| HS Code | 749678 |
| Density | 1.18 g/cm³ |
| Melt Flow Rate | 10 g/10 min |
| Tensile Strength | 40 MPa |
| Elongation At Break | 15% |
| Flexural Strength | 65 MPa |
| Flexural Modulus | 2300 MPa |
| Notched Izod Impact Strength | 100 J/m |
| Heat Deflection Temperature | 75 °C |
| Vicat Softening Temperature | 90 °C |
| Rockwell Hardness | 100 R |
| Molding Shrinkage | 0.4-0.6% |
| Water Absorption | 0.2% |
| Ul94 Flammability Rating | V-0 |
As an accredited Dongguan Hongsheng ABS 569 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dongguan Hongsheng ABS 569 is supplied in 25 kg moisture-proof paper-plastic composite bags, palletized for industrial transport. |
| Container Loading (20′ FCL) | Dongguan Hongsheng ABS 569 loaded in a 20′ FCL container, securely packed, sealed, labeled, and ready for export shipment. |
| Shipping | Dongguan Hongsheng ABS 569 is typically shipped as a non-hazardous thermoplastic resin in 25 kg bags or bulk. Store in a cool, dry, ventilated area away from moisture, direct sunlight, and ignition sources; handle with standard industrial precautions. |
| Storage | Store Dongguan Hongsheng ABS 569 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, and flames. Keep containers tightly closed, palletized, and protected from moisture, dust, and static buildup. Separate from strong oxidizers and acids. Avoid prolonged outdoor exposure; use grounded equipment; regularly inspect containers for damage/leaks; follow the SDS and local regulations. |
| Shelf Life | Typically 12 months in a dry, cool, ventilated warehouse, protected from sunlight and moisture; confirm exact shelf life with supplier. |
ABS 569 enters automotive interior trim production as a medium-flow acrylonitrile-butadiene-styrene resin; lot acceptance is normally performed against ISO 2580-1 designation data and a melt volume-flow rate measured under ISO 1133-1:2022. Before moulding, the granulate is dried in a desiccant dryer with a dew point below -20 °C at 80 °C for 2 h to 4 h; at ambient relative humidity above 60 %, drying time is extended to 4 h because residual moisture above 0.05 wt% measured by ISO 15512 Method A causes hydrolysis of the polybutadiene phase and produces splay on textured surfaces. The material is processed on a reciprocating screw injection moulding machine with an L/D ratio of 20:1 to 24:1, a compression ratio of 2.2:1 to 2.6:1, and a shut-off nozzle. Barrel temperatures are profiled from rear 200 °C to front 240 °C, with the centre zones held at 220 °C to 235 °C. Mould temperature is maintained at 50 °C to 80 °C by turbulent water circuits; a mould temperature below 40 °C produces visible knit-line weakness in perforated speaker-grille sections. Pack pressure between 40 MPa and 70 MPa, applied for 3 s to 6 s per millimetre of nominal wall, is required to prevent sink marks over rib roots. Regrind addition is restricted to 15 wt% to 20 wt% for non-appearance substrates; above 20 wt%, surface gloss measured at 60 ° per ISO 2813 falls by more than 5 units and notched Charpy impact per ISO 179-1/1eA becomes batch-dependent. Production-scale failure modes include gate blush, splay at the end of fill, and blistering after paint or electroplating. Gate blush is reduced by setting the first injection stage velocity below 60 mm/s and enlarging the gate land to at least 0.8 mm. Splay appears when the melt contains volatiles or when screw speed exceeds 120 rpm; back pressure is maintained at 0.5 MPa to 1.0 MPa to disperse colourant but not above 1.5 MPa because excessive shear heats the melt beyond 250 °C. For electroplated ABS parts, the surface is etched in a chromic acid bath with controlled chromium trioxide content, and surface roughness before plating should be below 0.5 μm Ra per ISO 4287. Adhesion is monitored by thermal cycling between -30 °C and 80 °C for 100 cycles; loss of adhesion at gate areas indicates over-shearing of the polybutadiene phase during moulding. Terminal parts include lower instrument panel brackets, centre console side supports, glove box bins, and air vent housings. Automotive interior compliance is documented under FMVSS 302 and ISO 3795 with horizontal burn rates below 100 mm/min; material certifications prepared to IATF 16949 lot traceability include REACH SVHC confirmation under Regulation (EC) No 1907/2006 and RoHS recast 2011/65/EU Annex II limits for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE.
