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Polycomp PDR CB 08 UV2 PP Copolymer

    • Product Name: Polycomp PDR CB 08 UV2 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 802541
    Density 0.905 g/cm³
    Melt Flow Rate 8.0 g/10min (230°C, 2.16 kg)
    Tensile Strength At Yield 24.0 MPa
    Elongation At Break 50.0 %
    Flexural Modulus 1100 MPa
    Izod Impact Notched 23c 8.0 kJ/m²
    Heat Deflection Temperature 1 80mpa 55.0 °C
    Vicat Softening Temperature 150.0 °C
    Uv Resistance UV-stabilized, excellent weathering resistance
    Carbon Black Content 2.5 %

    As an accredited Polycomp PDR CB 08 UV2 PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Polycomp PDR CB 08 UV2 PP Copolymer is supplied as granules in 25 kg sealed polyethylene-lined bags, protecting against moisture and contamination.
    Container Loading (20′ FCL) 20′ FCL container loading: Polycomp PDR CB 08 UV2 PP Copolymer packed in bags on pallets, secured for safe transport.
    Shipping Polycomp PDR CB 08 UV2 PP Copolymer ships as a dry, free-flowing granular solid in sealed, moisture-barrier bags or drums. Transport in clean, dry containers, protected from extreme heat and direct sunlight. Handle with care to avoid dust generation. See SDS for handling, ventilation, and disposal requirements.
    Storage Store in a cool, dry, well-ventilated area away from direct sunlight, heat sources, open flames, and strong oxidizers. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid static discharge and dusty conditions. Maintain moderate room temperature; under these conditions, the PP copolymer remains stable for its specified shelf life.
    Shelf Life 12 months from manufacture date when stored in original, unopened packaging in a cool, dry place.
    Application of Polycomp PDR CB 08 UV2 PP Copolymer

    In automotive exterior lower trim applications, the UV-stabilised black PP impact copolymer designated Polycomp PDR CB 08 UV2 is typically selected when the part combines thin ribs, long flow paths and low-temperature impact requirements without the cost penalty of a compounded elastomer-rich TPO. Molten material is held at 210 °C to 240 °C, with the nozzle set at 200 °C to 220 °C and the mould maintained at 20 °C to 60 °C; hydraulic back pressure is normally limited to 0.5 MPa to 1.0 MPa to avoid excessive shear on the stabiliser package. The mould shrinkage of this class of PP impact copolymer is generally 1.0% to 1.5%, but the exact value must be read from the supplier datasheet because carbon black loading and the UV2 additive package can shift cross-flow shrinkage by several tenths of a percentage point. Automotive qualification programmes commonly reference ISO 179-1/1eA Charpy notched impact at −30 °C with a minimum of 6 kJ/m² for wheel arch liners and side sill claddings, while underhood-adjacent exterior parts are sometimes tested at −40 °C to account for cold-soak conditions. Weatherability is validated under ISO 4892-2 Cycle 1 with a black panel temperature of 65 °C and a dry/spray cycle of 102/18 min; after 1,500 h, surface cracking must be absent and the colour shift ΔE should remain below 3 for most OEM visible black parts. The primary processing failure observed on multi-gate side sill tools is a weld line in the impact-critical lower flange; instead of raising melt temperature across the entire melt stream, the preferred corrective action is to raise holding pressure at the secondary gate to 3.5 MPa to 5.0 MPa and reduce melt-front velocity to 0.5 m/s to 0.8 m/s in the weld zone. Regrind addition should not exceed 20 wt% for exterior black parts because additive-rich regrind can shift viscosity and produce visible black-tone variation across the moulding. The material should be supplied with a REACH 1907/2006/EC SVHC statement and a RoHS 2011/65/EU Annex II compliance statement covering cadmium, lead, mercury, hexavalent chromium, PBB and PBDE, since these are routine documentary requirements for exported automotive service parts. Finished products in this segment include wheel arch liners, side sill extensions, lower bumper brackets, mudguard shells, undertrays and bumper lower grilles, where the black UV2 system is expected to maintain matte surface integrity under direct sunlight.

    What Limits the Weatherability Threshold for Garden Furniture and Cordless Tool Housings?

