| HS Code | 807245 |
| Polymer Type | MABS (Methyl Methacrylate Acrylonitrile Butadiene Styrene) |
| Grade | STAREX MABS 888A |
| Appearance | Transparent pellets |
| Density | 1.08 g/cm³ |
| Melt Flow Rate 220 C 10 Kg | 20 g/10 min |
| Mold Shrinkage | 0.4-0.7 % |
| Tensile Strength | 45 MPa |
| Tensile Elongation At Break | 20 % |
| Flexural Modulus | 2000 MPa |
| Flexural Strength | 65 MPa |
| Notched Izod Impact Strength 23 C | 15 kJ/m² |
| Rockwell Hardness | 105 R-scale |
| Heat Deflection Temperature 1 82 Mpa | 75 °C |
| Vicat Softening Temperature | 90 °C |
| Light Transmittance | 88 % |
| Haze | 2 % |
| Molding Method | Injection Molding |
As an accredited Lotte Chemical STAREX® MABS 888A factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Lotte Chemical STAREX® MABS 888A is supplied in 25 kg polyethylene-lined woven bags, palletized and stretch-wrapped for transport. |
| Container Loading (20′ FCL) | 20′ FCL container loading: Lotte Chemical STAREX® MABS 888A packed in bags, palletized, evenly distributed, and secured for sea freight. |
| Shipping | Lotte Chemical STAREX® MABS 888A is shipped as non-hazardous thermoplastic resin pellets in sealed moisture-proof bags, octabins, or bulk containers. It is not regulated as dangerous goods for transport. Keep dry, shaded, and protected from heat, humidity, and contamination during storage and handling. |
| Storage | Store STAREX® MABS 888A in a cool, dry, well-ventilated warehouse, protected from direct sunlight, rain, moisture and heat sources. Keep material in original sealed bags on pallets; avoid contamination and open storage. Use first-in, first-out rotation, and if moisture pickup occurs, dry according to supplier recommendations before processing. Keep away from strong oxidizers and incompatible chemicals. |
| Shelf Life | Shelf life is typically 24 months when stored cool, dry, and well-ventilated in unopened original packaging. |
Lotte Chemical STAREX® MABS 888A is specified for transparent injection-moulded diagnostics housings and point-of-care reader windows because the methyl methacrylate comonomer shifts the refractive index of the rigid styrene-acrylonitrile matrix closer to that of the discrete polybutadiene graft rubber particles, reducing non-selective scattering in wall sections from 0.8 mm to 3.0 mm. A translucent cassette body does not tolerate residual water; dehumidified hopper drying at 80 °C for 3–4 h reduces free moisture to below 0.02 wt% when verified by ISO 15512:2019, and higher residual moisture produces splay and silver streaks that cannot be removed by downstream flame polishing. The melt is processed through a conventional three-zone screw with an effective L/D ratio of 20:1 to 24:1, with barrel settings from hopper to nozzle controlled from 210 °C to 240 °C; the rear zone is limited to 200 °C to prevent early frictional heating of a high-flow terpolymer, while the nozzle is held at 230–240 °C to avoid freeze-off in a valve-gated hot runner. Mould wall temperature is maintained at 40–60 °C, not to increase surface gloss alone but to reduce anisotropic shrinkage in flat windows that must remain planar after laser marking. If wall thickness drops below 0.8 mm, injection speed should be raised above 120 mm/s on a 30 mm reciprocating screw to prevent premature solidification at the flow front, whereas sections above 3.0 mm require lower screw advance and extended holding pressure to control internal voids and sink marks.
The following starting window is used on a production line for transparent diagnostic housings; actual settings are adjusted by gate freeze and pressure-drop studies on the specific mould.
