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Guangdong Daosheng ABS A6200FN/R

    • Product Name: Guangdong Daosheng ABS A6200FN/R
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 399301
    Density 1.18 g/cm³
    Melt Flow Rate 10 g/10 min (220°C/10 kg)
    Tensile Strength 45 MPa
    Elongation At Break 20%
    Flexural Strength 70 MPa
    Flexural Modulus 2200 MPa
    Notched Izod Impact Strength 15 kJ/m²
    Heat Deflection Temperature 80 °C
    Vicat Softening Temperature 95 °C
    Flammability Rating UL94 V-0
    Dielectric Strength 15 kV/mm
    Volume Resistivity 1.0E+15 Ω·cm
    Water Absorption 24h 0.2%
    Molding Shrinkage 0.4-0.6%
    Processing Method injection molding

    As an accredited Guangdong Daosheng ABS A6200FN/R factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Guangdong Daosheng ABS A6200FN/R is packaged in 25 kg moisture-proof woven bags, typically supplied on pallets.
    Container Loading (20′ FCL) 20′ FCL loaded with Guangdong Daosheng ABS A6200FN/R resin in 25 kg bags, palletized, shrink-wrapped, and securely stowed for export.
    Shipping Guangdong Daosheng ABS A6200FN/R is shipped as solid thermoplastic resin pellets in moisture-proof 25 kg bags, palletized and shrink-wrapped. Store in a cool, dry, ventilated area away from direct sunlight and heat. Normally not classified as dangerous goods; handle according to the SDS.
    Storage Store Guangdong Daosheng ABS A6200FN/R in a cool, dry, well-ventilated warehouse, away from direct sunlight, rain, heat, sparks, and open flames. Keep original bags sealed and palletized; avoid moisture, static buildup, and contact with strong oxidizers, acids, or bases. Prevent bag rupture and unstable stacking. Follow the supplier’s SDS, local regulations, and first-in, first-out stock rotation.
    Shelf Life Shelf life is typically 12 months from manufacture when stored dry, cool, ventilated, away from sunlight and moisture.
    Application of Guangdong Daosheng ABS A6200FN/R

    Thermal Degradation, Drying and Barrel Residence Limits in Thin-Wall Housings

    Guangdong Daosheng A6200FN/R is supplied as a flame-retardant ABS compound for thin-wall electrical accessory enclosures where minimum wall thickness is 1.5 mm. The pellets are dried in a closed-loop desiccant dryer at 80 °C for 4 h to reduce residual moisture below 0.02 wt%; if moisture exceeds 0.05 wt% at melt temperatures above 220 °C, hydrolysis of the butadiene-rich elastomer phase generates volatile by-products that appear as silver streaking adjacent to edge gates. A general-purpose screw with L/D 20:1 to 24:1 and compression ratio 2.2:1 to 2.6:1 is preferred because screws with compression ratios above 3.0:1 can shear-heat the brominated flame-retardant and antimony trioxide synergist beyond 245 °C even when the control-zone setpoints are lower. Dry blending with amine-based stabilisers is avoided because acid scavenging interferes with the antimony trioxide–bromine radical termination cycle and lowers the UL 94 vertical burn rating. The narrow thermal window is a process conflict: the flame-retardant package undergoes decomposition above 250 °C, releasing antimony tribromide and hydrogen bromide, which causes mould plate staining, gate blush and a measurable fall in vertical burn performance from V-0 to V-2 on snap-fit plaques.

    Barrel zone setpoints ascend from 180 °C at the feed throat to 210 °C, 215 °C and 220 °C in the transition and metering zones, with nozzle temperature not exceeding 225 °C. Melt temperature measured by an immersion thermocouple is kept between 200 °C and 225 °C. Screw speed is maintained between 30 rpm and 60 rpm for a 40 mm diameter screw; higher screw speeds produce frictional heating more than 10 °C above the barrel setpoint. Injection speed is set to fill the cavity within 0.5 s to 2.5 s and then reduced at the runner-to-wall transition to hold shear rates at the gate land below 10,000 s⁻¹. Holding pressure is maintained at 55 MPa to 75 MPa hydraulic, and screw back pressure is controlled between 0.5 MPa and 1.0 MPa. Mould temperature is held at 40 °C to 70 °C with turbulent water channels; mould zones below 35 °C produce brittle weld lines, while zones above 75 °C extend cooling cycle time and increase surface gloss scatter on textured vertical walls. Residence time at melt temperature is limited to 5 min; accidental machine stoppages longer than 5 min require the barrel to be purged with a low-MFR polypropylene to remove degraded FR char before resuming production.

