| HS Code | 367836 |
| Product | Guangzhou Keyuan New Material ABS 810 |
| Density | 1.05 g/cm³ |
| Melt Flow Rate | 10 g/10 min |
| Tensile Strength | 45 MPa |
| Elongation At Break | 20% |
| Flexural Strength | 70 MPa |
| Flexural Modulus | 2300 MPa |
| Notched Izod Impact Strength | 200 J/m |
| Heat Deflection Temperature | 85 °C |
| Vicat Softening Temperature | 95 °C |
| Rockwell Hardness | 105 R |
| Molding Shrinkage | 0.4-0.6% |
| Water Absorption | 0.2-0.3% |
As an accredited Guangzhou Keyuan New Material ABS 810 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Guangzhou Keyuan New Material ABS 810 packaging: 25 kg net woven bags, palletized and shrink-wrapped for industrial transport. |
| Container Loading (20′ FCL) | One 20-foot FCL container loaded with Guangzhou Keyuan New Material ABS 810 resin, securely packed for export shipment. |
| Shipping | Guangzhou Keyuan New Material ABS 810 is packed in moisture-proof bags or containers and shipped as non-hazardous general cargo. Keep cool, dry, ventilated, and protected from direct sunlight, rain, punctures, contamination, and heavy stacking. Follow the SDS and local transport regulations. |
| Storage | Store Guangzhou Keyuan New Material ABS 810 in a cool, dry, well-ventilated warehouse, protected from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed to prevent moisture and contamination. Separate from strong oxidizers, control dust/static, and follow the manufacturer’s SDS and local regulations. Use appropriate personal protective equipment when handling. |
| Shelf Life | When stored sealed in a cool, dry, ventilated place, shelf life is typically 12 months from production date. |
Guangzhou Keyuan New Material ABS 810 is charged into a desiccant-bed hopper dryer with a dew point of -30 °C or lower and dried at 80±5 °C for 2–4 h. Residual moisture is determined by ISO 15512:2019 and held at ≤0.05%; lots exposed to ambient air for more than 4 h at RH 60% are redried. In desktop power adapter enclosure production, a nominal wall thickness of 0.9–1.2 mm is filled on a 1200 kN hydraulic injection moulding machine with a 35 mm general-purpose screw and an open nozzle. Barrel settings from rear to nozzle are 220–230–235–240–235 °C, with nozzle melt temperature measured at 230–245 °C. First-stage injection pressure is recorded at 850–1150 bar; holding pressure is set at 50–70% of the actual fill pressure, and holding time is established by gate-seal time rather than part weight only. Screw speed is limited to 60–90 rpm, back pressure to 5–10 bar hydraulic, and shot size to 40–70% of barrel capacity so that residence time at 240 °C remains below 6 min. Mould surface temperature is controlled at 45–60 °C; mould temperatures below 40 °C deepen weld lines at boss intersections and reduce small-radius gloss, while mould temperatures above 70 °C extend required cooling time without measurable property gain. Cold-runner regrind is added at no more than 20 wt%; higher regrind fractions reduce instrumented puncture energy under ISO 6603-2 and increase lot-to-lot colour drift. A 1 wt% carbon black masterbatch is used for black enclosures, and colour-matched lots are verified for melt-flow stability under ISO 1133-1:2022 at 220 °C/10 kg. Lot-to-lot melt-flow variation is monitored because a shift of ±2 g/10 min is enough to change thin-wall injection pressure by 60–100 bar. Enclosure safety is evaluated under IEC 62368-1:2023; flammability classification of ABS 810 in this end use is UL 94 HB at 1.5 mm unless a lot-specific UL Yellow Card lists another rating. ABS 810 is not substituted for flame-retardant ABS or PC/ABS where a V-0 rating at 0.8 mm is required by the product standard. RoHS screening under 2011/65/EU Annex II and REACH SVHC communication under 1907/2006 are managed through supplier declarations; these are not substitutes for end-product conformity.
