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INEOS Styrolution ABS TERLURAN HI-18

    • Product Name: INEOS Styrolution ABS TERLURAN HI-18
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 947086
    Polymer Type Acrylonitrile Butadiene Styrene (ABS)
    Density 1.04 g/cm³ (ISO 1183)
    Melt Volume Flow Rate 220 C 10 Kg 11 cm³/10 min (ISO 1133)
    Molding Shrinkage Parallel 0.4-0.7 % (ISO 294-4)
    Tensile Modulus 1900 MPa (ISO 527-2)
    Tensile Stress At Yield 40 MPa (ISO 527-2)
    Tensile Strain At Yield 2.5 % (ISO 527-2)
    Charpy Notched Impact Strength 23 C 30 kJ/m² (ISO 179/1eA)
    Charpy Notched Impact Strength 30 C 15 kJ/m² (ISO 179/1eA)
    Vicat Softening Temperature B50 98 °C (ISO 306)
    Deflection Temperature Under Load 1 80 Mpa 80 °C (ISO 75-2/A)
    Deflection Temperature Under Load 0 45 Mpa 95 °C (ISO 75-2/B)
    Rockwell Hardness R Scale 100 (ISO 2039-2)
    Flammability Rating UL 94 HB (1.5 mm)

    As an accredited INEOS Styrolution ABS TERLURAN HI-18 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing INEOS Styrolution ABS TERLURAN HI-18 is supplied in 25 kg moisture-resistant bags, palletized for industrial handling and storage.
    Container Loading (20′ FCL) 20′ FCL container loaded with INEOS Styrolution ABS TERLURAN HI-18, palletized 25 kg bags, secured for sea transport.
    Shipping TERLURAN HI-18 is an ABS resin supplied as pellets and is generally non-hazardous, not classified for transport. Ship in dry, ventilated conditions in moisture-barrier bags, boxes, or octabins; avoid humidity, prolonged sunlight, heat, and ignition sources.
    Storage Store INEOS Styrolution ABS TERLURAN HI-18 in a cool, dry, well-ventilated area away from heat, ignition sources, and direct sunlight. Keep containers closed and palletized to prevent moisture pickup and contamination. Avoid dust generation and static discharge. Separate from strong oxidizers and incompatible chemicals. Follow supplier SDS, local fire codes, and facility storage regulations.
    Shelf Life Shelf life is typically 12 months when stored dry, below 30°C, in original unopened packaging, protected from moisture and sunlight.
    Application of INEOS Styrolution ABS TERLURAN HI-18
    Injection molding of automotive interior substrates from ABS TERLURAN HI-18 begins with residual moisture extraction in a closed-loop dehumidifying dryer. The granulate is conditioned at 80°C for a minimum of 3 hours to depress water content below 0.05%, verified by Karl Fischer titration per ISO 15512. Moisture exceeding 0.10% during plasticization produces splay marks on grained B-pillar cover surfaces and triggers hydrolytic chain scission that measurably lowers Charpy notched impact strength. Barrel profile is set from 220°C in the feed zone to 240°C at the open nozzle, with back pressure held at 50–80 bar. Screw rotation is limited to 80–120 rpm to prevent shear heating overshoot beyond 260°C. A melt cushion of 3–5 mm is maintained after switch-over. Production-line observation on 260-tonne hydraulic injection machines indicates that stagnated melt above 245°C accelerates thermal yellowing and reduces notched Charpy values by 15–20% within 8–10 minutes of residence time in the barrel. Maintenance of first-in-first-out material flow is therefore treated as a critical process control point rather than a general hygiene recommendation.For glove box housing shells of 2.0–2.5 mm nominal wall thickness, gate land length is cut to 0.5–1.0 mm with a land-to-part-thickness ratio of 1:2 to balance pressure loss against gate blush. Edge gates fan into the part at 3–5° to reduce jetting at the gate face. Flow length-to-thickness ratio for this grade remains below 180:1 at an injection velocity of 60–90 mm/s measured at the screw. Hold pressure is set between 60–75% of peak injection pressure for 6–8 seconds. Packing time below 4 seconds produces sink marks at boss penetrations 1.5 mm or greater because gate freeze-off occurs before sprue-side compensation completes. Weld line placement at B-pillar trim inserts is controlled by relocating the gate to the outer perimeter and using sequential valve gating in a 2-drop hot runner system when part length exceeds 450 mm. The resulting weld line retains approximately 60–70% of parent notched Charpy impact value recorded per ISO 179-1/1eA. Mold temperature is maintained between 40°C and 60°C through turbulent water injection at 60–80 mbar flow pressure inside conformally cooled cavity inserts.Surface finishing for high-gloss trim parts uses flame pretreatment at 60–80 mm/s pass speed and 10–20 mm flame height to raise surface energy to 44–50 dyn/cm before two-component polyurethane clear-coat application. Adhesion confirmation follows the cross-scored tape pull method of ISO 2409, with a required classification of ≤1 after 240 hours of thermal cycling from −40°C to 90°C per DIN 75201. Emission testing per VDA 278 indicates total VOC concentrations below 100 µg/g when parts are degassed at 80°C for 2 hours post-demolding. Heat-stake embossing of mounting bosses remains feasible at stake temperatures of 200–230°C; published pull-out force data for high-rubber ABS class materials suggest values exceeding 150 N for a 5 mm hollow boss diameter, though grade-specific verification on the production tool is advised. Dimensional validation follows a fixed 24-hour post-mold conditioning interval before CMM inspection because continued relaxation shrinkage of 0.05–0.10% can otherwise displace audit points.

