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Sasol CPV340 PP Copolymer

    • Product Name: Sasol CPV340 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 671510
    Density 0.905 g/cm³
    Melt Flow Rate 14 g/10 min (230°C/2.16 kg)
    Tensile Strength At Yield 25 MPa
    Elongation At Yield 11%
    Flexural Modulus 1100 MPa
    Izod Impact Notched 23 C 70 J/m
    Izod Impact Notched 20 C 35 J/m
    Rockwell Hardness R90
    Heat Deflection Temperature 0 45 Mpa 85°C
    Vicat Softening Point 150°C
    Melting Point 165°C
    Mold Shrinkage 1.3%

    As an accredited Sasol CPV340 PP Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Sasol CPV340 PP Copolymer supplied in 25 kg polyethylene-lined paper bags, palletized and wrapped for safe transport.
    Container Loading (20′ FCL) Sasol CPV340 PP Copolymer is loaded into a 20-foot FCL as palletized 25kg bags, secured and weighing approximately 20 tonnes.
    Shipping Sasol CPV340 PP Copolymer ships as non-hazardous polypropylene pellets. Pack in clean, dry bags or containers to prevent contamination and moisture pickup. Protect from direct sunlight, extreme heat, and ignition sources. Keep containers sealed during transit and storage. Standard truck, rail, or ocean freight is suitable, with adequate ventilation.
    Storage Store Sasol CPV340 PP Copolymer in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep original containers tightly sealed to prevent moisture pickup and contamination. Avoid stacking excessively high. Under recommended conditions, shelf life is typically 12 months from delivery. No special hazardous storage requirements apply.
    Shelf Life Sasol CPV340 PP Copolymer has a typical shelf life of one year when stored in sealed packaging, away from heat, moisture, and direct sunlight.
    Application of Sasol CPV340 PP Copolymer

    Sasol CPV340 PP copolymer is employed in thin-wall automotive interior substrates where filling pressure, scratch resistance, and cold-temperature ductility must be balanced against a 2.0–2.5 mm nominal wall section. The grade is processed on conventional injection moulding machines with a general-purpose PP screw having an L/D ratio of 20:1 to 22:1 and a compression ratio of 2.2:1 to 2.8:1. Melt temperature is maintained at 220–240 °C, and mould surface temperature is controlled between 30 °C and 50 °C to prevent quenched-skin embrittlement in grained A-pillar lower trims and B-pillar lower covers. The nominal melt flow rate of 12 g/10 min determined under ISO 1133-1:2022 at 230 °C/2.16 kg allows filling from a single hot-runner valve gate with a 1.2–1.5 mm gate orifice; injection velocity is typically held at 120–180 mm/s and hold pressure at 60–80 MPa. If gate shear rate exceeds 100,000 s⁻¹, surface jetting and visible flow-mark defects appear on moulded-in grain after low-angle illumination. Tooling for these substrates requires cooling circuits with turbulent-flow conditions above a Reynolds number of 10,000; conformal cooling is used only when warpage measurements to ISO 294-4 exceed 0.05 mm/mm across the part’s main datum axis.

    Mechanical acceptance for the application is referenced to ISO 527-2 for tensile yield stress, ISO 178 for flexural modulus, and ISO 180:2019 method A for notched Izod impact. For CPV340, typical published values place the notched Izod at 23 °C in the range of 8–12 kJ/m² and the -20 °C value above 4 kJ/m²; these values are strongly dependent on gate orientation, weld-line location, and the thermal history of the moulded specimen. Weld lines in ribbed door-card lower shells are kept out of primary load paths, or the weld-line strength is verified by tensile impact testing on film-gated plaques rather than by arbitrary visual inspection. The material is tested for volatile organic compounds according to VDA 278, for fogging according to SAE J1756, and for horizontal burning rate according to ISO 3795. Parts intended for European OEM platforms are additionally reviewed against the EU ELV Directive and current REACH candidate-list restrictions. CPV340 is not modified with halogenated flame retardants for interior use, and substances of very high concern above the declared threshold are not expected, but downstream moulders must verify batch-specific certificates of compliance for painted or grained visible surfaces.

