| HS Code | 774640 |
| Materialtype | MABS (Methyl Methacrylate Acrylonitrile Butadiene Styrene) |
| Density | 1.08 g/cm3 |
| Meltflowrate | 15 g/10 min (220°C/10 kg) |
| Tensilestrength | 45 MPa |
| Flexuralmodulus | 2000 MPa |
| Izodimpactstrengthnotched | 15 kJ/m2 (23°C) |
| Heatdeflectiontemperature | 75°C (1.8 MPa) |
| Vicatsofteningtemperature | 90°C |
| Rockwellhardness | 100 R-scale |
| Lighttransmittance | 88% |
| Haze | 3% |
| Moldingshrinkage | 0.4-0.6% |
As an accredited Lotte Chemical STAREX® MABS TX-0550K factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg moisture-resistant bags, Lotte Chemical STAREX® MABS TX-0550K resin pellets are supplied on pallets for industrial handling. |
| Container Loading (20′ FCL) | Container loading (20′ FCL): Lotte Chemical STAREX® MABS TX-0550K in standard export packaging, palletized, securely stowed, and sealed for shipment. |
| Shipping | Lotte Chemical STAREX® MABS TX-0550K is typically supplied as dry polymer pellets in 25 kg bags or 1,000 kg jumbo bags, palletized and stretch-wrapped. It is non-hazardous for transport; keep dry, ventilated, and away from heat, sunlight, and moisture during shipping and storage. |
| Storage | Store Lotte Chemical STAREX® MABS TX-0550K in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and ignition sources. Keep original containers or bags tightly sealed to prevent moisture pickup and contamination. Palletize and stack according to packaging instructions. Avoid contact with strong oxidizers and acids. Maintain good housekeeping, avoid dust accumulation, and use first-in, first-out stock rotation. |
| Shelf Life | Typically 24 months from manufacture when stored unopened in original packaging, dry, at room temperature, and away from direct sunlight. |
Cosmetic packaging lines running Lotte Chemical STAREX® MABS TX-0550K in continuous production typically configure hot-runner injection moulding cells with polished S136 or Stavax cavities, because surface fidelity around a lipstick mechanism thread or compact hinge is directly affected by the melt-temperature profile, mould surface roughness and gate position relative to shear-sensitive transparent sections. Under Regulation (EC) No 1223/2009, the finished packaging article is not a cosmetic ingredient but is subject to Packaging and Packaging Waste Directive 94/62/EC Annex II, which restricts the sum of lead, cadmium, mercury and chromium(VI) in packaging components to 100 ppm by weight, and to REACH Regulation (EC) No 1907/2006 Annex XVII where intentionally added substances are present. The formulation is run at 100 parts by weight of TX-0550K with 0.6–1.2 wt% of a solvent dye masterbatch for tinted transparent parts or 1.0–2.0 wt% of a pearl masterbatch for high-depth effects; in-house regrind is limited to 15 wt% because higher reclaim fractions raise haze from a baseline below 2.0% to more than 4.0% when measured according to ISO 14782. The downstream process consists of desiccant drying at 80 °C for 3–4 h to a residual moisture below 0.05%, followed by injection moulding at a melt temperature of 220–250 °C, a tool temperature of 50–70 °C, a nozzle temperature of 230–240 °C and an injection speed not exceeding 120 mm/s; the screw is specified with an L/D ratio of 20:1 to 22:1 and a compression ratio of 2.0:1 to 2.5:1. Screw recovery times between 18 s and 28 s are typical for multi-cavity tools with hot-drop and valve-gate systems. If the tool temperature drops below 50 °C, weld-line visibility increases at the hinge area and around thread splits; above 70 °C, cooling time lengthens and the material tends to adhere to mirror-finished cores. Terminal parts produced under this protocol include lipstick sleeves, compact base inserts, fragrance caps, mascara cylinder bodies and transparent outer shells for cream jars; these components can be UV metallized, tampo-printed with low-aromatic solvent-based ink or laser-marked after moulding when the gate region is stress-relieved.
