| HS Code | 936904 |
| Density | 1.04 g/cm³ |
| Melt Flow Rate 220c 10kg | 20 g/10 min |
| Tensile Strength | 44 MPa |
| Tensile Elongation | 25% |
| Flexural Strength | 73 MPa |
| Flexural Modulus | 2300 MPa |
| Notched Izod Impact Strength 23c | 18 kg·cm/cm |
| Heat Deflection Temperature 1 82mpa | 88 °C |
| Vicat Softening Point | 103 °C |
| Rockwell Hardness | R105 |
| Mold Shrinkage | 0.4-0.7% |
| Flammability Ul94 | HB |
As an accredited Formosa Chemicals & Fibre (FCFC) ABS AN4500 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | FCFC ABS AN4500 is packaged in 25 kg moisture-resistant paper bags, typically palletized for safe transport and storage. |
| Container Loading (20′ FCL) | Formosa Chemicals & Fibre ABS AN4500 is packed in 25 kg bags and loaded into a 20′ FCL container for sea shipment. |
| Shipping | Formosa Chemicals & Fibre (FCFC) ABS AN4500 is a non-hazardous thermoplastic resin supplied as pellets, typically packed in 25 kg bags or 1,000 kg jumbo bags, palletized and shipped in dry containers. Store dry, away from direct sunlight and heat; not regulated for transport. |
| Storage | Store FCFC ABS AN4500 in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and ignition sources. Keep containers tightly closed and avoid dust generation or static buildup. Separate from oxidizers and incompatible chemicals. Use proper grounding and PPE; maintain good housekeeping. Under these conditions, the resin is stable and retains its properties. |
| Shelf Life | Typically 12 months from manufacture when stored sealed in a cool, dry, ventilated area away from direct sunlight. |
In thin-wall injection molding of Formosa Chemicals & Fibre ABS AN4500 enclosure bases for DIN-rail power supplies and relay modules, the process window is governed by flow-length-to-wall-thickness ratio, melt temperature, and mold-filling pressure. The compound is dried to a residual moisture content below 0.1% by weight using a desiccant dryer with a dew point of -30°C or lower; drying at 80°C for 2 h to 4 h is typical for high-flow ABS grades of this class, although the exact AN4500 melt mass-flow rate and drying conditions should be confirmed against the supplier certificate. Melt temperature set points between 220°C and 250°C are selected, with the lower end preferred for longer residence times and the upper end reserved for sections below 1.5 mm. The melt mass-flow rate is reported by the supplier under ISO 1133-1:2022 or ASTM D1238-20; cross-grade comparisons require identical temperature and load because shear history changes flow classification. At a wall thickness of 1.0 mm to 1.5 mm, a switchover to packing pressure at 95% to 98% of peak injection pressure reduces flash and short-shot variation. Mold-filling pressure is commonly observed in the range of 600 bar to 1,200 bar for cold runner systems, which translates into clamp force requirements of approximately 3 kN/cm² to 5 kN/cm² of projected area for parts with flow-length-to-wall-thickness ratios above 150:1. Gate land length should be kept between 0.8 mm and 1.2 mm, and gate diameter for subgates may be set at 0.8 mm to 1.5 mm depending on part mass; undersized gates cause shear-induced degradation of the polybutadiene phase, visible as silver streaks radiating from the gate. The mold temperature is maintained at 40°C to 70°C; below 40°C, weld lines in bosses and snap-fit features lose tensile strength, while above 70°C, cycle time increases without proportional gloss improvement. Dimensional stability is assessed according to ISO 294-4, and tensile properties are verified by ISO 527-2/1A at 23°C; notched Charpy impact is measured to ISO 179-1/1eA. For electrical housings, the relevant flammability assessment is UL 94 HB at specified minimum thickness; the glow wire ignition temperature may be tested under IEC 60695-2-11, and comparative tracking index may be reported under IEC 60112. Production constraints include the presence of knit lines at openings for vents and connector cutouts; moving the gate location or using sequential valve gates reduces visible flow marks but increases hot-runner cost. The end products in this segment include DIN-rail power supply housings, relay module covers, terminal box bases, and junction enclosures installed indoors. Outdoor use is not recommended without UV stabilization or opaque pigmentation confirmed by Xenon arc weathering to ISO 4892-2; published data for AN4500 in long-term outdoor exposure is limited.
