| HS Code | 559732 |
| Polymer Type | Acrylonitrile Butadiene Styrene (ABS) |
| Grade | NOVODUR 248 |
| Processing Method | Injection Molding |
| Density | 1.05 g/cm³ |
| Melt Volume Flow Rate 220 C 10 Kg | 20 cm³/10 min |
| Mold Shrinkage | 0.4-0.7% |
| Tensile Modulus | 2200 MPa |
| Tensile Stress At Yield | 45 MPa |
| Tensile Strain At Yield | 2.5% |
| Charpy Notched Impact Strength 23 C | 15 kJ/m² |
| Heat Deflection Temperature 1 80 Mpa | 85 °C |
| Vicat Softening Temperature B 50 | 98 °C |
| Rockwell Hardness | 100 R |
| Ul Flammability Rating | HB |
As an accredited INEOS Styrolution ABS NOVODUR 248 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | INEOS Styrolution ABS NOVODUR 248 is supplied in 25 kg moisture-resistant paper bags, stacked and palletized for bulk shipment. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with INEOS Styrolution ABS NOVODUR 248, palletized 25 kg bags, shrink-wrapped and secured for ocean freight. |
| Shipping | INEOS Styrolution ABS NOVODUR 248 is shipped as solid thermoplastic pellets in moisture-proof bags or octabins. It is not regulated as dangerous goods for transport. Keep packages closed, cool, dry, and protected from sunlight and contamination. No special shipping labels or UN number are required. |
| Storage | Store INEOS Styrolution ABS NOVODUR 248 in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and open flames. Keep containers or bags sealed and palletized to prevent moisture pickup, contamination, and damage. Avoid prolonged high humidity and elevated temperatures, follow first-in, first-out rotation, and maintain good housekeeping to minimize dust. |
| Shelf Life | Shelf life is typically 24 months when stored in dry, closed original packaging at moderate temperatures, protected from moisture and direct sunlight. |
Production of high-gloss cosmetic parts for countertop kitchen appliances relies on the high melt-volume rate of INEOS Styrolution ABS NOVODUR 248 to fill contoured facia tools without visible flow hesitation marks. A desiccant dryer is set to 80 °C with a sealed hopper exit dew point of −20 °C or lower, and residence time is held at 2–4 h until residual moisture is below 0.10 wt%. If moisture is not controlled, splay and a measurable reduction in specular gloss on polished mould surfaces occur, a failure observed on production floors where ambient humidity exceeds 60 % RH. Melt temperature is maintained within 230–255 °C at the nozzle, with a flat barrel profile leaning toward the upper bound only when the part length exceeds 300 mm. Mold temperature is kept at 55–75 °C with a tolerance band of ±5 °C across movable and fixed halves to stabilise gloss and reduce post-mould dimensional drift. Injection velocity is profiled, with switch-over at 95–98 vol% fill by screw position and packing pressure at 50–70 MPa hydraulic for 6–12 s depending on gate freeze. Polished tool steel with surface roughness Ra 0.05 µm or better is required; textured surfaces lower measured gloss per ISO 2813 and should be reserved for non-cosmetic rear shells. Regrind from sprues and runners is capped at 20 wt% and only closed-loop metered to avoid melt viscosity drift that changes flow-front velocity and visible contour lines. Terminal parts include blender base housings, espresso machine front bezels, stand-mixer head covers, and electric kettle lower shells. Compliance for such appliances is against IEC 60335-1 for general safety, with migration of food-contact-adjacent surfaces excluded from this grade unless separately validated; non-food-contact external housings dominate.
