| HS Code | 668736 |
| Manufacturer | Guangdong Wanxi |
| Productname | ABS 111 |
| Grade | 111 |
| Materialtype | Acrylonitrile Butadiene Styrene (ABS) |
| Appearance | Opaque pellets |
| Density | 1.05 g/cm³ |
| Meltflowrate | 15 g/10 min (220°C/10 kg) |
| Tensilestrength | 45 MPa |
| Elongationatbreak | 20% |
| Flexuralmodulus | 2300 MPa |
| Notchedizodimpactstrength | 200 J/m (23°C) |
| Heatdeflectiontemperature | 85°C (1.82 MPa) |
| Vicatsofteningtemperature | 95°C |
| Rockwellhardness | 105 R |
| Moldingshrinkage | 0.4–0.6% |
| Waterabsorption | 0.2% (24 h) |
| Ul94flammabilityrating | HB |
As an accredited Guangdong Wanxi ABS 111 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Guangdong Wanxi ABS 111 is supplied in 25 kg moisture-proof paper bags, palletized for industrial handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Guangdong Wanxi ABS 111, securely packed on pallets and shrink-wrapped for export shipment. |
| Shipping | Guangdong Wanxi ABS 111 is shipped as a non-hazardous thermoplastic resin in moisture-barrier bags, woven sacks, or bulk containers. Store in a cool, dry, ventilated area away from sunlight, heat, and ignition sources. Handle carefully to prevent rupture and contamination; no special dangerous-goods classification is typically required. |
| Storage | Store Guangdong Wanxi ABS 111 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, moisture, ignition sources, and oxidizing agents. Keep containers tightly closed and prevent dust generation or static buildup. Avoid prolonged high-temperature and UV exposure. Stack properly to prevent package damage, use spill containment, and follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Store in a dry, ventilated area away from sunlight and moisture; typical shelf life is 12 months in unopened packaging. |
On 120–180 tf hydraulic injection molding lines producing thin-wall information and communication technology enclosures from Guangdong Wanxi ABS 111, the practical lower wall-thickness boundary at flow lengths of 200–250 mm is usually 1.8–2.2 mm because the melt front freezes below 190°C at low injection velocity and residual moisture above 0.05 wt% produces splay at the gate and along weld lines. The controlling compliance boundary for finished assemblies is IEC 62368-1:2023, with horizontal burn classification tested to IEC 60695-11-10:2013 and substance restrictions under RoHS 2011/65/EU Annex II and REACH SVHC at 0.1 wt%. Formulation addition ratio starts at 100 phr ABS 111, 0.2–0.5 phr hindered phenolic antioxidant, 2–4 phr color masterbatch, and 0.1–0.4 phr calcium stearate mold release; antistatic masterbatch at 0.5–1.5 phr is introduced only where surface resistivity below 10^10 Ω/sq is specified. The downstream process uses desiccant drying at 80°C for 2–4 h to reach residual moisture below 0.05 wt%, barrel profile 210/225/240/235°C, nozzle 235°C, mold 40–60°C, injection velocity 80–120 mm/s, hold pressure 55–70 MPa, and cooling time 12–18 s for a 2.0 mm nominal wall. Finished part types include router housings, set-top box covers, UPS enclosures, monitor back covers, and cable modem shells.
On production lines, the dominant failure modes are short shots at rib and boss intersections when the melt front stalls below 190°C, and splay when residual moisture exceeds 0.05 wt%. Batch-to-batch variation in melt mass-flow rate measured by ISO 1133-1:2022 at 220°C/10 kg appears as fill time drift of 0.3–0.8 s, so a cushion of 3–6 mm is maintained and switchover position is set by screw stroke rather than timer. Tooling uses vent depths below 0.02 mm to avoid flash, and cold-runner subgate diameters of 2.0–2.5 mm to balance pressure drop. Tensile and flexural data used for section design are generated to ASTM D638-14 and ISO 178:2019, but designer allowable values must be confirmed on the lot certificate for ABS 111 rather than a generic ABS datasheet.
