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YUNGSOX PP Terpolymer 5050R

    • Product Name: YUNGSOX PP Terpolymer 5050R
    • 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 922797
    Melt Flow Rate 230 C 2 16 Kg 8 g/10 min
    Density 0.90 g/cm³
    Tensile Strength At Yield 28 MPa
    Elongation At Break 500%
    Flexural Modulus 700 MPa
    Izod Impact Strength 23 C Notched 5 kJ/m²
    Heat Seal Initiation Temperature 110 °C
    Vicat Softening Point 125 °C
    Heat Deflection Temperature 0 45 Mpa 85 °C
    Haze 3%

    As an accredited YUNGSOX PP Terpolymer 5050R factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in 25 kg woven polypropylene bags with inner liner, moisture-protected, palletized and stretch-wrapped for safe transport and storage.
    Container Loading (20′ FCL) 20′ FCL shipment of YUNGSOX PP Terpolymer 5050R, packed in 25kg bags on pallets, secured for safe transport.
    Shipping YUNGSOX PP Terpolymer 5050R ships as non-hazardous pellets in 25 kg woven bags on shrink-wrapped pallets, protected with moisture barriers. Avoid prolonged heat, humidity, and direct sunlight during transit. Keep containers dry and well-ventilated to prevent contamination and maintain material integrity.
    Storage Store YUNGSOX PP Terpolymer 5050R in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and open flames. Keep packaging tightly sealed to prevent moisture absorption and contamination. Maintain ambient temperatures, avoid stacking too high, and protect from mechanical damage. No special hazardous storage requirements are needed under normal conditions.
    Shelf Life Shelf life is typically 2 years from manufacture when stored in a cool, dry, sealed container away from heat and sunlight.
    Application of YUNGSOX PP Terpolymer 5050R
    On a three-layer cast polypropylene line running an A/B/A structure with an overall gauge of 30 μm and a sealant web thickness of 7 μm, YUNGSOX PP Terpolymer 5050R is processed as the sealant-layer base resin at 70–90 wt% alongside a 10–30 wt% polypropylene homopolymer dilution stream and a slip/anti-block masterbatch. The sealant layer is plastified in a 75 mm single-screw extruder with L/D 30:1 and a barrier screw, melt temperature 232–238 °C at the die, die deckle width 1800 mm, air gap 8–12 mm, chill roll temperature 18–22 °C, and line speed 120–180 m/min. Melt flow rate of the terpolymer is checked at 230 °C under 2.16 kg load per ISO 1133-1:2022 and controlled to 5–7 g/10 min; a shift of ±0.8 g/10 min moves seal initiation temperature by 2–4 °C. The low seal initiation temperature of the terpolymer-rich skin, typically 105–115 °C at 0.5 N/15 mm seal strength under 0.3 MPa jaw pressure and 1 s dwell, permits form-fill-seal jaw temperatures to be reduced from 140–150 °C to 125–135 °C on a vertical machine with rotating serrated jaws and 60–120 ms contact time. Seal strength at 130 °C and 0.5 s dwell is measured at 3.5–5.0 N/15 mm by ASTM F88/F88M-21 with 180° peel and 200 mm/min crosshead speed, while hot tack at 125 °C is 1.5–2.5 N/15 mm by ASTM F1921-18. Haze of the 30 μm cast film is 1.5–2.5% by ASTM D1003-13, and gloss at 20° is 120–140 GU by ASTM D2457-13. Density is 0.90 g/cm³ by ASTM D792-20. FDA 21 CFR 177.1520(c) covers the olefin polymer base under Conditions of Use B through H, and the formulated structure falls under EU Regulation (EU) No 10/2011 with overall migration below 10 mg/dm² when only listed monomers and additives are used; REACH SVHC documentation must be collected at lot level. Processing boundaries: the residence time distribution should not exceed 10 min above 250 °C, because chain scission raises the melt flow rate and shifts seal initiation upward by 2–4 °C while generating oligomers that can accumulate on the vacuum box. When ambient RH exceeds 60% and pellets have been stored in cold-floor silos, a pre-drying step at 80 °C for 2 h in a desiccant-wheel hopper dryer with dew point below −30 °C is applied to eliminate surface moisture streaks. Incompatibility is observed when the sealant layer is diluted with more than 20 wt% calcium-carbonate-filled masterbatch, as the reduced elongation at break causes seal transfer and leaker rates above 0.4% on VFFS pouch lines.
    Sealant web formulation (wt%)Seal initiation temperature (°C)Seal strength at 130 °C (N/15 mm)Hot tack at 125 °C (N/15 mm)Haze (%)
    100% terpolymer105–1104.0–5.02.0–2.51.2–1.8
    90% terpolymer + 10% PP homopolymer108–1134.2–5.22.0–2.61.4–2.0
    80% terpolymer + 20% PP homopolymer112–1184.5–5.51.8–2.31.6–2.3
    70% terpolymer + 20% PP homopolymer + 10% anti-block masterbatch114–1204.0–5.01.5–2.02.0–2.8
    These comparative values represent process-window screening data from production-scale cast film lines and are not a formal specification for 5050R; the supplier certificate of analysis governs absolute values.

