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INEOS Styrolution Terlux® MABS 2812 Q434

    • Product Name: INEOS Styrolution Terlux® MABS 2812 Q434
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 567576
    Density 1.08 g/cm³
    Melt Volume Rate 12 cm³/10 min (220 °C/10 kg)
    Molding Shrinkage 0.4–0.7 %
    Tensile Modulus 1900 MPa
    Tensile Strength 50 MPa
    Elongation At Break 15 %
    Charpy Notched Impact Strength 12 kJ/m² (23 °C)
    Vicat Softening Temperature 95 °C
    Heat Deflection Temperature B 75 °C
    Light Transmission 90 %
    Haze 1 %
    Refractive Index 1.56
    Water Absorption 0.2 %

    As an accredited INEOS Styrolution Terlux® MABS 2812 Q434 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in 25 kg polyethylene bags, palletized and stretch-wrapped for safe industrial storage and transport.
    Container Loading (20′ FCL) 20′ FCL loading for INEOS Styrolution Terlux® MABS 2812 Q434: palletized 25 kg bags, shrink-wrapped, dry container, ambient, approx. 20–22 MT payload.
    Shipping Shipping description: INEOS Styrolution Terlux® MABS 2812 Q434 is supplied as non-hazardous thermoplastic polymer pellets in moisture-protective bags, boxes, or octabins. It is not classified as dangerous goods for transport. Keep dry, avoid excessive heat, and follow the SDS and local transport regulations.
    Storage Store INEOS Styrolution Terlux® MABS 2812 Q434 in a cool, dry, well-ventilated area, protected from direct sunlight, heat, flames, and oxidizing agents. Keep containers tightly closed in original packaging to prevent moisture, dust, and contamination. Avoid static buildup and mechanical damage. Maintain good housekeeping and comply with local storage regulations.
    Shelf Life Typical shelf life is 12 months if stored dry, below 30°C, in unopened original packaging and protected from moisture and UV.
    Application of INEOS Styrolution Terlux® MABS 2812 Q434

    When Terlux® MABS 2812 Q434 is specified for transparent medical device housings and diagnostic cartridge windows, the first production variable is not melt temperature but residual moisture. The resin is loaded into a desiccant dryer with a return-air dew point of -30 °C or lower and dried at 80 °C for 4 h to reach a target moisture content below 0.05 wt%. Failure to hold this condition produces splay and silver streaking on lens areas, a defect that often becomes visible only after ethylene oxide sterilisation. The melt is conditioned in a three-zone screw with an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.0:1 to 2.5:1; nozzle melt temperature is held between 230 °C and 250 °C when measured by needle pyrometer. Accumulator settings are adjusted so that shot size remains between 40% and 70% of barrel capacity, preventing prolonged residence time that yellows the methyl methacrylate segment. Mould surface temperature is maintained at 50 °C to 70 °C to reduce flow lines and improve weld-line strength. Injection velocity for 1.0 mm to 1.5 mm diagnostic windows is set in the 60 mm/s to 100 mm/s range; higher velocities induce gas traps at the end of fill in cassette channels. Hold pressure is established by gate-seal study, typically between 400 bar and 700 bar hydraulic, with switchover at 96–98% of shot volume. Finished cartridges must satisfy risk-management documentation under ISO 14971:2019 and manufacturing traceability under ISO 13485:2016. Cytotoxicity is evaluated on the final component using ISO 10993-5:2009 with extract preparation according to surface-area-to-volume ratios defined in ISO 10993-12:2021; Terlux MABS does not itself confer biocompatibility unless the moulded article passes these tests after full production handling, lubricant selection, and sterilisation validation. The grade is used for transparent cases, sample observation windows, and non-fluid-path housings in point-of-care diagnostic devices and insulin pump display covers.

    Compliance verification matrix for medical and laboratory components
    Application sectorTestStandardCondition
    Medical device housingsCytotoxicityISO 10993-5:2009Extraction per ISO 10993-12:2021
    Medical device housingsSensitisationISO 10993-10:2021Final moulded part
    Drug-delivery windowsExtractablesISO 10993-18:2020Worst-case solvent
    Laboratory consumablesBioburdenISO 11737-1:2018Pre-sterilisation
    Cosmetic packagingChemical resistanceISO 175:201040 °C/14 days
    Household appliance panelsBall-pressureIEC 60335-1:2020Clause 30

    What Changes When High-Flow MABS Replaces Polycarbonate in Transparent Aerosol Overcaps and Collars?

