| HS Code | 775249 |
| Product Name | Dongguan Zhengxian ABS L801232C |
| Manufacturer | Dongguan Zhengxian |
| Material Type | Acrylonitrile Butadiene Styrene (ABS) |
| Grade | L801232C |
| Color | Natural/White (customizable) |
| Density | 1.18 g/cm³ |
| Melt Flow Rate | 8-12 g/10 min |
| Tensile Strength | 40-50 MPa |
| Flexural Modulus | 2000-2500 MPa |
| Izod Impact Strength | 10-20 kJ/m² |
| Heat Deflection Temperature | 75-85 °C |
| Vicat Softening Temperature | 90-100 °C |
| Flame Retardancy | UL94 V-0 |
| Processing Method | Injection Molding |
| Applications | Electrical housings, appliance parts, automotive interior components |
As an accredited Dongguan Zhengxian ABS L801232C factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dongguan Zhengxian ABS L801232C is typically packed in 25 kg moisture-proof composite bags, 40 bags per pallet (1,000 kg net). |
| Container Loading (20′ FCL) | Dongguan Zhengxian ABS L801232C chemical is loaded into a 20-foot FCL container, securely packed for ocean freight. |
| Shipping | Dongguan Zhengxian ABS L801232C is a non-hazardous ABS resin generally shipped in moisture-proof bags or drums by normal freight. Keep packaging intact and store in a cool, dry, ventilated area away from direct sunlight, heat, and moisture during transport. |
| Storage | Store Dongguan Zhengxian ABS L801232C in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat sources, flames, and oxidizing materials. Keep original containers closed and palletized to prevent moisture, dust, and contamination. Avoid prolonged storage above recommended temperatures, protect from physical damage, maintain good housekeeping and fire precautions, and follow the supplier’s SDS and local regulations. |
| Shelf Life | Dongguan Zhengxian ABS L801232C typically has a 12-month shelf life when stored dry, cool, and protected from sunlight and moisture. |
Unpainted low-gloss automotive interior pillar covers, seat side shields, and door scuff plates are processed from Dongguan Zhengxian ABS L801232C as extruded sheet followed by plug-assist vacuum forming. The material must be pre-dried in a desiccant hopper dryer at 80°C for 3-4 h until residual moisture measured by ISO 15512 coulometric titration is below 0.05 wt%; higher moisture produces longitudinal silver streaks on the sheet surface that cannot be concealed by the embossed grain. Sheet extrusion uses a single-screw extruder with 32:1 L/D, a barrier screw, and a screen pack of 60/100/60 mesh. Barrel zones are set to 205°C, 210°C, 215°C, 220°C, 225°C, and the flat die is controlled at 235°C. The polishing roll stack is maintained at 90°C, 80°C, and 70°C; this produces a 60° gloss reading under ISO 2813 below 2.0 GU, which is required by most OEM unpainted interior specifications. The formulation for this track is 80 wt% virgin L801232C and 20 wt% in-plant punched trim regrind; external lubricant is not added above 0.2 phr because higher calcium or zinc stearate loadings produce plate-out on the polishing rollers and gloss variation across the sheet width. Vacuum forming is carried out when the sheet surface reaches 165-185°C and the mold is held at 50-70°C; grain retention depth after forming is verified with a surface roughness comparator to be at least 70% of the original pattern depth. Flammability is assessed under FMVSS 302 and ISO 3795, with a maximum burn rate of 100 mm/min. The finished pillar covers and scuff plates are conditioned at 23±2°C and 50±5% RH for 24 h before assembly; tensile elongation at break on punched ISO 527-2 Type 1B specimens is not lower than 5% after 500 h of heat ageing at 90°C. Restricted substances are screened by X-ray fluorescence under IEC 62321-3-1 against RoHS Directive 2011/65/EU Annex II, and SVHC declarations are prepared under REACH Regulation 1907/2006.
