| HS Code | 501996 |
| Grade | SABIC ABS X11HF |
| Polymer Type | Acrylonitrile Butadiene Styrene (ABS) |
| Mold Shrinkage Percent | 0.5-0.7 |
| Ul94 Flame Rating | HB (1.5 mm) |
As an accredited SABIC ABS X11HF factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SABIC ABS X11HF is supplied in 25 kg polyethylene-lined, moisture-resistant bags, palletized for industrial storage and transport. |
| Container Loading (20′ FCL) | SABIC ABS X11HF resin is securely loaded into a 20-foot full container load (FCL) for ocean shipment. |
| Shipping | SABIC ABS X11HF is a thermoplastic ABS resin supplied as pellets in bags or octabins. Ship in dry, ventilated containers, avoiding moisture, heat, and direct sunlight. It is not classified as dangerous goods for transport; follow the SDS and local regulations. |
| Storage | Store SABIC ABS X11HF in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers tightly closed to prevent moisture pickup and contamination. Avoid prolonged UV exposure, maintain stable temperatures, and follow first-in, first-out stock rotation. |
| Shelf Life | SABIC ABS X11HF has a shelf life of 24 months when stored dry in original, unopened packaging at ambient temperature. |
Competitive SABIC ABS X11HF prices that fit your budget—flexible terms and customized quotes for every order.
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| Property | Method | Typical range | Unit |
|---|---|---|---|
| Melt flow rate, 220 °C / 10 kg | ISO 1133-1:2022 | 18–24 | g/10 min |
| Density | ISO 1183-1:2019 | 1.04–1.05 | g/cm³ |
| Tensile stress at yield, 50 mm/min | ISO 527-2/1A/50 | 38–42 | MPa |
| Tensile elongation at yield | ISO 527-2/1A/50 | 2.2–2.8 | % |
| Flexural modulus, 2 mm/min | ISO 178 | 2,100–2,400 | MPa |
| Flexural strength, 2 mm/min | ISO 178 | 60–66 | MPa |
| Notched Izod impact, 23 °C | ISO 180/1A | 14–20 | kJ/m² |
| Notched Izod impact, -30 °C | ISO 180/1A | 7–10 | kJ/m² |
| Vicat softening temperature, B/50 | ISO 306 | 94–98 | °C |
| Heat deflection temperature, 1.8 MPa | ISO 75-2/A | 82–88 | °C |
High-fluidity ABS grades are differentiated from standard ABS by a combination of controlled rubber-phase morphology and a reduced high-molecular-weight tail in the styrene-acrylonitrile copolymer. In comparative terms, X11HF delivers higher melt flow than a general-purpose ABS of the X11 family but exhibits lower notched Izod impact, lower melt elasticity, and a modest reduction in heat deflection temperature. The practical result is that X11HF fills thinner sections and replicates fine mould texture at lower injection pressure, while parts show lower resistance to high strain-rate impact. For a wall section of 1.0 mm, filling pressure may be 25–35 % lower than that required for a medium-flow grade of the same family based on production-scale screw transfer profiles; this benefit can be applied to add cavities, reduce clamp force, or reduce flash formation in worn tools. The trade-off is that the grade should not be used in thick sections above 3.5 mm where impact and dimensional stability requirements favour a medium-flow or high-impact ABS.
