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Lotte Chemical STAREX® MABS TX-0530T

    • Product Name: Lotte Chemical STAREX® MABS TX-0530T
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 333333
    Density 1.08 g/cm³
    Melt Flow Rate 220 C 10 Kg 20 g/10 min
    Tensile Strength At Yield 45 MPa
    Tensile Elongation At Break 20%
    Flexural Modulus 2100 MPa
    Notched Izod Impact Strength 23 C 12 kJ/m²
    Heat Deflection Temperature 1 82 Mpa 78°C
    Vicat Softening Temperature 94°C
    Rockwell Hardness R Scale 105
    Light Transmittance 88%
    Haze 3%
    Molding Shrinkage 0.4-0.6%

    As an accredited Lotte Chemical STAREX® MABS TX-0530T factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Lotte Chemical STAREX® MABS TX-0530T is supplied in 25 kg moisture-proof bags, palletized for industrial handling and storage.
    Container Loading (20′ FCL) Lotte Chemical STAREX® MABS TX-0530T loaded in a 20′ FCL container as palletized 25 kg bags, shrink-wrapped and securely stowed.
    Shipping Lotte Chemical STAREX® MABS TX-0530T is shipped as non-hazardous thermoplastic resin pellets in sealed moisture-barrier bags or bulk containers. Keep containers closed, dry, and cool, away from direct sunlight and heat. Use standard industrial hygiene; no special transport classification is normally required.
    Storage Store in a cool, dry, well-ventilated warehouse away from direct sunlight, heat sources, and moisture. Keep in original sealed bags or packaging, palletized off the floor, and protect from physical damage and contamination. Avoid prolonged high humidity and observe manufacturer/SDS guidance and local regulations.
    Shelf Life Typically 24 months from manufacture when stored in original sealed packaging—dry, cool, and protected from direct sunlight.
    Application of Lotte Chemical STAREX® MABS TX-0530T

    STAREX® MABS TX-0530T is a methyl methacrylate–acrylonitrile-butadiene-styrene copolymer formulated for transparent rigid injection molding. Downstream application scenarios below are confined to documented sectors for this grade family. All processing values assume desiccant drying to ≤0.05 wt% residual moisture and are not transferable to uncontrolled hot-air dryers. No food-contact, medical, or potable-water approval is conveyed by resin supply; certification resides with the finished article under the cited standard.

    In point-of-care diagnostic housings, clarity retention after ethylene oxide sterilization and repeated disinfection with proprietary quaternary ammonium products is the primary selection criterion. STAREX® MABS TX-0530T is processed neat at 100 phr with an MABS-carrier color masterbatch limited to 0.5–1.5 wt% to preserve luminous transmittance above the grade-specific threshold measured under ISO 13468-1:2019 and haze below 3.0% at 3.0 mm wall under ASTM D1003; higher pigment loadings produce unacceptable scatter in barcode-reading windows. A silicone-based internal mold release at 0.05–0.2 wt% is permitted only when validated under ISO 10993-5:2009 for cytotoxicity and ISO 10993-10:2010 for skin sensitization on the finished device, not on resin alone. Pre-drying at 80°C for 3–4 h in a desiccant dryer with dew point below -40°C reduces moisture to ≤0.05 wt%; higher residual moisture causes silver streaking in transparent lens areas and weld-line weakness. Downstream processing is direct injection molding on 30–80 t clamp-force machines with rectangular sprue bushings; barrel set points range from 220°C at the rear to 245°C at the nozzle, mold temperature is held at 40–60°C, and holding pressure is 50–80 MPa with cushion control at 2.0–4.0 mm. Mold vent depths are limited to 0.015–0.025 mm to prevent flash while allowing gas evacuation; diamond-polished core pins reduce ejection friction. Terminal finished products include lateral flow test cassette windows, glucose meter display lenses, coagulation analyzer cuvette housings, and transparent caps used in respiratory pathogen assay kits. Ethylene oxide cycles are qualified at 50–60°C and 45–65% RH with ethylene oxide concentration 600–800 mg/L; after sterilization, aeration at 50–60°C for 12–24 h is required to drop residual gas below device-specific limits. The material is not rated for steam autoclave at 121°C; terminal sterilization is limited to ethylene oxide or electron beam after dose validation. Prolonged contact with lipid emulsions without stress-crack testing under ISO 22088-1 is not recommended because such media may plasticize the butadiene domain and reduce weld strength.

    Why Do Cosmetic Packaging Lines Run TX-0530T at Lower Mold Temperatures Than PMMA?