In high-gloss washing machine top covers and air purifier shells molded from ABS 111, uneven cavity surface temperature gradients rather than hydraulic hold pressure often drive post-ejection bowing. When the fixed half of the tool is held at 50°C and the moving half falls to 30°C due to unbalanced cooling circuits, differential solidification creates warpage in grain-across wall parts of 2.5 mm nominal thickness and projected areas above 1,200 cm². The relevant appliance standards are IEC 60335-1:2020 and glow-wire testing to IEC 60695-2-11:2021 at 750°C for unattended appliance enclosures, with traceability under REACH and RoHS 2011/65/EU. Starting loadings are 100 phr ABS 111, 0.2–0.5 phr antioxidant, 2–4 phr pigment masterbatch, and 0.5–1.5 phr silicone lubricant; a high-gloss black version may use 0.05–0.2 phr carbon black dispersion rather than an additional wax. Conversion uses desiccant drying at 80°C for 3 h, barrel 220–245°C, mold 50–70°C, sequential valve gating, hold pressure 60–80 MPa, and initial fill velocity 60–100 mm/s; after ejection, parts are placed on flat fixtures because stress relaxation at ambient humidity can change camber by 0.2–0.5 mm. Finished articles include washing machine top covers, refrigerator drawer front panels, vacuum cleaner housings, air purifier shells, and electric kettle base surrounds. Cleaning-agent resistance must be tested under ISO 22088-3:2008 using isopropanol or fabric softener wiping because visual stress cracking can appear after 24 h at 0.5% strain.
At ambient relative humidity above 60%, pre-drying time is extended to 4 h to prevent surface gloss loss and gas marks at the gate. Regrind is typically limited to 20 wt% because higher fractions shift melt viscosity and produce visible gloss banding on the cavity surface.
Following separate drying of polycarbonate and ABS 111, automotive interior trim programs requiring higher heat resistance than neat ABS use PC/ABS compounds in which ABS 111 is added at 60–80 wt% with PC pellet at 20–40 wt%, plus 0.3–0.8 phr phosphite antioxidant and 0.3–0.6 phr mold release. The resulting Vicat softening temperature shifts from 95–100°C to 115–130°C depending on PC content, but notched Izod impact can fall below 15 kJ/m² if PC pellet moisture is not kept below 0.02 wt%. The controlling standards for interior trim are FMVSS 302 and ISO 3795:1989 with a burn rate below 100 mm/min, ELV 2000/53/EC Annex II limits for lead, cadmium, mercury and hexavalent chromium, and OEM fogging and odor limits measured by VDA 278:2011. Production-scale limitations appear first in the PC drying stage: PC pellets must be dried at 120°C for 4 h, ABS 111 at 80°C for 3 h, then dosed gravimetrically to avoid separation caused by pellet size difference. Twin-screw compounding with an L/D ratio of 40:1 uses barrel zones 250–270°C, screw speed 300–500 rpm, and melt temperature below 280°C; injection molding runs with barrel 250–270°C, mold 70–90°C, back pressure 0.3–0.6 MPa, and total residence time below 8 min to limit PC molecular weight loss. Boss retention is qualified by screw-driving torque and pull-out force on bosses with a diameter of at least 2.5× the screw nominal diameter; failures occur at the boss root when mold temperature drops below 65°C because frozen-in stress reorients the outer skin. End products include center console side panels, glove box surrounds, door trim inserts, lower B-pillar covers, and speaker grille frames. Published data for ABS 111 specifically at PC contents below 70 wt% is limited; each tool should be qualified with instrumented falling-dart impact at 23°C, −10°C, and −30°C.
At the gate, melt shear rate above 25,000 s⁻¹ can induce surface delamination between the PC-rich skin and ABS-rich core, so gate diameters are kept above 2.0 mm and injection velocity is staged to avoid jetting. Tooling for automotive interior parts also requires high polish on cavity surfaces but textured grain on exterior surfaces to hide knit lines; this dual finish changes the thermal contact coefficient and must be accounted for in cooling time predictions.
Because melt fronts recombine behind ribs or bosses in molded toy shells, drop-impact energy absorption from Guangdong Wanxi ABS 111 is governed more by knit-line placement than by bulk Izod data; local notched impact at a knit line can fall to 8–12 kJ/m² while the virgin sheet records 15–25 kJ/m² under ASTM D256-23. Compliance is driven by EN 71-3:2019+A1:2021 for migration of 19 elements, ASTM F963-23, REACH Annex XVII restrictions, and CPSIA Section 108 for phthalate content. Material loadings under this compliance boundary are 100 phr ABS 111, 2–4 phr color masterbatch, 0.2–0.5 phr hindered phenolic antioxidant, and 0.1–0.3 phr mold release; no phthalate plasticizer is added because the article must remain free of the restricted phthalate list. Conversion uses desiccant drying at 80°C for 2–4 h, barrel 200–230°C, mold 30–50°C, injection velocity 60–100 mm/s, and a cushion of 3–5 mm to avoid unmelted color streaks. Finished part types include building block outer shells, action figure shells, ride-on toy body panels, play kitchen appliance panels, and remote-control toy chassis. For parts with through-holes smaller than 3 mm, molders must verify that edge radii meet the toy safety small-part limits, but the resin itself is selected for the shell rather than the small-part interface.