    Replacing bisphenol-A polycarbonate with Terlux 2812 Q434 in transparent overcaps for aerosol sprays and pump dispensers shifts the processing window toward lower melt and mould temperatures but imposes stricter limits on chemical contact after moulding. The MABS grade is moulded with melt temperatures of 220 °C to 245 °C and core temperatures of 55 °C to 65 °C, producing full transparency at wall thicknesses from 1.0 mm to 2.0 mm without post-mould annealing. Unlike polycarbonate, the flow length of this MABS allows filling of slim collar undercuts at lower injection pressure, reducing flash in multi-cavity tools with worn vents. However, the assembled package is exposed to ethanol, isopropyl alcohol, and hydrocarbon propellants at levels that can initiate environmental stress cracking if the component is over-constrained. A mandatory screening protocol uses ASTM D543-21 immersion testing with the specific fragrance or propellant blend at 50 °C for 72 h on strip specimens cut at 0.8 mm thickness; visual inspection at 10× magnification under polarised light detects microcrazing before release. Shrinkage of the MABS overcap measured after 48 h post-mould is in the 0.5–0.8% range parallel to flow and 0.4–0.7% perpendicular, requiring cap-to-collar radial clearance of at least 0.15 mm over the nominal diameter to prevent stress build-up. Gate placement uses a side edge gate of 0.8 mm thickness and 2.5 mm length to minimise gate blush on the outer dome; hot-drop valve gates are used only when colour change frequency demands reduced runner loss. The terminal components include transparent overcaps, actuator sleeves, and decorative collars for fragrance and personal-care aerosol packaging.

    Indicative injection-moulding windows for Terlux 2812 Q434 by wall thickness
    Part wall thicknessMelt temperatureMould cavity surfaceInjection velocityHold pressureBack pressure
    0.8–1.2 mm240–255 °C60–75 °C80–130 mm/s500–800 bar5–10 bar
    1.5–2.5 mm230–245 °C50–65 °C45–90 mm/s400–700 bar5–12 bar
    3.0–4.0 mm225–240 °C55–70 °C25–50 mm/s350–600 bar5–12 bar

    Lipid-Rich Cosmetic Compacts and Cream Jar Bases: Flow Length, Weld Line Integrity and Surface Replication

    High-gloss transparent cream jar bases and compact platforms moulded from Terlux 2812 Q434 require optical-grade tool polishing and controlled venting to prevent burn marks on the sealing lip. Melt temperature for thick-section cosmetic parts is held at 230 °C to 255 °C with mould cavity surface temperature raised to 65 °C to 75 °C where the wall exceeds 3.0 mm. This higher cavity temperature delays the formation of a frozen skin and improves replication of polished SPI/SPE A-1 surfaces without visible flow lines. For a cream jar base with a 2.5 mm side wall and a 25 mm central gate boss, injection velocity is profiled with an initial stage of 30 mm/s to 50 mm/s through the gate and a second-stage velocity of 80 mm/s to 120 mm/s for the rim, preventing gas entrapment in the sealing area. Hold pressure is set to 500–800 bar hydraulic with a hold time determined by free deflection of the part after ejection; ejection too early produces sink at the base rim. Cosmetic formulators expose the polymer to esters, fatty acids, and nonyl acetate; immersion testing by ISO 175:2010 using the actual cream formulation at 40 °C for 14 days is necessary because the methyl methacrylate-rich phase of MABS provides better alcohol resistance than standard ABS but remains susceptible to ketones, aromatic hydrocarbons, and acetate esters. The dimensional stability of moulded jars is evaluated using conditioning under ISO 291:2008 at 23 °C/50% RH for 24 h, followed by measurement of closure dimensions with a coordinate measuring machine. Weld line strength in double-gated compact bases can be as low as 55–70% of the un-welded tensile strength tested by ISO 527-2:2012; for this reason, dual injection points are positioned adjacent to the rear hinge rather than across the latch region. Terminal applications include transparent jar bases, compact trays, and magnifier lids.