    Lower mold temperatures of 35–55°C, compared with 60–80°C for PMMA, reduce cycle time and lower the risk of gate blush in high-polish closures while maintaining surface replication from diamond-finished cavities. Compliance for cosmetic packaging is governed by Regulation (EC) No 1223/2009 for the finished article, with migration assessment under EU 10/2011 when refillable jars contact leave-on or rinse-off emollient formulations; U.S. cosmetic packaging may be assessed against 21 CFR 177.1010 or 21 CFR 177.1030 only after migration testing on the specific formulation. Formulation addition ratios for transparent amethyst or cobalt tints use solvent dyes at 0.001–0.01 wt% because higher dye loads shift haze and reduce light stability; opaque pearl masterbatch is added at 0.5–2.0 wt% when a translucent compact case is specified. A mold release agent of 0.05–0.2 wt% is pre-compounded, and external silicone sprays are not permitted because they migrate to the surface and cause fish-eye defects in UV-curable top coats. Production employs multi-cavity cold-runner tools with 8–24 cavities, valve-gated hot runners for thick lipstick overcaps, and direct edge gates for jar bodies; melt temperature is set between 230°C and 250°C, with injection velocity 80–150 mm/s and screw recovery below 0.35 m/s to avoid adiabatic shear that yellows the methyl methacrylate phase. Hold pressure is profiled at 40–70 MPa for 2–5 s at 1.5–2.5 mm wall; pack-to-hold switch is set by screw position at 5.0–8.0 mm. Terminal finished product types include lipstick caps, mascara applicator shafts in co-injection with elastomeric liners, pressed-powder compact lids, fragrance overcap bodies, and travel jar bases. Chemical compatibility tests with isododecane, cyclomethicone, and ethanol-water systems are performed on actual molded parts because MABS stress-crack resistance is formulation-specific; published data for this specific grade in prolonged ethanol contact is limited.

    Application zoneRelevant published standard or regulationMeasured property / thresholdProcess boundary
    Point-of-care diagnosticISO 10993-1:2018, ISO 10993-5:2009Cytotoxicity; residual moisture ≤0.05 wt%No steam autoclave at 121°C
    Cosmetic packagingRegulation (EC) No 1223/2009, EU 10/2011Migration of pigments and optical agentsMold 35–55°C
    Office automationRoHS 2011/65/EU, REACH 1907/2006Annex II restricted substancesContinuous use ≤70°C
    Toy glazingEN 71-3:2019, ASTM F963-23Element migration; drop at 1.35 mLow-temperature impact below -10°C requires validation
    Drinking-water connectorNSF/ANSI 61, EU 10/2011Extractables; overall migration 10 mg/dm²Hot water ≤70°C; chlorine ≤1.0 ppm

    For thin-wall transparent covers in office automation equipment, flame retardance is usually not imparted by the resin but by segregation from hot-wire or internal power-supply shielding; the relevant compliance is RoHS Directive 2011/65/EU Annex II for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE, plus REACH Regulation (EC) No 1907/2006 Annex XVII restrictions and SVHC candidate-list screening at the molded-part level. STAREX® MABS TX-0530T is processed with an antistatic masterbatch at 1.0–3.0 wt%, a tint masterbatch at 0.5–2.0 wt%, and no external lubricant above 0.1 wt% because deposit on cavity surfaces shortens cleaning intervals in 500,000-shot production campaigns. The downstream process is high-speed injection molding of 1.2–1.8 mm wall sections; barrel temperatures of 220°C rear and 240–250°C front are maintained, with mold temperature 40–60°C and injection velocity 150–250 mm/s to prevent flow hesitation at weld lines. Sequential valve gating is used in two-shot control-panel lenses; gate freeze time is estimated from the square of wall thickness and not from total shot weight. Clamp force is selected on 4.0–6.0 kN/cm² projected area to avoid flash at 250°C melt. Terminal finished products include printer front covers, scanner lid windows, copier control-panel lenses, barcode reader windows, and projector lens rings. Continuous surface temperature is limited to 70°C because higher temperatures shift the butadiene phase toward oxidative yellowing; no UL RTI above 70°C is implied by this processing guidance. Polycarbonate-like appearance is achieved only when mold steel is polished to SPI A-2 or finer; lower polish grades create micro-roughness that scatters light and lowers total transmittance under ISO 13468-1:2019.