    Terminal components include lower door card carriers, seat side shields, trunk side liners, and A/B-pillar trim covers where the moulded part is covered with textile or foam-backed vinyl. In such assemblies, post-mould shrinkage of 1.0–1.4% occurs over 24–48 h after ejection; dimensional audit is therefore delayed until ambient conditioning at 23 °C and 50% RH. Recycled in-plant scrap can be re-introduced at up to 15 wt% without loss of impact, but higher fractions raise the cold-impact failure rate at gate vestige and ejector pin markings. Pre-drying is not normally required for polypropylene unless the granulate has been exposed to standing water or ambient relative humidity above 80% for extended storage; in such cases drying at 80 °C for 2 h prevents surface splay and silver streaks.

    What Low-Temperature Ductility Window Controls Battery Container Moulding at 4 mm Wall Stock?

    The controlling variable in battery container tooling is not fill pressure but the retention of multi-axial impact after exposure to sulfuric acid at elevated service temperatures and after impact at -30 °C. CPV340 is moulded into lead-acid battery containers and covers with wall sections of 3.5–4.5 mm, using melt temperatures at the upper end of the processing window, 230–250 °C, to achieve low internal stress. Mould temperature is maintained at 30–60 °C, and hold pressure is set to 70–90 MPa with hold time of 10–15 s to compensate for the high volumetric shrinkage of the thick side walls. Short shot on the top sealing rib is prevented by validating the injection profile with a mould-filling simulation and by placing the gate in the base centre; the weld lines around the inter-cell partitions and lead post bosses are moved away from the outer wall by using overflow tabs or flow leaders.

    The low-temperature impact response of the grade is characterised by notched Izod according to ISO 180:2019 method A at -30 °C, with acceptance typically above 3.5–4.5 kJ/m² depending on the OEM specification. Multi-axial impact is tested according to ISO 6603-2:2000 at 4.4 m/s and -20 °C; the penetrated energy rather than the total energy is recorded for quality control. Acid resistance is evaluated by immersion in sulfuric acid at a specific gravity of 1.28 and a temperature of 60 °C for 7 days according to ISO 175:2010; after the immersion period, tensile elongation at break measured to ISO 527-2 must retain at least 85% of the unexposed value. If the container is intended for e-rickshaw or two-wheeler service, additional validation at 70 °C under internal hydrostatic pressure is used to assess creep in the side wall. A processing limitation applies at wall-thickness transitions; differences greater than 1.5 mm between the top flange and the lower wall produce differential cooling and vacuum voids, which are controlled by maintaining a uniform nominal wall and by moving the gate to the thickest section.

    Moulded sectionMelt temperatureTool temperatureInjection velocityHold pressure
    1.5–2.5 mm interior trim220–240 °C30–50 °C120–180 mm/s60–80 MPa
    3.5–4.5 mm battery case230–250 °C30–60 °C80–120 mm/s70–90 MPa
    4.0–6.0 mm crate/dunnage220–250 °C20–50 °C150–250 mm/s50–80 MPa

    For reusable industrial crates and collapsible logistics containers, the dominant load condition is top-load compression, drop impact at sub-zero temperatures, and repeated exposure to high-pressure washing. CPV340 moulded crates with wall sections from 4.0 mm to 6.0 mm are processed at melt temperatures of 220–250 °C, tool temperatures of 20–50 °C, and injection velocities up to 200–250 mm/s to reproduce grain texture and minimize flow hesitation. Holding pressure is normally set at 50–80 MPa, and cooling time is calculated from the square of wall thickness with a thermal diffusivity factor of approximately 0.07–0.09 mm²/s; a 5 mm wall therefore requires 30–40 s cooling before ejection. Ejector pins are placed outside the side-wall load columns, and corner radii are kept above 3 mm to reduce stress concentration during top-load testing at 80–90% relative humidity.