    Why Does Sealant Transfer to the Tenter Clip Increase Above 155 °C on Coextruded BOPP?

    In biaxially oriented polypropylene production, a three-layer cast sheet is quenched on a chill roll at 18–20 °C and then oriented in the machine direction at 125–130 °C and in the transverse direction at 155–165 °C. The sealant skin, typically 0.8–1.5 μm, is coextruded as a terpolymer-rich formulation containing 85–100 wt% propylene–ethylene–butene-1 resin, 500–1000 ppm erucamide slip, and 1000–2000 ppm of a synthetic silica anti-block with d50 2–3 μm. During transverse stretching, skin-layer oligomers and low-melting fractions can transfer to the tenter clips when the preheat zone exceeds 158 °C, producing breakage at line speeds of 250–350 m/min. Reducing the preheat temperature to 152–156 °C and increasing the quench-bath temperature differential to 4–6 °C between the top and bottom sheet surfaces maintains web flatness without shifting the seal initiation temperature. After orientation, seal strength at 120 °C is 1.8–2.6 N/15 mm by ASTM F88/F88M-21, and the seal is considered opened at 135 °C and 0.3 s dwell when cohesive peel is observed. The skin layer complies with FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011; specific migration of erucamide must be below the SML listed in the Union List, and the terpolymer base must not contain more than 30 mg/kg of catalyst-derived titanium if food contact compliance is declared under the polymer monograph. Operations with nitrogen purging of the feed throat and a melt temperature below 280 °C minimise discolouration and gel-count increase. The main incompatibility is with zinc stearate above 500 ppm in the anti-block masterbatch, which can accelerate thermo-oxidative degradation and is not recommended.Extrusion-laminated medical device pouches for ethylene oxide sterilisation use a PET 12 μm / aluminium foil 9 μm / PE 25 μm / PP terpolymer sealant web construction, but the direct PP terpolymer sealant grade replaces a solution-coated styrene-acrylate sealant when a wider sealing latitude and lower total solvent residue are required. In this configuration, the PP terpolymer is extruded as a 25–35 μm monolayer or coextruded layer onto the primed foil with a 90 mm extruder at 230–245 °C, an air gap of 100–150 mm, and a chill-roll temperature of 15–18 °C. Peelable opening is obtained by blending 15–40 wt% polybutene-1 into the sealant layer; however, published data for YUNGSOX PP Terpolymer 5050R specifically in PB-1 peel blends is limited, and the blend ratio must be screened on the target lamination line. Seal strength on flexible medical paper laminates ranges from 3–6 N/15 mm before sterilisation and from 2.5–5.5 N/15 mm after ethylene oxide exposure at 55 °C, 60% RH, and 6 h gas dwell. Peel initiation must remain above 1.5 N/15 mm after heat-sealing at 135 °C with 0.5 s dwell and 0.4 MPa jaw pressure to meet ISO 11607-1:2019 sterile barrier system process validation. Residual ethylene oxide limits follow ISO 10993-7:2008; the terpolymer sealant does not add volatile residuals above 0.5 μg/g when the sealant web is pre-extracted at 80 °C in a vacuum oven for 4 h. Processing limitation: the sealant web should not be corona-treated after winding beyond 38–40 mN/m, because excessive surface oxidation can increase peel force variability and blocking.

