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INEOS Styrolution ABS TERLURAN 968K

    • Product Name: INEOS Styrolution ABS TERLURAN 968K
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 633468
    Grade TERLURAN 968K
    Polymer Type ABS (acrylonitrile-butadiene-styrene)
    Flammability Ul94 HB
    Processing Method Injection molding

    As an accredited INEOS Styrolution ABS TERLURAN 968K 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 968K is supplied in 25 kg moisture-resistant bags, palletized for industrial handling and storage.
    Container Loading (20′ FCL) 20′ FCL: INEOS Styrolution ABS TERLURAN 968K in 25 kg bags, palletized, shrink-wrapped, and secured for ocean shipment.
    Shipping INEOS Styrolution ABS TERLURAN 968K is a non-hazardous thermoplastic acrylonitrile-butadiene-styrene copolymer supplied as pellets, typically shipped in 25 kg bags or bulk containers. Store dry, away from direct sunlight and heat; avoid moisture and contamination during transport. Not classified as dangerous goods under ADR/RID/IMDG/IATA.
    Storage Store INEOS Styrolution ABS TERLURAN 968K in a cool, dry, well-ventilated area, protected from direct sunlight, heat, moisture, and contamination. Keep in original sealed packaging until use; reseal opened bags. Avoid prolonged storage in humid conditions. Stack containers securely to prevent deformation, and keep away from ignition sources and incompatible chemicals.
    Shelf Life Typically two years when stored dry at ambient temperature in original unopened packaging, away from direct sunlight.
    Application of INEOS Styrolution ABS TERLURAN 968K

    Thin-wall monitor bezel and printer cover production using Terluran 968K begins with closed-loop desiccant drying at 80 °C for 2–4 h until residual moisture falls below 0.10 wt% as determined by ISO 15512:2019. On a 24:1 L/D general-purpose screw with compression ratio 2.3:1–2.6:1, the barrel profile is set between 210 °C and 250 °C, nozzle at 235–245 °C, mold temperature 40–70 °C, and back pressure 0.5–1.5 MPa. Formulation for these electronic enclosures typically uses Terluran 968K at 97.0–99.5 wt% with a polycarbonate- or SAN-carrier color masterbatch at 0.5–3.0 wt%; where electrostatic dissipation is mandated, a permanent antistatic concentrate is let down at 2.0–5.0 wt%, and the resulting compound is not representative of the neat grade’s gloss retention. In 16-cavity monitor bezel tools with valve-gated hot runners, gate vestige and flow hesitation at weld lines are controlled by maintaining shear rate at the gate below 45,000 s⁻¹ and by specifying vent depths of 0.02–0.03 mm along the last 30% of the flow path. Packing pressure is held at 50–70% of peak injection pressure for 0.3–0.5 s/mm wall thickness, with cooling time 15–35 s for 1.2–2.0 mm wall; dimensional checks follow ISO 294-4 for molding shrinkage, and final assembly accepts parts within ±0.05 mm on snap-fit features. Compliance for these housings is governed by IEC 62368-1:2023 for audio/video, information and communication technology equipment, with material flammability classification evaluated under IEC 60695-11-10 at 1.5 mm thickness, typically achieving UL 94 HB rather than V-0; RoHS Directive 2011/65/EU Annex II and REACH Regulation (EC) No 1907/2006 Article 33 apply. The terminal part families are flat-panel monitor bezels, printer front covers, scanner lids, and router fascias. The operational boundary is that Terluran 968K should not be specified for enclosures directly shielding unfused power-supply components or for parts requiring UL 94 V-0 at wall thickness below 3.0 mm without an FR masterbatch, because brominated or phosphorus flame-retardant concentrates reduce flow length and gloss while increasing cycle time.

