
    Food contact polypropyleneFDA 21 CFR 177.1520Olefin polymer specification; end-use conditions apply
    EU food contact plasticsRegulation (EU) No 10/2011Overall migration and SML depend on final compound
    REACH SVHCEC No 1907/2006No SVHC above 0.1 % w/w declared
    RoHS restricted substancesDirective 2011/65/EUMatrix below thresholds; additives to be verified
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