| HS Code | 292020 |
| Density | 1.19 g/cm³ |
| Melt Flow Rate | 10 g/10 min |
| Tensile Strength | 44 MPa |
| Flexural Modulus | 2300 MPa |
| Flexural Strength | 70 MPa |
| Notched Izod Impact Strength | 20 kJ/m² |
| Elongation At Break | 20% |
| Heat Deflection Temperature | 80 °C |
| Vicat Softening Temperature | 90 °C |
| Rockwell Hardness | 105 R-scale |
| Flammability Rating | UL94 V-0 |
| Molding Shrinkage | 0.4-0.7% |
As an accredited LG Chem ABS AT-553 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LG Chem ABS AT-553 is supplied in 25 kg moisture-resistant paper bags, typically 40 bags (1,000 kg) per pallet. |
| Container Loading (20′ FCL) | 20′ FCL loads approximately 17–18 MT of LG Chem ABS AT-553 in 25 kg bags, palletized and secured for export. |
| Shipping | LG Chem ABS AT-553 is a solid ABS resin supplied as pellets, typically in 25 kg bags or bulk octabins. It is not classified as dangerous goods for transport. Ship as general cargo in dry, ventilated conditions, avoiding moisture, excessive heat, and direct sunlight. |
| Storage | Store LG Chem ABS AT-553 in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and ignition sources. Keep original packaging sealed and palletized to prevent moisture pickup and contamination. Avoid prolonged exposure to high humidity and static buildup. Do not stack excessively; observe shelf-life and SDS recommendations. Use first-in, first-out. |
| Shelf Life | Shelf life is approximately 2 years when stored in a cool, dry, well-ventilated area, away from direct sunlight and moisture. |
Moisture uptake during pellet transfer from bulk railcar to machine-side hopper at ambient relative humidity above 60% is the first determinant of surface defect density in automotive lower interior trim parts molded from LG Chem ABS AT-553. Drying in a closed-loop desiccant dryer at 80°C for 3–4 h to a dew point below −20°C reduces pellet moisture below 0.05 wt% before plastication in a 20:1 L/D single-screw injection unit. Failure to reach this threshold produces splay, silver streaking, and gloss reduction on grained A-pillar trim surfaces even when barrel temperatures remain inside the 210–240°C melt window. The processing constraint in this application zone is not maximum tensile strength but the interaction between fast-flowing melt fronts and sudden wall-stock transitions from 1.5 mm to 3.0 mm in center console side cover designs. On production-scale multi-cavity tools equipped with valve-gated hot runners, thin-to-thick transitions require a two-stage injection profile: 75–85% of fill by volume at 120–180 mm/s screw forward velocity, then controlled deceleration to 30–50 mm/s before switchover to a holding pressure of 40–55 MPa. This profile limits jetting, rib-root sink depth, and surface flash along side-action shut-off lands. Mold temperature is held at 45–60°C through turbulent-flow water circuits, and cooling time for a 2.5 mm nominal wall is 25–35 s. Clamp force demand falls between 3.5 kN/cm² and 5.5 kN/cm² of projected area depending on runner balance and part surface area.
| Control parameter | Thin-wall below 1.2 mm | Structural 2.5–3.0 mm |
|---|---|---|
| Melt temperature | 230–240°C | 210–225°C |
| Mold temperature | 55–60°C | 45–50°C |
| Screw forward velocity | 150–250 mm/s | 80–120 mm/s |
| Holding pressure | 50–65 MPa | 40–55 MPa |
| Maximum pellet moisture at inlet | 0.05 wt% | 0.05 wt% |
Compliance for automotive interior trim using AT-553 is anchored to IATF 16949:2016 production part approval, OEM-specific interior emissions measurement under VDA 278:2016, and fogging assessment according to ISO 6452:2021. The resin is not supplied pre-certified for every cockpit zone; molders must verify VOC and fogging behavior on the finished decorated part because paint, mold-release residue, and regrind history influence thermodesorption results. Formulation-level addition ratios in commercial interior-trim work use 95–98 wt% virgin AT-553, 2–4 wt% pre-tested ABS-carrier color masterbatch, and up to 15 wt% clean plant regrind only after three consecutive production lots show notched Charpy retention above 85% of virgin value under ISO 179-1:2010. Downstream production is injection molding followed by surface preparation for waterborne primer and topcoat systems: the molded shell is wiped with 70% isopropanol-water solution, corona treated to 38–48 mN/m surface energy, and coated within 4 h to preserve adhesion. Terminal article types include lower instrument panel garnishes, center console side covers, glove box outer lids, and steering column upper and lower covers. Continuous service temperature in direct sunlight must remain below 80°C unless a heat-stabilization package is validated because unpainted ABS can exhibit surface-grazing and gloss loss above that boundary.
