| HS Code | 714057 |
| Density | 0.90 g/cm³ |
| Melt Flow Rate | 15 g/10 min (230°C, 2.16 kg) |
| Tensile Strength At Yield | 35 MPa |
| Elongation At Break | 100% |
| Flexural Modulus | 1450 MPa |
| Izod Impact Strength Notched 23 C | 40 J/m |
| Heat Deflection Temperature | 105 °C |
| Vicat Softening Temperature | 150 °C |
| Rockwell Hardness | R-100 |
| Mold Shrinkage | 1.5% |
As an accredited YUNGSOX PP 3015 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | YUNGSOX PP 3015 is packaged as polypropylene pellets in 25 kg woven bags, palletized and shrink-wrapped for safe transport. |
| Container Loading (20′ FCL) | YUNGSOX PP 3015 loaded in 20′ FCL, packed in 25kg woven bags, palletized and secured for safe, dry transport. |
| Shipping | YUNGSOX PP 3015 is a polypropylene resin supplied as solid pellets. Ship in clean, dry containers or bags, protected from moisture, direct sunlight, and excessive heat. No special hazardous-materials classification applies, but avoid dust accumulation and handling near ignition sources. Keep packaging sealed and store in a well-ventilated area. |
| Storage | Store YUNGSOX PP 3015 in a cool, dry, well-ventilated area, away from heat, open flames, strong oxidizers, and direct sunlight. Keep containers tightly closed to prevent contamination and moisture pickup. Avoid static discharge and mechanical damage. Follow local regulations; no special temperature control is required under normal conditions. |
| Shelf Life | Store in a cool, dry place away from sunlight. Shelf life is two years from date of manufacture. |
YUNGSOX PP 3015 is a low-flow random copolymer polypropylene with a nominal melt flow rate of 1.5 g/10 min at 230 °C under 2.16 kg load, measured in accordance with ISO 1133-1:2022. The random comonomer distribution lowers crystallinity and melting point relative to PP homopolymer, which widens the thermoforming temperature window and improves contact clarity in thick sections. Processing temperatures are lower than those used for homopolymer grades; stable melt homogeneity is generally obtained between 190 °C and 230 °C, while degradation accelerates above 260 °C through chain scission and discoloration. Moisture on cold pellet surfaces should be removed at 80 °C for 2 h when storage relative humidity has exceeded 80 %. The grade is not hygroscopic, but retained surface moisture can produce splay in clear sheet and bottle flashing.
Clear extruded sheet for thermoformed packaging uses this grade for rigid packs where PET clarity is not required but low-temperature impact resistance and flex-cracking resistance are essential. Sheet lines typically run a single-screw extruder with an L/D of 30:1 to 36:1, a barrier screw, and an adapter temperature set no higher than 230 °C. The flat die is maintained at 210 °C to 230 °C, and the three-roll polishing stack is operated with roll temperatures between 30 °C and 60 °C to balance haze and sheet flatness. For random copolymer PP, excessive chill roll temperature above 70 °C can create visible flow marks and increase sheet surface tack; roll gaps must be adjusted to a nip pressure just sufficient to exclude air, because over-compression creates transverse thickness variation. Plug-assisted forming is performed at sheet surface temperatures of 150 °C to 165 °C, lower than homopolymer PP due to the reduced crystalline melting point. Positive forming with a heated aluminum plug at 95 °C to 115 °C controls wall thinning in tray corners to no more than 25 % of nominal sheet thickness. Finished articles include clear deli containers, portion cups, and protective packaging closures; food-contact confirmation is governed by FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011, subject to additive formulation and final-article migration testing.
| Reference | Application scope | Required verification |
|---|---|---|
| FDA 21 CFR 177.1520 | Food-contact trays and containers | Olefin polymer composition and additive limits |
| EU Regulation (EU) No 10/2011 | Food-contact trays and films | Overall migration limit of 10 mg/dm²; specific migration for additives |
| REACH Regulation (EC) No 1907/2006 | All exported articles | SVHC declaration for Candidate List substances |
| RoHS Directive 2011/65/EU | Electronics-handling trays | Pb, Cd, Hg, Cr VI, PBB, PBDE concentrations below thresholds |
| IEC 61340-2-3:2024 | Static-dissipative sheet | Surface resistivity after 48 h at 23 °C and 12 % RH |
In extrusion blow moulding, the low MFR of PP 3015 reduces parison sag and permits intermittent parison drop lengths above 400 mm without excessive wall thinning. Die temperatures between 195 °C and 215 °C are used, which is lower than for translucent homopolymer PP; elevated die temperatures above 220 °C accelerate melt oxidation and create yellowing in the flash regrind stream. The blow mold is cooled to 20 °C to 35 °C and blow pressure is set between 0.6 MPa and 0.8 MPa. Contact clarity is controlled by the quench rate of the inflated parison; a slow cooling rate increases spherulite size and haze, while very rapid cooling can introduce residual stress that reduces drop impact at 4 °C. Bottles should be tested for drop impact after conditioning at 4 °C for 24 h using ASTM D2463-15. Applications include transparent containers for personal-care packing and non-sterile liquid pharmaceutical packaging; no medical-grade claim is made without USP Class VI or ISO 10993 testing of the finished container.
