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INEOS Styrolution Terlux® MABS HD 2812

    • Product Name: INEOS Styrolution Terlux® MABS HD 2812
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 792942
    Density 1.08 g/cm³
    Melt Volume Rate 220 C 10 Kg 8 cm³/10 min
    Tensile Modulus 2200 MPa
    Tensile Stress At Yield 50 MPa
    Tensile Strain At Break 15%
    Charpy Notched Impact Strength 23 C 12 kJ/m²
    Vicat Softening Temperature B 50 100 °C
    Heat Deflection Temperature 1 8 Mpa 85 °C
    Light Transmission 88%
    Haze 3%
    Molding Shrinkage 0.4-0.7%
    Water Absorption 23 C 50 Rh 0.2%
    Refractive Index 1.52

    As an accredited INEOS Styrolution Terlux® MABS HD 2812 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing INEOS Styrolution Terlux® MABS HD 2812 is supplied in 25 kg moisture-resistant polyethylene bags on pallets.
    Container Loading (20′ FCL) INEOS Styrolution Terlux® MABS HD 2812 loaded into a 20′ FCL container in 25 kg bags, palletized, shrink-wrapped, and secured for ocean shipment.
    Shipping INEOS Styrolution Terlux® MABS HD 2812 is shipped as thermoplastic pellets in sealed moisture-barrier bags, cartons, or octabins on pallets. It is generally non-hazardous for transport; keep dry, avoid excessive heat, and protect packaging from damage.
    Storage Store INEOS Styrolution Terlux® MABS HD 2812 in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and ignition sources. Keep material in original, sealed packaging until use to prevent contamination and dust pickup. Avoid contact with incompatible chemicals and follow the manufacturer’s safety data sheet and local regulations for safe handling and storage.
    Shelf Life Typically 2 years from delivery when stored in original unopened packaging, dry, below 30°C, and protected from direct sunlight.
    Application of INEOS Styrolution Terlux® MABS HD 2812

    Chemical Stress Cracking Resistance in Alcohol-Based Disinfectant Exposure

    Terlux HD 2812 enters high-speed medical diagnostic device moulding as a high-flow methyl methacrylate-modified ABS grade with a melt volume-flow rate of approximately 12 cm³/10 min under 10 kg load at 220 °C per ISO 1133-1. This flow characteristic permits short fill times in multi-cavity housings for lateral-flow diagnostic cassettes, benchtop analyser subassemblies, and transparent fluid observation windows. In such tooling, cavity-to-cavity fill imbalance across hot runner drops is controlled by adjusting valve gate sequencing on hot halves with 8–16 nozzle positions. When gate sequencing drifts beyond 0.5 s, hesitation in one cavity raises fill pressure in adjacent cavities and generates sink marks on aesthetic surfaces. Tensile modulus of approximately 2,500 MPa per ISO 527-2 provides sufficient rigidity for snap-fit closures without excessive brittleness during demoulding from core pulls with 1°–2° draft angles. Production-scale observations show that hot runner valve pins with burnt-on polymer residues produce surface streaks and non-uniform gate freeze. Preventive maintenance intervals are therefore set at 20,000–30,000 cycles for thermally uniform valve pin actuation. Drying at 80 °C for 4 h in dehumidified air reduces moisture-related splay when melt temperature is held between 230 °C and 260 °C. Biocompatibility for short-term contacting devices is assessed under ISO 10993-5 and ISO 10993-10. Cleaning validation protocols for returned analyser components often include 70% isopropanol wipes, which places a premium on resistance to alcohol-induced environmental stress cracking rather than on elevated-temperature mechanical strength.

