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INEOS Styrolution ABS TERLURAN HH-104

    • Product Name: INEOS Styrolution ABS TERLURAN HH-104
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 887638
    Polymer Type Acrylonitrile butadiene styrene (ABS)
    Density 1050 kg/m³
    Melt Volume Flow Rate Mvr 220 C 10 Kg 5.0 cm³/10 min
    Tensile Modulus 2100 MPa
    Tensile Stress At Yield 45 MPa
    Tensile Strain At Yield 2.5%
    Nominal Strain At Break 15%
    Charpy Notched Impact Strength At 23 C 12 kJ/m²
    Charpy Notched Impact Strength At 30 C 6 kJ/m²
    Vicat Softening Temperature B 50 104 °C
    Heat Deflection Temperature Hdt A 95 °C
    Heat Deflection Temperature Hdt B 100 °C
    Molding Shrinkage 0.4–0.7%
    Water Absorption 0.6%
    Ul 94 Flammability Rating HB

    As an accredited INEOS Styrolution ABS TERLURAN HH-104 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packed in 25 kg moisture-proof polyethylene bags, typically palletized at 1,000 kg per pallet for safe industrial storage and transport.
    Container Loading (20′ FCL) INEOS Styrolution ABS TERLURAN HH-104 loaded in a 20′ FCL container, palletized, dry, securely stowed, protected from moisture and heat.
    Shipping INEOS Styrolution ABS TERLURAN HH-104 is shipped as non-hazardous thermoplastic pellets in moisture-barrier bags, octabins, or bulk containers. It is not classified as dangerous goods for transport (no UN number, class, or packing group). Store dry, away from heat and sunlight; avoid humidity and contamination during handling.
    Storage Store INEOS Styrolution ABS TERLURAN HH-104 in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and ignition sources. Keep original containers sealed, palletized, and protected from physical damage and dust. Avoid contact with solvents and incompatible chemicals, and follow local regulations and good housekeeping practices.
    Shelf Life TERLURAN HH-104 ABS has a typical shelf life of 24 months when stored dry in original sealed packaging.
    Application of INEOS Styrolution ABS TERLURAN HH-104

    Where HVAC diffuser outlets cycle between 18 °C and 95 °C, instrument-panel air vent housings, vane assemblies, and bezels moulded from TERLURAN HH-104 are processed as 1.9–2.3 mm nominal wall parts, with gate land thickness held to 0.8–1.0 mm to avoid jetting at the vane pivot. The grade is dried in a closed-loop desiccant dryer at 80 °C for 2–4 h until residual moisture is ≤0.05 wt%; higher moisture produces butadiene-phase hydrolysis at plastication and silver streaks on the visible vane crown. Melt temperature is controlled at 240–260 °C, with hot-runner manifold zones maintained within 10 °C of the nozzle set point to avoid local thermal decomposition. The tool cavity is polished P20 or 1.2738 steel with water-side temperature 60–80 °C, and hold pressure is set at 50–70% of peak injection pressure with switchover at 95–98% volume fill by screw position. Regrind from sprues and rejected black vent bodies may be added at ≤15 wt%; grained high-visibility surfaces are limited to 0–5 wt% regrind because repeated heat history creates polybutadiene gel specks that alter microgloss. Dimensional stability is checked on a 3-axis fixture with gap and flushness tolerance of ±0.3 mm, and post-mould shrinkage is referenced to ISO 294-4:2018. VOC and fogging are evaluated on the finished vent assembly, not on pellets, using VDA 277 and DIN 75201-B, with odour threshold classified under VDA 270 after a 24 h conditioning at 23 °C and 50% RH.

    What Limits High-Gloss Upper B-Pillar Trim in Variothermal Injection Moulding?