Melt temperature is the dominant variable when ABS 569 is pushed into thin-wall map pocket backings and speaker grilles with nominal wall stock below 1.2 mm. The stable processing window narrows to approximately ±5 °C around the recommended melt temperature; barrel settings above 255 °C accelerate oxidative degradation of the polybutadiene rubber phase and shift notched Izod impact measured at 23 °C per ISO 180/1A downward by more than 10 %, while settings below 225 °C fail to fill flow-length-to-wall-thickness ratios above 120:1 at thin ribs. Residence time in the barrel is held below 5 min; on a two-cavity hot-runner mould with valve-gated drops and a projected area of 350 cm², a clamping force of 1200 kN is normally sufficient when cavity pressure is maintained at 35 MPa. Injection velocity is profiled in 3 stages: a slow initial fill to the gate, a high-velocity fill across the thin walls, and a reduced final velocity before switch-over to hold pressure. Regrind is limited to 10 wt% for thin-wall appearance surfaces because higher regrind fractions raise melt viscosity and increase gas traps at the end of fill. Thin-wall tooling requires a polished runner and gate diameter of 0.8 mm to 1.2 mm for direct edge gates; valve-gated hot drops are set to 230 °C to 245 °C. A shear rate above 10 000 s⁻¹ at the gate can cause melt fracture on the surface; therefore, gate land length is held below 1.0 mm. The pressure drop across the hot runner is measured with pressure transducers; a drop above 30 MPa indicates a restricted manifold channel and is corrected by increasing the manifold temperature in 5 °C increments, not by raising barrel temperature, because barrel temperature above 255 °C damages the rubber phase. Batch-to-batch variation in impact is monitored with a moving range chart; a shift above 1.5 sigma triggers re-qualification of the lot under ISO 180/1A before release. Tensile elongation at break is checked after moulding on dry-as-moulded specimens per ASTM D638-14; a drop below 5 % indicates excessive thermal history. Terminal products include map pocket backing panels, seat side trim, and instrument panel speaker grilles. Compliance requires dimensional checks under ISO 291 standard atmosphere, flammability documentation under ISO 3795, and PPAP submissions with process capability indices for part mass and notched impact. Published data for this specific thin-wall configuration is limited; processors usually confirm the processing window with a design-of-experiment matrix across melt temperature and injection velocity before serial production.
Sheet extrusion of ABS 569 is run on a single-screw extruder with a barrier screw, L/D ratio 30:1 to 36:1, and screen packs graded 60/80/100 mesh. Melt temperature at the die is kept between 210 °C and 230 °C; die zones are set 5 °C to 10 °C below the maximum barrel temperature to reduce die-lip drool. A gear pump placed between the screw tip and the flexible-lip die stabilises volumetric output; across a 1.2 m wide sheet line, thickness variation is held to ±0.05 mm at a nominal gauge of 2.0 mm by closed-loop thickness gauging. The sheet is cooled on a three-roll stack with roll temperatures of 80 °C to 100 °C; lower roll temperatures below 70 °C increase residual orientation and cause excessive thermoforming reversion in the finished part. Regrind from edge trim is introduced into the core layer at up to 30 wt% of the total extrudate when a coextruded cap layer is used; without a cap layer, regrind is kept below 15 wt% to preserve surface gloss and impact. Thermoforming of the sheet is carried out at a surface temperature of 140 °C to 170 °C, with plug speeds below 300 mm/s for deep-draw refrigerator liners. Thermoforming reversion is measured on a 10 cm × 10 cm specimen heated in oil at 160 °C for 10 min; reversion above 5 % in the machine direction indicates excessive roll-stack draw. Coextruded sheet with a virgin cap layer of 0.2 mm to 0.5 mm over a core containing regrind retains gloss above 80 GU at 60 ° per ISO 2813 after forming. For deep-draw parts, plug assist temperature is controlled at 110 °C to 130 °C to prevent premature sheet cooling. The major operational boundary is moisture pickup in regrind stored in open bins; edge trim that has absorbed more than 0.1 wt% moisture produces bubble defects in the final sheet, and the dryer must reduce moisture below 0.02 wt% before the regrind enters the core layer. Terminal products include refrigerator door liners, luggage shells, and low-gloss thermoformed panels. Food-contact status, where required for refrigerator liners, falls under FDA 21 CFR 181.32 for acrylonitrile copolymers; the converter must verify the supplier’s regulatory letter for ABS 569 and maintain extraction testing under the applicable food-contact migration protocol. Failure to dry the regrind before reintroduction leads to silver streaks and a local reduction in sheet ductility measurable as a loss of more than 15 % in notched Izod impact per ISO 180/1A.
