| HS Code | 877806 |
| Manufacturer | Guangdong YinXi |
| Product Name | ABS ABS3360E |
| Material Type | Acrylonitrile Butadiene Styrene (ABS) |
| Grade | ABS3360E |
| Appearance | Pellets |
| Processing Method | Injection Molding |
| Density | 1.18 g/cm³ |
| Melt Flow Rate | 20 g/10 min |
| Tensile Strength | 45 MPa |
| Flexural Strength | 70 MPa |
| Flexural Modulus | 2200 MPa |
| Izod Notched Impact Strength | 10 kJ/m² |
| Heat Deflection Temperature | 75 °C |
| Vicat Softening Temperature | 95 °C |
| Flame Retardancy | UL94 V-0 |
As an accredited Guangdong YinXi ABS ABS3360E factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Guangdong YinXi ABS ABS3360E is supplied in 25 kg moisture-resistant woven bags, palletized for industrial shipment and storage. |
| Container Loading (20′ FCL) | Guangdong YinXi ABS ABS3360E is loaded into a 20-foot FCL container with standard export packaging and secure stowage for shipment. |
| Shipping | Guangdong YinXi ABS ABS3360E is a non-hazardous thermoplastic resin, typically shipped in 25 kg moisture-proof bags or bulk sacks. Transport in clean, dry, ventilated containers, away from direct sunlight, heat, and moisture; avoid sharp impacts and follow MSDS handling requirements. |
| Storage | Store Guangdong YinXi ABS ABS3360E in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed to prevent moisture, dust, and contamination. Avoid contact with strong oxidizers and solvents. Maintain good housekeeping, prevent static buildup, and follow the SDS and local regulations. |
| Shelf Life | Guangdong YinXi ABS ABS3360E has a shelf life of about 12 months when stored dry, cool, ventilated, and in unopened original packaging. |
Publicly available English-language data for Guangdong YinXi ABS ABS3360E do not provide a complete ISO 2580-1 designation block; a production release must therefore be based on the lot-specific certificate of analysis, including melt volume-flow rate under ISO 1133-1 at 220 °C with a 10 kg load, residual styrene/acrylonitrile, and notched Izod impact under ISO 180. The downstream tracks below are restricted to established unfilled ABS conversion routes and identify the standards, equipment constraints, and failure modes that control each route.
Vacuum-assisted plug forming of refrigerator inner liners from ABS sheet imposes a biaxial orientation state that differs fundamentally from the uniaxial melt flow in the sheet die. For ABS3360E sheet extrusion, a 90 mm single-screw extruder with L/D 33:1, a barrier screw, and a gear pump is the baseline equipment configuration; the gear pump is required to steady die pressure at 8–12 MPa because the butadiene rubber phase creates melt-pressure pulsation under starve-fed conditions. Pellets are dried in a desiccant dryer at 80 °C for 2–4 h to a moisture content below 0.05% by ISO 15512. The barrel profile is normally set from 210 °C to 240 °C, with the flexible lip die held at 230 °C. Roll temperatures are kept between 80 °C and 105 °C; the upper limit is fixed by gloss banding, while the lower limit increases frozen-in stress and stress whitening at trim lines. Thermoforming is conducted at sheet surface temperatures of 140–180 °C, below which webbing occurs at deep-draw plug corners, and above which butadiene-phase thermo-oxidative degradation releases detectable volatile organics. Colour masterbatch should be based on a styrenic carrier and used at a let-down ratio no greater than 2% by mass, because higher dilution shifts low-temperature impact and gloss. The formed liner requires compliance with FDA 21 CFR 180.22 and EU Regulation (EU) No 10/2011 when it is intended for food-contact or odour-sensitive refrigerator compartments; overall migration limits are determined according to EN 1186-1 and should not exceed 10 mg/dm². Terminal products are refrigerator inner liners, door liners, and dairy-case thermoformed trays. This grade should not be used for hot-fill equipment or continuous service above 70 °C because long-term creep under thermomechanical load causes door-seal flange distortion.