In high-gloss black pillar garnishes, ABS 810 is processed on a 1600 kN accumulator-assisted or high-speed electric machine. The cavity wall is 0.8 mm at the visible face; attachment ribs are 0.45–0.55 mm thick and must fill without flash. The critical interaction is between melt temperature, surface replication and resin residence time. Melt temperature below 230 °C increases shear viscosity and produces short shots or deep weld lines at rib roots; melt temperature above 245 °C can volatilize low-molecular-weight additives and generate splay at the gate, reducing 20° gloss under ISO 2813. A control band of ±5 °C around the optimal nozzle temperature is therefore maintained. Capillary rheometry under ISO 11443:2021 at 230 °C and 1000 s⁻¹ typically places shear viscosity in the 90–160 Pa·s band for high-flow injection ABS; lot-specific curves from the ABS 810 certificate of analysis determine the final setpoint. Injection time is set at 0.45–0.75 s; longer fill times create hesitation marks where the melt front crosses rib intersections. Holding pressure is 65–80 MPa, with switch-over position controlled to 2–4 mm cushion. Tool temperature is kept at 50–70 °C to reproduce the polished cavity finish; above 75 °C parts tend to stick to the cavity and colour shift becomes measurable. Formulation for this application is 100 mass parts ABS 810 with 0.3–0.5 phr external lubricant, 0.2 phr antioxidant and 1.0–1.5 phr UV stabiliser. Regrind is restricted to 10 wt% or less because higher regrind fractions lower 60° gloss below 90 GU and widen the shot-to-shot peak injection pressure. Gate location is placed at a hidden edge to avoid visible gate blush; sequential valve gates are avoided because they introduce flow-front temperature loss of 5–10 °C and create halo marks. Rib root radius is specified at 0.4–0.6 mm; sharp corners below 0.2 mm radius produce stress concentration and reduce weld-line strength by 30–40% in short-beam tests under ISO 178. Flammability of the finished trim is tested under ISO 3795:1989 or FMVSS 302; ABS 810 does not provide inherent flame retardance and is used only where the prescribed burn rate is met by part design and wall section. The grade should not be mixed with PVC or acetal regrind; HCl from PVC decomposition catalyzes ABS chain scission, while formaldehyde from acetal degradation produces voids and delamination. Automotive fogging and odour requirements such as DIN 75201 or VDA 278 must be verified separately because published data for ABS 810 in this specific configuration is limited.
Processing window matrix for ABS 810 across three principal conversion routes.
| Conversion route | Drying condition | Melt/die/sheet surface temperature | Tool/roll temperature | Throughput or cycle parameter | Key test method |
|---|---|---|---|---|---|
| Injection moulding | 80±5 °C, 2–4 h, dew point ≤-30 °C | 230–245 °C nozzle | 45–60 °C | shot size 40–70% of barrel capacity | ISO 1133-1:2022 |
| Sheet extrusion | 80±5 °C, 4 h minimum, ≤0.05% moisture | 220–240 °C die | roll stack 85–110 °C | screw speed 35–60 rpm | ISO 15512:2019 |
| Thermoforming | re-dry sheet at 70–80 °C for 1–2 h if exposed | sheet surface 150–180 °C | mould 40–55 °C | plug assist 110–130 °C | ISO 2813 |