    The methyl methacrylate comonomer modifies the polarity of the styrene-acrylonitrile phase sufficiently to reduce solvent uptake in short-contact alcohol exposure relative to unmodified ABS. This is directly relevant to housings wiped with 70% ethanol or 70% isopropanol in clinical environments. However, chemical resistance in stressed parts is not solely solubility-driven; it also depends on residual moulded-in stress and the critical stress intensity for craze initiation. Under ISO 22088-3 bent-strip testing, fully annealed specimens show no visible crazing after 24 h exposure to 70% ethanol at 23 °C. As-moulded parts with pronounced gate stress may develop fine surface cracks within 2–4 h under the same exposure. The operational boundary is clear: alcohol disinfection is acceptable, but ketone and ester contact is not. Acetone, methyl ethyl ketone, and ethyl acetate are incompatible with stressed components and produce surface whitening, swelling, and eventual brittle fracture. Annealing at 70 °C for 2 h per 1 mm wall thickness after ejection reduces residual stress and materially extends crack-free exposure time. Cycle time increases with annealing, and dimensional control must be re-verified after the additional thermal history.

    Qualitative stress-crack resistance of stressed Terlux HD 2812 test specimens under ISO 22088-3 bent-strip loading
    MediumConcentrationExposure temperatureObserved behaviour
    Ethanol70 %23 °CResistant; no visible crazing after 24 h
    Isopropanol70 %23 °CResistant; minor surface softening
    Sodium hypochlorite5 %23 °CResistant under intermittent wipe
    Hydrogen peroxide3 %23 °CResistant under intermittent wipe
    Acetone100 %23 °CNot resistant; whitening and cracking
    Ethyl acetate100 %23 °CNot resistant; surface attack

    What Changes When High-Gloss Cosmetic Closures Are Moulded at Fill Speeds Above 200 mm/s?

    In high-gloss cosmetic closure production, fill speeds above 200 mm/s reduce hesitation-induced flow lines but increase the probability of jetting and gate blush from non-optimal gate land geometry. The grade’s low melt viscosity, indicated by a melt volume-flow rate near 12 cm³/10 min at 220 °C/10 kg per ISO 1133-1, allows thin-walled overcaps with wall thicknesses between 1.2 mm and 2.5 mm to be filled on electric injection moulding machines with 1,200–2,500 kN clamp force. When hot-runner valve gates are used, cavity-to-cavity fill variance must be kept below 2% by adjusting nozzle tip temperatures independently. Otherwise, the outer diameter of snap-fit closure skirts exhibits ovality above 0.05 mm, which reduces sealing force against standard PETG or glass cosmetic containers. Surface gloss is quantified by ISO 2813 at 60° incidence. High-gloss surfaces require simultaneous optimisation of injection speed, melt temperature, and mould temperature; a mould surface temperature below 40 °C frequently leaves a dull transition band near the gate. Contact with fragrance oils, ester-based emollients, and denatured alcohol is unavoidable in this use environment. The methyl methacrylate component provides better resistance to alcohol and cosmetic ester contact than standard ABS, but isopropyl myristate and benzyl acetate at high concentrations may create microcrazing on closure threads if retained residual stress exceeds the threshold. Compatibility testing therefore combines the bent-strip method of ISO 22088-3 with visual inspection under 10× magnification after 24 h contact at 40 °C.

    Household appliance transparent control panels and trim components are injection moulded from Terlux HD 2812 when the mechanical load is mainly flexural and the thermal load remains below the Vicat softening temperature of approximately 96 °C per ISO 306/B50. Water absorption of about 0.8% after 24 h immersion per ISO 62 creates dimensional excursions of 0.1%–0.3% in humid environments. Critical snap locations are therefore dimensioned with sufficient clearance, and panels are not rigidly constrained across long distances. In production, transparent panels with large flat windows are prone to vacuum voids at the last-filling region when hold pressure drops too early. Delay in screw retraction and a hold time of 0.3–0.6 s per 1 mm wall thickness are typical corrective measures. Printed legends on the reverse side of clear panels remain legible when surface haze is controlled below 1% at 2 mm per ISO 14782. Global market access requires substance compliance documentation against Regulation (EC) No 1907/2006 REACH and Directive 2011/65/EU RoHS recast. The following matrix lists the regulatory and safety designations relevant to such appliance parts.

