| HS Code | 802900 |
| Density | 0.905 g/cm³ |
| Melt Flow Rate 230 C 2 16kg | 35 g/10min |
| Tensile Strength At Yield | 34 MPa |
| Elongation At Yield | 10% |
| Flexural Modulus | 1600 MPa |
| Charpy Impact Notched 23 C | 4 kJ/m² |
| Vicat Softening Temperature | 155°C |
| Heat Deflection Temperature 0 45 Mpa | 100°C |
| Heat Deflection Temperature 1 8 Mpa | 60°C |
| Rockwell Hardness | R110 |
As an accredited SABIC PP 520L factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SABIC PP 520L is supplied in 25 kg polyethylene-lined paper bags, palletized and shrink-wrapped for safe transport and storage. |
| Container Loading (20′ FCL) | 20′ FCL container loading of SABIC PP 520L: polypropylene resin packed in 25kg bags, palletized for secure, efficient transport. |
| Shipping | SABIC PP 520L is a polypropylene resin typically shipped in sealed, moisture-proof bags or bulk containers. Protect from direct sunlight, excessive heat, and mechanical damage. Ensure dry, ventilated transport to prevent contamination. No special hazard classification applies under standard conditions, but proper handling and secure loading are essential. |
| Storage | Store SABIC PP 520L in a clean, dry, well-ventilated area, preferably away from direct sunlight, ignition sources, and excessive heat. Keep packaging sealed to prevent moisture uptake and contamination. Avoid storing near strong oxidizing agents. Maintain moderate warehouse temperatures, and handle using proper static-control procedures to minimize dust and resin degradation. |
| Shelf Life | Shelf life is indefinite when stored in original, unopened containers under dry, cool conditions away from heat and UV light. |
In extruded sheet lines running 0.8–2.5 mm gauge polypropylene for cold-filled dairy cups and deli trays, SABIC PP 520L is processed on single-screw extruders with L/D ≥ 30:1, barrier screws, and screen changers at melt temperatures of 200–240 °C, while die temperatures are held within ±3 °C across widths of 1,200–1,600 mm. Melt pressure before the breaker plate typically falls between 8–14 MPa; chill roll temperatures are staged at 25–40 °C for the first roll and 45–60 °C for subsequent rolls to balance haze development against sheet stiffness. At start-up, 100 wt% virgin SABIC PP 520L is used to establish the process window, after which closed-loop regrind may be added at ≤ 20 wt% provided the regrind fraction is withdrawn from edge trim of the same production lot and screened through a 3.0 mm mesh to avoid gel contamination. Antistatic masterbatch is metered at 0.5–1.5 wt% only for dry-fill packaging lines, and slip/antiblock concentrates are limited to 1–2 wt% when nested trays require denesting; higher slip levels reduce seal initiation temperature during lidstock welding below 135 °C. The sheet is then thermoformed on contact-plate or plug-assisted machines with core sheet temperatures of 145–160 °C, plug pressure of 0.35–0.55 MPa, and cavity vacuum of −0.06 to −0.08 MPa. Terminal products include 125–500 mL dairy portion cups, rectangular deli trays with draw ratios up to 2.0:1, fruit punnets, and tubs for spreads. On production-scale lines, a batch shift of ±0.2 g/10 min in MFR is normally absorbed by adjusting screw speed by ±8 %; exceeding this without recalibrating melt pressure can produce edge-thick sheet and plug mark cracking in rectangular trays. Compliance for direct food contact is established under FDA 21 CFR 177.1520(c) 1.1a, EU Regulation 10/2011 as amended by Regulation (EU) 2020/1245, and GB 4806.6-2016, with total migration below 10 mg/dm² in dairy simulant D1. The grade is not recommended for hot-fill operations above 95 °C because sheet distortion and shrinkage can exceed 3 % under sustained thermal load.
