| HS Code | 186490 |
| Polymer Type | Acrylonitrile Butadiene Styrene (ABS) |
| Density | 1.04 g/cm³ |
| Melt Flow Rate | 30 g/10 min (220 °C/10 kg) |
| Tensile Strength At Yield | 44 MPa |
| Elongation At Break | 30% |
| Flexural Strength | 68 MPa |
| Flexural Modulus | 2300 MPa |
| Notched Izod Impact Strength At 23c | 245 J/m |
| Rockwell Hardness | R105 |
| Heat Deflection Temperature At 1 82mpa | 85 °C |
| Vicat Softening Temperature | 95 °C |
| Mold Shrinkage | 0.4–0.7% |
| Ul 94 Flammability | HB |
| Processing Method | Injection Molding |
| Color | Natural |
As an accredited Kumho Petrochemical ABS 750SW factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Kumho Petrochemical ABS 750SW is supplied in moisture-resistant 25 kg paper bags, palletized for industrial handling and storage. |
| Container Loading (20′ FCL) | A 20-foot FCL container loaded with Kumho Petrochemical ABS 750SW, securely palletized and optimized for safe, efficient transport. |
| Shipping | Kumho Petrochemical ABS 750SW is a non-hazardous ABS resin supplied as solid pellets. It is not regulated for transport and has no UN number or hazard class. Ship as general cargo in closed, dry packaging; protect from moisture, heat, sunlight, and contamination. Follow the SDS and local regulations. |
| Storage | Store Kumho Petrochemical ABS 750SW in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, moisture, and ignition sources. Keep original bags closed and palletized, avoiding crushing or deformation. Maintain stable temperature and low humidity to prevent moisture pickup and property changes. Use first-in, first-out stock rotation; avoid prolonged outdoor exposure and excessive stacking. |
| Shelf Life | Typically 12 months in unopened original packaging, stored cool, dry, and protected from moisture and direct sunlight. |
Kumho Petrochemical ABS 750SW is introduced into automotive interior mounting-clip and trim-bezel production lines as an unfilled ABS injection-moulding compound. In a typical multi-cavity cold-runner tool with 8 to 24 cavities, the pellet feed is first dehumidified in a desiccant-wheel hopper dryer set to 80 °C for 3 h to 4 h, with a return-air dew point of -30 °C or lower. The target residual free moisture, determined by Karl Fischer titration according to ISO 15512, is below 0.05 % by weight. If moisture content exceeds 0.08 %, splay marks and local melt fracture appear at gate lips because the butadiene phase generates volatile decomposition products during high-shear filling. On the injection side, a general-purpose screw with 20:1 L/D ratio and a non-return ring is operated with a flat temperature profile from rear zone to nozzle of 210 °C to 240 °C. Mould wall temperature is commonly held between 40 °C and 60 °C. Short-fill in thin clip arms is controlled not by raising barrel temperature but by increasing injection velocity; when ram velocity is too low, premature frozen skin forms in ribs as thin as 1 mm and the filling stage terminates before full packing. Packing pressure for clip retention features is set at 60 % to 80 % of the peak cavity pressure, with holding time of 3 s to 6 s for wall sections around 2 mm. Post-mould shrinkage measured against ISO 294-4 is normally in the range of 0.4 % to 0.7 %, and clip retention design must compensate for this linear contraction. Accelerated heat ageing at 85 °C for 500 h in accordance with ISO 188 is used by several automotive first-tier suppliers to screen colour drift and embrittlement before production release. The butadiene phase is the limiting microstructural feature during continuous exposure above 80 °C; therefore unpainted under-hood use is not recommended for this grade. Compliance for interior parts is checked against OEM-specific VOC and odour panels based on VDA 270 and VDA 278, the latter quantifying toluene equivalents and total volatile condensable substances rather than a single generic emission figure.
