| HS Code | 976527 |
| Polymer Type | MABS |
| Density | 1.08 g/cm³ |
| Melt Flow Rate | 12 g/10 min (220 °C/10 kg) |
| Tensile Strength | 45 MPa |
| Elongation At Break | 30% |
| Flexural Modulus | 2100 MPa |
| Notched Izod Impact Strength | 15 kJ/m² |
| Heat Deflection Temperature | 75 °C at 0.45 MPa |
| Vicat Softening Temperature | 90 °C |
| Light Transmission | 88% |
| Haze | 2% |
| Rockwell Hardness | R105 |
As an accredited PTS Trilac® MABS TR558-CL factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PTS Trilac® MABS TR558-CL is supplied in 25 kg net-weight, moisture-resistant polyethylene-lined bags, palletized for industrial handling. |
| Container Loading (20′ FCL) | A 20′ FCL container is loaded with palletized PTS Trilac® MABS TR558-CL, securely strapped and protected for ocean transport. |
| Shipping | PTS Trilac® MABS TR558-CL is normally shipped as a non-hazardous thermoplastic resin in sealed, labeled bags or drums. Confirm the current SDS and local transport rules for any UN/hazard classification. Keep containers closed, dry, and away from excessive heat or contamination during transit. |
| Storage | Store PTS Trilac® MABS TR558-CL in a cool, dry, well-ventilated area, using tightly closed, labeled original containers. Protect from moisture, direct sunlight, heat, sparks, and open flames. Keep away from incompatible materials and prevent physical damage. Follow local regulations and the supplier’s safety data sheet for shelf life and specific handling requirements. |
| Shelf Life | Typically 24 months from production date when stored unopened in a dry, cool place, protected from moisture and direct sunlight. |
In cleanroom injection molding of transparent medical device components, the MABS feedstock is first dried in a desiccant dryer to a residual moisture target below 0.02% by weight, because hydrolytic degradation of the methacrylate phase generates splay and reduces impact stability. Barrel temperature profiles typically ascend from 180–200°C in the feed zone to 220–250°C at the metering zone and nozzle, while mold temperatures are held at 40–70°C to balance surface gloss against cycle time. Multi-cavity tools for clear luer fittings, dialyzer housings, and fluid-management manifolds are run on electric injection molding machines with clamp force of 2.5–5.0 kN/cm² of projected area and screw L/D ratios from 20:1 to 24:1. Gates must be sized to avoid high shear heating: valve-gate diameters below 1.2 mm produce melt fracture and visible gate blush in thin transparent sections, while edge gates above 2.0 mm create gas entrapment at the end of flow. Holding pressure is set between 30–60 MPa and adjusted until sink marks are eliminated at thick bosses, but packing above 70 MPa increases molded-in stress near ribs and can materially lower environmental stress crack resistance after sterilization. The most frequent defect observed on production-scale molding of clear MABS medical parts is silver streaking caused by inadequate drying or high shear at the non-return valve. The check-ring design should use a clearance of 0.02–0.04 mm and a low-compression screw ratio of 2:1 to reduce dead spots and resin stagnation.
Biocompatibility documentation for this polymer cannot be assumed from the resin supplier alone; each finished medical device must be evaluated under ISO 10993-5:2009 for cytotoxicity and ISO 10993-10:2010 for irritation and skin sensitization. For devices with prolonged skin-contact exposure, risk assessment under ISO 10993-1:2018 may require additional subchronic testing, and manufacturing under ISO 13485:2016 is required for most regulated markets. Sterilization of MABS devices is generally restricted to ethylene oxide processing according to ISO 11135:2014, followed by aeration to residual ethylene oxide and ethylene chlorohydrin limits given in ISO 10993-7:2008. Gamma irradiation at 25 kGy or higher tends to produce a measurable yellow shift in the methacrylate-styrene phase, and published data for TR558-CL at higher doses are limited. If irradiation is unavoidable, optical transmission and yellowness must be tracked according to ISO 13468-2:2021 and ASTM E313-20 on each production lot. Steam autoclave cycles at 121°C or 134°C are outside the operational boundary for MABS because heat deflection temperature under 1.8 MPa is below the autoclave temperature and the part will distort. Lipid exposure in stopcock applications can initiate crazing at stressed gate regions; this failure mode requires molded-in stress reduction rather than post-molding coating. Silicone-based mold release is generally avoided in these components because it migrates to the surface and impairs adhesion of printed markings or subsequent solvent bonding.
