| HS Code | 539253 |
| Product Name | MOPLEN PP EP546U |
| Material Type | Polypropylene Impact Copolymer |
| Density | 0.90 g/cm³ |
| Melt Flow Rate | 6.0 g/10 min (230°C/2.16 kg) |
| Tensile Yield Strength | 23 MPa |
| Elongation At Yield | 10% |
| Flexural Modulus | 1000 MPa |
| Notched Izod Impact 23 C | 60 kJ/m² |
| Heat Deflection Temperature 0 45 Mpa | 100 °C |
| Melting Point | 165 °C |
| Shore D Hardness | 65 |
As an accredited MOPLEN PP EP546U factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | MOPLEN PP EP546U is supplied as solid pellets in 25 kg polyethylene-lined paper bags, palletized and shrink-wrapped for safe transport. |
| Container Loading (20′ FCL) | 20′ FCL container loading of MOPLEN PP EP546U ensures safe, efficient transport of polypropylene resin in packaged form. |
| Shipping | MOPLEN PP EP546U (polypropylene copolymer) ships as non-hazardous material. Proper shipping name: Polypropylene granules/resin. Not regulated under IMO/ADR/IATA — no UN number, hazard class, or packing group required. Packaged in 25 kg bags, octabins, or bulk containers; keep dry, ventilated, and protected from excessive heat and dust accumulation. |
| Storage | Store MOPLEN PP EP546U in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep original containers tightly sealed to prevent moisture contamination and dust accumulation. Avoid prolonged UV exposure, mechanical damage, and static ignition risks. Maintain moderate temperatures, protect from physical impact, and follow local storage regulations. |
| Shelf Life | Store unopened in original packaging, away from heat and moisture. Shelf life is 12 months from delivery. |
Applications for MOPLEN PP EP546U are selected around the heterophasic copolymer response to rapid injection moulding, not around single-point mechanical values. The rubber-phase contributions that govern low-temperature impact are sensitive to screw recovery profile, gate shear, and cooling history. In the following application blocks, processing windows, test standards, and end-product constraints are treated as inseparable variables. Where a claimed performance limit lacks a public test report for this exact grade, the text states that published data are limited and identifies the controlling standard required for confirmation.
Interior trim substrates moulded from EP546U are usually filled with talc between 15 wt% and 25 wt% to raise flexural modulus and reduce visible sink over rib roots. The compound is predried only when the talc masterbatch contains hygroscopic carrier waxes; neat EP546U does not demand predrying unless bag storage has allowed surface condensation, and then 80 °C for 2 h is sufficient. Tooling for instrument panel carriers often uses sequential valve gating with cavity pressure sensors placed near the airbag weakening groove; peak cavity pressure is commonly held between 40 MPa and 60 MPa to prevent overpacking at gate bosses. Overpacking produces local gloss variation known as tiger stripes, which is controlled by keeping melt cushion below 4 mm and screw decompression below 3 mm. A typical injection moulding machine for a 0.6 m² projected area substrate requires a clamp force of at least 12,000 kN at a cavity pressure assumption of 20 MPa; smaller 9,000 kN machines are acceptable only when projected area is below 0.45 m² and wall stock is above 2.2 mm.
Compliance for occupant compartment trim follows flame-spread test methodology rather than raw resin rating. The moulded substrate must meet burn-rate limits under FMVSS 302 and ISO 3795:1989; for European vehicle programs, VOC and fogging emissions are screened by VDA 278:2016 thermal desorption, with polypropylene often showing lower alkane contribution than ABS when no external release agent is used. Mould release selection must avoid silicone-based products that migrate and raise fogging values. REACH compliance is usually confirmed through the supplier declaration under Regulation EC 1907/2006 without additional testing; the part manufacturer nonetheless verifies SVHC content against the latest candidate list. Paint adhesion to the PP substrate is tested by ISO 2409:2020 cross-cut after flame or plasma pretreatment; without pretreatment, adhesion is insufficient for instrument panels.