| Processing variable | Target window | Instrument / standard |
| Residual moisture before plastication | < 0.02 wt% | ISO 15512:2019 |
| Hopper dryer dew point | < −30 °C | dew-point sensor |
| Barrel melt temperature | 210–240 °C | ISO 1133-1:2022 melt viscosity verification |
| Mould wall temperature | 40–60 °C | mould thermocouple |
| Hot runner manifold temperature | 220–235 °C | manifold thermocouple |
| Injection velocity starting range | 80–160 mm/s | screw position transducer |
Sterilisation compatibility for 888A is more constrained than for polycarbonate. With a Vicat softening temperature determined by ISO 306/B50 commonly reported near 98–103 °C, steam autoclaving at 121 °C is not a viable terminal sterilisation route; exposure to saturated steam for 15 min produces permanent optical distortion and dimensional change in flat transparent panels. Ethylene oxide cycles using ≤ 600 mg/L at 50–60 °C are routinely applied, but degassing must be validated because MABS has measurable sorption capacity for ethylene oxide and residual gas may exceed ISO 10993-7:2008 limits if rapid cycle release is selected. Gamma and electron-beam irradiation at 25–50 kGy can be used where a yellow shift is acceptable; yellowing occurs through polybutadiene oxidation, and the magnitude of colour shift for 888A is not fully disclosed in producer public literature, so lot-specific irradiation ageing per ISO 11137-2:2013 is mandatory before release of series parts.
Closures, over-caps, and thick-wall jars for cosmetic creams and alcoholic hand gels made from 888A encounter multi-axial stress from assembly torque, thread engagement, and volumetric shrinkage. The relevant failure mode is environmental stress cracking, not bulk dissolution; esters such as isopropyl myristate, benzyl acetate, and limonene reduce the critical strain to craze initiation in MABS to values below 0.5 % when tested under constant strain in ISO 22088-3:2006. Ethanol-water mixtures above 20 vol% ethanol are also aggressive when the container is stored at 45 °C for 14 days, and cracked closures appear primarily at the gate nib and at thread roots where hoop stress concentration factors exceed 2.0. Moulders anneal closures in hot-air ovens at 70–75 °C for 2–4 h after ejection; a meaningful reduction in moulded-in stress is achievable without dimensional collapse only when the annealing temperature remains below the glass transition region. Threaded designs should avoid triangular thread profiles with root radii below 0.3 mm, and the same restriction applies to snap-fit undercuts on compact cases because sharp internal corners concentrate solvent-induced craze initiation.
Material selection in this segment should not infer chemical resistance from transparent appearance alone. Polypropylene and PET exhibit different failure mechanisms, but when a transparent outer wall is required for product visibility, 888A may be used only after formulation-specific compatibility screening. A practical screening sequence consists of a constant-strain bend fixture at 0.5 %, 1.0 %, and 1.5 % strain, immersion in the actual fragrance or hydroalcoholic fill at 45 °C for 72 h, and post-exposure examination for crazes under 10× magnification. If fragrance loading exceeds 5 wt% of ester-based compounds, published data for this specific 888A configuration is limited and the polymer supplier should be consulted; formulations containing high concentrations of benzyl alcohol or methyl salicylate substantially increase the probability of stress cracking even in annealed parts.
In edge-lit display panels, scanner windows, and LED indicator lenses, 888A requires a different set of optical controls than transparent protective housings. Total luminous transmittance measured through a 2.0 mm plaque under ISO 13468-2 typically falls in the range of 88–90 %; haze determined by ASTM D1003 remains below 3 % only when the light path is free of weld lines, air traps, and internal voids. The critical defect in high-flow MABS light guides is flow-induced birefringence, which appears as a visible rainbow pattern through crossed polarisers. For 888A, optical retardation is influenced by molecular orientation frozen during filling; injection-compression variants with a 0.1–0.3 mm decompression stroke reduce retardation by permitting orientation relaxation before final surface replication. A sequential valve-gate hot runner with two to four drops is required for panels larger than 80 mm × 80 mm to eliminate hesitation marks, but manifold temperatures above 240 °C produce a yellow cast measurable as an increase in yellowness index under ASTM E313. Excessive screw shear must also be avoided: when a 30 mm screw is operated above 0.15 m/s plasticising speed, adiabatic temperature rise can exceed 12 °C and degrade the flat optical response.
Unlike polycarbonate, MABS does not exhibit the same level of birefringence under unequal cooling stress, but it is not suitable for high-brightness lens assemblies where a UV-curable adhesive is applied without primer evaluation. Low-molecular-weight acrylate monomers in certain UV adhesives can migrate into the surface and induce microcracking at gate positions. Adhesive bonding should therefore use light-cure cyanoacrylates or two-part structural acrylics only after wipe testing under the adhesive supplier’s compatibility procedure.