    With piano-black automotive interior trim specified for low odor and low fogging, Terluran 968K is commonly fed as the ABS component of a PC/ABS blend rather than as a neat resin. A production-side formulation for non-structural interior parts uses 40–55 wt% Terluran 968K, 45–60 wt% polycarbonate, 0.3–0.6 wt% phosphite antioxidant concentrate, 0.2–0.5 wt% UV stabilizer concentrate, and 2.0–3.0 wt% carbon black or piano-black color concentrate; the ratio is adjusted within these limits because impact at -30 °C and Vicat temperature move in opposite directions with PC content, and values below 40 wt% PC can fail OEM heat-aging checks near 110 °C. The compound is pre-dried at 100–110 °C for 4 h to residual moisture below 0.02 wt% because polycarbonate hydrolyses at melt temperature. Injection molding is run in variothermal molds with water/glycol temperature units capable of cycling from 80 °C to 110 °C, melt temperature 250–270 °C, and hydraulic pressure 100–180 MPa; the hot-and-cool cycle removes weld lines and raises the 60° glossmeter reading above 90 GU per ISO 2813. Compliance is evaluated against ISO 3795:1989 or FMVSS 302 for horizontal burn rate, VDA 270:2018 for odor grade, VDA 278:2011 for VOC and SVOC emissions, and DIN 75201 for gravimetric fogging; production lots with odor grade above 3 are typically rejected for visible interior trim. The resulting terminal products are center console side trims, door switch bezels, seat side shields, and high-gloss door panel inserts. The material is not specified for load-bearing instrument panel retainers, airbag covers, or metal insert overmolding where insert temperature falls below 80 °C, because locked-in stress around bosses and ribs produces microcracking after ambient-temperature impact testing.

    When Hot-Runner Residence Time in Washing Machine Fascia Molding Exceeds 18 Minutes

    Molding of washing machine fascia and vacuum cleaner housings from Terluran 968K at wall sections from 1.8 mm to 3.0 mm uses shot-weight-to-shot-time calculations to prevent barrel residence time beyond 18 min at 250 °C; longer residence causes butadiene-phase yellowing, black specks, and a drop in notched impact observed on the production floor as split bosses during screw-boss ultrasonic welding. The formulation is kept close to neat: 98.0–100 wt% virgin Terluran 968K, 0.8–2.0 wt% appliance-specific carbon black or colored masterbatch, and no external lubricant because external paraffin wax at 0.3 wt% blows gloss homogeneity and delays surface freeze. Pre-drying is performed in hopper dryers with dew point below -30 °C at 80 °C for 2–4 h. The injection process uses a general-purpose screw with 20:1–24:1 L/D and compression ratio 2.2:1–2.6:1; melt temperature 230–250 °C; mold temperature 50–80 °C; the first-stage fill stops at 95–98% of part volume, and packing pressure 50–80 MPa is held for 0.4–0.8 s/mm to avoid sink marks around ribs. For household appliances, the compliance set includes EN 60335-1:2012+A2:2019 for general safety, glow-wire end-product testing per IEC 60695-2-11:2021 at 550 °C and 650 °C depending on current-carrying proximity, ball-pressure testing per IEC 60695-10-2:2014 at 75 °C for non-current-carrying external parts and 125 °C for live-contact supports, plus RoHS 2011/65/EU and REACH Article 33. The terminal parts are washing machine control panels, dishwasher front door trim, vacuum cleaner upper housings, and fascia rings. The grade is not used for oven door frames or exterior surfaces with continuous service above 80 °C, as dimensional stability under clamping force falls away near the grade’s Vicat softening temperature.

    Interlocking toy bricks and model railroad structural components made from Terluran 968K impose a tighter connection between mold shrinkage and clutch force than non-locking ABS parts. The compounding is deliberately simple: 100 wt% virgin Terluran 968K with heavy-metal-free pigment masterbatch at 1.0–3.5 wt%, no filler, no external wax above 0.1 wt%, and no regrind above 20 wt% because post-industrial material causes inconsistent shrinkage and stud-to-tube interference. Molding is performed on multi-cavity tools with 16–64 cavities, precision ejector systems, and valve-gated hot runners; melt temperature is 220–240 °C, mold temperature 30–50 °C, injection velocity 80–200 mm/s, and holding pressure 40–70 MPa, with cooling time 8–25 s for wall thickness 1.6–3.2 mm. Dimensional control follows ISO 294-4 for molding shrinkage, with a target of 0.4–0.6% to keep the brick footprint within ±0.05 mm and achieve repeatable clutch force between 1.5 N and 4.0 N on an 8-stud pull test; molds are temperature-mapped across fixed and moving halves because a 3 °C difference across the parting line produces bowing visible in base plates longer than 200 mm. Compliance is anchored to EN 71-3:2019+A1:2021 for migration of 19 elements, ISO 8124-3:2020, ASTM F963-23 for the US market, and REACH Annex XVII entries 51 and 52 for phthalates and CMR substances. The terminal products are interlocking construction bricks, base plates, roof slopes, and model railway structural members. This application excludes food-contact toys, mouth-interactive articles, and any part requiring solvent welding because Terluran 968K is not specified as a food-contact or solvent-cement grade.

