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Kumho Petrochemical KUMHO® ASA XC811-HW

    • Product Name: Kumho Petrochemical KUMHO® ASA XC811-HW
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@sinochem-nanjing.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 406004
    Density 1.05–1.08 g/cm³
    Melt Flow Rate 4–8 g/10 min at 220°C/10 kg
    Tensile Strength At Yield 45–50 MPa
    Tensile Elongation At Break 20–30%
    Flexural Modulus 2000–2300 MPa
    Notched Izod Impact Strength 10–15 kg·cm/cm
    Heat Deflection Temperature 80–90°C at 1.82 MPa
    Vicat Softening Temperature 100–108°C
    Rockwell Hardness R100–R110
    Mold Shrinkage 0.4–0.7%
    Flammability Rating UL94 HB
    Weather Resistance High
    Color Stability Good
    Chemical Resistance Good
    Processing Temperature 220–260°C
    Drying Conditions 80°C for 2–4 h

    As an accredited Kumho Petrochemical KUMHO® ASA XC811-HW factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing KUMHO® ASA XC811-HW is supplied in 25 kg moisture-resistant paper bags, palletized, with 1,000 kg jumbo bags available for bulk orders.
    Container Loading (20′ FCL) 20′ FCL container loaded with Kumho Petrochemical KUMHO® ASA XC811-HW in original packaging, palletized, secured, and sealed for ocean shipment.
    Shipping KUMHO® ASA XC811-HW is shipped as solid ASA thermoplastic pellets, typically in 25 kg moisture-barrier bags or bulk sacks on pallets. It is not classified as dangerous goods under normal transport regulations. Keep containers closed, dry, ventilated, and protected from moisture, direct sunlight, and contamination during storage and handling.
    Storage Store KUMHO® ASA XC811-HW in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and moisture. Keep original packaging sealed and palletized off the floor. Avoid strong oxidizing agents and dust generation. Do not store outdoors or near flammable materials; rotate stock, inspect containers for damage, and follow the SDS and local regulations.
    Shelf Life KUMHO® ASA XC811-HW typically has a 24-month shelf life from manufacture when stored unopened in a cool, dry place away from sunlight.
    Application of Kumho Petrochemical KUMHO® ASA XC811-HW

    Injection moulding of acrylonitrile–styrene–acrylate copolymer for exterior automotive mirror housings requires rigorous thermal history control to preserve surface gloss stability through the component lifetime. The material is pre-dried in a desiccant dryer with a dew point of −35 °C or lower at 80–85 °C for 3–4 h, achieving residual moisture below 0.03 wt%. Barrel zone settings typically follow a rising profile from 220 °C at the feed throat to 245–255 °C at the metering zone and nozzle, with melt temperature measured at the nozzle tip not exceeding 260 °C. Residence time at melt temperature is limited to ≤8 min to prevent acrylic ester rubber phase degradation, which manifests as yellowing and a measurable reduction in Izod impact strength under ASTM D256 (Method A). Mould temperature is maintained at 50–70 °C using a thermolator with a flow rate of 12–18 L/min per circuit on moulds with 0.02–0.04 mm vent depths. Clamp force requirements for a single-cavity mirror housing of projected area 220–280 cm² fall within 250–400 tonne hydraulic or toggle machines. Injection pressure is set at 700–950 bar, with holding pressure at 55–70% of peak injection pressure for 6–10 s, followed by cooling time derived from the 2.5 mm nominal wall thickness at 18–22 s. Weld line formation at the attachment boss radii is a documented failure mode; gate positioning at the part periphery and sequential valve gate actuation on hot runner systems with 2–3 drop configurations mitigate knit-line visibility in Class A surfaces. The moulded housing must demonstrate no tack, splay, or silver streaks at 0.04 mm machined vent depth under production cycle times of 45–60 s.