Electroplated ABS exterior and interior trim components demand a molded-in low-stress skin, controlled butadiene phase distribution, and etch conditions matched to the grade’s rubber particle content. The etching bath is typically a mixed chromic acid–sulfuric acid solution held at 60°C to 70°C; immersion time is set between 300 s and 900 s depending on butadiene domain size and molded-in stress level. The acid bath removes a fraction of the polybutadiene particles from the surface, producing microcavities with diameters in the order of 1 μm to 5 μm. After neutralization, catalyst activation and autocatalytic electroless nickel or copper deposition produce the conductive layer required for subsequent copper, nickel, and chromium electroplating. Adhesion is not a single paint-like bond but mechanical interlocking, so melt-speed lines, knit lines, and high shear at the gate reduce peel strength. Molded parts should be annealed at 60°C to 75°C for 1 h to 2 h before etching if hot-runner gate vestiges or thick-to-thin transitions create internal stress. Plate adhesion is evaluated by peel testing in accordance with ASTM B533 using a 25 mm-wide strip pulled at 180°; specification values are set by the OEM, and published data for AN4500 in electroplating configuration is limited. Thermal cycling of plated parts is controlled by OEM test standards rather than ISO methods, commonly alternating between -30°C and 80°C with dwell times of 30 min to 60 min. Failure modes include blister formation near gate locations, cracking at sharp radii below 0.5 mm, and adhesion loss after copper-accelerated acetic acid salt spray or neutral salt spray exposure. End products include grille bars, radiator grille surrounds, side mirror housings, door handle bezels, and wheel cover inserts; each requires plate distribution that tolerates thermal expansion mismatch between the chromium top layer and the ABS substrate. The processing boundary is set by impact retention after electroplating: if the molded part contains high levels of frozen-in orientation, the ductile-to-brittle transition shifts to higher temperature, and the plated article becomes sensitive to low-speed impact at 0°C and below.
In cut-sheet thermoforming, gauge variation in extruded ABS sheet is the dominant cause of sag and wall thickness nonuniformity; the extrusion line therefore requires a barrier screw with an L/D ratio of 30:1 to 36:1, a gear pump for stable output, and a flex-lip sheet die with a restrictor bar to control transverse gauge variation. Melt temperature is maintained between 230°C and 250°C at the die entry; resin drying before extrusion follows the same desiccant parameters as injection molding, with residual moisture below 0.1% and dryer dew point below -30°C. Roll stack temperatures are set asymmetrically, with the upper roll at 70°C to 90°C and the lower roll at 80°C to 100°C, depending on surface gloss and sheet thickness. Gauge variation across the web is held within ±0.05 mm for sheet of 1 mm to 4 mm thickness; deviations beyond this range produce sag in the heating tunnel of a cut-sheet thermoforming line. The heating tunnel temperature is set at 180°C to 220°C for ABS sheet; actual core sheet temperature at forming should be 130°C to 160°C. Below 130°C, forming pressure increases and corner thinning intensifies; above 160°C, sheet sag causes non-uniform wall thickness and potential melt fracture at plug assist contact. Plug-assisted thermoforming with syntactic foam or acetal plug is used only when draw ratios exceed 1.5:1; the plug temperature is kept below 90°C to avoid premature chilling or surface blemishes. Regrind addition is permitted up to 20 wt% to 30 wt% in sheet coextruded without a cap layer; beyond this level, die lines and notched impact loss become measurable by ISO 179-1. End products include luggage shells, equipment housing covers, interior door panels, thermal-formed automotive components, and point-of-purchase display bases. Flammability of extruded sheet is assessed by UL 94 HB at the nominal sheet thickness, but where thermoformed parts are used in unattended appliances, glow wire and ball pressure requirements under IEC 60335-1 take precedence.