| Processing parameter | Set range or target | Test or equipment reference |
|---|---|---|
| Dryer type | Desiccant-wheel hopper dryer | Return-air dew point monitoring |
| Drying temperature | 80 °C | Hopper thermocouple calibration |
| Drying time | 3 h to 4 h | Dryer residence timer |
| Return-air dew point | -30 °C or lower | Capacitance dew-point sensor |
| Residual moisture target | 0.05 % by weight maximum | ISO 15512 / Karl Fischer |
| Melt temperature range | 210 °C to 250 °C | Nozzle pyrometer |
| Mould wall temperature range | 40 °C to 70 °C | Thermocouple or thermal imaging |
| Screw L/D ratio | 20:1 to 24:1 | General-purpose ABS screw |
| Melt cushion | 3 mm to 5 mm | Screw-position transducer |
| Maximum hot residence time | 8 min | Barrel discharge timer |
In thin-wall appliance control-panel frames for microwave ovens and washing-machine facias, wall thickness is frequently reduced to 1.2 mm to 2 mm to save mass and cycle time. The melt flow length from the central gate to the last filling corner may exceed 150 mm, which places the ABS 750SW melt in a shear-thinning regime where apparent viscosity at 1000 s⁻¹ falls below the low-shear plateau. If the cushion is maintained outside the 3 mm to 5 mm window, screw-stroke position variation causes inconsistent transfer from velocity-controlled filling to pressure-controlled packing. A cushion below 2 mm risks decompression of the non-return ring and sends pressure oscillations back through the screw; a cushion above 6 mm leaves excessive melt residence time in the barrel and can darken the resin through oxidation of butadiene unsaturation. Mould temperature is typically set between 45 °C and 70 °C, with higher values used for grained surfaces requiring improved texture reproduction. The melt temperature measured at the nozzle is maintained between 230 °C and 250 °C, and residence time at melt temperature is capped below 8 min to avoid yellow shift. Flow hesitation at rib intersections is monitored through short-shot series at 85 %, 90 %, and 95 % fill, with the short-shot data used to relocate venting rather than to increase packing pressure. Regulatory compliance for household appliance enclosures is verified with IEC 60335-1:2020 clause 30.2, and the material is tested according to IEC 60695-11-10 for burning behaviour, the end part usually classified as HB at the minimum wall thickness. Colour fastness in appliance white grades is measured by ISO 4892-2 method A or B after 100 h of xenon-arc exposure, although the base resin is not suitable for UV-stable exterior applications without painting or co-extrusion. Venting depth for ABS is limited to 0.02 mm to 0.03 mm; deeper vents create flash at thin-edge junctions. Cycle time for a 2 mm wall appliance facia is frequently constrained by cool time rather than filling, and cool time is calculated from part thickness and mould temperature rather than prolonged holding pressure.
When ABS 750SW is used in visible electrical accessory bodies such as wall switch plates and socket cover trims, the ejection temperature and surface-replication indices dominate process-control decisions because the consumer side is treated as a Class A surface. The mould cavity is commonly polished or etched to an SPI B-1 or equivalent texture, and the part is ejected only after the surface temperature drops below the Vicat softening temperature measured by ISO 306 method B50, which is typically above 90 °C for unfilled ABS. Draft angles of 1.0° to 2.0° per side are used on perpendicular walls, but textured surfaces require an additional 0.5° per 0.025 mm of texture depth. Small ejector pins in switch plates often leave witness marks if ejection speed is too high; therefore ejector-stroke velocity is limited to 50 mm/s to 80 mm/s until the part separates. Shrinkage anisotropy in flat plate geometries is controlled by using a rectangular fan gate rather than a pinpoint gate; a fan gate across 60 % of the short side produces unidirectional flow and reduces side-to-side bow measured after 24 h of post-mould storage per ISO 294-4. Electrical accessory parts require compliance with the RoHS Directive 2011/65/EU recast for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE; screening is performed by X-ray fluorescence according to IEC 62321-3-1. The ABS butadiene phase does not generate listed restricted substances, but pigment masterbatches must be verified because certain cadmium-based reds and lead-based chromes are not permissible. For wall plates, dimensional stability under mechanical loading is not evaluated by tensile tests alone; the relevant creep behaviour under a 10 N point load at 40 °C for 1000 h is usually screened with a bespoke fixture based on ISO 899-2. The processing boundary is that ABS 750SW is not inherently weather resistant; repeated exposure to ultraviolet light without a UV-absorbing additive, paint, or film lamination leads to carbonyl formation and gloss loss after outdoor exposure cycles under ISO 4582.
