| HS Code | 883648 |
| Density | 1.05 g/cm3 |
| Melt Flow Rate | 15 g/10 min (220°C/10 kg) |
| Tensile Strength | 45 MPa |
| Elongation At Break | 20% |
| Flexural Modulus | 2300 MPa |
| Izod Notched Impact Strength | 20 kJ/m2 |
| Rockwell Hardness | 105 R-scale |
| Heat Deflection Temperature | 85°C (1.82 MPa) |
| Vicat Softening Temperature | 100°C |
| Mold Shrinkage | 0.4-0.6% |
| Ul Flammability Rating | HB |
| Dielectric Strength | 15 kV/mm |
As an accredited Lotte Chemical ABS PW-1000 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Lotte Chemical ABS PW-1000 is supplied in 25 kg moisture-proof paper bags, palletized for industrial handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Lotte Chemical ABS PW-1000 resin in 25 kg bags, palletized, strapped, and secured for export. |
| Shipping | Lotte Chemical ABS PW-1000 is shipped as non-hazardous ABS resin pellets, typically in 25 kg bags or 1,000 kg FIBCs. Keep containers sealed, dry, and protected from heat, sunlight, and moisture during road/sea transport; no special dangerous-goods classification is normally required. |
| Storage | Store Lotte Chemical ABS PW-1000 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, moisture, and ignition sources. Keep original bags or containers tightly closed and palletized to prevent contamination and moisture pickup. Avoid dust generation and static buildup. Maintain stable temperature, observe FIFO, and dry before processing if required. Store away from oxidizing agents and incompatible materials. |
| Shelf Life | Shelf life: approximately 12 months from manufacture when stored in original sealed packaging, cool, dry, and away from direct sunlight. |
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Lotte Chemical ABS PW-1000 is a plating-grade acrylonitrile-butadiene-styrene terpolymer supplied for electroplated plastic components in automotive, sanitary, and consumer hardware applications. The material is specified by moulders and platers where a balance of melt flow, impact resistance, and controlled surface etch morphology is required. In the chromium-plating sequence, the polybutadiene phase is selectively oxidized by a chromic acid/sulfuric acid etch, generating a microcavity network that anchors electroless and electrolytic metallic layers. Component geometries commonly associated with PW-1000 include radiator grilles, door handles, wheel centre ornaments, and bezels with thin-wall sections and complex flow paths. Because electroplated ABS is subject to both moulded-in stress and differential thermal expansion between the ABS substrate and the metal layer, the resin must provide low residual internal stress and consistent rubber-phase dispersion. The product is characterized under the ISO 2580 ABS designation system, with lot release data typically reported against ISO 1133-1:2022 for melt flow and ISO 527-2:2012 for tensile yield. No single property value is sufficient for lot acceptance; the combination of melt rheology, rubber-phase morphology, and surface quality after moulding determines plated part capability.
Across electroplating lines processing ABS substrates, adhesion failure is most commonly traced to non-uniform etch pit distribution rather than insufficient bulk tensile strength. The chromic acid/sulfuric acid bath operates at 60°C to 70°C, with immersion times of 5 min to 15 min depending on bath age and part wall thickness. A typical etch bath contains 350–400 g/L chromic acid and 350–400 g/L sulfuric acid; hexavalent chromium process control is subject to REACH Annex XIV authorization and surface treatment permitting. During this stage, oxoacid attack removes butadiene-rich domains from the surface while the styrene-acrylonitrile matrix remains largely intact. If the rubber particle size distribution is excessively broad, large extracted pits produce macro-roughness that reduces specular gloss after plating; if the gel fraction is too high, etching becomes slow and micro-roughness is insufficient for mechanical locking. PW-1000 is positioned to provide a controlled gel fraction and a rubber domain size range that supports uniform micro-roughening under conventional etch conditions. Subsequent activation in palladium/tin colloidal systems produces catalytic nucleation sites on the micro-roughened surface, followed by electroless nickel deposition at 0.5–1.0 µm and electrolytic copper build. The role of PW-1000 is not to alter the metallization chemistry but to ensure that the substrate micro-topography after etching is reproducible across moulded-in skin layers and weld lines. Adhesion after electroless nickel initiation is evaluated by peel methods based on ASTM B533-85(2019) or by thermal-cycling protocols in which parts are exposed to alternating -40°C and 80°C conditions specified by individual OEM specifications. Published data for quantitative peel values on this specific grade is limited; therefore, platers must establish internal process capability using actual tooling.