    Impact-Modified Transparent Toy Glazing under Drop Test Criteria and Gate Location

    Toy-grade transparent glazing made from STAREX® MABS TX-0530T is subject to Directive 2009/48/EC and EN 71-3:2019 migration limits for nineteen elements, with U.S. requirements under ASTM F963-23 for heavy elements and mechanical drop testing from 1.35 m onto a steel tile for toys intended above 3 years; for under-3 items, small-part and sharp-edge testing controls design. Formulation addition ratios use high-dispersion color masterbatch at 1.0–3.0 wt%; light-stable organic pigments are selected because cadmium- and lead-based colorants are prohibited by EN 71-3:2019 at their specific migration limits. External impact-modifier addition is not recommended above 2.0 wt% because MABS already contains a grafted butadiene phase; exceeding that level increases haze under ASTM D1003 and lowers flexural modulus under ASTM D790 without proportional gain in notched Izod impact under ASTM D256. Production is direct injection molding with edge gates located at 1.5–2.0 mm wall non-appearance ribs to push flow fronts uniformly across large lenses; melt temperature is 230–245°C, mold temperature is 35–55°C, and hold pressure is 45–70 MPa for 3–6 s. Insert metal axles are preheated to 80°C to reduce differential shrinkage stress. Terminal finished products include transparent windows in toy vehicles, activity-center lens plates, toy robot eye shields, dollhouse furniture doors, and transparent gears in mechanical learning kits. The operational boundary is that repeated impact at low temperatures below -10°C can shift the failure mode from ductile hinge to brittle crack, so drop testing should bracket the lowest intended transport temperature, not only ambient 23°C.

    When TX-0530T Appears in Drinking-Water Connector Housings, Hydrolysis and VOC Compliance Take Priority

    Potable-water sight glasses and connector housings are not automatically approved by resin sale; certification under NSF/ANSI 61, KTW recommendations, or AS/NZS 4020 must be performed on the exact molded article with the exact gasket and lubricant package. The applicable migration framework for Europe remains EU 10/2011 with overall migration limit 10 mg/dm² and specific migration limits for acrylonitrile and methyl methacrylate; U.S. food-contact articles may be evaluated under 21 CFR 177.1030, but potable-water contact is a separate plumbing-code matter. Formulation addition ratios are tighter than cosmetic or toy grades: no silicone-based external mold release is used because it becomes an extractable peak in GC-MS screening; an internal release is permitted at 0.05–0.1 wt%, color masterbatch at 0.5–1.5 wt%, and regrind limited to 20 wt% with no more than 3 heat histories because hydrolysis of the nitrile group increases formaldehyde and ammonia headspace. Production is injection molding of 2.0–4.0 mm wall sight tubes and threaded collars with melt temperature 225–240°C, mold temperature 40–65°C, and cycle hold time extended to 8–15 s to reduce sink marks around threads. Molds are purged after color change; no copper-containing pigments are allowed because copper ions catalyze thermo-oxidative degradation during processing. Terminal finished products include water-purifier flow indicators, coffee-machine water-tank windows, humidifier sight tubes, beverage-dispenser hopper windows, and transparent diverter-valve caps. Continuous exposure to water above 70°C or chlorine above 1.0 ppm free chlorine requires chemical-resistance validation under ASTM D543; published data for this specific TX-0530T configuration in hot chlorinated potable water is limited.

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    Certification & Compliance
    More Introduction

    Lotte Chemical STAREX® MABS TX-0530T is an injection-molding grade of methyl methacrylate-acrylonitrile-butadiene-styrene. It is supplied as a transparent thermoplastic for thin-wall components that require visible-light transmittance, practical toughness, and lower processing temperatures than polycarbonate. The grade belongs to the STAREX MABS family, in which methyl methacrylate is copolymerized into the styrene-acrylonitrile matrix to reduce the refractive-index mismatch with dispersed butadiene-phase particles. This structural difference from standard opaque ABS reduces internal light scattering and yields a transparent material with specific flow and impact characteristics. The material is amorphous; mold shrinkage is uniform in the flow and cross-flow directions, and the density is lower than PMMA or polycarbonate.

    Published application references for MABS grades include transparent appliance windows, cosmetic packaging, medical device housings, diagnostic instrument covers, and consumer electronics accessory parts. The exact usability of TX-0530T in a given device depends on wall thickness, gate placement, sterilization method, and regulatory requirements for the final compounded formulation. Incoming quality control normally uses ISO and ASTM test methods on dry-as-molded specimens, because moisture and uncontrolled molding conditions alter both optical and mechanical data.

