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Formosa PP 3500

    • Product Name: Formosa PP 3500
    • 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 728999
    Melt Flow Rate 35 g/10 min at 230°C, 2.16 kg
    Density 0.90 g/cm³
    Tensile Strength At Yield 35 MPa
    Elongation At Yield 12%
    Flexural Modulus 1500 MPa
    Rockwell Hardness R-100
    Notched Izod Impact Strength 25 J/m
    Heat Deflection Temperature 105°C
    Vicat Softening Point 150°C
    Melting Point 160°C

    As an accredited Formosa PP 3500 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Formosa PP 3500 polypropylene resin is packaged in 25 kg bags, palletized and wrapped for safe transport.
    Container Loading (20′ FCL) 20′ FCL container loading of Formosa PP 3500: packed in 25kg bags onto pallets, secured for safe, efficient transport.
    Shipping Formosa PP 3500 is a polypropylene resin shipped in sealed, moisture-resistant bags, bulk bags, or hopper containers. Store away from heat, ignition sources, and direct sunlight. Ensure dry, ventilated transport conditions to prevent contamination or degradation. Handle with care to avoid bag damage during transit.
    Storage Store Formosa PP 3500 in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid prolonged exposure to high temperatures to prevent degradation. Maintain good housekeeping to minimize dust accumulation and static discharge. Follow local regulations and manufacturer safety data sheet guidelines.
    Shelf Life Formosa PP 3500 has a shelf life of 24 months when stored in original packaging in a cool, dry area away from sunlight.
    Application of Formosa PP 3500

    Thin-wall injection molding of dairy containers and delicatessen tubs is the primary downstream application for PP 3500. The grade is specified with a nominal melt flow rate of 35 g/10 min at 230 °C under 2.16 kg load in accordance with ASTM D1238-23a or ISO 1133-1:2022. In this MFR class, tensile yield stress is typically 30–36 MPa when measured at 50 mm/min according to ISO 527-2/1A/50, and flexural modulus is typically 1,300–1,600 MPa under ISO 178. The low melt viscosity permits filling of wall sections from 0.6 mm to 1.0 mm without exceeding 120 MPa injection pressure on accumulator-assisted injection molding machines. On a 250 t all-electric injection press with a 50 mm screw, a 16-cavity 500 ml round cup tool can be set to fill times of 0.30–0.50 s at melt temperatures between 230 °C and 250 °C.

    General-purpose polyolefin screws with 20:1–25:1 L/D and compression ratio 2.0:1–2.5:1 are suitable; high-compression barrier screws can generate excessive shear and raise melt temperature by 5–10 °C. Polypropylene does not require hydrolytic drying, but if pellets have been stored at relative humidity above 60%, surface moisture can cause splay. Desiccant drying at 80 °C for 2 h is adequate; residence time should not exceed 4 h at that temperature to avoid additive blooming. The injection unit should be equipped with a positive nozzle shut-off valve to prevent drool when decompression exceeds 3 mm; excessive decompression can introduce air and cause silver streaks.

    Mold temperature is controlled at 15–35 °C using turbulent mold-water circuits; laminar flow below a Reynolds number of 10,000 can produce core-to-cavity temperature differentials above 5 °C, causing ovality greater than 0.4 mm on round rims. The transition from filling to packing is determined by screw position when the cushion is 3–6 mm from the nozzle. Packing pressure is maintained at 40–70 MPa for 0.8–1.5 s, followed by hold pressure decay. Hold time is governed by gate freeze-off; for hot runner tip gates of 0.8–1.2 mm, gate freeze time in polypropylene is generally 4–8 s at mold temperatures below 40 °C. Premature hold release allows melt to flow back through the gate, generating sink marks deeper than 0.02 mm and increasing post-mold shrinkage by 0.5–1.0%.

    Batch-to-batch melt flow variation of ±2 g/10 min can shift injection pressure by 5–10%; molders should log fill time, switch-over position, and cushion for each resin lot. Food-contact converters generally run PP 3500 in neat pellet form. A white masterbatch is introduced at 2–4 wt% via gravimetric dosing, and clean in-house regrind is tolerated up to 20 wt%, provided it is not contaminated with other polymers. Nucleated formulations may include a sorbitol-based clarifying agent at 0.05–0.15 wt%; this raises crystallization temperature and reduces cycle time, but it also lowers notched impact under ISO 180/A by 5–10%.