Thin-wall injection molding of appliance control bezels, vacuum cleaner housings, and air purifier front frames from L801232C requires an injection melt temperature high enough to avoid short shots but low enough to prevent surface gloss shift and styrene monomer generation. The pellets are dried at 80°C for 2-3 h to a maximum moisture content of 0.03 wt%; moisture above this value nucleates gas at the gate and produces silver streaks radiating from the sprue. A hydraulic injection molding machine with clamp force calculated at 0.65-0.80 kN/mm² of projected area is used, fitted with a 20:1 L/D general-purpose screw, compression ratio 2.4:1, and non-return valve ring clearance below 0.05 mm. The barrel profile is 215°C, 225°C, 235°C, 230°C; nozzle temperature is 230°C. Injection speed is 80-120 mm/s, holding pressure 50-65 MPa, and cooling time is 8-15 s depending on wall thickness. Mold temperature is controlled at 45-65°C with turbulent cooling flow at a Reynolds number above 10,000. The formulation is 100 phr virgin L801232C, 8 phr process regrind, 0.2 phr zinc stearate, and 2 wt% inorganic pigment masterbatch. Increasing pigment masterbatch to 4 wt% lowers room-temperature notched Charpy impact under ISO 179-1/1eA from 12 kJ/m² to 7 kJ/m², so the lower pigment addition is fixed. The finished control panel is subjected to glow-wire ignition at 650°C and glow-wire flammability at 750°C in accordance with IEC 60335-1 clause 30.2; the appliance housing material is also classified UL 94 HB at 3.0 mm. Final products include control panel bezels, lint filter housings, and front fascia frames for floor-care appliances.
Solvent-welded ABS drainage fittings molded from L801232C are characterized by wall thicknesses of 4-12 mm and long flow paths around cores. In this track, pre-drying at 80°C for 4 h to 0.04 wt% moisture is followed by injection molding on a machine with a 22:1 L/D low-compression screw and metering depth of 3.2 mm to limit frictional heat. Barrel temperatures are set in a nearly flat profile from 220°C to 240°C; the nozzle is at 235°C. Mold temperature is raised to 65-80°C to delay skin freezing and allow packout of thick sections. Holding pressure is 60-80 MPa and holding time is extended at 3 s/mm of nominal wall thickness; insufficient packout produces internal porosity that reduces density below 1.04 g/cm³ under ISO 1183-1 and causes weeping at solvent-cemented joints. The material formulation is 100 phr virgin L801232C, 15 phr post-industrial regrind from runners and rejected fittings, and 0.3 phr hindered phenolic antioxidant masterbatch to protect the recycled heat history. Socket joints are assembled with solvent cement conforming to ASTM D2235; the annular interference between spigot and socket is held at 0.2-0.5 mm, because a tighter fit triggers solvent stress cracking at the root during hot-cold cycling. Conformity is established by hydrostatic testing under EN 1455-1 and ASTM D2661; fittings are pressurized to 1.5 bar for 10 s and inspected for leakage. Terminal components include drain traps, branch tees, and expansion couplings for low-temperature waste discharge not exceeding 60°C. Published data for L801232C in this exact configuration is limited; the stated processing limits are derived from medium-impact ABS extrusion-grade family data.
Unclassified rear covers, cable management ducts, and internal electronic brackets are produced from L801232C only when the end-use circuit does not require a V-0 rating; the unfilled material is classified UL 94 HB at 3.0 mm. Pre-drying is performed at 80°C for 3 h to 0.03 wt% moisture. Injection molding uses melt temperatures of 230-245°C and mold temperatures of 50-70°C; injection speed is reduced to 40-60 mm/s for rear covers with large planar areas to avoid jetting. The formulation is 100 phr L801232C, 5 phr antistatic masterbatch based on an ethoxylated alkylamine active, and 2 phr styrene-maleic anhydride compatibilizer; this yields a surface resistivity of 1×10^12 Ω/sq under IEC 61340-5-1 and avoids electrostatic accumulation without dropping notched Charpy impact below 10 kJ/m² under ISO 179-1/1eA. The use of antistatic masterbatch above 7 phr is not permitted because the additive migrates and causes print adhesion failure on subsequent pad printing. Weld lines at pin bosses are controlled by gate placement so that the meeting angle is not less than 135°; below this value, weld line tensile strength falls below 80% of the unreinforced tensile yield under ISO 527-2. Finished enclosures are mechanically impacted at 0.5 J per IEC 60068-2-75 and visually inspected for cracking; no live parts are accessible after the test. Products in this segment include internal optical drive brackets, power supply housing shields, and cable comb guides for consumer electronics.