    Outdoor furniture shells, planter modules, storage box lids and cordless garden tool housings impose a different failure hierarchy from automotive parts because the visible surface is textured, the part is often assembled outdoors without paint, and consumer-level weathering is assessed after two or more summer seasons. The main qualification standard for this segment is ISO 4892-2 Cycle 2, in which specimens are exposed to xenon-arc radiation at 0.51 W/m² at 340 nm, a black panel temperature of 65 °C, and 18 min of water spray within a 120 min cycle; a high-tier garden furniture specification commonly requires ΔE of no more than 3 after 2,000 h and retained Charpy notched impact strength of at least 60% of the original value. With black UV-stabilised PP copolymer, the decisive process variable is not stabiliser dosage alone but the degree of dispersion in the finished moulded wall; carbon black agglomerates above 1 µm can act as crack initiation sites and accelerate surface microcracking on exposed rib roots. In field failures, cracking appears first at the base of self-tapping screw bosses where the local wall thickness is excessive, so the boss wall should be held between 60% and 70% of the main wall and the boss diameter should not exceed 1.5× the screw minor diameter. For cordless mower decks and strimmer bodies, the part is typically moulded with a fan-gated central runner and textured to VDI 3400 No. 33 to No. 36 to bury flow lines; a hot runner with externally heated nozzles is acceptable if the residence time in the manifold does not exceed 10 min at 230 °C. Finished articles in this group include garden lounger shells, planter walls, cordless strimmer bodies, lawn mower deck covers and outdoor storage box lids, all of which depend on resistance to UV-induced chalking and yellowing. When the part is assembled with stainless steel screws, the coefficient of linear thermal expansion for PP impact copolymer of approximately 1.0×10⁻⁴ K⁻¹ to 1.3×10⁻⁴ K⁻¹ must be accommodated by oversized holes or shoulder screws; otherwise narrow fixing holes will crack at the upper service temperature of 80 °C. The grade should not be painted without an adhesion promoter validated for PP, because painting over black PP without flame, corona or plasma treatment is not an acceptable process route for exposed furniture parts.

    When an Outdoor Telecommunication Enclosure Requires Impact Resistance Without Flame Retardancy

    The absence of a UL 94 V-2 or V-0 rating in Polycomp PDR CB 08 UV2 PP Copolymer restricts its use in outdoor telecommunication enclosures to low-voltage, non-current-carrying shells, cable splice closures, antenna housing covers and similar passive housings. For these installations, the mechanical acceptance test is often ASTM D256-23 Izod notched impact at −20 °C with a minimum of 40 J/m, plus a practical drop impact requirement of no cracking at −30 °C when struck by a 1 kg steel ball from 1 m. Weathering is evaluated under ISO 4892-2 or by combined UV exposure and thermal cycling from −40 °C to +85 °C; the black PP copolymer is significantly more stable than natural PP, but the enclosure hinge line remains the critical stress concentration. When an enclosure cover is connected by an integral living hinge, the hinge should be gated on one side only, the land thickness should be 0.35 mm to 0.50 mm, and the hinge root should be rounded to a radius of at least 0.2 mm; a thicker hinge exceeds the molecular orientation limit and will crack after repeated outdoor opening cycles. Moulders often increase melt temperature to improve hinge strength, but melt temperature above 240 °C can degrade the UV stabiliser at the hinge region and create a brittle oxidative skin. Fill pressure should be kept at 50 MPa to 80 MPa for enclosures with flow length to wall thickness ratios greater than 150:1, and the flow front should advance without hesitation because a hesitation mark on a black textured surface is visible as a pale lip. This material is not suitable for enclosures that must pass IEC 60695-2-11 glow wire testing at 850 °C or 960 °C, nor for terminal housings carrying live current without an internal flame-retardant barrier; the UV benefit must not be interpreted as an electrical safety rating. The compound should also be supported by a supplier declaration covering the absence of PFOS/PFOA and restricted phthalates where the enclosure is marketed into the European telecommunication sector under REACH 1907/2006/EC.

