| HS Code | 995607 |
| Density | 0.905 g/cm³ |
| Melt Flow Rate 230 C 2 16 Kg | 8 g/10 min |
| Tensile Stress At Yield | 21 MPa |
| Tensile Strain At Yield | 10% |
| Flexural Modulus | 900 MPa |
| Charpy Notched Impact Strength 23 C | 50 kJ/m² |
| Rockwell Hardness | R80 |
| Melting Temperature | 165 °C |
| Vicat Softening Temperature | 148 °C |
| Heat Deflection Temperature 0 45 Mpa | 85 °C |
As an accredited Moplen EP548P PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Moplen EP548P PP Copolymer is packaged in 25 kg multiwall paper bags, palletized and shrink-wrapped for secure handling and transport. |
| Container Loading (20′ FCL) | 20′ FCL loading: 20 metric tons of Moplen EP548P PP Copolymer in 25 kg bags, palletized and shrink-wrapped for safe transport. |
| Shipping | Moplen EP548P PP Copolymer ships as a non-hazardous polypropylene resin in pellet form. It is packaged in sealed multiwall paper bags or bulk hopper trucks. Store away from direct sunlight, moisture, and heat sources. Keep packaging intact to prevent contamination. No special hazard labeling required. |
| Storage | Store Moplen EP548P PP Copolymer in a dry, clean, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep containers sealed to prevent moisture pickup and contamination. Avoid prolonged storage above 40°C. Protect pellets from dust and mechanical damage, and rotate stock to ensure first-in, first-out usage. |
| Shelf Life | Moplen EP548P PP Copolymer has a shelf life of several years when stored in a cool, dry, shaded area, away from UV and moisture. |
In thin-wall automotive interior moulding, door panel substrates produced from Moplen EP548P are processed on hydraulic injection moulding machines with clamp forces from 1,000 kN to 2,500 kN. Melt temperature measured at the nozzle is maintained between 220°C and 250°C; the barrel profile is typically set from 200°C rear, 210°C centre, 220°C front, to 230°C nozzle. Water-circulating mould temperature is held at 20°C to 40°C to balance surface gloss against cycle time. Fill times for door panel carriers in the 500 g to 800 g shot weight range are set between 1.2 s and 2.5 s; packing pressure of 35 MPa to 60 MPa is applied for 4 s to 8 s to suppress sink marks at rib intersections. The dispersed ethylene-propylene rubber phase in the heterophasic copolymer provides ductile response at interior temperatures, but grained surfaces are required to mask flow lines and scratch initiation. Low-emission additives are incorporated before injection moulding; fogging condensate of Class A visible interior parts is tested per DIN 75201:2011 with gravity-flow condenser temperatures of 100°C for 16 h. Pre-drying is not normally required for unopened silos, but storage at relative humidity above 60% for more than 48 h makes hot-air drying at 80°C for 2 h necessary to prevent silver streaks. The material is supplied in natural pellet form and is conventionally masterbatched with carbon black, talc, or colour concentrates at 2 wt% to 5 wt%; masterbatch carriers must be PP-based to avoid delamination at weld lines.
Wheel arch liners and underbody shields injection moulded from Moplen EP548P are produced with shot weights from 900 g to 2,500 g and nominal wall thicknesses from 2.0 mm to 2.5 mm. The primary failure mode is brittle fracture under stone impact at low ambient temperature; multiaxial impact behaviour is therefore assessed per ISO 6603-2 at -30°C using a 20 mm diameter hemispherical striker and a 40 mm ring clamp. Unfilled medium-flow heterophasic copolymers of this MFR class typically exhibit total penetration energy in the range of 15 J to 25 J at -30°C, with ductile-to-brittle transition determined by rubber phase size, ethylene content, and nucleation. Moulding trials on a 1,600 kN accumulator-assisted machine show that injection speeds above 80 mm/s and melt temperatures above 240°C reduce visible flow lines around attachment bosses, but melt temperatures above 260°C increase the risk of molecular weight degradation and a drop in impact energy of 10% to 20% after a second heat history. Fastener bosses for trim clips are designed with a minimum boss diameter of 8 mm, a draft angle of 0.5° to 1.0°, and a wall thickness ratio to nominal wall of 0.6 to 0.7 to avoid sink marks and cracking at insertion. Road salt and stone debris are simulated by immersion in 10 wt% aqueous sodium chloride at 23°C for 7 days followed by tensile property retention testing per ISO 527-2:2012; retention of tensile stress at yield above 90% is considered acceptable for wheel arch applications. Because the component is not a Class A exterior surface, surface defects are less critical, but warpage from differential shrinkage must be controlled by symmetrical runner layout and uniform cooling within 5°C across the mould face.