On the production floor, batch-to-batch variation in MABS melt viscosity is controlled by measuring melt volume-flow rate under ISO 1133-1:2022 and adjusting barrel temperature rather than injection speed. Hot-runner systems require full internal flushing between color changes, and residence time at melt temperature should not exceed 5–8 minutes to prevent yellowing. When molding parts with wall thickness below 1.0 mm, injection speed is raised to fill before freeze-off, but excessive speed beyond 350 mm/s may cause mold deposit formation on polished cavity surfaces due to decomposition products. Ejection from A-1 polished cavities must use air-assisted or poppet ejectors; mechanical ejector blades in visible areas produce stress whitening that is unacceptable under ISO 13485:2016 visual acceptance criteria.
Transparent covers and panels on hospital equipment and household appliances are repeatedly wiped with quaternary ammonium disinfectants, dilute sodium hypochlorite, and alcohol-based cleaners. In MABS, the methacrylate-acrylonitrile-styrene matrix provides better chemical resistance than standard ABS, but the polybutadiene-rich dispersed phase remains vulnerable to stress cracking when molded-in tensile stress exceeds a threshold. Evaluation is conducted with constant-strain exposure per ASTM D543-21, using bent-bar specimens with strain levels from 0.5% to 1.5% and 72-hour contact at room temperature. Quaternary ammonium solutions at concentrations above 0.5% active quaternary ammonium compound can cause microcrazing at gate bosses and weld lines, especially when the cleaning solution is allowed to pool in recesses. Alcohol-based hand sanitizers containing 60–70% ethanol or isopropanol are generally less aggressive to MABS than to transparent polycarbonate, but repeated exposure of stressed injection-molded clips with sharp internal corners may still produce craze networks. This distinction is critical for designing cleaning protocols: a wipe with immediate evaporation is less damaging than submersion or continuous liquid contact. Molded-in stress is minimized by using generous corner radii above 1.5 mm, uniform wall thickness transitions of 1:3 or less, and cooling time sufficient to reach ejection temperature below the heat deflection temperature.
For household appliance panels covered by IEC 60335-1:2020, the enclosure must resist mechanical impact and maintain creepage distances after cleaning exposure. Flame performance is not implicit; MABS can be compounded to meet UL 94 HB or sometimes UL 94 V-2, but the transparent grade itself must be tested on the final part thickness. Because transparent MABS contains no flame-retardant pigments, compliance with glow-wire tests in IEC 60695-2-11:2021 may require separate evaluation at the appliance level. The cleaning-agent compatibility of TR558-CL should be verified using a matrix of disinfectant types, strain levels, and exposure cycles before tool release; published data for this specific grade in concentrated quaternary ammonium contacts are limited. Stress relief annealing can be performed at 70°C for 2 hours in air, but annealing changes dimensions by up to 0.3% and must be validated against fixture tolerances. In applications where the housing is cleaned with high-level disinfectants at 45°C or above, MABS should not be specified without continuous-strain ESC testing, because the combination of elevated temperature and polar cleaning agents shifts crack initiation time significantly. This is an operational boundary rather than a universal incompatibility; the failure depends on stress state, not chemical class alone.
In cosmetics packaging, thick-wall transparent components such as jar bases, cap over-shells, and lipstick mechanisms are injection molded with A-1 diamond-polished cavities to reach high gloss without post-molding spraying. The MABS grade is processed at melt temperatures from 220–250°C and mold temperatures of 50–70°C; lower mold temperatures reduce cycle time but create flow lines that become visible in deep-draw cylindrical parts. Cosmetic formulations containing ester-based emollients, essential oils, and benzyl alcohol can act as stress cracking agents on clear polymers. Compatibility screening is performed under ISO 175:2010 with immersion conditions matched to the filling line temperature, typically 40–60°C for lipstick pouring. Typical qualification programs include visual inspection at 10× magnification and tensile property measurement per ISO 527-2:2012 after accelerated aging at 45°C for 14 days. The most aggressive contact media are not water-based emulsions but high-load ester and solvent-containing anhydrous systems; these formulations can migrate into the polymer surface and produce microcrazing over weeks.