    Material Handling Pallets: Thick-Wall Flow, Shrinkage and Racking Load

    For injection-moulded export pallets and collapsible crates stored outdoors, the long service life depends less on UV stabilisation and more on balanced filling of thick sections, because a hot runner delivering melt into a 6 mm to 12 mm wall creates a solidification gradient that governs warpage. The cooling time in a thick PP copolymer section scales with the square of wall thickness; a wall increase from 4 mm to 8 mm can increase cooling time by a factor of approximately 4, so the economic moulding cycle is set by the thickest load-bearing pad rather than by the outer deck. Polycomp PDR CB 08 UV2 can be used in this segment if the injection machine screw diameter is matched to shot weight such that shot size is 25% to 65% of maximum capacity; smaller shots reduce plastication consistency and larger shots increase residence time. The black compound should be processed at a mould temperature of 30 °C to 60 °C, because a colder mould freezes the flow front before welding around core-out openings and can generate brittle weld lines at pallet window corners. Differential shrinkage between flow direction and transverse direction for PP impact copolymer is normally 0.1% to 0.3%; when the pallet top deck is centre-gated, the outer corners may lift by 3 mm to 6 mm per metre of length unless the tool includes reverse draft or the cooling layout extracts heat faster from the centre. Outdoor storage pallets are frequently washed with alkaline detergents at pH 9 to 11 and occasionally with hypochlorite-based sanitizers; the grade tolerates these solutions at ambient temperature but should not be exposed to hot sulfuric acid or concentrated oxidising acids, which will attack the PP backbone and cause surface erosion. Finished products in this group include export pallets, collapsible container side walls, cold-store crate bases and racking trays, where long-term UV exposure is managed through the black UV2 package and the main failure mode is mechanical creep under sustained racking load. The purchaser should require a documented tensile creep modulus in accordance with ISO 899-1 and should avoid specifying the same deflection limit for PP copolymer as for HDPE pallets, because PP exhibits a higher short-term modulus but a lower allowable continuous load limit at 60 °C unless the design includes reinforcing ribs.

    Outdoor HVAC condensing unit housings, fan shrouds and compressor access panels form another application cluster in which the UV2 package is used, but process discipline is driven by dimensional stability rather than weathering alone. The black PP impact copolymer is injection-moulded with wall sections between 2.5 mm and 4.0 mm, and the part is exposed to a combination of direct solar radiation, hot compressor discharge air and periodic vibration. For PP impact copolymer, the heat deflection temperature under 0.45 MPa ISO 75-2/B is normally below 100 °C, and the black surface can reach 80 °C on a roof-mounted unit in a 40 °C ambient environment; the design should therefore limit continuous loaded service near the compressor to 70 °C. The main processing constraint is the large circular fan shroud, where imbalance from uneven melt fill causes out-of-roundness and blade tip interference. Moulders should balance the runner system using naturally balanced spider gates or valve-gated hot drops; fan tip clearance of 0.8 mm to 1.5 mm is common in shrouds with a diameter of 600 mm or less, and the moulded shroud should be checked for free-state shrinkage after ejection rather than after the part has cooled on a heavy flat table. The black UV stabilization package can slightly increase viscosity relative to natural PP; therefore the melt temperature should be set at the upper end of the recommended range only when the supplier datasheet confirms that the stabiliser is stable at that temperature. Polycomp PDR CB 08 UV2 is not a substitute for a UL 94 V-0 material in an open compressor electrical bay, and the user must separate the plastic shroud from unprotected live wiring with an air gap or a sheet-metal barrier. End products include outdoor condensing unit top covers, fan orifice rings, side louvres and pump access doors.