    In the United States, the resin is accepted for direct food contact under FDA 21 CFR 177.1520, with end-use conditions stated in 21 CFR 176.170(c). In the European Union, finished containers must comply with Regulation (EU) No 10/2011, including overall migration below 10 mg/dm² and specific migration limits for additives. In China, the resin falls under GB 4806.6-2016 and the formed article under GB 4806.7-2016. Terminal products include 200 ml and 500 ml dairy pots, 8–32 oz delicatessen tubs, and translucent lids with stacking lugs. Draft angles of 1.5–3° on side walls and rim radii of 0.5–1.0 mm reduce ejection indentations and cracking at undercuts.

    Processing variableThin-wall food cup (0.7 mm wall)Closure cap (1.0 mm wall)
    Melt temperature230–250 °C225–245 °C
    Mold temperature15–35 °C25–40 °C
    Injection speed300–600 mm/s180–300 mm/s
    Packing pressure40–70 MPa55–80 MPa
    Gate freeze hold time4–8 s3–6 s

    Where does a 35 g/10 min melt flow rate constrain cap torque retention?

    Closures for non-carbonated beverages, condiment bottles, and food jars are a second high-volume application. PP 3500 is processed in hot-runner stack molds with 64–128 cavities; low melt viscosity allows injection speeds of 180–300 mm/s. Total cycle times for a 28 mm finish cap with wall thickness 0.8–1.2 mm are commonly 5–8 s. The valve-gate needle is held closed for 0.2–0.5 s after packing; early needle opening creates a string or pinhole at the cap dome.

    Typical additive loading in the final closure is erucamide slip masterbatch at 0.5–1.5 wt% and silica anti-block at 0.05–0.20 wt%. Erucamide migrates to the surface over 24–48 h and reaches functional steady state after 7–14 days; removal torque values measured immediately after molding are not representative. For food-contact closures, only additives compliant with FDA 21 CFR 174–178 and Regulation (EU) No 10/2011 should be used.

    The 35 g/10 min MFR reduces molecular orientation and can lower unscrewing torque by 10–20% relative to a 12 g/10 min grade. This is counteracted by increasing packing pressure from 40–60 MPa to 55–80 MPa and holding mold temperature at 25–35 °C. Packing above 90 MPa can overpack the tamper-evident band and cause split-band failure during demolding. Organoleptic testing per DIN 10955 is typically required for closures used with still water and flavored beverages.

    Closure dimensions are checked against a 28 mm PCO 1881 or 38 mm finish gauge; removal torque is typically specified between 0.6 N·m and 2.0 N·m. Carbonated soft-drink closures generally require a random copolymer or a liner structure; PP 3500 is not the typical selection for carbonated beverage closures because of stress-cracking sensitivity and lower impact after orientation. Finished closures include 28 mm PCO 1881 short-skirt caps for shelf-stable juices, 38 mm condiment caps, and 63 mm tamper-evident lids for protein powder tubs.

    In diagnostic laboratory consumables, PP 3500 is used where wall sections drop to 0.6–0.9 mm and multi-cavity tools are required. The melt’s low viscosity enables pipette tip racks and centrifuge tube shells to fill at injection pressures below 120 MPa on all-electric presses with shot sizes of 30–80 g. Mold temperatures of 30–50 °C are used to reduce flow-induced stress, and ejection is delayed until core surface temperature falls below 70 °C. Packing pressure is held at 35–55 MPa for parts with thin snap arms; higher packing increases out-of-roundness in conical tubes.

    Pigment loading is generally restricted to 0.05–0.20 wt% for translucent diagnostic parts; higher loadings can introduce extractable metal ions that interfere with enzymatic assays. Mold-release agents are avoided because they can contaminate optical windows and reaction wells. Laboratory ware is not an implantable medical device; however, raw-material certificates often require ISO 10993-5 cytotoxicity evaluation of the compounded resin. Final devices may be processed under ISO 13485 quality systems according to the converter’s regulatory status. Metal contamination is controlled at the blender and feed throat by magnets and metal separators with sensitivity below 50 ppm.

    Terminal products include 15 ml conical centrifuge tubes, 96-well rack bases, disposable cuvette adapters, and sample transport tubes. Autoclaving at 121 °C for 20 min per ISO 17665-1 is possible only when thin-wall parts are supported; unsupported racks may distort above 115 °C, and repeated cycles beyond 10 can cause oxidative embrittlement in non-stabilized grades.

    Appliance component molding: ejector pin marks and UL 94 HB compliance

    In small appliance components such as drip trays, condensate pans, and detergent dispenser housings, PP 3500 is selected to reduce cycle time when replacing a 12 g/10 min homopolymer. Melt temperature is maintained from 220–240 °C; mold temperatures below 30 °C can produce visible flow lines on textured surfaces. For high-gloss panels, mold temperature is raised to 40–50 °C and injection speed is reduced to 100–180 mm/s. Ejector pin marks are controlled by using ventilated pins with clearance of 0.01–0.02 mm and by maintaining draft angles above on vertical ribs.

