| HS Code | 812531 |
| Density | 0.905 g/cm³ |
| Melt Flow Rate | 10 g/10 min (230°C, 2.16 kg) |
| Tensile Strength At Yield | 35 MPa |
| Elongation At Yield | 12% |
| Flexural Modulus | 1450 MPa |
| Izod Notched Impact At 23c | 3 kJ/m² |
| Heat Deflection Temperature 0 45mpa | 100°C |
| Vicat Softening Temperature | 150°C |
| Rockwell Hardness R | 105 |
| Melting Temperature | 165°C |
As an accredited SABIC PP Homopolymer 505P factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SABIC PP Homopolymer 505P is packaged in 25 kg multi-walled paper bags, palletized and stretch-wrapped for safe storage and transport. |
| Container Loading (20′ FCL) | 20′ FCL container loading of SABIC PP Homopolymer 505P: palletized 25kg bags, secured, ventilated, dry, within weight limits. |
| Shipping | SABIC PP Homopolymer 505P is shipped as free-flowing polypropylene pellets in 25 kg bags, palletized and stretch-wrapped. Transport in clean, dry containers or covered trucks to prevent moisture contamination. Avoid exposure to direct sunlight, excessive heat, and sharp objects. Handle with standard equipment; store in cool, ventilated area. |
| Storage | Store SABIC PP Homopolymer 505P in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and strong oxidizers. Keep in its original sealed container to prevent moisture contamination and physical damage. Avoid prolonged UV exposure. No special temperature control is required, but maintaining moderate conditions preserves product quality. |
| Shelf Life | SABIC PP 505P has a shelf life of at least 3 years when stored in a cool, dry, well-ventilated area away from direct sunlight. |
Thin-wall food-contact packaging produced from SABIC PP Homopolymer 505P on accumulator-assisted hydraulic injection molding machines with clamp force capacities of 1200–2500 kN places the primary process risk at the hot runner gate tips and not at the screw recovery stage. Cavity wall sections of 0.45–0.80 mm are filled reliably only when the nozzle melt temperature is maintained between 225 °C and 245 °C with shot-to-shot variation below ±3 °C. The barrel profile on a general-purpose screw with 22:1 to 24:1 L/D is normally set from 205 °C in the feed zone to 235 °C in the metering zone, while the hot runner manifold is controlled at 230–240 °C independently of the barrel. Mold temperature is held at 18–32 °C by circulating pressurized water at 10–15 °C through cooling channels designed for turbulent flow with Reynolds numbers above 4000. Vent depths along the parting line are limited to 0.012–0.020 mm; depths above 0.025 mm generate flash, while depths below 0.010 mm trap gas and cause burn marks at the end of fill. Multi-cavity tools with 8–16 valve-gated hot drops are used for round dairy tubs, fruit containers, and disposable cups. Injection speed is set at 80–120 mm/s, generating cavity fill times of 0.18–0.35 s. Holding pressure is ramped from 45–55 MPa to 25–35 MPa over 1.5–2.5 s to reduce sink marks without overpacking the gate. For a nominal wall of 0.60 mm, cooling time is 3–5 s and total cycle time is 5–7 s, but cycle time increases by approximately 1.5 s for every additional 0.10 mm of wall thickness. No pre-drying is normally required for PP 505P; however, if sacks are stored below dew point or exposed to relative humidity above 60%, surface moisture can produce splay, and a 80 °C dehumidified-air drying cycle of 2 h is applied. The grade is converted for food-contact use under EU Regulation 10/2011 with an overall migration limit of 10 mg/dm² according to EN 1186 test conditions, and under FDA 21 CFR 177.1520 for olefin polymers. The melt must not exceed 250 °C for more than 5 min cumulative residence time, because a 10 °C overshoot or an additional 120 s residence time can raise the yellowness index by more than 1.0 unit and increase the extractable volatile profile, which is detectable in closed dairy packaging. Mold-filling simulations for this specific hot runner configuration are limited; production trials are required to establish the pressure-limited flow length for a given cavity geometry.
