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Propilven PP Homopolymer J-300

    • Product Name: Propilven PP Homopolymer J-300
    • 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 964734
    Polymer Type Homopolymer Polypropylene
    Melt Flow Rate 230 C 2 16 Kg 3.0 g/10 min
    Density 0.905 g/cm³
    Tensile Strength At Yield 33 MPa
    Elongation At Yield 12%
    Flexural Modulus 1500 MPa
    Izod Impact Strength Notched 23 C 3.5 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 100 °C
    Vicat Softening Point 155 °C
    Rockwell Hardness R95
    Mold Shrinkage 1.5%
    Barrel Temperature Typical Injection 190-230 °C

    As an accredited Propilven PP Homopolymer J-300 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Propilven PP Homopolymer J-300 is supplied as solid pellets in 25 kg bags, with packaging designed for safe handling and storage.
    Container Loading (20′ FCL) Container Loading (20′ FCL): One 20-foot full container load of Propilven PP Homopolymer J-300, packed in bags and secured for safe transport.
    Shipping Propilven PP Homopolymer J-300 is a polypropylene homopolymer resin, shipped as non-hazardous material. It is transported in clean, dry containers or bulk bags, protected from moisture and direct sunlight. Standard handling applies; no UN dangerous goods classification required. Keep away from ignition sources and store in a well-ventilated area.
    Storage Store Propilven PP Homopolymer J-300 in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and open flames. Keep in its original sealed packaging to prevent moisture absorption and contamination. Avoid contact with strong oxidizers and store elevated, protected from mechanical damage. Ensure good ventilation and follow local regulations.
    Shelf Life Store in a cool, dry place away from sunlight and heat. Shelf life is 12 months from manufacture when properly sealed.
    Application of Propilven PP Homopolymer J-300

    Propilven PP Homopolymer J-300 is moulded into thin-wall dairy containers, delicatessen tubs, and reusable food transport trays on hydraulic injection presses of 60–120 tonnes clamp force. Melt temperature is held at 220–245°C; tool wall temperature is set at 10–25°C to force rapid solidification of the skin layer. The pellets do not require desiccant drying when stored in closed silos below 60% relative humidity, but surface condensation during moist conveyor transfer introduces splay and flow marks at the gate. Thin-wall tools with nominal wall thickness of 0.8–1.2 mm are filled at injection velocities between 150 mm/s and 300 mm/s through valve-gated hot-runner drops; edge gating produces offset core orientation and increases warpage. Holding pressure is staged from 40 MPa to 60 MPa, and back pressure is limited to 5–10 MPa to avoid excessive shear heat and molecular weight loss. The screw should have L/D of 20:1–24:1, a compression ratio of 2.5:1–3.0:1, and a non-return valve with clearance below 0.05 mm to prevent melt leakage during holding. The frozen skin is a smectic quenched structure, while the core develops spherulites; this gradient controls both haze and post-mould shrinkage. Sidewall thickness variation above 0.2 mm produces differential cooling and lid seal distortion in dairy containers. Draft angles are maintained at 1°–3° on sidewalls and 0.5°–1° on ribs. Food contact clearance is assessed under FDA 21 CFR 177.1520(c) and European Commission Regulation (EU) No 10/2011 Annex I, with overall migration testing according to EN 1186-1 and specific migration of propylene according to EN 13130-1. Published data for J-300 in this specific packaging configuration are limited; converter-run migration and organoleptic protocols must be executed on production tools.

    Thin-wall injection process envelope for Propilven J-300
    ParameterLower set pointUpper set pointReference method or equipment
    Melt temperature220°C245°CResin melt probe
    Tool wall temperature10°C25°CMould thermocouple
    Injection velocity150 mm/s300 mm/sScrew position transducer
    Holding pressure40 MPa60 MPaHydraulic or electric pressure transducer
    Back pressure5 MPa10 MPaHydraulic pressure transducer
    Nominal wall thickness0.8 mm1.2 mmMould dimension
    Cooling time6 s12 sMould thermocouple

    Which screw geometries safeguard closure integrity in high-speed cap moulding?