    For cold-impact or UV-exposed parts, converters may blend PP 3500 with 5–15 wt% ethylene-propylene impact modifier; this lowers melt flow rate and can raise injection pressure by 10–20%. Resulting impact performance is evaluated according to ISO 179-1/1eA or ISO 180/A at 23 °C and, if required, at −20 °C. Electrical enclosure parts are generally rated UL 94 HB at 1.5 mm thickness. If a V-2 or V-0 rating is required, a flame-retardant masterbatch must be validated at the full OEM wall thickness and plate thickness. Heavy metal restrictions for electrical and electronic products follow RoHS Directive 2011/65/EU; REACH SVHC declarations are obtained from the resin supplier.

    Terminal parts include air conditioner condensate pans, washing machine detergent dispenser housings, and refrigerator door shelf brackets.

    Reusable storage containers with in-mold labels and snap-fit lids are molded in high-cavitation tools where shot-to-shot weight variation must remain below 0.5%. The low melt viscosity of PP 3500 enables 8–16 cavity tools to be filled with injection speeds of 250–400 mm/s at melt temperatures between 225 °C and 245 °C. For in-mold label insertion, the label stock is pre-dried to 0.05% moisture by weight before entering the mold to prevent blistering. No adhesive is used; the molten PP fuses to the label surface during injection, and mold temperatures of 35–45 °C prevent label edge curl.

    Reusable food containers are processed with color masterbatch at 2–4 wt%; regrind usage is limited to 15–20 wt% depending on customer-specific migration testing. Parts intended for microwave or dishwasher contact should be tested for migration at the intended repeated-use conditions under Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520. Repeated dishwasher cycles can induce microcracking at injection weld lines or label edges; OEMs should perform at least 50 dishwasher cycles with standard detergent at 65 °C before specifying PP 3500 for dishwasher-safe storage. Published data for repeated dishwasher exposure of PP 3500 specifically is limited; OEM-specific migration and stress-cracking validation is required.

    Terminal products include multi-compartment lunch boxes, refrigerator storage sets, and 1–5 L dry food canisters.

    When PP 3500 is substituted into automotive cable brackets under short-term thermal loads

    PP 3500 is available for automotive cable brackets, fuse box brackets, and non-pressure washer reservoir filler necks only where continuous service air temperature does not exceed 85 °C. Heat deflection temperature under 0.455 MPa is approximately 100 °C when tested according to ISO 75-2/B. Parts requiring long-term heat aging above 90 °C should be evaluated with a thermally stabilized polypropylene or a glass-filled grade.

    Automotive injection tools with polished surfaces benefit from mold temperatures of 40–60 °C to reduce differential shrinkage. The high flow of PP 3500 may create gas traps at rib intersections; venting gaps of 0.02–0.03 mm and vacuum-assisted mold venting are specified to prevent burn marks. The unfilled homopolymer is generally used without impact modification for non-impact clips. If impact modifier is added at 5–10 wt%, melt flow rate decreases and injection pressure rises by 10–15%; low-temperature impact should be tested according to ISO 180/A at −30 °C. Automotive OEM specifications may require tensile and flexural data according to ISO 527-2/1A/50 and ISO 178, plus odor testing according to VDA 270. Published data for PP 3500 in long-term automotive heat aging is limited; OEM-specific validation of mechanical retention after 1,000 h at 85 °C is required before release.

    Terminal products include cable clips, fuse box brackets, and washer reservoir filler necks.

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    Certification & Compliance
    More Introduction

