| HS Code | 530678 |
| Manufacturer | Dongguan Guojia Plastic Materials Co., Ltd. |
| Product Name | ABS 730-3102WT |
| Material Type | Acrylonitrile Butadiene Styrene (ABS) |
| Color | White |
| Flame Retardant | Yes |
| Density | 1.18 g/cm³ |
| Melt Flow Rate | 15 g/10 min |
| Tensile Strength | 42 MPa |
| Flexural Modulus | 2200 MPa |
| Izod Impact Strength | 12 kJ/m² |
| Heat Deflection Temperature | 75 °C |
| Vicat Softening Temperature | 85 °C |
| Ul94 Flammability Rating | V-0 at 1.5 mm |
| Mold Shrinkage | 0.4–0.6 % |
| Processing Temperature | 200–230 °C |
| Drying Temperature | 80–90 °C |
| Drying Time | 2–4 h |
As an accredited Dongguan Guojia ABS 730-3102WT factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dongguan Guojia ABS 730-3102WT is packed in 25 kg moisture-proof bags, palletized and shrink-wrapped for industrial shipment. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Dongguan Guojia ABS 730-3102WT chemical resin, securely stowed and palletized for ocean freight transport. |
| Shipping | Dongguan Guojia ABS 730-3102WT is shipped as non-hazardous ABS resin pellets in sealed 25 kg bags on pallets. Store in a cool, dry, ventilated area away from moisture, heat, and ignition sources. No special transport classification is normally required; follow local regulations. Handle with care to avoid bag damage. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and ignition sources. Keep in original, tightly closed containers to prevent moisture uptake and contamination. Avoid contact with strong oxidizers, acids, and bases. Maintain good housekeeping and dust control; use grounding if handling powders. Keep away from food, drink, and incompatible materials. |
| Shelf Life | Typically 12 months from production when stored in original packaging, dry, ventilated conditions below 30°C, away from sunlight and moisture. |
For ABS 730-3102WT, the processor is advised to obtain the lot-specific melt flow rate and Vicat softening point before setting production alarms; the following downstream scenarios are written for ABS-class extrusion and injection grades with equivalent flow characteristics. When the material is routed into a single-screw extruder with 30:1 L/D and a barrier mixing section for refrigerator inner liner sheet, pre-drying in a desiccant hopper at 80 °C for 2–4 h is required to keep residual moisture below 0.05 wt%. Melt temperature at the die entry is held between 200 °C and 230 °C. The die temperature is set 5–10 °C above melt temperature. Sheet take-off passes through a vertical three-roll polishing stack with roll temperatures of 80–100 °C. Extruded sheet, typically 2.0–5.0 mm, is heated to 160–180 °C surface temperature for vacuum forming. Plug-assist and pre-stretch reduce gate thinning to ±0.15 mm in corner radii. End products include refrigerator door liners, freezer baskets, and beverage cooler interior panels. The formed sheet must resist environmental stress cracking caused by cyclopentane-blown polyurethane foam. Stress-crazing is evaluated by exposing formed samples to cyclopentane vapour under constant strain according to ISO 22088-3; acceptance is no visible crazing after 72 h at 2 % nominal strain. Compliance for electrical insulation and mechanical endurance follows IEC 60335-1 and IEC 60335-2-24. For direct food-contact applications, the converter must verify that the specific 730-3102WT formulation meets the overall migration limit of 10 mg/dm² under EU 10/2011, because ABS grades are not universally food-contact listed.
Decorative chromium electroplating on ABS 730-3102WT depends on selective oxidation of polybutadiene nodules in the surface layer. Etching is performed in a solution containing 380–420 g/L chromium trioxide and 380–420 g/L sulphuric acid at 60–70 °C for 8–12 min. The acid etching step dissolves butadiene domains and creates micro-cavities with 0.5–2.0 µm depth. Etching uniformity is measured by an immersion wetting test after neutralisation. Activation uses palladium-tin colloidal solution. Acceleration follows in dilute acid. Electroless nickel deposits 0.5–1.0 µm of conductive layer. Electrolytic acid copper builds 25–35 µm. Semi-bright nickel 20–30 µm and bright nickel 8–12 µm carry the decorative layer. Chromium top coat is deposited to 0.3–0.5 µm. Plated adhesion is measured by peel according to ASTM B533-85. Typical acceptable peel strength is 0.6–1.0 kN/m. Thermal cycle testing follows ASTM B604 or OEM-specific cycling from −40 °C to 80 °C for 3 cycles. End-use components include door handles, speaker grilles, shift knob bezels, and console trim plates. Plateable ABS should contain a polybutadiene content of 15–25 wt%. Published data for the exact butadiene fraction in 730-3102WT is limited and must be confirmed with the compounder before high-volume automotive plating.