    Where unfilled ABS fails the 650 °C glow wire test when wall thickness falls below 2.5 mm, A6200FN/R is specified for terminal guards, relay bases and power meter enclosures. The compound is moulded in tools with ejector pins located away from thin snap-fit sidewalls because localised high ejection force after shrinkage of 0.4 % to 0.7 % can generate microcracks at flame-retardant-rich surface layers. Rib-to-wall ratio is maintained below 0.4 and boss height-to-OD below 2.0 to avoid sink marks and internal voids, which lower glow-wire ignition temperature by exposing the flame-retardant system to oxygen at internal surfaces. The gate is located at the thickest section, not at a living hinge or snap-fit root, because gate-adjacent molecular orientation creates a zone where UL 94 vertical burn afterflame times are consistently 2 s to 4 s longer than in the mid-wall position. Because the butadiene-rubber phase is susceptible to environmental stress cracking under contact with ketones, esters and chlorinated hydrocarbons, assembly cleaners are restricted to aqueous detergents at pH below 10; solvent-based pad-printing inks are applied only after a compatibilising primer or over a flame-treated surface.

    Compliance for unattended appliance housings carrying current above 0.5 A is assessed under IEC 60335-1 Clause 30.2.3.1 using glow-wire apparatus specified in IEC 60695-2-10. A6200FN/R must demonstrate GWFI at 850 °C or GWIT at 775 °C on the final moulded wall thickness, not on a laboratory plaque, because flame-retardant distribution varies with flow length and packing pressure. The comparative tracking index is measured under IEC 60112 using solution A; typical FR ABS grades fall between 250 V and 400 V, which supports creepage-distance reductions for polluted micro-environments but does not permit unfilled insulation above pollution degree 3. Moulded parts are annealed at 70 °C for 2 h after ejection to relieve frozen-in stress before testing; unannealed parts often exhibit greater scatter in tensile elongation at break because shrinkage-induced residual stress concentrates at weld lines.

    What Restricts Hot Runner Manifold Temperature in Multi-Cavity Charger Shells?

    In multi-cavity USB charger shell production, the hot runner manifold is controlled at 210 °C to 225 °C, not at the 240 °C setpoint sometimes used for non-flame-retardant ABS. The restriction comes from stagnant melt at manifold corners and valve-gate bushings; when cavity-block changeovers extend cycle time, local residence time exceeds 5 min. Under these conditions brominated flame-retardant species undergo dehydrobromination, producing free hydrobromic acid that corrodes nickel-plated runner channels and deposits a brown-powder residue on valve pins. The result is visible gate smear on dark-grey shell surfaces and a reduction in UL 94 vertical burn rating from V-0 to V-1 because the char-forming synergist is partially consumed before injection into the cavity. Multi-cavity tools with 8 to 16 cavities are more sensitive than single-cavity tools because runner volume-to-shot-weight ratio increases above 0.30, extending thermal history.

    Valve-gate pins are operated with a delay of 0.2 s after fill begins to avoid freezing the flame-retardant skin layer at the gate. Sequential filling from the centre cavity outward reduces melt-front advancing speed, maintaining a melt-front angle below 45° across engraved logo ribs. The clamping force on a charger shell with projected area 35 cm² and cavity pressure 45 MPa is kept above 160 kN per cavity; insufficient clamp force produces flash at the mould parting line that reduces flame-retardant layer thickness at the edge and fails the IEC 60695 glow-wire test. Screw decompression after plastication is limited to 3 mm to 5 mm because larger suckback introduces air and causes brown oxidation streaks in light-grey parts.

    Standard designationTest parameterTypical FR ABS envelope / acceptance basis
    UL 94Vertical burn, 1.5 mmV-0; afterflame ≤ 10 s per flame application
    IEC 60695-2-12Glow-wire flammability index850 °C for unattended appliance current-carrying parts
    IEC 60695-2-13Glow-wire ignition temperature775 °C minimum for housing parts
    IEC 60112:2009Comparative tracking index, solution A250–400 V
    ISO 1133-1:2022Melt volume rate, 220 °C/10 kg15–30 cm³/10 min
    ISO 527-2Tensile yield, 50 mm/min38–45 MPa
    ISO 178Flexural modulus, 2 mm/min2,200–2,600 MPa

    Ultrasonic welding of router and set-top box chassis introduces local frictional heating at the joint line that can exceed 180 °C within 0.3 s; if the joint design is a shear joint with interference 0.25 mm, the energy director melts and flows into a flash trap. A6200FN/R is weldable only when the joint is placed away from flame-retardant skin concentrations at gate-frozen walls; near-gate weld lines often fail the V-0 test because the FR skin is broken and exposed polybutadiene phase burns with dripping. For snap-fit-heavy chassis, the living hinge is formed at 40 °C mould temperature and flexed only after the part cools below 45 °C; hot flexing above the amorphous-phase glass transition of 95 °C to 105 °C creates stress-whitening and preferential ignition paths. Post-mould machining such as drilling for antenna ports is performed with low-feed drills below 1,000 rpm to avoid melting chips that adhere to hole edges and form combustion channels.