    Steam-generating household appliances with transparent control facades impose thermal endurance requirements that rule out standard ABS but remain within the performance envelope of Terlux 2812 Q434. High-gloss transparent control panels for steam irons and garment steamers are moulded at a cavity surface temperature no lower than 55 °C when the part length exceeds 180 mm; lower temperatures produce a visible skin-layer difference at the weld line. The tool is built with a sequential valve-gate system so that flow fronts merge at a single controlled position, reducing the loss of impact strength that occurs when two free-flow fronts meet at an uncontrolled knit line. The resin is dried at 80 °C for 4 h and supplied to the screw with a nominal residence time of less than 6 min at melt temperature 240 °C to 250 °C. For a panel of 1.2 mm nominal wall thickness, clamp force is calculated on the basis of 3.0–4.0 kN/cm² of projected area and the injection pressure is limited to 90–110 MPa machine setting. The part is cooled for 12–18 s before ejection; ejection speed is reduced to 5–10 mm/s for the first 5 mm of travel to avoid stress whitening at the ribs. After moulding, the panel is annealed at 70 °C for 2 h in a forced-air oven to relax orientation and stabilise dimensions prior to laser etching or hot-pad printing. The dominant compliance requirement for this application is IEC 60335-1:2020 for household electrical appliance safety, specifically clause 30 ball-pressure testing, because the panel is in proximity to heated surfaces. Terminal products are transparent covers for steam generator bases and control display windows in floor-care appliances.

    When the Mould Temperature Is Below 55 °C in a Four-Cavity Hot-Runner Medical Ware Tool

    Some multi-cavity tools for transparent specimen containers and sterile ware are run with mould surface temperatures as low as 35 °C to shorten cycle time. This condition reduces the hot-runner gate droplet size but increases the risk of a visible cold slug at the sub-gate and lowers weld-line toughness. The process response for Terlux 2812 Q434 is to raise nozzle temperature to 245 °C and reduce the injection velocity to 30–50 mm/s through hot drops of 0.6 mm to 0.8 mm diameter, while keeping the runner manifold at 230 °C. In four-cavity fluidic manifolds, cavity-to-cavity fill imbalance must be corrected through individual valve-gate timing, not by raising hold pressure alone; otherwise the last-filled cavity is overpacked and displays birefringence when viewed under crossed polarisers. Birefringence in MABS within the 0–3 fringe order is acceptable for simple covers, but fluidic optical windows require 0–1 fringe order, verified using a strain viewer. Drying is performed to the 0.05 wt% moisture limit, and regrind from sprues and runners is limited to 15 wt% for products that must maintain a total luminous transmittance higher than 89% per ASTM D1003. For medical ware intended for gamma sterilisation at 25 kGy, the compound is evaluated for yellowness index increase under ASTM E313 after one and two sterilisation cycles; published data for this specific configuration is limited, and serial validation under final sterilisation load configuration is required. Terminal products include urine specimen containers, transparent trays, and non-fluid-path laboratory consumables.

    Gate Blush Suppression in Thin-Walled Drug-Delivery Dose Counter Windows

    The dose counter window in dry powder inhalers and pressurised metered dose inhaler actuators uses a 0.8 mm to 1.0 mm transparent window that must survive assembly press-fit without cracking. Terlux 2812 Q434 is dried to 0.04 wt% or lower and injected through a fan or tab gate of 0.5 mm thickness to restrict the shear rate below the critical value for white blush. Melt temperature is held at 235 °C to 250 °C; the screw speed is limited to 60–100 rpm and back pressure to 5–10 bar to prevent excessive shear heating in the methyl methacrylate phase. The window area is moulded with a single gate at the long edge, not the centre, so the flow front advances uniformly across the optical zone and prevents the formation of a central weld within the viewing field. For a 12 mm × 6 mm × 0.9 mm window, packing pressure is maintained for 1.0–1.5 s after gate freeze; longer hold times do not improve dimensional accuracy but increase residual stress. After ejection, windows are annealed at 65 °C for 1 h to lower hoop stress before press-fit into the actuator body. The finished drug-delivery component is subject to extractables testing under ISO 10993-18:2020 for leachables that might migrate from the polymer after contact with propellant or powder. Chemical compatibility with ethanol-based cleaning solutions is assessed by ISO 10993-13:2010 as part of the overall risk file. Terminal products are transparent dose counter windows, actuator windows, and inspection lenses for inhalation devices.