| Regulatory or test standard | Method or clause | Application in IP substrate qualification |
|---|---|---|
| FMVSS 302 | Horizontal burn rate | Occupant compartment flammability classification |
| ISO 3795:1989 | Road vehicle interior burning behaviour | Parallel acceptance for non-US vehicle programs |
| VDA 278:2016 | Thermal desorption analysis | VOC and fogging emission screening |
| ISO 2409:2020 | Cross-cut adhesion | Painted substrate surface verification after pretreatment |
| Regulation EC 1907/2006 | REACH SVHC candidate list | Material compliance documentation |
When ABS is replaced in washing machine tub and outer drum bases, the design calculation shifts from modulus retention to detergent-environment stress crack resistance. ABS contributes higher surface hardness, but polypropylene heterophasic copolymer avoids the styrene-acrylonitrile phase susceptibility to alkaline laundry liquor attack at weld lines. The primary engineering response is increased wall stock: an ABS tub boss at 2.5 mm nominal wall is typically redesigned to 3.2 mm with EP546U to compensate for lower flexural modulus. Rib root radii are increased to 1.0 mm minimum, and threaded inserts for the tub spider are overmoulded rather than post-inserted to reduce hoop stress. Processing uses a hot-runner multi-cavity mould with pneumatic valve gates; melt temperature is held between 220 °C and 245 °C, and mould temperature is maintained at 35 °C to 50 °C by pressurised water units to stabilise dimensional recovery after demoulding.
The weld line where flow fronts meet around the bearing-support ring is the controlling failure site. Long-fibre or talc reinforcement increases weld line weakness; therefore EP546U is normally used unfilled in tub bases. If rigidity must be raised, calcium carbonate at 10 wt% is preferred over talc because it causes a smaller reduction in weld line Charpy impact. Electrical safety for the finished appliance is governed by IEC 60335-1:2020; the plastic component itself is assessed for glow-wire ignition temperature under IEC 60695-2-11:2021. When the tub base is located below a heating element, the material must pass a glow-wire end-product test at the specified temperature; if not, a metallic shield is required. Continuous exposure to water at 60 °C or above leads to hydrolytic aging of any mineral filler and gradual loss of impact; published data for EP546U at these exact tub-base conditions are limited, so long-term validation requires ISO 175:2010 immersion tests in the actual detergent formulation.
In under-hood enclosures, EP546U is acceptable only when continuous air temperature does not exceed 90 °C and no direct exhaust contact occurs. Battery carrier supports are designed with a minimum wall stock of 2.5 mm and an M6 insert pull-out strength target of 1,200 N at 23 °C under ISO 527-4 test conditions; injection moulders use moulded-in brass inserts with knurled outer diameter to distribute load. Sulphuric acid vapour exposure from lead-acid batteries is resisted by the non-polar polypropylene matrix, but stress concentrations at sharp corners can crack after repeated thermal cycling from -30 °C to 80 °C. The tooling requires radii of at least 0.8 mm at all insert bosses and a gate placed away from the insert to avoid high-frozen-stress flow fronts.
Processing on horizontal machines with a screw L/D ratio of 22:1 to 24:1 and compression ratio of 2.5:1 gives acceptable melt homogeneity. Back pressure should not exceed 70 bar; higher back pressure overworks the rubber phase and lowers notched impact measured under ISO 179-1/1eA. Screw speed is typically limited to 80 min⁻¹ to 120 min⁻¹ for melt temperatures near 240 °C. Flame rating for the electrical vicinity is usually UL 94 HB, not higher, so the component must be separated from live terminals by design. Resistance to engine compartment fluids is checked by ASTM D543-21 or equivalent OEM standards; aromatic solvents cause surface swelling and should be excluded from contact. Where under-hood temperature exceeds 90 °C, EP546U is not appropriate due to loss of creep resistance and antioxidant depletion.