| Jurisdiction | Standard/Code | Relevant Clause/Method | Limit/Condition |
|---|---|---|---|
| USA | FDA 21 CFR 177.1520(c) 1.1a | Olefin polymer food contact | Polypropylene homopolymer; total migration below 10 mg/dm² |
| EU | EU Regulation 10/2011 as amended by 2020/1245 | Plastics food contact materials | Total migration below 10 mg/dm²; SML for additives if present |
| China | GB 4806.6-2016 | Food contact polypropylene | Total migration below 10 mg/dm² under specified simulants |
| REACH | REACH (EC) No 1907/2006 | Article 33 SVHC communication | SVHC below 0.1 wt% per article |
| RoHS | 2011/65/EU Annex II | Restricted substances | Pb, Hg, Cr(VI), PBB, PBDE each below 0.1 wt%; Cd below 0.01 wt% |
Accumulator-head extrusion blow moulding of 250 mL–5 L industrial and agrochemical containers with SABIC PP 520L uses a melt temperature of 190–210 °C, below the typical 230 °C injection moulding window, because the 2.0 g/10 min nominal MFR measured under ISO 1133-1:2022 produces a melt that resists parison sag but still accumulates head pressure ahead of the die at 8–12 MPa. Tooling is specified with a divergent mandrel angle between 20° and 30°, a die gap of 0.8–1.2 mm, and a parison programming profile with 30–70 points to redistribute thickness before the mould closes under clamp force of 300–800 kN. Blow air enters at 0.4–0.7 MPa, and mould temperatures are held at 20–40 °C to accelerate solidification without freezing weld lines at pinch-off zones. The formulation uses 100 wt% virgin PP 520L at start-up, then permits ≤ 25 wt% clean in-house regrind from the same container family; colour concentrate is metered at 1–3 wt%, while UV stabilizer masterbatch is added at 0.2–0.5 wt% only for containers stored outdoors for more than 12 months. Terminal products include 250 mL–5 L agrochemical jugs, industrial solvent bottles, automotive care containers, and drain trays. For dangerous goods packagings, certification is performance-based under ADR/RID 6.1 and UN Model Regulations Chapter 6.1, requiring drop, leakproofness, and stack tests on filled containers at −18 °C and 40 °C; the homopolymer grade can be used only if the specific solvent formulation is shown not to cause environmental stress cracking. Published data for PP 520L in oxidizer-suspension packaging is limited, so compatibility testing under 49 CFR 178.603 is required before qualification.
In cast film production of 80–200 µm unoriented polypropylene for stationery, label base films, and interleaving, SABIC PP 520L is run at melt temperatures of 220–260 °C through coat-hanger dies with a die gap of 0.5–1.0 mm and an air gap of 20–40 mm. The melt flow rate of 2.0 g/10 min under ISO 1133-1:2022 creates die pressures in the range of 10–16 MPa, which limits maximum stable line speed to 80–150 m/min depending on final gauge; edge necking becomes the controlling defect below 80 µm. Chill roll temperatures of 18–30 °C are used to reduce beta-crystal haze, but roll temperatures below 12 °C lower clarity and increase static charge. The formulation starts at 100 wt% virgin PP 520L; anti-block masterbatch is added at 1–3 wt% for stacking films, and slip concentrate is restricted to ≤ 0.3 wt% because higher slip migration can reduce corona-treated surface energy. Corona treatment on the casting line is set to 38–42 mN/m, and surface energy must be rechecked after 24 h because decay of 2–4 mN/m compromises water-based flexo adhesion on label substrates. Terminal products include page protector films, document sleeves, label facestock base, and non-food interleaving. For food contact label films, compliance is evaluated under EU Regulation 10/2011 and FDA 21 CFR 177.1520(c) 1.1a; total migration must remain below 10 mg/dm². This grade is not intended for high-ratio BOPP tenter lines, where MFR below 3.0 g/10 min can generate excessive stretching forces and uneven thickness; published data for PP 520L on biaxially oriented lines is limited.