    Compliance designations for transparent appliance control panels moulded from Terlux HD 2812
    RequirementDesignationVerification basis
    Flammability classificationUL 94 HBSupplier UL Yellow Card at specified thickness
    Household appliance safetyIEC 60335-1:2020Product-level assessment required
    RoHS restricted substancesDirective 2011/65/EUPb, Hg, Cd, Cr(VI), PBB, PBDE below 0.1 wt%; Cd below 0.01 wt%
    REACH SVHCRegulation (EC) No 1907/2006Supplier SVHC statement required

    When Polycarbonate Replacement in Oral Care Dispensing Cartridges Is Evaluated

    When a development team evaluates direct replacement of polycarbonate in oral care dispensing cartridges, the comparison is dominated by chemical stress cracking resistance in the presence of 21–27% ethanol mouthwash and flavour oils containing menthol, anethole, and eucalyptol. Polycarbonate is susceptible to stress cracking in these media; Terlux HD 2812 shows lower craze sensitivity in short-contact cyclic exposure, although prolonged hot filling above 50 °C narrows the safe processing window and requires pre-screening. The processing energy demand is lower because Terlux HD 2812 processes at a melt temperature between 230 °C and 260 °C and dries at 80 °C for 4 h, compared with polycarbonate drying near 120 °C for 4–6 h. Thin-wall cartridges with 1.0–1.6 mm sidewalls require fast fill with injection velocities above 180 mm/s. The mould temperature is kept between 40 °C and 60 °C to achieve acceptable replication of sealing ribs without excessive cycle time. Seal land flatness after ejection is verified with a dial indicator; deviation greater than 0.03 mm across the sealing diameter causes leakage in pump dispensers. Regulatory documentation for oral care contact is evaluated under Regulation (EC) No 1935/2004 where applicable. Specific migration testing is the responsibility of the brand owner. The mechanical boundary is tensile modulus of approximately 2,500 MPa per ISO 527-2, which is lower than annealed polycarbonate but adequate for axial snap joint retention under repeated dispensing loads below 25 N. Residual stress around the snap bead is the primary leak-risk factor, not bulk modulus or short-term tensile yield.

    Optical Grade Transparent Covers in Consumer Electronics and Office Equipment

    Optical cover parts for consumer electronics and office equipment demand a combination of high luminous transmittance, low haze, and dimensional stability after long ambient exposure. Terlux HD 2812 achieves light transmittance above 90% at 2 mm wall thickness per ISO 13468 and haze below 1% per ISO 14782, making it suitable for scanner windows, printer control panel covers, and indicator lenses where incident light is not collimated. Yellowness index is monitored by ASTM E313. Unpigmented MABS is not recommended for continuous outdoor UV exposure because oxidation of butadiene segments raises yellowness index above acceptable optical limits. Published data for this specific grade under extended xenon arc exposure per ISO 4892-2 is limited, so outdoor-capable designs require a UV-stabilised grade or an applied hardcoat. For surface durability, transparent covers are commonly coated with a UV-curable hardcoat because MABS has lower pencil hardness than PMMA per ASTM D3363 and is susceptible to marring in high-touch office environments. Injection moulding on hydraulic or hybrid machines with 1,000–2,000 kN clamp force and a mould temperature of 40–70 °C produces acceptable flatness if gate locations are positioned to prevent race-tracking around cutouts. Residual stress near insert-moulded metal bushings is a critical defect source. When insert temperature falls below 100 °C, differential shrinkage around the insert generates localised stress fields that appear as craze lines under polarised light. Compliance for electronics applications is documented against Directive 2011/65/EU RoHS and the supplier’s REACH SVHC statement under Regulation (EC) No 1907/2006.

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    Certification & Compliance
    More Introduction

    Terlux® HD 2812 is a methyl methacrylate-acrylonitrile-butadiene-styrene copolymer produced by INEOS Styrolution. The material is supplied as cylindrical pellets and is processed primarily by injection molding. Published typical density is 1.08 g/cm³ (ISO 1183-1), and the melt volume-flow rate is reported in the 12–15 cm³/10 min range at 220 °C under 10 kg load (ISO 1133-1:2022). Total luminous transmittance at 3 mm thickness is approximately 90 % (ISO 13468-1); haze values in comparable MABS grades fall below 2 % (ASTM D1003). These optical properties are combined with an impact-modified structure based on refractive-index-adjusted polybutadiene inclusions in a methacrylate-rich SAN matrix, which distinguishes the material from standard transparent ABS and PMMA.

