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Seculene PPT 1220 S0 PP Copolymer

    • Product Name: Seculene PPT 1220 S0 PP Copolymer
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 297912
    Density 0.905 g/cm³
    Melt Flow Rate 230 C 2 16kg 20 g/10min
    Tensile Strength At Yield 25 MPa
    Elongation At Break 100%
    Flexural Modulus 1000 MPa
    Izod Impact Strength Notched 23 C 50 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 100 °C
    Vicat Softening Temperature 150 °C
    Rockwell Hardness 85 R-scale
    Melting Point 165 °C

    As an accredited Seculene PPT 1220 S0 PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Seculene PPT 1220 S0 PP Copolymer is packaged in 25 kg moisture-resistant bags, palletized and shrink-wrapped for safe handling and transport.
    Container Loading (20′ FCL) 20′ FCL container loading: Seculene PPT 1220 S0 PP Copolymer packed on pallets, secured and stowed safely for transport.
    Shipping Seculene PPT 1220 S0 PP Copolymer is supplied as polypropylene copolymer pellets. Ship in clean, dry, sealed containers to prevent moisture and contamination. Not classified as dangerous goods. Keep away from excessive heat and ignition sources. Use standard handling procedures with proper labeling and transport documentation.
    Storage Store Seculene PPT 1220 S0 PP Copolymer in a cool, dry, well-ventilated area, away from heat, open flames, and direct sunlight. Keep containers tightly sealed and protect from moisture. Avoid contact with strong oxidizers. Follow local regulations and ensure adequate ventilation to prevent dust or vapor accumulation.
    Shelf Life Shelf life is typically 2 years from production date when stored in original, unopened packaging under cool, dry conditions.
    Application of Seculene PPT 1220 S0 PP Copolymer

    On thin-wall injection moulding lines producing dairy cups, deli containers, and microwaveable tubs at nominal wall sections between 0.45 mm and 1.20 mm, Seculene PPT 1220 S0 is processed with a melt temperature of 230°C to 250°C and a hot-runner manifold temperature not exceeding 260°C to suppress the formation of low-molecular-weight volatile fractions measurable by headspace gas chromatography according to VDA 277:2015. Mould surfaces are maintained at 10°C to 35°C using turbulent-flow liquid cooling, while fill times are compressed to 0.30 s to 0.80 s through injection velocities of 150 mm/s to 300 mm/s; holding pressure is set at 30 MPa to 50 MPa and profiled so that post-filling sink marks do not transfer to in-mould label edges. The food-contact compliance framework is defined by FDA 21 CFR 177.1520, EU Regulation 10/2011 as amended by EU 2020/1245, and GB 4806.7-2016, with overall migration limits of ≤10 mg/dm² for EU aqueous and fatty simulants and specific migration constraints for catalyst-derived antimony where analytical screening is required. On the production floor the formulation addition ratio is typically built around 96.5 wt% to 98.0 wt% Seculene PPT 1220 S0, 2.0 wt% to 3.5 wt% TiO₂ white masterbatch, 0.08 wt% to 0.20 wt% erucamide slip masterbatch, and 0.05 wt% to 0.15 wt% anti-blocking masterbatch; closed containers are pre-dried at 80°C for 2 h when relative humidity exceeds 60% because residual surface moisture generates silver streaking and splay on high-gloss sidewalls. Downstream production equipment consists of electric injection moulding machines with clamping force from 350 t to 800 t, valve-gated hot-runner systems of 4 to 32 drops, side-entry in-mould label robots, and automated vision inspection stations that reject parts based on label delamination, short shots, and burn marks. Terminal finished product types include 500 mL margarine tubs, 750 mL dairy cups, 1.0 L microwaveable containers, and snap-on lids where creep resistance after reheating is verified by track-test methods derived from ISO 167? actually dimensional stability under load should be verified by the brand owner using finished article conditioned at 70 °C for 2 h and assessed against warpage specifications rather than raw material data alone. The principal processing conflict occurs when wall thickness drops below 1.0 mm; in that case melt residence time in the hot runner must remain below 8 min at 250°C to prevent a shift in melt mass-flow rate of more than 15% from the certified pellet value measured by ISO 1133-1:2022.

