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MOPLEN PP EP548Q

    • Product Name: MOPLEN PP EP548Q
    • 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 629750
    Product MOPLEN PP EP548Q
    Polymer Type Impact Copolymer Polypropylene
    Melt Flow Rate 230 C 2 16 Kg 38 g/10 min
    Density 0.91 g/cm³
    Tensile Stress At Yield 23 MPa
    Tensile Strain At Yield 5%
    Tensile Strain At Break >50%
    Flexural Modulus 1300 MPa
    Charpy Notched Impact Strength At 23 C 5 kJ/m²
    Charpy Notched Impact Strength At 20 C 2.5 kJ/m²
    Heat Deflection Temperature At 1 8 Mpa 53°C
    Vicat Softening Temperature 65°C
    Melt Processing Temperature Range 200-250°C

    As an accredited MOPLEN PP EP548Q factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing MOPLEN PP EP548Q polypropylene is packaged in 25 kg woven polypropylene bags with polyethylene liner for protection.
    Container Loading (20′ FCL) 20′ FCL loading of MOPLEN PP EP548Q polypropylene; bagged on pallets, shrink-wrapped, secured for safe, efficient transport.
    Shipping MOPLEN PP EP548Q ships as a non-hazardous polypropylene copolymer in sealed bags or bulk containers. Protect from moisture, direct sunlight, and excessive heat during transit. Store in a dry, ventilated area, away from ignition sources. Handle with care to prevent bag damage and product contamination.
    Storage Store MOPLEN PP EP548Q in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep containers tightly sealed when not in use to prevent contamination and moisture pickup. Avoid creating dust clouds, as polymer dust may form explosive mixtures. Separate from strong oxidizing agents. Maintain good housekeeping to minimize spillage and static buildup. No special temperature controls required if storage conditions remain stable.
    Shelf Life Shelf life is 2 years from production date when stored in original packaging, away from heat, moisture, and direct sunlight.
    Application of MOPLEN PP EP548Q

    Automotive door module carrier production with MOPLEN PP EP548Q starts from a reactor-made heterophasic ethylene-propylene copolymer metered into a single-screw injection moulding machine with a general-purpose screw L/D ratio of 20:1 to 24:1 and a compression ratio of 2.1:1 to 2.3:1. The barrel temperature profile is set from feed throat to nozzle at 210 °C, 220 °C, 230 °C, 235 °C, and 240 °C, while the melt temperature measured by an immersion pyrometer is maintained at 230 °C to 245 °C. For a nominal wall stock of 2.5 mm, the mould surface temperature is held between 30 °C and 40 °C. The injection velocity is configured so that cavity fill time remains between 0.8 s and 1.4 s; fill times below 0.6 s produce local shear rates above 10,000 s-1 at the gate and can exceed the critical shear stress of the ethylene-propylene dispersed phase, producing flow-front delamination and visible gate blush. A sequential valve-gate programme is used on carrier tools with a flow length exceeding 400 mm, because simultaneous filling of all gates creates weld lines at rib intersections. Weld-line tensile properties are measured on injection-moulded plaques according to ISO 527-2, and the strength retention of a weld line relative to the un-welded reference is typically 0.55 to 0.70 for impact-copolymer PP at 2.5 mm wall thickness. Rib cross-sections are designed no thicker than 0.6 times the adjoining wall to avoid sink marks and cold-slug formation, and the holding pressure is set to 60 % of peak injection pressure with a final cushion of 4 mm to 6 mm to prevent screw bottoming. Mould release is restricted to silicone-free formulations for interior parts. Conditioning after demoulding is performed at 23 °C and 50 % relative humidity for 40 h according to ISO 291, and part dimensions are checked against the cavity tolerance of ±0.10 mm on snap-fit features. Emissions compliance for the finished interior component is verified by VDA 277 for total volatile organic compounds, VDA 278 for fogging volatiles and semi-volatile compounds, and DIN 75201-B for windscreen fogging reflectance. A drying step of 2 h at 80 °C is applied only when sacks or silo storage have exceeded relative humidity of 65 % for more than 72 h, because water uptake in polypropylene is generally below 0.03 % but condensation on cold granules can produce surface splay on flat interior panels. The final door module carrier is assembled by vibration welding of the PP door panel substrate to the injection-moulded carrier using a weld amplitude of 1.0 mm to 1.5 mm at 200 Hz to 240 Hz on multi-head vibration welders.

