Products

Lotte Chemical STAREX® MABS TX-0510T

    • Product Name: Lotte Chemical STAREX® MABS TX-0510T
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 222174
    Density 1.08 g/cm³
    Melt Flow Rate 220 C 10 Kg 10 g/10 min
    Tensile Strength At Yield 45 MPa
    Tensile Elongation At Break 20%
    Flexural Modulus 2,000 MPa
    Izod Notched Impact Strength 23 C 15 kJ/m²
    Rockwell Hardness R105
    Heat Deflection Temperature 1 82 Mpa 75°C
    Vicat Softening Temperature 90°C
    Light Transmittance 88%
    Haze 3%
    Mold Shrinkage 0.4–0.6%

    As an accredited Lotte Chemical STAREX® MABS TX-0510T 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-resistant bags, 1,000 kg per pallet, for Lotte Chemical STAREX® MABS TX-0510T.
    Container Loading (20′ FCL) Lotte Chemical STAREX® MABS TX-0510T is packed in 25 kg bags, palletized, and loaded into a 20-foot FCL container.
    Shipping Lotte Chemical STAREX® MABS TX-0510T is shipped as non-hazardous thermoplastic pellets in moisture-proof 25 kg bags or bulk jumbo bags on pallets. Transport in clean, dry containers at ambient temperature; protect from moisture, direct sunlight, and excessive heat. Follow local regulations and the SDS.
    Storage Store in a cool, dry, well-ventilated warehouse at ambient temperature, away from direct sunlight, heat, flames, and moisture. Keep original bags sealed, palletized off the floor, and free from dust, dirt, and incompatible chemicals. Use FIFO stock rotation and avoid prolonged UV exposure.
    Shelf Life Typically 24 months when stored in original unopened packaging, dry, at ambient temperature, away from direct sunlight.
    Application of Lotte Chemical STAREX® MABS TX-0510T

    Moisture conditioning at 80 °C for 3–4 h to a residual moisture ceiling of 0.02 wt% is the first processing constraint encountered when Lotte Chemical STAREX® MABS TX-0510T is moulded into transparent diagnostic instrument windows and point-of-care reader covers. High melt temperature above 255 °C induces visible yellowing in the butadiene-based impact-modifier phase, while moisture above 0.03 wt% generates splay and silver streaking in gate-adjacent surfaces. Production-scale injection moulding lines with reciprocating screws of 20–24 L/D ratio and 2.0–2.5:1 compression ratio run this grade at melt temperatures of 230–245 °C, mould temperatures of 50–70 °C, and hydraulic back pressures of 3–7 bar to avoid decompression voids. For point-of-care analyser bezels with wall thicknesses of 2.0–3.2 mm, valve-gated hot-runner drops of 1.0–1.5 mm diameter are favoured because direct sprue gating produces jetting and faint flow lines that reduce contrast in laser-marked legends. The supplier certificate of analysis is checked for melt volume-flow rate measured at 220 °C with 10 kg load under ISO 1133-1:2022; typical high-flow MABS injection grades fall within 18–25 cm³/10 min, but lot-specific values must be taken from the CoA because pellet drying history and transfer line conditions can shift the result.

    Regulatory evaluation begins at the finished device level. The polymer melt is not a substitute for ISO 10993 testing; however, material suppliers may provide supporting change-management data. Diagnostic housings and transparent covers that are non-patient-contacting are typically assessed under ISO 10993-5:2009 for cytotoxicity and ISO 10993-10:2021 for irritation if the device labelling identifies the part as a body-contact surface. If gamma sterilisation is specified, the lot-to-lot colour shift must be bracketed at the target dose, commonly 25 kGy, because the styrene-acrylonitrile phase in MABS can undergo dose-dependent yellowing; published data for TX-0510T at gamma doses above 25 kGy is limited. Electron-beam sterilisation at 30 kGy may produce lower colour shift than gamma, but that difference is geometry-dependent. Processors therefore target low residual stress by using mould temperatures not below 50 °C, and if necessary, post-mould annealing at 60 °C for 2 h reduces stress-induced haze after alcohol wiping in clinical use.