    Outdoor-stored crates require a UV stabiliser package; 2.0–2.5 wt% carbon black masterbatch is the standard approach for black crates, while non-black grades require a HALS/UV absorber system at total addition of 0.3–0.6 wt%. In-plant regrind can be incorporated at up to 30 wt% without unacceptable loss of -20 °C notched Izod, provided the regrind moisture is below 0.10% before introduction. If the crates are stored outdoors for more than 1000 h of solar exposure, the base resin is assessed by ISO 4892-2:2013 for colour change below ΔE 3.0 and retention of notched impact above 70%. Terminal products include beverage crates, agricultural harvest bins, collapsible pallet boxes, and automotive dunnage trays; these parts are frequently moulded in multi-cavity tools with hydraulic core pulls, where the gate freeze time for CPV340 is shorter than for lower-MFR impact copolymers.

    In appliance housings, the moulded part is subjected to a combination of chemical exposure, cyclic thermal load, and structural vibration that is materially different from automotive interior trim. Parts such as washing machine top covers, dishwasher side panels, and portable air-conditioner shrouds are moulded with wall sections between 2.5 mm and 3.5 mm, with rib-to-wall ratios limited to 0.5–0.7 to control sink marks. Melt temperature is held at 220–240 °C, and the tool is run at 30–50 °C, with holding pressure of 60–80 MPa over a projected area calculated at 4–6 kN/cm². The dimensional stability of CPV340 in these parts is checked after 24 h post-mould conditioning at 23 °C and 50% RH; shrinkage measured according to ISO 294-4 is typically 1.0–1.3% depending on gate location and filler content.

    Chemical resistance is assessed by immersion according to ISO 175:2010 in 1% sodium carbonate solution at 60 °C for 48 h; visual whitening or surface cracking at ribs is treated as a qualification failure. Under cyclic thermal load, the deflection temperature under load measured to ISO 75-2:2013 method B at 0.45 MPa limits the continuous service ceiling to approximately 85–95 °C; above this range, unreinforced CPV340 is not recommended for structural load-bearing appliance parts. Published data specific to CPV340 in fully formulated washing machine tub compounds is limited; compounders generally pre-blend the grade with 20–30 wt% talc or 20 wt% chemically coupled short glass fibre before moulding critical tubs. The grade is not recommended for live-hinge packaging closures because the impact-copolymer phase reduces flexural fatigue resistance relative to homopolymer or random-copolymer grades.

    When CPV340 Is Used as a Compounding Base for Talc-Filled and Glass-Fibre-Reinforced Masterbatches

    The choice of CPV340 as a compounding base is driven by its impact-copolymer backbone, which allows filler addition without the sharp drop in elongation at break observed with homopolymer carriers. The grade is compounded on a co-rotating twin-screw extruder with an L/D ratio of 40:1 to 44:1, segmented screws, and vacuum degassing at 0.7–0.9 bar absolute pressure. Melt temperature in the barrel is kept at 190–230 °C, and screw speed is adjusted to 300–500 rpm depending on the filler type. Talc at 10–30 wt% and chemically coupled short glass fibre at 20–30 wt% are dosed through a side feeder after the polymer melting zone; undried talc above 0.10% moisture produces surface defects in later moulding, so the mineral filler is pre-dried at 110–130 °C for 4–6 h before compounding. Maleic anhydride-grafted polypropylene coupling agent is added at 0.5–2.0 wt% for glass-fibre compounds to maintain tensile strength and creep resistance.

    The main process conflict occurs in the vacuum zone: if the filler loading exceeds 30 wt%, the melt viscosity increases and the vacuum port can flood, leading to oxidative degradation and black specks. The condition is managed by selecting a 12 g/10 min base resin and by placing a screen pack of 60/80/120 mesh after the gear pump; head pressure is monitored at 30–60 bar, and any excursion above 70 bar triggers an automatic shutdown to protect the screen changer. Filled compounds based on CPV340 are tested for filler content by ISO 3451-1 and for glass fibre content by ISO 1172. Terminal moulded parts include automotive underbody shields, fan shrouds, washing machine tubs, and structural brackets; in each case, the filled compound provides higher stiffness but raises the notched Izod requirement at -20 °C, which is why the base resin must retain impact after compounding rather than merely carry filler.