    Marine and Poolside Components Under Repeated Wet-Dry Cycling

    When a black UV-stabilised PP copolymer is specified for poolside equipment housings, dock fender covers and swim ladder step shells, the loading conditions differ from furniture or enclosure applications because chlorine, salt spray and cyclic wetting act on the moulded surface at the same time as UV radiation. Polypropylene impact copolymers are generally low-moisture-uptake materials; the water absorption of unfilled PP after 24 h immersion under ISO 62 is commonly below 0.05%, so the dimensional impact of water is not the main risk. The principal chemical boundary is chlorinated pool water: hypochlorite-based disinfectants at active chlorine concentrations below 1% are tolerated at ambient temperature, but repeated wet-dry cycling can concentrate oxidant residues on the surface and accelerate microcracking at weld lines and injection gate scars. For poolside housings that contain a transparent cover or a soft elastomeric seal, the PP part should be overmoulded with a thermoplastic elastomer only after the PP surface has been activated by flame, corona or plasma treatment; without activation, the bond strength can fall below 1 N/mm and the soft seal will peel after fewer than 1,000 opening cycles. Metal inserts in dock fender brackets should be preheated to 80 °C to 100 °C before insert moulding because cold inserts freeze the surrounding melt and create a highly oriented skin that is sensitive to impact. The mould temperature should be kept at 30 °C to 50 °C; temperatures above 60 °C slow the cycle without giving a measurable improvement in impact strength for black PP copolymer. In this segment, the typical acceptance standard is ISO 4892-2 weathering accompanied by ISO 9227 neutral salt spray at 35 °C for 500 h to 1,000 h; after salt spray, the part should not show blisters, surface chalking or a drop in ISO 179-1/1eA Charpy notched impact strength greater than 25%. Finished components include pool pump covers, filter tank shrouds, dock fender profiles, kayak hatch rims and swim ladder treads; for direct saltwater immersion at depths greater than 1 m, published data for this specific configuration is limited, and the buyer should run a part-specific hydrostatic test because creep and seal retention are governed by gasket design rather than by the base resin.

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    Certification & Compliance
    More Introduction

    Polycomp PDR CB 08 UV2 PP Copolymer is a carbon-black-coloured polypropylene impact copolymer formulated with a dual-level ultraviolet stabilization system. The grade is intended for injection moulding and profile extrusion of components that require an intermediate melt-flow, low-temperature ductility, and outdoor weatherability. In the product designation, 08 corresponds to the nominal melt mass-flow rate of 8 g/10 min determined at 230 °C with a 2.16 kg load in accordance with ISO 1133-1:2022. The CB segment identifies the presence of a fine-particle carbon black pigment, and UV2 denotes a two-component ultraviolet stabilization package. Manufacturer-published nominal values are presented in Table 1; these values are lot-average targets and must be confirmed against the batch certificate and laboratory testing before release of production tooling.

    What Distinguishes the CB 08 UV2 Stabilization System from Generic Black PP Copolymer?

    Generic black polypropylene compounds frequently rely on a low-cost carbon black masterbatch that provides opacity but does not control particle dispersion below a critical agglomerate size. In Polycomp PDR CB 08 UV2 PP Copolymer, the carbon black is specified to function as an ultraviolet screen in the 280–400 nm region while the UV2 package provides radical scavenging and photon absorption at the part surface. The hindered amine light stabilizer component of UV2 operates through a cyclic nitroxyl regeneration pathway, and the ultraviolet absorber converts incident photons into thermal energy. Carbon black alone can screen ultraviolet radiation but is less effective at surface microvoids, weld lines, and pigment-poor boundary layers. The combination therefore shifts the outdoor failure mode from rapid chalking and tensile embrittlement toward slower gloss loss and microcrack formation. Accelerated weathering comparisons are performed according to ISO 4892-2:2013 method A, cycle 1, with a xenon arc source, daylight filters, irradiance of 0.51 W/m² at 340 nm, and black-standard temperature of 65 °C. Users who require long-term Florida-type exposure data should request product-specific results for the intended part thickness and surface texture, because published data for this specific configuration is limited. Carbon-black dispersion is assessed by microscopy using ISO 18553, and the manufacturer specifies a maximum agglomerate rating to prevent local embrittlement and surface defects. The functional difference from a generic black impact copolymer is therefore not pigment loading alone but the controlled dispersion and the co-stabilization of surface photo-oxidation.

    The mechanical and thermal profile in Table 1 is based on injection moulded specimens conditioned at 23 °C and 50% relative humidity for 40 h according to ISO 291:2008. Short-term tensile and flexural values are not design allowables and do not account for long-term oxidative embrittlement, chemical exposure, or weld-line reduction.

