| HS Code | 788252 |
| Material Type | ABS |
| Density G Cm3 | 1.18 |
| Melt Flow Rate G 10min | 8 |
| Tensile Strength Mpa | 45 |
| Elongation At Break Percent | 25 |
| Flexural Modulus Mpa | 2200 |
| Notched Izod Impact Strength Kj M2 | 18 |
| Heat Deflection Temperature C | 85 |
| Vicat Softening Temperature C | 95 |
| Ul94 Rating | V-0 |
| Glow Wire Ignition Temperature C | 750 |
| Molding Shrinkage Percent | 0.4-0.6 |
| Processing Method | injection molding |
| Form | pellets |
| Color | natural/black |
| Rohs Compliance | compliant |
As an accredited Dongguan Anshuyi ABS 346A-8-G factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dongguan Anshuyi ABS 346A-8-G is supplied in 25 kg moisture-resistant woven bags, palletized for industrial shipment. |
| Container Loading (20′ FCL) | 20′ FCL loading of Dongguan Anshuyi ABS 346A-8-G, palletized bags secured in a clean, dry container for export. |
| Shipping | Dongguan Anshuyi ABS 346A-8-G is generally shipped as non-hazardous ABS copolymer pellets in sealed moisture-barrier bags, cartons, or bulk containers. Keep dry and away from heat, sunlight, and contamination. Handle according to the SDS and applicable transport regulations; no UN number is normally required. |
| Storage | Store Dongguan Anshuyi ABS 346A-8-G in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and oxidizing agents. Keep containers tightly closed, in original packaging, and palletized to prevent moisture, dust, and contamination. Avoid prolonged high humidity or temperatures that may affect material properties. Follow the supplier’s SDS and local regulations. |
| Shelf Life | Store in a cool, dry, ventilated area; typical shelf life is 12 months in unopened original packaging under recommended conditions. |
In low-gloss automotive interior applications, ABS 346A-8-G is evaluated as the styrenic phase in polycarbonate/ABS blends rather than as a neat resin because the polycarbonate contributes heat deflection temperature and the ABS phase lowers melt viscosity for long-flow instrument panel cavities. The industrial compliance framework for this configuration includes FMVSS 302 and ISO 3795 for horizontal burn behaviour with a maximum burn rate of 100 mm/min, ISO 6452:2021 for gravimetric fogging with a typical acceptance limit of 5 mg or tighter depending on OEM specification, VDA 278:2011 for volatile organic compound and fogging condensate reporting, SAE J2412 xenon-arc weathering for interior trim with ΔE criteria commonly set between 1.5 and 3.0, and Regulation (EC) No 1907/2006 REACH together with Directive 2011/65/EU RoHS Annex II substance restrictions. In downstream compounding, ABS 346A-8-G is metered at 30–50 mass % against polycarbonate at 50–70 mass %, with an MBS core-shell impact modifier at 2–5 mass % and a hindered phenolic phosphite stabilizer package at 0.1–0.3 mass % to suppress thermal degradation during twin-screw extrusion. Compounding is conducted on a co-rotating twin-screw extruder with 40:1 L/D ratio, vacuum venting at -0.08 MPa, melt temperature of 240–270 °C, and screw speed adjusted to avoid shear heating above 280 °C because polybutadiene degradation releases oxidative radicals that create brown streaks and odour in the molded part. Injection molding of the compounded pellets requires pre-drying at 80 °C for 2–4 h when relative humidity exceeds 60 %, a reciprocating screw with 20:1 L/D ratio, melt temperature 250–280 °C, mold temperature 60–80 °C, and textured tool surfaces with grain depth of 25–35 μm to achieve low-gloss retention. Production-scale experience indicates that gloss variation is more often controlled by rubber particle size distribution and polycarbonate melt viscosity than by mold polish alone, and mold trials should include short-shot, gate-freeze, and residence-time studies before tool release. Terminal part types include lower instrument panel inserts, glove box outer doors, center console side panels, door grab handle covers, and seat side shields. Published data for this specific configuration is limited; therefore, production validation on the intended tooling is necessary when migrating from an established ABS grade.