For diagnostic device housings and fluid observation windows, the selection of TX-0550K is governed by the need to combine transparent visual inspection of liquid levels with resistance to isopropyl alcohol, citric acid-based instrument cleaners and quaternary ammonium disinfectants used in point-of-care equipment. The relevant biological evaluation framework is ISO 10993-1:2018, with cytotoxicity testing according to ISO 10993-5 and, where patient-contact classification requires, USP <87> and USP <88> under the current compendial edition; manufacturing controls fall under ISO 13485:2016 and 21 CFR Part 820. The compound is run at 100 parts by weight of virgin TX-0550K with a biocompatibly assessed colour masterbatch added at 0.3–0.8 wt%; no post-consumer reclaim and no regrind are introduced into patient-contacting or fluid-transmitting components unless a validated clean-room re-pelletisation study has been completed. In production, the resin is desiccant-dried at 80 °C for 3–4 h, and injection-moulded in an ISO Class 8 cleanroom with a cold-runner or hot-runner tool at a melt temperature of 230–250 °C and a mould temperature of 60–80 °C. The higher mould temperature is used to reduce residual stress in snap-fit closures and to avoid white stress marks around threaded ports; cooling time per millimetre of wall thickness is approximately 4–6 s, and the gate size for transparent diagnostic windows is kept above 60% of the nominal wall section to prevent jetting defects. Terminal articles include non-implantable diagnostic cartridge housings, sample viewing windows for in vitro diagnostic instruments, reagent reservoir shells, fluid-level sight tubes and transparent covers for analyser sample compartments. Operational boundaries are as follows: steam sterilisation above 121 °C is outside the dimensional stability range of the grade, gamma or electron-beam sterilisation must be validated for each dose, and continuous contact with lipid-based media or strong aromatic solvents is not recommended because environmental stress cracking can occur in stressed sections.
Long-term contact of transparent MABS with deionised water, potable water and citric acid descaling solutions imposes a processing constraint that is most frequently observed as weld-line haze around inlet bosses and side-wall gussets; pre-production trials establish a critical mould-temperature corridor of 55–70 °C, below which weld-line visibility increases and above which cycle time exceeds 25 s without a corresponding gain in mechanical integrity. For these water-contact reservoir parts, the applicable safety framework includes IEC 60335-1 with IEC 60335-2-98 for humidifiers or IEC 60335-2-15 for liquid-heating appliances; if the reservoir is marketed for drinking-water contact, NSF/ANSI/CAN 61 certification and KTW-BWGL approval are required, and the resin supplier's certification file must be checked against the final article. The formulation is run at 100 parts by weight of TX-0550K, with 0.5–1.0 wt% of an external silicone-lubricant masterbatch for ejection and 0.2–0.5 wt% of an acid-pH-stable blueing agent where a water-white tint is required; amine-based antistatic packages are avoided because they reduce transparency stability after prolonged contact with descaling acids. Downstream processing uses a two-plate cold-runner tool or a sequential valve-gated hot runner, with desiccant drying at 80 °C for 3–4 h, a melt temperature of 220–240 °C, a nozzle temperature of 230 °C and a mould temperature maintained between 55 °C and 70 °C. The injection speed is profiled from 30 mm/s at the gate to 80 mm/s in the main filling phase to avoid turbulence and air entrapment at the float boss; after ejection, parts are annealed at 70 °C for 1.5–2 h to reduce internal stress and to improve resistance against environmental stress cracking in citric acid solutions at 40 °C. Terminal finished products include transparent water tanks for humidifiers, air purifier water troughs, steam mop reservoirs and robot vacuum mopping dock water compartments.