Wall stock below 1.2 mm in set-top box and network gateway enclosures forces the melt front through side-gated two-plate molds at screw forward velocities from 150 mm/s to 250 mm/s; the resulting shear heating raises local melt temperature by 5–15°C above barrel set point and can initiate surface ester burns if vent grooves are shallower than 0.02 mm or if clamp tonnage permits parting-line separation above 0.03 mm flash tolerance. Processing AT-553 in this regime uses barrel zones from 200°C at the feed throat to 230–235°C at the nozzle and a mold temperature of 50–55°C to restrict frozen-in orientation at the weld line behind pin-out openings. Weld-line strength retention is assessed by cutting a flow-path specimen from the molded housing at the boss and transverse rib and testing under ISO 527-2:2012 at 20 mm/min crosshead speed; successful lots maintain weld-line tensile strength no less than 65% of the unwelded bulk value when the moisture level in pellets has been held below 0.05 wt% before injection.
Compliance for ICT enclosures is maintained against IEC 62368-1:2023 for mechanically protective enclosures and against UL 94 at the relevant final wall thickness. This general-purpose ABS carries an HB classification; therefore circuit-bearing products with fire-enclosure duties specified at V-0 or V-1 must not substitute AT-553 unless an approved ignition barrier separates live conductors from the polymer surface. RoHS Directive 2011/65/EU Annex II and REACH Regulation (EC) No 1907/2006 Annex XVII restrict lead, cadmium, mercury, and short-chain chlorinated paraffins in the supplied pellet; the molder is responsible for verifying color masterbatch contribution through IEC 62321 analytical workflows. Formulation addition ratios in this segment are tightly constrained because masterbatch and regrind alter melt flow and dry-as-molded dimensions. Published production practice uses 97–99 wt% virgin AT-553, 1–3 wt% ABS-based colorant masterbatch, and 0–10 wt% regrind in black or dark gray parts. For white or pale high-gloss colors, regrind is excluded to prevent yellow shift and lot-to-lot Delta E drift above 1.5 CIELAB units under D65/10° illumination. Terminal downstream processing employs injection molding followed by ultrasonic welding of snap-fit bosses and adhesive bonding with polyurethane hot-melt; finished article types include set-top box housings, network router covers, smart home hub enclosures, and voice assistant shells. The operational boundary is that AT-553 is unsuitable in enclosures exposed to methoxypropanol-based cleaning agents or concentrated organic acids, because molded-in residual stress above 5 MPa can induce environmental stress cracking under polar solvent contact as evaluated by ASTM D543-21 immersion.
The governing injection parameter for large vacuum cleaner canister shells is not peak injection pressure but the post-filling switchover point and the cooling time needed to sustain dimensional accuracy across the rear axle bossing. In multi-cavity molds with two shells per shot, the hold profile for AT-553 is set to 45–60 MPa for 6–10 s, followed by a decay ramp of 12–18 MPa/s until gate freeze. Premature release before gate seal creates recovered strain in the form of sidewall sink and boss-hole ovality greater than 0.15 mm after 24 h at 23°C. Because the canister shell is later joined to a mating half by hot-plate or ultrasonic welding, dimensional mismatch above this threshold transfers directly to weld flash and burst-pressure scatter across the assembly line. Compliance for household vacuum appliances is anchored to IEC 60335-1:2020 Clause 30.2 for fire hazard under abnormal operation and to IEC 60335-2-2:2019 for particular requirements of vacuum cleaners and water-suction cleaning appliances. AT-553 is used in non-current-carrying outer shells and motor housing covers; the molder must confirm that the part is not classified as a live part or as a support for current-carrying components under the appliance standard.