    Electrostatic discharge compliance for router housings is achieved by external metallisation or conductive pads, not by carbon-fibre filling of the grade, because conductive filler additions at levels above 5 wt% degrade UL 94 vertical burn performance and create surface resistivity below 10⁶ Ω. The moulded part is measured for surface resistivity under IEC 62631-3-2 at 23 °C and 50 % RH; typical unfilled flame-retardant ABS remains in the insulative range above 10¹² Ω. If end-user specifications require a dissipative surface, the design carries a separate painted conductive layer rather than modifying the base polymer, because flame-retardant synergist migration to the surface increases contact resistance variability by ±20 % after 240 h at 60 °C.

    When Post-Consumer Recyclate Dilution Is Required in E/E Enclosures

    The decision to dilute virgin A6200FN/R with post-consumer ABS recyclate is constrained by the flame-retardant loading in the recyclate stream. Closed-loop E/E enclosure recyclate containing 8 wt% to 12 wt% brominated FR and 4 wt% to 6 wt% antimony trioxide can be added at 10 wt% to 20 wt% without losing V-0 at 1.6 mm, but batch-to-batch variation in FR concentration and rubber crosslink density widens Charpy notched impact scatter from ±0.8 kJ/m² to ±1.8 kJ/m² under ISO 179-1/1eA. The recyclate fraction is recompounded on a co-rotating twin-screw extruder with L/D 36:1 and a two-stage vacuum vent at -0.08 MPa; low-kneading screw elements are used downstream of the feed zone because excessive shear breaks the brominated FR char network and reduces char yield during UL 94 testing. Recyclate containing 0.2 wt% moisture creates hydrolysis-derived pitting on textured surfaces; the blend is therefore re-dried at 80 °C for 6 h because pre-compounded recyclate pellets hydrate faster than virgin pellets due to higher surface area from regrind.

    Published data for this specific configuration is limited; converters therefore run an incoming melt volume rate check under ISO 1133-1 at 220 °C/10 kg and reject recyclate lots with MVR shift above ±15 % relative to virgin pellets. A pvT gate-freeze study performed on an instrumented multi-cavity tool shows that the recycled blend reaches gate freeze 1.5 s earlier than virgin compound because the recyclate lowers melt compressibility; holding-time profiles are shortened accordingly to prevent overpacking at the gate land. No open-loop claims are made for colour shift; dark grey and black parts are preferred over white shades because an additional 0.5 wt% titanium dioxide used in white pigment packages can reduce UL 94 vertical burn performance from V-0 to V-2 when wall thickness is below 1.8 mm.

    Low-Emission Automotive Interior Trim Retains Dimensional Integrity at 85 °C

    Long-term exposure of automotive interior components to 85 °C cabin air does not eliminate the flame-retardant function of A6200FN/R, but it shifts the failure mode from combustion to mechanical creep at snap-fit engagements. Steering column upper and lower covers, instrument panel side trims and air vent grilles are moulded with an average wall thickness of 2.0 mm to 2.5 mm and are subjected to heat ageing under DIN 75220 or equivalent OEM specifications at 85 °C for 1,000 h. After ageing, retention of tensile elongation at break exceeds 60 % of the unaged value only if the parts are annealed at 70 °C for 2 h before heat ageing; unannealed parts develop environment-assisted cracking at moulded-in assembly bosses because frozen-in stress from ejection adds to thermal expansion stress.

    Emission behaviour is measured by VDA 277 total volatile organic compound testing. The accepted upper limit for low-emission interior trim is typically 50 µgC/g; grade-specific results should be verified with Daosheng documentation because migration of antimony trioxide synergist into the vapour phase at elevated temperature is influenced by the carrier resin and pigment formulation. Fogging under DIN 75201 method B remains below 2.0 mg on glass plates only when the mould release is low-aromatic and fully evaporated before assembly. Light-coloured grades exposed to sunlight through side windows require opaque UV-cured polyurethane coating because the butadiene phase in ABS yellows after 300 h of ISO 4892-2 cycle A xenon exposure; the coating, not the base resin, provides the UV barrier. Uncoated parts in unpainted grained finishes are therefore restricted to hidden positions or dark colours, and outdoor f1 ultraviolet ratings are not claimed.