    High-gloss black upper B-pillar trims are moulded from TERLURAN HH-104 only when the cavity steel is heated above the apparent glass transition of the SAN matrix during filling; if the tool remains at 60 °C, visible flow lines and microshrinkage appear under oblique light inspection. The variothermal cycle raises cavity surface temperature to 120–135 °C during injection and holding, then cools to 60 °C before ejection, increasing cooling time by 18–25% compared with an isothermal 60 °C tool. Melt temperature is kept at 245–255 °C, and injection speed is profiled to maintain a flow-front velocity below the threshold that entrains air at the gate land. No regrind is permitted on A-surface; sprues and runners are diverted to non-visible structural parts at ≤10 wt% regrind. Finished unpainted trim attached to the B-pillar bracket uses ultrasonic or heat-staked bosses with collapse depth below 0.5 mm to reduce internal stress. Unpainted exterior service is not recommended because polybutadiene phases undergo photo-oxidative crosslinking and gloss loss under side-window UV and car-wash chemicals; a co-extruded PMMA or ASA surface is required for exterior weatherability. The relevant long-term exposure test is SAE J2412 xenon arc, but published weatherability data specific to HH-104 in this exact unpainted configuration is limited.

    In recirculating-air plenums, defroster nozzles, and blower motor carriers, the load profile differs from automotive trim: low oscillating stress at 50–70 °C, occasional condensation during cooling mode, and projected flow lengths of 250–400 mm across 2.5 mm nominal walls. A four-cavity hot-runner tool with sequential valve gates is required to shift weld lines away from the blower scroll sealing face; fill time of 2.0–2.5 s is typical for a 2.5 mm wall at 230–250 °C melt temperature. Tool temperature is held at 50–70 °C, with regrind from sprues and short shots added at ≤20 wt% in black or non-grain visible HVAC parts. The finished plenum is joined to a rubber gasket and must retain clip engagement at 80 °C; dimensional heat-age checks use a 48 h exposure at 90 °C, with warpage allowance of ≤0.5% of nominal length. Constant-load creep is evaluated under ISO 899-2 only when design stress exceeds 5 MPa; below that stress, short-term tensile data from ISO 527-2:2012 is generally sufficient for section sizing. Continuous pooling of condensate below the evaporator core is not recommended, because absorbed water hydrates polar nitrile groups and repeated wet/dry cycling can initiate debonding at polybutadiene-matrix interfaces; for direct condensate-wetted pans, a PP or modified PPO/PS grade should be selected instead.

    When Control-Cabinet Internals Stabilize Above 65 °C in Continuous Operation

    Low-voltage control cabinets, DIN rail mounting plates, and relay housings fabricated from TERLURAN HH-104 are constrained by the UL 94 classification of unfilled ABS: the grade is selected for HB-class internal structural parts, not for V-0 or V-2 enclosures that require flame-retardant modifiers. Relay housing walls are 1.8–2.5 mm; screw bosses use an outside diameter of 2.0–2.5 × the nominal screw diameter and a pilot hole not greater than 0.7 × the thread major diameter to avoid boss splitting. Melt temperature is limited to 230–250 °C because prolonged residence above 260 °C shifts the colour of light RAL 7035 parts; tool temperature is 50–70 °C, back pressure 5–10 bar, and decompression 2–3 mm before screw recovery. Regrind for light-coloured enclosures is kept at ≤10 wt% to avoid yellowing from polybutadiene thermal history. Glow-wire flammability index according to IEC 60695-2-12 at 650 °C is part-specific; the grade should not be used where the final enclosure must satisfy IEC 62368-1 fire containment tests unless an FR ABS variant is substituted. Ultrasonically welded cable-entry bosses and heat-staked terminal blocks are qualified on a part-specific basis; published data for HH-104 at 35 kHz ultrasonic amplitude and 0.3–0.5 s weld time is limited, so weld strength must be confirmed by burst or pull-out testing on production welded assemblies.