In thin-wall power tool shells with nominal wall thickness 1.5–2.0 mm and flow path/wall thickness ratios exceeding 200:1, gate blush and weld-line brittleness are the main process-defect pairs. The high MVR of the grade—reported in lot certificates in the 24–30 cm³/10 min range at 220 °C/10 kg per ISO 1133-1:2022—permits fast filling on toggle clamp machines of 800–1,600 kN clamp force without exceeding practical injection pressures. Nozzle melt temperature is raised to 250–260 °C only where weld-line depth is visible on textured surfaces, but the upper bound is constrained by yellowing and by mould deposit on vents. Mold temperature is biased to 60–80 °C because higher thermal mass of steel keeps the weld region above the glass transition long enough for molecular interdiffusion; part-specific impact retention at the weld line should be measured using ISO 179-1/1eA on notched specimens cut from the last converging flow front. Gate blush is controlled by a two-stage injection profile: slow initial velocity of 20–40 mm/s screw advance through the gate for the first 2–3 mm of linear displacement, followed by ramp to 120–200 mm/s depending on cavity volume. Packing pressure is limited to 60–80 % of peak injection pressure, applied for a duration corresponding to the gate-seal time on the pressure-drop curve; underpacking produces sink opposite bosses and overpacking creates gate stress that lowers drop-impact performance on cordless drill housings. Hot runner geometry uses valve-gated drops with tip orifice not exceeding 1.0 mm and manifold temperature 240–260 °C; dead spots in open nozzles can produce black specks after colour change. Peripheral vents of 0.02–0.03 mm depth are required along the last-fill boundary, because deeper vents create flash under pack pressure and shallow vents trap gas-caused short shots at the swirl texture. A three-zone screw with L/D 20:1 and compression ratio 2.0–2.5:1 is used. Regrind from rejected shells is limited to 10–15 wt% because higher levels reduce weld-line impact retention on drop-tested tools. Terminal products include orbital sander grips, angle-grinder motor housings, and cordless drill clamshells where the part must survive a 1 m drop onto concrete per customer-specific production audit, typically evaluated by change in internal boss height or visible shell separation rather than a formal standard.
Automotive interior applications using NOVODUR 248 are restricted to indirect-sunlight lower trim and passenger-compartment components because the grade is not specified for long-term exterior UV exposure. Accelerated interior solar simulation under DIN 75220 can be used for part validation, but published data for this specific configuration is limited beyond lot-specific certificates. For glovebox housings, driver-side lower column shrouds, and seat-belt buckle trim in dark colours, melt temperature is kept at 240–255 °C and mold temperature at 50–70 °C. Continuous heat exposure at 85 °C in a forced-air convection oven for 500 h typically requires post-age tensile strength retention above 80 % of the original value tested to ISO 527-2/1A and notched Charpy retention above 60 % of the original value tested to ISO 179-1/1eA; final acceptance is vehicle-platform-specific. Drying is 2–4 h at 80 °C to 0.10 wt% residual moisture because any moisture-related splay on visible grain surfaces is unacceptable after IMG skin lamination or low-pressure back-foaming. For polyurethane foam-backed instrument panel lower trim, the ABS substrate must be free of external mould release that inhibits adhesion; silicone-free mould release or clean-room mould maintenance is used. Regrind for automotive soft-feel parts is usually limited to 10 wt% because higher regrind fractions widen molecular weight distribution and reduce grain definition in laser-textured or chemical-etched mould surfaces. Migration of plasticisers from PVC skin laminates into the ABS core can be assessed by storage at 70 °C/50 % RH; if plasticiser migration is observed as surface tack, an ABS/PVC-compatible barrier is required because NOVODUR 248 does not include an intrinsic barrier layer.
| Sector | Standard / Test method | Condition | Control criterion |
|---|---|---|---|
| Kitchen appliance fascia | IEC 60335-1, ISO 2813 | 20° specular gloss on polished reference plaque | No visible splay; gloss within customer-lot upper/lower limits |
| Power tool housings | ISO 179-1/1eA | Notched Charpy on weld-flow-front specimens | Part-specific minimum accepted by drop-test correlation |
| Automotive lower trim | DIN 75220, ISO 527-2/1A | Interior solar simulation, 85 °C heat age for 500 h | Tensile retention above 80 %; impact retention above 60 % |
| Toys and recreational parts | EN 71-3 | Migration of elements on finished component | Within EN 71-3 category limits for the stated material |
| Electrical enclosures | IEC 60695-2-11 | Glow wire at 650 °C | No ignition or self-extinguishing within 30 s where end-product standard requires |
| Regrind return on non-cosmetic parts | ISO 1133-1:2022 | MVR at 220 °C/10 kg after 100 h continuous return | Lot value deviation not more than 10 % from virgin reference |
For toys and recreational components, the use of ABS NOVODUR 248 is driven by complex multi-cavity filling and by the absence of intentionally added plasticisers. The production environment must maintain melt temperature below 250 °C to avoid generation of styrene monomer odour that becomes detectable in sealed polybagged toys after storage at 40 °C. Drying uses 80 °C for 2–4 h to 0.05–0.10 wt% residual moisture; the lower end applies when parts are shipped to tropical distribution centres with high warehouse humidity. Mould temperature is set at 40–60 °C for general toy parts and raised to 60–70 °C for high-gloss wheels, head shapes, or build-block surfaces where sink marks are visually inspected. Ejector pin placement follows the requirement that no pin mark creates a sharp edge; ejection angle is not less than 0.5° per side and part designs use radii of 0.4 mm minimum on internal corners to reduce stress-cracking risk under repeated drop loads. Regrind from coloured toy lots is excluded from white or pastel lots because pigment carryover shifts colour coordinates beyond tolerance; for dark colours, 10 wt% is allowed if optical sorting rejects black specks. The material must be tested by the converting producer against EN 71-3 for migration of elements—barium, cadmium, chromium, lead, mercury, selenium, antimony, arsenic—on the finished component, with the caveat that pre-coloured masterbatch pigments and process additives can alter the migration profile. Terminal parts include building-block housings, ride-on toy fenders, doll furniture panels, and handheld plastic toy casings. In two-colour moulding with thermoplastic elastomer overmoulding, melt-temperature interlocking requires the substrate surface to reach 110–130 °C at the bonding interface before TPE injection; bond strength is then evaluated by peel testing on a tensile machine rather than by subjective hand-pull.
