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REPOL PP Homopolymer H350FH

    • Product Name: REPOL PP Homopolymer H350FH
    • 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 823376
    Product REPOL PP Homopolymer H350FH
    Type Polypropylene Homopolymer
    Form Pellets
    Melt Flow Rate 230 C 2 16 Kg 35 g/10 min
    Density 0.905 g/cm³
    Tensile Strength At Yield 35 MPa
    Elongation At Yield 10%
    Elongation At Break 50%
    Flexural Modulus 1450 MPa
    Notched Izod Impact Strength 23 C 3 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 105°C
    Vicat Softening Point A50 155°C
    Rockwell Hardness R110
    Melting Point 165°C
    Water Absorption <0.01%

    As an accredited REPOL PP Homopolymer H350FH factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing REPOL PP Homopolymer H350FH is supplied in 25 kg sealed bags, protecting purity and ensuring safe, convenient handling.
    Container Loading (20′ FCL) 20' FCL container loading of REPOL PP Homopolymer H350FH: polypropylene resin pellets, packed in woven PP bags, palletized for safe transport.
    Shipping REPOL PP Homopolymer H350FH ships as non-hazardous polypropylene pellets in sealed bags, gaylord boxes, or bulk hoppers. Keep packaging dry, protected from direct sunlight, and away from ignition sources. Use clean handling equipment to avoid contamination. No dangerous goods classification applies under ADR/IMDG/IATA. Avoid generating dust during transfer.
    Storage Store REPOL PP Homopolymer H350FH in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep packaging sealed to prevent moisture or contamination. Store indoors on clean, dry surfaces, avoiding rough handling that may damage bags. Maintain moderate temperatures and protect from UV exposure to preserve material quality.
    Shelf Life Shelf life is typically 12 months if stored in original sealed packaging, away from heat, moisture, and direct sunlight.
    Application of REPOL PP Homopolymer H350FH

    On high-cavitation injection lines producing rigid food-contact containers with sidewall sections between 0.35 mm and 0.80 mm, REPOL PP Homopolymer H350FH is processed using a general-purpose PP screw with an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.5:1 to 3.0:1. The melt temperature at the nozzle is maintained between 230 °C and 250 °C, while core and cavity surface probes record mould temperatures between 10 °C and 30 °C. The lower mould-temperature bound preserves cycle times below 4.0 s on a 0.45 mm wall round cup, whereas the upper bound reduces moulded-in stress and post-demoulding corking in rectangular containers. Hot-runner manifold balance is controlled to a temperature differential of no more than 5 °C across drops, because a wider spread produces localised melt-temperature variation and directly increases part-mass scatter. Pack pressure is applied for 0.3–0.8 s depending on gate diameter; gate diameters below 0.8 mm with this melt-flow class frequently produce jetting and flow marks on tapered sidewalls. The grade is normally processed without predrying when surface moisture is below 0.1 %, but transfer from cold warehouses into a warm processing hall may require shallow-hopper drying at 80 °C for 2 h. Food-contact compliance is assessed under FDA 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011; the latter applies an overall migration limit of 10 mg/dm² for aqueous and dry simulants. Terminal products include dairy yogurt cups, delicatessen containers, vending cups and microwaveable meal trays. Top-load acceptance values for a filled 250 ml container are commonly specified in the range of 120–180 N, measured by ISO 12048 or an equivalent force-deflection test.

    ParameterThin-wall food packaging envelopeMeasurement or standard
    Melt mass-flow rate35 g/10 minISO 1133-1:2022, 230 °C, 2.16 kg
    Melt temperature230–250 °CNozzle thermocouple
    Mould temperature10–30 °CCore and cavity surface probes
    Hot-runner differential5 °CMulti-drop manifold balance
    Overall migration limit10 mg/dm²EU Regulation (EU) No 10/2011