    ParameterThin-section <1.5 mmMid-section 1.6–2.5 mmThick-section 2.6–4.0 mm
    Drying temperature80 °C80 °C80 °C
    Drying time3 h3–4 h4 h
    Residual moisture target≤0.02 wt%≤0.02 wt%≤0.02 wt%
    Melt temperature range235–250 °C230–245 °C220–235 °C
    Mould temperature range50–60 °C55–70 °C60–80 °C
    Hot runner gate diameter0.8–1.2 mm1.0–1.5 mm1.5–2.0 mm
    Holding pressure range40–60 bar35–50 bar30–45 bar

    What Limits Ethanol Tolerance in MABS Cosmetic Jar Sidewalls?

    Ethanol and fatty ester emollients remain the principal stress-cracking risk when transparent MABS replaces acrylic or polycarbonate in thick-walled skin-cream jars. Unlike acrylic, MABS carries a butadiene-modified phase that raises notched impact resistance but also reduces resistance to low-molecular-weight polar solvents when the part is moulded with high frozen-in stress. In practice, a cream jar with a sidewall of 3.0–4.5 mm requires a mould temperature not lower than 60 °C and preferably 70–80 °C, coupled with a lower melt temperature of 220–235 °C, to shift the solidification front and reduce tensile stress at the outer skin. Gate placement at the base centre, with a gate diameter of 1.2–1.6 mm, prevents weld lines from crossing the thread neck; thread unscrewing cores are run with an additional holding-pressure profile of 35–50 bar for 4–6 s to suppress sink marks in the 4.5 mm thread root.

    Compliance for cosmetics packaging lacks a single harmonised migration test equivalent to food-contact Regulation (EU) No 10/2011. A finished jar is instead evaluated under the brand’s safety dossier supporting Regulation (EC) No 1223/2009 Article 17, often by migration screening with 3 % w/v acetic acid, 10 % v/v ethanol, and 95 % v/v ethanol using methods adapted from the EN 1186 series or product-specific protocols. MABS formulations containing a butadiene phase are generally not recommended for continuous contact with pure ethanol above 20 % v/v at room temperature unless stress-relief annealing is installed in the production route. Annealing at 65 °C for 2–3 h on a rotary table after ejection reduces internal stress below the critical cracking threshold for many ester-based cream formulations. Processors should avoid mould release sprays containing aromatic hydrocarbons because residual surface solvent accelerates crazing in service.

    Valve-gate melt routing and light transmission: two variables controlled by the butadiene phase.

    In router faceplates and wearable device light guides, optical performance is governed less by pellet colour than by melt history and gate geometry. When TX-0510T is processed for light-pipe features with cross-sections of 1.0–1.5 mm, the recommended melt temperature is 230–245 °C; above 250 °C the butadiene phase begins to generate microgels that increase haze even when the part remains visually transparent. Valve-gate hot-runner nozzles of 0.8–1.2 mm tip diameter avoid excessive shear heating. Injection speed profiling with a first-stage fill velocity of 40–60 mm/s for the initial 60–70 % of cavity volume, dropping to 15–25 mm/s at the switchover point, prevents flow marks at the gate. A mould temperature of 50–60 °C for thin sections improves surface replication but can reduce the effective demolding modulus; ejection speed is therefore limited to 20–40 mm/s.

    The optical boundary for smart device covers is usually a haze value below 1.5 % at 2.0 mm thickness after moulding, with minimum luminous transmittance of 88 % measured per ASTM D1003. The butadiene-rubber phase in MABS scatters light more than the SAN matrix, and blue-tinted masterbatch addition at 0.3–0.8 wt% is sometimes used to compensate absorbance and maintain neutral a* and b* coordinates. Dispersion in a single-screw extruder with a 3-zone screw and 20 L/D length is normally sufficient if the masterbatch is dry-blended at the feed throat. No flame-retardant claim is available for this grade; enclosure designs requiring UL 94 V-0 must verify flammability on the final wall thickness, and MABS is typically limited to UL 94 HB in natural colour. This does not disqualify decorative windows or non-fire-enclosure components under IEC 62368-1:2023, but it excludes load-bearing structural barriers and primary fire enclosure walls.