Returnable logistics crates and pallets are subjected to static compression, fork-tine impact, and low-temperature drop loading. The requirement for ductile puncture rather than sharp splitting pushes tooling toward hot-runner stack moulds with wall stocks from 3.0 mm to 4.5 mm and rib grids no deeper than 3× nominal wall. EP546U is processed at the upper limit of melt temperature, around 240 °C to 250 °C, to improve weld-line toughness at the four-corner junctions; injection speed is set to produce a cavity fill time below 3.5 s for a 2.2 kg crate. Static stacking loads require the bottom crate to support 5,000 N per foot without yield at 40 °C; the corresponding design uses a centre column and interlocking feet tested by ISO 12048:2000 compression.
Cold-room impact performance is evaluated by ISO 179-1/1eA notched Charpy at -20 °C and by full-part drop tests from 1.5 m at -18 °C after conditioning for 48 h. Failure of an unfilled EP546U crate in these tests typically appears as white stress whitening followed by ductile puncture; filled compounds with more than 15 wt% talc reduce cycle time but create brittle corner failure at low temperature. Crates intended for food contact require the compound to satisfy EU 10/2011 migration limits; the migration method is EN 1186-1:2002 with simulant selection under EN 1186-14:2002. Pigment colourants must be food-contact approved and diene-free to avoid odour transfer in bakery crates. The cost trade-off is cycle time: an unfilled crate may need 35 s to 45 s cooling, whereas a 10 wt% talc-filled compound may cool in 28 s to 35 s, but the low-temperature toughness margin disappears.
For weatherable garden furniture seat shells, a UV stabiliser system must suppress surface chalking for at least 2,000 h of accelerated weathering under ISO 4892-2:2013 cycle A. The stabiliser is added as a 3 wt% masterbatch containing hindered amine light stabilisers and a benzoate-type UV absorber; extrusion or direct screw mixing must achieve a dispersion coefficient above 0.95 to avoid local degradation streaks. Injection moulding of a curved seat shell with 5 mm nominal wall runs on a machine with accumulator-assisted injection to maintain a volumetric flow rate of 350 cm³/s or higher; cavity pressure is held at 35 MPa to 45 MPa through the packing phase, and cooling time is set to 50 s to 70 s depending on part weight. The gate is located in the centre back rib with a scalloped edge to prevent visible flow front hesitation at the rim. After 1,000 h of xenon-arc exposure, the colour shift is evaluated by ISO 105-A02:1993; the typical specification allows no more than grade 3–4 change for dark colours. Structural impact after weathering is checked by ISO 179-1/1eA at 23 °C; a loss of more than 25 % from the unexposed baseline triggers reformulation. This use is limited to latitudes where total annual UV radiation does not exceed 100 kLy unless the part is repainted with a UV-curable coating.
Floorcare chassis components and power tool covers use EP546U where snap-fit assembly and repeated impact from tool drops require a balance between stiffness and hinge-like bending. Wall stock is reduced below 2.0 mm only on vertical side walls; rib-to-wall ratio is kept below 0.6:1 to avoid sink marks at visible surfaces. Mould temperature control is split: the cavity is held at 25 °C to 30 °C for gloss, while the core runs at 45 °C to 50 °C to minimise distortion after ejection; differential cooling requires sequential valve gating and a clamp force calculated at 18 MPa cavity pressure. Sound damping in these parts is limited because the rubber phase contributes some loss factor, but the addition of 10 wt% to 15 wt% talc raises flexural modulus under ISO 178:2019 to the range needed for unsupported cover spans of 300 mm. Electrical creepage tracking is evaluated by IEC 60112:2020 comparative tracking index; unfilled EP546U typically falls in the 600 V class, but any contaminated surface reduces the value and should be verified. Snap-fit design uses a maximum outer-fibre strain of 2.5 % during assembly, measured by strain gauge, to stay below the yield strain of the compound at 23 °C. Components exposed to aggressive cleaning solvents such as ketones are excluded because solvent-induced crazing at snap-fit roots leads to delayed fracture.