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    Certification & Compliance
    More Introduction

    Guangdong Daosheng ABS A6200FN/R is supplied as a pelletized acrylonitrile-butadiene-styrene compound for injection moulding and profile extrusion. The grade designation follows the polymer family ABS; the suffix A6200FN/R is manufacturer-specific and is not defined by the ISO 2580-1 designation system for ABS moulding and extrusion materials. Incoming characterization should therefore not rely on the alphanumeric suffix alone but on a certificate of analysis and the supplier’s published technical data sheet. This is particularly important when thin-wall electrical enclosures or electrotechnical components must satisfy end-product flammability and thermal requirements.

    What specification fields must be resolved before lot acceptance?

    At minimum, lot acceptance for a high-flow ABS such as A6200FN/R should include melt volume-flow rate under ISO 1133-1 at 220 °C/10 kg, density under ISO 1183-1, tensile yield stress and tensile modulus under ISO 527-2 at 50 mm/min, flexural strength and flexural modulus under ISO 178, Charpy notched impact under ISO 179-1, heat deflection temperature under ISO 75-2, and Vicat softening temperature under ISO 306 method B50. Flame-retardant grades should additionally be assessed by UL 94 vertical burn at the production wall thickness. Suppliers sometimes report ASTM-based data, but values obtained under ASTM D638-14 are not directly interchangeable with ISO values because specimen dimensions and test speed differ.

    Field Test procedure Typical high-flow ABS band Lot-release note
    Density ISO 1183-1 1.04–1.07 g/cm³ Denser if flame-retardant additive is present
    Melt volume-flow rate ISO 1133-1, 220 °C, 10 kg 12–35 cm³/10 min Not comparable to ASTM D1238 unless conditions identical
    Tensile yield stress ISO 527-2 34–45 MPa Flame-retardant grades may be at lower end
    Tensile modulus ISO 527-2 1800–2600 MPa Specimen type 1A
    Flexural strength ISO 178 50–65 MPa Rate-dependent; report test speed
    Charpy notched impact ISO 179-1, 1eA, 23 °C 10–25 kJ/m² Verify at low temperature if required
    Heat deflection temperature ISO 75-2, 1.8 MPa 75–95 °C Thickness affects test result
    Vicat softening temperature ISO 306, B50 95–110 °C Not a continuous-use rating
    Flammability class UL 94 vertical burn V-2 to V-0 at 1.5–3.0 mm Thickness-dependent; check UL Yellow Card
    Residual moisture ISO 15512 or Karl Fischer ≤0.05 % Before melt processing

    Published data for the A6200FN/R-specific configuration is limited; the ranges above are representative of high-flow ABS compounds and should not replace the supplier’s certificate of analysis.

    Melt rheology and pre-drying boundary conditions

    The dominant process risk for high-flow ABS is moisture-induced splay and thermal degradation. ABS absorbs moisture slowly, but in humid environments above 60 % RH, unpredried pellet can reach 0.1 % moisture. During injection, rapid expansion of moisture generates visible silver streaks and reduces weld-line tensile strength. Desiccant drying at 80 °C for 2–4 h with a dew point below -30 °C is the standard boundary. Residual moisture must be held at or below 0.05 % by Karl Fischer titration or ISO 15512. Drying above 85 °C or beyond 4–6 h can cause oxidative degradation, yellowing, and depletion of impact modifier.

    Melt temperature settings for high-flow ABS are typically 210–240 °C from feed throat to nozzle; the nozzle should be controlled at 230–240 °C to avoid premature solidification while limiting thermal residence. If the grade contains a flame-retardant additive system, the upper melt temperature should be capped at 240 °C and residence time below 5 min. On 80–150 t injection moulding machines with 25–35 mm three-zone screws, holding cushion is maintained at 3–6 mm and decompression at 2–3 mm. Batch-to-batch MVR variation can shift fill time and injection pressure by more than 5 %, so process control should use fill time and cushion position as primary indicators rather than fixed injection speed. Failure modes observed on production lines include splay, black specks, nozzle clogging, delamination at weld lines, and gate blush. These are commonly traced to moisture, contaminated regrind, or residence time.

    When A6200FN/R replaces general-purpose ABS in thin-wall electrical housings

    When A6200FN/R is substituted for general-purpose ABS in thin-wall electrical housings, the primary advantage is lower filling pressure and shorter cycle time. At wall thicknesses of 1.5–2.0 mm, a high-flow ABS can fill a multi-cavity tool at lower injection pressure than a standard ABS, but the grade must be confirmed for the required flammability class. A UL 94 V-0 listing at 1.5 mm or 2.0 mm is common for flame-retardant ABS grades, but it is not an intrinsic property of all ABS. The supplier’s UL Yellow Card is the controlling document for minimum thickness and substrate identity.