Formulation addition ratios in this segment are 90–95 wt% virgin material with 5–10 wt% plant regrind processed through a closed-loop granulator, plus 2–3 wt% masterbatch selected to withstand extended residence time in hot-runner manifolds without thermal yellowing. Regrind above 10 wt% is not recommended for snap-fit hooks and rear axle bosses because notched Izod retention measured under ISO 180:2019 can fall below 80% of virgin value after three heat histories. Downstream production uses hot-runner injection molding with valve gates at 2.0–2.5 mm nominal wall, screw L/D 20:1, barrel temperature 210–230°C, mold temperature 50°C, and injection speed 80–150 mm/s. Terminal article types include canister shells, wand handles, floor-nozzle top covers, and robotic vacuum sensor windows where AT-553 is coated with a scratch-resistant UV lacquer after molding. Welding of the two shell halves is performed by hot-plate or ultrasonic methods; hot-plate welding parameters are 180–220°C plateau temperature with 0.3–0.6 mm melt displacement, producing burst pressures above the cleaned-filter back-pressure threshold in the assembled canister. If the mold is run with more than 10 wt% regrind, the production line records higher weld-line crack incidence at the rear axle boss, a failure mode observed only after repeated flex cycles on carpeted surfaces.
If the mold filling direction in a toy building block is gated at the underside wall, the primary dimensional risk is not warpage but shrinkage anisotropy across the undercut-bearing internal bore. AT-553 molded at 210–225°C melt temperature and 45°C mold temperature typically produces mold shrinkage of 0.4–0.7%; measured values can shift by 0.1–0.2% when a low-viscosity external lubricant masterbatch is substituted for a high-viscosity organic pigment masterbatch. To keep block-to-block engagement force within catalogue limits, molders pre-compensate the core and cavity dimensions using the supplier’s mold shrinkage range for the specific melt mass-flow rate measured under ISO 1133-1:2022 at 220°C and 10 kg. Running a multi-cavity stack mold with 4–16 cavities requires the sprue, runner, and gate balance to be verified by short-shot progression; fill imbalance above 5% by weight across cavities creates cavity pressure differences that alter engagement dimensions beyond the allowed tolerance. Drying follows the same 80°C for 2–3 h desiccant regimen; the granulate is not processed above 240°C because thermal degradation of the elastomeric phase reduces low-temperature drop ductility.
Compliance for toy components in the European Union and North America is governed by EN 71-3:2019+A1:2021 for migration of elements and by ASTM F963-23 for extractable heavy metals and mechanical hazards. The pellet itself is not a finished toy; finished product certification requires first-party or third-party testing of the molded article, including surface coating if applied, against the relevant migration limits for lead, cadmium, chromium VI, and mercury. Formulation addition ratio in toy applications is usually 96–99 wt% virgin AT-553 with 1–4 wt% pigment masterbatch from a supplier that provides a heavy-metal declaration. Regrind is avoided unless the molder can demonstrate batch traceability and unchanged migration results because cross-contamination in the granulator is difficult to audit after multiple color changes. Terminal production routes are conventional injection molding followed by dimension-sorting with automated gauges; finished product types include ABS construction blocks, attachable toy figure parts, and structural chassis for educational robotics kits. The operational limitation is that AT-553 retains ductility at household temperatures but becomes noticeably stiffer below −10°C; impact-dependent toy designs intended for outdoor winter conditions must be impact-tested at the lowest intended use temperature rather than at 23°C alone. Exposure to flame-retardant additive packages without recertification is not permitted because halogenated FR additives can alter the elemental migration profile and may fall outside the extractable limits of EN 71-3 and ASTM F963-23.
| Standard or method | Test endpoint | Applicability boundary |
|---|---|---|
| EN 71-3:2019+A1:2021 | Element migration from article surfaces | Finished toy component after molding, coating, and assembly |
| ASTM F963-23 | Extractable heavy metal and mechanical hazard | Articles sold in North America; final article certification belongs to the brand owner |
| ISO 1133-1:2022 | Melt mass-flow rate | Incoming pellet lot release; not a toy compliance test |
| REACH 1907/2006 Annex XVII | Phthalates and restricted substances | Pellet and molded article; enforcement by importer under Article 51 |
Large-format printer side covers and paper-path housings maintain flatness through the use of multiple gate drops and a fill-balanced runner system. AT-553 at 230°C melt temperature in a 2.5 mm wall exhibits out-of-plane deformation of 0.6–1.0 mm across a 300 mm span when cooling-water temperature varies by more than 5°C between cavity circuits. Injection process windows therefore specify mold temperature uniformity of ±3°C and coolant inlet pressure sufficient for turbulent Reynolds number above 10,000 in conformal channels. The amorphous shrinkage behavior of ABS provides a wider flatness window than partially crystalline olefins, but the large projected area of printer side panels still requires clamping force from 4 kN/cm² to 6 kN/cm² and core-cooling circuits zoned to remove heat at the gate region before part ejection. Prototype trials on a 900 t toggle-clamp injection machine have shown that reducing mold temperature difference between the gate-adjacent cavity and the farthest edge to less than 3°C lowers post-eject warpage by 0.2–0.4 mm relative to unbalanced cooling configurations.