In cyclone housings for canister and upright vacuum cleaners, ABS 810 is processed as a 2.0 mm main wall with 1.2 mm scroll ribs and multiple snap-fit tabs. The tooling is a multi-plate mould on a 1600 kN hydraulic press with a valve-gated hot runner. Drying before use follows 80±5 °C for 3–4 h; residual moisture above 0.08% is associated with silver streaking at the hot gate and reduced weld strength. Melt temperature at the nozzle is kept at 230–245 °C, and mould temperature is set at 50–65 °C. The annular scroll geometry creates converging flow fronts; weld lines inside the scroll are unavoidable, so the gate is positioned to shift the weld line to a low-stress region and the cavity is vented around the convergence line. Weld factor for static strength under ISO 527-2:2012 at 23 °C is typically 0.7–0.8 of the bulk tensile yield value; if higher retention is required, a lower-viscosity or higher-toughness grade should be evaluated. Impact resistance at the snap-fit tab is checked with notched Izod under ISO 180/A at 23 °C and at -10 °C; failure of sharp-corner tabs below 0.2 mm root radius is often due to tool wear rather than resin lot variation. Regrind is added at 15 wt% maximum, and black colour is obtained with a 2 wt% carbon black masterbatch. Electrical safety is assessed under IEC 60335-1:2020; ABS 810 is used for structural enclosures that do not exceed 75 °C surface temperature during normal operation. Glow-wire testing under IEC 60695-2-11 is performed at the end-product level; if an unattended appliance requires 850 °C glow-wire ignition temperature, plain ABS 810 may not pass and a flame-retardant or mineral-filled grade should be selected. Avoid dry blending with amine-based flame retardant additives; amine species can interfere with moisture uptake and accelerate yellowing at 240 °C. To avoid sink marks over 2.5 mm bosses, gas counterpressure or foaming is not recommended; instead the boss is cored and gusseted at 0.8–1.0 mm wall to maintain packing.
Chrome-plated bathroom and sanitary fittings are produced from ABS 810 by injection moulding a low-stress preform, followed by etch-and-plate processing. The first requirement is that the moulded surface be free of high shear stress; internal mould release levels above 0.2 phr or silicone-containing mould release residues migrate to the surface and cause skip plating. The plating line operates with a chromic acid etch bath containing 380–420 g/L chromium trioxide and 180–220 g/L sulphuric acid at 60–70 °C. Etch time is set at 8–15 min, depending on butadiene particle etch rate; a uniform microporous surface with Ra in the 0.2–0.5 µm range is required before neutralization. After etch, parts are treated in a neutralizer, then electroless or electrolytic copper strike is applied, followed by bright nickel and decorative chromium layers. Current density for copper strike is controlled at 2–5 A/dm²; higher current densities produce roughness at high current density edges. Adhesion of the plate is evaluated by thermal cycling under ASTM B604, with no blistering, cracking or peel-back after cycles between -40 °C and 80 °C. Coupon peel strength is commonly required above 100–200 N/m; if ABS 810 has not been specifically designated as a plating grade, a lot-specific etch-rate and peel-strength validation must be performed because published data for this grade in electroplating systems is limited. The compound must not be contaminated with PVC or acetal; polyolefin contamination produces unetched islands and local loss of plate adhesion. Regrind above 10 wt% is not recommended for plated parts because regrind history widens surface etch rate and creates visible pits after plating. Preform moulding uses melt temperature 220–235 °C rather than the higher settings used for thin-wall parts, because lower melt temperature reduces residual stress; mould temperature is set at 60–75 °C to minimise frozen-in orientation. After electroplating, dimensions grow by the thickness of the deposited metal stack; tolerances must allow for 20–40 µm total plate thickness on functional bosses and threads.