For creepage clearance assessment in low-voltage enclosures molded from AN4500, dimensional stability after heat aging and defined creepage clearances under IEC 60664-1 are more critical than tensile failure. For pollution degree 2 applications, creepage distances are determined by working voltage and the material’s comparative tracking index. General-purpose ABS grades in this class may be assigned to material group IIIa or IIIb depending on CTI value; the exact AN4500 CTI must be read from the supplier certificate rather than assumed from generic ABS data. The minimum creepage distance for a 250 V working voltage at pollution degree 2, material group IIIb, is 2.5 mm; for reinforced insulation requirements, the distance increases according to the tables in IEC 60664-1. Internal bosses and snap-fit mounts must not reduce creepage through a wall section; when a boss wall thickness falls below 1.2 mm, filler loading is not an option, and the design should add a barrier rib or extend surface distance. Heat aging is often specified at 85°C for 168 h to 1000 h, followed by visual inspection for cracking, color shift, and deformation according to IEC 60068-2-2, test Bb. The following table identifies the compliance matrix applied to such enclosure parts:
| Standard | Clause / method | Property assessed | Application relevance |
|---|---|---|---|
| IEC 60664-1 | Clause 4.2 and 5.2 | Creepage and clearance distances | Spacing on live parts |
| IEC 60112 | Full test | Comparative tracking index | Material group classification |
| IEC 60695-2-11 | Glow wire 650°C to 960°C | Ignition temperature | Unattended appliance parts |
| IEC 60243-1 | Short-time breakdown | Dielectric strength | Insulation barrier integrity |
| UL 94 | HB minimum thickness | Horizontal burning rate | Enclosure fire classification |
End products include low-voltage distribution board covers, residual-current device bases, miniature circuit breaker housings, and metering enclosures. Continuous indoor service above 85°C or proximity to uninsulated live parts requires additional high-temperature aging and glow wire verification beyond the baseline UL 94 HB rating.
Replacement of flame-retardant PC/ABS with AN4500-class high-flow ABS is considered only in small appliance housings where the maximum continuous surface temperature remains below 85°C and the fire classification permits HB materials. The injection mold requires an SPI A1 or A2 high-gloss finish, with mold temperature maintained at 60°C to 80°C to replicate polish; below 60°C, the high-flow melt may freeze too rapidly, producing sink marks opposite ribs and bosses. Melt temperature is set at 230°C to 250°C; excessive melt temperature above 260°C causes yellowing and polybutadiene degradation, which lowers Izod impact measured by ISO 180/A and creates gas burns. Packing pressure is held at 60% to 80% of peak injection pressure for 3 s to 6 s after switchover, depending on gate freeze time. Venting insert sets or vacuum boxes are recommended on the clamp side for gloss surfaces; poor venting burns polybutadiene and leaves black specks. The material’s heat deflection temperature is measured by ISO 75-2/Ae or ASTM D648 at 1.82 MPa; if the housing is tested to IEC 60335-1 clause 30.2 for glow wire, the relevant test is performed on the final wall thickness and color. End products include vacuum cleaner canister shells, benchtop tool housings, hair dryer outer shells, and non-food appliance covers. This replacement is not recommended for parts adjacent to heating elements, reflectors, or within 10 mm of uninsulated live parts unless the specific regulatory test is passed. Part weight reduction of 10% to 20% compared with filled FR PC/ABS may be achieved only if rib and boss thicknesses are redesigned; high-flow ABS has lower modulus and creep resistance, so load-bearing snap arms require finite element verification under creep load.