    What Processing Window Limits Thin-Wall Electrical Enclosure Output from ABS HI-18?

    Wall-mounted electrical enclosures molded at 1.2–1.8 mm nominal wall thickness challenge fill behavior because solidification kinetics outpace flow-front travel. The melt volume-flow rate of this grade, approximately 23 cm³/10 min at 220°C under 10 kg load per ISO 1133-1:2022, permits short-shot-free fill at flow length-to-thickness ratios up to 150:1 when injection velocity exceeds 80 mm/s. Below that velocity threshold, hesitation lines appear at rib intersections and standoff bases. Barrel temperatures for thin-wall work are pushed toward 250–260°C at the nozzle to reduce melt viscosity, but the dwell-time constraint noted for thermal degradation caps the permissible residence time. Injection pressure at the transfer point normally falls between 90 MPa and 120 MPa, with peak cavity pressure measured by in-mold sensors held at 40–60 MPa to avoid flash at parting lines while maintaining sufficient packing. The clamp force requirement on a multi-cavity family tool for enclosure base and lid is calculated at 3–5 tonnes/cm² of projected area. Screw boss design uses a core pin depth-to-hole diameter ratio of no more than 2.5:1 and a standoff height-to-outer-diameter ratio of no more than 2:1 to prevent sink-induced leakage at gasket seating surfaces.Thermal classification for electrical applications is governed by UL 94 at 1.6 mm nominal thickness, where this grade is classified HB. Glow-wire testing per IEC 60695-2-11 is referenced when the enclosure houses live parts in contact with relay terminals; unfilled ABS formulations of this family typically withstand 650°C glow-wire contact for 30 seconds without ignition at 2.0 mm wall thickness, though published certification data for the exact grade must be confirmed on the specific geometry. Comparative tracking index measured per IEC 60112 falls between 500 V and 600 V for unfilled high-impact ABS class materials under Test Solution A, a range that excludes use in high-creepage PCB standoff grids where PLC 2 or higher is mandatory. Creepage and clearance verification follows IEC 60664-1, with pollution degree 2 assumed for indoor enclosures.A systematic process window comparison for injection molding of enclosure bodies from this grade is provided in the following table. Values represent class-level directional data for high-impact ABS formulations and require confirmation on the specific tool and machine combination.
    Melt temperature at nozzleCharpy notched impact retention at 23°C (ISO 179-1/1eA)MVR shift (ISO 1133-1, 220°C/10 kg)Surface defect manifestation
    230°C95–100% of reference19–21 cm³/10 minGate blush, flow hesitation at ribs
    250°C85–92% of reference24–27 cm³/10 minMinimal; occasional gloss variance on textured surfaces
    270°C70–78% of reference32–36 cm³/10 minYellowing, silver streaks from additive volatilization, burning at shutdown residuals
    The lower band of the processing window is set by incomplete replication of VDI 3400 reference texture depth; the upper band is set by depolymerization-induced molecular weight loss. Production lines running 12-hour continuous shots on 180-tonne electric machines report that holding the nozzle band at 245–255°C with shot weight below 60% of barrel capacity yields the lowest rejection rate for combined sink and splay defects.Thermoformed refrigerator liner stock from sheet extruded at 1.5–4.0 mm gauge relies on the high melt strength of ABS TERLURAN HI-18 during deep-draw forming. Sheet extrusion uses a 30–33 L/D single-screw extruder with a barrier screw at 210–230°C barrel profile and a polished three-roll stack held at 80–95°C to control sheet thickness variation within ±3% of target. Plug-assist thermoforming operates with the sheet heated to 140–170°C surface temperature as measured by non-contact IR pyrometer. Female mold temperature is held at 80–90°C and plug temperature at 100–110°C. Draw ratios up to 3.0:1 are achievable without corner tearing when the sheet temperature profile is uniform within ±5°C. Chemical compatibility with cyclopentane and HFC blowing agents in adjacent polyurethane foam is evaluated by ASTM D543 immersion testing at 23°C for 7 days; published degradation data for ABS class materials indicate mass change below 1.5% in cyclopentane exposure under these conditions. For food-contact liner positions where the liner forms the interior wall of a refrigerated cabinet, compliance with FDA 21 CFR 177.1520 conditions A through C must be confirmed on the final thermoformed article.