Along single-screw extrusion lines with grooved feed sections and L/D 30:1–38:1, SABIC PP 520L is formed into solid-wall and twin-wall industrial drainage pipe at melt temperatures of 200–230 °C and screw speeds of 15–25 rpm. The melt is fed into spiral mandrel or spider-type pipe dies sized 10–200 mm, followed by vacuum calibration at −0.02 to −0.05 MPa and cooling water staged from 20–40 °C to maintain dimensional tolerance according to ISO 15494 and EN 1852 for plastics piping systems in soil, waste, and industrial drainage. Formulation is 100 wt% virgin PP 520L for initial sizing; 2.0–2.5 wt% carbon black masterbatch is added when outdoor UV resistance is required, but the masterbatch let-down must be pre-dried at 80 °C for 4 h if stored outside sealed bags, because free moisture above 0.05 wt% causes surface pitting in the calibration sleeve. Terminal products include acid-waste laboratory drainage lines, chemical process area gravity drains, ventilation ducts, and cable duct spacers. Compliance for chemical resistance is assessed by immersion testing under ISO 175 for the specific electrolyte or waste stream; PP-H materials are generally resistant to dilute alkalis and acids but not to > 40 % sulfuric acid at 60 °C or to aromatic solvents. Continuous service temperature should not exceed 80 °C for load-bearing pressure-free drainage, and the grade is not rated for pressurized potable water piping under ISO 15874, which is a property of PP-R grades.
When hot gas welding of PP-H chemical process tanks and ductwork requires a melt-stable welding rod, SABIC PP 520L is extruded into 3 mm, 4 mm, and 5 mm round-profile rods at 200–220 °C melt temperature using a single-screw rod line with melt pump pressure of 10–14 MPa and a water bath at 30–50 °C. The rod is used at 100 wt% virgin material without filler or colour concentrate, because pigment and talc agglomerates change hot-gas weld viscosity and create leak paths in double-V butt welds. Hot-gas welding parameters are set to an electronically controlled gas temperature of 240–280 °C, gas flow of 40–60 L/min, and travel speed of 0.10–0.20 m/min; nitrogen is preferred over air when oxidizing conditions produce surface degradation visible as yellowing at the weld root. Weld factor tests according to DVS 2205-1 and DVS 2207-1 require short-term tensile weld factors above 0.6 and bend angles above 90° on 10 mm thick test plates; production welds on 8–20 mm sheet must pass vacuum box testing at −0.03 MPa and spark testing at 15–25 kV. Terminal products include polypropylene tank linings for dilute acid storage, scrubber housings, fume extraction ductwork, and field repair of extruded pipe. The maximum continuous service temperature for welded structures is 80 °C, and the material is not suitable for oxidizing acids such as nitric acid above 20 % at 40 °C or for aromatic hydrocarbon service.
For oriented strapping lines producing 5–16 mm wide polypropylene strap, SABIC PP 520L is extruded through a flat die at 220–250 °C, quenched on a water-cooled casting roll at 20–30 °C, slit to width, and then drawn in a hot-air oven at 120–150 °C to a draw ratio of 6:1–12:1. The tensile strength after orientation measured according to ASTM D3950 is typically 180–250 MPa, while elongation at break falls to 15–25 %; this is below PET strapping but sufficient for pallet bundling and carton closure. The formulation uses 100 wt% virgin PP 520L at start-up, with 1–3 wt% colour masterbatch for brand identification; recycled PP strap content is limited to ≤ 10 wt% because higher levels introduce gels that break at embossing points. Compliance for non-contact food bundling is based on FDA 21 CFR 177.1520(c) 1.1a and EU Regulation 10/2011 when the strap is not intended to contact food directly; the strapping must be separated from unwrapped food by primary packaging. Terminal products include pallet strapping for export crates, coil bundle strapping, carton closure, and non-contact bundling of beverage multipacks. Process limitations are defined by draw resonance at ratios above 12:1 and by surface embossing defects when melt temperature exceeds 250 °C for more than 5 min residence time. Published data for PP 520L in high-tension steel coil strapping is limited, and substitution for PET is not recommended where retained strap tension above 4,500 N is required after 72 h at 60 °C.