    The mechanical penalty of flame-retardant packaging appears mainly in notched impact and tensile elongation. For enclosure bosses, snap-fit beams, and heat-stake inserts, design should use lower allowable strain. A general-purpose ABS with Charpy notched impact of 18–30 kJ/m² at 23 °C may be compared with a high-flow flame-retardant ABS at 8–16 kJ/m² under the same test. Boss outer diameter should be at least 2.0–2.5 times screw diameter, and hole-to-edge distance at least 1.5 times hole diameter to avoid cracking in thin sections.

    Mould temperature should be held at 40–60 °C to balance surface appearance and shrinkage control. Packing pressure between 50–70 MPa and packing time sufficient for gate freeze are required; for 1.5 mm walls, gate freeze time is typically below 3–4 s. Cold runner diameters below 3 mm can produce excessive shear heating and should be avoided unless flow analysis supports smaller dimensions.

    Polycarbonate blends and high-heat ABS grades impose different thermal boundaries

    High-flow ABS A6200FN/R should not be considered a direct substitute for PC/ABS when the service temperature exceeds 80 °C under load. PC/ABS grades typically exhibit heat deflection temperature at 1.8 MPa of 95–115 °C and notched Izod impact values higher than 25 kJ/m², but they require melt temperatures of 260–280 °C and higher drying temperatures. High-heat ABS grades may reach HDT values near 90–100 °C, but their melt viscosity is higher and their flow length is shorter. For A6200FN/R, published data for this specific configuration is limited; the performance boundary should be established by spiral-flow testing and HDT under ISO 75-2 at the actual part thickness.

    Grade family HDT at 1.8 MPa Charpy notched impact at 23 °C Typical melt temperature Main limitation
    General-purpose ABS 75–95 °C 18–30 kJ/m² 220–240 °C No flame resistance
    High-flow flame-retardant ABS 78–88 °C 8–16 kJ/m² 210–235 °C Lower ductility; narrow thermal window
    PC/ABS 95–115 °C 25–45 kJ/m² 260–280 °C Higher processing energy and cost
    High-heat ABS 90–100 °C 15–25 kJ/m² 240–260 °C Higher melt temperature may exceed flame-retardant stability

    The choice among these materials is governed by the end-product heat exposure, flame-retardant class, and tooling capability. A6200FN/R’s position in this matrix is inferred as high-flow and potentially flame-retardant based on the suffix convention, but the supplier’s datasheet remains the sole authoritative source for grade-specific HDT and impact.

    For the European Union, electrical and electronic equipment applications require compliance with Directive 2011/65/EU on the restriction of hazardous substances and Regulation 1907/2006 for REACH. ABS A6200FN/R should be evaluated at the article level because pigment masterbatches, flame-retardant packages, and recycling content can influence the final SVHC profile. If the part is used in a household appliance enclosure, glow-wire testing under IEC 60695-2-11 at 650 °C or 750 °C and ball-pressure testing under IEC 60695-10-2 may also be required by product safety standards such as IEC 60335-1. These are end-product obligations, not resin-only declarations.

    Regrind management for high-flow ABS should be limited to clean, unpainted, unconverted scrap from the same grade. Regrind levels up to 20–25 wt% are routinely used; above this level, cumulative thermal history can reduce notched impact and increase yellowing. The compound is incompatible with polyamide and acetal, and contamination of 0.5 wt% or less can cause visible delamination and brittle weld lines. In hot-runner systems, small gate orifices below 1.0 mm can generate excessive shear, increasing melt temperature locally beyond the degradation threshold and causing black specks or nozzle clogging. For multicolour assemblies, the second resin should be verified for chemical compatibility and matched to the same shrinkage class; ABS grades with large differences in MVR can create boundary-layer orientation defects.

    For sheet extrusion of ABS A6200FN/R, a single-screw extruder with L/D 32–40, vacuum venting, and barrel temperatures of 205–225 °C is the typical configuration. The melt should be passed through a screen-pack of 60/80/100 mesh to trap degraded gel particles; die lip opening is set at 2.0–3.0 times the intended sheet thickness to compensate die swell. Polished three-roll calendering at 70–90 °C is used for gloss control. The grade is not recommended for load-bearing structural components where sustained tensile stress above 60 °C would exceed the creep resistance of unfilled ABS.

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