When ABS 750SW is combined with bisphenol-A polycarbonate at a mass ratio of 70:30 or 60:40 for automotive pillar trim and knee-bolster substrates, the viscosity mismatch between the two phases determines the screw-recovery rate and the lower barrel-temperature limit in a co-rotating twin-screw extruder. Polycarbonate at 260 °C to 280 °C has a zero-shear viscosity roughly one order of magnitude higher than ABS at equivalent processing temperature, so a single-stage mixing zone operating at 240 °C to 260 °C may leave undispersed polycarbonate domains. The melt-blending line is typically configured with a 40:1 to 44:1 L/D ratio and kneading blocks arranged in two dispersion zones; barrel zone temperatures are set from 240 °C to 270 °C, with the last zones held at 250 °C to limit thermal degradation of the butadiene phase. Vacuum venting at -0.08 MPa to -0.09 MPa gauge is applied downstream of the first mixing zone to remove residual moisture and low-molecular-weight volatiles. Screw speed is constrained by specific mechanical energy input, commonly between 0.18 kWh/kg and 0.25 kWh/kg for this class of blend. Increasing screw speed above 600 rpm can generate local temperature overshoot at the intermeshing region and initiate oxidative yellowing; die-plate melt temperature is maintained below 280 °C. The compounded material is tested for Charpy notched impact according to ISO 179-1/1eA, tensile properties according to ISO 527-2, and Vicat softening temperature according to ISO 306 method B50. Process-control charts track screw torque, melt pressure at the screen changer, and pellet moisture after centrifugal drying; if melt pressure ahead of the screen changer drifts above the normal band by more than 0.5 MPa, the operator checks screen-pack blinding from undispersed PC domains. Published data for the specific ABS 750SW/PC melt-blend configuration is limited; blend mechanical data must be generated on the production extruder rather than inferred from similar ABS grades.
In consumer toy and child-care moulding programmes, the first gate-freeze stage is usually retarded by using a lower mould temperature to prevent excessive glossy patches on matte-textured surfaces. ABS 750SW parts are gated at the hidden underside and packed for 2 s to 4 s after screw transfer to avoid sink marks above bosses. The assembly of a toy housing often uses ultrasonic welding; horn design and amplitude are selected to produce a shear joint with an interference of 0.3 mm to 0.5 mm. Because toy standards apply to the finished article rather than the resin alone, mechanical and chemical tests are performed on the final coloured moulding. Heavy-metal release is controlled by EN 71-3, and phthalate plasticisers are screened under EU Regulation 1907/2006 Annex XVII entries 51 and 52. ABS 750SW does not require phthalate plasticisers, but a supplier masterbatch or processing aid can introduce restricted substances. Flammability of toys is tested according to EN 71-2; the surface-pile flashover criterion is not applicable to rigid ABS, but burn rate is still assessed on the assembled toy. Impact evaluation of small-format wheeled housing parts is often performed by a 1 J to 5 J falling-dart test based on ISO 6603-2. Residual monomer and volatile content are relevant where mouth contact is foreseeable, and the manufacturer should consult applicable migration limits under EU 10/2011 or national food-contact legislation for the final coloured article.