Instrument panels, A/B/C-pillar covers, and door trim substrates produced from ABS3360E require the injection mould to be gated for uniform packing because the coefficient of linear thermal expansion of unfilled ABS measured by ISO 11359-2 is typically 7 × 10⁻⁵ K⁻¹ to 9 × 10⁻⁵ K⁻¹, higher transverse to flow; differential shrinkage at rib roots produces sink marks and visible gloss differences on grained surfaces. Drying to below 0.03% moisture at 80 °C for 3–4 h is mandatory before melt processing. The melt temperature at the nozzle is held at 230–250 °C, and the tool surface is maintained at 40–70 °C to balance flow length and grain reproduction. Hold pressure is set between 40 MPa and 70 MPa; back pressure is limited to 0.5–1.5 MPa to avoid excessive rubber-phase shear heating and yellowing. If the part is painted, ≥38 mN/m surface energy after plasma or corona treatment is required for adhesion of two-component polyurethane topcoats. Amine-based mould-release agents are incompatible because they block isocyanate crosslinking and produce fish-eye defects. Flammability is controlled under FMVSS 302 / 49 CFR 571.302, with a horizontal burn rate not exceeding 102 mm/min for production specimens. Interior emissions are assessed by VDA 278 thermal desorption; ABS grades without post-polymerisation stripping may emit styrene and 4-phenylcyclohexene, so the moulder should request an emissions-reduced lot if the assembler’s specification sets total VOC below 100 µg/g. Terminal products are pillar covers, door panel inserts, and console side panels.
In low-voltage distribution mouldings, the absence of flame-retardant additives changes the compliance route from glow-wire to horizontal burn classification. ABS3360E can be injection moulded into enclosure bases, blanking plates, and DIN-rail housings with wall thicknesses of 2.5–4.0 mm. A mould temperature of 50–80 °C and a melt temperature of 220–250 °C are typical, with packing pressure held at 60–80 MPa for 8–15 s to minimise sink over bosses. Flow length should not exceed 120:1 at 2.5 mm wall section, because hesitation at rib-to-wall intersections creates knit lines with reduced notched impact. Electrical enclosure flammability is verified under IEC 60695-11-10 as an HB classification at 3.0 mm; general-purpose ABS is not a glow-wire ignition-resistant compound at 750 °C. The processor must conduct a full IEC 60695-2-11 glow-wire test at the final wall thickness before any declaration for unattended appliance use. For low-voltage safety, insulation resistance and tracking resistance should be verified by IEC 62631-3-1 and IEC 60112. Terminal products are consumer distribution board covers, DIN-rail enclosures, and switch mounting plates. The material is not recommended for outdoor enclosures unless UV stabilised and not recommended where ketone-based cleaning solvents contact stressed bosses.
Hydrostatic pressure testing of ABS extrudate is governed by ISO 1167, and the material designation is placed under ISO 15493-1 for industrial piping systems. ABS3360E may be used for non-pressure drainage pipe and injection-moulded fittings only when the lot certificate confirms a hydrostatic design basis; the grade must not be placed in pressure service on the basis of nominal melt flow or notched impact alone. Pipe extrusion on a 60 mm single-screw extruder with L/D 30:1 typically uses a melt temperature of 210–230 °C and a die temperature of 190–210 °C; vacuum calibration is run with water at 20 °C and a vacuum of 0.4–0.8 bar. Fittings are injection moulded at 220–250 °C with a mould temperature of 60 °C. The critical failure modes are knit lines at core-pin bosses and gate blush on thin sealing faces; both are managed by using multiple tab gates and by keeping the flow path below 100:1 at the boss root. Notch sensitivity is assessed by ISO 180 Izod impact, but the pipe-specific requirement is resistance to slow crack growth; qualification therefore requires ISO 1167 hoop-stress testing at 20 °C and 60 °C, not only laboratory impact data. Terminal products are industrial drainage pipes, solvent-welded fittings, and aeration lines. If the grade is assembled with solvent cements, the cement must be certified for ABS and must not contain methyl ethyl ketone as the primary solvent at high residual stress, because ketone swelling at weld fillets accelerates environmental stress cracking.