Monitor bezels and audio-video panel frames are moulded from ABS 810 in multi-cavity tools with cold runner gates of 0.8–1.0 mm and a projected area that typically requires a 2000 kN or larger press. The dimensional specification is tied to ISO 291 standard atmosphere 23±2 °C, 50±5% RH and ISO 294-4 for moulding shrinkage. For ABS 810, moulding shrinkage is 0.4–0.6% in the flow direction and 0.5–0.7% transverse, with post-mould shrinkage less than 0.1% after annealing at 80 °C for 2 h. These values are not constants; they shift with wall thickness, gate geometry and packing time. Cavity-to-cavity mass variation is held below 0.2% by balancing hot runner or cold runner scrap, and cushion position is kept at 2–4 mm to maintain consistent packing. Weld lines formed at screen cutouts and cable exit slots are moved to non-appearance zones by gate relocation or flow leaders. A 2 wt% colour masterbatch produces colour consistency; shade is measured at D65/10° using ISO 11664-4. Surface quality is checked under ISO 2813 at a 60° geometry; visible splay, halo and gate blush are rejected. Flammability classification remains UL 94 HB at 1.5 mm unless the final product standard permits horizontal burning; if the display enclosure is specified under IEC 62368-1:2023, the end product must meet the enclosure flammability and ball-pressure requirements, and ABS 810 is used only for parts that do not require V-0 at wall sections below 1.5 mm. To avoid warpage after painting or metallizing, parts are stress-relieved at 70–80 °C for 30–60 min; skipping this step increases paint crazing and dimensional drift in assemblies. Compatibility with cleaning agents is tested under ISO 175:2010 before production; ABS 810 is not recommended for direct contact with ketone-based solvents.
Regulatory and test method matrix for ABS 810 target end uses.
| Target end use | Standard or directive | Property evaluated | Acceptance condition for ABS 810 |
|---|---|---|---|
| Desktop power adapter enclosure | IEC 62368-1:2023, UL 94 | Flame classification, ball pressure | UL 94 HB at 1.5 mm; ball pressure 75 °C |
| Automotive interior pillar garnish | ISO 3795:1989, FMVSS 302 | Burn rate | ≤100 mm/min or end-product limit |
| Vacuum cleaner cyclone housing | IEC 60335-1:2020, IEC 60695-2-11 | Glow-wire, surface temperature | ≤75 °C surface; glow-wire end-product test |
| Electroplated sanitary fitting | ASTM B604 | Plate adhesion thermal cycling | No blistering from -40 °C to 80 °C |
| Monitor bezel / AV panel | ISO 294-4, ISO 291, IEC 62368-1:2023 | Shrinkage, dimensional stability, flame | shrinkage 0.4–0.6% flow; UL 94 HB |
| Thermoformed luggage shell | ISO 4892-3 if ASA-capped | Artificial weathering | ΔE limit set by end product; ABS 810 core not exposed |
ABS 810 sheet for thermoformed luggage shells is produced on a co-rotating twin-screw extruder with an L/D ratio of 33:1 and vacuum venting. The resin is dried at 80±5 °C for 4 h minimum to a moisture content below 0.05%; wet resin causes steam bubbles in the sheet that become pinholes after thermoforming. Screw speed is set at 35–60 rpm, melt temperature at the die is 220–240 °C, and die pressure is recorded to detect gel or filler accumulation. The three-roll polishing stack is held at 85–110 °C; lower roll temperatures increase gloss but produce higher sheet orientation and warp, while higher roll temperatures cause sheet sticking and cooling line slowdown. Raising die temperature above 250 °C does not improve sheet sag; in 400 mm unsupported sheet spans on a single-station thermoformer, sag depth increases by 6–10 mm and draw uniformity deteriorates. Sag is controlled instead by lowering melt temperature to 215–230 °C, increasing roll stack speed, and using sheet-edge heating to reduce local cooling. During thermoforming, the sheet surface is heated to 150–180 °C; plug assist temperature is 110–130 °C and mould temperature is 40–55 °C. Typical draw ratio is 1:1.5 to 1:2.0; deeper draws cause thin-out below 0.3 mm at corners unless pre-stretch is optimised. The ABS 810 core is capped with a 10–15% ASA layer of total sheet thickness where UV stability is needed; testing is performed under ISO 4892-3 to the end-product ΔE limit. Regrind from skeleton trim is reintroduced at no more than 25 wt% in the core layer. Higher regrind content raises the thermoforming temperature and increases brittleness after low-temperature drop tests. If a customer-specific drop test at -20 °C is specified, a separate low-temperature impact grade should be screened because published data for ABS 810 at this condition is limited.