Low-voltage electrical enclosure compounds formulated from ABS 346A-8-G are constrained by the decomposition window of halogenated flame-retardant synergists, tool corrosion from acidic by-products, and surface blush caused by incompatibility at the venting zone. The base ABS is dosed at 75–85 mass %, a brominated epoxy oligomer or TBBPA derivative at 12–20 mass %, antimony trioxide at 3–5 mass %, and a thermal stabilizer/acid scavenger at 0.5–1.5 mass %; only RoHS-compliant flame retardants are used because Directive 2011/65/EU restricts polybrominated biphenyls and polybrominated diphenyl ethers. Compounding is performed on a twin-screw extruder with 32:1 to 40:1 L/D ratio, temperature profile from 180 °C rear zone to 220 °C die, vacuum venting, and underwater pelletization to minimize fines. Pre-drying at 80 °C for 2–4 h to below 0.05 % moisture is mandatory because residual water hydrolyzes the flame-retardant package and produces surface splay. Injection molding uses a medium compression screw with 20:1 L/D, melt temperature 200–230 °C, nozzle temperature 220–240 °C, mold temperature 40–70 °C, and clamp force calculated at 0.3–0.5 t/cm² projected area. Terminal part types include miniature circuit breaker housings, residual current operated device bases, wall socket faceplates, consumer unit enclosures, and industrial control panel components. The operational boundary is the melt temperature: sustained heating above 240 °C accelerates release of acidic species that can etch uncoated tool steel and produce brown deposits in hot runner manifolds, so residence time should be minimized and shutdown purging with a flame-retardant-compatible styrenic purge compound is required.
| Standard | Specimen / condition | Acceptance criterion |
|---|---|---|
| UL 94 | 1.5 mm thickness | V-0 rating; no cotton ignition |
| IEC 60695-11-10 | 50 W flame, 1.5 mm specimen | Afterflame ≤ 10 s, total afterflame ≤ 50 s |
| IEC 60695-2-11 | 650 °C glow wire | No ignition; flame and glow time ≤ 5 s |
| IEC 62368-1 | Fire enclosure assembly | Compliance with clause 6.4 |
For small appliance structural housings, the replacement of flame-retardant HIPS with ABS 346A-8-G is justified by higher notched impact resistance and better resistance to common kitchen oils when the housing is exposed during service. The relevant compliance base is IEC 60335-1 household appliance safety, especially clause 30 for resistance to heat and fire, and UL 746C for polymeric materials used in electrical equipment, with ball-pressure evaluations conducted at 125 °C under IEC 60695-10-2 where end-product temperature rise requires it. The formulation is generally a neat ABS system with 96–99 mass % ABS 346A-8-G, 2–4 mass % color masterbatch, and 0.5–1.5 mass % processing aid when thin-walled sections below 1.5 mm require improved flow length; no plasticizer is added because low-volatility plasticizers migrate and degrade surface adhesion in overmolded or decorated parts. Processing uses a conventional injection molding machine with a 20:1 L/D general-purpose screw, melt temperature 220–250 °C, mold temperature 50–80 °C, and a hot runner with valve gating for multi-cavity appliance tools. The failure mode to avoid is environmental stress cracking at gate areas when the molded part is exposed to concentrated acetone, methyl ethyl ketone, or ester-based plasticizers; chemical compatibility with cleaning agents must be tested on production parts, not only on ASTM flexural bars. Terminal part types include vacuum cleaner canisters and hose connections, hand tool motor housings, food processor bases, steam iron shrouds, and lightweight floor care structural parts. Because high-gloss surfaces show flow lines more readily than textured surfaces, tooling layouts should balance fill velocity and avoid hesitation lines when wall thickness varies by more than 0.5 mm.