| Application segment | Critical standard designation | Test condition or threshold | Purpose |
|---|---|---|---|
| Refrigerator liner | FDA 21 CFR 180.22 / EU 10/2011 | Overall migration ≤ 10 mg/dm² by EN 1186-1 | Food-contact compliance |
| Automotive trim | FMVSS 302 / 49 CFR 571.302 | Horizontal burn rate ≤ 102 mm/min | Interior flammability |
| Automotive emissions | VDA 278 | VOC/FOG thermal desorption after specified cycles | Odour and fogging |
| Electrical enclosure | IEC 60695-11-10 | HB classification at 3.0 mm | Flammability classification |
| Electrical tracking | IEC 60112 | Comparative tracking index on final moulding | Low-voltage safety |
| Pipe fitting | ISO 1167 / ISO 15493-1 | Hoop stress at 20 °C and 60 °C | Hydrostatic pressure resistance |
| Luggage shell | ISO 6603-1 / ISO 4892-2 | Puncture at 4.4 m/s and −20 °C | Impact and weathering |
| Small appliance housing | RoHS 2011/65/EU / IEC 62321 | Pb, Hg, Cr6+, PBB, PBDE ≤ 0.1%; Cd ≤ 0.01% | Restricted substance compliance |
Historically, ABS shell stock has been used in hard-sided luggage because the rubber-phase toughening delays crack propagation at corner radii. For ABS3360E, sheet is extruded at 2–4 mm thickness on a single-screw line without a gear pump if a barrier screw is used, then thermoformed on a plug-assisted machine at sheet surface temperatures of 150–180 °C. Twin-sheet forming of luggage shells requires matched thermal history of both sheets; mismatched sag depth across the oven zone causes hinge misalignment after trimming. The formed shell must pass puncture impact under ISO 6603-1 at 4.4 m/s and −20 °C to avoid brittle corner failures during baggage handling. UV stabilisation is not optional for this application; unpigmented ABS should not be specified, and validation is by ISO 4892-2 xenon-arc exposure with no surface chalking before the agreed exposure interval. Adhesive bonding of inner frames or textile linings uses moisture-curing polyurethane adhesives; solvent-borne chloroprene adhesives must be qualified for stress-crazing resistance because ABS under thermoformed residual stress is susceptible to ketone and aromatic hydrocarbon attack. Compliance for European retail goods is tied to REACH Regulation (EC) No 1907/2006, Annex XVII entry 50 for polycyclic aromatic hydrocarbons, and AfPS GS 2019:01 PAH. Terminal products are hard-shell luggage, cosmetic cases, and instrument cases.
When the melt is processed on a 120–180 t toggle-clamp machine with a 30–40 mm screw and L/D 20:1, ABS3360E can replace HIPS in vacuum cleaner canisters, power tool shells, and sewing machine covers because its butadiene content raises notched impact without requiring a separate elastomer masterbatch. Drying is carried out at 80 °C for 2–4 h to below 0.05% moisture. The nozzle melt temperature is held at 230–250 °C; injection velocity is set at 80–150 mm/s for thin-wall sections down to 2.0 mm. The hold pressure is 50–70 MPa, and cooling time is 15–25 s depending on wall thickness. The switch from HIPS requires adjustment of the screw decompression stroke because ABS has a narrower melt elasticity window; excessive suck-back can cause air venting at the check ring, while insufficient decompression produces drool at the nozzle. For small appliance enclosures, adherence to RoHS Directive 2011/65/EU Annex II is verified using IEC 62321 methods; maximum concentration values are 0.1% by weight for lead, mercury, hexavalent chromium, PBB and PBDE, and 0.01% for cadmium. Cosmetic surfaces can be textured or painted; when painting is specified, stress-relief annealing at 70 °C for 2 h before coating reduces solvent crazing. Chemical compatibility must be checked against cooking-oil aerosols and citrus-based cleaners because these fluids cause environmental stress cracking in ABS at moulded-in stress concentrations such as screw bosses and snap-fit undercuts. Terminal products are vacuum cleaner housings, power tool clamshells, and home appliance front panels. Continuous local surface temperature should remain below 70 °C; higher temperatures require a polycarbonate/ABS or heat-stabilised grade.
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Guangdong YinXi ABS3360E is an acrylonitrile-butadiene-styrene terpolymer grade intended primarily for extrusion and thermoforming rather than high-gloss injection moulding. The material is a two-phase system in which polybutadiene rubber particles are grafted to a styrene-acrylonitrile continuous phase. Published manufacturer datasheets for ABS3360E remain limited in consolidated international databases; the following sections therefore use category-typical ranges for medium-high impact extrusion ABS and require replacement with lot-specific certificate-of-analysis values where available. Melt volume-flow rate under ISO 1133-1:2022 at 220 °C/10 kg is expected to lie between 4 cm³/10 min and 10 cm³/10 min. Density under ISO 1183-1:2019 is 1.03–1.07 g/cm³. Notched Izod impact under ISO 180/1A:2019 at 23 °C is typically 30–45 kJ/m². The CAS registry number for the ABS terpolymer is 9003-56-9. The neat resin is not a flame-retarded system and is normally classed HB under UL 94 at 1.5 mm and 3.0 mm; coloured or filled lots must be retested.