For washing machine bottom plates, front panels, and top frames, Moplen EP548P is selected where creep resistance under static load, low-speed impact after repeated thermal cycles, and dimensional stability are required. Melt temperature is maintained between 230°C and 260°C for hot-runner gates above 1.5 mm to prevent jetting; cold-runner sprue bush orifice diameters below 3.5 mm require screw decompression of 3 mm to 5 mm to prevent drool. For washing machine front panels with projected area around 0.35 m², clamp force requirements are calculated at 90 kN to 120 kN per 0.01 m² of projected area when using melt pressures of 35 MPa to 50 MPa. Dimensional tolerance for hinge and latch mounting points is held to ±0.3 mm by post-mould cooling fixtures for 60 s to 120 s and by minimising mould temperature differentials to less than 5°C. Creep testing per ISO 899-2:2024 at 23°C and 6 MPa for 1,000 h is used to screen long-term deflection in load-bearing ribs; for unfilled impact copolymers of this class, creep modulus after 1,000 h generally falls below 50% of the short-term flexural modulus. Unfilled Moplen EP548P is classified UL 94 HB; components used in unattended appliance circuits or near electrical connections require flame-retardant modification or shielding because the glow-wire ignition temperature per IEC 60695-2-11 for unfilled polypropylene is typically in the 550°C to 650°C range. When detergent exposure is expected, stress-crack resistance is screened by mounting a strained specimen in a 0.5% sodium dodecylbenzene sulfonate solution at 60°C for 48 h; visual cracking at the gate region indicates insufficient melt homogenisation or excessive flow length.
Industrial crates, pallets, and distribution containers moulded from Moplen EP548P use closed-loop regrind streams as standard production practice. Edge trim, runner scrap, and rejected parts are granulated through a screen aperture of 8 mm to 10 mm, then reintroduced into virgin pellets at 20 wt% to 40 wt% via gravimetric dosing. The technical risk is progressive chain scission: each pass through a reciprocating screw at melt temperature above 230°C increases melt flow rate by 2 g/10 min to 5 g/10 min after three heat histories, measured per ISO 1133-1:2022 at 230°C and 2.16 kg. If MFR exceeds 18 g/10 min, short shots occur in thin ribs below 1.5 mm wall and hinge boss cracking increases in drop tests from 1 m at -20°C. To limit this drift, barrel residence time is kept below 5 min and screw rotational speed is maintained between 80 rpm and 120 rpm on a 2,500 kN injection moulding machine with a 60 mm diameter screw. The optimum regrind ratio for heavy-duty crates with a 600 mm × 400 mm × 300 mm internal volume is 30 wt%; at this level, Charpy notched impact at -20°C per ISO 179-1:2010 remains within 80% of the virgin value, while tensile stress at yield per ISO 527-2:2012 drops by less than 5%. Stacked pallet performance is evaluated by applying a static load of 2,500 kg for 24 h at 23°C; permanent set of the pallet deck after unloading must remain below 5 mm to maintain racking stability. When black masterbatch is added at 1.5 wt% to 2.0 wt%, dispersion quality is checked by measuring pressure before the screen changer; a pressure increase above 20% from clean screen condition indicates agglomerates that will initiate impact failure at weld lines.