In non-patient-contact diagnostic device enclosures, ABS 810 is used for external shells that are not intended for skin contact beyond occasional handling and are cleaned with 70% isopropanol or quaternary ammonium disinfectants. The grade is not certified for body-contact or fluid-path applications under ISO 10993-1:2018, and no biocompatibility claim is made. Moulding is performed on a 1200–1600 kN electric press with a 30 mm or 35 mm screw, melt temperature 225–240 °C, and mould temperature 50–65 °C. The shell design uses a 1.5–2.0 mm wall to meet impact and structural requirements, with snap-fit retention features and ultrasonic weld joints. Ultrasonic welding is performed at 20 kHz with a 0.25–0.5 mm shear-joint interference and amplitude of 30–40 µm; excessive amplitude creates weld flash and weakens the joint because ABS 810 dissipates energy rapidly at the weld interface. Regrind is allowed up to 15 wt% internally, but regrind from painted or metallized parts is excluded. Chemical resistance is a key processing boundary; ABS 810 is incompatible with ketones, esters and aromatic hydrocarbons. Compatibility with the intended hospital disinfectant is tested under ISO 175:2010 before production; stress cracking can occur at moulded-in stress if the part is exposed to solvent without post-mould annealing. Annealing at 70 °C for 1 h reduces solvent stress-cracking in critical snap-fit regions. Electrical safety of the finished device is assessed under IEC 60601-1:2005/AMD1:2012/AMD2:2020; ABS 810 contributes mechanical enclosure protection but does not provide electrical insulation or flame retardance beyond its natural polymer limits. Where the product standard requires flame-rated enclosures, ABS 810 is not a substitute for flame-retardant ABS or PC/ABS.
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Guangzhou Keyuan New Material ABS 810 is a medium-flow acrylonitrile-butadiene-styrene copolymer supplied as pelletized feedstock for injection molding and selected extrusion processes. The grade suffix places the product within the nominal melt mass-flow rate interval of 8–12 g/10 min under ISO 1133-1:2022 at 220 °C/10 kg; however, the controlling specification is the Guangzhou Keyuan New Material certificate of analysis, and published grade-specific data for this configuration is limited. The material is specified where processors require a balance among cavity filling, notched Charpy impact retention under ISO 179-1:2010, and dimensional stability in nominal wall thicknesses from 1.5 mm to 3.0 mm. Virgin pellet bulk density typically ranges from 600 kg/m³ to 700 kg/m³, which affects hopper capacity calculations and feed-throat behavior rather than molded-part quality.
Moisture control is the first processing boundary. ABS absorbs water from atmospheric exposure; residual moisture above 0.08% by mass, determined by ISO 15512:2019, produces splay, silver streaks, and transient effervescence at the nozzle. A desiccant dryer with an air dew point below -30 °C and air temperature of 80–85 °C for 2–4 h is the standard pre-conditioning route. At ambient storage conditions above 60% RH, the drying interval should be extended to 4–6 h, and regrind fractions exceeding 20% should be dried and verified separately because residual moisture in regrind is non-uniform. Hopper inlet air temperature should not exceed 70 °C to prevent pellet softening and bridging in the feed throat. On a multi-cavity injection molding line with a 1200 kN clamp force, feeding wet ABS 810 class resin to a hot-runner tool can produce cavity pressure fluctuations exceeding 5% of peak pressure and intermittent short shots; this failure mode is avoidable by closed-loop dew point monitoring at the dryer outlet.
Melt stability in medium-flow ABS is governed by the interaction between conductive barrel heat, shear heating, and residence time. On a single-stage general-purpose screw with an L/D of 20:1 and a compression ratio of 2.5:1, barrel set temperatures from rear to nozzle are commonly 190–210 °C, 200–220 °C, 210–230 °C, and 210–230 °C. Mold surface temperature should be maintained between 40 °C and 80 °C; the lower boundary reduces cycle time and surface gloss, while the upper boundary improves weld-line strength and reduces frozen-in orientation stress. Screw back pressure of 0.3–0.7 MPa and a screw surface speed of 0.15–0.30 m/s are suitable for dispersion of color concentrates without excessive shear heating. Injection velocity should be profiled to sustain a flow-front velocity of 100–300 mm/s in cavities of 1.5–3.0 mm wall thickness. Thin-wall sections below 1.0 mm usually require a higher-flow ABS class rather than elevated melt temperature alone, because raising barrel temperatures above 245 °C accelerates polybutadiene phase degradation and increases yellowing.