When a transparent ABS grade is introduced as a PC/ABS replacement in thin-wall consumer electronics accessories, the main processing differences are the lower melt temperature and the narrower shear-rate range before surface defects appear. The regulatory set for this segment is IEC 62368-1 for audio/video and information technology equipment safety, RoHS Directive 2011/65/EU Annex II limits of 0.1 wt% lead, 0.01 wt% cadmium, 0.1 wt% mercury and 0.1 wt% hexavalent chromium in homogeneous materials, and REACH Regulation (EC) No 1907/2006 candidate list restrictions for the final article. The compound is run as 100 wt% TX-0550K for standard gloss and transparency; for improved surface pencil hardness measured by ASTM D3363, a blend at 85–95 wt% TX-0550K with 5–15 wt% PMMA is used, provided that the supplier verifies compatibility and does not generate haze above 3.0% when tested to ISO 14782. Downstream production uses a desiccant dryer at 80 °C for 3–4 h, a screw L/D of 20:1, a melt temperature of 220–240 °C, a tool temperature of 50–65 °C and hot-runner valve gates for parts with wall thickness from 0.8 mm to 2.0 mm. Injection speed is limited to 60–100 mm/s for thin ribs and boss pads; higher speeds create streaking, while lower speeds cause premature freeze and short shots in pinpoint-gated lenses. The transparent substrate can be vacuum-metalized, UV-coated or laser-marked; adhesion of UV hard-coat systems is verified by ISO 2409 cross-cut tests after 24 h conditioning at 23 °C and 50% relative humidity. Terminal finished products include headphone earcup outer covers, portable speaker lens rings, router front panels, smart-home sensor covers and transparent charger housings. The operational limit is continuous service above 80 °C, because the Vicat softening temperature of MABS is below that of PC/ABS and dimensional distortion can occur in enclosed charging devices.
In toy and juvenile product production, transparent components such as toy vehicle windscreens, microscope accessory housings and toy cash-register drawers are injection-moulded from TX-0550K under the chemical migration framework of EN 71-3:2019+A1:2021 and the safety requirements of EU Directive 2009/48/EC; for the United States and Canada, the applicable standard is ASTM F963-23, and in all cases the final colour masterbatch must not contain heavy metals above the element-specific migration limits. The formulation is 100 parts by weight of TX-0550K with 0.5–1.5 wt% of a toy-grade colour masterbatch or 1.0 wt% of a pearlescent masterbatch; regrind is permitted up to 10 wt% only when the material has been generated from clean, unpigmented runners and its melt-flow retention is confirmed by ISO 1133-1. The production process uses the same desiccant drying and 220–240 °C melt-temperature window, but the mould temperature is lowered to 40–60 °C and hold pressure is increased to avoid sink marks at thick bosses; cycle times for transparent toy parts with wall sections from 1.5 mm to 3.0 mm are typically 25–35 s. Terminal products include transparent toy vehicle windscreens, toy microscope accessory housings, transparent toy storage canisters and toy cash-register drawers; these parts are not intended for hot food contact or for use as containers for ingestion.
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Specified as a transparent methyl methacrylate–acrylonitrile–butadiene–styrene terpolymer, Lotte Chemical STAREX® MABS TX-0550K is intended for injection moulding of high-gloss cosmetic closures, transparent pump housings, display frames, point-of-sale components, and thin-wall consumer appliance parts where clarity and high melt flow are simultaneous processing constraints. The methyl methacrylate comonomer reduces the refractive-index mismatch between the styrene–acrylonitrile continuous phase and the dispersed polybutadiene rubber domains, producing transparency without the high drying and melt temperature demands of polycarbonate. The product is differentiated from opaque ABS grades by lower rubber-phase content, which reduces impact energy absorption but permits visible-light transmission. It is differentiated from PMMA by lower melt viscosity and better resistance to sharp-corner fracture, but with lower surface hardness and heat resistance. Published data for this specific configuration is limited; property statements that are not lot-specific are class-representative and must be verified against the manufacturer’s technical data sheet.