For wall plates longer than 120 mm, post-mold shrinkage anisotropy of 0.4–0.7% determines whether modular inserts seat without gapping; the cavity is pre-compensated by 0.6% in the flow direction and 0.4% in the transverse direction to hold 0.1 mm gap tolerance around modular insert openings. Standards are IEC 60669-1:2017 for switches for household and similar fixed electrical installations, glow-wire testing to IEC 60695-2-11:2021, and material traceability under RoHS 2011/65/EU. A lean formulation uses 100 phr ABS 111, 2–3 phr color masterbatch, 0.2–0.4 phr antioxidant, and 0.2–0.5 phr silicone lubricant; UV-stabilized masterbatch at 0.5–1.0 phr is added for prolonged indoor sunlight exposure. Production is a cold-runner injection process with barrel 210–240°C, mold 40–60°C, initial injection velocity 70–100 mm/s, packing at 50 MPa for 6 s then 30 MPa for 4 s, and drying at 80°C for 2 h. Terminal article types include switch faceplates, socket covers, dimmer knobs, and modular front plates up to 146 mm length.
When diagnostic cart housings are disinfected with quaternary ammonium wipes, melt residence time and gate size determine whether ABS 111 survives repeated exposure without stress cracking. The relevant standards are IEC 60601-1:2012/AMD2:2020 for mechanical strength and enclosure integrity, ISO 14971:2019 for risk management, RoHS 2011/65/EU, and REACH SVHC reporting; ISO 10993-1 biological evaluation is not required for non-patient-contacting external housings. The specified formulation is 100 phr ABS 111, 0.2–0.5 phr antioxidant, 2–3 phr color masterbatch, and 0.5–1.5 phr antistatic additive where surface resistivity below 10^10 Ω/sq is specified; no DEHP or BPA is intentionally added. Conversion uses desiccant drying at 80°C for 3 h, barrel 210–240°C, mold 40–60°C, hot runner gates of 2.0–2.5 mm diameter, and post-molding annealing at 70°C for 2 h to reduce surface tensile stress. Finished part types include diagnostic cart housings, ultrasound monitor enclosures, infusion pump housings in non-patient-contact zones, and medical computer terminal covers. Cleaning validation uses ISO 22088-3:2008 with 30% isopropanol wipes or 0.1% quaternary ammonium solution at 23°C because the published data for ABS 111 under repeated alcohol disinfectant exposure is limited and must be confirmed on molded plaques before release.
Competitive Guangdong Wanxi ABS 111 prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618005193850
Email: sales8@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Guangdong Wanxi ABS 111 is classified as a medium-impact acrylonitrile-butadiene-styrene copolymer supplied for injection moulding, sheet extrusion, and profile extrusion. The grade identifier 111 designates a controlled-flow material within the manufacturer’s ABS range; it is separated from higher-flow grades by a lower melt mass-flow rate and from high-heat grades by a lower Vicat softening temperature. The material is supplied in pellet form and is intended for conversion on standard thermoplastics processing lines. Users should treat the data in this document as class-representative technical boundaries rather than a substitute for the lot-specific certificate of analysis issued by Guangdong Wanxi. Where published data for this specific configuration is limited, the corresponding boundary is identified as class-derived.
The control window for this resin is expressed through ISO and ASTM methods because ABS 111 is used across both Asian and North American manufacturing lines. Representative class values for medium-impact extrusion ABS, against which the lot certificate should be audited, are summarised in Table 1. The melt mass-flow rate under 220 °C and 10 kg load typically falls between 3 g/10 min and 6 g/10 min when tested to ISO 1133-1:2022. Tensile yield stress measured on injection-moulded Type 1A specimens at 50 mm/min crosshead speed is generally within 38–46 MPa by ISO 527-2:2012. Notched Charpy impact response at 23 °C is subject to specimen preparation and notch radius; values in the region of 18–28 kJ/m² are expected under ISO 179-1:2023/1eA. Thermal performance under load should be referenced to heat deflection temperature at 1.8 MPa flatwise, with class values of 84–90 °C by ISO 75-2:2013.