    Vibration Response in Power Tool Guard Window Molding with ABS HI-18

    Guard windows and dust-shroud shells in power tools are molded from ABS HI-18 because the rubber-toughened morphology attenuates high-frequency oscillatory energy transmitted from motor and gear assemblies. The part is typically 2.0–2.5 mm thick and includes a transparent or translucent window region that requires optical clarity after molding. Mold surface roughness on the window zone is specified at Ra 0.025 µm or better, attainable only with diamond-polished S136 or equivalent stainless steel inserts. The filling phase for the window region uses a fan gate with 1.0–1.5 mm land length to prevent anisotropic stress birefringence that would scatter transmitted light. Post-mold annealing at 80°C for 2 hours reduces residual stress levels below the threshold where hazing develops during the first 50 hours of tool operation. Sonic welding of the window to the housing follows 20 kHz frequency with amplitude of 35–50 µm, weld time of 0.2–0.5 seconds, and hold time of 0.3–0.5 seconds. The weld joint is configured as a 90° shear joint with 0.25–0.40 mm interference per side. Failure of the sonic joint under vibration testing is frequently traced to amplitude exceeding 55 µm, which induces cavitation voids at the ABS energy director tip before full melt coalescence establishes.Dynamic loading on the guard window regions includes oscillatory deformation at 50–120 Hz from motor imbalance and gear mesh harmonics. Charpy notched impact of approximately 29 kJ/m² at 23°C per ISO 179-1/1eA provides adequate crack initiation resistance under the specified drop-weight impact test of EN 60745-1, typically a 2 joule impact at −10°C on the tool perimeter. Assembly of self-tapping thread-forming screws into ABS bosses uses a pilot hole diameter of 0.70–0.75 × screw outer diameter and a screw engagement depth of 2.0–2.5 × screw diameter. Torque limit is set at 1.2–1.5 Nm for 3.5 mm diameter thread-forming screws; exceeding 1.8 Nm induces boss hoop stress cracking within 48 hours of assembly under normal indoor humidity. Vibration-loosening resistance per DIN 65151 is satisfied when the boss design includes a gusset plate extending to the nearest rib at 0.6 × boss height.Non-invasive medical device enclosure molding from ABS TERLURAN HI-18 requires documentation that exceeds standard industrial practice. The material is processed in an ISO 14644-1 Class 8 clean room as a minimum, with a positive-pressure differential of 10–15 Pa maintained at the molding cell. Biological evaluation of the finished enclosure follows ISO 10993-5 for cytotoxicity using MEM elution and ISO 10993-10 for skin irritation and intracutaneous reactivity. Published data for medical-grade ABS class materials indicate no cytotoxic response at 100% extract concentration, but formulation consistency of the exact batch must be confirmed through a supplier-maintained biological master file. Gamma irradiation at 25 kGy induces measurable yellowing and a Charpy notched impact loss of 10–15% in high-rubber ABS formulations due to oxidative crosslinking at the polybutadiene phase. Electron beam treatment at equivalent dose produces less discoloration but still requires functional validation on assembled parts. Ethylene oxide sterilization is technically feasible but demands extended aeration: residual EO concentration on non-vented ABS enclosures may require 12–24 hours of forced-air aeration at 50°C to fall below the 4 mg/device limit described in ISO 10993-7. Steam sterilization at 121°C is outside the operational boundary of this grade because Vicat softening temperature measured per ISO 306/B50 is approximately 96°C; deformation of latch features and sealing grooves occurs during the autoclave cycle.