    When Melt Temperature Falls Below 220 °C in Thin-Wall EV Battery Bracket Moulding

    Thin-wall battery pack brackets for electric vehicle modules are moulded at a nominal wall thickness of 1.8 mm to 2.0 mm, and the melt temperature must remain above 220 °C to prevent the ethylene-propylene dispersed phase from creating visible flow hesitation at the end of fill. A tool with 16 to 24 cavities for cell module side plates is supplied by a hot runner manifold held at 240 °C to 250 °C; valve gates are preferred over thermal gates because the gate vestige must not exceed 0.3 mm in height to avoid interference with cell compression pads. The injection unit is operated with a melt cushion of 3 mm to 5 mm and a decompression distance of 4 mm to 6 mm after plastication, which reduces drool at the valve gate during mould open. Fill time is kept at 0.5 s to 1.0 s, and injection pressure is allowed to rise to 90 MPa to 110 MPa; if the machine cannot reach 90 MPa without exceeding a screw speed of 120 min-1, the recommended correction is to raise the melt temperature in 5 °C increments rather than to reduce pack pressure. Regrind usage is limited to 15 wt% for brackets requiring low-temperature impact and dimensional stability, because repeated heat history reduces the elastomeric phase concentration. The final bracket is not in direct contact with busbars or current-carrying components, because EP548Q is a non-flame-retardant impact copolymer and is limited to UL 94 HB classifications; any design requiring V-0, V-1, or 5VA must use a different compound or an intumescent coating. Dimensional checks are performed after conditioning at 23 °C and 50 % relative humidity for 40 h per ISO 291; the width across snap-fit features is measured with a contact gauge to an acceptance of ±0.10 mm. Warpage in long brackets is reduced by running the fixed and moving mould halves at a controlled temperature difference of 5 °C to 10 °C, with the fixed half warmer. Published data for this specific configuration is limited; weld-line strength for 1.8 mm EV bracket geometries should be validated by cutting ISO 527-2 type 1BA specimens perpendicular to the weld line and comparing break stress with an un-welded reference. The bracket is subsequently assembled by heat-staking the PP boss at 170 °C to 190 °C with a dwell of 6 s to 10 s and a stake force of 200 N to 400 N per boss, followed by a 2 h post-assembly dimensional stabilisation at 80 °C.

    Processing parameterThin-wall EV bracket windowLarge-format tub/crate window
    Melt temperature230 °C250 °C220 °C240 °C
    Mould surface temperature20 °C40 °C20 °C35 °C
    Injection pressure90 MPa110 MPa70 MPa100 MPa
    Holding pressure60 %70 % of peak50 %65 % of peak
    Back pressure2 MPa6 MPa4 MPa6 MPa for talc-filled
    Melt cushion3 mm5 mm4 mm6 mm
    Regrind ratio15 wt%20 wt%; ≤10 wt% at -20 °C service

    Does Washing Machine Outer Tub Material Resist Alkaline Detergent Stress Cracking at 95 °C?