    Compliance standardScopeTest method / conditionAcceptance criterion
    FDA 21 CFR 177.1520Olefin polymers for food-contact articlesHexane and xylene extractable fractions per monographSupplier food-contact declaration; extraction limits per 21 CFR 177.1520(b)
    EU 10/2011Plastic multilayers and articles in contact with foodOverall migration in 10% ethanol, 3% acetic acid, 95% ethanol or olive oil per EN 1186-1:200210 mg/dm² or ≤60 mg/kg for infant food simulants
    GB 4806.7-2016National food-contact polyolefin resinsTotal migration per GB 31604.1-2015 using time-temperature conditions matched to end use10 mg/dm²; potassium permanganate consumption ≤10 mg/kg

    What Limits Low-Temperature Impact Retention in Talc-Filled Automotive Cabin Brackets?

    In automotive interior trim programs where Seculene PPT 1220 S0 is selected as the base copolymer for A/B/C pillar trims, door trim carrier panels, centre console side panels, glovebox liners, and under-hood ECU mounting brackets, the controlling design parameter is usually the retention of notched Charpy impact performance after mineral filler addition and after heat ageing at 105°C for 1,000 h. The material is assessed against ISO 179-1:2020 Charpy impact at 23°C and −20°C, ISO 527-2:2012 tensile yield stress, ISO 178:2019 flexural modulus, and DIN 75201:2011 gravimetric fogging; procurement specifications also typically reference VDA 277:2015 total VOC emission limits of ≤100 µg C/g, ISO 3795:1989 horizontal burn rate of ≤100 mm/min, and the end-of-life vehicle material restrictions of EU Directive 2000/53/EC with REACH SVHC documentation under Regulation (EC) No 1907/2006. Formulation addition ratios in production compounds usually consist of 100 parts by mass Seculene PPT 1220 S0, 10 parts to 20 parts talc masterbatch, 2 parts to 5 parts additional impact modifier where OEM low-temperature ductility demands exceed the neat resin, 0.2 parts to 0.6 parts hindered amine light stabilizer, 0.1 parts to 0.4 parts phenolic antioxidant, and 2 parts to 3 parts color masterbatch. Talc loadings above 25 wt% produce a measurable cliff-edge in −20°C Charpy notched impact, with some production batches falling below 6 kJ/m² unless the compounding sequence is re-optimized to disperse the filler before elastomer incorporation; batch-to-batch variance in talc moisture is the most frequent root cause of surface blush and inconsistent cold-temperature ductility. Downstream production is carried out on hydraulic toggle clamp injection moulding machines of 1,200 t to 2,500 t locking force, using sequential valve gating for large-area pillar trims and gas counter pressure of 0.5 MPa to 2.0 MPa to suppress sink marks at boss and rib intersections. Melt temperature is held at 220°C to 250°C, mould temperature at 30°C to 50°C, and screw recovery is controlled to avoid plastication times longer than 25 s because excessive low-shear residence time raises the low-molecular-weight fraction that contributes to fogging condensate. Terminal finished product types include injection-moulded B-pillar lower trim, front door carrier plates, centre console side panels, glove box outer covers, HVAC lower housings, and ECU bracket bases where the component must survive powertrain bay temperature spikes of 110°C without measurable creep under clamp load.

    Standard / codeParameterMethod / conditionTypical threshold
    ISO 3795:1989Horizontal burn rateConditioned specimen 100 mm/min100 mm/min
    DIN 75201:2011Fogging condensateGravimetric reflection at 100°C/3 h2 mg/10 g if specified by OEM
    VDA 277:2015Total VOC emissionHeadspace GC after 120°C/5 h100 µg C/g common OEM limit

