| HS Code | 847156 |
| Density | 1.04 g/cm³ |
| Melt Flow Rate 220 C 10 Kg | 10 g/10 min |
| Tensile Strength At Yield | 45 MPa |
| Tensile Elongation At Break | 15% |
| Flexural Modulus | 2200 MPa |
| Flexural Strength | 65 MPa |
| Charpy Notched Impact Strength 23 C | 20 kJ/m² |
| Vicat Softening Temperature | 100°C |
| Heat Deflection Temperature 1 82 Mpa | 80°C |
| Rockwell Hardness | 105 R |
| Processing Temperature | 230-250°C |
| Bed Temperature | 90-110°C |
| Drying Temperature | 80°C |
| Drying Time | 4 h |
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Versalis Impressio ABS B 10 is an unfilled acrylonitrile-butadiene-styrene terpolymer supplied in pellet form for conversion into fused-filament-fabrication feedstock. The product is not a finished monofilament; it is an extrusion-grade resin whose downstream product is typically a round filament with a nominal diameter of 1.75 mm or 2.85 mm, wound onto spools under controlled tension. The material contains a continuous styrene-acrylonitrile copolymer phase and a dispersed grafted polybutadiene rubber phase. The styrene-acrylonitrile phase governs stiffness, chemical resistance, and thermal softening, while the rubber phase provides energy absorption in notched impact. The designation Impressio ABS B 10 identifies a medium-flow ABS in which the melt volume-flow rate is controlled for stable strand geometry and acceptable screw torque during filament extrusion. Where Versalis-specific certified values are unavailable, the following engineering data are identified as class-representative for unfilled medium-flow ABS rather than manufacturer-locked specifications.
For pellet-to-filament conversion, the controlling envelope is set by the thermal sensitivity of the polybutadiene phase and the shear heating generated in a single-screw extruder. Barrel profiles for unfilled ABS extrusion grades are typically set with a feed-zone temperature of 180–200°C, a compression-zone temperature of 210–230°C, and a metering/die-zone temperature of 220–250°C. Melt temperature above 260°C should be avoided because the unsaturated butadiene segments undergo oxidative degradation, producing yellow chromophores, reduced melt strength, and volatile products that can generate vacuum voids in the filament. A single-screw extruder with a screw L/D ratio of 24:1 to 30:1 and a barrier-flight section is suitable; compression ratios are maintained between 2.5:1 and 3.0:1. Melt pressure at the breaker plate is usually held between 50 bar and 150 bar, with screen packs of 60–100 mesh to trap gel bodies without imposing excessive backpressure. The graded MVR of Impressio ABS B 10, when confirmed by ISO 1133-1:2022 at 220°C/10 kg, falls within the medium-flow envelope of approximately 8–12 cm³/10 min; this is low enough to preserve melt strength in free-air strand formation but high enough to limit screw-torque excursions. Closed-loop diameter control, using a dual-axis laser gauge and vacuum sizing tank, is required for maintaining 1.75±0.05 mm or 2.85±0.10 mm geometry.
Residual moisture is a less obvious but equally significant process variable. Although unfilled ABS does not hydrolyze as rapidly as polyamide or PET, equilibrium moisture at 23°C and 50% RH is in the 0.2–0.4% range. If the resin enters the hopper above 0.05% moisture, steam can evolve in the metering zone and disrupt the melt seal, producing splay, elliptical filament cross-section, and surface microvoids. Production-scale desiccant dryers with a dew point of −40°C and an air temperature of 80±5°C for 4 h are used when bulk moisture exceeds 0.1%. In plants with ambient humidity above 60% RH, hopper venting alone is insufficient; the feed throat must be blanketed with dry air, and reground edge trim must be re-dried before blending at 20–30 wt% with virgin pellets. Batch-to-batch variation in moisture and residual monomer can shift melt viscosity by more than the MVR envelope suggests; therefore the converter controls barrel profile by melt-temperature feedback rather than by fixed heater setpoints alone.
The performance of filament produced from Impressio ABS B 10 is specified through the test methods applied to molded standard specimens and, where necessary, printed coupons. Because ABS properties are conditioned strongly by sample preparation, ISO 291:2008 atmosphere of 23°C and 50% relative humidity is applied before testing. The candidate envelope in Table 1 covers unfilled medium-flow ABS grades; it is not a substitute for the Versalis batch certificate for the B 10 designation. Machines used to verify these properties include universal testing machines with Class 1 load cells per ISO 7500-1:2018, pendulum impact testers with appropriate energy ranges, and capillary melt-flow testers conforming to ISO 1133-1:2022.
| Property | Reference method | Candidate engineering envelope |
|---|---|---|
| Density | ISO 1183-1:2019 | 1.04–1.06 g/cm³ |
| Melt volume-flow rate | ISO 1133-1:2022 | 8–12 cm³/10 min at 220°C/10 kg |
| Tensile stress at yield | ISO 527-2:2012 | 40–46 MPa |
| Tensile modulus | ISO 527-2:2012 | 2,200–2,600 MPa |
| Charpy notched impact strength at 23°C | ISO 179-1:2010 | 18–22 kJ/m² |
| Vicat softening temperature B50 | ISO 306:2022 | 96–102°C |
| Heat deflection temperature at 0.45 MPa | ISO 75-2:2013 | 90–98°C |
| Mold/printed linear shrinkage | ISO 294-4:2018 | 0.4–0.7% |
The tensile properties alone do not determine fused-filament performance. The limiting mechanical property is interlayer weld strength. Test specimens printed in the vertical Z direction fail at a lower stress than those cut in the XY plane because the diffusion of polymer chains across the weld interface requires sufficient nozzle temperature and a high-chamber-temperature environment. For a medium-flow ABS such as B 10, the ratio of Z-direction tensile strength to XY tensile strength is commonly reported by filament converters but is absent from general resin datasheets; published data for this specific configuration is limited. The practical implication is that tensile modulus and yield stress from molded plaques should be treated as upper-bound values for printed parts.