When cavity pressure transducers read a peak fill pressure above 120 MPa in thin, long-flow wiring-duct covers, the ABS melt enters a region where frozen-layer growth during filling accelerates pressure loss and increases the risk of short shots at the last rib intersection. The wiring-duct cover has a flow-length-to-thickness ratio above 150:1, and the initial injection speed is often raised to 120 mm/s to 200 mm/s ram velocity to keep the melt-front velocity above 200 mm/s. A slow melt front causes premature solidification and visible hesitation lines at each rib, while an excessively high velocity at the gate area overheats the local melt and lowers surface gloss around the gate. Pressure measurement is carried out with piezoelectric cavity-pressure sensors installed behind ejector sleeves or directly in the movable half; the integral of pressure over time after switch-over is used to monitor hold consistency. Packing pressure is set to 70 % to 90 % of the peak injection pressure, and gate-freeze time for a 1.2 mm-thick section is estimated from the decay of the hydraulic pressure curve. If the screw does not reach the set transfer position because fill pressure exceeds machine capability, the options are to add a flow leader in the tool, increase mould temperature from 50 °C to 65 °C, or increase melt temperature within the allowed upper limit of 250 °C. Dimensional control in wiring-duct covers is checked against ISO 294-4 for shrinkage and ISO 291 conditioning at 23 °C and 50 % relative humidity for 24 h. The part is also subjected to ball-pressure testing according to IEC 60695-10-2 when used as an enclosure in electrical installation. The ABS 750SW resin cannot be expected to retain geometry at continuous service above its heat deflection temperature; wiring-duct covers near high-current busbars therefore require a temperature-mapping study with thermocouples placed at the contact points.
On painted decorative trim lines for door upper mouldings and centre console side panels, the thermal load of the curing oven is the limiting boundary condition for ABS 750SW rather than the injection phase itself. Moulded parts are first washed with an alkaline degreaser and oven-dried below 60 °C for 15 min to 20 min; adhesion promoters based on chlorinated polyolefins or acrylic primers are then applied before a two-pack polyurethane topcoat. The curing oven is held at 80 °C to 85 °C for 30 min, which is near the upper continuous thermal tolerance of the butadiene phase. Heat deflection temperature measured by ISO 75-2 method A at 1.80 MPa is generally below the oven set point, but unsupported flat parts can warp when local surface temperature exceeds the Vicat softening point; fixture lines must support complex curvature during curing. Cross-cut adhesion is tested according to ASTM D3359 method B, with a passing score of 5B on the moulded grain surface after 24 h ambient recovery. Chemical resistance of the cured clearcoat is screened with automotive-fluid spot tests using ISO 2812-4; rejection occurs if the paint film loses adhesion around the spot boundary. The ABS 750SW substrate is not inherently resistant to strong solvents; exposure to methyl ethyl ketone, acetone, or esters in cleaning operations must be strictly excluded because these solvents swell and craze the butadiene phase. A paint-line audit also monitors gloss consistency of the unpainted moulded grain, because local surface-shear differences from injection phase alter topography and influence final painted appearance after clearcoat. The most common production failure is paint delamination over gate-blush zones, which is traced back to excessive melt temperature or poor gate design rather than to the paint system itself.
In multi-cavity connector bodies moulded with valve-gated hot-runner systems, the sequencing of valve-pin opening controls knit-line placement and pack uniformity. If all valve pins open simultaneously, the melt fronts collide at unintended locations and create V-notched knit lines that reduce impact performance in snap-fit latching arms. The valve-pin opening stroke is typically set to 8 mm to 12 mm, and the opening delay between adjacent gates is tuned to 0.2 s to 0.5 s so that the leading melt fills the main body before side gates inject into bosses. Melt temperature is maintained at 240 °C to 250 °C, with the hot-runner manifold controlled within ±2 °C between nozzles. A thermal imbalance of 5 °C or more causes the hotter nozzle to deliver lower-viscosity melt and produces cavity-to-cavity mass variation beyond 1 %. Part mass acceptance is usually set to ±0.5 % of the mean shot mass, measured on a precision scale with 0.01 g resolution. Injection speed profile is stepwise: slow initial advance of 20 mm/s for the first 5 mm of screw movement, then fast fill at 120 mm/s to 180 mm/s, and a final deceleration before switch-over. Electrical connector bodies tested under IEC 61984 require dimensional stability through soldering heat, and the part must resist short-term peak temperature without losing pin retention. Pin retention is evaluated by a pull-out fixture at 50 mm/min crosshead speed, with acceptance values derived from the end-use connector specification. ABS 750SW is selected when the connector housing does not require sustained exposure above 80 °C; for high-heat connectors, the material class is changed to a heat-modified grade rather than extending the service boundary of standard ABS.