For cast film and sheet used on horizontal or vertical form-fill-seal machines, the random copolymer chain structure lowers the heat seal initiation temperature compared with PP homopolymer. Seal strength is evaluated after jaw temperature profiling; a typical starting window is 130 °C to 150 °C for 0.5 mm thick rigid film, with dwell time of 0.8 s to 1.2 s at 0.3 MPa sealing pressure. The grade’s low MFR makes it suitable for thick monolayer film above 250 µm where cast film lines can still sustain edge stability; thin-gauge high-output lines may require a higher-flow skin layer to avoid melt fracture. Hot-tack strength is measured under ASTM F1921-18, and the seal initiation temperature should be recorded for each batch because comonomer content affects sealing behavior. Terminal products include single-serve thermoformed lidding, transparent pack inserts, and form-fill-seal base web for non-sterile medical devices. Oxygen barrier is not a property of PP; when extended shelf life is specified, a multilayer structure with EVOH or PVdC is required rather than a thicker PP monolayer.
Transparent stationery sheet and folder stock extruded from PP 3015 is die-cut and creased into ring binder panels, file folders, and presentation covers. The sheet is extruded at a die temperature of 210 °C to 230 °C and passed through a vertical three-roll stack with a patterned or polished roll; polished rolls produce gloss values above 85 GU at 60° under ASTM D2457-19 on 0.8 mm sheet. The random copolymer gives better hinge life than general-purpose PS or PVC sheet when repeated folding is required; hinge durability is evaluated by fold cycling under a fixed load of 500 g until cracking exceeds 1 mm. Because PVC and PS sheet have higher stiffness per unit thickness, PP folder stock is typically extended by 0.1 mm to 0.2 mm to match tab rigidity. Die-cutting requires sharp edges with a clearance of 3 % of sheet thickness to avoid white stress marks in the fold line; creasing bars heated to 60 °C to 80 °C reduce surface rupture. The material accepts screen and UV offset inks only after surface oxidation; inline corona treatment at 42 mN/m to 46 mN/m is recommended, with dyne level verified by ISO 8296:2022. Finished products include archival stationery and punched file covers; archival stability requires pH-neutral paper contact and no plasticizer migration.
Because PP 3015 is substituted for PET in transparent deli trays and chilled-food packs, the comparison must account for lower flexural modulus, higher oxygen transmission, and better low-temperature impact. For a nominal wall thickness of 0.6 mm, tensile modulus in PP is approximately 1.0 GPa to 1.2 GPa, while PET sheet typically exceeds 2.0 GPa; tray sidewall ribbing must therefore be added to preserve stacking strength. Drop tests at 4 °C after 24 h conditioning are performed using ASTM D2463-15 or an internal bruise-height protocol; PP can sustain a higher drop count without corner cracking, but the advantage is lost if the tray is embossed with sharp cold-forming features. The substitution is valid only for chilled distribution below 10 °C; PP is not suitable for retort or autoclave cycles above 120 °C because wall softening and dimensional distortion become unacceptable. Food-contact compliance under EU Regulation (EU) No 10/2011 must be re-verified after the addition of anti-fog and slip masterbatches; these additives migrate to the surface and may alter overall migration results.
The low MFR of PP 3015 limits its use in high-cavity injection blow moulding, but it can be run on single-cavity and two-cavity machines with heated manifolds. Preform injection temperatures are held between 210 °C and 225 °C at the nozzle; lower temperatures produce flow lines and knit-line weakness at the gate, while higher temperatures extend cycle time and may cause gate stringing. The core rod temperature is controlled in the range 90 °C to 120 °C, which promotes uniform wall distribution during the blow stage because the polymer layer adjacent to the core remains above the softening point. Mold temperature is set at 20 °C to 40 °C, and blow air pressure is maintained at 0.7 MPa to 0.9 MPa. Products include small clear packaging bottles with snap-on cap finishes where a heavier base push-up is required due to the lower parison melt strength compared with high-flow grades. Dimensional stability of the bottle finish is verified by top-load testing under ASTM D2659-16 after 48 h at 40 °C. Published data for this specific configuration is limited; converters should validate preform weight dispersion to ±0.5 % before committing to production tooling.