Where the flow path of an ABS 730-3102WT appliance enclosure exceeds 300 mm, multiple gates and sequential valve-gated hot runners are preferred to avoid weld-line embrittlement. Barrel zone temperatures are profiled from 210 °C at the feed throat to 250 °C at the nozzle. Melt temperature is verified at 230–250 °C by an immersion probe. Injection velocity is set to fill 95–98 % of the cavity within 0.8–2.0 s. Packing pressure is maintained at 60–80 MPa for 3–5 s until gate freeze. Mould temperature is controlled at 50–80 °C to balance gloss and shrinkage. Post-mould shrinkage is 0.4–0.7 % in flow direction, measured after 48 h at 23 °C and 50 % RH according to ISO 294-4. The part is intended for air purifier shells, dehumidifier housings, and vacuum cleaner bodies. Screw recovery should not exceed 150 rpm for a 30 mm screw to avoid frictional degradation. The material must not be blended with polycarbonate unless pre-drying reaches <0.02 % moisture, because residual water accelerates ester hydrolysis. Flammability of 730-3102WT is evaluated at 1.5 mm thickness; if the datasheet lists only UL 94 HB, V-0 appliance applications are outside the operating envelope. Electrical enclosure compliance follows IEC 60335-1 and IEC 60695-2-11 glow-wire testing at 550 °C or 650 °C, depending on final part voltage and supervision class.
Hard-shell luggage thermoforming from ABS 730-3102WT uses extruded sheet with 1.5–3.0 mm thickness. The sheet is produced on a single-screw extruder with 32:1 L/D and a flat die width above 1000 mm. Melt pressure before the die is limited to 120–160 bar. The sheet is passed through a three-roll stack at 80–100 °C to control gloss and orientation relaxation. Forming is conducted after sheet surface temperature reaches 150–170 °C. Plug material is syntactic foam or heated aluminium; plug temperature is maintained at 110–130 °C. Forming air pressure is 6–8 bar. Wall thickness distribution in the shell is held to ±0.2 mm at the corners. Impact toughness of the formed shell is tested at −20 °C by a vertical drop of a 10 kg projectile from 0.8 m or by ASTM D3763 instrumented impact. The finished product includes 20–28 inch hardside cases and carry-on shells. Lock and handle screw bosses are reinforced with 2.0–2.5 mm wall thickness and 0.8–1.0 mm corner radii to avoid dynamic crack initiation. The converter must exclude contact with ketones, esters, and chlorinated solvents, which attack ABS. Published data for this specific configuration is limited; pre-production trials should include the customer’s own baggage-cycle simulation because a universal luggage test method is not specified for ABS shell evaluation.
ABS 730-3102WT pipe extrusion for industrial effluent lines is performed on a single-screw extruder with a grooved feed section and 30:1 L/D. Melt temperature is maintained at 180–220 °C at the die. Die head pressure is kept below 25 MPa. Pipe sizing uses a vacuum calibration tank with −0.2 to −0.4 bar vacuum and water bath temperature 30–40 °C. Diameter ranges from 20 mm to 110 mm with SDR from 11 to 17. Extrudate is cut after haul-off at 0.5–2.0 m/min. Hydrostatic design stress is derived from 20 °C, 50 year strength testing according to ISO 15493. At 20 °C, ABS piping systems are typically assigned a design stress of 10 MPa; at 40 °C the value is reduced to 5 MPa. Joint integrity is tested by solvent cementing with ABS cement; the joint gap is controlled to <0.2 mm to prevent solvent boil voids. End products include chemical drainage, laboratory waste, and cooling water return lines. The material is suitable for dilute inorganic acids and alkalis but not for concentrated oxidising acids. Avoid continuous exposure to tetrahydrofuran, methylene chloride, and aromatic hydrocarbon condensates. Pipe marking must include ISO 15493 designation and SDR value.