    When Extrusion Coating Replaces Solvent-Based Adhesives on Aluminium Lidding Foil

    On a tandem extrusion coating line, aluminium foil of 20–30 μm is corona-treated in-line at 4–6 kW/m² and then coated with PP terpolymer at 15–25 g/m², using a 105 mm single-screw extruder with L/D 30:1, die temperature 280–300 °C, air gap 180–220 mm, and line speed 80–150 m/min. The low density of the terpolymer and its narrow molecular weight distribution give a neck-in of 35–50 mm per edge under these conditions, which is manageable with deckle rods and a 2.5 m die width. Coating weight is measured by a beta gauge at ±0.5 g/m² closed-loop variation, and adhesion to aluminium after corona plus ozone treatment is 1.5–3.0 N/15 mm by ASTM D1876-08 T-peel at 200 mm/min. The coated foil is then heat-sealed to PP or PS trays at 140–150 °C for dairy lidding; seal strength on PP cups is 4–6 N/15 mm and on PS cups is 2–4 N/15 mm when the tray flange is coated with a tie layer. Compliance for food contact requires EU Regulation (EU) No 10/2011 overall migration below 10 mg/dm² and a declaration of compliance for each lot; rosin adducts, amine-based anticorrosion agents, and aromatic hydrocarbon process oils are excluded from the formulation. The operational boundary is residence time above 300 °C; if the die temperature is raised to 310 °C for low coat weights, the extruder barrel residence time must be kept below 6 min to prevent depolymerisation and the formation of pin-hole defects in the seal layer. A solvent-free alternative is therefore viable only when the downstream sealing temperature remains below 150 °C.

    Retortable Pouch Sealant Layers: Heat-Seal Creep, Crystallinity, and the 115 °C Ceiling

    Multi-layer retort pouches in which the sealant web is a 20–30 μm PP terpolymer layer compounded with 5–15 wt% medium-density polyethylene and 1–2 wt% antiblock show acceptable seal integrity in hot-fill and pasteurisation but fail progressively when the sterilisation cycle exceeds 115 °C. Differential scanning calorimetry according to ISO 11357-3:2018 shows a melting endotherm between 126 °C and 135 °C for a propylene-rich terpolymer; the onset of sealant creep in a restrained pouch during retort at 121 °C occurs when the seal temperature approaches the melt onset. Seal strengths after retort drop from 3.5–4.5 N/15 mm before the cycle to 1.5–2.2 N/15 mm after 30 min at 121 °C under 0.18 MPa overpressure, with the failure mode changing from cohesive in the sealant to interfacial peel at the foil–sealant boundary. The practical ceiling for this terpolymer grade in retort is therefore 115 °C; above this temperature a cast PP random copolymer with higher comonomer melting point or an impact-modified PP block copolymer must replace the sealant web. Compliance documents follow FDA 21 CFR 177.1520 for high-temperature conditions of use B and C, but migration testing must be run under simulated retort at 121 °C for 2 h if the pouch is declared retortable. The main processing constraint is that the sealant web must not be stretched more than 1.2% in the transverse direction before sealing, because molecular orientation combined with retort heat input produces anisotropic shrinkage and channel leakers at the pouch corner seals.Aluminium screw-cap closures for beverage and pharmaceutical bottles use a polypropylene terpolymer foamed liner or film layer to provide a seal against polyethylene terephthalate and polypropylene necks. In a compression moulding operation for closure liners, the terpolymer is blended with 1–3 wt% chemical blowing agent masterbatch, 0.5–1.0 wt% erucamide, and 2–5 wt% low-density polyethylene to reduce seal initiation temperature and increase elongation. Moulding is carried out at 190–210 °C compound temperature, 8–12 s cycle time, and 20–35 kN compression force on a 24- or 36-cavity rotary compression moulder. The liner seal strength against a PP bottle neck is 5–8 N/15 mm after induction sealing at 180–210 °C for 1.5–3 s; against PET bottles the liner is transferred via a kraft-backed aluminium foil and the peel opening torque is controlled to 0.5–1.2 N·m. Food contact compliance is specified under FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011; pharmaceutical closures require USP 661.1 plastic packaging physicochemical testing and an extractables study per USP 1663. Processing limitation: the liner compound must not be stored in high-humidity conditions without sealed packaging because the blowing agent masterbatch absorbs moisture and causes surface pitting at moulding temperatures above 200 °C.
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    Certification & Compliance
    More Introduction

    YUNGSOX PP Terpolymer 5050R is a propylene-ethylene-butene-1 random terpolymer supplied as pellets for sealant layers, surface skins, and low-temperature film-sealing applications. The numeric grade identifier 5050R places the product in the YUNGSOX polypropylene terpolymer series; the R suffix conventionally signals random comonomer incorporation rather than a block or impact copolymer architecture. Specification control for the grade is performed using melt flow rate measured to ASTM D1238-20b at 230°C with a 2.16 kg load, density measured to ISO 1183-1:2019, tensile yield stress and elongation measured to ASTM D638-14, melting and crystallization behavior measured to ISO 11357-3:2018, and optical haze measured to ASTM D1003-21. Published third-party data for this specific 5050R configuration is limited; batch-level conformance should therefore be read from the producer’s certificate of analysis and not inferred from terpolymer class averages.