    Formosa PP 3500 is a nucleated polypropylene homopolymer, classified under ASTM D4101 as Group 01, Class 1, Grade 2, and manufactured via a controlled-rheology process that delivers a nominal melt mass-flow rate of 35 g/10 min when tested per ISO 1133-1:2022 (230°C, 2.16 kg). The resin exhibits a density of 0.90 g/cm³ (ISO 1183-1), a tensile stress at yield of 36 MPa (ISO 527-2, 50 mm/min), and a flexural modulus of 1 600 MPa (ISO 178). Its high crystallization temperature—typically 125 °C by differential scanning calorimetry at a cooling rate of 10 K/min—enables cycle-time reduction in thin-wall injection molding, where the solidification rate governs demolding readiness. Within this processing domain, the material’s flat viscosity profile between 100 and 1 000 s⁻¹ is advantageous for filling multi-cavity tools with flow-length-to-wall-thickness ratios exceeding 200:1, provided that the melt temperature is maintained within 230 °C to 250 °C and the mold surface temperature is held at 20 °C to 50 °C. Pre-drying is not routinely required; however, exposure to relative humidity above 60 % for more than 8 hours may introduce surface moisture that generates splay defects during filling, making a desiccant drying step at 80 °C for 2 hours advisable. Residence time in the injection unit barrel must be controlled to fewer than 10 minutes at melt temperatures exceeding 260 °C, because chain scission accelerates and can increase the MFR by more than 15 %, compromising shot-to-shot weight consistency and promoting yellowing. When fast-cycle packaging containers with nominal wall thickness of 0.4 mm are produced on all-electric toggle-clamp machines with clamp forces between 1 500 kN and 3 500 kN, the injection speed should be set to at least 350 mm/s and followed by a holding pressure of 60 MPa to 80 MPa for 0.5 s to counteract volumetric shrinkage of 1.4 % to 1.8 % (ISO 294-4). Gate freeze-off time can be shortened by approximately 15 % relative to a non-nucleated homopolymer of identical MFR, owing to the nucleating agent’s effect on raising the onset of crystallization under shear.

    How Does Nucleation Alter Crystal Superstructure and Haze in Transparent-Core Polypropylene?

    In nucleated homopolymers such as Formosa PP 3500, rapid spherulite initiation creates a fine-grained morphology that reduces internal light scattering compared to coarse non-nucleated systems, yet the absence of ethylene comonomer precludes the true optical clarity attainable with random copolymers. The haze value for a 1 mm injection-molded plaque measured per ASTM D1003 typically falls in the range of 30 % to 45 %. In contrast, a 35 MFR random copolymer containing 2.5 wt% ethylene can achieve haze below 15 %, making it the preferred choice for transparent houseware. However, the nucleated homopolymer retains a stiffness advantage: its flexural modulus of 1 600 MPa exceeds that of a comparable-flow random copolymer by 300 MPa to 400 MPa, which permits downgauging of rigid packaging sidewalls without compromising top-load strength. The crystallization rate differential also impacts warpage during cooling—anisotropic shrinkage in the flow and transverse directions can differ by as much as 0.4 percentage points, necessitating part geometry adjustments such as rib-to-wall thickness ratios of 0.5:1 and integrated corner radii of at least 0.8 mm to mitigate out-of-flatness.

    For closure systems with integrated living hinges, Formosa PP 3500 offers sufficient elongation at yield (8 % to 10 %, ISO 527-2) to survive repeated flexing, but the hinge’s endurance limit is governed more by molecular orientation during flow than by the initial MFR alone. Molds must be designed to place the hinge gate so that the melt front traverses the hinge region perpendicular to the flex axis, inducing orientation sufficient to withstand at least 5 × 10⁵ cycles at a flex angle of 180° before whitening or fracture, according to in-house durability testing conducted on 0.35 mm hinge thickness samples. Products formulated with a high-flow homopolymer alone, such as a 50 MFR grade, exhibit a lower fatigue threshold under identical conditions because of reduced chain entanglement density, whereas a low-MFR grade (4 g/10 min) may provide superior hinge performance but entails excessive injection pressure and risk of short shots in closures with intricate tamper-evident band features.

    What Differentiates a 35 MFR Homopolymer from Block Copolymers in Dashboard Carrier Assemblies?

    When comparing Formosa PP 3500 to a typical 20-MFR heterophasic copolymer used in automotive interior substrates, the homopolymer’s notched Izod impact strength at 23 °C is 2.5 kJ/m² (ISO 180/A), while a medium-impact block copolymer can reach 15 kJ/m² to 30 kJ/m² at the same temperature and retain ductile behavior down to -30 °C. This fundamental difference means that PP 3500 is not suited for airbag covers, glove-box doors, or any component subjected to cold-temperature impact without substantial impact-modifier addition. When 15 wt% to 20 wt% of an ethylene-propylene elastomer is compounded into the homopolymer using a co-rotating twin-screw extruder with an L/D ratio of 40:1 and a screw speed of 400 rpm, the notched Izod can be increased to 8 kJ/m² at 0 °C, but the flexural modulus drops to approximately 1 100 MPa. This trade-off must be managed through the incorporation of a high-aspect-ratio talc filler if stiffness is to be partially recovered; however, talc addition beyond 15 wt% alters the weld-line strength in complex flow paths and may reduce the fracture energy of sonic-welded joints by 30 % or more, a risk documented in component-level burst tests.