    ComponentMelt temperatureTool temperatureRegrind limitCritical test
    Instrument-panel air vents240–260 °C60–80 °C≤15 wt% black; 0–5 wt% visibleVDA 277, DIN 75201-B
    High-gloss B-pillar trim245–255 °C120–135 °C variothermal; 60 °C ejection0 wt% A-surface; ≤10 wt% non-visibleSAE J2412, OEM gloss
    HVAC plenum230–250 °C50–70 °C≤20 wt%ISO 899-2, heat-age fixture
    Electrical enclosures230–250 °C50–70 °C≤10 wt% light colourIEC 60695-2-12, pull-out
    Appliance fascia235–255 °C60–80 °C≤25 wt% pigmentedIEC 60695-2-11, ISO 22088-3

    Exposed to intermittent steam, detergent films, and fingertip oils, espresso machine upper consoles, air fryer control surrounds, and high-ambient kitchen appliance fascia panels are textured to VDI 24–27 and require draft angles of 0.8–1.0° per side for clean ejection without mould-release sprays. The melt temperature is set at 235–255 °C; tool temperature is 60–80 °C for textured cavities, and ejection is allowed only after the surface temperature drops below the heat-deflection temperature minus 20 K to preserve texture replication. White or pigmented fascia panels use 2–3 wt% masterbatch; regrind is limited to ≤25 wt% because titanium dioxide and opacifier platelets concentrate at weld lines and create optical density shifts. Finished parts are evaluated for glow-wire ignition under IEC 60695-2-11 and for heat resistance under IEC 60335-1 Clause 30; direct food-contact claims are not made for HH-104, and any food-contact component must be reassessed against FDA 21 CFR 177.1020 or EU 10/2011. Environmental stress cracking resistance to descaling solutions is screened with 1.5% citric acid at 65 °C under 0.5% strain using ISO 22088-3; if stress crazing occurs before 24 h, the part is annealed at 70 °C for 2 h per 2.5 mm wall thickness or redesigned to lower moulded-in stress. Heat-shield inserts around boiler ports and snap-fit engagement features must not exceed 0.6% outer fibre strain during assembly, as checked by strain gauge on three production parts per cavity.

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    Certification & Compliance
    More Introduction

    INEOS Styrolution ABS TERLURAN HH-104 is a high-heat acrylonitrile-butadiene-styrene copolymer supplied as cylindrical pellets for injection moulding and, to a lesser extent, profile extrusion. Under the designation system of ISO 2580-1:2004, the grade is classified as an ABS moulding material with elevated Vicat softening temperature; the suffix HH-104 corresponds to a Vicat B/50 value of approximately 104 °C when tested according to ISO 306:2022. Manufacturer literature lists automotive interior structural parts, heating/ventilation/air-conditioning ducts, loudspeaker grilles, and appliance housings as primary conversion routes. Published datasheet values should be treated as centroid values for natural colour; lot-specific certificates of analysis govern actual production validation because pigmentation, regrind level, and trapped moisture influence the final test results.

    How Does the High-Heat Architecture Affect Short-Term Thermal Performance?

    Vicat softening temperature is determined under ISO 306:2022 using method B/50, in which a 50 N load and 50 °C/h heating rate are applied to a standard test specimen. For TERLURAN HH-104, the method B/50 value is approximately 104 °C; this is typically 8–10 K higher than general-purpose TERLURAN grades and makes HH-104 suitable for short-term paint-baking or hot-air exposure in automotive interior locations. Heat deflection temperature under a 1.8 MPa flexural load is reported near 96–98 °C using ISO 75-2:2013 method A. The deflection temperature is lower than the Vicat value because the applied stress accelerates relaxation of the rigid SAN-rich phase. Continuous-use temperature is not equivalent to Vicat temperature; for this grade, continuous-load service above 85–90 °C should be supported by creep-modulus data from ISO 899-2:2003 rather than short-term thermal indices alone.