Compliance for printer housings is based on IEC 62368-1:2023 for business equipment with energy source protection and on UL 94 HB at final wall thickness. Laser printer fuser sections above 180°C must be separated from AT-553 housings by distance or insulation because the polymer’s deflection temperature under 1.8 MPa is below the fuser surface temperature. Formulation addition ratios common in printer housing molding are 95–98 wt% virgin resin, 2–4 wt% color masterbatch, and up to 20 wt% internally recycled regrind when the closed-loop granulator is not cross-contaminated with paper dust, silicone oil, or polyester label waste. Surface preparation for painting uses manual wipe with 70% isopropanol-water solution followed by adhesion-promoting primer; bulk painting with two-component polyurethane topcoat achieves cross-hatch adhesion classification 0–1 according to ISO 2409:2020 only when the molded surface is pre-cleaned within 4 h before paint and the paint-film thickness is controlled at 15–25 µm dry.
Secondary joining of boss supports and hinge supports is performed with cyanoacrylate adhesives of 50–100 cP viscosity; fixture time at 40–60% relative humidity is 20–40 s, though bond orientation is critical because cyanoacrylate forms brittle fillets that propagate under repeated paper-tray closure impacts. Terminal article types include desktop printer housings, multi-function printer side panels, paper cassette trays, and scanner lid frames. Electrical connectors and solenoid mounts are not overmolded into AT-553 without a thermal-isolation insert because the heat generated by continuous paper-path motors can soften the boss area if local temperature exceeds 70°C for more than 2 h. The operational limitation is stress-cracking under ketone-based maintenance cleaners; methyl ethyl ketone or acetone used for roller maintenance lowers craze initiation stress below 2 MPa within minutes of exposure, requiring shielding or replacement with chemically resistant materials at service points where these solvents are applied.
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For injection-moulding programmes that require an unfilled acrylonitrile-butadiene-styrene resin with a verified flow path for medium-flow tooling, LG Chem ABS AT-553 is specified as a pelletised virgin feedstock. The polymer architecture consists of a continuous styrene-acrylonitrile matrix and discrete polybutadiene rubber domains; the graft density and rubber particle size distribution determine low-temperature notched Izod response, melt elasticity, and grained-surface appearance. A current manufacturer technical datasheet should be used for design allowables, but typical published ranges for this unfilled ABS family place melt mass-flow rate under ASTM D1238 at 220 °C/10 kg in the 10–25 g/10 min band, density by ASTM D792 in the 1.04–1.06 g/cm³ range, tensile yield strength by ASTM D638-14 in the 40–48 MPa range, flexural modulus by ASTM D790-17 in the 2.0–2.5 GPa range, and notched Izod impact at 23 °C in the 20–35 kJ/m² range when tested under ISO 180/A. Actual lot certificates of analysis control shipment values because rubber content and molecular weight can shift within published specification limits.
The intended processing route is injection moulding. Applications specified in supplier literature include interior trim components, appliance housings, console side panels, and general-duty enclosures. The resin is not a direct replacement for polycarbonate/ABS blends where higher heat deflection is required; for such cases a heat-resistant grade such as LG Chem ER-461 or a PC/ABS alloy should be compared under the same load and geometry. Compared with glass-filled or flame-retardant ABS, AT-553 exhibits larger mould shrinkage because no rigid filler constrains the PVT response; published mould shrinkage by ASTM D955 for unfilled ABS generally falls in the 0.4–0.7 % range, with flow-direction and cross-flow anisotropy dependent on gate location, packing pressure, and hold time.
Moisture in ABS feedstock is not a hydrolytic degradation risk in the same way as polyamide or PET, but residual surface moisture and absorbed water vapour are the dominant cause of splay, silver streaks, and inconsistent melt cushion in hot-runner tools. Above 60 % ambient relative humidity or after 8 h of open storage, pre-drying is required. Desiccant-wheel dryers with a dew point of ≤ -40 °C and a closed-loop hopper supply are the accepted production configuration. Drying at 80–90 °C for 2–4 h reduces residual moisture below 0.1 %; for critical foam-free surfaces a target of 0.05 % is sometimes specified. Moisture analysis may be performed by ISO 15512:2019. A water-cooled feed throat at 40–70 °C prevents pellet clumping but must not generate condensation; the bypass of wet air into the screw flights is a known source of intermittent gate blush.