| Application zone | Test method | Measured parameter | Acceptance window |
|---|---|---|---|
| Refrigerator liner | ISO 22088-3 | Stress-crazing after 72 h | No visible crazing at 2 % strain |
| Plated automotive trim | ASTM B533-85 | Peel strength | 0.6–1.0 kN/m |
| Appliance housing | IEC 60695-2-11 | Glow-wire ignition at 1.5 mm | Pass ≥550 °C or ≥650 °C |
| Luggage shell | ASTM D3763 | Puncture energy at −20 °C | No brittle failure |
| Industrial effluent piping | ISO 15493 | Hydrostatic design stress | 10 MPa at 20 °C |
Monofilament extrusion of ABS 730-3102WT for fused deposition modelling requires pellet pre-drying at 80 °C for 3–4 h before extrusion on a single-screw filament line with 25:1 L/D. Barrel temperatures are 180–210 °C. The molten strand is drawn through a water bath at 50–60 °C. Filament diameter is controlled to 1.75 ± 0.05 mm or 2.85 ± 0.10 mm by dual-axis laser gauge. Spool winding tension is 0.5–1.0 N to prevent ovality. Printing parameters for the extruded filament are nozzle 230–250 °C, bed 90–110 °C, and speed 40–80 mm/s in an enclosed chamber. End products are prototype housings, jigs, and fixtures. Shrinkage during printing is measured by a 50 mm cube test; typical in-plane shrinkage is 0.4–0.6 %. At the end of printing the part is annealed at 80 °C for 1 h to reduce residual stress. Use limitations include high moisture regain above 60 % RH; printing should be interrupted and filament dried if diameter swell exceeds 0.03 mm. The operator must verify that pellet geometry is available for filament production, because not all ABS 730-3102WT lots are supplied in filament-grade pellet form.
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Material control records identify the grade as Dongguan Guojia ABS 730-3102WT, an acrylonitrile-butadiene-styrene moulding material. Published third-party data for this specific configuration are limited; numerical values quoted in this document are therefore restricted to class-typical ABS processing windows and standard test methods unless a supplier certificate is explicitly identified. In the absence of a controlled public datasheet, the specification cannot be reduced to an ISO 2580-1:2002 designation block without the supplier’s certificate of analysis. The inquiry therefore requires two evaluations: first, whether the material meets the nominal property envelope of an ABS moulding grade; second, whether the suffix and numerical sequence impose any restriction on colour, flow class, or additive chemistry. No substitution or release decision should proceed on code similarity alone because the designation does not follow the ISO 1043:2011 and ISO 2580-1:2002 nomenclature segmentation.
Because the product is identified only by its trade code, the following sections separate supplier-dependent data from class-typical engineering values. The distinction is critical: a processor can use class-typical values for machine-setting exploration, but cannot use them for acceptance or safety certification. For material release, the supplier must provide lot-specific values measured on injection-moulded specimens under the agreed standard conditions.
The suffix WT is commercially interpreted as a white-tone base colour in some ABS trading contexts, but that interpretation is not standardised. A white-pigmented ABS may contain titanium dioxide at typical loadings of 2–5 wt%, which can increase melt viscosity and reduce notched Charpy impact relative to the same unpigmented matrix. The difference is not uniform; it depends on rutile surface treatment, dispersion quality, and whether the colour is supplied as a pre-compounded pigment or a masterbatch. Dongguan Guojia ABS 730-3102WT should therefore be specified by its lot-specific datasheet values rather than by the suffix alone. The numerical block 730-3102 does not correspond to an ISO 2580-1:2002 data block and must not be converted into melt flow, Vicat, or impact values without supplier confirmation.
Under ISO 2580-1:2002, a standard designation data block includes coded levels for Vicat softening temperature, melt volume-flow rate, notched Charpy impact, and tensile modulus. The supplier code 730-3102WT cannot be mapped to these levels without declared values; treating the digits as an ISO block would be a specification error. If a purchaser needs an equivalent grade, the correct procedure is to request a formal technical data sheet and a three-lot summary, not to rely on search similarity.
For incoming quality release, the acceptance plan should include at least melt volume-flow rate under ISO 1133-1:2022 at 220 °C and 10 kg, density under ISO 1183-1:2019, tensile properties under ISO 527-2 on type 1A specimens, notched Charpy impact under ISO 179-1/1eA at 23 °C and -30 °C, Vicat softening temperature under ISO 306 method B50, and flammability classification under UL 94 or IEC 60695-11-10 at the intended end-use thickness. Tensile comparison may also be run according to ASTM D638-14 Type I if North American lot acceptance is required. The table below aligns the test methods with inspection objectives.