ABS 346A-8-G is injection molded into DWV fittings where continuous service temperature remains below 60 °C and intermittent exposure does not exceed 80 °C; above this boundary the modulus and long-term creep resistance of unplasticized ABS become limiting. Product compliance is anchored to ASTM D2661-21 for acrylonitrile-butadiene-styrene plastic drain, waste, and vent pipe and fittings, ASTM D3965-21 for ABS plastic pipe and fittings materials, ISO 15493:2003 for industrial ABS piping systems, and EN 1455-1 where European DWV installations require system certification. The formulation uses 95–100 mass % ABS 346A-8-G with 0.5–2 mass % carbon black and/or UV stabilizer masterbatch for outdoor exposure and 0.1–0.5 mass % antioxidant; no impact modifier dilution is normally required because the ABS already contains the polybutadiene rubber phase. Injection molding uses a cold runner mold with side cores and unscrewing cores for threaded trap adapters, melt temperature 200–230 °C, mold temperature 40–60 °C, and controlled screw recovery to avoid excessive shear heating; residual moisture above 0.05 % causes splay and reduces weld-line strength in the vicinity of core pins. Terminal product types include P-traps, wyes, couplings, sanitary tees, threaded adapters, closet flanges, and cleanout plugs. ABS DWV systems are not pressure-rated for continuous hot water lines, and compressed air service requires derating and additional risk assessment because ABS can exhibit brittle failure when notched and exposed to impact at low temperatures or incompatible thread sealants.
Diameter stability during filament extrusion of ABS 346A-8-G is governed by melt temperature uniformity, moisture content, and the consistency of the melt pump suction pressure. The formulation is based on 100 parts ABS 346A-8-G, 0.5–1.5 phr of a styrenic processing aid, 0–3 wt% pigment masterbatch, and no plasticizer because plasticizer reduces dimensional stability and increases warpage in printed parts. Filament produced from this compound is characterized under ASTM D638-14 or ISO 527-2:2012 for tensile properties and ISO 1133-1:2022 for melt volume-flow rate; diameter tolerance is set at 1.75 ± 0.05 mm or 2.85 ± 0.10 mm with ovality not exceeding 0.03 mm. Extrusion is performed on a single-screw extruder with 24:1 to 30:1 L/D ratio, screen pack 40/60/80 mesh, melt pump, and a dual-axis laser gauge with closed-loop control; pre-drying at 80 °C for 2–3 h to below 0.04 % moisture is required to prevent microbubbles that cause filament breakage during spooling. Printed parts are produced with nozzle temperature 220–250 °C, bed temperature 90–110 °C, an enclosed chamber, and print speeds adjusted to avoid excessive curl; styrene vapour extraction is required because ABS releases styrene during extrusion and printing. Terminal product types include functional prototypes, assembly jigs, inspection fixtures, drill templates, and low-volume vacuum forming tools. Published data for this specific configuration is limited; when changing color masterbatch or pigment chemistry, re-validation of laser gauge scatter and spooling tension should be performed because carbon black and fine pigment aggregates alter melt viscosity at low shear rates.
Because network equipment enclosures operate continuously at elevated internal temperatures, ABS 346A-8-G is compounded into flame-retardant or PC/ABS formulations rather than neat general-purpose ABS when fire enclosure requirements apply. Flame-retardant versions use 70–80 mass % ABS, 15–25 mass % brominated flame-retardant package, 3–5 mass % antimony trioxide, and 0.5–1.5 mass % stabilizer/acid scavenger; PC/ABS versions use ABS at 30–50 mass % with polycarbonate at 50–70 mass % for improved heat deflection. Compliance is evaluated under IEC 62368-1 for fire enclosure and mechanical strength, UL 94 V-0 at 1.5 mm or V-1 at 1.5 mm depending on enclosure size and internal power density, IEC 60695-11-10 for flame testing, and Directive 2014/30/EU electromagnetic compatibility for the finished device; the ABS itself provides no inherent EMI shielding and requires conductive coating, electroless copper-nickel plating, or metal inserts to meet radiated and conducted emission limits. Injection molding uses melt temperature 230–260 °C, mold temperature 60–80 °C, texture depths of 18–25 μm for matte surfaces, and low-pressure filling near the end of stroke to reduce gas traps at snap-fit bosses. Terminal product types include router clamshells, set-top boxes, network switches, optical network terminal enclosures, and wall-mount brackets. Prolonged residence above 250 °C can produce brown streaks and reduce flame-retardant effectiveness, so cycle interruption protocols must include immediate purge and barrel temperature reduction.