Extrusion blow molding of MABS bottle bodies uses a parison temperature of 190–210°C and a blow mold temperature of 20–40°C; parison swell and melt strength are lower than those of PETG and require calibrated die gaps. Injection blow molding is preferred for small cosmetics bottles with threaded necks because it produces tighter neck tolerances and avoids pinch-off flash. In both processes, the material must be dried to below 0.02% moisture and processed with screw residence times below 6 minutes to avoid a visible yellow cast in thick preforms. Some fragrance and sunscreen active ingredients, particularly octocrylene, avobenzone, and high-load ester emollients, can migrate into the polymer surface and induce microcrazing over time. Regulatory compliance for the finished cosmetic package must be assessed under EC No 1223/2009, while substances intentionally released or migrating are addressed under REACH Regulation (EC) No 1907/2006. If the container is marketed as food-contact or multi-use with food contents, migration testing under EU Regulation (EU) No 10/2011 may additionally apply, and grade-specific compliance documentation must be obtained from the resin manufacturer. Decorating techniques include hot stamping, pad printing, and metallization; MABS has lower heat resistance than polycarbonate, so hot stamping die temperatures should be kept below 150°C and dwell time below 0.5 s to avoid surface crazing. UV-cured topcoats can improve scratch resistance, but solvents in some UV-curable inks penetrate the surface and cause microcrazing; therefore ink formulations must be screened under ASTM D543-21 as a chemical exposure test. Snap-fit designs in MABS caps use interference below 0.4 mm and assembly strain below 1.0% to prevent stress whitening during capping.
Light guide plates and display lenses for consumer electronics are molded in multi-cavity tools with wall thickness from 0.5 mm to 2.0 mm. The processing window for transparent MABS in these applications is narrow because melt temperature below 230°C increases viscosity and leads to short shots or flow hesitation at thin ribs, while melt temperature above 260°C accelerates methacrylate depolymerization and shifts color toward yellow. Barrel profiles are programmed with a reverse temperature profile to improve melt quality, and hot runners are operated with thermal gate tips of 0.8–1.5 mm diameter. Injection speed is set between 250–450 mm/s for thin-wall filling, with switchover by cavity pressure rather than screw position to prevent overpacking the optical edges. Mold temperature is held at 60–80°C for high polish replication; cooling time accounts for the low thermal conductivity of the acrylic phase and is typically 15–30 seconds for a 1.0 mm thick light guide. The resulting optical properties are measured using ISO 13468-2:2021 for total luminous transmittance and ASTM D1003-13 for haze. Yellowness index is tracked by ASTM E313-20, and lot-to-lot variation is more sensitive to residence time than to melt temperature in the lower portion of the range.
Electrical safety and material compliance for these components fall under IEC 62368-1:2023 for audio/video, information and communication technology equipment, and restricted substances are controlled under RoHS Directive 2011/65/EU Annex II. Unlike polycarbonate light guides, MABS offers lower heat deflection but generally better inherent light transmittance after thin-wall molding and fewer black speck defects when hot-runner shutoff and needle wear are controlled. The most serious process failure is cold-slug formation at the gate tip when valve-gate timing is too slow; this produces visible birefringence at the entrance of the light guide under polarized inspection. Molded-in stress can be characterized with a polariscope and should be reduced to levels that do not create visible retardation fringes. If the light guide is assembled with a laser-welded clear cover, the material must be tested for near-infrared transmission at the laser wavelength 808–980 nm, because additives and moisture can absorb in that band. Published laser-welding data for TR558-CL are limited; feasibility should be confirmed on the actual joint geometry before product approval. Melt flow length in thin sections depends on the melt volume-flow rate under ISO 1133-1:2022, which is measured for MABS at 220°C and 10 kg load. For a high-flow transparent grade, spiral-flow trials in 0.6 mm sections may exceed 120 mm, but hot-runner pressure drop and gate geometry change that value in production tools. Low-pressure filling below 60 MPa at the gate reduces shear-induced haze but prolongs cavity filling and can cause flow marks at the edges; high-pressure filling above 120 MPa at the gate transfers shear heating into the melt and may generate yellow streaks at the hot tip. Cavity pressure sensors are placed near the end of fill to switch from velocity to pressure control at 40–60 MPa, preventing overpacking that raises residual stress and optical retardation.