Optical acceptance is typically measured with an integrating-sphere spectrophotometer according to ASTM D1003. For transparent injection-moulding MABS at 3.2 mm thickness, total luminous transmittance remains in the 88% to 91% range, and haze is generally below 2%; product-specific values for TX-0550K must be taken from the release certificate. Gamma irradiation at 25 kGy to 40 kGy produces free radicals in the SAN continuous phase that recombine into conjugated chromophores, increasing yellowness index and lowering transmittance. The change is dose-rate dependent and cannot be removed by drying. Autoclave sterilization at 121°C is outside the thermal capability of this product class because the heat deflection temperature under 1.82 MPa remains below 90°C when tested according to ISO 75-2/A. If sterile medical packaging is considered, the finished device must undergo biological evaluation per ISO 10993-1:2018; the raw material itself is not automatically approved for body contact, and the specific radiation stabilizer package must be declared by the converter.
Desiccant drying is mandatory before injection moulding. A closed-loop desiccant-bed dryer with an air dew point below -30°C and resin residence time of 3 h to 4 h at 80°C brings moisture below the 0.02% target. If loading is from a gaylord stored at ambient relative humidity above 60%, surface moisture can exceed 0.05% within 8 h; the result on the press is gate-area splay, elevated haze, and unstable filling due to hydrolytic chain scission. On a 30:1 L/D single-screw injection unit with a 25 mm to 60 mm screw diameter, melt temperature measured at the nozzle is maintained from 230°C to 255°C. Residence time above 10 min at the maximum barrel temperature produces yellowing and should be avoided. A back pressure of 5 bar to 15 bar hydraulic and low-compression screw geometry with a smoothly cut three-zone profile are used to avoid shear heating beyond 260°C.
On a 500 kN to 2 000 kN electric injection moulding machine producing 2.5 mm thick flat closures, the molten material should be injected at velocities from 30 mm/s to 80 mm/s and held at a packing pressure 1.5 to 2.0 times the peak cavity pressure to avoid sink and warpage. Low mould temperatures between 40°C and 70°C preserve surface gloss but reduce flow length and increase orientation. If the tool uses a valve-gated hot runner, manifold temperature is set 10°C to 20°C above nozzle melt temperature, but not above 270°C; film gates are preferred over sub-gates because shear heating at the gate causes free-surface haze. Gate freeze time for a 2.5 mm wall should be determined by short-shot cavity weight versus hold time, not by generic processing tables.
Recovery conditions on a 50 mm screw should keep the screw rotation below 150 min⁻¹ and the melt residence time below 10 min. If regrind is used at 20% or higher, loss of luminance and an increase in haze above 1.5% at 3.2 mm can be detected with a spectrophotometer; regrind streams must be sieved through a 5 mm screen and dedusted to prevent streaking. These are production-floor failure modes observed in high-cavitation tooling where direct gated cold-runner systems are not purged frequently enough; purging with a high-viscosity acrylic compound is performed at 250°C to remove oxidized residue.
When PMMA is replaced by MABS TX-0550K in a low-profile cosmetic cap, the first measured difference on the shop floor is filling pressure at constant melt temperature. PMMA grades typically require melt temperatures from 230°C to 250°C and still exhibit higher viscosity because of their methacrylate backbone; MABS flows more readily at the same shear rate and permits lower injection pressure. The trade-off is surface hardness and scratch resistance: PMMA has a Rockwell M-scale hardness and Taber abrasion resistance superior to most MABS products when tested according to ASTM D785 and ASTM D4060, while MABS provides better resistance to brittle failure during side-gate ejection. Compared with transparent polycarbonate, MABS has lower heat resistance and lower notched impact strength, but is generally easier to process in high-cavitation tooling because melt viscosity is lower and drying demands are less severe. Compared with opaque ABS, TX-0550K sacrifices impact strength for clarity and is more susceptible to stress cracking when exposed to alcohols in rigid mouldings with high residual stress.