In production-scale injection moulding of complex grille tools with six to twelve hot-drop gates, ABS PW-1000 requires pre-drying in a desiccant dryer with a dew point of -30°C or lower at 80°C for 2–4 h; residual moisture above 0.05% produces splay and local surface hydrolysis that destabilizes subsequent electroplating. Melt-temperature set points between 230°C and 250°C are typical, with mould temperatures maintained between 40°C and 80°C. A mould temperature below 40°C can freeze the filling front prematurely and raise frozen-in orientation; a mould temperature above 80°C increases cycle time and may raise the thermal expansion mismatch strain in the plated skin. Injection speed is set to a moderate-to-high profile, with cavity-to-cavity balance monitored through pressure sensors installed behind ejector pins; excursions in cavity pressure at gate freeze beyond ±10% often correlate with local non-uniform etch response near weld lines. Clamp force selection follows projected-area multiplication against cavity pressure; structured tools with long flow length-to-wall-thickness ratios may require higher holding pressure but should avoid overpacking near the gate, which increases residual stress and can cause stress-cracking whitening during chromic acid immersion. On hot-runner systems, manifold temperatures should not exceed 260°C and hold-up volumes should be minimized; stagnant melt in dead zones promotes thermal yellowing and SAN oligomer accumulation that reduces plate adhesion. High-shear viscosity data for this specific grade under production-relevant filling conditions are not commonly published; evaluation on capillary rheometry per ISO 11443:2021 is recommended when validating hot-runner simulation inputs.
Substitution of PW-1000 for a general-purpose ABS in an existing chrome-plated component is not a drop-in change when plater etch conditions are fixed. General-purpose ABS grades are often designed for balanced mechanical properties and may contain rubber particle size distributions that are broader than those tolerated in electroplating. In contrast, high-impact ABS grades may carry higher butadiene contents, which improve impact strength but can produce coarse etch pits after chromic acid oxidation, resulting in light scattering and loss of mirror reflectivity. PW-1000 is formulated to shift the balance toward finer, more uniform micro-roughness while retaining sufficient impact resistance for automotive interior and exterior trim. The difference is not simply melt flow; platers evaluate the etching response through surface roughness parameters such as Sa and Sdr measured by confocal microscopy or stylus profilometry before electroless nickel, but no harmonized ISO or ASTM acceptance limit exists for these roughness values. Mechanical property comparisons are performed using ISO 180/A:2019 notched Izod, ISO 527-2:2012 tensile yield, ISO 178:2019 flexural modulus, and ISO 75-2/Ae:2016 heat deflection temperature; because pigmentation and processing history shift these values, a lot certificate is required for normative limits. Quantitative comparison data against all other Lotte ABS grades in the same cavity and etch line is not published; published data for this specific configuration is limited. The distinction between PW-1000 and fibre-reinforced ABS or mineral-filled ABS is also significant for electroplating: fillers exposed on the surface undergo etching at different rates, creating microgalvanic features that degrade plating uniformity. Unfilled plating grades avoid this incompatibility and are preferred when Class A chrome surfaces are required. Where flame-retarded ABS is specified, brominated or phosphorus-based additives can interfere with palladium activation or promote skip plating at high loading; PW-1000 should not be assumed to be interchangeable with flame-retarded grades unless the complete etch and activation process is requalified.
For incoming inspection and quality planning, the following test method designations are used to evaluate ABS PW-1000. The table does not reproduce lot-specific values, which are supplied on the manufacturer certificate and are valid only for the sampled production campaign.
| Test discipline | Standard / method | Condition |
|---|---|---|
| Melt volume-flow rate | ISO 1133-1:2022 | 220°C, 10 kg |
| Tensile yield stress | ISO 527-2:2012 | 50 mm/min |
| Flexural modulus | ISO 178:2019 | 2 mm/min |
| Notched Izod impact | ISO 180/A:2019 | 23°C |
| Heat deflection temperature | ISO 75-2/Ae:2016 | 1.82 MPa, flatwise |
| Vicat softening temperature | ISO 306/B50:2013 | 50 N, 50°C/h |
| Density | ISO 1183-1:2019 | 23°C |
| Mould shrinkage | ISO 294-4:2001 | parallel and normal to flow |
| Peel adhesion of electroplated coating | ASTM B533-85(2019) | as plated, after deposit build |
RoHS compliance is assessed according to IEC 62321-5:2013 for cadmium, lead, and mercury, and IEC 62321-8:2017 for phthalates if specified by customer drawing. REACH SVHC declarations are provided by the manufacturer against the candidate list in force at the date of supply; the plater is responsible for authorization of hexavalent chromium etch solutions under REACH Annex XIV. Typical mould shrinkage for unfilled ABS is 0.4% to 0.8%; tooling design for plating grades should account for the additional thickness of the metallic layer, typically 20–45 µm total copper-nickel-chromium, when fine-fitting mating parts are assembled after plating. Pre-drying capacity and dryer dew-point monitoring become controlling parameters when relative humidity exceeds 60% in the compounding or moulding hall; under such conditions, moisture regain in open storage can exceed the 0.05% threshold before closed-loop drying is complete. Process deviation investigations on production-scale lines have identified gate blush and jetting-induced surface orientation as recurring causes of non-uniform etch response, even when bulk property data remain within specification. For this reason, ultrasonic or thermal stress-relief treatments are sometimes introduced before electroplating, but any relaxation step must be validated against ASTM B533-85(2019) peel results and OEM thermal-cycle requirements.