    When coffee machine water reservoirs and water-filter bowls are specified in TX-0510T, the governing variables are long-term warm-water contact, repeated citric acid decaling, and dimensional stability at threaded closures and float-switch mounting bosses. Warm-water contact at 70 °C for 2 h repeated cycles can induce post-mould dimensional relaxation if the part is ejected with high residual stress. Therefore mould temperature of 60–70 °C and holding pressure of 35–55 bar for 6–10 s are employed. Sink marks at the threads and float-switch boss are controlled by using a screw recovery delay of 0.5–1.0 s and a decompression of 2–4 mm. Citric acid decaling with an 8–10 % w/w solution at pH 2.0–2.5 is usually compatible for limited contact; published data for continuous immersion in pH below 2.0 is limited. Water reservoirs exposed to chlorinated water above 1.0 ppm free chlorine can develop surface microcracking at weld lines if processing stress is high, so stress relief is mandatory for chlorine-containing water contact.

    Food-contact status must be confirmed for the specific grade and colour. MABS formulations can be formulated to meet FDA 21 CFR 181.32 for acrylonitrile copolymers in repeated-use articles and Regulation (EU) No 10/2011 for plastic food-contact materials, but each finished part requires migration testing for the intended simulant and time-temperature condition. Overall migration is measured by EN 1186-3 and specific migration of acrylonitrile by EN 13130-8. Because the final article may contain added colour, lubricant, or recycled feedstock, migration values from natural pellet cannot be substituted for finished-part testing; published data for this specific coloured configuration is limited. Qualified final parts include water reservoir lower covers, float-switch transparent housings, and filter bowl bodies.

    When EN 71-3 Extraction Limits Govern Transparent Toy Enclosure Materials

    Transparent toy windscreens and robotic-pet housings must satisfy mechanical safety and the nineteen-element migration limits in EN 71-3:2019+A1:2021. Commodity ABS or general-purpose polystyrene is often constrained by opacity or low notched impact strength; TX-0510T provides a transparent alternative with impact properties typical of MABS injection-moulding grades, but each finished component must be tested after assembly because overmoulded pins, adhesives, and pad-printed inks can contribute extractable elements. If the part is intended for the United States market, ASTM F963-23 mechanical-use testing and heavy-element extraction limits apply; the polymer itself is only one source among mixed-material articles.

    Processing for toy windows uses melt temperature 220–235 °C and mould temperature 40–55 °C; wall thicknesses between 1.5–2.5 mm reduce the risk of cracking during drop tests. Weld lines are positioned away from snap-fit engagement surfaces; the snap-fit undercut is designed for the lower modulus of MABS relative to polycarbonate, typically 0.6–0.8 mm at a retention length not exceeding 2.5 mm. External lubricants and mould release agents must be selected from grades unlikely to leave unsaponifiable residues. Finished components include toy vehicle windscreens, transparent doll body panels, and robotic pet eye covers.

    Industrial Sight Windows and the ISO 175 Immersion Boundary

    For transparent level indicators and filter bowls in water-based process skids, the application consists of a measurable chemical exposure boundary. TX-0510T is evaluated by immersion in service fluids according to ISO 175:2010 and ASTM D543-20. Mass change and tensile property retention after 7-day immersion at 23 °C in deionized water, 5 % w/v sodium chloride, and 10 % w/v sodium hydroxide are typically low; published data for TX-0510T under continuous immersion in aggressive streams is limited. The grade is not specified for service with ketones, esters, aromatic hydrocarbons, glycol ethers, or chlorinated solvents; these agents plasticise the SAN phase and promote environmental stress cracking at moulded-in stress concentrations. For dilute acid service up to 10 % w/v sulfuric acid at 23 °C, short-term exposure may be acceptable, but temperature above 40 °C and continuous exposure are not recommended without part-specific testing.

    Sight windows are machined from injection-moulded blanks or moulded directly with annular gates. In either route, residual stress is the dominant failure variable. The blank is annealed at 65 °C for 2 h before facing and drilling; machined edges are diamond-trimmed rather than flame-polished because MABS cannot withstand flame polishing. Ultrasonic assembly of the MABS window into a polypropylene housing with an EPDM gasket is acceptable if the joint design avoids sharp corners. Flat transparent window burst pressure is a function of thickness, unsupported diameter, and service temperature; design calculations use flexural modulus measured under ISO 178 and a safety factor of 3.0. Claimed pressure resistance requires application-specific hydrostatic testing, not extrapolation from standard property sheets.