    Accelerated weathering validation for exterior mirror housings follows SAE J2527 using xenon arc apparatus with daylight filters at 0.55 W/m² irradiance at 340 nm, black panel temperature 70 ± 2 °C, and chamber air temperature 47 ± 3 °C. Typical acceptance criteria specify ΔE* < 3.0 after 2000 kJ/m² radiant exposure and retained gloss at 60° incidence equal to or greater than 75% of initial value determined per ASTM D523. Dimensional stability under thermal excursion is characterised by heat deflection temperature per ISO 75-2:2013 (Method A, 1.8 MPa) and coefficient of linear thermal expansion per ISO 11359-2:2021 over the range −30 °C to +80 °C. Long-term colour fastness of pigmented ASA in automotive exterior service is influenced by titanium dioxide grade selection; rutile TiO₂ at 2.5–3.5 phr with an inorganic surface treatment suppresses photocatalytic degradation of the acrylic ester phase. Published data for this specific grade under multi-year Florida outdoor exposure is limited; validation programmes typically rely on correlation between SAE J2527 xenon exposure and ≥36 month field results on equivalent ASA material classes.

    What limits melt viscosity matching in coextruded ASA capstock over PVC window profiles?

    Coextrusion of ASA capstock over rigid PVC substrate demands melt viscosity matching within the die land region to prevent encapsulation defects and interfacial flow instability. The capstock layer at 0.15–0.25 mm thickness is processed through a single-screw extruder with screw diameter 30–45 mm and L/D ratio of 24:1 to 28:1, using a barrier screw with Maddock mixing section and compression ratio of 2.0:1 to 2.5:1. Barrel temperatures are profiled from 185 °C at the feed zone to 225–235 °C at the metering zone, with adapter and die manifold temperatures held at 220–230 °C. Melt temperature at the die entry is measured with an immersion thermocouple and maintained at 232 ± 5 °C. The rigid PVC substrate is processed at 190–205 °C melt temperature through a counter-rotating twin-screw extruder with L/D 22:1. The viscosity ratio between the two melts at the shear rates prevailing in the die land (100–500 s⁻¹) must remain within 1:0.8 to 1:1.2; excursions outside this band generate layer thickness oscillation detectable as surface waviness with amplitude exceeding 0.03 mm on the extruded profile. Melt pressure at the die entry is typically 120–180 bar for profile throughput of 80–150 kg/h depending on cross-sectional complexity.

    The feedblock and die design for ASA/PVC coextrusion incorporates a dual-manifold configuration with independently adjustable restrictor bars to trim layer uniformity across profile widths up to 120 mm. Interfacial adhesion between the ASA capstock and the PVC substrate is evaluated by peel testing according to DIN 53357 or equivalent internal methods; acceptable peel strength for window profile capstock is typically > 2.5 N/mm. Surface appearance of coextruded profiles is assessed for gloss at 60° per ASTM D523, with capstock gloss retention targets specified in RAL GZ 716/1 Section 3.2. Weathering performance of the coextruded system is validated per ISO 4892-2:2013 (xenon arc, Method A, cycle 1) with exposure of 8000 h, during which the ASA capstock must exhibit ΔE* < 5.0 and no chalking, cracking, or delamination. The substrate PVC formulation typically contains calcium-zinc stabiliser systems; cadmium-barium formulations are prohibited under REACH Annex XVII entry 23 and must be excluded from compatibility assessments. Process control during coextrusion includes continuous measurement of capstock thickness via non-contact capacitance gauges with tolerance ±0.02 mm from nominal, and melt pressure transducers at the feedblock entry with alarm setpoints at ±15 bar deviation from baseline. Batch-to-batch melt flow rate variation of the ASA capstock material, measured per ISO 1133-1:2022 at 220 °C / 10 kg, must not exceed ±1.5 g/10 min within a production campaign to maintain stable layer distribution.