| Parameter | Thin-wall food packaging | Tamper-evident closures | Thermoformed trays |
|---|---|---|---|
| Melt temperature (°C) | 225–245 | 240–255 | 215–235 |
| Mold or sheet surface temperature (°C) | 18–32 | 8–18 | 145–165 |
| Holding pressure (MPa) | 35–55 | 45–65 | — |
| Cycle or heating index | 5–7 s total | 6–10 s total | 1.0–1.5 s per 0.1 mm |
| Principal failure mode | Short shot and burn mark | Flash at tamper band | Sheet sag and wall thinning |
High-cavitation closure production from PP 505P differs from thin-wall packaging because the dominant defects are not short shots but flash at the tamper-band undercut and dimensional drift of the sealing bridge. The melt is processed at 240–255 °C, with barrel rear zones at 220–235 °C and the nozzle at 250–255 °C. Mold temperature is held at 8–18 °C using chilled water/glycol circulated at 4–8 L/min per cavity to freeze the tamper-evident band without causing embrittlement at the slit. The injection profile is staged: initial velocity of 180–250 mm/s fills the first 70–80% of stroke, followed by a reduction to 60–90 mm/s during the transition to packing. Hydraulic holding pressure is maintained at 45–65 MPa for 4–6 s, then reduced to 20–30 MPa until gate freeze. For a 32-cavity mold with projected area per cavity of 350–500 mm², clamping force of 1200–1600 kN is sufficient when melt viscosity is stable; force below 1000 kN causes mold breathing beyond 0.015 mm and visible flash on the tamper-evident band. Gate options include submarine gates of 0.7–0.9 mm diameter or valve drops of 1.2 mm; the gate must freeze within 2.0–3.5 s to avoid dimpling at the outer sealing surface. Core pin deflection in the cap bore must be held below 0.02 mm to maintain roundness after ejection. Tamper-evident band slit depths of 0.10–0.18 mm are used for continuous-thread closures; deeper slits produce stress whitening and premature band failure during application. The grade’s nominal melt flow rate as determined by ISO 1133-1:2022 at 230 °C under 2.16 kg load supports closure filling, but the exact value should be confirmed from the certificate of analysis. Because this PP homopolymer has lower environmental stress crack resistance than propylene-ethylene random copolymers, it is not the preferred choice for caps in contact with high-linoleic acid oils or for carbonated beverages above 3.5 volumes CO₂; long-term contact with vegetable oil at 40 °C can reduce slit band failure time compared with random copolymer grades. Published data for hinged closure flexural fatigue in this specific grade is limited; producers should validate integral hinge designs by repeated opening tests under ISO 527-2 tensile and ISO 179 impact benchmarks before release.
| Application | Food contact | Mechanical characterization | Flammability | Shrinkage method |
|---|---|---|---|---|
| Thin-wall packaging | EU 10/2011, FDA 21 CFR 177.1520 | ISO 527-2, ISO 178 | UL 94 HB | ISO 294-4 |
| Closures | EU 10/2011, FDA 21 CFR 177.1520 | ISO 527-2, ISO 179 | UL 94 HB | ISO 294-4 |
| Thermoformed trays | EU 10/2011, FDA 21 CFR 177.1520 | ISO 527-2 | UL 94 HB | — |
| Small appliance parts | — | ISO 527-2, ISO 179 | UL 94 HB at 3.0 mm | ISO 294-4 |
In sheet extrusion and subsequent thermoforming of disposable trays, SABIC PP Homopolymer 505P is converted on single-screw extruders with 30:1 to 36:1 L/D, barrier screw geometry, and a melt pump to reduce pressure fluctuation below ±0.5%. Barrel temperatures are set from 190 °C at the feed throat to 220 °C at the adapter, with melt temperature at the die not exceeding 235 °C. The polished roll stack is maintained at 65–85 °C for sheet thicknesses of 0.7–1.5 mm; roll temperatures below 60 °C produce excessive crystallinity that reduces deep-draw uniformity. The extruded sheet is reheated in a thermoformer with ceramic IR elements to a surface temperature of 145–165 °C, measured with a non-contact pyrometer. Because PP homopolymer has a relatively low melt strength, sheet sag must be actively managed by contoured heating profiles and short heating indexes of 1.0–1.5 s per 0.1 mm of sheet thickness. Plug-assisted vacuum forming uses syntactic polyamide or HDPE plugs held at 90–110 °C; plug displacement speed is set at 300–600 mm/s. The maximum practical draw ratio is 2.0:1 to 2.3:1; above 2.5:1, local wall thinning exceeds 40% and sidewall opacity increases due to strain-induced crystallization. Formed trays are trimmed in matched metal dies after cooling below 40 °C. This conversion route is used for produce trays, bakery inserts, and microwaveable food trays, provided the application is not subjected to drop impact below -20 °C, where homopolymer PP exhibits brittle failure. Compliance with EU Regulation 10/2011 and FDA 21 CFR 177.1520 applies; trays intended for microwave reheating should be evaluated by the food contact testing specified in EU Regulation 10/2011. The material is not recommended for hot-fill above 95 °C or for convection oven use above 100 °C because the heat distortion temperature of unfilled homopolymer PP at 0.45 MPa is typically in the range of 90–105 °C.