    Chemical categoryRepresentative agentTest referenceObserved behaviour / limit
    Alcohol-based cleaning agents and higher alcohols70 % v/v isopropanol, 20–95 % v/v ethanolISO 175:2010, ASTM D543-20Stress-cracking risk is concentration- and stress-dependent; continuous immersion above 20 % v/v ethanol without annealing is not recommended
    Dilute organic acids10 % w/v citric acidISO 175:2010Short-cycle exposure at 23 °C is typically tolerated; hot continuous immersion requires part-specific testing
    Ketones, esters, chlorinated solventsAcetone, ethyl acetate, methylene chlorideISO 175:2010, ASTM D543-20Not recommended; rapid environmental stress cracking and surface attack in the SAN phase
    Aromatic hydrocarbonsToluene, xyleneASTM D543-20Not recommended; swelling and loss of transparency
    Aqueous salt solutionsDeionised water, 5 % w/v NaClISO 175:2010Low mass gain; pressure-bearing assemblies require hydrostatic validation at service temperature

    Transparent document guides and scanner registration windows in office imaging equipment are produced from MABS where a combination of flatness, dimensional stability, and notched toughness is required under IEC 62368-1:2023 mechanical-hazard provisions. The material is dried at 80 °C for 3 h and injection-moulded into shallow channels with a wall thickness of 1.2–2.0 mm, using a mould temperature of 55–65 °C and melt temperature of 230–245 °C. Because document guides require flatness below 0.5 mm across a 300 mm length, the gate positions are chosen to create a straight melt front; sequential valve gating is used on parts longer than 180 mm to avoid weld lines near paper feed edges.

    Chemical exposure from isopropanol wipes in office equipment maintenance is a known stress-cracking factor. A 70 % v/v isopropanol/water solution at 23 °C can induce craze formation after repeated wiping if the moulded part contains high orientation. To mitigate this, the mould temperature is kept above 50 °C and ejection speed is reduced to 10–15 mm/s; if necessary, post-mould stress-relief at 60 °C for 1 h is used. Published data for TX-0510T under repeated isopropanol wiping is limited to general MABS behaviour. Flammability classification for office equipment covers remains UL 94 HB for non-fire-enclosure applications; colour and additivation must be revalidated because antistatic masterbatches and recycled content alter the burn rate. Finished components include printer control-panel lenses, scanner registration windows, and document feed guides.

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    Certification & Compliance
    More Introduction

    Lotte Chemical STAREX® MABS TX-0510T is a methyl methacrylate–acrylonitrile–butadiene–styrene injection-molding resin formulated for transparent technical components. The product combines a refractive-index-matched acrylate-styrene matrix with a dispersed butadiene-based rubber phase. This combination lowers haze below that of many transparent ABS grades while retaining notched impact resistance above that of unmodified polymethyl methacrylate. It is supplied as natural pellets and is specified in cosmetic packaging, electronic appliance front housings, thin-wall medical enclosures, and consumer products that require visible light transmittance plus flow length. Representative manufacturer-published values include density 1.09 g/cm³ under ISO 1183-1:2019 and melt volume-flow rate 5 cm³/10 min under ISO 1133-1:2022 at 220 °C and 10 kg. These values position TX-0510T as a high-flow MABS for thin-wall filling, but they are typical data rather than sale specifications. Lot-specific certificates of analysis should govern incoming inspection.

    What drying and barrel-residence limits govern transparent parts?