Before the melt enters the screw, pellet feedstock must be dried in a closed-loop desiccant dryer using air with a dew point of -30 °C or lower. Drying at 80 ± 5 °C for 2–4 h is recommended; when ambient relative humidity exceeds 60 %, the 4 h upper bound is used and residual moisture should be verified below 0.05 wt% by Karl Fischer titration or a moisture analyser with 0.001 wt% resolution. Barrel temperature settings for a three-zone reciprocating screw of 20:1 to 24:1 L/D with compression ratio 2.2:1 to 2.6:1 are normally rear zone 210 °C, centre 220 °C, front 230 °C, and nozzle 225–235 °C. Air-shot melt temperature should not exceed 250 °C. Mould temperature is maintained at 40–60 °C for general thin-wall work; increasing cavity-surface temperature to 70 °C improves knit-line strength but extends cooling time by 10–20 % per 10 °C increment. Back pressure is set at 5–10 bar hydraulic; pressures above 15 bar can add melt enthalpy and exceed the thermal stability limit of the lubricant package. Screw rotation rate should be selected so that recovery ends 1.0–1.5 s before the cooling timer expires, avoiding static melt residence in the front zone. For microcellular or foamed processing, published data for this specific configuration is limited; X11HF is intended for compact injection-moulded structures rather than structural foam.In multi-cavity tools with flow-length-to-wall-thickness ratios above 150:1, the high fluidity of X11HF permits shorter fill times and lower cavity-pressure peaks than medium-flow ABS. The gate diameter should not be reduced below 0.6 mm for a 1.0 mm wall without verifying shear-rate limits; land lengths above 0.8 mm increase pressure drop and can cause premature gate freeze before pack. Balanced runner layouts require pressure-drop calculation with the grade-specific viscosity curve because an asymmetric layout that produces less than 0.5 % cavity-to-cavity mass variation in a medium-flow grade may produce unacceptable variation in a high-flow grade, since the lower overall pressure drop amplifies thermal imbalance. For hot-runner multi-cavity moulds, zone-to-zone temperature difference should be held within ±5 °C. When gloss is required, flow-front velocity should remain in the range 200–400 mm/s; velocities above 500 mm/s may generate jetting or gloss loss at direct gates. The injection speed profile should therefore be linear in the first 60–70 % of fill and retarded near the end of fill to prevent flash and overpacking.
The substitution of X11HF for general-purpose ABS must be evaluated as a balance between processability and end-use mechanical requirements. Under ISO 180/1A at 23 °C, X11HF notched Izod impact usually falls within 14–20 kJ/m², while a standard-flow ABS of the same product family is reported between 20 and 26 kJ/m², and a high-impact ABS can exceed 30 kJ/m². This difference restricts X11HF from thick structural brackets, power-tool housings, and low-temperature impact applications where ductility below -20 °C is required. Conversely, the higher flow of X11HF supports connector housings, appliance fascias, charger shells, printer/copier internal components, and other thin-wall parts with a nominal wall between 0.8 mm and 2.5 mm and with predominantly static loading. Compared with flame-retarded ABS grades, X11HF offers better melt stability and colour consistency because halogenated or phosphorus additives are absent. Compared with high-heat ABS grades, X11HF has a lower Vicat softening temperature and should not be used where continuous service above 85 °C is expected. Table 2 summarises representative property ranges for three ABS positions. Published data for this specific configuration is limited for coloured and recycled-content blends; validation on the production tool is required.
| Grade position | Melt flow rate, 220 °C / 10 kg | Notched Izod impact, 23 °C | HDT, 1.8 MPa | Flexural modulus |
|---|---|---|---|---|
| High-fluidity X11HF | 18–24 g/10 min | 14–20 kJ/m² | 82–88 °C | 2,100–2,400 MPa |
| Standard-flow ABS | 12–16 g/10 min | 20–26 kJ/m² | 84–90 °C | 2,000–2,300 MPa |
| High-impact ABS | 6–10 g/10 min | 30–40 kJ/m² | 86–94 °C | 1,700–2,100 MPa |
Operationally, external hot-runner manifolds should be started with manifold setpoints at 225 °C and nozzle tips at 230 °C, then allowed a thermal soak of 20–30 min before the first shot. Because X11HF has low melt viscosity, pressure drop across valve-gate systems is lower than with medium-flow ABS, but the same characteristic can create gate drool if nozzle-tip temperature exceeds 235 °C or if screw decompression is set above 3–5 mm. Accumulative residence time at melt temperatures above 240 °C should not exceed 10 min; longer hold times degrade the butadiene phase, producing yellowing, lower notched Izod impact, and increased odour. Purging after interruptions should use a high-viscosity engineering purging compound; polyolefin purge should not be used because residual incompatible material is difficult to displace from the manifold. For edge gates, gate freeze time in a 1.0 mm wall is approximately 0.5–1.0 s; transfer to hold pressure should occur just before gate freeze to maintain packing control. If the tool contains interchangeable inserts, process parameters should be re-qualified after insert changes because the low pressure margin of X11HF leaves less tolerance for cavity-volume variation.