Electrical enclosure covers and base shells made from NOVODUR 248 require part design that manages ejection temperatures high enough to cause post-mould warpage if cooling time is shortened below 15 s. Melt temperature is set from 230–250 °C; the lower end is used for thick bosses with 3.0–4.5 mm wall intersections to reduce sink. Mold temperature at 40–70 °C is selected by wall thickness distribution, with thin snap features run at the upper end to minimize frozen-in stress. Injection pressure measured at the machine screw tip typically falls within 90–140 MPa for moulded parts with wall thickness 2.0–2.5 mm; holding pressure is fixed by observing pressure drop at the gate and is generally 60–70 % of peak. For ventilation slots and louvre grids, ejection speed is reduced to 20–30 mm/s for the first 5 mm of ejector travel to avoid plastic deformation of the still-soft ribs; a forming-force test using a force gauge verifies that no louvre exceeds 5 N deflection resistance loss after sorting. Compliance is against IEC 60695-2-11 glow-wire tests where the end-product standard demands a 650 °C glow wire with no ignition or with self-extinguishing within 30 s after the wire is removed; however, the base grade is only UL 94 listed as HB at 1.5 mm, so it is unsuitable for enclosures requiring V-2 or better unless an FR grade is substituted and separately approved. Indoor switchgear cover plates, low-voltage terminal shrouds, and LAN router lower shells are typical products where live parts are separated and the material serves as non-current-carrying structural cladding. Regrind is capped at 15 wt% and must be free of polyester label contamination because label remnants can generate carbon specks at processing temperatures above 240 °C.
With post-industrial regrind fractions above 10 wt% in NOVODUR 248, melt viscosity shifts and gloss uniformity on high-cosmetic parts can be reduced if the regrind contains shredded hot-runner drool or material previously dried at excessive temperature. The conditional scenario applies mainly to rear housings, internal brackets, and wire-management channels where appearance is secondary. On production inline regrind blending equipment, metered addition is set at 10–25 wt% only if the regrind fraction is closed-loop with loss-in-weight feeders and the base resin is dried in a separate hopper at 80 °C for 2–4 h. Higher regrind content, particularly above 25 wt%, lowers the melt viscosity to the point that cushion length becomes unstable and switch-over by screw position varies by ±2 mm, producing inconsistent packing on multicavity tools. Melt temperature should be reduced by 5–10 °C when regrind content exceeds 20 wt% because the regrind fraction already carries a heat history; this prevents yellowing and formation of gels in the melt. A production-scale test protocol includes measuring MVR to ISO 1133-1:2022 after 100 h of continuous regrind return and confirming that the lot value does not deviate more than 10 % from the virgin value. Tensile yield stress is checked per ISO 527-2/1A and notched Charpy per ISO 179-1/1eA on specimens from the first, middle, and last shots of a production day. Gloss readings are compared to the incoming virgin reference moulding under ISO 2813; a drop of more than 10 GU at 20° geometry triggers regrind reduction to 10 wt% or part downgrade to non-visible duty. Typical components under this scenario include appliance rear covers, vacuum cleaner wheel housings, cable spools, and internal printer chassis parts.