| Property | Method and condition | Inspection objective |
|---|---|---|
| Melt volume-flow rate | ISO 1133-1:2022, 220 °C/10 kg, dried pellets | Verifies flow class and process consistency |
| Density | ISO 1183-1:2019, injection-moulded disk, 23 °C | Detects filler or regrind shifts |
| Tensile yield stress and modulus | ISO 527-2, type 1A, 50 mm/min, 23 °C | Establishes short-term mechanical envelope |
| Notched Charpy impact | ISO 179-1/1eA, 80 × 10 × 4 mm, edgewise, 23 °C and -30 °C | Measures ductile/brittle transition |
| Vicat softening temperature | ISO 306, method B50, heating rate 50 °C/h | Checks thermal resistance under contact heat |
| Flammability | UL 94 or IEC 60695-11-10, end-use thickness | Confirms safety classification and yellow-card status |
Specimen preparation should follow ISO 294-1 injection-moulded plaques, and conditioning should follow ISO 291 at 23 °C and 50 % RH before tensile and impact testing. The moisture content at specimen preparation should be below 0.05 %. Acceptance limits are not specified here because published data for this specific configuration are limited. The processor should generate three-lot qualification data on the intended production press and set upper and lower control limits at ±3 standard deviations for MVR and Charpy impact. That procedure is more reliable than comparing to class-typical printed ranges.
Moisture is the primary process variable. Generic ABS should be dried to a moisture content below 0.05 % before melt processing; a desiccant dryer at 80 °C for 2–4 h is the usual class-typical setting. At relative humidity above 60 %, the residence time is extended to 4 h and sealed storage is used. White grades are more sensitive to prolonged heat exposure because titanium dioxide in the presence of oxygen can contribute to yellowing. The dryer temperature should not exceed 80 °C unless the supplier certificate permits a higher set point. Even after drying, pellets should not remain in open machine hoppers for more than 30 min at 23 °C and 50 % RH because moisture regain can exceed the 0.05 % threshold.
Barrel temperature profile on a general-purpose screw with L/D 20–24 and compression ratio 2.0–2.5:1 is class-typically set from rear 180 °C, middle 200 °C, front 210 °C, and nozzle 220 °C. White grades are sometimes run at the lower end to reduce yellowing, but nozzle temperature below 210 °C can produce high melt viscosity and short shots. Melt temperature measured at the nozzle should remain within 220–250 °C for medium-flow ABS; total residence time should not exceed 8 min at full melt temperature. Back pressure is maintained at 0.5–1.0 MPa to improve pigment dispersion without excessive shear heating. Thermal stability is screened by running MVR at 220 °C/10 kg on dried pellets and on material retained in the barrel for 10 min. A change greater than ±20 % in MVR indicates a narrow processing window and should trigger supplier review. For white grades, the first visible sign of thermal degradation is usually a shift in CIE L*a*b* b* value rather than a gross MVR change.
For a 120-tonne hydraulic injection moulding machine, class-typical settings for intermediate-flow ABS include injection velocity 50–100 mm/s, holding pressure 50–70 MPa, and mould temperature 30–60 °C depending on surface gloss and dimensional tolerance requirements. White surfaces highlight flow lines and gate blush more than dark colours, so sequential valve gating or a well-shaped cold slug well is often used to prevent visible jetting. Production-scale failure observations include silver streaks when moisture exceeds 0.05 %, brown striations after excessive residence time or screw speed, and uneven white colour caused by insufficient back pressure or poor dispersive mixing.
If the grade is converted by sheet extrusion rather than injection moulding, a single-screw extruder with L/D 24–28 and a reverse barrel profile from 190 °C to 220 °C is class-typical; die temperature is held at 220 °C. However, this product’s extrusion viscosity must be confirmed because white pigmentation can shift melt elasticity and die swell. Published data for this specific configuration are limited, so a rheometer sweep under ISO 11443 capillary conditions is recommended before continuous extrusion is committed.
Candidate end uses for a white ABS moulding grade include appliance housings, small kitchen appliance panels, electronic equipment fronts, sanitary products, and automotive interior trim parts. Each application imposes a different standards matrix. For an appliance housing, the material should demonstrate creep resistance under continuous load at the required service temperature; for electronic enclosures, flame retardancy is verified under UL 94 or IEC 60695-11-10 at the minimum wall thickness, not at a different thickness. The presence of white pigmentation does not imply ultraviolet stability; if the part is exposed to light, the supplier must be asked for UV stabilisation data or the part must be coated or lacquered.