For power supply housings and router bottom shells, ABS 569 is processed on a reciprocating screw injection machine with a three-plate mould or hot-runner edge gate; melt temperature is set at 220 °C to 240 °C and mould temperature at 40 °C to 60 °C. Drying at 80 °C for 2 h to 3 h to a residual moisture below 0.05 wt% is mandatory because electrically live enclosures with internal ribs show blistering at high humidity if the granulate is damp. Colour masterbatch is added at 2 wt%; carbon black masterbatch at 2 wt% is acceptable, but excessive lubricant in some masterbatches reduces Vicat softening temperature measured under ISO 306/B50 by 2 °C to 4 °C. Regrind is limited to 10 wt% to 15 wt%; higher fractions shift the melt volume-flow rate and cause short shots at the thin wall sections around screw bosses. Terminal parts include desktop charger enclosures, LAN switch housings, and measurement instrument covers. Flammability of ABS 569 in these applications is typically classified as UL 94 HB; it is not an UL 94 V-0 material, and any enclosure requiring a V-0 rating at final thickness must switch to a flame-retardant ABS or ABS/PC grade. Glow-wire performance under IEC 60695-2-11 is validated at 650 °C for unattended appliances, provided the final part passes the IEC 62368-1 flammability clauses; terminal product documentation includes dielectric strength per IEC 60243-1 and creepage distance verification per IEC 60664-1. Exposure to aromatic hydrocarbons, ketones, and esters must be excluded because these solvents induce environmental stress cracking in ABS; compatibility with flux residues from soldering processes should be checked by immersion testing under the manufacturer’s protocol, because published data for this specific configuration is limited.
| Application sector | Standard or regulation | Test method / clause | Limiting criterion |
|---|---|---|---|
| Automotive interior trim | FMVSS 302 | Horizontal burn rate | Below 100 mm/min |
| Automotive interior trim | ISO 3795 | Flame propagation | Below 100 mm/min |
| Electrical enclosures | IEC 62368-1 | Fire enclosure assessment | UL 94 HB or glow wire 650 °C |
| Electrical enclosures | IEC 60695-2-11 | Glow-wire flammability | No ignition at 650 °C for unattended use |
| Household appliances | IEC 60335-1 | Ball pressure test | Indentation below 2.0 mm at 75 °C |
| Food-contact sheet | FDA 21 CFR 181.32 | Acrylonitrile copolymer requirements | Supplier regulatory letter required |
| General materials | ISO 2580-1 | Designation system | ABS lot certification |
In humid bathroom appliance applications, ABS 569 replaces HIPS where the enclosure must withstand repeated contact with soapy water and intermittent condensation. The process is injection moulding with high-gloss polished tool surfaces and mould temperature of 60 °C to 80 °C to achieve surface gloss above 90 GU at 60 ° per ISO 2813. Melt temperature is limited to 220 °C to 240 °C; above 250 °C, yellowing of the SAN matrix becomes visible on white or light colours within 3 min of residence time. A white masterbatch with titanium dioxide is added at 3 wt% to 4 wt%; if pearl pigment is used, the addition is 0.05 wt% to 0.15 wt% because higher loadings reduce weld-line strength at the tongue-and-groove seam of the housing. Regrind is held below 10 wt% for light-coloured parts because regrind darkens the polymer and increases yellowing under the hot runner. Terminal products include electric toothbrush charger bases, oral irrigator housings, and shaver stands. Compliance under IEC 60335-1 is documented for heated or unattended components with a glow-wire end-product test at 650 °C according to clause 30.2; ball pressure testing under IEC 60695-10-2 is run at 75 °C, and the material must not show an indentation diameter greater than 2.0 mm. The operational boundary is explicit: ABS 569 is not acceptable for enclosures exposed to aqueous solutions containing more than 10 % ethanol, acetone, or ethyl acetate, and compatibility with aggressive bathroom cleaners must be verified by immersion testing at 23 °C for 24 h under the manufacturer’s protocol.