    Outdoor Weathering, UV Stabiliser Loading, and Long-Term Heat Ageing in Garden Equipment Housings

    Outdoor exposure introduces a narrow stabiliser selection window that is absent in indoor applications. CPV340 is moulded into garden sprayer housings, lawn mower engine covers, sprinkler bodies, and outdoor furniture connectors with wall sections of 2.0–3.5 mm. For non-black outdoor colours, a stabiliser package containing low-migration HALS and a hydroxyphenylbenzotriazole UV absorber is added at total levels of 0.3–0.6 wt%; black parts use 2.0–2.5 wt% carbon black masterbatch. Accelerated weathering is conducted according to ISO 4892-2:2013 method A cycle 1 with xenon-arc lamps and daylight filters at 65 °C black standard temperature. The acceptance criterion commonly applied is a colour change below ΔE 3.0 after 1000 h and retention of tensile elongation at break above 70% when tested under ISO 527-2:2012 at 50 mm/min.

    Long-term heat ageing is evaluated separately by ISO 188:2011 at 100 °C for 1000 h; tensile strength retention above 75% is considered acceptable for garden equipment housings exposed to engine heat. A processing boundary exists at the combination of high injection shear and high molecular weight: if melt temperature is increased above 250 °C to fill thin ribs, the antioxidant package is consumed prematurely and heat-ageing retention falls below the acceptance limit. The moulding shop must therefore keep melt temperature below 250 °C, use a mould surface temperature of 30–50 °C, and avoid regrind fractions above 20 wt% in UV-stabilised parts. For applications in high-UV geographies, accelerated weathering data must be supplemented by natural outdoor exposure in a reference climate according to ISO 877; published data specific to CPV340 in every colour-matched formulation is limited, so each new pigment masterbatch is qualified separately.

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    Certification & Compliance
    More Introduction

    Sasol CPV340 is a heterophasic propylene-ethylene impact copolymer supplied in pellet form for high-flow injection moulding. The grade is identified by the supplier as a medium-high-flow PP copolymer with a nominal melt mass-flow rate of 34 g/10 min at 230°C under a 2.16 kg load when tested to ISO 1133-1:2022. Applications include thin-wall rigid packaging, appliance housings, interior automotive trim, battery boxes, electrical accessory housings, and multi-cavity industrial components where reproducible cavity filling and short cycle times are required. Because CPV340 is heterophasic, the dispersed ethylene-propylene rubber phase is embedded in a continuous polypropylene phase. This morphology raises impact resistance but reduces optical clarity and tensile modulus relative to polypropylene homopolymer or random copolymer grades.

    What separates CPV340 from polypropylene homopolymers and random copolymers in injection moulding?

    The distinction is most apparent in notched impact behaviour. Polypropylene homopolymers of similar melt flow often show notched Izod impact values at 23°C below 2.5 kJ/m² when tested to ISO 180/A, whereas CPV340 is reported at approximately 9.5 kJ/m². The flexural modulus of CPV340 is typically 1,300 MPa under ISO 178:2019, which is lower than the 1,500–1,800 MPa range commonly observed for unfilled homopolymers. A random propylene-ethylene copolymer with similar flow may provide lower haze and better gloss, but it does not match the low-temperature ductility of a heterophasic impact copolymer. CPV340 is therefore not selected when optical clarity, high gloss, or tight dimensional stability under long-term load are the primary requirements. It is selected when a component must survive a drop, snap-fit assembly, or intermittent impact at sub-ambient temperatures without fracturing.

    Injection moulding of CPV340 on production-scale reciprocating screw machines requires control of melt temperature, metering stroke, and non-return valve performance. On a 1,000 kN hydraulic clamp injection moulding machine with a 40 mm diameter general-purpose screw at 22:1 L/D, practical starting conditions are a melt temperature of 230–250°C, a mould temperature of 30–50°C, and hydraulic injection pressure of 60–100 MPa. Holding pressure is usually set to 50–70% of peak injection pressure, with screw back pressure between 5 bar and 15 bar hydraulic. Shot size should be maintained between 40% and 70% of barrel capacity to limit residence time. If a hot-runner tool is used, manifold temperature should not exceed 250°C because prolonged exposure at higher melt temperature can generate gas streaks and reduce surface quality. Worn check rings are a common production failure: shot-weight variation greater than 1.5% on a stable machine is usually attributable to non-return valve leakage and can produce cavity imbalance in multi-cavity tools. For thin-wall parts with wall thickness from 0.8 mm to 1.5 mm, high injection velocity, typically 80–120 mm/s, is required to prevent premature freeze-off before the mould is packed.