    Typical physical and mechanical values for INEOS Styrolution TERLURAN HH-104, based on manufacturer datasheet centroid values for natural colour.
    Property Test method Typical value or range
    Density ISO 1183-1:2019 1.05 g/cm³
    Melt volume rate at 220 °C/10 kg ISO 1133-1:2022 8 cm³/10 min
    Vicat softening temperature B/50 ISO 306:2022 104 °C
    Heat deflection temperature A (1.8 MPa) ISO 75-2:2013 96–98 °C
    Tensile modulus ISO 527-2:2012 2300–2500 MPa
    Yield stress ISO 527-2:2012 48–52 MPa
    Flexural modulus ISO 178:2019 2200–2500 MPa
    Charpy notched impact strength, 23 °C ISO 179-1:2010 18–22 kJ/m²
    Charpy notched impact strength, -30 °C ISO 179-1:2010 7–10 kJ/m²
    Mould shrinkage, flow direction ISO 294-4:2018 0.4–0.7 %

    Melt Rheology and Drying Requirements for Injection Moulding Lines

    High-heat ABS exhibits higher melt viscosity than general-purpose ABS at equivalent barrel temperatures. Apparent viscosity measured by capillary rheometry at 250 °C and shear rates between 100 s⁻¹ and 1000 s⁻¹ generally falls in the 150–400 Pa·s range for injection moulding grades; processors should reference the manufacturer's viscosity curve for lot-specific values. The increased viscosity raises screw recovery torque and can generate adiabatic overheating in undersized screws. On production-scale injection moulding machines with clamping force between 1000 kN and 6500 kN, a general-purpose screw with a length-to-diameter ratio of 20:1 and compression ratio of 2.0–2.5:1 is adequate for standard parts. For thin-wall parts below 2.5 mm, screws with higher mixing intensity and L/D near 22:1 are preferred to homogenise melt temperature without raising barrel set-points.

    The material is hygroscopic. Pellets exposed to ambient conditions above 60% relative humidity require dehumidified-air drying at 80 °C for 2–4 h to a residual moisture target below 0.1% before melt processing. Dryers controlled to a dew point of -30 °C or lower produce consistently low splay and better gloss retention. Regrind addition up to 20 wt% is generally tolerated if the regrind is dry and free of dust; higher levels shift melt viscosity and reduce notched impact due to cumulative thermal history. The SAN phase is susceptible to thermo-oxidative yellowing when melt temperature exceeds 280 °C or residence time exceeds 10 min; the butadiene phase can also gel. Purging after shutdown should use a low-viscosity acrylic or HDPE purge compound, not PVC, to avoid acid generation in the barrel.

    Typical injection moulding set-points for TERLURAN HH-104 high-heat ABS; values should be confirmed against the lot-specific certificate of analysis.
    Parameter Recommended range or condition
    Pre-drying temperature 80 °C for 2–4 h in dehumidified air
    Maximum residual moisture 0.1 %
    Melt temperature, rear to nozzle 240–270 °C
    Mould temperature 60–80 °C
    Back pressure, hydraulic 5–10 bar
    Screw circumferential speed 0.2–0.5 m/s for medium shot sizes
    Holding pressure 60–80 % of peak injection pressure

    Injection velocities of 100–200 mm/s are commonly used for thin walls to prevent premature freeze-off; however, excessively high shear rates above 10 000 s⁻¹ can induce surface haze at gates. Gate location should place weld lines away from direct high-velocity vent air because weld-line tensile strength measured on double-gate plaques under ISO 527-2:2012 is typically 60–80 % of the un-notched value in ABS. Injection moulding trials have shown that mould temperatures below 50 °C increase internal stress, gloss variation, and susceptibility to environmental stress cracking.

    If Dimensional Tolerance Below 90 °C or Immersion in Weak Acid Media Is Required

    TERLURAN HH-104 is not an intrinsically dimensionally stable material under load; short-term thermal resistance does not imply low creep. The coefficient of linear thermal expansion for ABS is typically 80–110 × 10⁻⁶ K⁻¹ according to ISO 11359-2:2021. Parts with tight dimensional windows should use mould shrinkage compensation according to ISO 294-4:2018; measured flow-direction shrinkage is commonly 0.4–0.7 %, with transverse shrinkage up to 0.6–0.8 %. In applications where hot air from a defroster impinges on an instrument panel carrier, the part must not be rigidly constrained because differential expansion against metal brackets can initiate stress cracking. Finite-element simulations should use creep-modulus values generated under ISO 899-2:2003 at the service temperature rather than short-term tensile modulus.