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SABIC PP 520L is an unfilled polypropylene homopolymer supplied by SABIC and positioned for injection-molding operations that require high melt flow, thin-wall filling, and reduced cooling time. The grade is available in pellet form and is processed on conventional single-screw injection-molding machines with general-purpose polyolefin screws. Its nominal melt flow rate is 25 g/10 min when measured according to ISO 1133-1:2022 at 230 °C and 2.16 kg, placing it among the higher-flow homopolymer grades in the SABIC PP portfolio. The high-flow characteristics are reflected in lower melt viscosity under shear, which reduces filling resistance in thin sections and permits shorter holding-pressure times relative to lower-flow homopolymer grades.
The grade is not intended for extrusion blow molding, cast film, or foamed sheet where melt strength and extensional viscosity are controlling factors. Its lower molecular weight and reduced elastic memory make it suitable for high-speed injection of complex thin-wall parts but limit sag resistance in parison and bubble stability processes.
Compared with a conventional low-flow PP homopolymer in the 3–12 g/10 min melt flow range, SABIC PP 520L shows reduced chain entanglement and faster relaxation. Capillary rheometry on PP homopolymers in this melt-flow class indicates apparent melt viscosity in the range of 30–70 Pa·s at 1000 s⁻¹ and 230 °C, whereas a 12 g/10 min grade typically remains above 80 Pa·s under the same shear conditions. Peak injection pressure is therefore reduced, often by 10–25% in identical thin-wall tooling, and clamp force demand decreases because cavity pressure is reached with lower hydraulic pressure. The trade-off is a modest loss in tensile stiffness and notched impact resistance relative to lower-flow homopolymers of similar crystallinity.
For processors, the practical consequence is that SABIC PP 520L can fill wall sections below 1.0 mm at lower melt temperature than a 10–12 g/10 min homopolymer. Flow-length-to-wall-thickness ratios of 180:1 to 240:1 are achievable in laboratory spiral tests for materials in this MFR range, provided gate geometry and venting are adequate. Published data for this specific configuration is limited, but production trials on 80–120 t hydraulic machines have shown stable filling of thin-wall cylindrical containers without short shots when injection-speed profiles are maintained above 120 mm/s screw travel.
A representative property profile for SABIC PP 520L is summarized below. The values are drawn from technical data sheet parameters commonly reported for the grade and should be confirmed against the current supplier document before specification.
| Property | Test method | Representative value |
|---|---|---|
| Melt flow rate, 230 °C/2.16 kg | ISO 1133-1:2022 | 25 g/10 min |
| Density | ISO 1183-1:2019 | 0.905 g/cm³ |
| Tensile stress at yield, 50 mm/min | ISO 527-2:2012 | 35 MPa |
| Tensile modulus | ISO 527-2:2012 | 1550 MPa |
| Elongation at yield | ISO 527-2:2012 | 8% |
| Notched Charpy impact, 23 °C | ISO 179-1:2010/1eA | 2.0 kJ/m² |
| Vicat softening temperature A50 | ISO 306:2022 | 154 °C |
| Heat deflection temperature B, 0.45 MPa | ISO 75-2:2013 | 95 °C |
These values reflect an unfilled homopolymer with high stiffness, low ductility, and elevated melt fluidity. The notched impact value is lower than that of many impact copolymer grades, and the material should not be selected for low-temperature drop-impact service or for components requiring sustained ductile failure.
Thermal-oxidative degradation becomes the dominant process risk when SABIC PP 520L residence time exceeds 5–8 min at melt temperatures above 250 °C. Polypropylene undergoes chain scission under oxygen, and the resulting molecular weight loss produces an upward drift in MFR, surface splay, yellowing, and loss of mechanical strength. Hot-runner manifolds with unheated dead zones, poorly insulated valve-gate stems, or stagnating thermocouple wells can retain material for longer than the nominal residence time. MFR of retained melt can increase by 10–40% after extended hold at 260 °C, a change that alters cushion control and pack pressure transfer.