For mold filling, peak hydraulic injection pressure should be set below 80% of the machine’s rated capacity, leaving margin for velocity-controlled filling. Gate land length should be 0.5–1.0 mm for side-edge gates, and gate thickness should be 60–80% of nominal wall thickness to maintain packing efficiency. Cold-runner diameters below 4 mm in multi-cavity tools can freeze prematurely and create cavity-to-cavity packing imbalance; full-round or trapezoidal runner cross-sections with a surface finish of 0.8 µm Ra or better are recommended. Cooling channel layout should target a mold-face temperature difference below 5 °C; larger differentials generate differential shrinkage and out-of-plane bow. Mold shrinkage for the medium-flow ABS class, measured on plaques according to ISO 294-4:2018, is typically 0.3–0.7% in the flow direction and 0.4–0.8% transverse, but the exact values depend on filler, pigment, wall thickness, and hold pressure.
Incoming-lot verification should use the matrix below. The numerical columns represent typical acceptance classes for medium-flow ABS, not guaranteed product values unless reproduced on the Guangzhou Keyuan certificate of analysis.
| Check | Test method | Typical medium-flow ABS acceptance class |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 | 8–12 g/10 min at 220 °C/10 kg |
| Moisture content | ISO 15512:2019 | ≤ 0.08% |
| Tensile yield stress | ISO 527-2:2012 | 40–50 MPa |
| Nominal tensile strain at break | ISO 527-2:2012 | 10–25% |
| Flexural modulus | ISO 178:2019 | 2100–2500 MPa |
| Charpy notched impact | ISO 179-1:2010 | 15–25 kJ/m² at 23 °C |
| Deflection temperature | ISO 75-2:2013 method A | 90–105 °C at 1.8 MPa |
| Flammability | UL 94 | Typically HB at 1.5 mm or 3.0 mm for non-FR form |
Differences from other ABS grades are principally rheological and thermal. Compared with high-flow injection grades in the 20–30 g/10 min interval, the nominal 8–12 g/10 min class exhibits shorter flow length in a 2 mm spiral-flow mold under equivalent injection pressure and melt temperature, which restricts filling in walls below 1.0 mm but retains higher notched impact energy and lower in-plane mold shrinkage anisotropy under ISO 294-4:2018. Against low-flow extrusion grades below 5 g/10 min, ABS 810 class materials fill multi-cavity tools at lower hydraulic pressure and with shorter fill times, but their reduced melt strength limits sheet extrusion, thermoforming, and thick-walled profile extrusion where draw-down stability is required. Compared with heat-resistant ABS grades with Vicat softening temperatures above 110 °C under ISO 306:2022 method B50, this medium-flow class softens generally between 100 °C and 106 °C and should not be specified for continuous service above 85–90 °C where creep modulus retention under load declines sharply.
In multi-gate or multi-cavity tools, flow fronts converge and form weld lines whose mechanical strength is systematically below the bulk material. For ABS copolymers, the loss is driven by incomplete chain interdiffusion at the melt interface and by local orientation of the polybutadiene phase. The weld-line retention of notched Charpy impact strength under ISO 179-1/1eA can fall to 30–50% of bulk values when the flow-front temperature at convergence drops below the Vicat softening temperature measured under ISO 306:2022 plus 60 °C. Molders should maintain mold surface temperature at the upper end of the 40–80 °C window, use sequential valve-gate actuation to reposition weld lines away from load-bearing bosses or snap-fit features, and install cavity pressure transducers with ranges up to 200 MPa near last-fill zones. Venting at the weld line should be at least 0.02 mm deep with a land length of 1.0–2.0 mm to prevent gas entrapment and diesel-effect burn marks. For hot-runner valve gates, the gate orifice should be sized for a shear rate below 50,000 s⁻¹ to limit local melt-temperature rise.