    The processing window for ASA capstock over PVC is further constrained by the thermal degradation sensitivity of the PVC substrate at temperatures above 210 °C. Prolonged residence time of the ASA melt at 240 °C in a dead spot within the feedblock can induce localised thermal decomposition of the acrylic ester phase, generating volatile degradation products that manifest as surface depressions or fish eyes on the extruded profile. Purging procedures between production runs utilise a commercial purging compound processed at 180–210 °C for 15–20 min, followed by the ASA material flush at production settings for 10–15 min. Adhesion failure at the capstock-substrate interface is a recognised field failure mode in window profiles exposed to direct solar gain in dark-coloured systems where surface temperatures exceed 70 °C; the linear expansion mismatch between ASA capstock and rigid PVC substrate (differential CLTE of approximately 2–3 × 10⁻⁵ K⁻¹) imposes shear stress at the interface during diurnal thermal cycling. Capstock formulations for dark colours (L* < 40) require elevated TiO₂ content of 4–6 phr combined with IR-reflective pigments to mitigate surface temperature rise; long-term creep of the PVC substrate under this thermal load is evaluated per ISO 899-1:2017 at 60 °C for 1000 h.

    Roofing ventilation components moulded from ASA operate under sustained UV irradiance at elevated surface temperatures that routinely reach 75–85 °C on dark-coloured profiles in summer conditions. The material is processed by injection moulding with melt temperature 240–255 °C, mould temperature 45–65 °C, and screw rotation speed 40–80 rpm to avoid excessive shear heating. Pre-drying at 80 °C for 3 h is mandatory when ambient relative humidity exceeds 60% or when regrind content exceeds 15 wt%. The moulded components, including static roof vents and ridge caps, are subjected to heat ageing per ISO 188:2011 at 90 °C for 500 h with evaluation of colour change and tensile impact strength. UV resistance is validated by ISO 4892-3:2016 (fluorescent UV lamps, UVA-340, cycle 1) at 50 °C black panel temperature; acceptance requires > 70% retained tensile strength after 3000 h exposure. Fastener torque retention in moulded bosses is tested per ASTM D6117 or internal equivalent, with minimum pull-out force of 800 N for 5 mm diameter self-tapping screw engagement of 8 mm depth. Published data specific to this grade in roofing applications is limited; grade selection is typically informed by equivalent ASA material performance documented in weathering atlases and supplier technical bulletins.

    Thermal cycling and creep behaviour in outdoor enclosure housings for electrical equipment

    Outdoor telecommunication and power distribution enclosures demand a combination of UV stability, dimensional stability across thermal cycling, and flame retardancy where regulatory requirements mandate self-extinguishing behaviour. ASA XC811-HW is processed for enclosure shells with nominal wall thickness 3.0–5.0 mm using injection moulding machines of 800–1600 tonne clamp force for single-cavity parts with projected areas of 800–1500 cm². Melt temperature is controlled at 235–250 °C, and mould temperature is maintained at 55–75 °C using pressurised water units. The moulding cycle for a 5 mm wall enclosure shell typically comprises injection time 4–7 s, holding pressure 500–700 bar for 12–18 s, and cooling time 35–50 s. Dimensional stability of the moulded enclosure under thermal cycling is evaluated per IEC 60068-2-14:2009 (Test Nb, change of temperature) with −40 °C to +85 °C excursions at 5 °C/min ramp rate, 100 cycles, followed by measurement of warpage and seal interface flatness with a coordinate measuring machine. Maximum permissible warpage at gasket lands is 0.5 mm per 300 mm of linear dimension.