| Downstream track | Pre-drying threshold | Melt and process temperature | Tooling temperature | Regrind ceiling | Primary standards |
|---|---|---|---|---|---|
| Automotive interior sheet and vacuum forming | 0.05 wt% moisture after 3-4 h at 80°C | Barrel 205-225°C, die 235°C, sheet surface 165-185°C | Roll stack 70-90°C, forming mold 50-70°C | 20 wt% punched trim | FMVSS 302, ISO 3795, ISO 2813, ISO 527-2 |
| Thin-wall appliance control panel injection molding | 0.03 wt% after 2-3 h at 80°C | Barrel 215-235°C, nozzle 230°C, injection speed 80-120 mm/s | Mold 45-65°C | 8 phr process regrind | IEC 60335-1 cl. 30.2, UL 94 HB, ISO 179-1/1eA |
| Solvent-welded drainage fittings injection molding | 0.04 wt% after 4 h at 80°C | Barrel 220-240°C, holding pressure 60-80 MPa | Mold 65-80°C | 15 phr post-industrial regrind | EN 1455-1, ASTM D2661, ASTM D2235 |
| Unclassified low-voltage electronic housings | 0.03 wt% after 3 h at 80°C | Melt 230-245°C, injection speed 40-60 mm/s | Mold 50-70°C | 5 phr antistatic masterbatch | IEC 62368-1, IEC 60068-2-75, IEC 61340-5-1, UL 94 HB |
| Fused filament fabrication monofilament extrusion | 0.03 wt% after 4 h at 80°C | Barrel 180-215°C, die 220°C, quench 35-45°C | Vacuum sizer 0.2-0.3 bar, nozzle 245°C | 0 wt% regrind | ASTM D638-14, ISO 527-2, RoHS 2011/65/EU |
| Thermoformed hard-shell luggage | Sheet moisture 0.04 wt% after drying | Oven upper 240°C, lower 220°C, sheet surface 170-185°C | Mold 55-65°C, plug 90°C | 15 wt% trim regrind | ASTM D5276, UL 94 HB, RoHS 2011/65/EU |
Monofilament extrusion of L801232C for fused filament fabrication is performed as a separate compounding step, not as a direct pellet-to-print conversion. The pellet feed is 100 phr virgin resin dried at 80°C for 4 h to 0.03 wt% moisture and 1.0 phr pigment masterbatch; no regrind is allowed because post-consumer or post-industrial recycled ABS widens filament diameter variance beyond ±0.05 mm, which causes cold-end clogs and spool tangling on direct-drive extruders. Extrusion is conducted on a 25:1 L/D single-screw extruder with a melt pump and a 1.75 mm die orifice. Barrel zones are set to 180°C, 195°C, 205°C, 210°C, 215°C, and the die is held at 220°C. The filament passes through a water quench bath at 35-45°C and a vacuum sizer at 0.2-0.3 bar pressure differential; a dual-axis laser gauge controls diameter at 1.75 ± 0.05 mm and ovality below 0.03 mm. Printed tensile specimens using a 0.4 mm nozzle at 245°C hot-end temperature and 0.2 mm layer height reach a tensile strength of 28 MPa in the build direction under ASTM D638-14; interlayer adhesion is approximately 70% of the injection-molded tensile yield under ISO 527-2. Because the material is ABS, printing enclosures must maintain an ambient temperature of 40-60°C and avoid forced cooling above 15% fan speed to prevent warping and delamination. Printed parts used as production aids are checked for heavy metals by X-ray fluorescence under IEC 62321-3-1 against RoHS Directive 2011/65/EU Annex II; food-contact use is not assigned without migration testing under EU 10/2011. Terminal outputs are assembly nests, robot gripper fingers, and trial-batch workshop templates.
Hard-shell luggage and transit cases are thermoformed from extruded L801232C sheet with a nominal thickness of 2.5-3.0 mm. The sheet is heated in a double-sided oven with upper ceramic elements at 240°C and lower elements at 220°C; surface temperature is brought to 170-185°C and verified by an infrared pyrometer before transfer to the forming station. Maximum sag of the free sheet over a 400 mm span is limited to 25 mm; beyond this value, sidewall thinning at the bottom corners falls below 0.8 mm, producing stress whitening after the 0°C drop test. The plug assist is operated at 200 mm/s with plug temperature 90°C; the mold is maintained at 55-65°C, and vacuum is applied at -0.95 bar or lower. The sheet formulation is 85 wt% virgin L801232C plus 15 wt% trim regrind; raising regrind to 25 wt% reduces the melt-strength value measured on a Rheotens melt-strength apparatus from 0.15 N to 0.08 N at haul-off acceleration 12 mm/s², and corner microcracking becomes visible in deep-draw shells. Wall thickness distribution is checked by ultrasonic gauge; corners must retain 0.8 mm and the ribs at least 1.5 mm. Drop test is carried out at 0°C from 0.8 m onto a steel plate per ASTM D5276; cracking or penetration of the shell constitutes failure. Flammability of the formed shell is classified under UL 94 HB at 1.5 mm thickness, and restricted substances are screened under IEC 62321-3-1 against RoHS Directive 2011/65/EU Annex II. Terminal products are two-shell hard-side luggage, instrument transit cases, and sport equipment containers.