Distinguishing the grade from unfilled PLA starts with thermal stability. PLA has a Vicat softening point near 55–60°C under ISO 306:2022 B50, which limits washed parts in warm machine housings and causes softening in enclosed service conditions. The candidate B 10 envelope of 96–102°C permits short-term contact with warmer surfaces but does not confer continuous-use approval above the HDT of the grade, measured at 0.45 MPa according to ISO 75-2:2013. PLA is also brittle under notch impact, whereas the polybutadiene phase in ABS B 10 dissipates energy. PETG generates less warp and gives better interlayer bonding, but its modulus is generally lower and its glass transition temperature is lower than the SAN continuous phase of ABS; PETG also requires stringent drying and is sensitive to moist storage. ASA substitutes a saturated acrylic ester elastomer for the unsaturated butadiene elastomer of ABS. B 10, unless specifically compounded with UV stabilizers, is therefore not the first selection for unpainted outdoor exposure; the butadiene double bonds are the main site of photo-oxidation. For indoor functional prototypes, jigs, fixtures, and low-series housings, the ABS choice is driven by the combination of notched impact, rigidity, and thermal resistance rather than by any single tested property.
Within the ABS polymer family, melt-flow class is the primary differentiator. High-flow ABS grades with MVR values above 20 cm³/10 min at 220°C/10 kg are formulated for rapid injection molding; their lower molecular weight reduces melt strength to the point where the molten strand necks under gravity between the die and cooling bath. They also exhibit lower Charpy impact and can suffer die-swell instability when pulled at filament speeds above 30 m/min. High-impact ABS grades contain a higher rubber fraction; Charpy notched impact may exceed 30 kJ/m², but tensile modulus and HDT decrease, and die swell increases, which complicates diameter control. Impressio ABS B 10 is positioned in the medium-flow, medium-impact segment, where the balance is biased toward filament processability. Published data for this exact grade in printed applications is limited; converters should obtain the batch-certified MVR, residual monomer content, and moisture specification before setting barrel profiles. Injection molders using B 10 may find the melt flow viable for thick-walled parts, but the grade is specifically marketed for filament extrusion rather than high-speed injection cycles.
On production-scale twin-screw compounding lines used to prepare color-matched variants, the base B 10 pellet can be dry-blended with pigments or carbon black masterbatch; however, the final filament converter must avoid high-shear mixing above 250°C because color concentrates can carry low-molecular-weight carriers that depress melt strength. Batch-to-batch variance in melt flow can be controlled by inline rheometers after the metering section; if measured viscosity deviates by more than ±5%, the barrel setpoints are adjusted. Spooling tension is maintained at 0.5–1.0 N for 1.75 mm filament and 2.0–4.0 N for 2.85 mm filament; higher tension induces ovality after cooling. A vacuum sizing tank with a water temperature of 40–60°C and laser diameter gauge at 1 kHz sampling provides the inline feedback necessary to hold tolerance.
Import, use, and specifying activities require the documentation set in Table 2. Documentation alone does not guarantee fitness for a particular electrical or food-contact end-use; the end product must be tested in final geometry.
| Obligation/Standard | Test or clause | Application to import and use |
|---|---|---|
| REACH Regulation (EC) No 1907/2006 | Article 33 SVHC communication | Resin and filament supply-chain declarations |
| RoHS Directive 2011/65/EU | Annex II, XRF or chemical screening | Printed parts for electrical/electronic equipment |
| ISO 291:2008 | 23°C/50% RH, 88 h conditioning | Mechanical testing of printed coupons |
| ISO 1133-1:2022 | MVR at 220°C/10 kg | Incoming resin acceptance |
| ISO 527-2:2012 | Type 1A/B tensile specimen | Molded and printed tensile values |
| ASTM D638-14 | Type I for rigid plastics | Comparison of FFF coupon data |
| ISO 179-1:2010 | Charpy notched impact at 23°C | Impact requirement verification |
| ISO 306:2022 | Vicat softening temperature B50 | Thermal misuse scenario verification |
Post-printing, B 10-based ABS parts can be solvent-welded or vapor-smoothed with acetone or methyl ethyl ketone under controlled ventilation. Vapor smoothing reduces surface roughness but may introduce residual solvent and reduce sharp features; for jigs and fixtures, the process is validated by dimensional checks before production use. Mechanical properties after solvent exposure should be re-tested per ISO 527-2:2012 because solvent uptake can plasticize the SAN phase. This is a further difference from PLA, which does not respond to acetone vapor smoothing; PLA typically requires abrasion or coating.
On an open-frame printer, a B 10-based filament exhibits differential shrinkage between the initial deposited layer and the heated bed. When bed temperature is below 90°C, corner lifting is observed as the part cools; when the bed is above 110°C, bottom-layer deformation can approach the Vicat softening point. An enclosed build chamber at 60–80°C reduces the vertical gradient and lowers the probability of interlayer cracking. The coefficient of linear thermal expansion for the ABS class is typically 80–110 µm/m·K under ISO 11359-2:1999, and this value drives the magnitude of residual stress. For thin-walled sections, print speed is reduced and the part-cooling fan is limited to avoid premature solidification at the weld line. These limits are operational boundaries inherent to styrenic three-dimensional printing feedstock, not defects of the B 10 grade.