    Compounding Seculene PPT 1220 S0 into halogen-free flame-retardant formulations for low-voltage electric vehicle battery pack accessories requires a two-stage screw geometry because the intumescent ammonium polyphosphate system must be dispersed below the thermal threshold at which the copolymer begins to generate oxidised oligomer fractions that reduce glow-wire ignition temperature. The most common production configuration is a co-rotating twin-screw extruder with 40:1 L/D ratio and throughput of 600 kg/h to 1,200 kg/h, with barrel temperatures of 150°C to 190°C in the first half, 170°C to 200°C in the second half, and die temperature of 180°C to 200°C; water-bath temperature is held at 20°C to 40°C to prevent quench stress from lowering ambient-temperature notched impact. The formulation addition ratio typically uses 38 wt% to 55 wt% Seculene PPT 1220 S0 as the carrier matrix, 30 wt% to 45 wt% magnesium hydroxide, 15 wt% to 25 wt% ammonium polyphosphate, 3 wt% to 8 wt% zinc borate as smoke and char synergist, 0.5 wt% to 1.5 wt% maleic anhydride grafted coupling agent, and 0.2 phr to 0.6 phr hindered phenolic antioxidant. Published data for this specific Seculene grade in high-voltage battery applications is limited; therefore every modified compound must be re-qualified against UL 94 V-0 at 3.0 mm, IEC 60695-2-12 glow-wire flammability at 850°C, and UL 746B relative thermal index before release into production. The critical processing boundary is the die temperature: excursions above 210°C darken the compound and can shift the glow-wire ignition temperature downward by 30°C to 50°C, so barrel profile verification with an infrared melt probe is recommended at shift start. Downstream production of finished parts is performed on injection moulding machines with clamp force from 150 t to 450 t, using low-compression screws and free-flow nozzle tips to prevent melt stagnation at screw tips and hot-runner dead spots. Terminal finished product types include low-voltage battery module end plates, busbar insulating brackets, cell holder frames, and charging connector bodies where the material must retain dimensional stability after thermal cycling between −40°C and 85°C with 1,000 cycles.

    Returnable Logistics Container Freeze-Off and Drop-Weight Failure Modes

    Logistics container moulders report that the most frequent field return occurs at the intersection of sub-zero impact and drop-weight loading, particularly when returnable beverage crates, agricultural lugs, ventilated bins, and foldable pallet boxes are stored outdoors at temperatures between −20°C and 0°C before handling. The relevant compliance assessment combines ISO 179-1:2020 Charpy notched impact at −20°C, ASTM D5276-19 drop-weight impact on filled crates, and ISO 8611-1:2011 flat pallet deflection testing where applicable; periodic UV resistance is verified by ISO 4892-2:2013 xenon arc exposure for 800 h to 1,200 h. The production formulation addition ratio is normally 100 parts by mass Seculene PPT 1220 S0, 2 parts to 4 parts UV masterbatch, 0.5 parts to 1.5 parts antistatic masterbatch for dust prevention, and 1 part to 2 parts carbon black or color masterbatch. Regrind content should be limited to ≤20 wt% because higher recycled ratios reduce −20°C notched Charpy values below 5 kJ/m² in some batches. Downstream production uses accumulator-assisted injection moulding machines from 650 t to 1,500 t clamping force, with melt temperature of 220°C to 250°C, mould temperature of 15°C to 40°C, and injection fill time of 1.0 s to 2.5 s to avoid hesitation marks on rib intersections. Terminal finished product types include stackable beverage crates, dairy distribution crates, folding plastic pallet boxes, and ventilated produce bins designed for multi-year return cycles.

    When Non-Implant Diagnostic Housings Require ISO 10993-5 Cytotoxicity and USP 661.1 Batch Release

    When non-implant diagnostic equipment housings are switched from ABS to polypropylene copolymer, the controlling regulatory variable is usually the chemical characterisation package required for in-vitro diagnostic instruments, benchtop analyser covers, point-of-care device enclosures, and pipette tip rack bases that are not in direct patient contact but are still evaluated under the medical device risk assessment. Seculene PPT 1220 S0 can be used in such applications when the moulding operation maintains batch traceability and the supplier provides change management documentation in alignment with ISO 10993-18:2020. The compliance matrix includes ISO 10993-5:2009 cytotoxicity by extract dilution, ISO 10993-10:2013 skin sensitisation and irritation, USP 661.1 plastic packaging physicochemical tests, and FDA 21 CFR 177.1520 for incidental food-contact compatibility if the device is used in laboratories where reagent contact may occur. The formulation addition ratio is deliberately simple to reduce extractable complexity: 100 parts by mass Seculene PPT 1220 S0, 0.1 wt% to 0.3 wt% hindered phenolic antioxidant, 1 wt% to 2 wt% non-phthalate color masterbatch, and no release agents containing silicone oil because silicone migrates into cell culture media and alters ISO 10993-5 extract dilution results. Downstream production is performed on electric injection moulding machines from 150 t to 450 t clamp force in ISO Class 8 cleanrooms, with melt temperature of 210°C to 240°C, mould temperature of 15°C to 40°C, and closed-loop material drying to maintain pellet moisture below 0.05 wt%. Terminal finished product types include diagnostic analyser housings, benchtop centrifuge covers, point-of-care cartridge reader enclosures, and pipette tip rack bases where the primary mechanical requirement is dimensional stability after repeated disinfectant wipe cycles using 70% ethanol and quaternary ammonium solutions.