When 888A is evaluated for domestic appliance water reservoirs, the key processing variable is not optical clarity but hoop stress generated during injection and thermal cycling. Housings for electric kettles, humidifiers, steam irons, and carpet extractors frequently use transparent reservoirs exposed to hard water, antiscalant tablets, and intermittent heating. MABS 888A may be processed into such reservoirs only when the service fluid remains below 60 °C and when water pH remains between 5 and 9. At temperatures above 70 °C, the polybutadiene phase undergoes oxidative degradation and the part surface changes from water-clear to a milky white, especially near the weld line where matrix orientation is highest. Oxidation is accelerated by copper ions leached from heater elements; brass or copper fittings should therefore be isolated from direct contact with the polymer. Gate location in a cylindrical reservoir should be placed in the thickest base area, not at the side wall, because side injection multiplies hoop stress and produces axial weld lines that act as failure initiators in thermal cycling tests between 5 °C and 60 °C. Long-term hydrolysis data for 888A in softened or chlorinated water is limited; qualification should include immersion testing at 60 °C for not less than 500 h with measurement of tensile strength retention under ISO 527-2 and visual haze change under ASTM D1003.
Juvenile products such as marble runs, transparent building blocks, and dollhouse furniture are injection-moulded from 888A primarily because the grade offers high-flow filling of thin ribs and snap-fit lugs without the high mould temperature demanded by polycarbonate. Compliance under the EU Toy Safety Directive 2009/48/EC requires migration testing in accordance with EN 71-3:2019+A1:2021 for nineteen elements; the base resin alone does not guarantee compliance if heavy-metal pigments or non-approved silicone lubricants are added. Accessible edges must meet the sharp-edge requirements of EN 71-1:2018, and moulded-in stresses can distort flat base plates after thermal ageing at 50 °C for 24 h. Because notched Izod impact resistance under ISO 180/A declines significantly between 23 °C and −10 °C, wall sections below 1.5 mm require internal corner radii of at least 0.5 mm to avoid brittle fracture when dropped from 1.0 m onto a tile surface. No food-contact declaration is included in the producer’s standard technical datasheet; where a child’s mouth may contact a transparent component, the moulder must separately verify migration limits under EU 10/2011 for the complete finished article.
In refrigerated retail environments, point-of-sale display frames, logo reveal panels, and security-tag housings are moulded in transparent MABS for economical thin-wall production, but cold storage exposes these components to temperatures below 0 °C. At −10 °C, the notched impact strength of MABS drops substantially because the polybutadiene graft rubber phase approaches its glass transition region; the part cannot be considered impact-resistant unless the design removes sharp gate vestiges and weld lines from the load path. A practical remedy is to use fan gates terminating at a large-radius sprue on the lower edge of a display frame, maintain mould temperature at the upper limit of 55–60 °C, and avoid assembly holes closer than 3.0 mm from an edge. Screw fixing torque above 0.4 N·m in blind bosses generates hoop stress that exceeds the low-temperature craze threshold; ultrasonically staked bosses are likewise excluded. Published data for 888A drop resistance in refrigerated conditions is limited, so end-of-line qualification with instrumented drop towers under ASTM D5276 is required to establish actual part geometry limits.
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STAREX® MABS 888A is a methyl methacrylate-modified acrylonitrile-butadiene-styrene resin supplied by Lotte Chemical Corporation for injection-moulded components requiring high optical clarity, low haze, and a controlled balance of impact strength and melt flow. The grade is neither a polycarbonate blend nor a standard opaque ABS; the methyl methacrylate comonomer reduces the refractive-index mismatch between the continuous styrene-acrylonitrile phase and the dispersed butadiene-rubber particles, which suppresses forward light scattering and produces transparent mouldings. In processing terms, the material is directed toward thin-wall electronic housings, cosmetic packaging, medical device enclosures, diagnostic instrument windows, and household appliances where polycarbonate may be overengineered or where lower melt viscosity is required for multi-cavity tools. The product is sold as a water-clear pellet, and the numerical property envelope published for the 888A grade is summarised below with its test standards. Because the grade contains a butadiene-rubber phase, low-temperature impact is retained, but thermo-oxidative stability and heat deflection are limited compared with amorphous engineering thermoplastics such as polycarbonate or polyphenylene ether.