    When Hot Runner Balance Depends on Viscosity Consistency Within a Range of ±2 Pa·s

    On hot-runner systems with more than 16 drops, the cavity-to-cavity weight variation in caps molded from Formosa PP 3500 is strongly correlated with the melt viscosity stability at the shear rates characteristic of the manifold channels, typically 200 s⁻¹ to 800 s⁻¹. Capillary rheometry data ( ISO 11443, 230 °C, die L/D 30:1) indicates that the steady-shear viscosity at 400 s⁻¹ lies at 95 Pa·s ± 2 Pa·s when the MFR is maintained within the 32 g/10 min to 38 g/10 min band. Lot-to-lot excursions beyond this window have been observed to produce a 3 % to 5 % inter-cavity mass imbalance in 48-cavity stack molds, ultimately triggering downstream closure-liner insertion failures. Molders therefore integrate in-line rheometers or monitor specific injection work (energy per gram of material) as a real-time proxy; a rise in specific work exceeding 0.45 kJ/g without a corresponding increase in melt temperature signals molecular weight degradation that demands immediate purging of the hot-runner manifold to avoid carbonized deposits in the 0.8 mm nozzle tips.

    In masterbatch and compound production, Formosa PP 3500 serves as a high-flow carrier resin that facilitates pigment dispersion in single-screw extruder operations where distributive mixing is limited. The powder-form carrier masterbatch, when let down at 2 wt% in a 70 MFR random copolymer base, achieves a Color strength deviation (ΔE) of less than 0.5 units under D65 illuminant at 10° observer (ISO 11664-4) provided that the melt temperature during compounding is kept below 200 °C to protect thermally sensitive organic pigments. However, the combination of PP 3500 with peroxide-based controlled-rheology masterbatches in a twin-screw extruder operating above 600 rpm and 220 °C can cause a runaway chain-scission reaction that drives the final MFR beyond 45 g/10 min, producing an excessively fluid material that exhibits die drool and poor strand pelletizing. Published data for the long-term thermal oxidative stability of this specific grade in continuous-use applications above 100 °C is limited; accelerated aging per ISO 4577 at 150 °C in a forced-air oven indicates embrittlement within 360 hours unless a hindered phenolic antioxidant package is supplemented with a thioester synergist at a minimum total concentration of 0.15 wt%.

    PropertyTest StandardFormosa PP 3500Formosa PP 1040 (low MFR homopolymer)Formosa PP 7520 (impact copolymer)
    Melt mass-flow rate (230°C/2.16 kg)ISO 1133-135 g/10 min4 g/10 min20 g/10 min
    Tensile stress at yieldISO 527-236 MPa38 MPa27 MPa
    Flexural modulusISO 1781 600 MPa1 700 MPa1 200 MPa
    Notched Izod impact strength (23°C)ISO 180/A2.5 kJ/m²3.0 kJ/m²30 kJ/m²
    HDT B (0.45 MPa)ISO 75-2/B100 °C105 °C90 °C
    Mold shrinkage (flow direction)ISO 294-41.4 % – 1.8 %1.5 % – 2.0 %1.2 % – 1.6 %

    Food Contact and Hazardous Substance Compliance Under Migration Testing Protocols

    Formosa PP 3500 is manufactured in compliance with the compositional and extractive limits stipulated for polypropylene homopolymers intended for repeated contact with all food types, as defined by FDA 21 CFR 177.1520(c) 3.1 and EU Regulation 10/2011 with its subsequent amendments. Migration testing using simulants 10 % ethanol and 3 % acetic acid at 100 °C for 2 hours yields global migration values below 10 mg/dm², and specific migration of the nucleating agent (when a sorbitol-based clarifier is used) remains below the SML defined in Annex I of the regulation, provided the maximum processing temperature does not exceed 260 °C. The grade also satisfies the restricted substance criteria of Directive 2011/65/EU (RoHS) and has been assessed against the REACH Candidate List of substances of very high concern; no SVHC is intentionally added above the 0.1 wt% threshold. A summary of regulatory status is given below.

    Regulatory CriterionStandard or LegislationConformity Status
    Food contact – homopolymerFDA 21 CFR 177.1520Meets all requirements
    Plastic materials in food contactEU 10/2011Compliant under conditions of use A, B, C
    Restriction of hazardous substancesRoHS 2011/65/EUBelow maximum concentration values
    Chemical safety – SVHCREACH (EC) 1907/2006No reportable SVHC > 0.1 wt%
    Flammability classificationUL 94HB (nominal thickness 1.6 mm)
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