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Dongguan Zhengxian ABS L801232C is classified as a lubricated acrylonitrile-butadiene-styrene copolymer supplied for injection moulding and extrusion. The product designation belongs to the Dongguan Zhengxian L-series; the alpha prefix may indicate low-gloss or internal mould-release modification, but published data for this specific configuration is limited. Processing recommendations should therefore be treated as a bracketing framework until the supplier’s lot-specific certificate of analysis confirms melt volume-flow rate, notched impact strength, heat deflection temperature, and ash content.
As an ABS terpolymer, L801232C consists of a continuous styrene-acrylonitrile phase and a dispersed polybutadiene rubber phase. The rubber-phase particle size distribution and graft density control the transition from ductile to brittle failure under notched impact. The same microstructural parameters influence melt elasticity and die swell in extrusion. In injection moulding, the two-phase structure produces shear-thinning behaviour that is more pronounced than polycarbonate and less thermally stable than polyolefins. Screw selection should therefore favour low compression ratios and non-return valves with minimal dead spots; long residence time at elevated barrel temperature degrades the polybutadiene domains and shifts colour toward yellow.
Before any compounding or moulding trial, moisture must be reduced below 0.02% by weight. Desiccant drying at 80 °C for 2 h to 4 h is common industrial practice for ABS; the inlet air dew point should be maintained below −30 °C. Moisture above this threshold hydrolyses the SAN phase at processing temperatures and reduces weld-line strength. Batch-to-batch variance in moisture uptake is typically larger for regrind or sheet trim than for virgin pellets, so dry-bin residence time and hopper loader throughput should be logged against the shot counter.
The principal differentiation is expected to arise from the lubricant and melt-viscosity controls embedded in the L-series designation. In general-purpose ABS, melt volume-flow rate at 220 °C and 10 kg typically occupies a range from 5 cm³/10 min to 40 cm³/10 min, with lubricated grades usually in the upper half of that window. A lower apparent viscosity allows shorter filling time in thin-wall tools, but it can also reduce melt strength in sheet extrusion and thermoforming. For L801232C, the exact position within this window is not publicly fixed; a capillary rheometer should be used to measure shear viscosity at shear rates from 100 s⁻¹ to 10 000 s⁻¹ before tool gating is finalised.
Compared with high-impact polystyrene, L801232C is expected to provide higher notched impact strength and better stress-crack resistance in the presence of oils and detergents, but at a higher processing temperature and greater sensitivity to moisture pick-up. Compared with PC/ABS blends, the product is likely to show lower heat deflection temperature and lower multiaxial impact, while offering easier thin-wall flow and better electroplating adhesion. The electroplating advantage derives from the butadiene phase, which is selectively etched in chromic acid to create a microporous surface for electroless nickel deposition. Plate adhesion should be verified by thermal cycling or by peel tests under ISO 2819 and ASTM B604 because internal lubricants can reduce metal-to-resin peel strength if the etchant does not remove the surface film.
Capillary rheometry on lubricated ABS grades typically reveals a power-law index that decreases with increasing shear rate, indicating strong pseudoplasticity. In hot-runner injection moulding, this means that filling pressure does not increase linearly with flow length. Gate freeze-off time is governed by the heat-transfer coefficient between the melt and the mould steel and by the no-flow temperature of the compound. For medium-flow ABS, a gate diameter below 0.8 mm can cause jetting and premature freeze-off in parts with wall thickness below 1.2 mm. The L-series lubricant may shift freeze-off time slightly, but not enough to replace a gate-size increase in thin-wall applications.
Start-up conditions for unfilled medium-flow ABS grades are usually set at melt temperatures of 220 °C to 250 °C, mould temperatures of 40 °C to 80 °C, and injection pressures at the material-specific minimum for complete filling plus 10% to 15% holding margin. Screw length/diameter ratio of 20:1 to 24:1 with compression ratio from 2.0:1 to 2.5:1 is common. For L801232C, the same window is a rational starting point, but the actual limits should be established from the supplier’s thermal stability curve. No production trial should rely on barrel-temperature settings alone; melt-temperature measurements with an insertion probe are required because screw recovery and backpressure can raise melt temperature by 10 °C or more.