    Chemical resistance to dilute acids and alkalis is acceptable at ambient temperature. Immersion testing under ISO 2812-2:2007 commonly shows moderate mass gain without visible attack in 5 % acetic acid or 5 % sodium hydroxide at 23 °C for short exposure; however, stress-cracking solvents such as toluene, ethyl acetate, and methyl ethyl ketone must be avoided. Published data for this specific grade under continuous immersion at elevated temperatures is limited, and conversion trials should include chemical exposure with the actual production fluid.

    Chemical Compatibility Boundaries and Ultraviolet Ageing Response

    Absence of butadiene-phase ultraviolet stabilisation is a boundary condition. The material is not classified as UV-stable and should not be specified for unpainted exterior components unless a UV absorber and hindered amine stabiliser system is compounded at the converter or a protective cap layer is used. Xenon-arc exposure under ISO 4892-2:2013 has shown that standard ABS yellowing and gloss loss begin before mechanical embrittlement; the exact failure threshold depends on pigment loading and part thickness. For exterior unpainted parts, ASA or PC/ASA should be selected instead. Environmental stress cracking can be evaluated using ISO 22088-2:2006 with a constant strain method; ABS is particularly sensitive to esters, aromatic hydrocarbons, and chlorinated solvents. Compatibility with coolants, windshield washer fluids, and cleaning agents must be tested because blends containing ethylene glycol mono-butyl ether can induce stress cracking in amorphous thermoplastics. Avoid contact with glycol ethers in water-based paints and with plasticised PVC seating or adhesive films that can migrate plasticiser into the ABS surface.

    Automotive heating, ventilation, and air-conditioning components represent the largest conversion route for TERLURAN HH-104. In production-scale injection moulding cells using 1200 kN to 3000 kN clamp force and valve-gated hot runners, the grade has been used for defroster grilles, upper airbag trim panels, and pillar mouldings where the peak soak temperature after a summer heat cycle can exceed 95 °C but total sustained load is low. For these parts, gate location is selected so that weld lines are not placed in direct line of high-velocity vent air; weld-line strength measured by tensile testing on double-gate plaques under ISO 527-2:2012 is typically 60–80 % of the un-notched value in ABS grades. Part geometry determines whether that reduction is acceptable.

    Benchmarking Against General-Purpose and High-Impact Terluran Grades

    Compared with general-purpose TERLURAN GP-22, HH-104 shifts the Vicat B/50 upward by approximately 8 K while melt viscosity increases and low-temperature impact declines. The exact property spread depends on colourant: carbon black, titanium dioxide, and organic pigments alter nucleation and embrittlement. High-impact TERLURAN grades with higher butadiene rubber content can offer notched Charpy values above 25 kJ/m² at 23 °C, whereas the high-heat architecture of HH-104 typically falls in the 18–22 kJ/m² range; selection between high-heat and high-impact ABS is therefore controlled by whether hot bearing strength or ductile impact resistance is the first failure mode. Against polycarbonate/ABS blends, HH-104 has lower heat deflection temperature under load, lower notched impact, and lower raw-material cost; against ASA, HH-104 lacks exterior weatherability. These differences are documented in manufacturer datasheets and should be confirmed with current certificates of analysis.

    Shrinkage anisotropy under ISO 294-4:2018 is an often-overlooked discriminator. The high-heat grade's higher melt temperature typically produces slightly greater flow-direction shrinkage than standard ABS; mould designs should not simply reuse tools cut for general-purpose ABS without verifying gate and runner dimensions. Production moulds for HH-104 benefit from larger cold slug wells and polished runner surfaces to counteract the narrower processing window. Regulatory compliance statements regarding REACH Regulation (EC) No 1907/2006 and Directive 2011/65/EU are supplied through the material safety data sheet and should be verified for each shipment because additive packages can vary by region.

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