| Property | Class-representative range | Test standard | Measurement condition |
|---|---|---|---|
| Density | 1.04–1.06 g/cm³ | ISO 1183-1:2019 | 23 °C |
| Melt mass-flow rate | 3–6 g/10 min | ISO 1133-1:2022 | 220 °C, 10 kg |
| Melt volume-flow rate | 2.8–5.6 cm³/10 min | ISO 1133-1:2022 | 220 °C, 10 kg |
| Tensile yield stress | 38–46 MPa | ISO 527-2:2012 | 50 mm/min |
| Tensile elongation at yield | 2.5–3.5 % | ISO 527-2:2012 | 50 mm/min |
| Flexural modulus | 2000–2400 MPa | ISO 178:2019 | 2 mm/min |
| Flexural strength | 60–75 MPa | ISO 178:2019 | 2 mm/min |
| Charpy notched impact strength | 18–28 kJ/m² | ISO 179-1:2023/1eA | 23 °C |
| Charpy notched impact strength | 6–10 kJ/m² | ISO 179-1:2023/1eA | −30 °C |
| Heat deflection temperature | 84–90 °C | ISO 75-2:2013 | 1.8 MPa, flatwise |
| Vicat softening temperature B50 | 94–100 °C | ISO 306:2022 | 50 N, 50 °C/h |
| Mould shrinkage | 0.4–0.7 % | ISO 294-4:2018 | 60 × 60 × 2 mm |
| Moisture after drying | <0.05 % | Karl Fischer | 150 °C heating |
The lower bound of the melt-flow window is advantageous in sheet extrusion because melt strength resists draw-down and gauge thinning; the upper bound supports shorter filling paths in injection moulding. However, selecting a lot at the low-flow end can reduce impact strength if the moulded skin layer is highly oriented, while a high-flow lot can increase knit-line weakness in complex tool layouts. Injection moulders should therefore map both melt mass-flow rate and Charpy notch behaviour before changing supplier lots. Single-point melt-flow data do not capture shear thinning; capillary rheometry or spiral-flow trials should be used when validating thin-wall filling behaviour.
Material entering the hopper at a moisture concentration above 0.05 wt% will not necessarily produce immediately visible defects; the butadiene-rich phase absorbs moisture and releases it unevenly during melting, generating splay, silver streaking, and a measurable loss in notched impact strength. Desiccant drying at 80 °C for 2–4 h is the minimum practical boundary for production-scale handling, with a dew point of −40 °C or lower at the dryer inlet. In coastal southern China, where ambient relative humidity frequently exceeds 60 %, open containers should not be used for hot, humid-shift operations. The resin should be transferred in closed hopper-loading lines, and the hopper residence time should not exceed the dry-air residence time needed to reach 0.03–0.05 wt% residual moisture. Regrind generated from edge trim or sprues should be reintroduced at no more than 20 wt% of the total feed unless flat-die sheet trials confirm acceptable surface quality and impact retention. Above this level, variability in melt viscosity and butadiene particle size distribution can produce visible gel particles and inconsistent gloss on polished roll stacks. Equipment types that have shown stable processing with this material class include single-screw extruders with 30:1–36:1 L/D and barrier screws, or twin-screw extruders with 32:1–40:1 L/D, vacuum venting at −0.08 MPa, and closed-loop barrel temperature control. Melt temperature measured by immersion probe should be kept between 210 °C and 240 °C; barrel profiles from rear to nozzle typically range from 180 °C to 230 °C. Operating above 250 °C for extended residence periods accelerates butadiene-phase oxidation and shifts the melt toward lower impact strength and yellowing, which is an operational boundary that should not be inferred solely from melt-flow stability.
Production-scale lines have shown that batch-to-batch differences in butadiene rubber particle size distribution affect gloss and low-temperature impact even when melt mass-flow rate and density remain inside specification. Incoming inspection should therefore include notched Charpy at −30 °C and gloss measurement on a standard polished plaque in addition to routine melt-flow and moisture checks. Failure modes observed on manufacturing lines include splay from wet resin, gloss bands from uneven roll temperature, short shots from cold runner restrictions, and jetting when melt temperature falls below 210 °C. These defects are corrected by physical parameter adjustment rather than by additive use.