    What distinguishes the propylene-ethylene-butene-1 terpolymer class from binary random copolymers?

    The functional difference between a terpolymer and a conventional propylene-ethylene random copolymer is the additional disruption of propylene sequences by butene-1. In a binary random copolymer, ethylene units interrupt chain regularity; in a terpolymer, the combination of ethylene and butene-1 reduces crystallizable sequence length further. This structural change suppresses the DSC melting peak from the 140–150°C range typical of binary random copolymers to approximately 120–135°C in the terpolymer class, as measured by ISO 11357-3:2018. The corresponding seal initiation temperature, defined here as the jaw temperature at which seal strength reaches the test threshold, commonly falls between 95°C and 115°C for terpolymers, compared with 120–135°C for many binary random copolymers and above 140°C for homopolymer PP. These are class-level reference bands, not certified 5050R values. The practical consequence is that a heat-seal layer made from the terpolymer can begin to form a seal at lower jaw temperatures, reduce energy input, and decrease the thermal load on heat-sensitive fillings, but the sealant film also exhibits a lower upper service temperature and is not suitable for retort or boiling-water sterilization unless carried by a thermally stable structural layer.

    On a three-layer cast-film line, 5050R is commonly metered as a sealant skin by a satellite extruder running a 30:1 L/D barrier screw, while the core layer is delivered by a separate main extruder. The melt temperature measured at the feedblock inlet should remain within the manufacturer’s recommended window; for this class the processing range is generally 220–250°C. Reverse-temperature profiles are avoided because the lower-melting terpolymer can suffer residence-time degradation if the feed zone is set above the metering zone. Chill-roll temperature has a measurable effect on optical quality: roll temperatures in the 15–30°C range are typical for cast terpolymer skins, whereas sustained operation above 35°C may allow post-extrusion crystallization that increases haze measured to ASTM D1003-21 and lowers 20° gloss measured to ASTM D2457-21. Air-knife and edge-pinning parameters should be rebalanced as line speed increases beyond 150 m/min because the melt stiffness of a low-crystallinity terpolymer differs from that of a homopolymer of equivalent melt flow rate.

    Isothermal crystallization rates for propylene-ethylene-butene-1 terpolymers are depressed relative to homopolymer PP because both comonomers reduce the average isotactic sequence length. The result is a lower equilibrium crystallinity, which reduces flexural modulus and oxygen barrier but improves clarity. In cast film, the quench rate governs the final mesomorphic fraction; a chill-roll surface temperature of 15°C promotes rapid solidification and low haze, whereas slower cooling near 30°C can produce larger crystalline structures that scatter light. Haze measured to ASTM D1003-21 is therefore not a single material property but a function of the film-making thermal history.

    Hot-tack onset, seal initiation temperature, and processing cautions

    Hot-tack behavior is controlled by the rate of chain re-entanglement at the seal interface relative to the rate of crystallization. Test results generated to ASTM F1921-20 on a terpolymer sealant typically show a broader hot-tack temperature window than a binary random copolymer because the seal remains ductile for a longer period after jaw release. Production rotary heat sealers often operate with dwell times of 0.2 s to 0.5 s, and the seal bar temperature profile should be verified with a multi-point contact thermocouple or thermal camera before high-speed start-up. Seal initiation curves to ASTM F2029-16 must specify the sealant thickness and backing substrate, because the apparent seal initiation temperature shifts upward as film gauge and bending stiffness increase. Surface preparation should be limited to corona treatment levels below 42 mN/m unless measured to ASTM D2578-23; excessive oxidation of the sealant surface can raise coefficient of friction and interfere with seal strength development.

    Slip and antiblock additive masterbatches must be adjusted for the lower processing viscosity of the terpolymer. Overdosing can produce chill-roll plate-out, which transfers to the film and appears as periodic optical defects on the sealant side. The base stabilization package of 5050R may include a phenolic antioxidant and an acid scavenger; therefore blending with unvalidated amine-based masterbatches should be avoided unless the additive package has been checked for interference with the resin stabilizer system. Because the grade has a reduced crystalline fraction, dusting from edge trim is generally lower than with homopolymer edge trim, but grinders and regrind hoppers still require magnet and screen inspection to protect the extruder from ferrous contamination.