| Property | Test method | MABS class envelope | PMMA class envelope | PC class envelope |
|---|---|---|---|---|
| Density | ISO 1183-1 | 1.07–1.09 g/cm³ | 1.18–1.20 g/cm³ | 1.20–1.22 g/cm³ |
| Tensile stress at yield | ISO 527-2/1A/50 | 40–55 MPa | 65–75 MPa | 60–70 MPa |
| Flexural modulus | ISO 178 | 2 000–2 500 MPa | 2 800–3 300 MPa | 2 200–2 400 MPa |
| Charpy notched impact | ISO 179-1/1eA | 7–12 kJ/m² | 2–4 kJ/m² | 35–70 kJ/m² |
| Heat deflection temperature | ISO 75-2/A | 80–90°C | 95–105°C | 125–135°C |
| Total luminous transmittance, 3.2 mm | ASTM D1003 | 88–91% | 91–92% | 87–90% |
| Haze, 3.2 mm | ASTM D1003 | 0.8–2.5% | <1.0% | <1.5% |
The MABS column is a class envelope, not a product specification for Lotte Chemical STAREX® MABS TX-0550K. Some lot-specific values may fall outside the envelope; the manufacturer’s certificate of analysis controls.
Before a transparent closure is released for cosmetic or medical use, the converter must document compliance with regulatory schemes that are not automatically granted by the resin producer. EU RoHS Directive 2011/65/EU restricts lead, mercury, cadmium, hexavalent chromium, PBBs, and PBDE in homogeneous materials; verification is typically performed by XRF screening and wet chemical confirmation according to IEC 62321-5 and IEC 62321-6. EU REACH Regulation (EC) No 1907/2006 Article 33 requires communication if a substance of very high concern is present above 0.1 wt% in an article. For food-contact candidate uses, MABS may be evaluated under national migration regimes; in the United States, the relevant polymer safety review is based on 21 CFR 177.1020 for styrene–acrylonitrile copolymers and must include migration testing because the formulated colour package and processing residues are not automatically covered by resin compliance.
Chemical compatibility of MABS differs from PMMA and PC. Alcohol-based formulations and fragrance components that contain terpenes or esters can initiate environmental stress cracking in rigid parts with high internal stress. The classic screening method is ISO 22088-3:2016 using a bent-strip strain jig; mouldings immersed in 50% ethanol or isopropyl alcohol under strain should be examined for surface whitening after 24 h to 48 h. Ketones, chlorinated solvents, and aromatic hydrocarbons should be avoided. Mineral oil and polydimethylsiloxane-based lubricants are generally less aggressive, but each formulation must be tested at the maximum expected service temperature because stress-cracking severity increases above 40°C.
| Requirement | Primary standard/regulation | Typical test method | Scope |
|---|---|---|---|
| Hazardous substances in homogeneous materials | EU RoHS Directive 2011/65/EU Annex II | IEC 62321-5 and IEC 62321-6 | Lead, mercury, cadmium, hexavalent chromium, PBBs, PBDE |
| SVHC communication | REACH Regulation (EC) No 1907/2006 Article 33 | Analytical screening per article | 0.1 wt% threshold per homogeneous material |
| Food-contact safety | US FDA 21 CFR 177.1020 | End-use migration testing | Formulated article; not raw resin blanket approval |
| Biocompatibility for medical use | ISO 10993-1:2018 | Device-level biological evaluation | Cytotoxicity, sensitization, irritation as applicable |
| Environmental stress cracking screening | ISO 22088-3:2016 | Bent-strip immersion | Alcohol, terpene, ester exposure |
In a high-cavitation production environment for transparent over-caps, the largest source of lot-to-lot variability is not resin melt temperature but regrind history and hot-runner thermal gradient. When a valve-gated hot runner with 16 drops is operated with a manifold temperature difference above 10°C, the outer cavities fill later and show higher anisotropic shrinkage; using sequential valve-gate control and pressure transducers in each gate reduces optical rejects. For medical pump housings, the MABS surface must be evaluated for extractables under the intended sterilization dose and solvent exposure conditions of the finished device. Published data for this specific configuration is limited; therefore, process capability studies should be run on the production machine before locking the shrinkage compensation factor.