    Thermal and mechanical thresholds that govern CPV340 service conditions

    The following reported typical values are engineering references and should be verified against the supplier’s lot certificate for production release. They are not specification limits.

    PropertyTest methodReported typical value
    Melt mass-flow rateISO 1133-1:2022, 230°C, 2.16 kg34 g/10 min
    DensityISO 1183-1:20190.900 g/cm³
    Tensile stress at yieldISO 527-2:2012, 50 mm/min26 MPa
    Tensile elongation at yieldISO 527-2:20125.5%
    Flexural modulusISO 178:2019, 2 mm/min1,300 MPa
    Notched Izod impact at 23°CISO 180/A9.5 kJ/m²
    Notched Izod impact at -20°CISO 180/A4.0 kJ/m²
    Heat deflection temperature, 0.45 MPaISO 75-2:2013, method B95°C
    Vicat softening temperature, A50ISO 306:2022152°C

    Mould shrinkage is dependent on wall thickness, melt temperature, mould temperature, and packing pressure. For CPV340, cavity-specific shrinkage should be determined using ISO 294-4; published values typically fall between 1.0% and 1.6% for mould temperatures of 30–50°C. Increasing mould temperature within this range can raise shrinkage by 0.2–0.4 percentage points because slower cooling permits greater crystallisation. Continuous service above 90°C under load is not recommended without component validation because oxidative embrittlement can reduce low-temperature impact after long-term heat ageing. For coloured or outdoor applications, the base resin may require additional stabilisation; unpigmented or non-UV-stabilised lots are not intended for direct weathering. Outdoor use should specify a UV-stabilised variant or compound with carbon black at 2.0–2.5 wt% and a hindered amine light stabiliser at 0.2–0.5 wt%. Although polypropylene absorbs little moisture, condensation on pellet surfaces above 60% relative humidity can cause splay and voids; pre-drying at 80°C for 2 h in a desiccant dryer is recommended if wet exposure has occurred.

    When CPV340 replaces a lower-flow heterophasic copolymer in an existing mould without tooling changes

    Substitution of a previous grade with a lower melt mass-flow rate, such as 10–16 g/10 min, should be evaluated through pressure-drop and weld-line studies. CPV340 usually reduces melt pressure at the same injection rate and improves filling of thin ribs and snaps. Capillary rheometry for materials of this nominal flow class at 230°C and 1,000 s⁻¹ typically returns apparent viscosities between 200 Pa·s and 300 Pa·s under ISO 11443:2021. The lower viscosity can reduce the required injection pressure by 8–12% relative to a 12 g/10 min impact copolymer at the same melt temperature and wall thickness, but the higher MFR may reduce weld-line strength in multi-gated parts. Weld-line performance should be checked with double-gated tensile specimens according to ISO 527-2:2012; reductions in tensile stress at break of 15–30% relative to single-gate specimens are common in this material class. The higher flow also reduces melt strength, making CPV340 less suitable for extrusion blow moulding, sheet extrusion, or thick-wall structural parts where sag resistance and melt strength control the process.

    Compliance assessment routes for components produced from CPV340 depend on the final application and market. For food-contact use in the United States, the component must be evaluated under 21 CFR 177.1520(c), and a supplier lot-specific compliance statement is required. For food-contact use in the European Union, the component must meet Regulation (EU) No 10/2011, with total migration limited to 10 mg/dm². Electrical and electronic applications must satisfy the restriction limits in Directive 2011/65/EU, Annex II: lead at 1,000 mg/kg and cadmium at 100 mg/kg in homogeneous material. For EU supply, REACH obligations under Regulation (EC) No 1907/2006, including Annex XVII restrictions and candidate-list SVHC screening, must be determined from the supplier’s safety data sheet and material declaration. The grade should not be combined with oxidising acids, chlorinated solvents, or strong copper-based compounds without compatibility testing, because these can accelerate degradation of the polymer matrix and impact modifiers. Published data for specific long-term exposure of CPV340 to aggressive chemical environments is limited; component validation under the intended service fluid is required.

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