Moisture control is the first processing boundary. ABS granules equilibrate at 0.15–0.3 wt% moisture under 23 °C/50% RH; extrusion sheet requires residual moisture below 0.05 wt%. A closed desiccant dryer with dew point ≤ -30 °C, air temperature 80–90 °C, and residence time 2–4 h is the minimum condition. Inadequate drying causes hydrolysis-induced splay, microvoiding, and melt-pressure fluctuation, which appear as optical haze and gauge irregularity. The barrel profile should begin at 180–190 °C at the feed throat and rise to 210–225 °C at the die adaptor. Melt temperature should not exceed 250 °C; decomposition above this threshold produces yellowing, styrene odour, and measurable loss of notched Izod impact. Melt residence time should remain below 10 min. A single-screw extruder with L/D 30–36, compression ratio 2.5:1–3.0:1, and a 60/100 mesh screen pack provides suitable plastication and filtration. Published data for lot-to-lot variation of ABS3360E are limited; each batch should be verified against the certificate of analysis before line start-up.
On a flat-die sheet line equipped with a 120 mm single-screw extruder at L/D 36, a gear pump, and a 100/200 mesh screen pack, gear-pump inlet pressure is typically 8–15 MPa; sustained excursions above 18 MPa indicate gel or degraded rubber accumulation on the screen pack and require line interruption before gauge drift exceeds ±0.05 mm. The die lip gap is set 5–10% above target sheet thickness for draw-down; polishing-stack temperatures of 80–100 °C support gloss retention. Sheet from 0.8 mm to 6.0 mm is thermoformable. At sheet surface temperatures of 140–180 °C, sag behaviour is controlled by the high melt strength of the extrusion grade; heavy-gauge forming uses aluminium or epoxy tooling at 70–90 °C to avoid premature freeze-off. Thin-gauge parts below 0.4 mm require sheet gauge tolerance tighter than ±0.08 mm. Polished-sheet gloss measured at 60° under ASTM D523-14 is typically 85–95 GU; textured or matte surfaces fall to 10–35 GU depending on embossing depth.
Shear thinning is pronounced in extrusion ABS. Capillary rheometry at 220 °C shows apparent viscosity of 300–700 Pa·s at 1000 s⁻¹, increasing to 900–1800 Pa·s at 100 s⁻¹; these are category-typical values, not lot-specific ABS3360E curves. Die swell ratios of 1.3–1.8 are common in sheet ABS, affecting edge bead and trim recycle rates. External lubricants and low-molecular-weight processing aids may bloom to polished surfaces during long thermoforming campaigns, reducing printing and coating adhesion. Corona treatment typically raises surface energy from 34–38 mN/m as delivered to 44–48 mN/m; if flame treatment is used, a line speed below 15 m/min at 2 kW minimises gloss loss. Downgauge limits are not determined by tensile modulus alone; multiaxial impact retention can decline steeply below 0.4 mm when sheet orientation is lost. Use of regrind above 30 wt% increases black speck risk and shifts melt flow sufficiently to alter die swell.
Where lot-specific data are absent, procurement specifications should be based on the following category-typical envelope for medium-high impact extrusion ABS. The values are drawn from public ISO/ASTM method compilations and should be replaced with ABS3360E certificate-of-analysis values.