    In transparent fluid handling fittings and laboratory microtiter plate viewing strips, Terlux 2812 Q434 is employed only when the moulded part does not contact strong acids, aromatic hydrocarbons, or ketones at elevated temperature. The material is processed with a melt temperature of 220 °C to 235 °C and mould surface temperature of 40 °C to 50 °C for thin sections below 0.7 mm, using injection speeds of 150–220 mm/s to avoid premature freeze-off. For microfluidic manifold parts with multiple ribs and through-holes, the tool requires vacuum venting of 0.01–0.02 mm depth around the perimeter and along the runner branch points; inadequate venting creates burn marks and degradation odour at the end of fill. The parts are evaluated for dimension stability after 48 h at 23 °C/50% RH, with the expectation of 0.4–0.7% total mould shrinkage. Assembly of barbed fittings into flexible tubing after gamma or autoclave exposure is not recommended unless the barb design reduces hoop stress below the critical stress for the moulded MABS; if assembly is required, a minimum insertion angle of 15° and a barb undercut of 0.3 mm or less are used. The final products are transparent adaptor caps and viewing windows for laboratory automation equipment, where the primary regulatory reference is the laboratory equipment manufacturer’s own validation under ISO 13485:2016 if the assembly is sold as a medical accessory.

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    Certification & Compliance
    More Introduction
    Product identity and material class

    INEOS Styrolution Terlux® 2812 Q434 is a methyl methacrylate-acrylonitrile-butadiene-styrene moulding compound, classified under ISO 1043-1 as MABS. The methyl methacrylate comonomer shifts the refractive index of the matrix phase into the range of 1.52–1.54, bringing it close to the grafted polybutadiene rubber phase and reducing internal scattering at optical interfaces. The Q434 suffix identifies a demoulding and lubricant package tailored to high-output injection moulding rather than a separate base resin chemistry. Because suffix-level additive composition is not fully disclosed in consolidated literature, published values for the Terlux 2812 family should be treated as representative for the Q434 modification unless a batch certificate provides differentiated data. The product is normally processed as cylindrical pellets; it is not hygroscopic in the same manner as polyamide or PET, but surface moisture and pellet fines nevertheless control final optical quality.

    Is Terlux 2812 Q434 a drop-in replacement for clear ABS or PMMA?

    Not without revalidation of tool fill pressure, shrinkage allowance, and weld-line strength. Opaque ABS uses a styrene-acrylonitrile matrix with a deliberate refractive-index mismatch against the polybutadiene domains; MABS replaces part of the styrene with methyl methacrylate to match the rubber-phase index and create transparency. The resulting melt has a melt volume rate of 12 cm³/10 min at 220 °C under 10 kg load for the 2812 family, measured according to ISO 1133-1. This flow is higher than low-flow MABS grades used for thick sections and lower than high-flow MABS grades with MVR values near 28 cm³/10 min. Compared with PMMA, MABS offers higher notched impact strength but lower surface hardness and lower resistance to atmospheric UV degradation. Compared with polycarbonate, the compound processes at a lower melt temperature and shows easier thin-wall mould filling, but its Vicat softening temperature under ISO 306 VST/B/50 is typically near 83 °C, approximately 60 K below transparent polycarbonate. This thermal boundary excludes the material from continuous service above 80 °C in load-bearing transparent components.