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Kumho Petrochemical ABS 750SW is an unfilled acrylonitrile-butadiene-styrene terpolymer supplied as cylindrical pellets for injection moulding of dimensionally stable parts requiring high melt fluidity. The polymer class is identified under CAS 9003-56-9. The grade is positioned in the high-flow segment of the manufacturer's ABS portfolio, where a reduced continuous-phase molecular weight and controlled rubber-phase morphology are used to lower melt viscosity without eliminating the two-phase structure responsible for impact strength. Typical property determinations for this product class are reported under ISO 1183-1, ISO 1133-1:2022, ISO 527-2, ISO 178, and ISO 180/1A, although lot-specific certificates of analysis control the values that may be relied upon for production qualification. Published data for the exact 750SW formulation may vary between regional technical datasheets; therefore the representative ranges shown in the following comparison should be confirmed against the current supplier document.
The grade’s high melt fluidity separates it from general-purpose ABS because the continuous styrene-acrylonitrile copolymer fraction is adjusted to reduce chain entanglement and shear viscosity. In processing terms, this means the screw recovers more quickly, the pressure drop across a 1.5 mm flow path is lower, and thin-wall sections fill at lower hydraulic pressure. The trade-off is that notched impact strength and melt extensional toughness are reduced relative to medium-flow and high-impact ABS. The following table summarises class-typical comparative data for high-fluidity ABS, general-purpose ABS, and high-impact ABS categories; it is not a substitute for a specific 750SW certificate.
| Property | High-fluidity 750SW class | General-purpose ABS | High-impact ABS | Test method |
|---|---|---|---|---|
| Density | 1.04–1.05 g/cm³ | 1.04–1.05 g/cm³ | 1.03–1.04 g/cm³ | ISO 1183-1 |
| Melt mass-flow rate, 220 °C/10 kg | 40–60 g/10 min | 15–25 g/10 min | 8–15 g/10 min | ISO 1133-1:2022 |
| Tensile yield stress | 40–46 MPa | 43–48 MPa | 35–40 MPa | ISO 527-2/1A |
| Flexural modulus | 2,200–2,500 MPa | 2,300–2,600 MPa | 1,800–2,100 MPa | ISO 178 |
| Notched Izod impact, 23 °C | 18–24 kJ/m² | 25–32 kJ/m² | 33–45 kJ/m² | ISO 180/1A |
| Vicat softening temperature, B50 | 95–100 °C | 97–102 °C | 96–101 °C | ISO 306 |
Before melt processing, the pellet bulk is dried in a desiccant dryer at a dew point below -30 °C for 2–4 h at 70–80 °C. Hygroscopic absorption in ABS is lower than in polyamide or PET, but residual surface moisture above 0.05 wt% hydrolyzes the continuous phase at the nozzle and generates splay, silver streaking, and reduced weld-line strength. When ambient relative humidity exceeds 60 %, open hopper residence should be limited to 30 min; closed-loop conveying with dry-air purge is preferred. Hopper throat temperature should be maintained below 50 °C to prevent pellet bridging. Moisture analysis of ABS should be performed by Karl Fischer titration after vacuum drying rather than by infrared heating, because the rubber phase can degrade and release volatile matter during the measurement. A residual moisture limit of 0.05 wt% is stricter than the 0.10 wt% sometimes accepted for thick-section general-purpose ABS because surface defects in high-fluidity grades appear earlier when the melt front freezes quickly.