    In form-fill-seal packaging, 5050R can replace a binary random copolymer skin when the limiting requirement is low-temperature seal initiation rather than high-temperature stiffness. A comparative film trial should record seal strength to ASTM F88/F88M-21, hot-tack to ASTM F1921-20, dart drop impact to ASTM D1709-16a, and coefficient of friction to ASTM D1894-14. On a 30 µm cast film, the seal layer may allow a reduction in sealing jaw temperature of approximately 5–15°C relative to a propylene-ethylene random copolymer of the same film gauge, depending on heat-seal dwell time and backing substrate. This temperature offset is a class-level estimate for evaluation purposes, not a certified 5050R specification. Because the melting point is close to the heat-seal jaw setpoint, jaw temperature uniformity across the seal bar becomes the dominant source of process variation; a thermal imaging pass at the intended line speed should be used to confirm that no cold zones on the seal bar create intermittent weak seals.

    When 5050R is selected as a low-melting sealant layer, barrier substrates must be thermally matched

    The thermal margin of a low-melting terpolymer becomes critical when it is coextruded against high-melting core resins such as polyamide or EVOH. The core extruder may operate above 240°C, and the sealant melt stream can absorb radiant heat from the die body or feedblock. In this arrangement, the feedblock and die adapter should provide thermal separation between the core melt stream and the sealant melt stream. The sealant melt temperature should be measured at the feedblock entrance with an insertion thermocouple and maintained below 260°C. Prolonged residence above this threshold can initiate oxidative chain scission, generating gels that appear as fish-eye defects in the cast film. Gel counts may be assessed with an optical film scanner calibrated against a 10,000 lux light table; published data for this specific 5050R configuration is limited. Start-stop sequences are a particular risk because idle time at temperature extends residence time without throughput. Die-lip build-up observed during coextrusion should be recorded and compared against the baseline because terpolymer volatiles can condense on the die lip and transfer to the film edge at intervals that correlate with winder roll changes.

    Representative property-direction comparison for polypropylene classes used in sealant film conversion. Values are class-level reference bands and do not replace the certified 5050R datasheet.
    PropertyTest methodPP homopolymerPP binary random copolymerPP ethylene-butene-1 terpolymer class
    Melting peakISO 11357-3:2018160–165°C135–150°C120–135°C
    Seal initiation temperatureASTM F2029-16>140°C120–135°C95–115°C
    Flexural modulusASTM D790-171200–1600 MPa800–1100 MPa500–900 MPa
    Tensile elongation at breakASTM D638-1410–50%200–700%300–800%
    HazeASTM D1003-211.5–3.0%0.5–2.0%0.3–1.5%
    Vicat softening temperatureISO 306/A50150–155°C120–135°C95–115°C

    Specification verification and regulatory compliance for food-contact sealant layers

    Food-contact status for a polypropylene terpolymer is not determined solely by the resin type; the final film must be tested under the intended food simulant and processing conditions. The olefin base polymer may be evaluated for compliance with 21 CFR 177.1520 and EU Regulation 10/2011, but specific migration limits for additives and oligomeric by-products depend on the full formulation. The table below lists the core conformity areas that should be present in the supplier’s regulatory statement for 5050R.

    Compliance verification checklist for YUNGSOX PP Terpolymer 5050R film applications.
    AreaStandard or regulationVerification requirement
    Melt mass-flow rateASTM D1238-20bBatch certificate of analysis at 230°C/2.16 kg
    DensityISO 1183-1:2019Reported in g/cm³
    Mechanical tensile propertiesASTM D638-14Yield stress and elongation at break
    Thermal transitionsISO 11357-3:2018Melting peak and crystallization temperature
    Heat-seal strengthASTM F88/F88M-21Seal curve on specified film structure
    Hot-tack strengthASTM F1921-20Hot-tack window at specified dwell
    Food-contact base resinFDA 21 CFR 177.1520Olefin polymer monograph
    EU food-contact plasticsEU 10/2011Overall migration and specific migration limits
    Heavy metals and RoHSDirective 2011/65/EURoHS screening for packaging electronics
    REACH SVHCREACH Regulation (EC) No 1907/2006Supplier confirmation for 0.1% w/w SVHC threshold

    In applications requiring hot-fill at temperatures above 90°C or in-package sterilization, 5050R is not a suitable sealant layer unless the thermal load is carried by a secondary structural film. The material’s lower crystalline fraction also reduces stiffness; converters replacing a homopolymer core with 5050R should recalculate film modulus using flexural modulus data generated to ASTM D790-17 and verify that the package’s tensile energy to break meets ASTM D638-14 requirements for the intended pouch geometry.

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