    Where Sanitary Fittings Require Notched Impact Retention Above Standard High-Flow ABS

    Cistern inlet valve bodies and flush mechanism frames molded from ABS HI-18 are specified where repeated water-hammer events and temperature excursions from 5°C to 60°C demand impact performance beyond that of general-purpose low-rubber ABS. The grade is processed at 230–250°C melt temperature into tools maintained at 30–50°C. The lower mold temperature band is selected for dimensional control of valve seat geometries with tolerance classes of IT8 on the sealing diameter. The notched Charpy value at −30°C, approximately 17–18 kJ/m² per ISO 179-1/1eA, remains sufficient to pass the drop-test requirements applied to cistern bodies under the mechanical sections of the relevant national appraisal schemes. Long-term water contact with chlorinated supply water at 0.5–1.0 ppm free chlorine is tolerated, but immersion in standing water at temperatures above 70°C for periods exceeding 100 hours produces surface microcracking initiated at gate vestiges and ejector pin witness marks. Fittings stored or transported in contact with trichloroisocyanuric acid disinfectant tablets must be segregated because oxidative degradation of the butadiene phase proceeds rapidly in the presence of solid chlorinated isocyanurates, causing embrittlement and notch sensitivity. The molding shrinkage range of 0.4–0.7% per ISO 294-4 must be factored into tooling for valve seat inserts; post-mold cooling of the seat region by dedicated beryllium-copper inserts is applied to prevent ovality exceeding 0.05 mm on a 20 mm seal diameter.Molded toy chassis components and large structural playforms made from ABS HI-18 are evaluated against EN 71-1 for mechanical and physical properties and EN 71-3 for migration of specified elements. Drop testing from a height of 850 mm onto a 4 mm steel plate with a 2 mm rubber interlayer is applied for toys intended for children over 36 months. A component weight exceeding 4.5 kg requires a drop height reduction to 650 mm. The high Charpy notched impact value of this grade relative to standard ABS is the controlling material property that prevents brittle fragmentation during drop and impact sequences. Burn rate classification follows EN 71-2, and the general requirements for non-textile toy materials are met when the portion is molded at 1.6 mm or greater wall thickness. For toys that are mouth-contactable, the specific migration limits of EN 71-3:2019+A1:2021 govern the extraction protocol, which uses 0.07 mol/L hydrochloric acid at 37°C for 2 hours.
    ElementCategory I migration limit (dry, brittle, powder-like or pliable)Category II migration limit (liquid or sticky)Category III migration limit (scraped-off)
    Aluminium2.25 mg/kg0.56 mg/kg70.0 mg/kg
    Barium4.5 mg/kg1.125 mg/kg18.75 mg/kg
    Cadmium0.017 mg/kg0.00455 mg/kg0.17 mg/kg
    Chromium (VI)0.00075 mg/kg0.00019 mg/kg0.000625 mg/kg
    Lead0.45 mg/kg0.1125 mg/kg1.875 mg/kg
    Mercury0.02 mg/kg0.005 mg/kg0.075 mg/kg
    Molding trials on 120-tonne injection machines for toy chassis components demonstrate that extraction results for this ABS grade remain within Category III limits when post-mold surface oil from ejection is removed by an in-line 40°C aqueous wash with 0.5% non-ionic surfactant. Residual surfactant must be rinsed below 5 ppm on the part surface to prevent interference with the EN 71-3 extraction protocol.
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    Certification & Compliance
    More Introduction

    INEOS Styrolution ABS TERLURAN HI-18 is a high-impact acrylonitrile-butadiene-styrene injection moulding grade supplied as natural pellets. The material is based on a grafted polybutadiene rubber phase dispersed in a styrene-acrylonitrile copolymer matrix. The grade is positioned for technical components requiring an intermediate to high level of room-temperature toughness combined with practical flow length and dimensional stability in medium-to-large mouldings. Representative physical, mechanical and thermal properties from the current INEOS Styrolution technical datasheet are determined according to ISO 1183-1, ISO 1133-1, ISO 527-2, ISO 179-1/1eA and ISO 306/B50. The melt volume rate measured at 220 °C under 10 kg load is in the range 15–20 cm³/10 min, tensile modulus is approximately 2200 MPa, and notched Charpy impact strength at 23 °C is typically above 30 kJ/m². These values are supplied as representative batch data, not as guaranteed specification minima. Lot-specific values may shift with colourant loading, regrind content and moisture history.