    When Tamper-Evident Bridge Dimensions Are Reduced Below 0.25 mm

    Non-carbonated beverage, condiment and dry nutrition closures place the highest demands on melt flow in narrow bridge segments rather than on bulk impact strength. In high-cavitation closure tools with 24 to 96 cavities, REPOL PP Homopolymer H350FH is injected at melt temperatures of 220–240 °C and injection pressures below 1,200 bar. The tamper-evident bridge is commonly moulded at 0.20–0.35 mm; at the lower bridge dimension, valve-gate sequencing deviation above 0.05 s produces localised underfill at bridge tips because the polymer freezes before the pack phase builds pressure. Draft angles on the closure skirt are set at 1.5°–2.5° to control ejection force and prevent scoring of the tamper band. Food-contact closures are covered by FDA 21 CFR 177.1520 and EU (EC) No 1935/2004, with organoleptic screening under ISO 18103 for taint and odour. Finished closures on 28 mm PCO 1881 necks are routinely qualified at application torques of 1.8–2.5 N·m; above this range, stress cracking along the bridge root can initiate. Published data for H350FH in carbonated soft-drink closures above 2.5 volumes CO₂ is limited, and such applications are generally transferred to impact-modified PP grades. Amine-based antistatic or lubricant additives should be excluded from direct food-contact closure formulations because they can alter organoleptic profiles and reduce long-term bridge ductility.

    In disposable diagnostic and medical consumables, the constraints shift from bulk impact strength to flow length into micro-scale bosses, low sorption on reagent-contact surfaces and validated sterilisation stability. REPOL PP Homopolymer H350FH is processed neat or with a customer-qualified radiation-tolerant masterbatch into specimen collection cups, reagent reservoir bodies, analyser cuvette racks and transfer pipette bodies under cleanroom injection moulding. The base polymer does not carry a blanket medical conformity; biocompatibility is evaluated on the finished part using USP Class VI or ISO 10993-5 and ISO 10993-10 protocols as specified by the device owner. In cleanroom environments where ambient relative humidity exceeds 60 %, shallow-hopper drying at 80 °C for 2–3 h is required to prevent splay on polished mould surfaces. Mould temperatures are held between 15 °C and 25 °C to limit sink marks around standing bosses and to retain dimensional stability in microfluidic recesses. Gamma sterilisation at cumulative doses up to 50 kGy is commonly used for PP homopolymer, but the exact dose must be validated for colour shift and embrittlement because unstabilised homopolymer undergoes oxidative degradation after repeated high-dose irradiation. Ethylene oxide sterilisation is also applicable when aeration time is validated by the device manufacturer. The absence of impact modifier improves clarity and reduces sorption of aqueous reagents compared with impact-copolymer PP, but it limits drop resistance below 0 °C and is not recommended for load-bearing medical device housings.

    What Restricts Part Weight Reduction in High-Gloss Houseware Components Below 0.8 mm?

    Houseware and small appliance component producers specify high-flow PP homopolymer for thin-walled storage bases, drawer organisers, clothes hanger bodies, and handheld vacuum cleaner nozzle bodies where surface gloss and rigidity are primary specifications. REPOL PP Homopolymer H350FH is processed in a 12-cavity insulated food storage container tool at melt temperatures of 220–240 °C and a mould temperature of 20 °C. The main process conflict is between rapid cooling and surface gloss: cooling below 15 °C reduces total cycle time to 8–10 s but induces flow hesitancy and visible weld lines at handle-to-body junctions. Gloss is measured at 60° specular angle according to ASTM D523; on ungated smooth surfaces, homopolymer PP typically falls between 70–85 GU depending on mould polish, while textured surfaces require profilometer characterisation rather than specular gloss values. Load-bearing components used above 60 °C must be evaluated for creep, because tensile modulus retention of homopolymer PP declines under sustained load. Colour masterbatch addition above 2 % can shift melt flow and should be qualified separately against lot-to-lot part mass. Terminal products include reusable food storage bases, domestic storage boxes, hangers and small appliance nozzle bodies.

    In returnable thin-wall logistics trays, impact-copolymer toughness is not automatically required when wall sections are below 1.2 mm and service loads are predominantly compressive or short-span. REPOL PP Homopolymer H350FH is injection moulded into twin-wall or ribbed sidewall designs on high-pressure machines with clamp force above 300 t for 2+2 stackable tray tools. Melt temperature is held at 230–250 °C and mould temperature at 10–20 °C to permit cycle times below 20 s. Rib-to-wall thickness ratios are maintained below 60 % of the nominal wall to avoid sink marks on base platforms where label or tag inserts are placed. Because homopolymer PP loses impact resistance at low temperatures, trays operating at 2–4 °C in chilled distribution must be tested for puncture impact under ISO 6603-2 at the minimum service temperature. Stackability is validated by a top-load creep test at 40 °C for 24 h. Terminal products include egg transport flats, bakery stacking trays and parcel sequence trays.