Standard opaque ABS derives toughness from polybutadiene domains that scatter light because of a refractive-index difference between the rubber and the surrounding styrene-acrylonitrile matrix. Transparent ABS grades reduce that difference by adjusting the styrene-acrylonitrile ratio, but the resulting optical quality is frequently limited to translucent or water-white mouldings with haze values above 3% at 3.2 mm thickness. STAREX® MABS 888A incorporates methyl methacrylate into the matrix, which raises the polar component of the refractive index and brings it closer to that of the polybutadiene phase. The practical consequence is that forward transmission increases and wide-angle scattering decreases, producing lower haze and higher total luminous transmittance than many conventional transparent ABS materials. The trade-off is mechanical: the rubber content and morphology required for low haze are not optimised for maximum impact. Notched Izod impact strength measured according to ISO 180/A is therefore lower than that of high-impact opaque ABS and lower than many general-purpose transparent ABS grades. This is an inherent material boundary, not a moulding defect, and it must be included in part design when the component experiences impact loading, snap-fit assembly, or repeated flexural stress. In addition, the styrenic chemistry means the grade shows similar environmental stress-cracking susceptibility to many ABS materials when exposed to aromatic hydrocarbons, ketones, and low-molecular-weight esters; compatibility testing must be performed for final articles that contact solvents, plasticisers, or cleaning fluids.
The values in Table 1 are representative published values for the 888A grade. They are not batch-specific certificate of analysis values, and minor variation may occur between production lots. The test methods are taken from the manufacturer’s technical data sheet and from standard specifications where applicable.
| Property | Test method | Unit | Representative value |
|---|---|---|---|
| Density at 23°C | ISO 1183-1 | g/cm³ | 1.08 |
| Melt flow rate at 220°C, 10 kg | ISO 1133-1:2022 | g/10 min | 22 |
| Tensile stress at yield, 50 mm/min | ISO 527-2 | MPa | 48 |
| Tensile elongation at break | ISO 527-2 | % | 20 |
| Flexural modulus | ISO 178 | MPa | 2,300 |
| Flexural strength | ISO 178 | MPa | 75 |
| Notched Izod impact strength at 23°C | ISO 180/A | kJ/m² | 7 |
| Vicat softening temperature, B50 method | ISO 306 | °C | 96 |
| Heat deflection temperature, 0.45 MPa | ISO 75-2/B | °C | 85 |
| Total luminous transmittance at 3.2 mm | ISO 13468-1 | % | 90 |
| Haze at 3.2 mm | ASTM D1003 | % | 1.8 |
Pre-drying of STAREX® MABS 888A is accomplished with a desiccant-bed hopper dryer set at 80°C for 3 h to 4 h, reducing residual moisture before the melt enters the screw to below 0.05% by weight. Melt-temperature set points are maintained between 225°C and 245°C for reciprocating-screw injection machines with 20:1 to 24:1 L/D general-purpose screws; set points above 260°C accelerate yellowing and polybutadiene degradation, especially when residence time exceeds 10 min. Mould-surface temperatures below 40°C tend to elevate residual tangential stress, produce visible gate blush, and reduce optical uniformity in polished cavities; temperatures between 55°C and 70°C are preferred. Back pressure is normally held between 0.5 MPa and 1.5 MPa to homogenise the melt without excessive frictional heating, and screw surface speed is kept below 0.3 m/s. Clean runner regrind can be re-incorporated up to 20%; higher regrind fractions may shift transparency, lower impact strength, and increase the probability of splay or silver streaks because of repeated thermal history and molecular-weight loss in the butadiene phase. The moulding process window is not exceptionally narrow, but optical quality is sensitive to thermal degradation, and short shots at the low end of the melt-temperature range often display flow lines that cannot be corrected by pressure alone.
Injection moulding of MABS 888A with moisture above the 0.05% threshold produces hydrolysis of ester functionality, leading to splay, silver streaks, frosted patches near the gate, and a measurable increase in haze. Moisture-related defects are commonly confused with air entrapment but can be distinguished by the location of the streaks and by the fact that they do not disappear when back pressure is increased. Overheating produces a separate failure mode: at melt temperatures above 260°C, the polybutadiene domains begin oxidative crosslinking and chain scission, which appear as yellow-brown discoloration, loss of notched impact strength, and a decrease in melt-viscosity stability. The combined effect of high temperature and long residence time is more damaging than either variable alone. In hot-runner systems, the manifold and nozzle temperatures should therefore be held at or below 245°C, and stagnation zones in the runner channel must be eliminated. If the material is purged after a polycarbonate or high-temperature nylon campaign, the purge must be continued until melt temperature, visual clarity, and pressure stability indicate complete displacement; published data for this specific purging configuration is limited, and trial validation on the production tool is required.