At barrel temperatures above 240 °C, the polybutadiene rubber phase begins to undergo thermo-oxidative crosslinking and chain scission, producing gel particles that appear as black specks in the moulded part. The practical ceiling for continuous operation is therefore set at 240 °C at the nozzle, with residence time below 5 min when the barrel set point exceeds 230 °C. In screw-recovery stall conditions, the accumulated melt should be purged before restart because the gel content increases with time in the heated barrel. Screw designs with 20:1 to 22:1 L/D and a compression ratio of 2.2:1 to 2.6:1 are typical for ABS; high-shear mixing sections are unnecessary and may increase frictional heating.
| Processing parameter | Recommended range | Equipment or standard |
|---|---|---|
| Drying temperature | 70–80 °C | Desiccant dryer with dew point below -30 °C |
| Drying time | 2–4 h | Through-air hopper or tray dryer |
| Residual moisture | ≤0.05 wt% | ISO 15512 |
| Nozzle melt temperature | 210–240 °C | Melt probe or thermocouple |
| Mould surface temperature | 40–80 °C | Water-circulation thermolator |
| Injection pressure, hydraulic | 70–120 MPa | Screw diameter 35–80 mm |
| Hold pressure | 40–60 MPa | Switch-over by cavity pressure or screw position |
| Back pressure | 0.3–0.7 MPa | Rotational metering |
| Screw speed | 50–120 rpm | 20:1–22:1 L/D general-purpose screw |
In screw-recovery-limited operations, the high melt-flow rate of 750SW reduces rotational torque and allows shorter cycle times. On a 35 mm general-purpose screw, screw speed can be maintained at 80–120 rpm; however, shot-weight consistency depends on the non-return ring. When the screw tip and ring clearance exceeds 0.08 mm, the low melt viscosity permits backflow during injection, causing shot volume variation greater than 1.5 %. Processors machining a barrel with 20:1 L/D should set decompression to 2–5 mm; excessive decompression pulls air into the melt stream and produces burn marks at the nozzle. Barrel temperature profiles for 750SW are typically reverse or flat, with the feed zone at 40–60 °C, the compression zone at 220–240 °C, and the metering zone at 220–230 °C. Operating the rear zone above 70 °C can cause pellet softening and irregular feed; this is a common failure mode on older machines without a water-cooled feed throat. If screw-recovery time exceeds the cooling time, the product is not being used at its maximum flow potential; a reduction in rear-zone temperature or an increase in screw speed may recover the lost cycle-time margin.
Injection velocity profiling modifies the shear rate at the melt front and directly influences visible flow marks, weld-line strength, and cavity-pressure distribution. For a 750SW-class resin, a flow-front velocity of 200–400 mm/s in sections thinner than 1.2 mm reduces premature freeze-off; however, excessive velocity above 450 mm/s generates shear heating and can cause surface blush or material burning at the vent. After the cavity is filled, hold pressure is maintained at 40–60 MPa until the gate freezes. On a hydraulic clamp machine, the required clamp force is commonly estimated as 5–7 kN/cm² of projected area times the part area; low-viscosity melts may require higher clamp force than general-purpose ABS because the hold pressure transmits more efficiently into the cavity. Gate seal time in ABS parts typically ranges from 1.5 s to 4 s for wall thicknesses 1–3 mm. Premature swing-back of the injection unit before gate freeze causes backflow from the cavity, creating surface sink and lowering dimensional stability. A cavity-pressure transducer is preferred for switching from velocity to pressure control; a switch-over at 95–98 % of fill volume is a practical starting point, but a pressure-based threshold of 30–40 MPa at the near-gate transducer is more consistent across ambient temperature changes.
Thin-wall parts moulded from high-fluidity ABS show reduced packing pressure loss along the flow path, but differential shrinkage remains a function of local cavity pressure and cooling rate. Mould shrinkage for 750SW-class resin is typically reported between 0.4 % and 0.7 % under ASTM D955; the exact value depends on wall thickness, gate type, and post-mould cooling. A mould-temperature distribution of ±5 °C across the cavity is necessary to hold post-mould warp below print tolerance; otherwise, the faster-freezing regions resist the constrained shrinkage of the slower-cooling regions. For packaging or housing parts with a wall thickness below 1.0 mm, the tool should be vented at 20–30 mm intervals along the last-filled region to prevent gas-compression heating and short shots. Mould cores and cavity plates should be made of pre-hardened tool steel with thermal conductivity above 25 W/m·K to maintain the specified surface temperature. Beryllium-copper inserts can reduce hot spots but should not be used in contact with moist pellets because of corrosion risk; stainless steel tooling may require higher cooling-channel turbulence because its thermal conductivity is lower.