Packing pressure should be set between 50% and 70% of peak injection pressure. Gate-seal time for a 2.5 mm wall is commonly 4–8 s, but must be confirmed by cavity pressure decay rather than estimated from cycle time. If weld lines remain visible after normal processing, increased melt temperature within the allowed range and reduced injection velocity near the convergence zone can improve surface merging, but these adjustments must not push melt temperature above 245 °C or residence time above 10 min at 240 °C.
Application scope for the ABS 810 class includes electrical enclosure components, appliance housings, business machine panels, and automotive interior trim brackets. In electrical enclosures, the material is usually specified for non-live parts requiring dimensional stability, with post-mold shrinkage of 0.4–0.6% under ISO 294-4:2018 and 24-h water absorption below 0.3% under ISO 62:2008. For unattended appliance enclosures, glow-wire testing under IEC 60695-2-11:2021 should be conducted on the final pigmented formulation because non-FR ABS can show variability between 550 °C and 650 °C depending on thickness and colorants. Appliance housings require resistance to household cleaners and vegetable oils; these exposures should be evaluated using ASTM D543-21 on molded plaques with residual stress comparable to production parts. Automotive interior trim parts subjected to solar load require heat aging under ISO 2578:1993 at 90 °C for short-term exposure, but ABS 810 class materials are not suitable for continuous underhood use above 105 °C or for parts in direct contact with aggressive plasticizers.
The thermal degradation window is the most severe boundary in hot-runner or extended-cycle molding of medium-flow ABS. At melt temperatures above 250 °C, the polybutadiene phase undergoes oxidative and unsaturated-bond reactions that produce yellowing, gloss loss, and a measurable reduction in notched Charpy impact energy under ISO 179-1:2010. Total residence time above 240 °C should not exceed 15 min; at 260 °C, the allowable residence time falls below 5 min for color-sensitive natural or light-colored parts. Degradation onset can be monitored by capillary rheometry under ASTM D3835-16 using a die with L/D of 20:1 and a melt-temperature sweep of 220 °C, 230 °C, and 240 °C. A rise in apparent viscosity at low shear after extended holding indicates crosslinking or phase aggregation; a fall indicates chain scission. Hot-runner manifolds should use externally heated, thermally profiled zones with sheath temperatures not exceeding 260 °C, and shut-off nozzles should be positioned to minimize dead spots. In vented extrusion on a 32:1 L/D twin-screw machine, barrel zone settings above 240 °C and screw speeds above 80 min⁻¹ can initiate degradation when the screw fill ratio exceeds 0.75; a low fill ratio reduces residence-time distribution and prevents stagnation in partially filled screw channels.
Chemical incompatibility and regulatory testing complete the specification review for ABS 810. The resin swells or dissolves in ketones, esters, aromatic hydrocarbons, and chlorinated solvents; environmental stress cracking can occur under molded-in residual stress when parts are wiped with ketone-based cleaners. Compatibility under simultaneous load and chemical exposure should be tested according to ASTM D543-21 on plaques with residual stress equivalent to production parts. For electrical enclosure materials, comparative tracking index should be verified according to IEC 60112:2020 on the exact pigmented formulation; natural medium-flow ABS commonly exceeds 600 V, but carbon black and certain color concentrates can reduce tracking resistance. REACH and RoHS declarations must be obtained from Guangzhou Keyuan New Material for the specific lot because batch-level additive packages and recycled content can alter regulatory compliance. Avoid combination with amine-based or strongly alkaline color concentrates that can accelerate degradation of the styrene-acrylonitrile phase during long melt residence.