Moplen EP548P is used as a compounding base resin for talc-filled, elastomer-modified, and nucleated polypropylene formulations. Compounding is performed on co-rotating twin-screw extruders with a length-to-diameter ratio of 40:1 to 52:1, side-fed talc at 20 wt% to 40 wt%, and liquid or pelletized elastomer addition through a downstream port after the first melt seal. Barrel temperatures are set from 180°C at the feed throat to 230°C at the die, with screw speed between 300 rpm and 600 rpm and specific mechanical energy input ranging from 0.15 kWh/kg to 0.25 kWh/kg. The main processing conflict is the competing relationship between flexural modulus and notched impact strength: talc raises stiffness but reduces Charpy impact, while an elastomeric modifier restores low-temperature toughness at the cost of melt flow and heat deflection temperature. The table below gives typical compounded property ranges for medium-flow heterophasic copolymers on this type of line; values for Moplen EP548P must be verified against the current technical data sheet because published data for this specific configuration is limited.
| Formulation | Moplen EP548P (wt%) | Talc (wt%) | Elastomer (wt%) | Flexural modulus per ISO 178:2019 (MPa) | Charpy notched 23°C per ISO 179-1 (kJ/m²) | MFR per ISO 1133-1 (g/10 min) |
|---|---|---|---|---|---|---|
| Unfilled | 100 | 0 | 0 | 1,100–1,300 | 25–45 | 10–15 |
| Talced | 80 | 20 | 0 | 1,800–2,200 | 15–25 | 9–14 |
| High-stiffness | 60 | 40 | 0 | 2,800–3,400 | 8–15 | 8–13 |
| Toughness-modified | 70 | 20 | 10 | 1,500–1,800 | 30–50 | 8–12 |
After compounding, pellet MFR is measured per ISO 1133-1:2022, and a shift of more than 3 g/10 min from the target is used to reject the batch. The compounded pellets are then injection moulded into automotive interior substrates, appliance housings, or industrial containers. For talc-filled grades, mould shrinkage anisotropy between flow and cross-flow directions increases from 0.8% to 1.2% for the unfilled base to 0.4% to 0.8% in the flow direction and 0.8% to 1.4% cross-flow at 40 wt% talc, making gate location and cooling uniformity decisive for flatness. Nucleation and thermal stability packages are added at 0.10 wt% to 0.25 wt% to raise recrystallization temperature and shorten cycle time; overdosing above 0.3 wt% can nucleate excessive spherulitic refinement and reduce impact strength by 15% to 30%.
During qualification of battery peripheral brackets, covers, and charging connector housings, unfilled Moplen EP548P follows a different validation sequence than automotive interior parts. The unfilled heterophasic copolymer is normally rated UL 94 HB, so direct enclosure applications in unattended charging stations demand flame-retardant compounds or additional insulation barriers. Electrical tracking resistance is measured per IEC 60112:2020; unfilled PP typically shows comparative tracking index values of 600 V or higher, but this value is sensitive to surface contamination from mould release. Low-temperature ductility is screened by notched Charpy impact per ISO 179-1:2010 at -20°C; values below 8 kJ/m² are unacceptable for snap-fit battery covers that must survive disassembly with a flat tool at 0°C. Dimensional stability under heat is evaluated using heat deflection temperature at 0.45 MPa per ISO 75-2:2020; unfilled medium-flow grades in this class typically show HDT between 70°C and 90°C, which limits continuous use near high-voltage components to ambient temperatures below 65°C. For connector brackets with metal insert moulding, insert temperature before moulding should be raised to 80°C to 120°C to reduce residual stress; cold inserts below 50°C cause microcracking at the insert interface and loss of retention force after thermal cycling from -40°C to 85°C for 500 cycles. Gate location for cylindrical connector housings is placed opposite the snap-fit arms to orient weld lines away from maximum flexural stress; weld-line strength retention above 70% of the unfilled tensile stress at yield is considered the minimum acceptance threshold. Compliance declarations for supplied articles under RoHS 2011/65/EU and REACH SVHC screening are required; natural polyolefin base material normally contains no restricted phthalates or heavy metals. Because published data for this specific configuration is limited, mould qualification must include on-part impact testing and MFR verification per ISO 1133-1:2022 on first-article samples.
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Moplen EP548P is a heterophasic polypropylene copolymer supplied in pellet form for injection moulding, compounding, and selected extrusion conversion. The model designation distinguishes it from homopolymer and random copolymer grades of equivalent melt fluidity because the reactor composition includes a dispersed ethylene-propylene rubber phase within a polypropylene matrix. Procurement specifications for this grade are normally built around four indices: melt mass-flow rate measured under ISO 1133-1 at 230 °C with 2.16 kg, density measured under ISO 1183-1, tensile modulus measured under ISO 527-2, and notched Charpy or Izod impact strength measured under ISO 179-1/1eA or ISO 180/A. Typical release values fall in the 18–21 g/10 min melt-flow band, with density close to 0.900 g/cm³. Tensile modulus values usually occupy the 1100–1350 MPa range, and room-temperature notched impact values are generally above 20 kJ/m². These figures are purchase-order envelopes, not batch guarantees; the certificate of analysis controls each lot. The product is formulated for applications in which a homopolymer would fail by brittle fracture, particularly under impact at service temperatures near 0 °C or at weld lines.