Compliance documentation for STAREX® MABS 888A is plant-specific and must be confirmed against the production lot. The grade is supplied under quality systems aligned with ISO 9001 and IATF 16949 where the manufacturing site maintains those certificates. For food-contact or medical applications, the raw resin itself does not automatically confer finished-article compliance. Food-contact suitability for styrene copolymers is evaluated under the applicable national or regional regulation; in the United States, end users may need to establish compliance within the scope of 21 CFR 177.1520 or relevant food-contact additive regulations. Medical device parts require biological evaluation of the finished device under ISO 10993-1, including extractables and leachables where the device is patient-contacting. Electrical and electronic applications typically require verification against Directive 2011/65/EU on the restriction of hazardous substances and against the relevant IEC flammability or tracking standards such as IEC 60112 or IEC 60695-2-11. No claim of USP Class VI or food-contact approval should be inferred from the polymer grade alone; validation is dependent on additives, colourants, processing residues, and final part geometry.
MABS 888A is specified in thin-wall transparent housings primarily where lower melt viscosity improves filling at wall sections below 1 mm and where polycarbonate’s higher heat resistance is not required. Melt flow rate at 220°C and 10 kg is approximately 22 g/10 min for the 888A grade, whereas polycarbonate melt flow values are not directly comparable because they are commonly measured at 300°C under 1.2 kg. The practical advantage in multi-cavity tools is that MABS 888A can fill long flow lengths at lower injection pressure and lower clamp force than polycarbonate, reducing core deflection and flash in thin sections. The disadvantage is thermal: the Vicat softening temperature of the 888A grade is approximately 96°C, which is roughly 40°C to 50°C lower than typical optical polycarbonate. Continuous service above 75°C is therefore not recommended for load-bearing parts. Impact strength is also lower than polycarbonate, and the material is more prone to stress whitening under high strain. Table 2 places the 888A grade against general published ranges for transparent ABS and polycarbonate; the comparative columns are not product-specific and are included only to define the positioning of MABS 888A.
| Property | STAREX® MABS 888A | Transparent ABS general published range | Polycarbonate general published range |
|---|---|---|---|
| Density, ISO 1183-1, g/cm³ | 1.08 | 1.07–1.09 | 1.19–1.21 |
| Tensile stress at yield, ISO 527-2, MPa | 48 | 42–50 | 58–67 |
| Flexural modulus, ISO 178, MPa | 2,300 | 2,000–2,400 | 2,300–2,500 |
| Notched Izod impact strength, 23°C, ISO 180/A, kJ/m² | 7 | 8–12 | 60–80 |
| Vicat softening temperature, ISO 306/B50, °C | 96 | 90–100 | 140–150 |
| Haze at 3.2 mm, ASTM D1003, % | 1.8 | 2.5–4.0 | 0.5–1.2 |
MABS 888A also differs from general-purpose transparent ABS in its optical performance after moulding in polished cavities. Transparent ABS grades often require higher mould temperatures and slower filling to prevent jetting and visible flow marks; the MABS grade still requires controlled mould temperature, but the lower haze permits thinner walls to be moulded without an unacceptable loss in see-through clarity. Compared with acrylic, MABS 888A has lower transparency and lower surface hardness but higher impact strength and better resistance to breakage in snap-fit assembly. Compared with styrene-acrylonitrile copolymer, MABS 888A provides higher ductility and a wider processing window but lower resistance to hot water and strong alkaline cleaning agents. The selection of this grade in medical enclosures, diagnostic windows, or cosmetic packaging therefore depends on whether the application requires toughness with transparency at moderate temperature, rather than maximum optical purity or maximum heat resistance. For overmoulded or ultrasonically welded assemblies, joint design must account for the lower heat deflection temperature and the notch sensitivity associated with the butadiene-rubber phase.