Substitution is not a direct drop-in operation. Because ABS 111 has a medium-flow architecture, an existing thin-wall tool designed for high-flow ABS with a melt mass-flow rate above 15 g/10 min may exhibit short shots or higher injection pressure unless gate diameters and runner dimensions are rebalanced. The comparison in Table 2 summarises class-level differences. In a high-heat application, replacing a grade with a Vicat softening temperature of 108–115 °C with ABS 111 at 94–100 °C reduces heat distortion margin; the part must be evaluated under the actual heat-soak protocol, not only by nominal Vicat value. Mould shrinkage for ABS 111 is typically 0.4–0.7 % according to ISO 294-4:2018, which may be lower than high-flow grades and require tool modification when dimensional tolerance bands are tighter than ±0.2 %. Packing pressure, holding time, and gate freeze-off should be revalidated with cavity pressure sensors rather than inferred from hydraulic pressure readings.
| Parameter | ABS 111 class | High-flow ABS class | High-heat ABS class | Test basis |
|---|---|---|---|---|
| Melt mass-flow rate | 3–6 g/10 min | 20–35 g/10 min | 1–4 g/10 min | ISO 1133-1:2022 |
| Notched Charpy impact | 18–28 kJ/m² | 8–15 kJ/m² | 15–25 kJ/m² | ISO 179-1:2023/1eA |
| Vicat B50 | 94–100 °C | 90–96 °C | 108–115 °C | ISO 306:2022 |
| Mould shrinkage | 0.4–0.7 % | 0.3–0.6 % | 0.5–0.8 % | ISO 294-4:2018 |
| Typical melt temperature | 210–240 °C | 200–230 °C | 240–260 °C | Immersion probe |
Sheet gauge between 0.8 mm and 3.5 mm is typical for ABS 111 in vacuum-formed appliance and sanitaryware panels; roll-stack temperatures of 80–95 °C are used on polished three-roll stacks to stabilise surface gloss. Extrusion-grade ABS with this impact range is also used for edge-banding, furniture profile, and non-structural automotive interior trim where heat load remains below the Vicat boundary. Before specifying this material for painted or electroplated surfaces, adhesion workflows must be validated against the supplier’s surface energy and mould release recommendations, because external lubricant systems can reduce paint wetting and plating peel strength. A production-scale flat-die line running ABS 111 at 1.5 mm gauge with high-gloss roll finish requires lower roll temperatures and higher line speeds than a high-impact extrusion grade because the melt stiffness of medium-impact ABS allows gauge retention at lower calender pressure. In injection moulding, melt temperature of 215–235 °C, mould surface temperature of 40–80 °C, and hydraulic holding pressure of 50–70 MPa are practical starting values; cavity pressure should be monitored to maintain consistent packing. Thin-wall housings below 1.0 mm wall thickness can be moulded, but flow length is limited by the grade’s medium-flow characteristics. Electronic enclosure applications that require a flame-retardant V-0 or V-2 classification must not be assumed; general-purpose ABS 111 is ordinarily rated no higher than UL 94 HB at 1.5 mm, and any end-use certification requires independent verification.
Chemical environment restrictions are similar to other ABS resins: prolonged contact with aromatic hydrocarbons, esters, ketones, and concentrated organic acids produces stress cracking or surface attack. Continuous service above 80 °C is not recommended under load; the material is not inherently UV-stable and must be coextruded or painted for outdoor exposure. The medium-impact architecture also means that parts requiring ductile fracture at −30 °C should be tested under notched conditions rather than inferred from room-temperature data alone.
Compliance documentation for ABS 111 should be requested as a grade-specific statement from Guangdong Wanxi, not inferred from generic ABS classifications. The resin may be formulated to satisfy RoHS Directive 2011/65/EU Annex II restricted substance limits for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE, but this must be confirmed by lot-level X-ray fluorescence screening or supplier declaration. REACH SVHC concentration below 0.1 wt% per article is a commonly requested boundary under Regulation (EC) No 1907/2006; any specific SVHC on the candidate list above this threshold must be documented. Food-contact clearance is not automatic; if the grade is offered as complying with 21 CFR 180.22 or relevant food-contact provisions, the manufacturer’s formulation-specific letter should be retained and extraction limits verified by the converter. Processing plants using regrind must ensure traceability of any recycled content if a brand owner requires virgin-only material declarations. Moisture history and barrel temperature logs are recommended as part of the lot traceability record because thermal degradation during conversion can change the extractable monomer profile and invalidate a raw-resin compliance statement. No conclusion is drawn from these requirements; they operate as boundary conditions for specification review.