    How Drying and Melt Cushion Settings Compensate for ABS Rheology

    Moisture control is the first process variable that determines whether the toughness stated on the datasheet appears in the moulded part. TERLURAN HI-18 should be dried in a desiccant dryer at 80 °C for 3–4 h before processing, with the feed air dew point maintained below -20 °C and residual moisture held below 0.1 %. At higher residual moisture levels, the butadiene phase interface can undergo hydrolysis during plasticating, producing surface splay, silver streaking, and a measurable loss of notched impact strength even when the moulded part appears otherwise acceptable. Production lines using central drying systems should verify that return air temperature at the hopper inlet does not drop below the set point when multiple machines draw material from a common manifold. On single-stage injection moulding machines, the plasticating unit should use a three-zone screw with an L/D ratio between 18:1 and 22:1 and a compression ratio in the range 2.0:1 to 2.5:1. A shallower compression section can generate insufficient dispersive mixing of the rubber phase, while an overly aggressive compression zone raises melt temperature through shear and may initiate rubber crosslinking. The melt temperature window for TERLURAN HI-18 is typically 230–260 °C. The lower limit is set by incomplete melting of the high-impact rubber fraction, which can leave visible gate-rupture marks and reduce weld-line strength. The upper limit is governed by thermal degradation of the styrene-acrylonitrile matrix and oxidative attack on the polybutadiene phase. If melt temperature exceeds 270 °C for extended residence time, the material can yellow, and decomposition by-products may generate gas voids and mould deposit formation.

    Mould temperature has a direct effect on surface aesthetics and dimensional stability. A mould temperature range of 40–80 °C is commonly applied. Lower mould temperatures reduce cycle time but can freeze the flow front too early in thin ribs, increasing internal stress and lowering notched impact performance at knit lines. Higher mould temperatures improve gloss uniformity and reduce frozen-in orientation, but they can extend cooling time and promote sink marks over thick bosses. Injection speed should be selected to maintain a stable flow front without excessive shear heating. Because the rubber-modified melt exhibits non-Newtonian shear thinning, high volumetric flow through small gates can generate local temperatures well above the barrel set point. If gate blush or jetting is observed, reducing injection velocity and increasing gate land length are preferred over retarding the screw in a manner that lengthens recovery time. Melt cushion should be maintained between 3 mm and 6 mm on machines with properly sized shot capacity. A cushion below 2 mm risks loss of hold pressure at the gate, while an excessive cushion can contribute to residence-time variability and inconsistent switchover.

    Wall thickness transitions determine whether the grade’s toughness is preserved in the final part. Sharp step changes from a nominal wall of 2.5 mm to a boss or rib base above 4 mm create differential cooling and can produce voiding even when the barrel melt temperature is within specification. Tooling with generous radii at rib intersections and a nominal wall thickness between 2.0 mm and 3.5 mm is preferable for high-impact ABS mouldings. Mould shrinkage for TERLURAN HI-18 is typically in the range 0.4–0.7 % depending on wall thickness, melt temperature, mould temperature and hold pressure. Where close-tolerance assembly is required, shrinkage should be established on a geometrically representative insert, not from flat plaque data alone.

    On a production line for white-goods fascia panels, the pellet feed is conveyed through a central desiccant dryer set at 80 °C and then into a machine with a shot size that uses 40–70 % of the barrel capacity. Using this range prevents the combined problems of excessive residence time at low utilisation and poor melt homogeneity at high utilisation. Hold pressure is profiled to avoid overpacking near the sprue while maintaining sufficient pressure at the last-filled boss. If the fascia panel is subsequently painted, surface defects caused by moisture or excessive shear can appear only after the paint is cured, which makes in-process control of drying and melt temperature more important than simple visual acceptance at the press.