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YUNGSOX PP 3015 is a heterophasic polypropylene impact copolymer supplied in pellet form for injection moulding and thin-wall component production. The grade is positioned at a nominal melt mass-flow rate of 15 g/10 min when determined at 230 °C under a 2.16 kg load according to ASTM D1238-20, with a nominal density of 0.90 g/cm³ per ASTM D1505-18. The polymer architecture combines a continuous polypropylene matrix with a dispersed ethylene-propylene rubber phase, which raises notched impact resistance relative to homopolymer grades while retaining a portion of the tensile stiffness of a comparable-flow homopolymer. Applications reported for this grade include automotive interior trim, battery housings, appliance structural panels, and reusable transport packaging where low-temperature ductility after injection moulding is required. The product is supplied with a standard heat-stabilisation package; specific lot-to-lot property values are disclosed in producer certificates of analysis and should not be inferred from typical data sheets alone.
| Property | Test Method | Published Typical Range |
|---|---|---|
| Melt mass-flow rate | ASTM D1238-20 at 230 °C/2.16 kg | 15 g/10 min |
| Density | ASTM D1505-18 | 0.90 g/cm³ |
| Tensile stress at yield | ASTM D638-14 | 24–26 MPa |
| Elongation at yield | ASTM D638-14 | 5–7% |
| Flexural modulus | ISO 178:2019 | 900–1100 MPa |
| Notched Izod impact at 23 °C | ISO 180/A | 6.0–8.0 kJ/m² |
| Heat deflection temperature at 0.45 MPa | ISO 75-2/B | 80–90 °C |
| Mould shrinkage, flow direction | ASTM D955-21 | 0.9–1.2% |
Indicative values are for injection-moulded specimens conditioned according to the cited methods; they are not lot acceptance limits and are superseded by the producer’s current technical data sheet.
Compared with a homopolymer of equivalent melt flow at 230 °C/2.16 kg, the heterophasic structure shifts the fracture mechanism from brittle craze-dominated failure toward shear-yield deformation within the rubber domains. This shift is reflected in notched Izod values typically reported by producer literature as 6.0–8.0 kJ/m² at 23 °C under ISO 180/A, whereas a homopolymer of similar flow commonly exhibits 1.5–2.5 kJ/m² under the same condition. The trade-off is a reduction in flexural modulus, typically 900–1100 MPa by ISO 178:2019, compared with 1400–1600 MPa for selected homopolymer grades. The higher rubber content also lowers the heat deflection temperature under 0.45 MPa load to approximately 80–90 °C by ISO 75-2/B, which limits continuous structural use above this boundary unless the part is redesigned with ribbing or filled polymer alternatives.
Processing of YUNGSOX PP 3015 on hydraulic or electric reciprocating-screw injection moulding machines with a screw L/D ratio of 20:1 to 24:1 is appropriate for this melt flow class. The recommended melt temperature window is 220–240 °C; a flat-to-reverse barrel profile from 180 °C in the feed zone to 230 °C at the metering zone is typical for high-flow impact copolymers. Mould wall temperature should be held at 20–50 °C. Lower temperatures increase frozen-in orientation and reduce core ductility; higher temperatures extend cycle time and increase sink-mark tendency. Because the melt flow index places the grade in a medium-high flow band, injection pressures for thin-wall sections of 1.2–2.0 mm typically fall in the 50–80 MPa specific injection pressure range on machines with clamp force capacities from 1200 kN upward. Back pressure should not exceed 10–15 bar to limit shear heating and molecular weight loss.
Although polypropylene is not hygroscopic, surface condensation should be removed by drying at 80 °C for 2 h when pellets stored at relative humidity above 60% show visible surface moisture. Melt residence time above 5 min should be avoided because thermo-oxidative chain scission increases melt flow and reduces toughness. On a 1200 kN clamp-force injection moulding machine producing a battery tray with nominal side-wall thickness of 2.5 mm, gate freeze time is typically 6–8 s; reducing hold time below gate freeze time produces sink marks and internal voids. Screw cushion should be maintained at 3–6 mm to ensure consistent packing pressure transfer into the cavity.