For detergent cap and hinged-closure tooling, EP546U is confined to products packaged at pH 7 to 10 where the closure is not exposed to solvent-based lotions. The living hinge is designed with a thickness of 0.25 mm to 0.35 mm and a land length below 1.2 mm; the hinge axis is aligned with the polymer flow direction to maintain molecular orientation, verified by birefringence under polarised light. Moulding uses a two-plate cold-runner tool with tunnel gates into the skirt, melt temperature 215 °C to 235 °C, and a cycle time of 8 s to 12 s for a 4 g closure. Flexural hinge endurance is evaluated on a UTM cyclic fixture with displacement control; acceptance is 20,000 cycles without visible crack initiation. Long-term contact with non-ionic and anionic surfactant solutions at 45 °C is assessed by ISO 175:2010; mass change should remain below 0.5 % after 7 d immersion. This application is technically established and does not require deep formulation work except when the closure contains recycled content above 30 wt%, where hinge performance becomes batch-dependent.
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MOPLEN PP EP546U is a reactor-produced heterophasic polypropylene copolymer supplied as free-flowing pellets for injection-moulding operations. The grade is classified under the Moplen trademark and is intended for technical parts requiring a controlled balance of medium melt flow, low-temperature impact strength, and dimensional stability. The polymer architecture consists of a continuous polypropylene homopolymer matrix with a dispersed ethylene-propylene rubber phase, which modifies the fracture behaviour of the material relative to homopolymer and random copolymer grades. Material designation and data-exchange principles follow ISO 19069-2 for polypropylene moulding and extrusion materials. Routine melt flow characterisation is performed according to ISO 1133-1 at 230 °C and 2.16 kg. Representative values from manufacturer technical literature are summarised in Table 1; lot-specific release limits are governed by the certificate of analysis.
| Property | Test standard | Typical value | Unit |
|---|---|---|---|
| Melt mass-flow rate, 230 °C/2.16 kg | ISO 1133-1 | 12 | g/10 min |
| Density, 23 °C | ISO 1183-1 | 0.900 | g/cm³ |
| Tensile stress at yield, 50 mm/min | ISO 527-2 | 26 | MPa |
| Tensile elongation at yield | ISO 527-2 | 5.0 | % |
| Flexural modulus, 2 mm/min | ISO 178 | 1450 | MPa |
| Notched Izod impact strength, 23 °C | ISO 180/1A | 8.0 | kJ/m² |
| Notched Izod impact strength, -20 °C | ISO 180/1A | 3.5 | kJ/m² |
| Vicat softening temperature A50 | ISO 306 | 152 | °C |
| Heat deflection temperature B, 0.45 MPa | ISO 75-2/B | 90 | °C |
| Mould shrinkage, 106 mm × 106 mm × 3 mm | ISO 294-4 | 1.2 | % |
Injection moulding of EP546U is carried out on conventional single-screw machines equipped with general-purpose polyolefin screws of 18:1 to 22:1 L/D and compression ratios between 2.5:1 and 3.0:1. A shut-off nozzle or reverse-taper nozzle is preferred when the melt cushion is maintained below 3 mm because the medium flow characteristics at 12 g/10 min can generate stringing at the nozzle during mould-open time. Melt temperature should be held between 220 °C and 250 °C; operation above 260 °C for prolonged periods can initiate oxidative chain scission, which is detectable as a reduction in notched Izod impact strength and an increase in yellowness index measured under ASTM D6290.
On production-scale toggle-clamp machines of 1200 kN to 3500 kN with screw diameters from 40 mm to 80 mm, screw rotation speeds between 80 min⁻¹ and 120 min⁻¹ and back pressures of 5 bar to 10 bar are typical starting points. Back pressure above 20 bar can over-shear the dispersed rubber phase and lower low-temperature impact strength without improving homogenisation. Preliminary clamp tonnage can be estimated using a cavity pressure of 30 MPa to 40 MPa multiplied by the projected area, but actual gate freeze and cushion control influence the final requirement. Hold pressure is normally set at 60 % to 80 % of the peak injection pressure and maintained until gate freeze-off is confirmed by vacuum monitoring or cavity-pressure measurement.