In instrumented puncture tests under ISO 6603-2, the energy-absorbing mechanism changes from shear yielding to craze-dominated failure as temperature falls. The dispersed rubber domains act as stress concentrators; their efficiency depends on domain size, ethylene content, and the viscosity ratio between the rubber phase and the matrix. For Moplen EP548P, published data for thin-walled injection mouldings indicate that the advantage over homopolymer PP is greatest at 23 °C and diminishes sharply below 0 °C. Notched Izod values at −20 °C frequently drop below 8 kJ/m² unless the part is annealed, nucleated, or moulded at thicknesses above 3 mm. Weld lines impose an additional constraint. In production mouldings, weld-line energy absorption can be 40–60% lower than the un-welded baseline because the rubber domains do not re-entangle across the melt front. The practical consequence is that gate placement, flow-front temperature, and injection speed are stronger determinants of low-temperature service performance than minor variations in resin lot impact.
Compounding operations on a 40 L/D co-rotating twin-screw extruder typically set barrel temperatures between 180 °C and 230 °C, with screw speed between 250 rpm and 400 rpm. The grade accepts mineral fillers, glass fibre, and elastomer modifiers when the side feeder is positioned after the primary plasticization zone. Specific mechanical energy should be held below 0.25 kWh/kg; above this threshold, the rubber phase can undergo thermo-oxidative scission, and the retention of notched Izod impact declines even if the compound’s melt flow remains within specification. Batch-to-batch variance in the base resin is best monitored by capillary rheometry at 230 °C and apparent shear rates between 100 s⁻¹ and 1000 s⁻¹; a shift in shear viscosity of more than 10% at 1000 s⁻¹ typically alters filler dispersion uniformity on a production line. The grade is not hygroscopic, but additives and fillers may carry moisture; pre-drying at 80 °C for 2–4 h is recommended if the compounded formulation contains mineral filler stored in relative humidity above 60%.
The primary processing difference is not melt temperature but viscosity and pressure transmission. A 100 g/10 min thin-wall impact grade reaches a longer spiral-flow length at 230 °C and 80 MPa injection pressure than a 18–21 g/10 min controlled-rheology impact grade. On a 1300 kN clamp injection machine with a 1.0 mm nominal wall thickness, the EP548P grade may require a 10–20 °C higher melt temperature or 10–15% greater peak injection pressure to fill the same tool. However, the lower melt-flow grade typically produces less jetting, fewer gate blush defects, and stronger weld lines because molecular orientation at the flow front is less anisotropic. Moulders using hot-runner systems with 0.8 mm valve-gate orifices should set the hot-runner manifold 10–15 °C above the nozzle set-point to prevent premature freeze-off. Published data for this specific configuration is limited; tool trials with pressure-drop sensors are required to transfer settings between machines.
Small-amplitude oscillatory shear under ISO 6721-10 shows that heterophasic copolymers of this type exhibit a broader linear viscoelastic region and higher zero-shear viscosity than a homopolymer of equal MFR. In injection moulding, the practical result is postponed gate freeze-off. Crystallization kinetics, measured by differential scanning calorimetry at 10 °C/min under ISO 11357-1, indicate a polypropylene crystallization peak near 120–125 °C, but the copolymerized rubber phase slows overall solidification. Holding time should be set at 1.5–2.0 s/mm of nominal wall thickness for unfilled material; below this envelope, sink marks and post-mould warpage increase. If a nucleated variant is used, the crystallization peak shifts upward by 5–10 °C, and holding time can be reduced by 15–25% without degrading impact. However, nucleating agents that raise crystallization temperature also increase shrinkage anisotropy; tooling compensation should be verified using ISO 294-4 shrinkage plaques.