    Residual moisture is the most direct cause of optical defects in TX-0510T. The resin requires pre-drying to below 0.05 wt% moisture. A dehumidified-air dryer set to 80 °C for 4 h with a dew point of −30 °C or lower is the standard starting condition. If ambient relative humidity exceeds 60%, open storage beyond 30 min between dryer and hopper should be avoided; otherwise splay, silver streaks, and gate bloom appear at the gate and knit line. In production-scale molding, barrel residence time should be kept below 5 min when melt temperature exceeds 250 °C. A three-zone barrel profile of 220 °C rear, 235 °C center, and 240 °C front, with nozzle at 245 °C, is a representative starting condition for moderate shot sizes. Mold temperature is typically 40 °C to 70 °C; the lower region minimizes cycle time but may increase molded-in stress and haze, while the upper region improves gloss and flow-front replication. On a 320 kN clamp-force machine with a 20 mm diameter general-purpose screw and a 2.0 mm wall section, a melt temperature of 250 °C and mold temperature of 60 °C produced a clear part without gate blush when the hot-runner valve gate tip was held within ±5 °C of the nozzle set point. Published data for this specific configuration is limited; each tool should be characterized by pressure-drop and flow-length studies.

    Low-compression screws with a compression ratio of 2.0 to 2.5 and non-return valves designed for transparent resins reduce brown streaking and shear-induced yellowing. Avoid closed-loop melt-temperature controllers that overshoot above 260 °C during recovery; such overshoot can generate gels and black specks after 3 min of residence time. For light colors or natural parts, the barrel, screw, and hot runner should be purged with an acrylic-based purging compound before starting production. This reduces contamination from prior ABS or pigment residues. Batch-to-batch variation in melt viscosity may occur; proper monitoring includes checking melt volume-flow rate per ISO 1133-1:2022 at 220 °C/10 kg on incoming material and correlating fill time on a reference tool.

    Mechanical and thermal profile from molded specimens

    The properties below are manufacturer-published typical values for injected specimens in natural color. They are not intended as specification limits.

    Property Test method Unit Typical value
    Mass density ISO 1183-1:2019 g/cm³ 1.09
    Melt volume-flow rate ISO 1133-1:2022, 220 °C/10 kg cm³/10 min 5
    Tensile stress at yield ISO 527-2:2012 MPa 46
    Tensile elongation at break ISO 527-2:2012 % 15
    Flexural modulus ISO 178:2019 MPa 2200
    Flexural strength ISO 178:2019 MPa 65
    Charpy notched impact strength, 23 °C ISO 179-1:2010 kJ/m² 15
    Vicat softening temperature, B50 ISO 306:2013 °C 94
    Heat deflection temperature, 1.8 MPa ISO 75-2:2013/A °C 84
    Total luminous transmittance, 3 mm ISO 13468-1:2019 % 88
    Haze, 3 mm ASTM D1003-21 % 2.5
    Mold shrinkage ISO 294-4:2018 % 0.4–0.6
    Water absorption, 24 h ISO 62:2008 % 0.3

    The notched impact response of TX-0510T is thickness-dependent. Under ISO 179-1:2010, the Charpy notched value of 15 kJ/m² at 23 °C represents an energy absorption level sufficient for clip-style snap-fit housings where PMMA would fail by brittle crack propagation at undercuts. At wall thickness below 1.5 mm, molded-in orientation increases the yield stress but reduces crack propagation resistance in drop-impact loading. For thin-wall electronic front panels, instrumented falling-dart impact on finished parts should be used instead of relying solely on standard notched specimens. The heat deflection temperature of 84 °C under 1.8 MPa load indicates that continuous use under structural load at elevated temperature must be limited; non-load-bearing parts can tolerate brief excursions to the Vicat softening range around 94 °C but warpage increases as molded-in stress relaxes.

    Optical properties are sensitive to section thickness and mold polishing. The total luminous transmittance of 88% at 3 mm thickness under ISO 13468-1:2019 and haze of 2.5% under ASTM D1003-21 apply to a smooth, polished mold surface. A textured or re-polished mold changes light scattering and should be qualified by goniophotometric measurements rather than diffuse transmission alone. The resin does not retain PMMA-level scratch resistance; hard-coat layers can be applied post-molding, and the final article must be tested for adhesion and optical change according to the coating supplier’s method.

    Shrinkage behavior is used by tool designers to calculate cavity dimensions. Typical mold shrinkage reported by the manufacturer is 0.4% to 0.6% according to ISO 294-4:2018; however, actual shrinkage varies with gate geometry, wall thickness, and mold temperature. For a hot-runner side gate, measured shrinkage in a 2.0 mm plaque molded at 245 °C and 60 °C mold temperature tends toward the lower end of that range in the flow direction and the upper end transverse to flow. Tooling should allow steel-safe adjustment after first article inspection. No process condition removes this anisotropy; it is a function of molecular orientation.