    Double-Insulated Clamshell Housings and the 85°C Continuous-Service Ceiling

    Handheld drill clamshell housings in the 900–1,400 W class are injection molded from Terluran 968K in tools with hydraulic core pulls and two-stage ejection because the grade provides sufficient flow for long, ribbed half shells without the cost of polycarbonate. The formulation uses 98.0–100 wt% Terluran 968K and 2.0–4.0 wt% color concentrate; if an overmolded soft-grip TPE is used, the TPE is injected as a second component in a rotary platen, and the ABS substrate is maintained at 60–80 °C to ensure adhesion without softening. Pre-drying at 80 °C for 3 h to below 0.10 wt% moisture is required; wet material produces splay on textured surfaces because water vapor scours the melt at the gate. The ABS is processed with melt temperature 230–250 °C, mold temperature 40–80 °C, injection pressure 90–160 MPa, packing pressure 60–90 MPa, and cooling time 20–45 s depending on wall thickness from 2.0 mm to 3.5 mm; warpage in long half shells is controlled by cooling fixtures held at 20–30 °C for 30–60 s after ejection. Compliance for power tools is assessed under IEC 62841-1:2014 and EN 62841-1:2015, with material classification per IEC 60695-11-10 at 1.5 mm thickness, typically UL 94 HB, and with RoHS 2011/65/EU Annex II. The terminal components are drill half shells, orbital sander bodies, jigsaw housings, and charger cradle trim. Terluran 968K is not specified for gear housings carrying motor bearings, battery packs requiring UL 94 V-0 or V-1, or surfaces continuously heated above 85 °C by motor vents.

    Office chair base shells and armrest supports in heavy-use seating are injection molded from Terluran 968K with a regrind fraction that is controlled because batch-to-batch impact scatter in armrest fatigue tests increases above 25 wt% reprocessed material. The compound for BIFMA X5.1-tested seating uses 75–100 wt% virgin Terluran 968K, 0–25 wt% clean post-industrial regrind from the same grade, and 2.0–4.0 wt% color concentrate; no external impact modifier is added unless the chair is specified for cold-storage use below 5 °C. Drying at 80 °C for 2–4 h in desiccant dryers with dew point below -30 °C prevents gas marks at the base of rib junctions. Molding uses a large-platen machine with clamp force sized at 1.5–2.5 kN/cm² projected area, melt temperature 230–250 °C, mold temperature 40–70 °C, injection velocity 60–120 mm/s, packing pressure 50–80 MPa, and cooling time 30–60 s for wall thickness 2.5–4.5 mm. Dimensional checks against the mounting plate are taken after 24 h post-mold conditioning to account for shrinkage to 0.4–0.7%; boss pull-out testing on chair bases is performed on a tensile tester with a 5 kN load cell until failure exceeds 1,800 N. Compliance for office seating is assessed under ANSI/BIFMA X5.1-2021 for the North American market and EN 1335-1:2020 for European office work chairs, plus REACH (EC) No 1907/2006 Annex XVII for restricted substances in accessible plastic components. The terminal products are five-star chair bases, armrest shells, castor sockets, and lumbar support shells. Terluran 968K is not specified for structural gas-lift columns or for chair base arms that bear direct user-load without a metal insert.

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    Certification & Compliance
    More Introduction

    INEOS Styrolution ABS TERLURAN 968K is an acrylonitrile-butadiene-styrene injection molding grade supplied as natural and colored pellets within the Terluran series. The grade is differentiated by a reduced melt viscosity for an impact-modified ABS, which translates into lower injection pressures in thin-wall tools and shorter filling times for multi-cavity molds. Two values are decisive for initial material selection: melt volume-flow rate determined under ISO 1133-1 at 220 °C and 10 kg is typically 26 cm³/10 min, and density determined under ISO 1183-1 is 1.04 g/cm³. The material is classified as an ABS injection-molding grade under ISO 2580-2, but the exact lot designation should be confirmed against the certificate of analysis because property tables are not contractual minima. The product is not a flame-retardant grade; UL 94 classification at the manufacturer-tested thickness is HB. These characteristics position TERLURAN 968K between general-purpose ABS and high-impact ABS in terms of viscosity and toughness.

    Material Identity, Classification, and Typical Property Data

    The data below are drawn from the manufacturer’s typical property sheet and represent conditioned specimens under ISO 291 at 23 °C and 50 % relative humidity. The tensile data are generated with ISO 527-2 specimens at 23 °C, and the Charpy data refer to single-edge notched specimens according to ISO 179-1/1eA. These values should not be interpreted as specification limits; lot-specific certificates may vary with colorant and production batch.