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INEOS Styrolution ABS NOVODUR 248 is an amorphous acrylonitrile-butadiene-styrene terpolymer supplied as cylindrical pellets for high-flow injection moulding. The three-phase morphology consists of a continuous styrene-acrylonitrile matrix and discrete polybutadiene rubber particles, which provide the notch-sensitivity reduction that distinguishes ABS from polystyrene. In production planning, the grade is selected for thin-wall components where a balance between melt fluidity, dimensional stability, and moderate impact resistance is required. The polymer can be processed on conventional single-screw injection-moulding machinery with a general-purpose polyolefin screw and is commonly specified for electronic housings, appliance trim, cosmetic packaging, and non-structural automotive interior parts. The following paragraphs set out the standardized property window, processing boundaries, and product-positioning logic.
Incoming resin quality is controlled against ISO and DIN methods rather than supplier nominal values alone. The property ranges in Table 1 represent the typical public datasheet envelope for high-flow ABS in the NOVODUR family; the grade-specific certificate of analysis should be consulted for lot-level acceptance limits because the supplier may apply tighter internal release windows for automotive or appliance programmes.
| Property | Test method | Typical window |
|---|---|---|
| Density | ISO 1183-1 | 1.04–1.06 g/cm³ |
| Melt volume rate at 220 °C/10 kg | ISO 1133-1 | 16–24 cm³/10 min |
| Tensile stress at yield | ISO 527-2 | 40–48 MPa |
| Tensile modulus | ISO 527-2 | 2100–2600 MPa |
| Charpy notched impact at 23 °C | ISO 179-1 | 12–22 kJ/m² |
| Vicat softening temperature, 50 N/50 °C/h | ISO 306 | 94–102 °C |
| Heat deflection temperature at 1.8 MPa | ISO 75-2 | 88–96 °C |
| Mould shrinkage | ISO 294-4 | 0.4–0.7 % |
All values are single-point determinations on dry-as-moulded specimens conditioned at 23 °C and 50 % relative humidity. Charpy notched impact values cannot be interchanged with Izod notched results without a correlation study because the two test geometries produce different stress states and fracture paths. The certificate of analysis for each lot should be compared against the table envelope; releases outside the envelope do not necessarily indicate a defective lot if the deviation is within the supplier’s internal control limits and is traceable to a documented test apparatus bias.
The melt exhibits shear-thinning behaviour typical of ABS; apparent viscosity at processing shear rates between 500 s⁻¹ and 5000 s⁻¹ decreases by approximately an order of magnitude. This pseudoplastic response influences pressure drop calculations in runner systems. A capillary viscometer conforming to ISO 11443 can be used to generate the viscosity–shear-rate master curve; the data should be corrected for Bagley entrance pressure and Rabinowitsch wall shear rate before transfer to injection-moulding simulation packages.
Before melt processing, granules must be dried in a desiccant dryer with a dew point not higher than -30 °C and an air temperature maintained at 80 °C to 90 °C. A hopper residence time of 3 h to 4 h is normally sufficient when the as-received moisture content is below 0.2 %. If handling occurs above 60 % relative humidity, the residence time should be extended to 6 h; lot-to-lot moisture content should be checked before silo transfer because after ocean freight in high-humidity regions, as-received moisture can exceed 0.2 %. Inadequate drying manifests as splay, silver streaking, and loss of Charpy impact due to hydrolytic chain scission during plastication. Production-scale experience on dehumidifying hopper dryers shows that intermittent machine stoppages longer than 20 min can recharge surface moisture on dried granules; hopper outlets should therefore be heated or blanketed with dry air when the downstream injection unit is idle.
Pellets should be conveyed with clean stainless steel tubing and dedicated resin-handling lines. Cross-contamination with polycarbonate, polyamide, or acetal can generate delamination, odour, or melt-pressure instability. If the same hopper is used for multiple resins, the cleaning protocol should include a purging compound capable of removing degraded ABS from the screw root, check ring, and nozzle body.
For a wall thickness between 1.2 mm and 2.5 mm, the process window should be validated on the target machine rather than transferred from another grade. A melt temperature of 230 °C to 260 °C is typical; the lower bound is constrained by flow length and gate blush, and the upper bound by discoloration and volatile generation. Mold temperatures of 40 °C to 80 °C are used, with the upper half of the range applied when surface gloss or textured cavity replication is specified. Injection velocity is a pressure-limited parameter on hydraulic machines; values of 50 mm/s to 120 mm/s screw-ram speed are common, but cavity filling should be profiled to avoid jetting at the gate and hesitation marks behind ribs. Hold pressure typically falls between 50 MPa and 70 MPa, and gate seal time is set by weight stabilization after 3 s to 6 s of holding. Clamp force can be estimated from projected area multiplied by an assumed cavity pressure of 30 MPa to 45 MPa; a part with 250 cm² projected area therefore requires a machine with at least 750 kN clamp force under the lower cavity-pressure assumption. Conventional three-zone screws with L/D ratios of 18:1 to 22:1 and compression ratios of 2.0:1 to 2.5:1 are acceptable; high-shear barrier screws should be evaluated for excessive melt temperature rise above 5 °C at maximum screw speed.