Where solvent-borne topcoats are applied to ABS interior pillar covers and speaker grille surrounds, the risk of environmental stress cracking from ester and aromatic ketone solvents must be controlled by coating selection and baking temperature. The substrate surface energy after cleaning is commonly in the range of 34 mN/m to 42 mN/m; waterborne acrylic topcoats or UV-cured coatings are preferred over aggressive solvent-borne systems. If solvent-borne coatings are unavoidable, compatibility testing should involve surface exposure of an annealed part to the specific solvent blend for 24 h to 72 h, followed by tensile property retention per ISO 527-2 or chemical resistance evaluation per ASTM D543. Bake temperature is limited to 70°C to 80°C for 20 min to 30 min; higher temperatures may exceed heat deflection temperature and cause edge curl or clip deformation. Adhesion is checked by cross-cut test to ISO 2409, with no more than 5% removal in typical interior specifications. Fogging is assessed by DIN 75201 or VDA 278; ABS grades with high residual oils or low molecular weight fractions must show appropriate FOG values from the supplier. Knit lines at the perimeter of grille openings or snap-fit features remain visible after painting unless the mold is gated centrally or the part is textured above 10 μm Ra. End products include painted A-pillar covers, B-pillar trims, speaker grille frames, and console side panels. Parts with long-term UV exposure through glazing require accelerated weathering by ISO 105-B06 or SAE J2412, but published data for AN4500 in painted interior UV ageing is limited; color matching and topcoat durability are controlled by the painting line, not by neat resin data.
AN4500-class ABS may be converted into monofilament for fused filament fabrication when the extrusion line is equipped with a gear pump and closed-loop diameter sensing at 5 Hz to 20 Hz. The resin is dried to 0.1% moisture and extruded at 220°C to 240°C, with melt temperature variation limited to ±2°C to reduce viscosity drift at the die lip. Water quenching is set at 40°C to 60°C, and two-stage cooling with a tubular calibration sleeve controls ovality. Filament diameter is maintained within ±0.05 mm for 1.75 mm filament and ±0.08 mm for 2.85 mm filament, measured by dual-axis laser gauging. If regrind or dried material residence time exceeds 30 min at temperature, molecular degradation shifts melt viscosity and creates filament diameter fluctuations that appear as print under-extrusion. Published data for AN4500 in filament-grade configuration is limited; the processor should validate melt flow-rate stability after repeated extrusion through ISO 1133-1. End products include 1.75 mm and 2.85 mm ABS filament spools for fused filament fabrication printers.
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FCFC ABS AN4500 is a pelletized acrylonitrile-butadiene-styrene injection moulding grade supplied by Formosa Chemicals & Fibre Corporation. The resin is a two-phase styrenic terpolymer: a continuous styrene-acrylonitrile copolymer matrix surrounds a dispersed polybutadiene rubber phase. The manufacturer controls the SAN matrix molecular weight, the butadiene content, the rubber grafting ratio, and the rubber particle-size distribution to obtain a controlled flow–impact balance. The numerical suffix AN4500 is a product-series identifier; it is not a measured property value. The melt-mass-flow rate must be verified on the lot certificate using ISO 1133-1:2022 at the load and temperature condition stated in the manufacturer’s technical datasheet. ABS melts are shear-thinning, and a value obtained at 220 °C with 10 kg is not directly comparable with a value obtained at 220 °C with 5 kg. AN4500 is generally positioned for injection moulding of moderate-to-thin-wall parts. It is not routinely recommended for extrusion or blow moulding unless the manufacturer has confirmed melt strength and draw-down stability for the specific die geometry.
Pre-drying should be performed in a desiccant dryer supplying air with a dew point no higher than −40 °C. ABS grades in this polymerization family commonly tolerate drying at 80 °C to 90 °C for 2 h to 4 h, with residual moisture held below 0.05%. Drying above 95 °C for extended residence can induce oxidative yellowing of the SAN phase and reduce notched impact energy. Moisture analysis should use Karl Fischer titration or a temperature-controlled moisture analyzer with resolution to 0.001%. If a gravimetric moisture balance is used, the sample should be heated to 160 °C for 10 min under a controlled flow of dry nitrogen and the result correlated against Karl Fischer. Incoming lots with moisture above 0.05% should be re-dried before processing. If the material has been exposed to ambient air for more than 8 h, a drying cycle should be repeated because ABS regains moisture quickly in humid conditions. The dried granulate should not remain in an open feed throat for more than 30 min when ambient relative humidity exceeds 60%; a closed hopper fed with dried air is preferred. Hydrolytic splay, silver streaking, and loss of low-temperature ductility are typical consequences of residual moisture in the melt.