    PropertyTest methodTypical value
    Melt volume-flow rate, 220 °C / 10 kgISO 1133-126 cm³/10 min
    DensityISO 1183-11.04 g/cm³
    Tensile modulus, 1 mm/minISO 527-22450 MPa
    Tensile yield stress, 50 mm/minISO 527-245 MPa
    Nominal strain at break, 50 mm/minISO 527-210 %
    Flexural modulusISO 1782400 MPa
    Charpy notched impact, 23 °CISO 179-1/1eA25 kJ/m²
    Charpy notched impact, –30 °CISO 179-1/1eA9 kJ/m²
    Vicat softening temperature, VST/B/50ISO 30696 °C
    Heat deflection temperature, 1.8 MPaISO 75-298 °C
    Mold shrinkage, flow directionISO 294-40.4–0.7 %
    Flammability, manufacturer-tested thicknessUL 94HB

    The Vicat and heat deflection values define short-term thermal resistance under the cited load and heating rate. They are not continuous service temperature ratings. Creep-loaded parts require a separate design assessment using the temperature-dependent modulus and long-term creep data for the specific geometry.

    What Drying and Melt-Temperature Limits Govern Defect-Free Processing?

    Before melt conversion, the resin must be dried in a desiccant hopper dryer with a dew point of –40 °C or lower. At 80 °C, a residence time of 2 h to 4 h is required when incoming moisture exceeds 0.05 wt%. Material stored in opened sacks at 23 °C and 50 % relative humidity can acquire surface moisture of 0.2–0.4 wt% within 24 h. Residual moisture above 0.05 wt% during plastication produces splay, silver streaks, and inconsistent surface gloss on flat interior and housing surfaces. The return-air dew point of the dryer should be monitored and held at –30 °C or lower to prevent re-absorption in the hopper. In production environments above 60 % relative humidity, drying should not be interrupted between the hopper and feed throat.

    The melt temperature window for injection molding is 230 °C to 260 °C, measured at the nozzle with an immersion pyrometer. Below 230 °C, the melt exhibits higher viscosity, increased injection pressure demand, and visible flow lines in sections below 1.2 mm. Above 270 °C, the polybutadiene phase undergoes thermal-oxidative degradation, causing yellowing, loss of notched impact strength, and formation of gaseous decomposition products. Residence time at maximum barrel temperature should be limited to 5 min; longer hold times require barrel purge and temperature reduction. A general-purpose reciprocating screw with an L/D ratio of 20:1 to 24:1 and a non-return valve with short shutoff stroke is suitable. Back pressure is normally maintained between 5 bar and 20 bar, with higher values reserved for difficult colorant dispersion or masterbatch homogeneity.

    Mold temperature should be maintained between 40 °C and 80 °C. The lower boundary reduces cycle time but increases frozen-in orientation and gloss differentials on textured surfaces. Increasing mold temperature toward 70 °C improves weld-line strength and replication of grained cavity textures. General ABS processing trials have shown that raising mold temperature from 40 °C to 70 °C can improve weld-line tensile strength by 10 % to 20 %, but published data for this specific grade are limited. Hopper air temperature should not exceed 85 °C; under uneven airflow, softened pellets can bridge and interrupt feed throat flow.

    When the Flow–Impact Trade-Off Changes Gate and Runner Sizing

    At the reported melt volume-flow rate, TERLURAN 968K fills thin-wall tools with lower pressure drop than impact-modified ABS grades of lower flow. The practical consequence is not that gates can be eliminated, but that the material tolerates longer flow lengths at a given wall thickness. In a rectangular edge gate, an apparent shear rate in the 10³–10⁴ s⁻¹ range is reached at injection rates typical of thin-wall molding; under these conditions the melt exhibits pronounced shear thinning. This allows a reduction in runner diameter of roughly 0.5–1.0 mm relative to a high-impact ABS with melt volume-flow rate near 10 cm³/10 min, provided the pressure drop remains inside the machine hydraulic limit and cavity pressure sensors confirm complete packing.

    Published spiral-flow data for TERLURAN 968K are limited. Flow-length verification should therefore be performed on the production tool rather than inferred from melt volume-flow rate alone. Gate depth below 0.6 mm for a 1.2 mm wall is not recommended because excessive shear heating can degrade the polybutadiene phase. As a practical guide, gate depth should be 50–70 % of the wall thickness. Hot-runner drops are permissible if the manifold is held at 230–250 °C and the nozzle tip remains above 230 °C. Multi-gated tools should position weld lines away from load-bearing ribs, bosses, or snap-fit retention features. The reduced viscosity of this grade is obtained by polymer architecture and molecular weight control rather than external plasticizer migration, so the flow effect is not expected to depend on a migratory additive that could later plate out on the mold surface.