On production machinery, moisture-related rejection commonly appears first near the gate land because the pressure drop across the restricted gate reduces local vapour bubble solubility and produces a visible fan-shaped splay pattern on polished or grained surfaces. The defect is often misdiagnosed as shear burning or mould condensation. A process response that raises barrel temperature to clear splay may worsen the defect by increasing melt temperature and accelerating volatilisation; the correct corrective action is to verify dryer dew point, hopper residence, and conveying air moisture before changing the temperature profile.
| Parameter | Range / set-point | Control note |
|---|---|---|
| Dryer dew point | ≤ -40 °C | Desiccant wheel with closed-loop hopper |
| Drying temperature | 80–90 °C | Continuous drying, not static oven trays |
| Drying time | 2–4 h | Extend by 2 h if cold-storage condensation is present |
| Residual moisture | < 0.1 % | 0.05 % target for high-gloss surfaces |
| Barrel temperature profile | 200–240 °C | Flat-to-reverse profile if screw recovery is short |
| Nozzle temperature | 210–240 °C | Nozzle tip must not freeze on sprue break |
| Mould surface temperature | 30–60 °C | Higher within range for grained surfaces |
| Screw surface speed | 0.2–0.8 m/s | Screw surface speed above 0.8 m/s accelerates butadiene oxidation |
| Back pressure | 0.5–1.5 MPa | Use lower end for large shot weights |
| Cushion | 2–5 mm | Stable cushion avoids hold-pressure fluctuation |
| Maximum melt residence time | 5 min | Reduce to 3 min above 240 °C |
At melt temperatures above 240 °C, the butadiene phase in high-impact ABS begins to crosslink and oxidise; this shifts the melt from yellow to tan and reduces notched Izod impact. A maximum melt residence time of 5 min is applied on conventional reciprocating-screw injection machines. On shutdown or short-cycle interruptions, the barrel is purged with a styrene-based purging compound and the temperature set-point is reduced to 180–200 °C. Hot-runner manifolds should not be held at 250 °C or above with no resin flow for longer than 15 min, depending on drop configuration, because stagnant melt in the gate tip oxidises even if the screw is retracted. Published data for AT-553 under specific hot-runner geometries is limited, so thermal degradation thresholds should be confirmed by melt-flow shift and yellowness index measurements on retained samples.
A single-point melt mass-flow rate under ASTM D1238 or ISO 1133-1:2022 does not capture the shear-thinning behaviour that controls pressure-limited filling. Capillary rheometry according to ISO 11443 provides apparent viscosity data across shear rates of 10²–10⁴ s⁻¹ and temperatures of 220–240 °C. The viscosity curve for unfilled ABS displays pronounced non-Newtonian behaviour; at low shear, melt elasticity and rubber-particle interactions raise pressure drop through hot drops, while at high shear the viscosity approaches the SAN matrix value. For thin-wall sections below 1.5 mm, the available flow length is determined more by solidification at the frozen layer than by barrel MFR. Mould-filling simulation should use pvT data and Cross-WLF coefficients for the specific grade rather than generic ABS defaults; otherwise the predicted gate pressure can deviate by more than 15 % in long flow paths.
Gate diameter and land length are set to maintain shear rate below the critical value for visible burn marks; for unreinforced ABS, gate shear rates above 1 × 10⁵ s⁻¹ produce excessive melt fracture and gate blush. Sub-gates and tunnel gates should have an included angle of 20°–30° and a land length of 0.8–1.2 mm. In hot-runner needle-valve systems, the valve pin speed is reduced until the pressure spike at gate opening stays below 5 MPa; this minimises local shear heating and prevents premature gate freeze. Mould steel selection for grained surfaces should anticipate that ABS deposits volatiles on polished cores; hard-chromium plating or corrosion-resistant tool steel reduces cleaning cycle time.