    Pre-drying and moisture-control boundary

    Residual moisture rather than equilibrium water absorption controls haze and splay in moulded Terlux 2812 Q434. Equilibrium water pickup according to ISO 62 at 23 °C and 50 % RH is typically reported near 0.25 wt%, but regrind, fines, and condensation on cold pellets can raise localized moisture above this value. The recommended drying condition is 80 °C for 4 h in a dehumidifying hopper dryer with supply air at a dew point of −30 °C or lower. The target residual moisture before melting is ≤0.05 wt%. If this target is not reached, methacrylate ester groups can decompose at melt temperature and generate haze-inducing volatile degradation by-products. On production lines equipped with desiccant-wheel dryers, batch-to-batch haze variation is often traced to condensate accumulation in the return-air circuit or to a hopper baffle that channels pellets past the drying air. Dryer sizing should account for true residence-time distribution in the hopper cone; a machine with a 60 s cycle and a hopper capacity of 1.5 times the shot weight may expose only the lower pellet layer to the full 4 h drying period when the drying temperature is set below 80 °C.

    When the melt temperature reaches 250 °C at the nozzle, residence time becomes the critical variable

    Published injection-moulding processing guides recommend a melt temperature band of 230 °C to 250 °C, measured with a needle pyrometer at the nozzle, and a mould surface temperature of 50 °C to 70 °C. Shot size should be held between 30 % and 70 % of barrel capacity to limit melt residence time. A fill time of 0.3 s to 0.8 s is typically used for wall thicknesses of 1.2 mm to 1.5 mm in multi-cavity cold-runner tools. Back pressure is maintained at 5 bar to 10 bar hydraulic pressure, because higher back pressure increases shear heating and may accelerate yellowing without improving clarity. If production is interrupted for more than 5 min, the first 3 to 5 shots should be purged at 20 °C above the established melt temperature before optically clear parts are accepted. The upper processing limit is not a single number: at 250 °C, a 10 min residence time can produce measurable yellowing in unstabilized natural resin, whereas at 240 °C the same residence time may remain acceptable.

    Shrinkage values for injection moulding are generally reported between 0.4 % and 0.7 % in flow direction and 0.5 % to 0.8 % transverse; the exact value depends on wall thickness, mould temperature, and gate freeze time. For dimensionally stable parts, holding pressure should be applied until the gate seals. A gate-seal study plotted as part mass against holding time identifies the plateau where the gate freezes and mass no longer increases. The coefficient of linear thermal expansion is typically in the range of 80 × 10⁻⁶ K⁻¹ to 90 × 10⁻⁶ K⁻¹ according to ISO 11359-2; this is higher than PMMA and should be compensated in tool dimensions when close tolerances are required. After moulding, post-shrinkage can continue for 24 h to 48 h at ambient temperature, so dimensional inspection should be delayed accordingly.

    Application and compliance assessment

    Transparent diagnostic and drug-delivery accessory components are a common application area for this grade because the material combines lower brittle-fracture tendency than PMMA with lower processing cost than polycarbonate. Typical parts include transparent pipette tip racks, lancet housings, inhaler mouthpiece covers, cosmetic closure systems, and clear appliance control panels. Each use requires separate validation of final-article migration or biological response; the raw resin alone does not confer food-contact or medical-grade status. For medical device housings, biological evaluation is performed under ISO 10993-1 on the finished device, while cytotoxicity screening may follow ISO 10993-5. For food-contact applications, migration testing according to the applicable national or regional regulation is required because the Q434 demoulding package and any colorant masterbatch can alter overall migration values. The additive package reduces ejection force in polished cavity inserts; external mold release spray is generally unnecessary and may introduce interfacial haze.

    Light transmission and haze stability at 3 mm wall thickness

    For unpigmented Terlux 2812 mouldings, total luminous transmittance is typically reported at 90 % through a 3 mm plaque under ISO 13468-2 with illuminant D65 and a 2° observer. Haze is generally below 1 % when measured according to ASTM D1003. These values are not fixed material constants; they shift with cavity surface finish, melt temperature, moisture content, and the concentration of low-molecular-weight lubricant domains. Polished inserts with an SPI/SPE A-1 or A-2 finish are specified when maximum transparency is required. Textured surfaces reduce measured transmittance and increase haze, but they can hide gate blush and flow lines in complex geometries. The Q434 additive package may require requalification of light transmission after masterbatch dilution because some lubricants can form scattering domains below 500 nm. For tinted or UV-stabilized formulations, the haze target cannot be maintained at natural-resin levels and should be re-specified on the final part geometry.