| Property | Test method | ABS3360E extrusion class | High-gloss injection ABS |
|---|---|---|---|
| Melt volume-flow rate | ISO 1133-1:2022 | 4–10 cm³/10 min | 20–40 cm³/10 min |
| Density | ISO 1183-1:2019 | 1.03–1.07 g/cm³ | 1.04–1.06 g/cm³ |
| Tensile yield stress | ASTM D638-14 | 37–48 MPa | 40–50 MPa |
| Tensile elongation at break | ASTM D638-14 | 10–30% | 5–20% |
| Flexural modulus | ASTM D790-17 | 2000–2600 MPa | 2200–2800 MPa |
| Notched Izod impact, 23 °C | ISO 180/1A:2019 | 30–45 kJ/m² | 10–20 kJ/m² |
| Heat deflection temperature, 1.8 MPa | ASTM D648-16 | 85–100 °C | 90–105 °C |
| Vicat softening temperature | ISO 306/B50:2013 | 95–108 °C | 95–110 °C |
| Rockwell hardness, R scale | ASTM D785-15 | 100–110 | 105–115 |
| Mould shrinkage | ISO 294-4:2018 | 0.4–0.7% | 0.3–0.6% |
| 60° gloss, polished surface | ASTM D523-14 | 85–95 GU | 95–102 GU |
| Die swell ratio | Capillary rheometry | 1.3–1.8 | 1.1–1.4 |
If ABS3360E is diverted to injection moulding at clamp forces between 80 t and 150 t, melt temperature 220–240 °C, mould temperature 40–80 °C, and holding pressure 50–80 MPa are typical. Because the grade is extrusion-optimized, flow-length-to-wall-thickness ratio is lower than that of high-flow injection ABS grades; published data for ABS3360E in thin-wall injection are limited, and spiral-flow trials should be executed before tool commit. Short shots in hot-runner systems with manifold temperatures above 250 °C signal degradation rather than insufficient fill speed.
High-gloss injection ABS typically exhibits melt volume-flow rates above 20 cm³/10 min and notched Izod impact of 10–20 kJ/m²; it yields thin-wall moulding gloss above 95 GU but lacks the melt strength required for heavy-gauge sheet. ABS3360E is positioned at the opposite end: lower flow, higher rubber content, and higher thermoforming sag resistance. Flame-retarded ABS usually contains brominated flame retardants plus antimony trioxide; its density rises to 1.17–1.22 g/cm³, notched Izod impact falls to 8–18 kJ/m², and UL 94 can reach V-0 at 1.5 mm. Neat ABS3360E remains HB, avoiding the narrow thermal degradation window associated with FR packages. High-heat ABS based on α-methylstyrene increases heat deflection temperature at 1.8 MPa to 105–120 °C but sacrifices flow and impact; ABS3360E remains below 100 °C under ASTM D648-16 in most variants. PC/ABS offers heat deflection of 110–125 °C, density 1.12–1.18 g/cm³, and low-temperature impact retention, but has higher cost and different chemical resistance; ABS3360E cannot substitute for PC/ABS in instrument-panel skeletons requiring sub-zero ductility without part redesign.
For regulatory and compliance screening, ABS3360E should be verified under the following matrix. Base ABS polymers generally meet RoHS Directive 2011/65/EU Annex II limits; however, additives, colorants, and recycled regrind may alter compliance, so lot-level test reports are required.
| Standard or regulation | Substance or parameter | Typical limit or condition |
|---|---|---|
| RoHS 2011/65/EU Annex II | Lead, mercury, hexavalent chromium, PBB, PBDE | <1000 mg/kg per substance |
| RoHS 2011/65/EU Annex II | Cadmium | <100 mg/kg |
| RoHS 2011/65/EU Annex II | DEHP, BBP, DBP, DIBP | <1000 mg/kg each |
| REACH (EC) No 1907/2006 Candidate List | SVHC | No intentionally introduced SVHC; lot confirmation required |
| UL 94 | Flammability, neat resin | HB at 1.5 mm and 3.0 mm |
| FDA 21 CFR 177.1020 | Food-contact ABS copolymer | Migration testing and formulation verification required |
| Regulation (EU) 10/2011 Annex I | Overall migration | ≤10 mg/dm² for general plastic food-contact use |
Chemical incompatibilities for ABS3360E include ketones, esters, chlorinated hydrocarbons, and aromatic solvents; these agents induce environmental stress cracking in formed parts. Contact with polyacetal, PVC, or PLA in mixed regrind streams should be avoided because thermal degradation by-products can accelerate ABS chain scission. Outdoor exposure without a UV stabilizer package leads to yellowing and gloss loss under ISO 4892-2:2013 xenon-arc conditions; for UV-stable sheet, the lot certificate should explicitly state the stabilizer package and test result. Published data for ABS3360E in outdoor weathering configurations is limited, so service-life claims require validation on the actual formed part.