When the component is painted or adhesively bonded, the adhesion system must be screened with the actual mould release and antistatic package used on the line. Aromatic hydrocarbons, ketones, and esters can act as stress-cracking agents on ABS, especially at knit lines and injection-moulded bosses. ISO 22088-2 provides a ball-impression method for environmental stress-crack resistance. Trials that omit the production ejector grease or the customer’s alcohol-based cleaner may be invalid because surface contamination lowers paint crosslinking density and permits migration of low-molecular-weight processing aids to the interface. Mechanical interlock and surface polarity are not uniformly controlled across grained tools; a consistent texture depth of 25–40 µm is sometimes specified for painted interior trim to avoid visible gloss differentials after topcoat application.
Within the LG Chem ABS range, the AT-series is positioned for automotive and aesthetic interior applications where a controlled balance of flow, impact, and surface appearance is specified; published data for direct quantitative comparison between AT-553 and HI-121H is limited to current datasheets, and lot-specific values should not be transferred between grades. A general-purpose grade such as HI-121H may exhibit different low-temperature impact because the rubber particle size distribution is adapted to deep-draw and high-toughness housings. A high-flow grade such as HI-100 may fill thinner flow paths but may trade away notched impact. Heat-resistant grades such as ER-461 shift deflection temperatures upward; this is a different design solution than simply raising the mould temperature for AT-553, because heat deflection temperature is a material property and not a processing variable. The choice between AT-553 and a PC/ABS blend should be based on ASTM D648-18 values, not on supplier literature descriptions alone.
The unfilled nature of AT-553 means that mould shrinkage and coefficient of linear thermal expansion are higher than those of glass-filled ABS. A tool designed for 20 % glass-filled ABS cannot be assumed to produce dimensionally stable parts with AT-553; shrinkage differences greater than 0.2 % are possible. Tolerances for snap-fit beams and cantilever hooks should be validated with process-capability runs at the lower and upper melt temperature and hold-pressure limits, not at a single mid-range set-up.
Virgin AT-553 can be blended with clean sprues and runners; however, the regrind fraction changes melt elasticity, lowers the effective melt flow rate if the regrind is heat-historied, and raises the risk of black specks from degraded butadiene. For low-gloss grained surfaces, regrind addition above 30 % can alter grain definition and produce micro-pitting because the regrind particles carry oxidised surface residues. Granulator screens should reject fines smaller than 0.5 mm. Regrind that has been stored in open gaylord boxes must be re-dried to 0.1 % moisture before blending. Glass-filled or flame-retardant ABS regrind must never be mixed with AT-553; the resulting blend shifts weld-line strength and the unfilled UL 94 HB classification can no longer be assumed.
The list below consolidates the standard test methods used to verify unfilled ABS injection-moulding grades. Compliance statements for REACH, RoHS, and other regulatory regimes require a current supplier statement; class membership under UL 94 for unfilled ABS is generally HB, not V-0. No flame-retardant additive is present in standard AT-553 unless explicitly purchased as a specialty variant. Food-contact suitability is not automatic; a grade-specific letter of assurance under 21 CFR 177.1020 or equivalent regional migration testing is required before food-contact use.
| Property | Primary standard | Alternative/ISO equivalent | Verification note |
|---|---|---|---|
| Density | ASTM D792-20 | ISO 1183-1:2019 | Report to three decimal places |
| Melt mass-flow rate | ASTM D1238-20 | ISO 1133-1:2022 | 220 °C / 10 kg |
| Tensile properties | ASTM D638-14 | ISO 527-2 | Type I specimen or ISO multipurpose specimen |
| Flexural modulus | ASTM D790-17 | ISO 178 | Three-point loading, 2 mm/min |
| Notched Izod impact | ASTM D256-10e1 | ISO 180/A | Condition at 23 °C and -30 °C if low-temperature ductility is specified |
| Heat deflection temperature | ASTM D648-18 | ISO 75-2 | Report load: 0.45 MPa or 1.82 MPa |
| Vicat softening temperature | ASTM D1525-17 | ISO 306 | Method A or B must be stated |
| Mould shrinkage | ASTM D955-08 | ISO 294-4 | Report flow and cross-flow values |
| Flammability | UL 94 | IEC 60695-11-10 | Unfilled ABS typically HB; V-0 requires flame retardant |
For electroplating or adhesion-modified applications, the specific grade variant must be verified; standard AT-553 is not a plating grade and may require an additional adhesion treatment. Direct substitution into an established plating line without surface modification trials is not recommended because the rubber particle size distribution at the surface affects etchability and metal adhesion.