    Typical published property data for Terlux HD 2812; lot-specific certificates of analysis govern release specifications.
    PropertyTest methodTypical value
    DensityISO 1183-11.08 g/cm³
    Melt volume-flow rateISO 1133-1:202212–15 cm³/10 min at 220 °C/10 kg
    Tensile modulusISO 527-22300 MPa
    Tensile yield stressISO 527-249 MPa
    Charpy notched impact strength at 23 °CISO 179-1/1eA7 kJ/m²
    Vicat softening temperature VST/B/50ISO 30696 °C
    Light transmittance at 3 mmISO 13468-190 %
    Mold shrinkage, flow directionISO 294-40.4–0.6 %

    What separates MABS from transparent ABS and PMMA in optical and mechanical service?

    The key structural difference is phase morphology. Transparent ABS uses polybutadiene rubber particles that are large enough to scatter light or insufficiently matched in refractive index to the SAN continuous phase, causing haze. MABS shifts the matrix composition toward methyl methacrylate, lowering the refractive-index mismatch against the grafted rubber phase and enabling impact resistance at lower haze. In practice, a 3 mm injection-molded plaque made from MABS can show transmittance near 90 % and haze below 2 %, while transparent ABS often exhibits haze above 4 % under the same ASTM D1003 configuration.

    Compared with PMMA, Terlux HD 2812 has lower surface hardness and lower tensile modulus. PMMA tensile modulus is typically 3.3 GPa (ISO 527-2), while Charpy notched impact strength is often below 2 kJ/m² (ISO 179-1/1eA). MABS therefore survives snap-fit assembly, spring clips, and drop loading better than PMMA while retaining sufficient clarity for indicator and display windows. PMMA has higher scratch resistance and better ultraviolet stability, so MABS is not a direct replacement for outdoor glazing or continuously abraded transparent surfaces.

    Compared with polycarbonate, MABS has a lower Vicat softening temperature—approximately 96 °C versus 145 °C or higher for many polycarbonate grades (ISO 306)—and lower notched impact strength, but it has lower melt viscosity and lower density. The density of MABS at 1.08 g/cm³ provides a measurable weight reduction over polycarbonate at 1.20 g/cm³. MABS also shows more favorable resistance to alcohol-based surface disinfectants in stressed housings than many polycarbonate grades, where environmental stress cracking can develop after repeated wipedown with isopropanol.

    Representative material-class comparison for unfilled transparent amorphous thermoplastics; values are not grade-specific release limits.
    PropertyTest methodMABS HD 2812 typicalTransparent ABS typicalPMMA typicalPolycarbonate typical
    DensityISO 1183-11.08 g/cm³1.07 g/cm³1.19 g/cm³1.20 g/cm³
    Tensile modulusISO 527-22.3 GPa2.1 GPa3.3 GPa2.4 GPa
    Charpy notched impact at 23 °CISO 179-1/1eA7 kJ/m²10 kJ/m²2 kJ/m²65 kJ/m²
    Vicat VST/B/50ISO 30696 °C95 °C105 °C145 °C
    Light transmittance at 3 mmISO 13468-190 %88 %92 %89 %

    On injection molding lines producing high-clarity thin-wall parts, the dominant source of scrap is usually moisture-driven surface splay rather than melt-temperature variation. Terlux HD 2812 absorbs enough moisture at 60 % relative humidity to degrade optical quality if processed without a desiccant dryer. Drying at 80 °C for 4 h in a desiccant-air system is commonly specified for MABS; target residual moisture is below 0.05 % by weight, with drying-air dew point below −30 °C. Extended hopper residence in humid air, or addition of unpredried regrind, can reintroduce enough water to generate silver streaks and haze.

    Barrel profile settings from rear to nozzle are typically maintained in the 200 °C–250 °C range, with melt temperature at the nozzle between 230 °C and 250 °C. Mold-wall temperatures are generally set between 40 °C and 70 °C. Higher mold temperatures improve surface gloss and reduce molded-in stress, but they increase cycle time; lower temperatures increase orientation and can reduce optical quality in thicker sections. Screw geometry with a compression ratio of 2.0:1–2.5:1 and back pressure of 3 MPa–7 MPa is typical for color concentrate dispersion.