    PropertyTest standardNominal value
    Melt mass-flow rateISO 1133-1:20228 g/10 min at 230 °C and 2.16 kg
    Melt volume-flow rateISO 1133-1:20229.0 cm³/10 min at 230 °C and 2.16 kg
    DensityISO 1183-1:20190.910 g/cm³
    Tensile yield stressISO 527-2/1A/5024 MPa
    Tensile elongation at yieldISO 527-2/1A/505.0%
    Flexural modulusISO 178:20191,250 MPa
    Notched Charpy impact at 23 °CISO 179-1/1eA8.5 kJ/m²
    Notched Charpy impact at -20 °CISO 179-1/1eA3.5 kJ/m²
    Vicat softening temperatureISO 306:2022 method B5074 °C
    Heat deflection temperatureISO 75-2:2013 method B95 °C at 0.45 MPa
    Carbon black dispersion ratingISO 18553≤ 2.0

    The melt-flow rate of 8 g/10 min places the material in the medium-flow impact-copolymer class. It is not a high-flow grade for thin-wall micro-moulding, but it can fill nominal wall sections down to approximately 1.2 mm when tool geometry avoids long flow lengths. In comparison to an unfilled PP homopolymer, the impact copolymer retains ductility at sub-zero service temperatures; the notched Charpy value of 3.5 kJ/m² at -20 °C is a differentiating feature. Relative to a 20 wt% talc-filled PP impact copolymer exhibiting flexural modulus near 2,300 MPa, the CB 08 UV2 grade has lower stiffness and higher ductility, making it suitable for lightly loaded brackets, covers, and housings rather than structural support members. Its density of 0.910 g/cm³ is lower than typical talc-filled grades and reduces part mass when the lower modulus is acceptable. Another difference from unreinforced PP copolymer grades without the UV2 package is the retention of surface quality during outdoor exposure; an equivalent unfilled, non-UV-stabilized black copolymer would be expected to chalk and embrittle earlier under the same ISO 4892-2:2013 exposure.

    Melt Processing, Screw Conditions, and the Dispersion–Impact Retention Balance

    Although polypropylene does not undergo hydrolytic degradation, surface moisture can create splay and gate blush in poorly vented moulds. When opened packaging has been exposed to relative humidity above 60% for more than 24 h, pre-drying at 80 °C for 2 h in a desiccant dryer is recommended. Dryer set points above 90 °C should be avoided because additive migration to the pellet surface can produce screw slippage and colour variation. At the press, melt temperature measured at the nozzle should be held between 210 °C and 250 °C. A reciprocating screw with 20:1 to 24:1 L/D and compression ratio of 2.5:1 to 3.0:1 is standard for this grade. Barrel set points of 180 °C feed, 210 °C compression, 230 °C metering, and 230 °C nozzle are adequate for a 30 mm screw. Hydraulic back pressure from 5 bar to 10 bar and screw speed below 150 min⁻¹ improve melt homogeneity without excessive shear heating. If a hot runner is used, manifold and nozzle tip temperatures should not vary from the nozzle by more than 10 °C, and shut-off needles should be inspected for wear because carbon black is abrasive relative to unfilled melt.

    The processing window is constrained by two opposing requirements. High shear improves carbon black dispersion but also raises melt temperature by viscous dissipation. Compounding trials on similar carbon-black impact copolymers indicate that reaching a dispersion rating of ≤ 2.0 per ISO 18553 on a 25 mm twin-screw extruder with L/D 40:1 requires specific energy input in the range of 0.18 kWh/kg to 0.25 kWh/kg. Above 0.30 kWh/kg, chain scission in the ethylene-propylene rubber phase can diminish notched Charpy impact by more than 15% relative to optimum. Injection moulders should therefore avoid undersized gates and fast screw recovery speeds that impose additional shear heating. A production-scale evaluation on a 1,600 kN clamp injection moulding machine with a two-cavity tool found that increasing melt temperature from 220 °C to 240 °C improved visual dispersion but reduced notched impact by 8%; the corrective action was an increase in gate diameter rather than thermal profiling alone. Residence time above 240 °C should not exceed 5 min. Extended buffering in hot-runner systems can produce silver streaking and a measurable loss of low-temperature ductility, a failure mode observed when hot-runner shut-off valves leak during screw delay and retain degraded material in the manifold.