In multi-cavity hot-runner tools producing thin-walled containers, gate-vestige quality and core deflection on long cores are controlled by sequencing of injection velocity and pack pressure. Differential shrinkage between flow and cross-flow directions in this grade can produce post-mould warpage if cavity filling is unbalanced. Mould-filling simulation should use producer-supplied Cross-WLF viscosity coefficients and PVT data rather than single-point melt flow rate values. Published data for shrinkage anisotropy under variothermal mould conditions is limited; tool trials with pressure transducer monitoring are required for parts with flatness tolerances below 0.5 mm.
Substitution of ABS in non-cosmetic structural applications may reduce part mass by 5–10% at equivalent wall thickness because polypropylene density is 0.90 g/cm³ compared with 1.04–1.07 g/cm³ for standard ABS grades. However, the flexural modulus of YUNGSOX PP 3015 is approximately 50–60% that of a standard ABS grade, requiring rib reinforcement or wall thickness increases of 15–20% to maintain stiffness. The PP grade has better resistance to stress cracking in alkaline media than ABS but lower resistance to UV exposure without carbon black or hindered amine stabiliser systems. Long-term UV exposure should be validated under ISO 4892-2; unpigmented natural resin is not recommended for outdoor service beyond 6–12 months depending on part design and additive loading.
Processability differences are also material to substitution. ABS requires pre-drying and is more sensitive to splay from retained moisture, whereas PP 3015 can be processed with no pre-drying under normal indoor storage. The lower melt processing temperature of PP reduces barrel heater energy consumption but increases sensitivity to part ejection marks because the semi-crystalline matrix shrinks more than amorphous ABS. Tool draft angles should be increased to 1.0–1.5° for textured sidewalls, and ejector area should be enlarged by approximately 15% relative to an ABS tool to prevent surface deformation.
Assessing low-temperature performance of YUNGSOX PP 3015 requires instrumented puncture testing rather than single-point notched Izod values when the component carries impact loads below 0 °C. The heterophasic composition delays ductile-to-brittle transition, but the exact transition temperature depends on test speed and local rubber particle size distribution. At −20 °C, notched impact retention can decline to 30–50% of the 23 °C value, and weld-line regions may show a further reduction of 20–40% because of unfavourable orientation of the dispersed rubber phase. Published data for this specific configuration is limited; therefore, a design allowables programme following ISO 179-1 and ISO 6603-2 is required for load-bearing parts.
Moulded-in weld lines in battery housings and automotive trim are particularly susceptible to low-temperature embrittlement when the melt front temperature falls below 210 °C. Flow leaders, sequential valve gating, or local heating of the tool surface can move the weld line away from stressed regions. If the part must be welded by hot plate or linear vibration methods, joint strength retention should be verified in accordance with ISO 15877 or the relevant segment of ISO 19095, because the rubber phase can migrate to the weld interface and reduce local bonding.
Steam sterilisation at 121 °C for 20 min is generally below the melting temperature of polypropylene but above the 0.45 MPa heat deflection temperature of this grade. Under autoclave conditions, unsupported walls can deform under load, and the rubber phase may undergo post-crystallisation shrinkage of 0.2–0.5% over repeated cycles. Published data for repeated autoclave exposure of this specific grade is limited; therefore, validation under ISO 17665-1 with the actual part geometry and stacking load is necessary before medical device use. Gamma sterilisation at 25–50 kGy can cause chain scission in unstabilised polypropylene, leading to embrittlement and colour shift. If YUNGSOX PP 3015 is contemplated for radiation-sterilised applications, the producer’s stabilisation certificate and post-irradiation tensile tests per ASTM D638-14 are required.
Chemical contact with strong oxidising acids, halogenated solvents at elevated temperatures, or long-chain aliphatic oils can reduce molecular weight and initiate surface crazing. The material is not recommended for continuous contact with chromic acid or fuming nitric acid above 40 °C. For food-contact applications, the grade should be verified against FDA 21 CFR 177.1520 for olefin polymers, including extraction tests with food-simulating solvents as specified by the producer’s regulatory certificate.
| Regulatory Area | Method or Clause | Verification Basis |
|---|---|---|
| EU RoHS 2011/65/EU | IEC 62321-5:2013, IEC 62321-7-1:2015 | Producer compliance statement or lot analysis |
| REACH SVHC | Article 33 candidate list screening | Producer regulatory certificate |
| US food contact | FDA 21 CFR 177.1520 | Extraction test data from producer |
| Flammability class | UL 94 HB or V-2 with additive package | UL yellow card classification |
Each converter is responsible for verifying that the final component meets applicable end-market requirements under the specific processing conditions used.