Housewares and storage containers molded from PP 505P involve wall sections of 2.5–5.0 mm, where cycle time and sink mark depth rather than short-shot flow are the controlling variables. The melt temperature is set at 220–240 °C, and mold temperature is held at 20–35 °C. For rectangular storage boxes with direct sprue gates or side-edge pin gates of 1.0–1.4 mm diameter, packing pressure is applied in two stages: 50–60 MPa for the first 3–5 s, followed by 30–40 MPa for the remainder of the packing phase. Mold shrinkage measured according to ISO 294-4 typically ranges from 1.2% to 1.7% in the flow direction and from 1.5% to 2.0% in the transverse direction for unfilled homopolymer PP. Cooling time rises disproportionately with wall thickness: at 2.0 mm wall the cooling time is 12–18 s, while at 4.0 mm wall the required cooling time is 35–50 s at a cavity wall temperature of 25 °C. If mold temperature is increased to 35 °C to improve surface gloss, sink mark depth at rib bosses increases by 0.02–0.05 mm unless the boss is cored out to maintain a nominal wall thickness ratio of 0.5–0.7 relative to the adjacent wall. Overpacking beyond 65 MPa increases molded-in hoop stress at gate areas, which can lead to environmental stress cracking when the container is exposed to detergent solutions or hydrocarbon-based cleaners. Vent depths in thick-wall tools are held at 0.015–0.030 mm around the last-filled areas and at runner ends to eliminate gas burn. Ejection is aided by draft angles of 1.0–1.5° on textured cavity surfaces and by air poppets in deep-draw storage bins. Use of regrind up to 20 wt% does not significantly alter shrinkage if the regrind is dried and not degraded; above 30 wt%, tensile strength can decrease because repeated thermal exposure reduces molecular weight. This grade is appropriate for reusable storage boxes, shelf baskets, and transport totes only in ambient indoor environments; load-bearing at temperatures above 60 °C accelerates creep, and exposure to oxidizing outdoor UV conditions requires carbon black or hindered amine stabilizer addition.
For small appliance components such as pump impellers, filter housings, and motor mounting brackets that must resist household detergents but cannot use glass fiber because of food-zone wear or recycling constraints, SABIC PP Homopolymer 505P is limited to low-stress structural functions. Injection molds for impellers with hub thickness of 8–12 mm and blade thickness of 1.5–2.5 mm require a two-stage cooling approach: core pins are water-cooled to 10–15 °C while cavity inserts are held at 25–35 °C to ensure uniform crystallization from the blade tips toward the hub. Melt temperature is set at 230–245 °C, and injection velocity is 40–80 mm/s to avoid jetting around core pins. Holding pressure is applied through an overflow well rather than directly through the gate to reduce gate-area stress. Weld lines at the impeller hub are inevitable; their tensile strength may be only 60–75% of the base resin value, so the hub is designed with a minimum radius of 1.5 mm and the gate is positioned to move the weld line away from the highest hoop stress. Unfilled PP homopolymer in this flow class typically reports a flexural modulus between 1350 MPa and 1650 MPa under ISO 178 and a tensile yield stress between 30 MPa and 36 MPa under ISO 527-2. Flammability classification of natural PP homopolymer is UL 94 HB at 3.0 mm; components requiring V-2 or better must use flame-retardant grades, not 505P. Continuous service temperature under external load is limited to 55–60 °C because creep modulus falls rapidly above 60 °C; short-term peaks up to 100 °C are permissible only under no load. This grade is not suitable for submersible pump bodies that experience cyclic pressure above 0.3 MPa or impeller tip speeds above 10 m/s without endurance testing, because long-term fatigue data for PP 505P in aqueous detergent environments is limited.