Tooling considerations include generous venting at the end of fill, polished runners with no sharp conical restrictions, and gate diameters of 0.8 mm to 1.5 mm for pin-point or tunnel gates. Flow hesitation in ribs thinner than 0.7 mm has been observed when mold temperature is below 50 °C, producing lower gloss and visible knit lines. Weld-line strength in high-flow ABS is sensitive to melt temperature and holding; destructive pull tests on weld-line specimens should be included in process capability studies because weld-line efficiency can drop below 70 % of bulk tensile yield when the flow front temperature is too low.
Mold deposit formation is dependent on vent depth, melt temperature, and volatile degradation products. Vents should be maintained at depths of 0.02 mm to 0.04 mm for ABS; deeper vents can cause flash and shallower vents increase gas burn marks. Periodic tool maintenance should include inspection of vent channels after 50,000 cycles or when gloss reduction is detected on texture surfaces.
Chemical resistance is limited by the acrylonitrile and butadiene phases. The material tolerates aqueous acid and alkali solutions, aliphatic hydrocarbons, and many oils at ambient temperature, but stress cracking is accelerated by ketones, esters, chlorinated hydrocarbons, and aromatic solvents. Components under external strain above 0.5 % should not be exposed to methanol or isopropanol without validation using ISO 4599 or ISO 22088-3. Painting and solvent-based bonding operations require a masked adhesion and environmental stress-cracking test on production moldings, not on compression-moulded plaques, because frozen-in orientation alters solvent absorption kinetics. For decorative electroplating, the adhesion of the ABS substrate is influenced by the butadiene etch pattern; processers should verify the etch bath concentration and temperature against the supplier’s recommended range rather than substituting a generic ABS plating line without pilot trials.
The following checklist is not a declaration of conformity; each lot and colour match must be verified against the supplier’s current documentation and the specific end-use regulation.
| Regulatory domain | Reference | Typical requirement |
|---|---|---|
| REACH | Regulation (EC) No 1907/2006 | SVHC declaration at 0.1 % w/w per Article 33 |
| RoHS | Directive 2011/65/EU amended by (EU) 2015/863 | Restricted substances below threshold |
| Food-contact polymer class | 21 CFR 177.1020 | End-use suitability determination required |
| Flammability | UL 94 | Thickness-dependent Yellow Card classification |
The principal difference between NOVODUR 248 and high-impact NOVODUR P2H-AT lies in the rubber phase content and its effect on melt viscosity and energy absorption. NOVODUR 248 is positioned closer to the high-flow segment of the NOVODUR range, with a higher melt volume rate and a lower notched Charpy impact value than P2H-AT. This position makes it more suitable for multi-cavity tools with long flow paths and thin sections, where a high-impact grade would require higher melt temperature or wider gates. When compared with P2MC, the distinction is narrower; both are flow-optimized injection-moulding grades, but the datasheet ranking of low-temperature impact and Vicat softening must be checked for the current production version because compound modifications can shift the balance. Direct numerical comparison should not be based on single-point data alone; ISO 179-1 Charpy and ISO 1133-1 melt volume rate cover different shear histories and cannot be combined into a single selection index without defining a weighted scoring model. Published data for this specific configuration is limited in some regions; therefore, grade substitution must be confirmed against the current supplier technical datasheet and a production trial on the intended tool.
Operational boundaries for high-flow ABS apply with equal force to NOVODUR 248. Melt residence time at temperatures above 260 °C should not exceed 8 min, and shutdown sequences should lower barrel temperature to 180 °C within 30 min to avoid degradation products that plate out on screw and check-ring surfaces. The polymer is also incompatible with amine-based mould-release additives and with residual PVC purge; both can generate flow marks or delamination at the part surface. For any regulated food-contact or medical application, the converter must obtain a grade-specific declaration from INEOS Styrolution, because generic ABS compliance statements do not transfer across suppliers or grades.