    Commercially useful transparency requires the butadiene particle size distribution and the matrix refractive index to be controlled within narrow limits. If the butadiene domains exceed roughly 200 nm, forward light scattering increases and haze becomes measurable. Therefore, high-shear dispersion during compounding must balance particle size reduction against excessive shear heating. Twin-screw extruders used for MABS compounding are typically operated with L/D ratios of 36:1 to 52:1 and downstream devolatilization to control residual volatiles. Addition of color concentrates can change optical scattering; transparent color packages must be evaluated for admittance at the final wall thickness.

    What optical and mechanical property values govern incoming inspection for TX-0530T?

    Incoming resin qualification typically follows ISO and ASTM methods. The melt volume-flow rate is determined at 220°C under 10.0 kg load according to ISO 1133-1. The resulting values place the grade among the high-flow transparent MABS products used for thin-wall molding. Transparency and haze are evaluated on 3.0 mm injection-molded plaques using ASTM D1003. Because optical performance is sensitive to plaque cooling rate, the mold temperature should be recorded during specimen preparation; optical values measured on uncontrolled plaques are not directly comparable.

    Typical property ranges reported for STAREX MABS TX-0530T; lot-specific certificate-of-analysis data govern for acceptance.
    Property Test method Unit Typical value or range
    Density ISO 1183-1 g/cm³ 1.09
    Melt volume-flow rate ISO 1133-1 cm³/10 min 22–28 at 220°C/10.0 kg
    Tensile yield stress ISO 527-2 MPa 41–48
    Tensile elongation at break ISO 527-2 % 12–25
    Flexural modulus ISO 178 MPa 1,900–2,200
    Notched Izod impact at 23°C ISO 180 kJ/m² 8–14
    Vicat softening temperature ISO 306 °C 90–96 at 50 N/50°C/h
    Luminous transmittance at 3.0 mm ASTM D1003 % 88–90
    Haze at 3.0 mm ASTM D1003 % 1.5–3.0

    The tensile and flexural values position TX-0530T below polycarbonate in load-bearing stiffness but above unmodified PMMA in notched impact. The notched Izod range is sensitive to specimen moisture content and gate orientation; dry-as-molded values are higher than values measured after moisture absorption. When comparing lots, laboratories should use the same ISO 180 notch profile and include the notch radius in the report. The flexural modulus is more commonly reported for ABS-family materials than tensile modulus, because it is used directly in short-term snap-fit and cover-deflection calculations; creep and fatigue loading require separate long-term data.

    Desiccant drying is mandatory before melt processing when ambient relative humidity exceeds 60%. A desiccant hopper dryer delivering air at 80°C for 3 h to 4 h is typical for the MABS family. Residual moisture above 0.05% by weight can produce splay, surface haze, and a measurable reduction in notched Izod impact. The dew point of the drying air should be held at or below −20°C. If the material has been exposed to humid air for more than 24 h, the drying time is extended and the lot should be sampled for moisture before production.

    Processors running closed-loop material-handling systems should confirm that hopper capacity, drying residence time, and airflow rate meet the material consumption rate. In tropical plants with high humidity, an insulated stainless-steel hopper and secondary dry-air purge prevent moisture re-absorption at the feed throat. Moisture-induced splay is often mistaken for mold contamination or venting problems, but the defect appears at the same gate-adjacent region and can be reproduced by delaying drying. Thermogravimetric analysis of MABS grades typically shows initial decomposition above 280°C in nitrogen, but the practical upper processing limit is lower because the butadiene phase begins to oxidize at elevated melt temperatures. At 270°C, peroxide formation at unsaturated sites can initiate gel formation during extended residence. The resulting gels appear as fisheye defects in transparent parts.

    Melt viscosity, shear-rate response, and thin-wall fill behavior at production speeds

    TX-0530T exhibits pseudoplastic flow behavior. In capillary rheometry at 220°C, melt viscosity decreases as shear rate increases. The material fills thin wall sections more readily than lower-flow MABS grades, but the melt may still show a yield stress at low temperatures. Screw plastication should use barrel set temperatures of 200°C to 240°C, with nozzle temperature at 220°C to 250°C. Mold temperature is commonly maintained between 40°C and 70°C, with higher values within this range applied to polished optical surfaces to reduce flow lines and improve surface replication.

    During injection, high screw speed can generate shear heating. If the melt exceeds 270°C at the screw tip, thermal degradation of the butadiene phase begins to produce yellowing and gel specks. The manufacturer’s processing guidance for clear ABS grades recommends setting back pressure at 0.3 MPa to 0.7 MPa and avoiding long residence time. The recommended melt residence time is less than 15 min at melt temperatures above 240°C. Injection speed should be profiled to avoid jetting at the gate; initial injection speed is often reduced for 0.1 s to 0.3 s until the gate area fills. For components below 1.0 mm wall thickness, a fast-fill process may be necessary to prevent premature freeze-off. The high melt-flow rate of TX-0530T supports flow length-to-wall-thickness ratios typical of MABS, but the exact flow length depends on cavity thickness, mold temperature, and injection pressure.