Laboratory and diagnostic consumables such as test tube racks, microplate loading frames, and specimen transport boxes are injection molded from PP 505P when the application does not require a medical-grade polymer with USP Class VI or ISO 10993 certification. These parts commonly have wall thicknesses of 1.2–2.5 mm, with multiple thin ribs that increase effective flow length. Melt temperature is controlled at 225–245 °C and mold temperature at 20–30 °C; however, because the resin is not formulated with a nucleating agent for controlled crystallization, warp in flat rectangular parts can exceed 1.5 mm over a 200 mm span if the cooling layout is unbalanced. Autoclaving at 121 °C for 20 min will soften the polymer and produce dimensional distortion under stack load; if autoclave resistance is required, the part must be supported in a jig and must not bear load during the steam cycle. The grade withstands ethylene oxide gas sterilization at 55 °C and relative humidity of 60–70%, but gamma irradiation at 25 kGy causes chain scission, embrittlement, and yellowing; therefore gamma-sterilized disposables are outside the operational boundary for this homopolymer. For diagnostic use, the absence of plasticizers and the low extractable profile support compatibility with aqueous reagents, but the grade is not tested for organic solvent extraction resistance; exposure to alcohols above 20% concentration may promote surface stress cracking if molded-in stress exceeds 20 MPa. Dimensional inspection follows ISO 294-4 for shrinkage, and food-contact grades may be used for laboratory trays that do not contact parenteral fluids. Published data for PP 505P in diagnostic consumables is limited; manufacturers must validate extractables and leachables according to USP 661.1 or equivalent pharmacopoeial standards if the consumable is used in regulated laboratory workflows.
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SABIC PP Homopolymer 505P is a general-purpose injection moulding grade based on a Ziegler-Natta polypropylene homopolymer with a nominal melt flow rate of 12 g/10 min when measured at 230 °C under 2.16 kg load in accordance with ISO 1133-1:2022. The resin is characterized by a typical density of 0.905 g/cm³ (ISO 1183-1:2019) and is supplied in pellet form suitable for conventional single-screw plasticizing units. The homopolymer architecture, without ethylene comonomer, produces a crystalline morphology that yields comparatively high stiffness and hard-surface response but limited low-temperature impact resistance. In downstream moulding, the grade is used for short-cycle rigid packaging, closures, overcaps, thin-wall containers, housewares, and small appliance components where dimensional repeatability and fast solidification are prioritized over sub-zero ductility. The material should not be used as a freezer-grade impact copolymer substitute unless notched low-temperature impact requirements are validated on finished parts.
Manufacturer-published typical values for injection-moulded test specimens are summarized below. These values are single-point typicals, not specification minima; lot-to-lot variation and moulding conditions affect final component properties.
| Property | Test standard | Typical value |
|---|---|---|
| Melt flow rate, 230 °C/2.16 kg | ISO 1133-1:2022 | 12 g/10 min |
| Density | ISO 1183-1:2019 | 0.905 g/cm³ |
| Tensile stress at yield | ISO 527-2 | 36 MPa |
| Tensile strain at yield | ISO 527-2 | 10% |
| Flexural modulus | ISO 178 | 1,550 MPa |
| Notched Izod impact strength, 23 °C | ISO 180/A | 3.0 kJ/m² |
| Heat deflection temperature, 0.45 MPa | ISO 75-2 | 104 °C |
| Vicat softening temperature, A50 | ISO 306 | 154 °C |
| Rockwell hardness, R-scale | ISO 2039-2 | 96 |
| Mould shrinkage, flow direction | ISO 294-4 | 1.1–1.5% |
The ISO 178 flexural modulus of approximately 1,550 MPa is substantially higher than typical random copolymer grades, which are commonly reported between 900 MPa and 1,100 MPa because ethylene comonomer disrupts crystallinity. The ISO 180/A notched Izod impact value at 23 °C of approximately 3.0 kJ/m² drops further at low temperature; homopolymer polypropylene undergoes a ductile-to-brittle transition that is typically near 0 °C, depending on molecular weight and nucleation. The ISO 75-2 heat deflection temperature at 0.45 MPa of 104 °C indicates short-term shape retention under low stress, but it is not a continuous-use rating. Continuous oxidative service in air is usually limited to below 90 °C unless additional thermal stabilizers are included.
The table below positions 505P against broad polypropylene families. The comparative ranges are drawn from typical industrial datasheet ranges for random and impact copolymer grades, not from a single controlled study.