The first measurable shift during a grade substitution is usually cavity filling balance. If AN4500 has a higher melt-mass-flow rate than the incumbent medium-flow ABS, the pressure drop through the sprue, runner, and gate decreases, but the melt may reach the end of the cavity before the packing phase establishes sufficient pressure. Injection moulding machines used for such trials should have a hydraulic or electric injection unit capable of maintaining injection velocity without severe overshoot at short stroke. A screw with 20:1 to 24:1 length-to-diameter ratio and a compression ratio between 2.0:1 and 2.5:1 is typical for ABS. Flow analysis should use AN4500-specific pvT data generated by the material supplier rather than generic ABS data, because the pressure–volume–temperature response near the glass transition changes with rubber level. Published data for AN4500-specific pvT coefficients in open literature is limited; a sensitivity analysis should therefore be completed before committing production tooling. When cavity pressure transducers are installed, the gate-seal time may be observed by monitoring pressure decay near the gate. A high-flow grade can exhibit earlier or later gate freeze depending on thermal conductivity and solidification range, so the holding-time window cannot be transferred from another grade without direct measurement.
Melt-mass-flow rate values are frequently compared between laboratories, loads, and melt temperatures, but the comparison is only valid when the same standard condition is used. For AN4500, the certificate of analysis should state the exact extrusion plastometer condition. A higher reported value at 220 °C and 10 kg correlates with easier filling in thin sections, but it does not directly predict in-mold viscosity at injection shear rates above 1,000 s⁻¹. A capillary rheometer evaluation at 220 °C, 230 °C, and 240 °C across shear rates from 100 s⁻¹ to 10,000 s⁻¹ is needed to compare AN4500 against another ABS for moulding. The Bagley correction and Rabinowitsch correction must be applied to obtain true shear viscosity; apparent viscosity values alone overstate wall viscosity. Flow-length data from spiral-mould testing should not be used as a substitute for finite-element filling simulation. A controlled spiral-flow test for ABS might use a channel depth of 2 mm, a width of 5 mm, a melt temperature of 230 °C, a mould temperature of 60 °C, and a peak injection pressure of 100 MPa. Spiral-flow length is a comparative value, not an absolute design parameter. The following incoming-lot verification matrix identifies the minimum test methods and reporting conditions; actual specification limits must be supplied by the manufacturer.
| Property | Test Method | Condition to Verify | Comment |
|---|---|---|---|
| Melt-mass-flow rate | ISO 1133-1:2022 | 220 °C, 10 kg | Do not substitute 200 °C/5 kg results |
| Density | ISO 1183-1:2019 | 23 °C | Use for shot mass and cushion calculation |
| Tensile stress at yield | ISO 527-2:2012 | 50 mm/min, 23 °C | Report specimen type if not 1A |
| Notched Izod impact | ISO 180/1A:2019 | 23 °C, −30 °C | Verify notch radius and conditioning time |
| Vicat softening temperature | ISO 306:2022 | Method B50 or A50 | Compare only within the same method |
| Heat deflection temperature | ISO 75-2:2020 | 1.8 MPa or 0.45 MPa | Not a continuous-use temperature rating |
| Flammability | UL 94 | Sample thickness 1.5 mm or 3.0 mm | Colourants and regrind may alter rating |
If the OEM drawing requires a minimum notched Izod impact energy at −30 °C, a high-flow ABS may not achieve the same low-temperature ductility as a medium-impact grade because a lower entangled SAN matrix and possible lower rubber content reduce energy absorption. The comparison should be performed with ISO 180/1A:2019 Type 1A specimens conditioned at 23 °C and 50% RH, not on dry-as-moulded specimens. Weld-line strength in multi-gate parts can be more sensitive for high-flow ABS because the melt front skin is colder and interdiffusion at the knit line is reduced. A double-gate tensile bar moulded and tested to ISO 527-2:2012 should be used to compare the weld-line failure stress with a single-gate control. Chemical stress-cracking resistance in contact with oil, grease, or adhesive is not determined solely by flow grade; however, higher free volume in a high-flow SAN phase may lower barrier properties and shorten time to craze under constant strain. Testing should follow ISO 22088-2:2006 or an automotive OEM equivalent with defined strain and chemical exposure. The stabilizer package and rubber content of AN4500 should be confirmed from the supplier’s datasheet; open literature for this exact configuration is limited.