    Detergent stress cracking in PP washing machine outer tubs is evaluated by bending injection-moulded strips to a fixed strain of 1.0 % and exposing them to a 1 % by mass aqueous solution of a phosphate-containing laundry detergent at 80 °C to 95 °C for 200 h in accordance with the bent-strip method of ISO 22088-3. EP548Q in a 20 wt% talc-filled formulation shows a processing window that is narrower than that of the unfilled base resin: melt temperature must be kept between 235 °C and 250 °C because temperatures above 255 °C accelerate chain scission in the presence of mineral filler, while temperatures below 230 °C cause poor filler wet-out and lower weld-line strength. The screw is a low-shear barrier design with an L/D of 22:1 and a compression ratio of 2.5:1, and the back pressure is held at 4 MPa to 6 MPa to wet out the talc without generating excessive shear heating. An accumulator-assisted injection unit is used on outer tub tools with a shot weight of 4 kg to 7 kg; the fill stage is completed in 2.0 s to 3.5 s, followed by a pack stage of 50 MPa to 70 MPa for 8 s to 15 s. The mould temperature is set to 35 °C at the cavity and 20 °C to 25 °C in the core, which produces a frozen skin that limits detergent migration into the part while allowing sufficient crystallinity for creep resistance at 95 °C. If the tub is exposed to pH above 10.5 for prolonged periods, the outer surface is protected by a 0.3 mm to 0.5 mm co-polypropylene liner or a chemical-resistant coating, because EP548Q alone is not recommended for continuous immersion in strong alkaline solutions above 60 °C. The finished tub is tested after 1,000 h of thermal cycling between 25 °C and 95 °C; the acceptance criterion is no visible crack under magnification and no leakage under the appliance manufacturer’s specified internal pressure. Dimensional stability after demoulding is monitored by a 24 h post-moulding shrinkage check at 23 °C following ISO 294-4, with the talc-filled compound showing lower and more anisotropic shrinkage than the unfilled base resin.

    Unlike automotive interior components, logistics container tools impose a different balance of cycle time, stacking resistance, and low-temperature impact at -20 °C. For collapsible crates and industrial tote boxes with a wall thickness range of 2.0 mm to 4.0 mm, EP548Q is processed on a large injection press with a melting capacity matched to a shot weight of 1.5 kg to 5.0 kg; the melt temperature is set to 220 °C to 240 °C, and the mould temperature is controlled at 20 °C to 30 °C to reduce cooling time. The injection profile is divided into three stages: an initial high-velocity phase to fill the long side walls, a controlled deceleration across the middle 60 % of the stroke to prevent jetting, and a final low-velocity phase at 15 % to 25 % of the peak speed to pack the corner bosses. Up to 20 wt% regrind is allowed for non-food and non-pharmaceutical crates, but the maximum regrind level is reduced to 10 wt% when the crate is used for refrigerated storage at -20 °C because repeated grinding reduces the impact-modified phase concentration. Drop impact performance is measured at -20 °C using a falling dart impact test according to ISO 6603-2; the ductile-to-brittle transition behaviour is evaluated through a series of 10 drops from 2.0 m onto a concrete floor, and the acceptance is no crack longer than 10 mm. Stacking compression is measured at 40 °C for 72 h under a load of 250 kg per crate for the bottom position; creep deflection is recorded after 15 min, 1 h, 24 h, and 72 h to ensure that lid engagement features remain functional at 2.0 mm to 3.0 mm deflection. Flexural creep data for long-term stacking performance is generated according to ISO 899-2, and the creep modulus is compared between 23 °C and 40 °C to define the safe stacking height. The final article is identified by hot-foil marking or in-mould labelling on the side wall, and the label area is kept free of release agents to avoid adhesion failure. Gate locations are positioned away from bottom corners because freezer impact cracks initiate at gate vestiges when a crate is dropped onto its edge at -20 °C.