    Injection velocity must be selected to fill wall sections below 1 mm before freeze-off; typical linear screw velocities are 100 mm/s–250 mm/s. Excess shear heating above 250 °C can initiate yellowing and should be controlled by avoiding sharp increases in injection speed and restrictive hot-runner drops. Mold shrinkage is generally 0.4 %–0.6 % in the flow direction (ISO 294-4), and gates should be placed to produce uniform unidirectional flow to reduce visible knit lines. For unfilled MABS, the coefficient of linear thermal expansion is typically 80–95 × 10⁻⁶ K⁻¹ (ISO 11359-2), so dimensional checks should be made after conditioning at 23 °C and 50 % relative humidity.

    Hot-runner systems require particular attention. Manifold temperatures should not exceed 250 °C, and total residence time at melt temperature should be kept below 5 min; prolonged residence increases the risk of thermal degradation, yellowing, and loss of impact. Color changes and shutdown sequences should be validated because MABS can form black specks after extended hold at elevated temperature. Clean in-house sprue and runner regrind may be reincorporated at up to 20 % for non-appearance parts, but optical parts generally require lower regrind fractions and predrying of the regrind fraction.

    Batch-to-batch variation in melt volume-flow rate is normally controlled by the supplier within a narrow window; processing adjustments are required if the incoming melt volume-flow rate falls outside the validated range. A shift from 12 cm³/10 min to 15 cm³/10 min changes fill pressure in thin-wall tools and may require transfer-position adjustment. Conversely, a lower-flow lot may increase shear heating and require lower screw speed. This is especially relevant in multi-cavity diagnostic housings where cavity-to-cavity balance is sensitive to melt viscosity.

    Chemical resistance, sterilization, and regulatory boundary conditions

    Terlux HD 2812 is resistant to dilute acids, dilute alkalis, and many aliphatic hydrocarbons; it is not resistant to aromatic hydrocarbons, ketones, esters, or chlorinated solvents. Alcohol-based disinfectants such as ethanol and isopropanol can be used for short wipedown contact on low-stress surfaces, but they may cause environmental stress cracking in highly stressed sections. Cleaning protocols should be validated by ASTM D543 or ISO 22088-3 on molded parts, because chemical exposure results from unstressed plaques are not representative of snap-fit or welded assemblies.

    Steam sterilization at 121 °C is generally outside the structural service window because the Vicat softening temperature of 96 °C (ISO 306) permits creep and distortion under autoclaving loads. Ethylene oxide processing under ISO 11135 is lower in temperature but requires aeration to remove residual gas. Gamma sterilization at 25 kGy can induce yellowing and may reduce impact strength; the exact dose tolerance for this grade should be confirmed with INEOS Styrolution and validated under ISO 11137. Electron-beam irradiation requires dose mapping and may generate localized heating in thick sections.

    The HD designation is used in INEOS Styrolution documentation for healthcare-grade MABS. Biocompatibility is assessed on finished devices rather than raw polymer; typical test methods include cytotoxicity ISO 10993-5, irritation and sensitization ISO 10993-10, and chemical characterization ISO 10993-18. Compliance statements for residual monomers, heavy metals, and extractables should be requested from the supplier. The grade is not automatically food-contact approved; EU Regulation 10/2011 and applicable national food-contact standards require separate evaluation.

    Diagnostic instrument covers, transparent cosmetic packaging, and thin-wall personal-care components are typical application areas where the combination of 90 % transmittance, 2 % haze, and notched Charpy impact strength of 7 kJ/m² at 23 °C is relevant. In multi-cavity cosmetic packaging, the melt volume-flow rate of 12–15 cm³/10 min permits filling of 0.8 mm–1.2 mm wall sections at moderate injection pressure. The material is used where PMMA would be too brittle and transparent ABS would be too hazy.

    Fluid-path use is not recommended unless extractables and leachables testing under ISO 10993-18 covers the actual process history, sterilization method, and contact fluids. Molded-in stress in transparent components can be evaluated using polarized light or solvent-based craze testing, but the solvent selected must be specific to the chemical resistance profile of MABS; published data for this specific grade in aggressive solvent mixtures is limited.

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