    High-cavitation closure tools for Propilven J-300 run with 32–96 cavities and require barrier screws or double-flighted designs with L/D of 22:1–24:1 and compression ratio of 2.5:1–3.0:1. A Maddock mixer after the metering section disperses any remaining unmelted granules; homopolymer PP pellets with a narrow melting point leave white specks if plasticising is incomplete. Melt temperature is set at 230–255°C, nozzle temperature is kept 10–20°C below the melt to prevent drool, and tool temperature is maintained at 10–20°C for cycle times of 6–10 s. Tamper-evident bridges are slit on the tool; their break force depends on bridge thickness and PP homopolymer yield stress, with production tools targeting 1.5–3.0 N per bridge for 28 mm beverage closures. Gate-to-gate fill imbalance above ±4% on a 32-cavity stack raises the reject rate because tamper band hinge thickness varies below 0.35 mm and develops microcracks during demoulding. Torque retention after application is governed by creep under constant stress; closures aged at 40–60°C for 24–48 h before shipment show more stable removal torque. Physical conformance uses ISO 1133-1:2022 for melt flow rate, ISO 1183-1:2019 for density, ISO 527-2:2012 for tensile yield, ISO 178:2019 for flexural modulus, and ISO 180/A for notched Izod impact. Carbonated beverage closures must retain 2.5–3.5 volumes CO₂; PP homopolymer is not stress-cracked by carbonic acid but embrittles below −20°C. Cold-chain distribution below 0°C requires an impact copolymer or an elastomer-toughened grade. Published data for J-300 closure-specific performance are limited; validation on the multicavity tool is performed before commercial release.

    Rigid houseware and storage container sink mark control

    Storage boxes, hampers, compartment trays, and bins moulded from J-300 exhibit linear mould shrinkage between 1.2% and 1.8% under ISO 294-4; anisotropic shrinkage between flow and transverse directions reaches 0.2–0.4 percentage points. Undercuts and rib intersections are the controlling features for sink mark depth. Rib root thickness is kept at 50–60% of the adjacent wall; rib sections above 65% of the wall create visible sink marks and internal voids. Packing pressure is staged from 50 MPa to 25 MPa over 4–8 s, and gate freeze is confirmed before holding pressure is removed. Tool temperature of 15–30°C supports short cycle times, but thick bases with wall thickness above 3.0 mm require 40°C mould surfaces to reduce differential orientation and warpage. Open-topped storage containers need separate rim cooling circuits; differential cooling between the rim and base creates planoform distortion above 1.0 mm per 300 mm of length. Load-bearing pails are tested by ISO 12048 compression at 23°C and 40°C. Unfilled PP homopolymer retains flexural modulus near 1,300 MPa at 23°C, but creep at 40°C lowers long-term stacking load. Outdoor housewares require 0.2–0.5 wt% hindered amine light stabiliser and 0.1–0.3 wt% phenolic antioxidant; without these, tropical UV exposure produces surface crazing within 6–12 months.

    When J-300 replaces amorphous copolymers in appliance structural brackets

    Substitution of acrylonitrile-butadiene-styrene or high-impact polystyrene with Propilven J-300 in brackets, detergent drawers, and pump housings requires redesign of snap fits and weld joints. The homopolymer has density near 0.90 g/cm³ under ISO 1183-1:2019 and tensile yield stress near 34 MPa under ISO 527-2:2012; notched Izod impact under ISO 180/A is below 3 kJ/m² at 23°C. Snap-fit deflections that are acceptable in ABS at 1.0 mm fail in unfilled PP unless the beam deflection is reduced below 0.5 mm or insertion is limited to one cycle. Crystallisation shrinkage of 1.2–1.8% creates dimensional tolerance ranges wider than ±0.5%; mould flow analysis must overlay gate location, cooling-circuit layout, and cavity pressure curves. Chemical resistance removes environmental stress cracking in chlorinated detergent solutions that attacks ABS, but the heat deflection temperature under ISO 75-2 method B at 0.45 MPa is near 90°C. Appliance parts requiring glow-wire resistance at 750°C under IEC 60695-2-11 can use an unfilled HB-rated PP only when final product standards allow horizontal burning; V-2 or V-0 grades require flame-retardant compounds not present in neat J-300. Comparative tracking index under IEC 60112 is above 600 V for clean unfilled PP but decreases with carbon black or talc. Ultrasonic welding is preferred for non-planar joints; hot-plate welding at surface temperatures of 200–220°C gives slow melt fronts because thermal conductivity is near 0.20 W/m·K. J-300 is limited to non-appearance structural brackets where dimensional tolerance ranges of ±0.5 mm or larger are permissible.