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Dongguan Anshuyi ABS 346A-8-G is an acrylonitrile-butadiene-styrene copolymer supplied in pellet form for injection molding and sheet extrusion conversion. The grade identifier contains supplier-specific coding that requires verification against the lot certificate; published datasheet values for this exact configuration are limited. Incoming resin should be designated under ISO 1043-1:2011 and assessed within the specification framework of ISO 2580-1:2019. Representative general-purpose ABS reference data place density at 1.03–1.07 g/cm³, tensile yield stress at 35–50 MPa, flexural modulus at 1.8–2.5 GPa, and notched Charpy impact at 10–30 kJ/m² when tested to ISO 179-1/1eA. These values are control ranges, not lot-specific release limits. The resin is hygroscopic; at ambient relative humidity above 60 %, predrying at 80 °C for 2–4 h is required to reduce residual moisture below 0.1 %. Moisture above this threshold produces splay, silver streaks, and inconsistent gloss on molded surfaces. On production lines, a desiccant-bed dryer with a dew point below -30 °C is preferred over hot-air ovens because the outlet air temperature can be held within ±3 °C and moisture regain in the hopper is reduced.
On injection molding machines with clamp force from 800 kN to 12,000 kN, ABS 346A-8-G should be processed with barrel zones set between 220 °C and 260 °C. The feed throat is maintained below 60 °C to prevent premature bridging and pellet agglomeration. Nozzle temperature should track the front zone within ±5 °C; sustained operation above 265 °C increases the risk of butadiene degradation and yellowing, while operation below 215 °C raises melt viscosity, screw recovery torque, and the incidence of unmelted material in thin sections. Mold temperature should be held between 40 °C and 80 °C, with the upper range reserved for parts requiring low residual stress and higher surface gloss. Fill speed should be moderate to slow; shear rates above 50,000 s⁻¹ can induce jetting and surface haze. Hold pressure is set to achieve gate seal without overpacking, and specific values depend on gate diameter, wall thickness, and melt temperature. On single-screw sheet extrusion lines with L/D ratios from 24–30, a barrier screw with a mixing section provides more uniform melt temperature than a general-purpose metering screw. Barrel profiles are set flat or with a slight reverse profile. Published data for grade-specific melt mass-flow rate are limited; the operator should record melt volume-flow rate under ISO 1133-1:2022 at 220 °C with 10 kg load and compare it against the supply lot before regrind use. If the measured melt volume-flow rate shifts by more than 15 % between lots, processing parameters should be reestablished because filling pressure, gate freeze time, and shrinkage can change.
The suffix may indicate a glass-reinforced or glass-filled variant in some manufacturer coding systems. Published data for this specific configuration is limited; the following distinction is based on conventional ABS reinforcement behavior and must be confirmed against the certificate of analysis. In unfilled ABS, flexural modulus ranges from 1.8 GPa to 2.5 GPa; glass-reinforced ABS at 10–20 wt% typically raises flexural modulus to 3.5–6.0 GPa and tensile strength to 50–70 MPa, while notched impact strength falls from 10–30 kJ/m² to approximately 5–15 kJ/m². The heat deflection temperature under 1.8 MPa can increase by 10–20 °C, moving from 75–100 °C to 90–110 °C. If the grade is glass-filled, mold shrinkage becomes anisotropic; shrinkage parallel to flow is lower than transverse shrinkage by 0.1–0.3 %, and the use of round gates rather than film gates reduces warpage. The presence of glass also changes wear behavior: screw and barrel surfaces should be hardened or bimetallic, and check-ring clearance should be monitored for increased abrasive wear. Mixing with non-reinforced ABS regrind is acceptable only when the glass content is tightly controlled; variance above 2 wt% between lots can shift melt viscosity and mechanical properties beyond acceptable limits.
Electrical enclosures, appliance housings, and interior automotive trim produced from ABS 346A-8-G require dimensional stability after molding. Post-mold shrinkage for unfilled ABS is typically 0.4–0.8 %; parts should be measured after 24 h conditioning at 23 °C and 50 % relative humidity. For snap-fit features, strain at yield should remain below the material yield strain; unfilled ABS typically yields at 2.5–3.5 %. For living hinges, ABS is not recommended; polypropylene is preferred because repeated flexing above 2 Hz leads to stress whitening and fracture. The grade should not be processed in machines that previously ran PVC or acetal without purging; thermal decomposition residues from PVC evolve hydrogen chloride and degrade ABS at processing temperatures above 220 °C. On twin-screw compounding or re-extrusion lines, melt temperature control is critical because the residence time distribution can broaden if screw speed is increased without adjusting feed rate.