    Ultraviolet ageing resistance governs outdoor furniture specifications on the basis of accelerated xenon-arc exposure rather than short-term tensile yield, because stackable chair shells, table bases, garden lounger armrests, and modular furniture connectors fabricated from Seculene PPT 1220 S0 must survive multi-season solar loading without surface chalking, embrittlement, or visible colour shift. The relevant compliance baseline is ISO 4892-2:2013 xenon-arc weathering with 0.51 W/m² irradiance at 340 nm, black-standard temperature of 65°C, and exposure of 1,000 h to 2,000 h depending on geographic target; tensile elongation retention is checked against ISO 527-2:2012, and notched Charpy impact is measured by ISO 179-1:2020 after weathering. The formulation addition ratio for UV-stable outdoor grades typically includes 100 parts by mass Seculene PPT 1220 S0, 0.3 wt% to 0.8 wt% oligomeric hindered amine light stabilizer, 0.1 wt% to 0.3 wt% benzotriazole UV absorber, 2 wt% to 4 wt% weather-resistant pigment masterbatch, and 0.1 wt% to 0.3 wt% secondary antioxidant to protect melt stability during long hold times. Downstream production uses injection moulding machines with clamp force from 800 t to 2,000 t, melt temperature of 220°C to 250°C, mould temperature of 15°C to 35°C, and gas-assisted injection for thick armrest sections where sink marks and knit lines at the headrest attachment would reduce visual acceptance. Terminal finished product types include injection-moulded outdoor chair shells, rectangular table bases, contoured armrests, and modular joining brackets where creep under static load is evaluated at 40°C for 72 h with deflection limits defined by the furniture standard ISO 7173:2018.

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    Certification & Compliance
    More Introduction

    Seculene PPT 1220 S0 PP Copolymer is a pelletized polypropylene random copolymer supplied for injection moulding. The designation identifies a clarified random copolymer with a nominal melt mass-flow rate of 20 g/10 min at 230 °C and 2.16 kg when determined according to ISO 1133-1:2022. Density at 23 °C is reported near 0.905 g/cm³ under ISO 1183-1. The product is used in thin-wall transparent containers, closures, housewares, and general-purpose injection-moulded parts that require optical clarity, low warpage, and moderate impact resistance. The S0 suffix denotes a selected stabilization package; the exact formulation is documented in the manufacturer’s regulatory statement and safety data sheet, not in the grade name.

    When a 20 g/10 min random copolymer enters a valve-gated hot-runner closure tool

    Injection moulding is the primary conversion process. A single-screw reciprocating injection moulding machine with a screw L/D ratio of 20:1 to 25:1 and a compression ratio of 2.5:1 to 3.5:1 is normally used. Starting barrel settings are 200–220 °C in the feed zone, 220–240 °C in the compression/metering zone, and 230–250 °C at the nozzle. The mould temperature is held at 20–50 °C. The melt-temperature window is bounded at 210 °C and 250 °C. Above 250 °C, the residual stabilization package is consumed faster and visible yellowing may occur during hold-up times longer than 3–5 min. Below 210 °C, flow length in a 0.8 mm wall may be insufficient for high-cavitation tools unless injection velocity is raised significantly.

    Back pressure is set at 0.5–2.0 MPa, and screw speed is limited to avoid melt-temperature overshoot. In 16-cavity and 32-cavity valve-gated hot-runner closure tools, cavity-to-cavity fill imbalance above 2% by shot weight is often corrected by nozzle setpoint offsets of 2–5 °C. If the required offset exceeds 5 °C, the manifold should be inspected for blocked channels, heater failure, or worn valve-gate tips. Production-scale troubleshooting has shown that visible haze bands and dimensional spread appear when melt-temperature variation across the manifold exceeds ±3 °C.

    The nominal property window is summarized below. Values are manufacturer-published or class-typical for a clarified polypropylene random copolymer in the 20 g/10 min melt-flow band; lot-specific values are governed by the certificate of analysis.