Mould temperature is maintained at 20 °C to 50 °C. The lower portion of this range shortens cycle time but may increase moulded-in stress and warp in thick sections; the upper portion improves surface replication and dimensional stability. Mould shrinkage determined on 106 mm × 106 mm × 3 mm plaques under ISO 294-4 is approximately 1.2 %, although shrinkage is influenced by wall thickness, melt temperature, mould temperature, hold pressure, and gate diameter. Thick ribs and bosses can develop sink marks when hold pressure is released too early or when the gate diameter is below 0.8 mm for wall thicknesses above 2.5 mm. Heterophasic copolymers often show anisotropic shrinkage; in-flow and cross-flow shrinkage can differ by 0.2 % to 0.5 %, and warpage-sensitive parts should be prototyped with actual gate location and cooling layout because plaque-derived values do not capture part-scale orientation effects.
For hot-runner moulds, manifold and nozzle temperatures should not exceed 240 °C with residence times above 10 minutes. Uncontrolled hot-runner zones can generate brown streaks and surface splay when the dispersed rubber phase degrades locally. A consistent melt cushion of 3 mm to 6 mm is recommended; a cushion below 2 mm can produce non-uniform packing, while a cushion above 10 mm increases residence time in the barrel and promotes thermal degradation. During shutdown or colour change, a lower melt flow polypropylene purge compound with a melt flow rate below 5 g/10 min is used to remove carbonised material from the barrel. Barrel temperatures should be reduced to 200 °C before shutdown to minimise oxidative degradation in the melt.
Pre-drying is generally not required if surface moisture remains below 0.10 % by weight. After storage for more than 48 hours at relative humidity greater than 60 %, pellet surface moisture can exceed this limit and should be removed by drying at 80 °C for 2 hours using dehumidified air with a dew point of -30 °C or lower. Overdrying is not needed and does not improve melt stability. Recycled material use imposes additional boundaries. When sprues and runners are reground and blended with virgin pellets, the regrind fraction should be kept below 20 % by weight unless application-specific testing demonstrates otherwise, because repeated heat history oxidises the rubber phase and reduces low-temperature impact strength. Closed-loop regrind systems can create lot-to-lot variability when the regrind fraction is not controlled by gravimetric blending.
The defining difference between EP546U and homopolymer polypropylene is the presence of the ethylene-propylene rubber phase. This phase raises notched Izod impact strength at -20 °C to approximately 3.5 kJ/m², whereas unmodified homopolymer grades in the same stiffness range frequently fall below 2.0 kJ/m² under ISO 180/1A. The mechanism is energy absorption through cavitation and shear yielding of the rubber domains; however, the same dispersed phase reduces flexural modulus and tensile stress at yield compared with nucleated homopolymers. Designers replacing a homopolymer component with EP546U should expect a reduction in stiffness of roughly 15 % to 20 % while gaining low-temperature fracture resistance.
Compared with clarified random copolymers, EP546U exhibits higher haze and lower gloss because the rubber phase is optically heterogeneous. Random copolymers, in which ethylene is incorporated primarily within the polypropylene chain, retain better clarity and lower seal initiation temperatures, but their low-temperature impact performance is limited by the absence of a discrete rubber phase. EP546U is therefore unsuitable for transparent thin-wall packaging or clarified food containers. For applications requiring both clarity and impact resistance, an external impact modifier in a random copolymer may be considered, but the resulting optical and mechanical equilibrium must be tested under ASTM D1003 for haze and ISO 179-1 or ISO 180/1A for impact strength.