    Office Filing and Thin-Gauge Stationery Moulding Conditions

    Thin-wall stationery and filing products are moulded from REPOL PP Homopolymer H350FH at melt temperatures of 220–240 °C into file tray bodies, magazine files and binder spines with wall sections between 1.0 mm and 2.5 mm. The dominant technical criterion is resistance to stress whitening at snap-fit spine hinges, measured by three-point flexural recovery at 23 °C according to ISO 178 at a crosshead speed of 2 mm/min; the absence of visible whitening after 50 flexural cycles is commonly specified rather than a fixed modulus value. Reground material from rejected parts is re-introduced at up to 20 % when dark colours allow, provided particle size is below 5 mm and feeding is homogeneous.

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    Certification & Compliance
    More Introduction

    REPOL PP Homopolymer H350FH is a high-flow, nucleated polypropylene homopolymer supplied by Reliance Industries Limited for injection-moulded thin-wall packaging, caps, closures, housewares, and appliance components. The grade is classified as a polypropylene homopolymer and is supplied as natural or white pellets. Its nominal melt mass-flow rate is 35 g/10 min when measured under ISO 1133-1:2022 condition M at 230 °C and 2.16 kg load. Typical density is 0.905 g/cm³ under ISO 1183-1. Tensile yield stress is 34 MPa under ISO 527-2/1A/50; flexural modulus is approximately 1800 MPa under ISO 178; notched Izod impact strength at 23 °C is 2.5 kJ/m² under ISO 180/A. Heat deflection temperature at 0.45 MPa is approximately 105 °C under ISO 75-2/B; Vicat softening temperature is approximately 154 °C under ISO 306/A50. The defining processing characteristic of H350FH is controlled nucleation, which increases flexural modulus and reduces solidification time relative to non-nucleated homopolymers of comparable melt flow. Intended part-wall thicknesses range from 0.4 mm to 2.0 mm. In comparison with low-melt-flow raffia grades such as REPOL H030SG with a nominal 3.0 g/10 min melt flow, H350FH is not suitable for tape extrusion or woven sack production because the high melt flow reduces orientation-induced tensile strength in stretched tape.

    Does H350FH Differ from H350FG in Stiffness and Solidification Rate?

    The primary material difference between H350FH and the non-nucleated H350FG reference grade is the presence of a dispersed nucleating agent system. In the H350FH formulation, the heterogeneous nucleating particles increase the number of spherulitic nucleation sites during crystallisation. The result observed in injection-moulded plaques is a flexural modulus shift from approximately 1550 MPa to 1800 MPa when measured under ISO 178 at 2 mm thickness. The same crystallisation acceleration reduces the isothermal crystallisation half-time; differential scanning calorimetry under ISO 11357-7 shows crystallisation onset temperatures approximately 8 °C to 12 °C higher than the non-nucleated grade. On production moulding cells, this permits earlier gate freeze-off and ejection, and in multi-cavity closure tools the cycle-time reduction is commonly achieved without increasing mould temperature. The grade’s higher nucleation density also lowers haze in thin sections; haze measured on a 2 mm plaque under ASTM D1003 is typically below 40%, while the non-nucleated reference is above 45%.

    PropertyREPOL H350FH typicalREPOL H350FG typicalTest standard
    Melt mass-flow rate at 230 °C, 2.16 kg35 g/10 min35 g/10 minISO 1133-1:2022
    Tensile yield stress34 MPa32 MPaISO 527-2/1A/50
    Flexural modulus1800 MPa1550 MPaISO 178
    Notched Izod impact at 23 °C2.5 kJ/m²3.0 kJ/m²ISO 180/A
    Heat deflection temperature at 0.45 MPa105 °C100 °CISO 75-2/B
    Haze on 2 mm injection-moulded plaque38%48%ASTM D1003

    Representative values are manufacturer-reported typical data and are not procurement specifications.