Electroplating of ABS requires a butadiene-rich surface etch stage in chromic acid. For ABS 346A-8-G, the etch quality depends on the butadiene particle size and distribution at the surface; unfilled ABS with butadiene content 10–20 wt% provides suitable etch morphology. If the -8-G suffix denotes glass reinforcement, electroplating becomes more difficult because glass fibers at the surface create non-etchable domains; in that case, electroplating should be limited to decorative plating with an initial electroless copper-nickel strike and extended etch time. Painting and adhesive bonding require surface wipe with isopropyl alcohol, followed by corona or plasma treatment to remove low-surface-energy contaminants. Adhesive bond strength depends on the adhesive system; unfilled ABS bonds with methyl ethyl ketone or cyanoacrylate, but stress-cracking can occur at bonded joints if residual molded-in stress exceeds 10 MPa. Annealing at 70–80 °C for 1–2 h reduces solvent-induced crazing. The use of amine-based adhesion promoters or epoxy hardeners with high amine content should be avoided because amine species can accelerate oxidative degradation of butadiene at elevated service temperatures above 85 °C.
High-flow ABS grades with melt volume-flow rates above 20 cm³/10 min are used for thin-wall parts below 1.2 mm. ABS 346A-8-G is expected to occupy a medium-flow window; if its melt volume-flow rate falls between 8 cm³/10 min and 18 cm³/10 min, it will fill 2–3 mm wall sections with lower injection pressure than a general-purpose grade while retaining more impact than a high-flow grade. Compared with PC/ABS blends, unfilled ABS has lower heat deflection temperature under 1.8 MPa, typically 75–100 °C versus 95–115 °C for PC/ABS, and lower tensile elongation at break, typically 10–50 % versus 50–100 %. However, ABS is less sensitive to moisture during processing and less prone to hydrolysis; PC/ABS requires drying below 0.02 % residual moisture, whereas ABS can tolerate 0.1 %. The density and material cost are also lower for ABS. If the -8-G suffix indicates glass reinforcement, the stiffness gap against PC/ABS narrows, but the ductility gap widens; glass-reinforced ABS typically exhibits lower tensile elongation at break than unfilled ABS, often below 10 %, and lower multiaxial impact performance.
Incoming resin and molded-part testing should follow the matrix in Table 1. The listed ranges are representative general-purpose ABS control limits, not grade-specific release limits. Actual lot data should be taken from the supplier certificate of analysis or determined by internal laboratory testing.
| Property or check | Standard | Test condition | Typical ABS control range |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 23 °C | 1.03–1.07 g/cm³ |
| Melt volume-flow rate | ISO 1133-1:2022 | 220 °C, 10 kg | 4–25 cm³/10 min |
| Tensile yield stress | ISO 527-2:2012 | Type 1A, 50 mm/min | 35–50 MPa |
| Flexural modulus | ISO 178:2019 | 2 mm/min | 1.8–2.5 GPa |
| Notched Charpy impact | ISO 179-1/1eA | 23 °C | 10–30 kJ/m² |
| Heat deflection temperature | ISO 75-2:2013 method A | 1.8 MPa | 75–100 °C |
| Vicat softening temperature | ISO 306:2022 method B50 | 50 N, 50 °C/h | 90–110 °C |
| Mold shrinkage | ISO 294-4:2018 | parallel/perpendicular | 0.4–0.8 % |
Operational boundaries are defined by moisture, melt temperature, and incompatible additives. The resin should not be melted above 265 °C in the presence of moisture because hydrolytic chain scission and butadiene oxidation accelerate. Mineral acids and strong oxidizing agents should be avoided in cleaning; purging with polypropylene or a dedicated ABS purging compound is preferred. If the grade is glass-reinforced, melt filtration with screens below 40 mesh should be avoided on extrusion lines because fiber accumulation increases pressure and can cause screen replacement interrupts. Published data for this specific configuration is limited; each lot should be sampled and tested for melt flow, impact, and filler content before release into a production line.