    In non-implantable laboratory consumables, Propilven PP Homopolymer J-300 is moulded into pipette tips, centrifuge tubes, reagent bottles, and specimen containers. Melt temperature is maintained at 220–250°C, mould temperature at 15–30°C, and screw L/D at 20:1–24:1 with a shut-off nozzle to prevent melt leakage during plastication. Pipette tips are gated at the distal orifice to keep the conical wall weld-free; gate vestige height is held below 0.10 mm because liquid handling accuracy depends on tip coaxiality. Autoclave sterilisation at 121°C for 15 min is permissible only for freely supported thin parts; load-bearing components deform because modulus falls sharply above 90°C. Gamma irradiation at 25 kGy causes chain scission, yellowing, and embrittlement in unmodified PP; ethylene oxide or electron beam at doses below 10 kGy is the preferred sterilisation route for J-300 unless migration and mechanical data support gamma use. Cytotoxicity is evaluated under ISO 10993-5; lot-by-lot validation is required because the base resin is not automatically certified for every medical route. Under European Commission Regulation (EU) No 10/2011, overall migration into simulant A, B, or C is limited to 10 mg/dm². United States Pharmacopeia Class VI extraction data are required for parenteral or implantable routes; J-300 is not appropriate for long-term implantable use. Published data for J-300 under repeated sterilisation are limited; mechanical testing after 10 autoclave cycles is required for any reusable diagnostic device.

    Compliance matrix for J-300 in non-implantable labware
    RequirementStandard or codeTypical accepted result
    Overall migration in food simulantsEU Regulation (EU) No 10/2011≤10 mg/dm²
    Food contact olefin polymerFDA 21 CFR 177.1520(c)Extractable fraction maxima per regulation
    CytotoxicityISO 10993-5Cell viability ≥70%
    Biological reactivityUSP 88 Class VINo systemic toxicity after 72 h
    Melt mass-flow rateISO 1133-1:2022Injection moulding range 10–14 g/10 min at 230°C/2.16 kg
    Notched Izod impactISO 180/A≥2.5 kJ/m² at 23°C

    Processing window for industrial crates and returnable pallets

    Returnable transport packaging moulded from J-300 includes ventilated crates, pallet boxes, and industrial tote bodies with wall thickness above 2.0 mm. The polymer is processed at melt temperatures of 230–260°C on accumulator-assisted machines with shot capacities above 1,500 g; plasticising time is the dominant cycle constraint because unfilled PP pellets are not preheated. Tool temperature is held at 10–20°C to reduce cooling time, but thick ribs in pallet legs require bubblers and spiral cooling channels to avoid sink marks and internal porosity. Differential shrinkage between the top deck and the ribbed base creates flatness deviation of 3–8 mm per 1,000 mm when steel temperatures vary by more than 5°C. Stacking load is evaluated by ISO 8611-1 for pallets and by ISO 12048 or ASTM D642 for crates. Creep under stacked load at 40°C is the limiting failure mode; racking loads above 500 kg require corner reinforcement, inserts, or a transition to a higher-modulus filled grade. Unfilled J-300 is not suitable for freezer pallets because notched Izod impact under ISO 180/A drops below 2 kJ/m² at −20°C. UV stabilisation with 0.3–0.5 wt% carbon black provides outdoor storage for 3–5 years. Post-industrial regrind is limited to 10–15%; higher levels degrade notched impact and increase melt-flow instability across shots.

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    Certification & Compliance
    More Introduction

    Propilven PP Homopolymer J-300 is classified under ISO 19069-1 as a PP-H polypropylene homopolymer with a nominal melt mass-flow rate of 3.0 g/10 min determined by ISO 1133-1:2022 at 230 °C/2.16 kg. The numerical suffix in the grade designation corresponds to this nominal 3.0 flow index, placing the grade in the low-flow homopolymer segment for general-purpose injection moulding, sheet extrusion, and thick-wall rigid components. Because the polymer contains no ethylene comonomer, it is distinguishable from random and heterophasic polypropylene grades; the crystalline phase is predominantly α-form polypropylene with a density of 0.903 g/cm³ when measured by ISO 1183-1:2019. The material is supplied as natural free-flowing pellets in 25 kg multilayer bags or bulk hopper systems; storage at ambient temperature below 40 °C is recommended to avoid pellet blocking and oxidative ageing of the stabilizer package.