Surface gloss of 750SW parts is more dependent on mould steel finish than on grade-specific additives. A polished cavity finish of SPI A1–A3 or VDI 3400 texture is replicated only if the melt front remains above the freeze-off temperature defined by the SAN continuous phase. For rib dimensions, the nominal wall-to-rib ratio should not exceed 1:0.6 to avoid sink marks; gate location should be on the thickest section, and flow distance to the last fill point should be below 250 mm for a 1.2 mm wall in cold-runner tools. If a hot-runner system is used, the manifold temperature should be held within 210–240 °C and the nozzle tip should be insulated to prevent premature stringing. Textured surfaces with depth below 5 µm may lose feature definition if the hold pressure is too low; therefore, after changing from a general-purpose ABS to 750SW, the hold pressure should be revalidated because the lower melt viscosity reduces pressure drop but also reduces resistance to backflow across the gate. The use of negative draft angles is not recommended because the lower melt strength of the high-flow grade does not compensate for ejection friction; ejection force may increase if pack pressure is excessive and the part remains on the core.
The 750SW designation is not a flame-retardant grade and does not carry a recognised UL 94 V-0 classification at 1.5 mm unless a specific yellow-card listing is supplied by the manufacturer. If the application requires compliance with IEC 60695-11-10, an FR-compounded ABS or polycarbonate/ABS blend should be specified, because introduction of brominated or phosphorus-based additives into 750SW reduces melt fluidity, alters colour stability, and may generate plate-out on the mould surface. Similarly, 750SW is distinct from plating-grade ABS that is formulated with a controlled butadiene particle size and adhesion promoter for electroless copper-nickel-chromium deposition; 750SW is not specified as a substrate when maximum thermal-cycle adhesion is required. Conductive carbon black modified ABS grades are also a separate class. 750SW is not an electrically conductive grade; if the final part requires surface resistivity below 106 Ω, a specialised conductive ABS should be specified instead of dry-blending conductive additive, because the resulting viscosity increase eliminates the flow advantage. For static-dissipative packaging, an external antistatic coating is often preferred over modification of the resin.
Regrind usage is governed by the melt flow shift caused by chain scission and rubber crosslinking during multiple heat histories. For injection moulding of opaque components, regrind of 750SW can be reintroduced at 10–20 wt% in a blend with virgin pellets if the particle size distribution remains below 5 mm and the bulk density is stable. Above 30 wt% regrind, melt viscosity may shift downward and impact strength may fall below the lower specification boundary; therefore a full property check under ISO 180/1A is required before serial production. Moisture reabsorption in regrind is faster than in virgin pellets because the regrind has high surface area and damaged edges. Regrind should be dried in the same desiccant dryer for at least 1 h longer than virgin pellets if the storage time exceeds 24 h at room humidity. If the regrind stream contains dust above 0.5 wt%, fines can accumulate in the vent and cause blockages; a dust separation step is necessary for long campaigns.
Regulatory classification of the resin is governed by the supplier’s safety data sheet and product compliance statement. Under the EU REACH Regulation 1907/2006, any substance of very high concern present above 0.1 wt% must be identified; processors should request a current SVHC letter for 750SW because candidate list revisions occur at six-month intervals. Under RoHS Directive 2011/65/EU Annex II, cadmium, lead, mercury, hexavalent chromium, PBB, and PBDE concentrations are each constrained to the maximum concentration values; however, compliance is a finished-article requirement rather than a resin property. A manufacturing site that handles ABS pellets at temperatures above 240 °C should monitor total volatile organic compound emissions against local air-quality permits; styrene monomer 100-42-5 and acrylonitrile 107-13-1 may be generated during thermal degradation.