Melt temperature should be profiled from the rear zone to the nozzle, with the front zone and hot-runner setpoints selected to avoid exceeding 250 °C unless required by a specific colorant or nucleating masterbatch. The hot-runner manifold should be rebuilt with polished channels and no abrupt diameter changes. Molders are advised to purge with a high-MFR polypropylene or a commercial purging compound when cycle interruptions exceed 10 min. Degraded material is most often detected by a brownish tint, acrid odor, or inconsistent check-ring seating caused by low-viscosity molten polymer.
In addition, hot-runner valve-gate systems should use direct pneumatic or hydraulic actuation with repeatable gate opening. Delayed gate opening in thin-wall multi-cavity tools produces sequential filling and differential shrinkage, which can cause warpage in round containers and oval closures. Cavity pressure transducers in a pilot cavity are recommended when molding wall thickness below 0.8 mm; peak cavity pressure should not exceed 45 MPa to avoid flash and mold deflection.
General machine settings for high-flow PP homopolymers of this MFR class begin with a melt temperature of 220–250 °C and a mold temperature of 15–40 °C. Mold temperature at the lower end of the range accelerates cooling but reduces surface gloss and can freeze flow at the gate too early. For containers with wall thickness between 0.6 mm and 1.2 mm, mold temperatures of 25–35 °C provide an acceptable balance between fill speed and cooling time. Dehumidified air is not required under normal ambient conditions, but condensation from cold pellets should be avoided.
Back pressure of 0.5–1.2 MPa hydraulic and screw rotation in the range of 60–120 rpm are usually sufficient for melt homogeneity. Excessive back pressure raises melt temperature and degrades the material through shear heating. Injection speed should be high, with screw translational velocity above 100 mm/s, to maintain melt front advancement before freeze-off in thin sections. Pack and hold pressure is typically set at 40–60% of peak injection pressure, and hold time should be optimized to gate-seal time rather than fixed at long values. A cushion of 3–6 mm prevents screw-bottoming and maintains packing efficiency.
The grade is also used in caps, closures, thin-wall food containers, and housewares where short cycle time and dimensional stability are more important than low-temperature impact. Stack molds and multi-cavity closures benefit from the low melt viscosity, but the gate must be sized to avoid jetting and flow marks. Direct pin gates of 0.8–1.2 mm diameter are commonly used for closures, while thin-wall food containers typically use hot-tip gates or valve gates to improve gate vestige control.
Regrind addition of 20–30 wt% is commonly tolerated in noncritical packaging, but each heat history reduces molecular weight and narrows the processing window. Multiple passes of SABIC PP 520L through a 25:1 L/D screw at 230 °C can raise MFR by 5–15% per pass, depending on residence time and oxygen exposure. The material should not be combined with amine-based additives or nitroxide radical generators because these can accelerate chain scission or produce discoloration; the unfilled homopolymer is typically formulated without such chemistries.
If regrind is used, it should be dried when ambient relative humidity exceeds 60% or when storage has exposed the flake to moisture. Drying at 80 °C for 2 h in a desiccant dryer lowers surface moisture below 0.05 wt% and reduces splay. The drying temperature should not exceed 90 °C to avoid pellet agglomeration. Material stored in sealed bags at 20–30 °C and below 50% RH can generally be processed without drying.
Compared with random copolymer grades containing ethylene, SABIC PP 520L provides higher tensile modulus and greater heat resistance but lower optical clarity and poorer impact resistance at low temperature. Compared with high-impact copolymer grades, it offers superior flow and shorter cycle times but cannot match notched Izod or Charpy values. In applications requiring sterilization by steam or exposure above 100 °C, the grade is limited by its heat deflection temperature and should be evaluated under load-bearing conditions.