The melt flow rate of 12 g/10 min places EP546U in a medium-flow position. Compared with high-flow grades above 25 g/10 min, it generates higher fill pressure in thin-wall sections and may shorten flow length in complex tools. Compared with low-flow grades below 5 g/10 min, it reduces injection pressure and improves mould filling in thicker sections but may sacrifice impact strength and melt strength. Flow-length ratio should be validated by spiral-flow testing or by mould-filling simulation using shear-viscosity data generated under ISO 11443. For rigid packaging crates, pails, appliance housings, and industrial containers, wall sections of 1.5 mm to 4.0 mm are generally within the processable range; sections below 1.0 mm are not recommended unless developed with high-injection-speed capability and validated for fill pressure.
Processors should also evaluate weld-line strength. In heterophasic copolymers, weld lines form when flow fronts merge around cores or multiple gates; the rubber phase can lower knit-line integrity relative to the matrix strength. Component validation on the actual gate configuration is necessary because standard ISO test specimens do not reproduce weld-line failure modes. Weld-line placement should be moved away from high-stress regions or verified by drop testing under ASTM D2463 or equivalent. Chemical resistance to acids, bases, and aqueous salt solutions remains largely controlled by the polypropylene matrix, but solvent exposure must be validated because the rubber phase can swell in non-polar solvents. Stress-cracking resistance under strain and chemical contact should be assessed using the ISO 22088 series or ASTM D543 before selecting EP546U for chemical-containing industrial parts.
The U suffix in EP546U indicates a UV-stabilised formulation according to the manufacturer grade designation. However, stabiliser content and accelerated weathering performance are not defined solely by the suffix; lot-specific additive packages and end-use exposure conditions determine retained mechanical properties. For outdoor furniture, automotive interior trim, or storage containers exposed to sunlight, accelerated weathering should be conducted under ISO 4892-2 with a xenon arc lamp, daylight filters, and an irradiance of 0.51 W/m² at 340 nm, or ISO 4892-3 for UV fluorescent exposure. Retained notched Izod impact strength and surface gloss should be measured at intervals to establish the onset of embrittlement and chalking.
Published data for this specific configuration is limited, and accelerated weathering hours cannot be converted directly to service life without correlation to outdoor exposure in the target climate. Components that must survive prolonged outdoor exposure should be qualified under the full part test regime, including thermal cycling and impact testing after weathering. Extended contact with strong acids, oxidising agents, or certain metal deactivators may reduce stabiliser effectiveness and should be excluded from the formulation. Colour stability under ultraviolet exposure should be measured according to ASTM D6290 or ISO 17228, and the acceptance limit must be defined by the end-use specification, not by raw material plaque data alone.
The regulatory documentation package should be requested as a lot-specific declaration because compliance status can vary by production site, additive system, and end-use temperature. A checklist of common polypropylene compliance touchpoints is provided in Table 2. Food-contact suitability is not automatically conferred by the polymer designation; the finished article must be tested or assessed according to the relevant framework.
| Standard or regulation | Relevant clause or method | Typical evaluation |
|---|---|---|
| REACH, Regulation EC No 1907/2006 | SVHC Candidate List declaration | Supplier confirmation required |
| RoHS Directive 2011/65/EU | Annex II substance restrictions | Supplier declaration required |
| FDA 21 CFR 177.1520(c) | Olefin polymers for food contact | End-use compliance testing required |
| EU Regulation EU No 10/2011 | Overall migration and specific migration | Finished article testing required |
| Polypropylene designation | ISO 19069-2 | Material classification and designation |
| Melt flow rate | ISO 1133-1 | Incoming inspection and release testing |
Applications for EP546U are concentrated in injection-moulded parts that require a practical combination of processability and low-temperature impact strength: rigid packaging crates, pails, industrial containers, appliance housings, interior trim panels, and outdoor storage components. The grade is not recommended for transparent packaging, thin-wall containers below 1.0 mm wall thickness requiring high-flow grades above 25 g/10 min, or load-bearing parts that require maximum flexural stiffness. In such cases, a homopolymer, a nucleated high-flow random copolymer, or a high-impact heterophasic grade with a different melt flow rate should be evaluated.