    Under-Hood Fan Shroud Ageing and the 120 °C Oven Exposure Limit

    Accelerated oven ageing of EP548Q fan shroud specimens is performed at 120 °C for 1,000 h in a forced-air oven per ISO 188, with tensile elongation at break determined by ISO 527-2 type 1A specimens withdrawn at 250 h, 500 h, and 1,000 h. For heterophasic PP exposed to 120 °C, the practical failure boundary is usually identified when tensile elongation at break falls below 25 % of the unaged value, because further oxidation causes brittle fracture during vibration loading on the vehicle radiator frame. The grade is heat-stabilised by the resin supplier, but under-hood parts with service temperatures above 100 °C require additional melt compounding with 0.3 wt% to 0.6 wt% of a hindered phenolic antioxidant masterbatch and 0.2 wt% to 0.4 wt% of a phosphite process stabiliser; the combination is dispersed at a melt temperature of 230 °C to 245 °C and a screw speed of 80 min-1 to 100 min-1. Fan shroud tools typically include a hot runner with three to six valve gates around the circular bowl, and the gate openings are sized to deliver a shear rate below 40,000 s-1 at the gate land. The packing pressure is ramped from 50 MPa to 70 MPa over 2 s, then held for 10 s to 15 s to compensate for differential shrinkage in the reinforced mounting bosses. The final shroud is assembled with a clearance of 2 mm to 5 mm between the PP part and the radiator end tank, and the mounting bosses are allowed to absorb thermal expansion by using steel shoulder bushings with a hole clearance of 0.5 mm. UL 746B relative thermal index data for unreinforced PP impact copolymers is commonly in the 65 °C to 90 °C range; continuous exposure at 120 °C is therefore outside the generic long-term RTI envelope, and the part must be validated for the specific under-hood profile using engine-cover duty cycles. Vibration durability is screened on a shaker table using the ISO 16750-3 broad-band random vibration profile for engine-mounted components, with crack initiation inspected at rib roots and gate vestiges after each test block. If the fan shroud shows whitening at the gate after ageing, the gate diameter is increased stepwise from 1.2 mm to 1.8 mm to reduce gate-region stress concentration while maintaining acceptable freeze time.

    Crash-Relevant Instrument Panel Inserts and Rib-Fill Pressure Mapping

    In crash-relevant instrument panel work, EP548Q is qualified through a combined evaluation of low-temperature notched impact, airbag deployment crack behaviour, and rib-fill pressure mapping. The material is injection moulded at a wall thickness of 2.0 mm to 2.5 mm with ribs no thicker than 0.5 times the nominal wall; the melt temperature is set at 235 °C to 250 °C, and the mould temperature is held at 30 °C to 40 °C to improve surface replication without raising cycle time above 45 s. Piezoelectric cavity pressure sensors are placed in the last fill zone and near the airbag door hinge; if the sensor in the hinge reaches 30 MPa to 40 MPa before the end of fill, the gate freeze-off is considered insufficient and the holding pressure profile is extended by 2 s to 3 s. Notched Charpy impact at -30 °C is measured per ISO 179-1/1eA, and the value is compared with the 23 °C result to calculate the low-temperature retention factor; designs in the knee bolster region are typically accepted only when the -30 °C Charpy value remains above 4 kJ/m², but the exact lower limit is established by the vehicle manufacturer’s crash load case. The airbag deployment door is produced by laser scoring the PP substrate to a residual thickness of 0.4 mm to 0.6 mm; the scoring parameters are adjusted so that the material tears without producing loose fragments. Instrument panel components in the European market are validated against ECE R21 for interior projections, and for North American programmes against FMVSS 201 occupant protection requirements. Dimensional checks after moulding are conducted at 23 °C and 50 % relative humidity per ISO 291, with the critical hinge thickness measured by ultrasonic wall-thickness gauge to an accuracy of ±0.02 mm. A 2 wt% UV-stabilised black masterbatch is added when the insert is visible in the upper instrument panel area, and the concentrate is metered at the hopper with a gravimetric feeder to avoid colour variation that would affect laser scoring energy absorption. If the airbag deployment door shows angular fragments during cold deployment at -30 °C, the processing response is to increase melt temperature within the 245 °C to 250 °C window and to reduce packing pressure by 5 MPa steps, because overpacked PP hinges lose ductility in the scored ligament.

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    Certification & Compliance
    More Introduction

    MOPLEN PP EP548Q is a heterophasic polypropylene impact copolymer supplied in pellet form for high-speed injection moulding of thin-wall and technical articles. Two release-sheet values define its processing classification: the melt mass-flow rate is 100 g/10 min when determined at 230 °C under a 2.16 kg load in accordance with ISO 1133-1:2022, and the density is 0.900 g/cm³ when measured by ISO 1183-1:2019. The heterophasic morphology comprises a polypropylene homopolymer matrix and a discrete ethylene-propylene rubber phase. The Q suffix is used in manufacturer nomenclature for controlled-rheology grades; the exact rheology-modification route is not disclosed in the public datasheet. That phase architecture separates the product from random copolymers of equivalent comonomer content, which exhibit greater transparency but lower low-temperature ductility. The grade is opaque and is classified among impact copolymers rather than homopolymers.