Control panel housings for washing machines and dishwashers use ABS 569 in injection-moulded bezels, button trays, and fascia boards where peak surface temperature remains below 65 °C. The tool should be designed with generous radii at the junction between the front face and side walls; a minimum radius of 0.8 mm reduces stress concentration and prevents cracking during button-press cycling tests. Melt temperature is set between 220 °C and 240 °C, mould temperature at 50 °C to 70 °C, and packing pressure at 35 MPa to 55 MPa. Colour masterbatch is added at 2 wt%; if the part is overmoulded onto a polycarbonate light guide, the ABS melt temperature must not exceed 240 °C and the PC insert must be pre-dried to below 0.02 wt% moisture to prevent bubbling at the interface. Regrind is allowed up to 15 wt% for dark colours and 5 wt% for light colours. Failure modes in control panel moulding include cracking at clip towers, gloss variation across the visible face, and warpage above 0.8 mm over a 250 mm span. Clip towers are gusseted with a wall thickness of 1.2 mm and a radius of 0.6 mm at the root; ejection is performed with a balanced pin array because uneven ejection at 65 °C part surface temperature creates stress whitening on light colours. Warpage is controlled by separating the packing stage into two phases: the first phase at 45 MPa for 2 s and the second at 25 MPa for 5 s. Mould temperature differential across the two halves should not exceed 10 °C; a higher core temperature of 70 °C and lower cavity temperature of 60 °C counteracts bow. Adhesion of printed inks or UV-cured coatings is tested by cross-cut tape removal according to ISO 2409; the target is class 0 or 1. Terminal products include washing machine control bezels, dishwasher fascia panels, and touchpad trays. Compliance is assessed under IEC 60335-1 for mechanical endurance, IEC 60695-2-11 glow-wire ignition at 650 °C, and ISO 306/B50 Vicat softening temperature with a minimum expected value above 95 °C for this component class.
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Within the Dongguan Hongsheng grade portfolio, ABS 569 is designated as an unfilled acrylonitrile-butadiene-styrene terpolymer supplied as cylindrical granules for injection molding and limited profile extrusion. The model designation identifies a medium-high-flow material in which the butadiene rubber phase contributes impact resistance, the acrylonitrile fraction supplies chemical resistance and hardness, and the styrene phase provides melt processability and surface gloss. The grade is used primarily by converters manufacturing appliance housings, electronic enclosures, consumer-goods components, and automotive interior trim parts that require a balance of impact strength and mold filling. Because no independently published academic study of this specific formulation exists, application-specific decisions should be controlled by the manufacturer’s certificate of analysis and the processing guide for the lot in question.
Property measurements on conditioned specimens are carried out under ISO and ASTM methods. The following specification window has been compiled from typical unfilled ABS values in this viscosity class; lot-specific data from Dongguan Hongsheng may narrow the ranges. Mechanical tests are performed on specimens conditioned at 23 °C and 50 % relative humidity for at least 16 h unless the material specification states otherwise.
| Property | Test method | Typical specification window |
|---|---|---|
| Density | ISO 1183-1:2019 | 1.04–1.06 g/cm³ |
| Melt mass-flow rate, 220 °C / 10 kg | ISO 1133-1:2022 | 15–30 g/10 min |
| Tensile yield stress, 50 mm/min | ISO 527-2:2012 | 40–48 MPa |
| Flexural modulus, 2 mm/min | ISO 178:2019 | 2,200–2,600 MPa |
| Charpy notched impact, 23 °C | ISO 179-1:2023 | 18–28 kJ/m² |
| Vicat softening temperature, 50 N, 50 °C/h | ISO 306:2022 | 95–105 °C |
| Heat deflection temperature, 1.8 MPa | ISO 75-2:2013 | 85–95 °C |
| Rockwell hardness, R scale | ISO 2039-2:1987 | 105–115 |
| Mold shrinkage, parallel/normal | ISO 294-4:2018 | 0.4–0.7 % |
| Flame rating, 1.5 mm | UL 94 | HB unless a specific lot certification states otherwise |
Because the butadiene phase is susceptible to surface defects when moisture is present in the feed throat, pre-drying is required when ambient relative humidity exceeds 60 %. A desiccant dryer with a dew point of −30 °C or lower should be used, with a hopper temperature of 80 °C and residence time of 2 h to 4 h. Target residual moisture before processing is below 0.05 wt%. In high-humidity transfer lines, hopper loading should be sealed and dried-air purged; otherwise splay marks, silver streaks, and irregular gloss appear on molded parts. These defects are not solely cosmetic: at melt temperatures above 240 °C, residual moisture flashes to steam at the nozzle and produces localized porosity and delamination at knit lines. Drying hoppers should not be operated above 85 °C, because pellet surface sticking can occur and block material flow in the hopper throat.