    Creep behaviour under continuous sealing compression is assessed per ISO 899-1:2017 at 60 °C and 5 MPa compressive stress applied to integrally moulded sealing bosses; cumulative creep strain of < 0.8% after 1000 h is the typical acceptance criterion for maintaining IP65 ingress protection per IEC 60529:2013. Outdoor exposure validation follows ISO 4892-2:2013 (xenon arc, Method A, cycle 1) with 5000 h exposure and evaluation of colour shift per ISO 11664-4:2008 and gloss retention per ISO 2813:2014. Flame retardancy is not an inherent property of ASA; where enclosure applications mandate UL 94 V-0 classification, flame retardant additive packages must be incorporated during compounding, and the grade-specific suitability must be confirmed through third-party testing. Electrical clearance and creepage distance requirements per IEC 60664-1:2020 are unaffected by the base polymer but are relevant to moulded standoff and rib geometry design. UV-induced surface degradation of ASA at 5000 h xenon exposure is characterised by a slight increase in surface roughness from Ra 0.2 μm to Ra 0.3–0.4 μm on as-moulded surfaces, which does not impair sealing function when gasket compression exceeds 25% of original gasket thickness. Avoid combination with amine-based antistatic additives in enclosure formulations, as these can induce discolouration under sustained UV exposure through nitroxide radical-mediated oxidation pathways.

    Agricultural machinery body panels and instrument enclosures processed from ASA are exposed to combined UV radiation, pesticide spray drift, and mechanical impact from field debris. Injection moulding parameters mirror those used for automotive exterior components, with melt temperature 240–255 °C and mould temperature 50–70 °C. Chemical resistance to agricultural chemicals is assessed per ISO 22088-3:2008 (environmental stress cracking, bent strip method) using representative pesticide formulations at 1:100 dilution and exposure duration of 72 h at 23 °C; no crazing or cracking is permitted on the tension surface. Impact resistance at low temperature is characterised by notched Izod per ISO 180:2019 (Method A) at −30 °C, with typical retained impact of > 60% relative to room-temperature values for the ASA material class. UV exposure validation for agricultural housings follows ISO 4892-2:2013 with 3000 h xenon arc exposure; acceptance criteria specify colour fastness with ΔE* < 4.0 and no visible surface cracking at 10× magnification. Moulded-in inserts for mounting brackets require post-moulding dimensional audit of hole-to-hole spacing with tolerance ±0.15 mm over 200 mm spans to accommodate field assembly without induced stress. Regrind incorporation up to 20 wt% is permissible for non-appearance agricultural components, with impact strength degradation limited to < 10% relative to virgin material under ISO 180:2019 notched Izod at 23 °C. Published data for this specific grade in agricultural chemical resistance testing is limited; validation programmes must include chemical immersion testing specific to the end-user's pesticide portfolio.

    When hydrolysis resistance governs material selection in pool-side components

    Pool filtration housings, skimmer lids, and pump enclosures manufactured from ASA operate in continuously humid environments with intermittent exposure to chlorinated water and sodium hypochlorite solutions at concentrations up to 5 ppm free chlorine. Hydrolytic stability of the acrylic ester rubber phase is the critical material property, evaluated by immersion testing per ISO 175:2010 in deionised water at 60 °C for 1000 h with measurement of tensile strength retention, elongation at break retention, and mass change. ASA as a material class exhibits superior hydrolysis resistance compared to polycarbonate and certain polyester-based materials; acceptable retention criteria for pool-side components specify > 80% tensile strength and > 70% elongation at break after immersion. The material is injection moulded with melt temperature 235–250 °C and mould temperature 50–70 °C; parts with threaded bosses for plumbing connections are moulded with insert-free design using trapezoidal thread profiles to eliminate stress concentration at metallic insert interfaces. Threaded connection integrity is validated by torque-to-failure testing on 2-inch NPT threads with minimum failure torque of 35 N·m at 23 °C.