Optical performance further separates EP548P from random copolymer grades. On 1 mm injection-moulded plaques, haze values measured under ASTM D1003 typically exceed 60% for the impact copolymer family, while random copolymers can reach below 20%. The difference arises from the dispersed rubber domains, which scatter visible light. Consequently, Moplen EP548P is not specified for transparent packaging or syringe barrels where contact clarity is required. It is specified for pigmented interior automotive trims, appliance housings, and industrial containers where opacity is acceptable and low-temperature ductility is valued. Published data for this specific configuration is limited for glazing applications.
Controlled-rheology production of high-flow grades often uses organic peroxides to narrow molecular weight distribution. This route raises MFR and reduces die swell, but it also creates a low molecular weight fraction that can contribute to volatile organic compounds. For Moplen EP548P, downstream compounders adding peroxide should keep residual active oxygen below 50 mg/kg before pelletizing; otherwise, melt-flow drift during storage can exceed 2 g/10 min. Nucleation packages are sometimes offered in custom compounds to increase stiffness and HDT. A nucleation package based on a sorbitol derivative at 0.15–0.25 wt% can raise flexural modulus by 5–12% and HDT under 0.45 MPa by 8–12 °C. The effect is not free of trade-offs: the same additive can reduce elongation at break by 10–20% and change shrinkage behaviour. Injection moulders should qualify each nucleated lot with ISO 294-4 shrinkage measurements before cutting production tools.
Compared with a homopolymer PP of equal MFR, the EP548P designation indicates a deliberate compositional difference: the presence of ethylene-propylene copolymer raises the notched Izod impact at 23 °C by roughly an order of magnitude but reduces the tensile modulus by 20–35%. Compared with a random copolymer, the stiffness retention is generally higher and the low-temperature impact is better, but the optical clarity is poorer. Compared with a high-flow impact grade in the 50–100 g/10 min MFR class, the lower melt flow of EP548P improves weld-line strength at the expense of spiral-flow length.
| Property and test method | Moplen EP548P typical envelope | Homopolymer PP reference | Random copolymer PP reference |
|---|---|---|---|
| Melt mass-flow rate, ISO 1133-1, 230 °C, 2.16 kg | 18–21 g/10 min | 12–25 g/10 min | 8–25 g/10 min |
| Density, ISO 1183-1 | 0.900 g/cm³ | 0.900–0.910 g/cm³ | 0.895–0.905 g/cm³ |
| Tensile modulus, ISO 527-2 | 1100–1350 MPa | 1500–1800 MPa | 800–1100 MPa |
| Notched Izod 23 °C, ISO 180/A | 20–45 kJ/m² | 2–4 kJ/m² | 5–10 kJ/m² |
| Notched Izod −20 °C, ISO 180/A | 5–10 kJ/m² | 1–2 kJ/m² | 1–3 kJ/m² |
| Haze, 1 mm plaque, ASTM D1003 | >60% | 40–70% | <20% |
Regulatory status depends on the final compound and article. As a polyolefin base resin, Moplen EP548P is generally assessed under FDA 21 CFR 177.1520(c) for olefin polymers in food contact, and under Regulation (EU) No 10/2011 for plastic materials and articles intended to come into contact with food. Both frameworks require migration testing of the final article, not merely the resin. The grade is not exempt from automotive interior emission requirements; OEM specifications derived from VDA 278 often apply when the part is used in a cabin environment. Halogenated flame retardant packages containing antimony trioxide above 5 wt% are not recommended if low-temperature impact retention is required, because the particulate loading shifts the ductile-to-brittle transition upward. Oxidizing acids, strong bleaches, and prolonged exposure to aromatic hydrocarbons can stress-crack moulded parts under load; suitability must be validated under ISO 22088-3 bent-strip environmental stress cracking.
| Regulatory area | Standard / clause | Typical assessment for Moplen EP548P |
|---|---|---|
| US food contact | FDA 21 CFR 177.1520(c) | Olefin polymer class; final article migration testing required |
| EU food contact | Regulation (EU) No 10/2011, Annex I | Compliance determined by migration, not resin alone |
| RoHS | Directive 2011/65/EU, Annex II | No intentionally added restricted metals; verify colourants |
| REACH | Regulation (EC) No 1907/2006 | Registration of monomers and additives required at article level |
| Automotive indoor emission | VDA 278 | Requires low-VOC additive selection; not guaranteed for all lots |