    When heat resistance of polycarbonate is not required, selection shifts toward MABS

    Compared with general-purpose PMMA, TX-0510T has lower flexural modulus, lower surface hardness, and higher notched impact resistance. The flexural modulus of 2200 MPa under ISO 178:2019 is below the 3300 MPa typical of PMMA, so load-bearing panels may deflect more unless ribs or thickness are adjusted. The Charpy notched impact strength of 15 kJ/m² is substantially above the 2 kJ/m² commonly reported for unmodified PMMA, which permits snap-fit arms in housings; PMMA would require careful radii and may still crack under repeated load. Compared with standard transparent ABS, TX-0510T typically offers lower haze and higher total transmittance. Transparent ABS grades often range from 85% to 88% total luminous transmittance and 3% haze or higher at 3 mm thickness; TX-0510T is at 88% transmittance and 2.5% haze. The optical advantage comes from refractive-index matching between the rubber phase and the acrylic-rich matrix, which reduces interfacial light scattering. The trade-off is that MABS may show lower chemical resistance than opaque ABS because the matrix is modified for clarity, and environmental stress cracking resistance to alcohols, oils, and detergents can be different from high-acrylonitrile opaque ABS grades.

    Against polycarbonate, TX-0510T has lower heat and toughness. PC typically shows heat deflection temperature at 1.8 MPa around 130 °C and notched impact strength above 60 kJ/m², but requires melt temperatures from 280 °C to 320 °C and mold temperatures from 80 °C to 100 °C for optical parts. TX-0510T processes at 235–250 °C and 50–70 °C mold, reducing cycle time, energy input, and thermal degradation risk. The selection of TX-0510T over PC is therefore made when the use environment stays below 80 °C and impact loads are moderate; if autoclaving or continuous load near 130 °C is required, MABS is not an appropriate substitution. The lower melt temperature also permits molding of thinner flow paths without hot-runner overheating. In long-flow-length parts, the spiral flow length at 240 °C and 60 °C mold may be longer than PMMA but shorter than some high-flow PC grades; manufacturer-specific flow spiral data for TX-0510T is not universal and must be generated on the production tool.

    Because the matrix is acrylic-modified, chemical compatibility limits are significant for MABS TX-0510T. Exposure to ketones, esters, aromatic hydrocarbons, and chlorinated solvents can cause swelling, stress cracking, or haze. Cleaning agents should be evaluated under ASTM D543-21 using production parts under molded-in stress. Aliphatic alcohols and dilute aqueous acids generally produce less visual change in short contact, but published data for this specific grade is limited. In medical device enclosures, chemical cleaning with quaternary ammonium compounds or isopropanol wipes must be validated at the finished-device level because residual stress from molding and assembly determines stress-crack resistance. The resin itself does not provide device-level biocompatibility; validation under ISO 10993-1:2018 is required. Food-contact status must be confirmed through a manufacturer compliance letter because compositional variations and colorants affect regulatory coverage. In the United States, styrene copolymers may be evaluated under 21 CFR 177.1020 or related sections, and the finished article must comply with applicable migration limits and conditions of use.

    For applications that require sunlight exposure, UV stability of unpigmented MABS is limited. Outdoor exposure can cause yellowing and loss of impact due to butadiene-phase oxidation. Applications requiring sunlight exposure should use a UV-stabilized variant or an opaque coating and must be validated under ASTM G154-23 or equivalent outdoor weathering standards. UV absorber packages can reduce transmittance slightly; the effect on total luminous transmittance and haze should be measured after compound injection. The resin should be protected from moisture during storage and from temperatures exceeding 60 °C in hopper dryers for prolonged periods beyond the recommended drying temperature, because agglomeration and additive migration can occur. For cleanroom-molded parts, pellet handling should be controlled to prevent dust and paper fiber contamination. Conveying systems should use stainless steel contact surfaces and filtered air. Lot-to-lot pellet color variation in natural material is generally small, but color measurements under CIE Lab conditions with a spectrophotometer should be used to set incoming acceptance limits for visible appearance.

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