    Chemical compatibility with chlorinated water is assessed by cyclical immersion testing comprising 24 h immersion in 5 ppm sodium hypochlorite solution at 40 °C followed by 24 h drying at 23 °C, repeated for 30 cycles. Visual inspection after cycling permits no surface whitening, pitting, or craze development at 10× magnification. UV resistance of pool-side components is validated per ISO 4892-2:2013 with 2500 h xenon exposure at 0.51 W/m² at 340 nm; maximum permitted colour change is ΔE* < 5.0 per ISO 11664-4:2008. Moulded skimmer lids with 3 mm nominal wall thickness are subjected to point load testing at 1000 N on a 50 mm diameter indenter with maximum deflection of 2.0 mm and no permanent set exceeding 0.3 mm after load removal. Avoid combination with di(2-ethylhexyl) phthalate or other phthalate-based plasticiser migrants from flexible PVC components in the same assembly, as these can cause surface tack and accelerated soiling when pooled on ASA surfaces under solar heating.

    High-gloss exterior trim: mould filling, weld line integrity, and UV retention in building fascias

    Architectural fascia boards, corner trims, and decorative column wraps produced by profile extrusion or injection moulding from ASA require consistent high-gloss surface finish retained over decades of outdoor exposure. For profile extrusion, single-screw extruders with screw diameter 45–60 mm and L/D 28:1 to 32:1 are operated at barrel temperatures from 195 °C to 225 °C, with die temperatures 220–230 °C and downstream vacuum calibration using −0.6 bar gauge pressure in stainless steel calibrators with surface finish Ra ≤ 0.05 μm. Extruded profiles with wall thickness 2.5–4.0 mm are cooled through a temperature-controlled water bath at 35–45 °C to minimise frozen-in stress and post-extrusion warpage. Gloss at 60° on extruded surfaces is measured per ISO 2813:2014; acceptance for high-gloss architectural trim requires initial gloss of > 85 GU and retained gloss of > 70 GU after 5000 h xenon exposure per ISO 4892-2:2013. Colour consistency across production batches is controlled by CIELAB measurement with ΔE* tolerance of < 0.8 between batches under D65/10° illuminant per ISO 11664-4:2008.

    Injection-moulded fascia components with long flow paths exceeding 300 mm from gate to last-filled section require specific mould filling analysis to position weld lines outside visible surfaces. Computer-aided mould filling simulation with material viscosity data measured by capillary rheometry at 230 °C, 245 °C, and 260 °C across shear rates of 10–10⁴ s⁻¹ is employed to optimise gate locations before tooling fabrication. Weld line strength in ASA is characteristically lower than base material strength, typically retaining 50–65% of tensile strength per ASTM D638 when tested in tension perpendicular to the weld plane; design rules therefore require weld line placement in low-stress non-appearance regions or the use of hot runner valve gate sequencing to eliminate weld lines on Class A surfaces. Mould surface preparation uses diamond polishing to SPI A-2 or finer finish on cavity surfaces; parting line mismatch tolerance is 0.05 mm maximum. Dimensional audit of moulded fascia components uses a coordinate measuring machine with volumetric accuracy of ±0.015 mm; critical fit dimensions are held to ±0.2 mm for panel lengths up to 1200 mm. Thermal expansion compensation in installation is designed to accommodate CLTE of 0.8–1.0 × 10⁻⁴ K⁻¹ for the ASA material class over the temperature range −20 °C to +70 °C, equating to expansion allowance of 3.5–4.5 mm per 1000 mm of installed panel length.

    Published data specific to this grade in architectural trim applications is limited; validation programmes for equivalent ASA materials reference weathering results from 12-year Florida outdoor exposure showing ΔE* of < 4.0 for white and < 6.0 for dark brown formulations, with gloss retention of 50–60% relative to initial values. The discrepancy between accelerated xenon testing and outdoor weathering underscores the need for parallel exposure programmes during initial product qualification. Process stabilisation during colour changeover on extrusion lines requires purge sequences with 5–8 kg of the subsequent colour material or 2–3 kg of commercial purging compound, followed by 30 min of production-rate extrusion before colour specification compliance is confirmed by inline spectrophotometry. Regrind utilisation in architectural fascia is limited to 10–15 wt% for dark colours and 0–5 wt% for white due to yellowing sensitivity from thermal history accumulated in regrind streams.

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