    Mould surface temperature below 20 °C reduces weld-line strength and produces a matte finish, while temperatures above 60 °C extend cycle time without a commensurate improvement in crystallinity. A nominal mould temperature of 40 °C is prescribed. Vent depths should be 0.03 mm maximum to avoid flash, with vent land lengths between 1.0 mm and 2.0 mm. Gate shear rates below 50,000 s⁻¹ and generous cold-slug wells reduce jetting and improve carbon-black dispersion in the final part. Dimensional control requires attention to bench shrinkage after 24 h and 48 h; for this unfilled impact copolymer, injection-direction shrinkage is typically 1.2% to 1.4% and transverse shrinkage is 1.4% to 1.6%, but tool design should use the specific lot moulding-shrinkage data rather than generic values.

    Typical targeted applications are injection moulded outdoor electrical enclosures, irrigation valve bodies, black exterior trim brackets, battery trays, and wheel-arch liners. The material is selected when the part must survive low-temperature impact in service and cannot be painted or laminated. In such parts, unpigmented PP homopolymer often shows brittle failure in notched areas at -20 °C to -30 °C, while the CB 08 UV2 grade retains ductility because of the ethylene-containing impact phase. Extrusion of black UV-resistant sheet or cap layers is possible; however, the 8 g/10 min flow is at the low end for thick-wall sheet and may require an extrusion-grade variant if melt strength and drawdown control are dominant. Published data for this specific grade in extrusion is limited, and line trials are recommended.

    When the Grade Is Used for Outdoor Enclosures and Underhood Brackets

    The combination of carbon black and the UV2 package is not a substitute for adequate part design. In outdoor electrical enclosures, the carbon black lowers comparative tracking index relative to natural unfilled PP because it is a semiconductive pigment. Product-specific CTI values should be taken from the lot certificate and used to derive creepage distances under IEC 60112:2003. Glow-wire ignition temperature may be evaluated according to IEC 60695-2-11:2014; typical unfilled PP compounds are classified as HB under IEC 60695-11-10:2013, but ignition characteristics are thickness-dependent. Underhood brackets require verification of service temperature, chemical resistance to engine oil and coolant, and fatigue loading. The unfilled impact copolymer is generally resistant to aqueous acid and alkaline solutions at room temperature but may swell or crack in contact with chlorinated solvents and aromatic hydrocarbons. Continuous service above 80 °C accelerates oxidative degradation and should be subjected to heat-aging tests such as ISO 188:2011 or ASTM D3045-18. The stabilizer package delays outdoor photo-oxidation but is not designed to protect against copper-ion catalyzed degradation; contact with bare copper alloys can reduce oxidative induction time and should be prevented by design or by nickel-plating of copper components.

    In appliances and outdoor furniture, the grade is sometimes compared with ASA or weatherable ABS. Polypropylene has lower heat resistance than these amorphous resins but offers better chemical resistance to alkaline cleaning agents and lower density. The specific choice should be based on the required heat deflection temperature, gloss retention, and impact performance after weathering, not on a single property.

    Table 2 summarizes the compliance verifications that are typically relevant when qualifying the grade. The entries are not exhaustive and do not replace end-article testing.

    Requirement areaStandard/regulationStatus and boundary
    REACH SVHC candidate listEC 1907/2006, Article 330.1% w/w threshold; confirm lot certificate
    RoHS restricted substancesDirective 2011/65/EU; IEC 62321-8:2017No intentionally added Pb, Hg, Cd, Cr(VI), PBB, PBDE
    Food contactFDA 21 CFR 177.1520; FDA 21 CFR 178.3297Not automatically granted; migration testing required on finished article
    FlammabilityIEC 60695-11-10:2013Expected HB; thickness-dependent
    WeatheringISO 4892-2:2013Product-specific data required; request lot-specific retention curves
    Carbon black dispersionISO 18553≤ 2.0 rating specified
    Comparative tracking indexIEC 60112:2003Product-specific; carbon black reduces CTI versus natural PP
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