    In industrial practice, J-300 is transferred directly to the hopper without pre-drying unless surface moisture exceeds 0.05 wt% after storage at relative humidity above 80 %. In that condition, drying in a dehumidified-air hopper at 80 °C for 2 h is applied. The grade is evaluated for compliance with 21 CFR 177.1520 for olefin polymers intended for food-contact use, subject to supplementary migration testing by the article converter under the intended conditions of use. As a polypropylene homopolymer with no intentionally added heavy-metal-based pigments, the product is also assessed against the restrictions in Annex II of RoHS Directive 2011/65/EU for homogeneous materials.

    What Processing Window Does J-300 Require on Reciprocating-Screw Injection Machines?

    Melt temperature at the nozzle should be maintained between 210 °C and 240 °C, with the rear zone of the barrel set 10–20 °C lower to prevent bridging in the feed zone. Cylinder temperature profiles above 260 °C for sustained residence periods cause chain scission and melt-flow drift; on a 70 mm single-screw extruder with 30:1 L/D, a residence time greater than 8 min at 260 °C is avoided because subsequent lot samples exhibit measurable shift of the melt mass-flow rate under ISO 1133-1. For reciprocating screws with 20:1–22:1 L/D, screw surface speed of 0.4 m/s maximum limits shear heating; back pressure in the range 0.5–1.5 MPa maintains shot-to-shot melt density consistency. Mould temperature is typically controlled from 20 °C to 50 °C, with the upper half of the range used for opaque parts requiring lower surface stress whitening. Injection pressure is normally 70–100 MPa; hold pressure is held at 50–70 % of the initial injection pressure, and switch-over is triggered by screw position or cavity pressure at 6 MPa.

    Because J-300 has a low melt-flow index relative to thin-wall grades, gate sizing must account for higher melt viscosity. Freeze-off at edge gates with land thickness below 0.8 mm can occur before complete packing of ribs and bosses; for a 2.0 mm nominal wall section, gate land thickness of 0.8–1.2 mm and gate width of 50–75 % of the local wall thickness are used. In multi-cavity tools with hot-runner manifolds, cavity-to-cavity balance is checked by short-shot mass variation; deviations greater than 5 % are corrected by manifold temperature trim of 5–10 °C.

    For mechanical design calculations using datasheet typical values, the following properties are reported. Because polypropylene homopolymer exhibits strain-rate and temperature dependence, the values should not be extrapolated to continuous load-bearing designs without creep and stress relaxation data under ISO 899-1.

    PropertyStandardTypical value
    Melt mass-flow rate (230 °C, 2.16 kg)ISO 1133-1:20223.0 g/10 min
    Density (23 °C)ISO 1183-1:20190.903 g/cm³
    Tensile stress at yield, Type I specimen, 50 mm/minASTM D638-1434 MPa
    Tensile elongation at yieldASTM D638-1411 %
    Flexural modulus, 1 % secant, 13 mm/minASTM D790-171,450 MPa
    Notched Izod impact (23 °C)ASTM D256-10e128 J/m
    Rockwell hardness, R scaleASTM D785-1595
    Vicat softening temperature, A50ISO 306:2022154 °C
    Heat deflection temperature, 0.455 MPaISO 75-2:2013, Method B95 °C
    Mould shrinkage, flow/transverseISO 294-4:20181.4–1.6 %
    Xylene-soluble fractionISO 16152:2005<4 %

    These values correspond to production-lot average data and are not release limits. For lot-specific values, the certificate of analysis delivered with each batch should be used; the producer's release specification typically includes melt mass-flow rate, ash content, and tensile yield stress.

    Injection Moulding Parameter Drift in Multi-Cavity Tools

    During production-scale evaluation on a 150 t hydraulic injection moulding machine with a 16-cavity hot-runner tool and valve-gate drops, cavity pressure sensors positioned at the last 20 % of flow length recorded cavity pressure peak values of 30–35 MPa when mould temperature was held at 35 °C. The switch-over to hold phase was set when the sensor at the gate read 6 MPa. Under these conditions, the pressure at the end of fill was reproducible within ±2 MPa across a 500-cycle stabilisation window.