Chemical stress cracking is a recognised failure mode for ABS when parts contact plasticisers, ketones, esters, or glycol ethers. White parts in kitchen environments may be exposed to limonene, citrus-based cleaners, or fats; screening under ISO 22088-3 bent-strip conditions or an equivalent method is advisable. Contact with acetic acid-bearing silicones, strong solvents, or incompatible lubricants should be avoided unless validated. Annealing at 80 °C for 2 h can lower moulded-in stress but may alter dimensions; this should be evaluated on a pilot run before mass production.
Food-contact compliance is not granted by a white colour. If the application is food-contact, the grade must meet EU 10/2011 migration limits or FDA 21 CFR 177.1020 for ABS copolymers, and the pigment must also be compliant. No such compliance should be assumed for 730-3102WT without a signed statement. If Dongguan Guojia ABS 730-3102WT contains post-industrial or post-consumer recycled material, the supplier must declare the percentage and any REACH SVHC above 0.1 wt% per REACH Article 33; RoHS 2011/65/EU Annex II substances must be confirmed. The colour of a recycled white grade can vary batch-to-batch; CIE L*a*b* tolerances should be agreed between supplier and processor. A dark speck or colour streak is more visible on white surfaces, so incoming inspection should include a cosmetic plaque shot.
Substitution evaluation begins with a comparison of flow class. A high-flow ABS grade may have lower molecular weight and lower impact strength; a low-flow grade may have higher toughness but higher filling pressure. The target grade is therefore compared by melt volume-flow rate under ISO 1133-1:2022, not by supplier trade code. If the present grade has a lower MVR than the incumbent material, the processor may need higher injection velocity, higher melt temperature, or increased wall thickness. If the MVR is higher, the part may exhibit increased gate blush or jetting, especially on white surfaces.
Compared with heat-resistant ABS grades, which are often modified with α-methylstyrene or maleimide and exhibit Vicat B50 values above 100 °C, the present grade should be benchmarked using ISO 306 method B50. If continuous service temperature exceeds 80 °C, a high-heat ABS or PC/ABS alloy may be required. Compared with flame-retardant ABS, which may contain brominated or phosphorus-based additives that reduce melt stability and increase density, a standard ABS grade is usually UL 94 HB only, subject to thickness. If UL 94 V-0 is required, a white FR grade with a valid yellow card should be specified.
Compared with PC/ABS alloys, the differentiation is made by low-temperature impact and heat resistance. PC/ABS grades generally exhibit higher Vicat and higher notched Charpy impact at -30 °C or -40 °C under ISO 179-1/1eA; however, they are higher density and may require higher drying temperatures. If a white unpainted interior component requires low-temperature impact, the candidate should be compared on 80 × 10 × 4 mm Charpy bars rather than on a room-temperature test only. Compared with a natural ABS plus masterbatch route, a pre-compounded white grade may reduce dosing error and improve colour consistency, but it can shift melt viscosity due to titanium dioxide dispersion. The actual dispersion state should be checked on a polished cross-section or by optical microscopy at 100× magnification. Published data for this specific configuration are limited; therefore, a side-by-side trial with the incumbent material is the only reliable substitution test.
| Adjacent material class | Key differentiator | Typical class boundary | Consequence for substitution |
|---|---|---|---|
| General-purpose ABS | ISO 1133-1:2022 MVR at 220 °C/10 kg | Medium flow often 10–20 cm³/10 min | MVR must match the existing moulding window; colour does not override flow class |
| High-heat ABS | ISO 306 method B50 | HR grades routinely above 100 °C | Use only if continuous service temperature exceeds 80 °C |
| Flame-retardant ABS | UL 94/IEC 60695-11-10 | V-0 at specified thickness requires yellow card | Do not infer flame retardancy from the ABS base resin or white colour |
| PC/ABS alloy | ISO 179-1/1eA at -30 °C or -40 °C | Generally higher low-temperature impact than ABS | Use for low-temperature impact or high heat, with higher density and drying cost |
| Natural ABS plus white masterbatch | Dispersion and colour measurement | Masterbatch dosing typically 2–4 wt% but depends on pigment concentration | Pre-compounded white can reduce dosing error but may shift MVR and Charpy impact |
Before a production changeover, the incumbent and candidate materials should be compared on the same moulding machine using recorded cushion position, peak injection pressure, part mass, colour coordinates, and post-moulding shrinkage for at least three consecutive shots. The comparative values must be retained as part of the change-control record.