The melt window for ABS 569 falls between 210 °C and 240 °C for barrel zones, with a nozzle setting of 230 °C to 245 °C. At melt temperatures above 250 °C, the butadiene phase undergoes thermal oxidation and the acrylonitrile-styrene matrix begins to yellow; at temperatures below 200 °C, high injection pressures and incomplete filling of thin sections are observed. Mold temperatures should be maintained between 40 °C and 80 °C, with the upper half of the range used for high-gloss surfaces and reduced flow marks. General-purpose screw geometry with an L/D ratio of 20:1 to 22:1 and compression ratio of 2.0:1 to 2.5:1 is suitable. Back pressure should be held at 0.5 MPa to 1.5 MPa to prevent screw surging and ensure melt homogeneity without excessive shear heating. Screw rotation speeds of 30 rpm to 80 rpm are typical, but production-scale machines with high-dispersion mixing sections may generate shear heat that pushes melt temperature above the threshold even at low barrel settings.
Injection velocity is selected by part geometry. For wall thicknesses of 1.2 mm to 2.5 mm, a filling time of 0.5 s to 1.5 s is common in multi-cavity molds. Hold pressure is set from 60 % to 80 % of the actual peak injection pressure, with hold time determined by gate freezing. Cavity pressure transducers on production tools have shown that process capability improves when the peak cavity pressure is held between 25 MPa and 40 MPa. The high-flow character of this grade reduces peak injection pressure in thin-wall tools compared with general-purpose ABS, but weld-line strength can be reduced if the melt front temperature drops below 220 °C before knitting. Observed failure modes on production lines include nozzle drool at melt temperatures above 245 °C, screw slip during plastication if back pressure is below 0.3 MPa, and cold slug marks when the nozzle temperature drops below 220 °C>. Mold deposit formation on cores is reported in high-gloss cavities when mold temperature exceeds 80 °C and venting depth exceeds 0.03 mm; vents should be maintained at 0.02 mm to 0.03 mm.
At melt temperatures above 250 °C, thermal oxidative degradation begins with attack on the unsaturated butadiene segment, producing conjugated double-bond chromophores that shift the molded part color from natural white or light yellow to amber. The degradation pathway also liberates volatile compounds; ventilation at the mold and nozzle is required. Residence time at melt temperature should be kept below 5 min. During production interruptions, the barrel should enter screw-rotate mode with reduced temperature or be purged.
The melt is pseudoplastic; apparent viscosity at 100 s⁻¹ and 230 °C in capillary rheometry according to ISO 11443:2021 typically lies between 100 Pa·s and 300 Pa·s for this viscosity class. This allows filling of spiral-flow lengths around 30 cm to 50 cm in a 1.0 mm depth, 10 mm width spiral mold at 230 °C and 80 °C mold temperature, depending on gate and tool layout. Exact spiral-flow lengths must be verified on the production tool because mold cooling line layout and hot-runner geometry shift flow length. Hot-runner systems should use externally heated manifolds with no dead spots; gate orifices below 0.8 mm may generate excessive shear temperatures exceeding 260 °C even when the screw barrel is at 230 °C. Thermocouples in the hot-runner tip should be validated against an air-shot pyrometer before production.