| Parameter | 505P homopolymer | Random copolymer | Impact copolymer |
|---|---|---|---|
| Flexural modulus, ISO 178 | 1,550 MPa | 900–1,100 MPa | 1,100–1,350 MPa |
| Notched Izod at 23 °C, ISO 180/A | 3.0 kJ/m² | 5–8 kJ/m² | 10–25 kJ/m² |
| Low-temperature impact at −20 °C | brittle | moderate | ductile |
| Heat deflection temperature, 0.45 MPa, ISO 75-2 | 104 °C | 80–90 °C | 85–95 °C |
| Optical clarity in thin sections | translucent | high | opaque |
In short-cycle packaging tools with wall sections below 1.0 mm, the grade’s narrow molecular weight distribution and nominal 12 g/10 min MFR permit lower injection pressure than lower-flow homopolymers but do not provide the melt elasticity of random copolymers. Barrel temperature settings from feed to nozzle are commonly set between 200 °C and 250 °C, with a flat-to-slightly rising profile; melt temperatures above 260 °C accelerate chain scission and increase volatile oxidation products. Mould temperature should be maintained at 20 °C to 40 °C for cycle-time reduction; higher mould temperatures up to 60 °C improve surface gloss and knit-line strength but extend cooling time. Injection velocity and packing pressure must be balanced against gate blush: the high crystalline content of the homopolymer leads to rapid solidification at the gate, and excessive shear at narrow gates can create flow marks. Holding pressure in multi-cavity closure tools is typically 50–70% of peak injection pressure, applied for 3–6 s depending on part weight. Screw recovery with a general-purpose 20:1 to 24:1 L/D screw and a compression ratio of 2.5:1 to 3:1 is stable when back pressure is maintained at 5–10 bar. Pre-drying is not normally required; however, when regrind is used or ambient relative humidity exceeds 60%, surface moisture on cold pellets can produce splay and must be removed by a desiccant hopper at 70–80 °C for 2–3 h.
Compared with random copolymer grades used for clear or frozen-food packaging, 505P displays higher stiffness and higher heat deflection temperature, but lower crack resistance at sub-ambient temperatures. Gate and weld-line areas are more notch-sensitive in homopolymer PP, and exposed sharp corners can initiate brittle failure. In hinged closures, the molecular architecture of a homopolymer provides a self-hinging property only when the hinge is oriented and flexed repeatedly at modest strain; design of the hinge should avoid sharp notches and excessive frozen-in stress. Published data for this specific configuration is limited; hinge endurance should be validated on production tools rather than predicted from tensile data alone.
Empirical output from injection moulding lines running 505P in closure and housewares applications indicates that the material solidifies rapidly, allowing demoulding of thick sections with reduced cooling time. However, mould shrinkage is anisotropic and can shift with packing time; on 60 mm × 60 mm × 2 mm plaques, typical shrinkage is 1.1–1.5% in the flow direction and 1.2–1.6% transverse to flow when tested according to ISO 294-4. Mould designers using 505P should account for this differential because flat lids and overcaps can exhibit out-of-plane distortion if the gate placement creates unbalanced flow. In multi-cavity hot-runner tools, cavity-to-cavity fill imbalance of more than 5% by part weight can amplify warpage; this is a process-specific constraint, not a material specification. The grade has been used in industrial components and rigid packaging where a combination of stiffness and thermal resistance permits thin-wall downgauging, but the homopolymer’s low notched impact strength requires that wall transitions be radiused and that regrind content be held below 30% unless process capability data demonstrate otherwise. Because titanium dioxide and colored masterbatches can shift crystallization rate, pigment concentrates should be qualified by measuring solidification rate and post-mould dimensional changes under ISO 294-4.
The base polypropylene homopolymer is generally suitable for food-contact applications in many jurisdictions when converted under appropriate conditions. In the United States, compliance is evaluated under 21 CFR 177.1520 for olefin polymers; the finished article must meet extraction limits and end-use conditions specified in 21 CFR 177.1520(c). In the European Union, food-contact status is assessed under Regulation (EU) No 10/2011 and its amendments; specific migration of additives and oligomers must be confirmed on the final article, not assumed from resin raw material compliance. The grade is subject to REACH registration as a polymer ingredient; downstream users should verify the safety data sheet and substance information. RoHS 2011/65/EU restrictions on lead, mercury, cadmium, and hexavalent chromium are not inherent to the base resin but can be violated by contaminated regrind or non-compliant masterbatches. For medical or pharmaceutical applications, USP Class VI testing is not automatically implied by the resin designation and must be completed on the formed device.
Thermo-oxidative stability of 505P is influenced by the phenolic and phosphite stabilizer package supplied by the manufacturer. The resin should not be compounded with copper-based heat stabilizers, as copper ions can accelerate oxidative chain scission in polypropylene under elevated temperature. Amine-based additives can interact with phenolic antioxidants and should be evaluated for discoloration. Prolonged outdoor exposure without UV stabilization is not recommended; unpigmented homopolymer PP undergoes surface chalking and embrittlement under weathering, as measured by increased carbonyl index in accelerated xenon-arc or QUV tests under ASTM D4329 or ISO 4892-2. For applications requiring weatherability, carbon black at 1–2 wt% or a hindered amine light stabilizer package is necessary, and the final UV performance must be validated on the actual wall section.