    How Does the 100 g/10 min Melt Flow Rate Alter Injection-Moulding Processing Limits?

    The single-point MFR value in ISO 1133-1:2022 characterizes melt behaviour only at low shear rate. In production, gate and runner shear rates exceed 10,000 s⁻¹, so pressure drop is dominated by shear thinning. The 100 g/10 min value reduces injection pressure at equivalent melt temperature and wall thickness relative to a lower-flow impact copolymer, but it also shortens the packing window because the gate freezes earlier when mould steel is cold. Processing guides for high-flow heterophasic polypropylene specify melt temperatures of 220 °C to 250 °C and mould temperatures of 15 °C to 50 °C. Start-up trials on 1200 kN to 1800 kN clamping-force machines with 20:1 L/D general-purpose polyolefin screws should maintain a melt cushion of 3 mm to 6 mm and monitor screw recovery time against cooling time. Published data for this specific configuration is limited; therefore, capillary rheometry at 230 °C should replace single-point MFR for mold-filling simulation.

    The relationship between melt flow rate and clamp-force demand is not linear. Required clamping force is proportional to cavity projected area and cavity pressure at gate freeze. High-flow grades can reduce peak injection pressure, but moulders sometimes compensate by increasing injection speed to maintain fill time; the resulting pressure spike can erase the benefit. Injection-speed profiling should begin with a slow-to-fast profile that keeps the flow front at 100 mm/s to 300 mm/s at cavity walls. Published data for this specific configuration is limited; machine-specific printouts should be recorded from the first tool trials.

    Plastication on reciprocating-screw machines is rarely the limiting factor for this grade. The limiting factors are check-ring leakage and screw-recovery settings. When screw peripheral velocity exceeds 0.3 m/s, shear heating in the compression zone can produce nozzle melt-temperature overshoot. A nozzle setpoint of 240 °C ± 5 °C is a useful control window; wider variation indicates barrel-zone mismatch, check-ring wear, or feed-throat bridging. The material does not require the same moisture control as polyamide, but condensation on cold pellets transferred into a humid plant can generate surface splay. Where storage has occurred below 15 °C, a desiccant hopper dryer at 80 °C for 2 h is sufficient. Backpressure of 0.5 MPa to 1.5 MPa hydraulic, or its electric equivalent, is adequate for melt homogenisation; excessive backpressure raises melt temperature without improving dispersion in an unfilled impact copolymer.

    Mechanical Property Boundaries and Conditioning Requirements

    Both ASTM D4101-17 and ISO 19069-2:2016 provide classification frameworks for polypropylene injection and extrusion materials. Release-sheet mechanical values for heterophasic impact copolymers are not design constants; they are specimen-dependent. Tensile properties should be measured on specimens moulded and conditioned according to ISO 527-2:2012 at 23 °C ± 2 °C and 50 % ± 10 % relative humidity for at least 40 h before testing. Notched Charpy impact should be determined using ISO 179-1:2010 at 23 °C and 0 °C because the ethylene-propylene rubber phase has temperature-dependent failure behaviour. Flexural modulus is measured under ISO 178:2019. The manufacturer datasheet should be interpreted as a release range rather than an absolute design value. For load-bearing components, lot-specific tensile yield stress and elongation at yield must be obtained from the supplier.

    Continuous structural service above 60 °C requires creep-rupture verification because polypropylene exhibits pronounced creep at elevated temperatures. The impact-copolymer morphology improves toughness at ambient temperature but does not convert the material into an engineering polymer. Where dimensional stability under load is critical, glass-fibre-reinforced grades or alternate polymers should be evaluated.