The material is specified for appliance control panels, power tool housings, vacuum cleaner components, and electronic device enclosures where wall thickness is between 1.2 mm and 2.5 mm. In these tools, the higher melt-flow rate permits lower peak injection pressure and shorter fill time than a general-purpose extrusion ABS with an MFR of 5 g/10 min to 10 g/10 min. Where the part is not subject to fire enclosure requirements of IEC 62368-1:2023, the grade is evaluated at UL 94 HB. Long-term thermal aging data should be generated according to ISO 2578:1993 for the specific part wall thickness. Dimensional inspection is performed after conditioning at 23 °C and 50 % relative humidity for 24 h>; tool-specific shrinkage is evaluated using ISO 294-4:2018.
Where ABS 569 is compared with other ABS classes, the primary differentiators are melt viscosity, butadiene rubber content, heat resistance, and additive package. A low-gloss, general-purpose extrusion ABS with an MFR of 5 g/10 min to 10 g/10 min provides higher melt strength for sheet and profile but requires higher injection pressures for thin-wall parts. Flame-retardant ABS grades containing brominated or phosphorus-based modifiers are typically specified for enclosures requiring UL 94 V-0 at 1.5 mm or 0.8 mm; they exhibit densities above 1.16 g/cm³ and notched impact values 30 % to 50 % lower than unfilled ABS 569. Electroplating ABS grades contain a higher butadiene level and an oxidizable rubber phase that promotes adhesion of electroless nickel and copper after chromic-acid etching; ABS 569 is not formulated for electrolytic plating and should not be substituted into plated-part programs without adhesion validation under ASTM B533-85(2019). High-heat ABS grades use α-methylstyrene or maleimide comonomers to raise heat deflection temperature above 100 °C, but their melt-flow rate is lower and their processability is more constrained in long-flow parts. Transparent MABS grades with methyl methacrylate comonomer transmit light but have lower notched impact and are not a direct replacement for ABS in impact-critical applications.
| ABS grade class | Key formulation difference | Typical consequence relative to ABS 569 |
|---|---|---|
| General-purpose ABS | Lower melt-flow rate, higher molecular weight | Higher melt strength, lower injection productivity in thin sections |
| Flame-retardant ABS | Brominated or phosphorus additive package | Possible UL 94 V-0; higher density, lower impact |
| Electroplating ABS | Higher butadiene content, tailored rubber morphology | Better etch adhesion; not required for non-plated ABS 569 |
| High-heat ABS | α-methylstyrene or maleimide comonomer | Higher heat deflection temperature, lower melt flow |
| Transparent MABS | Methyl methacrylate comonomer | Light transmission, lower notched impact |
The grade is not formulated with flame-retardant synergists and should not be specified for enclosures requiring UL 94 V-0 or V-1 at thicknesses below 3.0 mm unless the certificate of analysis explicitly states a tested rating. Chemical resistance is limited: aromatic hydrocarbons, ketones, esters, and chlorinated solvents cause stress cracking or surface attack, particularly under molded-in stress; medium resistance is observed for alcohols and dilute aqueous acids. UV exposure without carbon black or hindered amine stabilizers leads to surface chalking and loss of gloss, so outdoor use is not recommended without accelerated weathering validation under ISO 4892-3:2024. RoHS compliance is assessed under European Union Directive 2011/65/EU Annex II, and REACH SVHC statements should be confirmed for each lot. For food-contact applications, compliance with 21 CFR 177.1020 must be verified by the supplier before use.
Regrind from sprues and runners can be added at up to 20 wt% if the material has been dried and is free of contamination. Higher regrind levels increase melt-flow rate and reduce Charpy impact, especially after multiple heat histories. Purging between colors or materials should use a styrenic purging compound or general-purpose polystyrene; flame-retardant or PVC residues are incompatible and should be excluded from shared hoppers and grinding systems. Profile extrusion is limited to thin-walled or small cross-section applications because the high melt-flow rate of ABS 569 reduces melt strength and neck-in. Sheet extrusion for thermoforming should instead select a general-purpose extrusion ABS with lower melt-flow rate unless a coextrusion tie layer or compounding step is used.
Production release should be based on cavity-pressure repeatability, part weight, and dimensional checks after conditioning. Since lot-to-lot variation in additive package and rubber particle size distribution can shift gloss and impact, each inbound lot should be qualified with a minimum of melt-flow-rate measurement under ISO 1133-1:2022, density under ISO 1183-1:2019, and Charpy notched impact under ISO 179-1:2023. The material should be rejected or downgraded if the melt-flow rate falls outside the agreed range or if moisture-induced splay persists after a verified drying cycle.