    On accumulator-assisted injection machines, molders often observe inconsistency in shot weight when the check ring is worn. Cushion stability should be held within ±2 mm for multi-cavity tools. A mold temperature of 70°C improves optical surface replication but increases cooling time; lower mold temperature raises cooling stress and can lead to stress whitening at gates or bosses. This trade-off is more visible in transparent grades than in opaque ABS because stress-induced haze is not masked by pigment.

    Visible-light transparency makes the grade suitable for diagnostic device housings, cosmetic closures, transparent aesthetic panels, and consumer electronics accessory covers. Transparent appliance windows and cosmetic closures require the optical properties measured under ASTM D1003 and the melt-flow rate under ISO 1133-1 to ensure filling of thin-walled aesthetic surfaces. In medical device housings, the material is often evaluated for biological safety by the final device manufacturer; the raw polymer supplier’s regulatory data should be requested for the exact grade and color concentrate. Compliance with ISO 10993-1 and REACH depends on the complete formulation and terminal sterilization method, not solely on the base resin.

    Food-contact suitability must be confirmed under EU Regulation (EU) No 10/2011 or the appropriate FDA 21 CFR references for the specific additive package and converter. The base resin publication may not cover colorants, mold release agents, or post-treatment. RoHS Directive 2011/65/EU and REACH Regulation (EC) No 1907/2006 declarations are applicable to the commercial product as supplied. Optical haze in MABS is measured on injection-molded plaques according to ASTM D1003. The haze value is thickness dependent; comparing a 3.0 mm plaque to a 1.0 mm plaque can be misleading. High-gloss polished mold surfaces produce higher luminous transmittance than textured surfaces. Gate type and part thickness affect molecular orientation and local birefringence; for diagnostic components requiring low optical retardation, annealing after molding may be required.

    When replacing PMMA or polycarbonate in transparent snap-fit housings

    Compared with PMMA, TX-0530T has lower modulus and lower surface hardness but higher notched impact strength and lower density. PMMA may show better scratch resistance and higher optical clarity in certain thicknesses, but it can be more brittle in snap-fit geometries and can require higher melt temperatures. MABS generally fills thin walls at lower melt temperature than PMMA of comparable molecular weight. However, surface hardness differences require design acceptance tests because MABS will show visible abrasion more quickly in repeated handling. The lower density of TX-0530T provides a mass reduction relative to PMMA in equivalent part volume.

    Compared with polycarbonate, MABS is not equivalent in high-temperature load-bearing performance. Polycarbonate has higher heat deflection temperature and significantly higher toughness, but requires drying at 120°C and melt temperatures of 280°C to 310°C. TX-0530T can be processed at 220°C to 250°C on standard ABS/PS injection lines without polycarbonate-specific screw materials and high-temperature mold oil. The lower melt temperature reduces energy input and may permit use of lower-cost tool steels in short runs, but the upper-use temperature of the finished part is also lower.

    Compared with standard opaque ABS, the methyl methacrylate comonomer introduces transparency but lowers resistance to certain solvents. Ketones, esters, aromatic hydrocarbons, and strong acids can attack the matrix. Designers should avoid prolonged contact with aggressive cleaning agents at molded-in stress concentrations. Avoid blending with polycarbonate, polyamide, or acetal contamination in regrind streams; these materials can create visible delamination, haze, or plate-out. For direct quantitative comparisons among TX-0530T, PMMA, and PC in the same tool geometry, published data for this specific configuration is limited; each conversion must rely on mold-flow simulation calibrated with capillary rheometry data from the actual lot.

    Storage environment should be dry, below 50°C, and protected from UV exposure. High ambient temperatures and prolonged sunlight exposure can yellow the pellets. The material is supplied in moisture-resistant packaging; after opening, remaining material should be resealed or dried before use. Because the material is amorphous, mold shrinkage is uniform and isotropic; published values are typically in the range of 0.4% to 0.7% depending on wall thickness, gate area, and packing pressure. Injection-molding process control should hold cushion and peak cavity pressure constant rather than using barrel temperature alone. If regrind is used in optical parts, it should be limited to 20% by weight and confirmed by transparency and impact testing after the first heat history.

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