    Representative physical and mechanical property values published for the Terlux 2812 family; Q434 suffix-specific values should be confirmed from the producer batch certificate.
    Property Typical value Test method
    Density 1.08 g/cm³ ISO 1183-1
    Melt volume rate 12 cm³/10 min at 220 °C/10 kg ISO 1133-1
    Water absorption equilibrium 0.25 wt% at 23 °C/50 % RH ISO 62
    Tensile modulus 2400 MPa ISO 527-1/-2
    Yield stress 50 MPa ISO 527-1/-2
    Yield strain 3.8 % ISO 527-1/-2
    Charpy notched impact, 23 °C 8 kJ/m² ISO 179-1/1eA
    Charpy notched impact, −30 °C 3 kJ/m² ISO 179-1/1eA
    Vicat softening temperature VST/B/50 83 °C ISO 306
    Light transmission, 3 mm 90 % ISO 13468-2
    Haze, 3 mm <1 % ASTM D1003

    Although the resin is transparent, gas trapping still produces burn marks

    Transparency does not eliminate the need for venting in multi-cavity tools. At the recommended melt temperature of 240 °C, residual moisture or degradation volatiles can accumulate at the flow front and produce silver streaks or burn marks if cavity air cannot escape. Vent depths for MABS are typically held between 0.02 mm and 0.03 mm on the parting line, with wider land channels leading to vacuum pumps when the part has a projected area above 200 cm². Gate geometry should place the gate at the thickest section and avoid direct impingement on polished lens surfaces; a fan gate of 0.8 mm to 1.2 mm thickness is used for flat optical panels. Ejector pins should be positioned away from high-gloss visible surfaces or recessed and polished to avoid witness marks. If the part contains a living hinge, the hinge notch radius should be at least 0.25 mm to prevent notch initiation; flexural endurance testing should follow ISO 178 on the actual moulded hinge geometry rather than on ISO test bars.

    Weld lines are a primary failure mode in transparent MABS components. The Charpy notched impact value of 8 kJ/m² is measured on a homogeneous ISO bar and does not apply to weld-line regions. When melt fronts join, the rubber particles remain within their respective flow fronts, and the interlocking matrix layer can be thin enough to reduce local impact resistance significantly. Groove-like flow leaders or increased melt temperature within the specified band can improve weld strength, but complete elimination is rarely possible in multi-gate tools. In medical or safety-relevant parts, minimum weld-line impact strength should be established by instrumented puncture testing at the weld location rather than inferred from standard single-gate specimens.

    Compliance and testing matrix for Terlux 2812 Q434 candidate applications
    Application context Relevant standard or regulation Evaluation requirement
    Medical device housing or accessory ISO 10993-1 Biological evaluation of final device; raw resin data are supporting only
    Cytotoxicity screening ISO 10993-5 Testing on finished extract; extraction conditions depend on use duration
    Food-contact article EU Regulation 10/2011; FDA 21 CFR Overall migration and specific migration limits tested on final article
    RoHS / hazardous substances IEC 63000 Technical documentation supporting restricted-substance assessment
    Mechanical quality control ISO 527-1/-2; ISO 179-1/1eA Injection-moulded specimens conditioned at 23 °C and 50 % RH per ISO 291
    Operational boundaries and chemical incompatibilities

    Material incompatibilities are dominated by polar solvents and certain amine-containing cleaning agents. Ketones such as methyl ethyl ketone can attack the methacrylate phase and cause stress cracking in moulded parts under residual strain. Cleaning of hot-runner systems should avoid aggressive solvent soaks that can swell the resin or deposit carbonized residue in the next run. For hot-runner temperature control, the manifold is held between 230 °C and 250 °C, and the nozzle tips are operated at the lower end of this range to minimize stringing. Colour changes from transparent natural to tinted formulations are best performed with a purging compound having a viscosity similar to or slightly lower than the MABS melt; no more than 10 % regrind is recommended for transparent optical parts because repeated heat histories increase haze. These limits define the process envelope within which the product retains its published optical and mechanical values.

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