    Post-moulding shrinkage measured according to ISO 294-4 on plaques 60 mm × 60 mm × 2 mm was 1.5 % in flow direction and 1.3 % transverse at 24 h after demoulding; after 48 h, total shrinkage increased by less than 0.1 percentage points. Higher injection speeds above 120 mm/s in the moulding machine cylinder can increase molecular orientation and flow-direction shrinkage by up to 0.3 percentage points; this is managed by reducing melt temperature to 220 °C and increasing hold time by 2–3 s.

    A processing conflict exists between low temperature to minimize degradation and sufficient melt temperature to avoid gate blush. At nozzle temperatures below 205 °C, high injection pressure leads to jetting and visible flow marks on polished cavities; at nozzle temperatures above 250 °C, dimensional stability decreases because post-moulding crystallinity changes. The practical operating window in production is therefore approximately 210–240 °C, with barrel residence time limited to 6–8 min.

    When J-300 Replaces Heterophasic Copolymer in Cold-Impact Applications

    The most significant operational boundary of J-300 arises at subambient temperatures. As a homopolymer without an ethylene-propylene rubber phase, the notched Izod impact value under ASTM D256 at 23 °C is approximately 28 J/m; at -20 °C the value falls below 20 J/m, producing brittle crack propagation. By comparison, a heterophasic polypropylene impact copolymer with a melt mass-flow rate near 4 g/10 min typically retains notched Izod values of 60 J/m or more at -20 °C, making it the appropriate choice for low-temperature containers and appliance components subjected to dropping. A converter replacing a heterophasic copolymer with J-300 in a part exposed to cold impact must therefore revalidate the part under the relevant drop-test standard, such as ASTM D5276 or ISO 6603-2 for instrumented puncture testing.

    Comparative propertyPropilven PP Homopolymer J-300High-flow PP homopolymer, nominal MFR 20 g/10 minHeterophasic PP impact copolymer, nominal MFR 4 g/10 min
    Melt mass-flow rate, 230 °C/2.16 kg3.0 g/10 min20 g/10 min4 g/10 min
    Flexural modulus, ASTM D790-171,450 MPa1,600 MPa1,050 MPa
    Notched Izod impact, 23 °C, ASTM D25628 J/m24 J/m200 J/m
    Notched Izod impact, -20 °C, ASTM D256<20 J/m<20 J/m60 J/m
    Vicat softening temperature, A50, ISO 306:2022154 °C153 °C140 °C
    Mould shrinkage, ISO 294-4:20181.4–1.6 %1.2–1.4 %1.0–1.4 %

    Published data for this specific configuration is limited for high-flow homopolymer comparators in the same producer portfolio; the values in the table represent typical ranges from technical bulletins and should be confirmed by certificate of analysis for each grade. The higher tensile stiffness of J-300 is a differentiating feature in rigid, creep-sensitive applications such as appliance frames and heating-ventilation ducting, where dimensional recovery after load is measured by creep modulus under ISO 899-1.

    During sheet extrusion on a 75 mm single-screw extruder with 30:1 L/D and a barrier screw, J-300 is processed with a flat temperature profile of 210–230 °C from feed to metering, and die temperature of 230 °C. The screen changer is equipped with a 60/80/60 mesh pack to retain contaminant particles above 0.15 mm. For sheet thickness of 1.0–3.0 mm, the polished roll stack is maintained at 80 °C to control clarity and reduce dynamic surface quench marks. The extruder head pressure is typically 12–18 MPa depending on throughput; melt temperature is checked at the die lip with an insertion thermocouple.

    Because melt strength of a 3.0 g/10 min homopolymer is higher than a 20 g/10 min grade, J-300 exhibits lower sag in thermoforming preheating; sheet surface temperature for plug-assisted forming is adjusted to 155–165 °C, monitored by infrared pyrometer, and sag depth is limited to 10 mm over a 500 mm span. Thermoformed parts are evaluated for wall-thickness distribution against ISO 2818 sampling; corner-thinning below 60 % of nominal wall is rejected for rigid packaging applications requiring top-load capacity.

    The grade is not compatibilised with polar engineering thermoplastics; blending with PET or polyamide without a maleic anhydride-grafted PP coupling agent results in delamination and loss of weld-line strength under ISO 527-1. It is also not recommended for use with amine-based acid scavengers at elevated processing temperatures because potential interaction with stabilizer chemistry can shift colour to yellow; published data for this specific configuration is limited.

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