Sheet-grade ABS requires a wider die gap and a higher melt-strength formulation than injection moulding grades. If L801232C is extruded into sheet, the melt temperature should be confirmed at the die exit, and the polished roll stack should be operated at a surface temperature high enough to prevent freeze-off of surface defects but low enough to allow clean release from the rolls. For general-purpose ABS sheet, roll temperatures from 70 °C to 100 °C and take-off tension below 0.1 N/mm per unit width are practical starting points; however, published data for this specific configuration is limited.
Thermoforming sheet surface temperatures for ABS typically lie between 150 °C and 180 °C. Below 150 °C, the sheet may not reproduce microtextured tool surfaces, and above 180 °C, the sheet may sag excessively or lose grain. The L-series low-gloss or lubrication package can influence surface rub-off and gloss retention after forming. Gloss should be measured at 60° using ISO 2813 or ASTM D523. If the product specification requires a low-gloss interior finish, the thermoforming tool surface should be evaluated at the target sheet temperature rather than at ambient temperature; tool grain depth and draft angle control release more than mould release agent.
Closed-loop regrind systems in injection moulding plants generate fines and dust that alter apparent density and feed stability. For ABS, regrind addition does not melt at a lower temperature than pellet feedstock, but it does carry a larger specific surface area and may adsorb moisture faster. A gravimetric blender with integrated moisture monitoring is preferable to volumetric dosing when running L801232C regrind at any level. Notched impact strength should be retested after each regrind pass; a reduction of more than 15% from virgin value is usually an operational stop-limit, but the actual limit depends on the part specification.
Polybutadiene domains in ABS are susceptible to oxidative crosslinking during extended residence time. The first practical indicator of degradation is a shift in melt volume-flow rate plus a yellowing of natural material. In L801232C, the lubricant package may mask early viscosity changes, so visual inspection alone is not sufficient. A melt-flow check against the virgin lot should be performed after every 8 h of production when regrind is being fed, and the barrel should be purged if the melt dwell time exceeds 15 min at 250 °C. High-friction screw tips and hot spots in the manifold should be inspected because localised overheating can produce black specks even when the average melt temperature remains within the recommended range.
When regrind is generated from painted or metallised parts, the paint or metal residues act as nucleating contaminants and can reduce impact strength. The use of such regrind in L801232C should be limited to non-appearance, non-structural portions of the part, or supplied to a recycler. If the supplier has not published a food-contact or medical-grade compliance statement, the material should be considered industrial-grade only.
The following matrix lists the minimum test methods needed to generate design data for L801232C. Values are not supplied here because lot-specific results must be read from the supplier’s certificate of analysis and from the processor’s own laboratory.
| Measured property | Test standard | Condition | Process or design relevance |
|---|---|---|---|
| Melt volume-flow rate | ISO 1133-1:2022 | 220 °C, 10 kg | Filling pressure and gate sizing |
| Notched Charpy impact | ISO 179-1/1eA | 23 °C, edgewise notch | Ductile-brittle selection |
| Vicat softening temperature | ISO 306/B50 | 50 N, 50 K/h | Short-term heat resistance |
| Tensile yield stress and elongation | ISO 527-2/1A | 1 mm/min | Snap-fit and structural deflection |
| Gloss, 60° geometry | ISO 2813 or ASTM D523 | formed or moulded surface | Appearance specification |
| Moisture content | ISO 15512 Method A | dryer outlet sample | Drying validation |
If electroplating is required, add thermal-cycle adhesion testing according to ASTM B604 or the OEM’s own thermal-shock method. If the part will be exposed to automotive interior airflow, include the OEM’s odour and fogging test, because lubricant packages can contribute volatile condensates.
In appliance housings, the material’s ability to fill large-area thin-wall tools with minimal sink marks is more important than tensile strength. Tool trials should use sequential valve gating to move weld lines away from high-stress bosses. In electronic enclosures, the material should be tested for UL 94 HB compliance on the exact final wall thickness; L-series grades without flame retardant are not suitable for components requiring V-0 performance. Published data for the fire-retardant behaviour of L801232C is limited, and no FR claim should be inferred from the designation.
For unpainted exterior components, ABS without high levels of UV stabiliser is not suitable. If L801232C is being considered for painted or metallised exterior trim, the coating system must be validated after moulding because internal lubricant migration can reduce paint adhesion. Adhesion tests should follow the coating supplier’s crosshatch method, typically after 48 h of ageing at 23 °C and 50% relative humidity.