Production experience with high-flow ABS in electronic housings indicates that the dominant process defects are jetting, weld-line visibility, and gloss differential near the gate. Injection velocity in the range of 100 mm/s to 250 mm/s may be used only if the tool has adequate venting and the gate cross-section is sufficiently large; smaller gates can require lower velocity to avoid jetting. Mould temperature between 40 °C and 80 °C is typical for ABS, with higher values within that range generally improving gloss and knit-line strength at the expense of cycle time. Published data for AN4500-specific mould-temperature optimization is limited; a design-of-experiments on the actual tool is required. In thin-wall electronic bezels with nominal wall thickness of 1.2 mm to 2.0 mm, the high-flow grade can reduce filling pressure relative to a medium-flow ABS. The process engineer should monitor peak hydraulic pressure and transfer position to avoid over-packing at the gate. Shot mass should occupy 50% to 75% of the barrel rated capacity; if the shot mass is below 25%, barrel residence time may exceed the stabilizer boundary and cause colour shift, odour, and loss of notched impact.
Gate freeze is governed by gate thickness, tool steel temperature, coolant flow, and melt temperature, not only by the resin. The holding-pressure profile for AN4500 should be derived from cavity pressure monitoring rather than from a generic table. Hot-runner manifolds held at 230 °C to 240 °C can impose additional residence time; the melt should not remain stagnant in the manifold for more than 15 min during stoppages unless a purge sequence is used. In hot-tip gates with small orifices, shear heating can raise actual melt temperature by more than 20 °C, contributing to gate-area discolouration. Thermal degradation in ABS proceeds by oxidation of the polybutadiene phase and chain scission or unzipping of the SAN matrix. Differential scanning calorimetry at 10 °C/min can locate the SAN glass transition, typically near 100 °C to 110 °C for many ABS products, but the exact value for AN4500 should be taken from the manufacturer’s datasheet. Melt temperature measured by an immersion probe is more useful than barrel set-point because shear heating can create a temperature differential of 10 °C to 20 °C under high back pressure or high injection speed. In the barrel, melt temperature should not exceed 250 °C unless the manufacturer explicitly permits a higher short-term limit.
AN4500 differs from extrusion grades in its molecular architecture. Extrusion ABS grades typically require higher melt strength and are specified with a lower melt-mass-flow rate under the same test condition; a lower value indicates higher molecular weight and greater die swell. In injection moulding, AN4500 would be expected to show lower die swell and reduced orientation, but this must be confirmed by the supplier because die swell is also influenced by rubber content and grafting. In painted or chrome-plated parts, rubber particle size and grafted SAN layer affect adhesion. A change from a lower-flow ABS to AN4500 may require revalidation of paint adhesion using a cross-cut tape test to ISO 2409:2020 and a water soak at 40 °C for 240 h. For electrical and electronic applications, the supplier should provide a declaration of conformity with RoHS Directive 2011/65/EU and, where applicable, REACH candidate-list SVHC statements. Food-contact status, if required, must be confirmed with a written statement under FDA 21 CFR 177.1020 or the applicable regional regulation for the specific grade and colour lot. The product should not be purged with polyacetal or PVC compounds; residual acid catalysts from these materials can degrade the butadiene phase. When changing from a flame-retardant PC/ABS or PVC, a polyolefin or acrylic-based purging compound should be used until the barrel is visually clean. The exact specification limits for AN4500 must be obtained from the manufacturer’s technical datasheet and applied to the specific machine, tool, and post-moulding operation.