    Mould shrinkage for unfilled heterophasic polypropylene injection moulding is anisotropic and gate-location-dependent. General industry references for heterophasic PP report mould shrinkage in the range of 1.0 % to 1.5 %; however, published data for this specific configuration is limited. Shrinkage must be determined on production-representative specimens according to ISO 294-4:2018. Gate proximity, flow direction, packing time, and cavity thickness create differential shrinkage that produces warpage in shallow rectangular containers. In thin-wall packaging, rib-to-wall ratios below 0.6:1 reduce sink marks but require adequate venting. Parting-line vents of 0.02 mm to 0.03 mm depth are typical for polypropylene; shallower vents trap gas and cause short shots, while deeper vents risk flash.

    When Thin-Wall Food-Contact Articles Require Reduced Cycle Time Without Random Copolymer Clarity

    Manufacturer application literature lists MOPLEN PP EP548Q for injection-moulded thin-wall packaging, housewares, caps, closures, and technical articles where an opaque impact copolymer is acceptable. The grade is not suitable for transparent food containers because the heterophasic morphology scatters light. For food-contact articles, compliance must be established on the finished moulding, not the raw pellet. EU Regulation (EU) No 10/2011 requires overall migration testing and specific migration testing where applicable. In the United States, the olefin polymers section 21 CFR 177.1520 may apply to unmodified polypropylene; however, pigments, nucleating agents, and processing aids must be individually cleared. The moulded article manufacturer is responsible for organoleptic evaluation because high-temperature hot-runner residence can generate taste and odour defects that are not present in the pellet.

    Standard or regulationDesignationRelevance to EP548QVerification requirement
    FDA 21 CFR 177.1520Olefin polymersFood-contact articles in the United StatesFormulation-specific supplier certification required
    EU Regulation (EU) No 10/2011Plastic materials and articles intended to come into contact with foodOverall and specific migration testingTest on finished article under intended conditions of use
    REACH Regulation (EC) No 1907/2006SVHC and Annex XVII restrictionsArticle compliance in the European UnionSDS review and supplier declaration required
    RoHS Directive 2011/65/EURestriction of hazardous substancesElectrical and electronic applicationsSupplier declaration for lead, cadmium, mercury, chromium VI, PBB, and PBDE
    ISO 19069-2:2016Polypropylene moulding and extrusion materialsSpecimen preparation and property determinationUse as a reference for comparable mechanical testing

    Comparative Differentiation Against Lower-Flow Impact Copolymers and High-Flow Homopolymers

    The selection boundary is defined by the melt-flow/impact balance. Lower-flow heterophasic copolymers with MFR values below 30 g/10 min generally retain higher low-temperature notched impact but require higher pack pressures and longer fill times in thin-wall tools. High-flow homopolymers at comparable MFR may provide higher tensile modulus and shorter cycle time but fail at lower impact energy. MOPLEN PP EP548Q occupies an intermediate position: high flow is achieved without moving to a homopolymer morphology, but the ethylene-propylene rubber phase reduces tensile modulus relative to a homopolymer. The grade should not be selected when transparency, high gloss, or low-temperature ductility below −20 °C are primary requirements. Published data for this specific comparison is limited; comparative moulding trials on the intended tool are required because tool-specific orientation and weld-line placement determine the final mechanical response.

    Production failure modes associated with this product class include short shots from undersized vents, jetting from gate geometries that allow free-jet filling, gate blush from excessive shear stress, and splay from surface moisture. Weld-line strength in thin-wall closures is reduced when two melt fronts meet at low temperature; increasing melt temperature within the 220 °C to 250 °C window improves weld-line strength but may extend cycle time and increase odour formation in hot runners. Regrind use should be limited to validated ratios. Multiple heat histories increase the MFR and shift shrinkage, impact, and colour. A prudent control plan measures melt flow rate and notched Charpy impact after 5 re-moulding cycles, and rejects regrind that raises MFR outside the supplier’s release limits. Foreign-polymer contamination, especially from polyethylene or polyamide, requires purging with a suitable polypropylene purge compound before start-up, because incompatible phases cause delamination and variable impact behaviour in the finished article.

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