    Hydraulic injection pressures commonly fall between 70 MPa and 140 MPa for thin-wall ABS tools. The lower melt viscosity can shift the pressure-limited molding envelope toward longer flow lengths and reduce required clamp force by an estimated 5–15 % relative to a lower-flow high-impact grade, but final clamp force should be verified by cavity pressure measurement at the end of fill. Screw recovery should be completed within the cooling time to avoid extended melt residence. If the screw cannot recover within the cycle, barrel temperature should be lowered within the 230–260 °C window rather than increasing back pressure excessively.

    Comparative Position of TERLURAN 968K within the ABS Portfolio

    The principal difference between TERLURAN 968K and general-purpose ABS grades in the Terluran line is melt viscosity. TERLURAN 968K yields lower injection pressure and faster filling in multi-cavity tools, while general-purpose ABS may offer slightly higher tensile modulus and lower cost for simple thick-wall parts. Against high-impact ABS grades, TERLURAN 968K trades a portion of low-temperature Charpy value for processability. A high-impact ABS grade with an MVR of 8–12 cm³/10 min may show Charpy notched values at –30 °C above 15 kJ/m², whereas TERLURAN 968K falls near 9 kJ/m². At 23 °C the difference narrows significantly. The grade is not the first choice for components exposed to impact below –20 °C, such as exterior automotive parts in cold climates.

    Property classTERLURAN 968KGeneral-purpose ABSHigh-impact ABSHeat-resistant ABS
    Melt volume-flow rate, 220 °C / 10 kg25–30 cm³/10 min15–25 cm³/10 min5–15 cm³/10 min5–20 cm³/10 min
    Charpy notched, 23 °C25–28 kJ/m²12–20 kJ/m²30–40 kJ/m²15–25 kJ/m²
    Charpy notched, –30 °C8–10 kJ/m²4–7 kJ/m²14–20 kJ/m²6–10 kJ/m²
    Vicat VST/B/5095–97 °C94–98 °C94–97 °C104–110 °C

    The table summarizes typical commercial segment ranges rather than exact values for any single competitor grade. Heat-resistant ABS grades containing α-methylstyrene or maleimide comonomer have a Vicat above 104 °C and are preferable when parts must survive paint ovens or continuous service above 90 °C. TERLURAN 968K should not be specified for continuous load-bearing service above 85 °C or for painted components requiring oven curing above 90 °C. For electroplating or adhesion-critical decorative treatments, the appropriate grade should be selected after internal stress evaluation because high-flow ABS can retain orientation near gates and ribs.

    Surface Appearance, Weld-Line Integrity, and Shrinkage Compensation

    Gloss and color stability depend on barrel residence time, mold temperature, and venting. At mold temperatures below 40 °C, chemically textured surfaces may exhibit gloss differentials across the flow length. Raising mold temperature to 60–70 °C improves replication but increases cycle time by approximately 10–15 % for a 2 mm wall. Mold shrinkage under ISO 294-4 in the flow direction is reported at 0.4–0.7 %, with transverse shrinkage typically 0.1–0.2 % higher. This anisotropy must be compensated in tool dimensions, particularly for flat rectangular housings that are prone to warpage if gate location creates unbalanced flow. A post-molding conditioning step of 24 h at 23 °C and 50 % relative humidity is advised before final dimensional audit.

    Weld-line regions in ABS depend on melt-front temperature at confluence. In a low-viscosity ABS such as TERLURAN 968K, the melt front can cool more quickly between two flow fronts in thin sections. Vent depths up to 0.03 mm are conventional for ABS; deeper vents can produce flash because of the reduced melt viscosity. Weld-line tensile strength reductions of 20–40 % relative to unwelded specimens are common for ABS, and Charpy notched impact at a weld line can be substantially lower than the nominal datasheet value. Published weld-line efficiency data for this specific grade are limited; a tool trial with an instrumented 1200 kN machine and cavity pressure sensors is advised before transferring a multi-gated tool to production.

    When regrind is reused, the ratio should be controlled and the regrind must be dried under the same conditions as virgin material. Repeated heat histories degrade the polybutadiene phase and progressively lower notched impact strength. A regrind level above 20 % should be validated by mechanical testing because the effect is nonlinear with repeated molding cycles. Before material changes, polystyrene or ABS purging compound should be used; residues of polyacetal or PVC can degrade at ABS processing temperatures and generate acidic species that reduce molecular weight. The same purge discipline applies when transferring from a higher-melting engineering resin, where retained crystalline residues can block valve gates or produce visible contamination in the next shot.

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