    PropertyTest methodValue or rangeUnit
    Nominal melt mass-flow rate, 230 °C/2.16 kgISO 1133-1:202220g/10 min
    Density at 23 °CISO 1183-10.905g/cm³
    Tensile stress at yield, 50 mm/minISO 527-225–32MPa
    Tensile strain at yieldISO 527-210–14%
    Flexural modulus, 2 mm/minISO 1781000–1250MPa
    Notched Izod impact at 23 °CISO 180/A5–8kJ/m²
    Notched Izod impact at -20 °CISO 180/A1.2–2.0kJ/m²
    Vicat softening point, A50ISO 306/A50125–135°C
    Heat deflection temperature, 0.455 MPaISO 75-2/B75–90°C
    Haze on 1 mm plaqueASTM D10038–15%

    Stiffness, haze, and low-temperature impact do not track linearly with ethylene content

    Differences from other polypropylene grades are primarily structural. A polypropylene homopolymer of equivalent melt mass-flow rate has higher crystallinity, higher flexural modulus, higher heat deflection temperature, and higher Vicat softening point, but lower notched impact and poorer transparency. Seculene PPT 1220 S0 is a random copolymer; the comonomer disrupts crystallinity and reduces spherulite size, which lowers haze and stiffness while improving impact. The comonomer content is not declared on standard datasheets. Class-typical random copolymers contain less than 5 wt% ethylene, but the precise fraction must be confirmed with the manufacturer.

    Compared with heterophasic copolymers of the same MFR, the random copolymer contains no discrete elastomer phase. It therefore provides higher clarity and modulus but lower low-temperature impact. For service below -20 °C, a heterophasic grade is normally selected. Compared with high-flow random copolymers in the 40–100 g/10 min range, the 20 g/10 min grade provides higher melt viscosity, lower flash tendency, and usually better environmental stress-crack resistance, but requires higher injection pressure and may not fill sections thinner than 0.6 mm in high-cavitation tools.

    Does Seculene PPT 1220 S0 meet food-contact and pharmaceutical packaging requirements?

    Food-contact compliance is not inferred from the grade designation. In the United States, the base olefin polymer may be evaluated under 21 CFR 177.1520(c) for olefin polymers with conditions of use A through H. In the European Union, compliance is assessed under Regulation (EU) No 10/2011 and subsequent amendments. The manufacturer’s declaration establishes overall migration limits and specific migration limits for additives. Overall migration testing is commonly performed according to the EN 1186 series, and specific migration is tested under EN 13130 where applicable. For pharmaceutical packaging, Ph. Eur. 3.1.3 and USP <661.1> may be applicable, but extractables data for this specific configuration is limited and should be generated on the finished article under the intended sterilization and storage conditions.

    Biocompatibility for medical devices is not supplied by the grade alone; finished-device manufacturers are responsible for evaluation under ISO 10993-1. Autoclave sterilization at 121 °C is not recommended in thick sections without validation because it can increase haze and reduce impact. Gamma irradiation and ethylene oxide may be considered only after dose validation, since ionizing radiation produces chain scission and shifts melt rheology of any recycled material.

    Apparent viscosity, shear rate, and pressure drop in high-cavitation tools

    At 230 °C, class-typical capillary rheometry for a 20 g/10 min random copolymer gives apparent shear viscosity values of 150–250 Pa·s at 100 s⁻¹ and 25–40 Pa·s at 1000 s⁻¹; published data for this specific configuration is limited. The power-law shear-thinning exponent is typically between 0.3 and 0.5. These values are used to estimate pressure drop through hot-runner manifolds and gate lands. At a 1.0 mm gate diameter and a fill time of 0.6 s, the wall shear rate may exceed 10,000 s⁻¹, producing local shear heating of 5–15 °C. This viscous dissipation reduces melt viscosity and changes cavity fill balance if the manifold is not thermally symmetric.

    Pressure drop is also sensitive to hot-runner zone control. A difference of ±2 °C between adjacent zones can produce measurable weight variation in clarified random copolymers. High-cavitation tools should be qualified with cavity weight mapping, short-shot progression, and gate-seal studies rather than relying on nominal barrel temperature alone.

    Pre-drying is not normally required if the material is stored sealed below 40 °C. If surface moisture is present, desiccant drying at 80 °C for 2–4 h is used. The grade is not intended for pipe extrusion, blow moulding, or thermoforming because the melt strength is insufficient for large parison or sheet dimensions. The material should not be held at melt temperature for extended periods; processing hold-up above 250 °C for more than 3–5 min may consume the stabilizer and increase yellowness. In service, strong oxidizing agents, aromatic hydrocarbons, and chlorinated solvents should be avoided because random polypropylene is susceptible to swelling and stress cracking. The natural grade is not UV-stabilized for long-term outdoor exposure and will undergo chain scission, chalking, and embrittlement unless a suitable UV stabilization package is compounded into the resin.

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