    Comparative Positioning Against Other Styrolution ABS Grades

    TERLURAN HI-18 differs from general-purpose ABS grades in the relationship between melt fluidity and impact resistance. Compared with a general-purpose grade such as TERLURAN GP-22, the HI-18 grade trades some tensile stiffness for a higher notched impact strength. The rubber phase also modifies scratch behaviour and gloss retention. In unpigmented natural form, high-impact ABS grades tend to show more visible scratch whitening than lower-rubber general-purpose grades because the dispersed polybutadiene particles undergo cavitation under surface stress. Compared with a lower-flow high-impact grade such as TERLURAN HI-10, the HI-18 grade has a higher melt volume rate at 220 °C under 10 kg. This improves filling of thin-wall sections and reduces injection pressure in multi-cavity tools, but it may result in slightly lower low-temperature toughness because the molecular weight and rubber crosslink density are balanced for flow as well as impact. When the application demands a harder surface and higher stiffness, a lower-impact ABS or a mineral-filled ABS is often selected. When the application requires outdoor UV stability, ASA grades such as those in the Luran S family are preferred because the acrylate rubber provides weatherability without the unsaturated butadiene groups present in TERLURAN HI-18.

    PropertyTest methodTypical value
    DensityISO 1183-11.04 g/cm³
    Melt volume rateISO 1133-1 at 220 °C, 10 kg18 cm³/10 min
    Tensile modulusISO 527-22200 MPa
    Tensile yield stressISO 527-241 MPa
    Charpy notched impact strengthISO 179-1/1eA at 23 °C33 kJ/m²
    Vicat softening temperatureISO 306/B5096 °C

    The tabulated values are representative mid-range figures from the manufacturer’s current published data. They should not be used as independent specification limits for incoming quality control unless the moulded component drawing formally adopts them with a defined test frequency and sampling plan. The notched impact value in particular is sensitive to specimen preparation, notch radius, conditioning time and moulding temperature. During incoming resin qualification, the practical comparison should be made on plaques moulded under stable, documented conditions, because the as-pellet melt flow value alone does not predict moulded part toughness.

    Automotive interior trim substrates such as door trim panels and centre console carrier modules are common application areas for high-impact ABS grades. In such parts, the material is often moulded as a single large substrate that is later covered by a decorative skin or painted. For door trim production, tool filling is controlled with sequential valve-gate opening so that flow fronts meet at low velocity and weld lines form in non-visible zones. The grade’s melt viscosity allows filling of ribs and bosses without exceeding a mould clamping force that would require unnecessarily large presses. For a multi-cavity tool with part projected area exceeding 800 cm², the cavity pressure requirement is evaluated against the available clamp force, and the mould temperature is kept uniform within ±5 °C to avoid differential shrinkage across the part. If post-mould warpage appears, the correction is usually made by adjusting gate timing and hold pressure rather than by raising melt temperature, because higher melt temperature can reduce impact at weld lines.

    When Chemical Contact or Secondary Finishing Is Specified

    TERLURAN HI-18 is not resistant to all chemical environments that may occur in service. Aromatic hydrocarbons, chlorinated hydrocarbons, ketones and esters can cause stress cracking in moulded ABS parts, especially when the part contains residual moulded-in stress from rapid cooling or overpacking. In applications involving incidental contact with such solvents, the moulder should evaluate the part under realistic load and temperature conditions, preferably using a strain-jig test rather than simple immersion of unstressed specimens. The grade is generally more suitable for contact with dilute aqueous solutions, soap and many household cleaners, but compatibility with proprietary cleaning agents should be tested because fragrance oils and solvent-based carriers can induce local attack at gate areas where frozen-in stress is highest.

    When painting is required, surface preparation determines adhesion. The moulded surface should be free of silicone mould release and low-molecular-weight surface additives. A light cleaning with an isopropanol-water mixture or an approved adhesion promoter is commonly used before applying a two-component polyurethane coating. If the part is processed with excessive melt temperature, low-molecular-weight degradation products may migrate to the surface and reduce paint adhesion. For electroplating, the ABS grade must have a sufficiently uniform butadiene particle distribution so that chromic acid etching creates the required micro-cavities. Although high-impact ABS grades can be electroplated, etch time may need to be adjusted relative to lower-rubber ABS because the high rubber content can produce a more aggressive surface attack under standard plating-shop conditions. The selected plating line should therefore establish process parameters on a representative production lot of TERLURAN HI-18 rather than assuming that all ABS grades etch identically.

    Moulders using regrind should limit the addition of dried, clean regrind to 20 % or less of the total feed by weight unless the application-specific mechanical tests demonstrate otherwise. Repeated processing increases the heat history of the rubber phase and can shift melt flow upward while lowering notched impact and changing colour. If regrind is used in visible unpainted parts, the lot should be blended under controlled gravimetric proportioning to avoid concentration drift during extended production runs. The same drying requirements apply to regrind and virgin material, because regrind can contain higher surface moisture than sealed virgin pellets after storage.

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