    Melt Rheology, Gate Freeze-Off, and Multi-Cavity Filling Behaviour

    Melt rheology of H350FH follows pseudoplastic behaviour. At a melt temperature of 230 °C, apparent viscosity decreases from approximately 140 Pa·s to 30 Pa·s as shear rate increases from 100 s⁻¹ to 1000 s⁻¹. The grade is processed on reciprocating-screw injection moulding machines with screw L/D ratios between 20:1 and 24:1 and compression ratios between 2.2:1 and 2.6:1. A shut-off nozzle or valve-gate hot runner is recommended because the high melt flow can produce nozzle drool in standard open nozzles. Melt temperature should be controlled in the range 220 °C to 250 °C. Residence time above 270 °C should be limited to less than 5 minutes to avoid thermo-oxidative chain scission and odour generation. Back pressure of 0.3 MPa to 0.7 MPa is used to disperse the nucleating agent; back pressure above 1.0 MPa increases screw recovery torque and may lower throughput. Injection speed in thin-wall sections below 1.0 mm should be set at 60 mm/s to 120 mm/s to prevent premature freeze-off. Holding pressure typically falls between 30% and 60% of peak injection pressure, with holding time set by gate seal measurement rather than a fixed value. In a 0.8 mm wall-thickness container, gate seal time is usually less than 2.5 s when the mould is run at 25 °C.

    On 16-cavity hot-runner closure moulds with clamp force of 150 t to 200 t, increasing mould temperature from 20 °C to 40 °C improves gate mark appearance but extends cycle time by approximately 1.2 s to 1.8 s. Decompression distance of 2 mm to 3 mm after screw recovery is applied to reduce stringing from valve-gate nozzles. Shot weight should be maintained between 30% and 70% of barrel capacity to limit residence time and maintain melt homogeneity.

    Food-contact compliance for H350FH is not established by a single resin certificate. Converter-specific migration testing under EU Regulation (EU) No 10/2011 using the appropriate food simulant for the intended use is required. A general label claim without end-use testing is not valid. Because polypropylene is hydrophobic, moisture absorption after 24 h immersion at 23 °C is below 0.02% under ISO 62; pre-drying is not normally required unless the pellets have gross surface water from outdoor storage. Storage above 80 °C for prolonged periods can deplete stabiliser packages and should be avoided. The product contains no intentionally added per- and polyfluoroalkyl substances.

    Regulatory areaStandard or regulationBasis or numerical threshold
    Food-contact resin compositionFDA 21 CFR 177.1520(c) 1.1Homopolymer polypropylene intended for food-contact use subject to end-use migration testing.
    European plastics food-contactEU Regulation (EU) No 10/2011, Annex IOverall migration limit 10 mg/dm² under specified simulant conditions; specific migration of additives must be confirmed.
    Heavy metals in packagingEU Packaging Directive 94/62/ECSum of Pb, Cd, Hg, Cr(VI) not exceeding 100 mg/kg.
    REACH SVHCRegulation (EC) No 1907/2006, Article 33No SVHC intentionally added above 0.1% w/w.
    RoHS recastDirective 2011/65/EU, Annex IIBelow maximum concentration values 0.1% w/w for Pb, Hg, Cr(VI), PBB, PBDE; 0.01% w/w for Cd.

    The grade is supplied with a manufacturer regulatory declaration only. Final article compliance must be verified by the converter because additive masterbatches, colourants, and process residues can alter the regulatory status of the finished product.

    Where H350FH Reaches Its Operational Boundary

    Limitations of REPOL H350FH arise from its homopolymer structure and high crystallinity. The grade is not intended for applications requiring ductile impact resistance below 0 °C; notched Izod values typically fall below 2.0 kJ/m² at 0 °C under ISO 180/A, and the ductile-to-brittle transition of unfilled homopolymer polypropylene is ordinarily near 0 °C. For freezer containers, caps, and closures, a heterophasic impact copolymer or an impact-modified grade should be selected. Outdoor parts require a UV stabiliser masterbatch; unstabilised homopolymer polypropylene undergoes surface chalking and tensile strength loss after 6 months to 12 months of tropical outdoor exposure when evaluated under ISO 4892-2 accelerated weathering protocols. The grade is also unsuitable for continuous service above 90 °C without load-bearing derating; heat deflection temperature under 0.45 MPa is approximately 105 °C, and creep under load must be assessed for pressurised containers.

    Combination with halogenated flame-retardant systems is not recommended because homopolymer polypropylene has low thermal stability with acid-generating additives; if flame retardancy is required, an intumescent phosphorus-nitrogen system should be evaluated with mechanical property loss measured under ISO 527-2 and ISO 178. Processors should not blend H350FH with high-density polyethylene at levels above 10% by weight for rigid packaging without performing rheological and tensile verification; incompatibility reduces weld-line strength and gloss. Published data for this specific blend configuration is limited, and weld-line tensile strength should be measured under ISO 527-2 using an insert mould before production release.

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