Transparent MABS is used in toy lenses, rattle shells, liquid-filled toy chambers, and decorative safety mirrors where impact performance and optical clarity are simultaneously required. Regulatory compliance is driven by EN 71-3:2019+A1:2021 migration limits for nineteen elements, ASTM F963-23 for the U.S. market, and CPSIA Section 108 for phthalate restrictions. The resin itself is not a source of phthalates, but color concentrates and lubricants used during compounding or molding must be reviewed against REACH Annex XVII Entry 51 and Entry 52. Because transparent grades are unpigmented, heavy-metal migration is usually below detection limits in molded articles, but final-part testing is required on every color mix and thickness combination. Sharp internal corners and gate vestiges act as stress concentrators; notched Izod impact is measured according to ISO 180:2023 and falls off significantly when radius drops below 0.2 mm. Therefore gate location must be moved to non-visible edges and ejector pins recessed below the surface.
| Reference | Focus | Typical endpoint |
|---|---|---|
| EN 71-3:2019+A1:2021 | Element migration from toy materials | 19 soluble elements in 0.07 mol/L HCl |
| ASTM F963-23 | Mechanical hazards and heavy metals | Small parts, sharp edges, eight heavy metals |
| CPSIA Section 108 | Phthalate content | DEHP, DBP, BBP, DIDP, DINP, DnOP limits |
| ISO 180:2023 | Notched Izod impact | kJ/m² at 23°C and −30°C where required |
Transparent toy lenses molded from MABS are subjected to repeated drop tests according to ISO 8124-1:2018 or EN 71-1:2014+A1:2018 depending on market, with impact surfaces chilled to 0°C and −10°C for cold-conditioned impact. Thickness below 1.5 mm in lenses reduces impact reserve; therefore the part must be gated away from the lens center and designed with a convex radius to distribute stress. Ultrasonic welding of liquid-filled toys introduces a sealing weld line that is inspected for leakage under 10 kPa air pressure for 5 seconds. Because MABS is hygroscopic, molded toy components stored in high-humidity environments before welding may contain residual moisture that foams at the weld joint; re-drying at 80°C for 4 hours before welding is recommended when ambient RH exceeds 60%.
In diagnostic device manufacturing, transparent MABS is processed into cuvettes, lateral flow cassette windows, reagent storage caps, and microfluidic cartridge bodies that require flat optical read areas. The molding process differs from packaging molding because the cavity must maintain flatness below 0.05 mm across the optical window and gate vestige height below 0.10 mm to avoid light scatter. Multi-cavity tools are run on electric machines with closed-loop injection velocity control and cavity pressure sensors; melt temperature is held at 230–250°C, mold temperature at 60–70°C, and holding pressure at 40–60 MPa. After molding, parts are conditioned at 23±2°C and 50±10% RH for at least 24 hours before optical testing. Light transmittance is measured across the filled reagent window with ISO 13468-2:2021, haze with ASTM D1003-13, and flatness with a non-contact profilometer. If capillary filling is required, plasma treatment or UV-ozone exposure is used to raise surface energy above 45 mN/m, verified by sessile drop contact angle measurement at 23°C.
Reagent compatibility is evaluated with soak tests per ISO 175:2010 using representative diagnostic buffers, detergents, alcohols, and dimethyl sulfoxide at concentrations found in the assay. MABS is generally resistant to dilute phosphate-buffered saline and common lysing detergents below 1%, but ketones, chlorinated hydrocarbons, and concentrated acids are incompatible. Alcohol-based reagent storage at above 30% ethanol can cause crazing in stressed sealing bosses, and exposure to 100% DMSO is not recommended without stress relief annealing and joint redesign. Bonding of microfluidic layers uses UV-curable adhesives or laser welding; solvent bonding with cyclohexanone or methylene chloride dissolves the methacrylate phase rapidly and creates channel deformation. If ultrasonic welding is used for cassette shells, energy directors with 0.3–0.5 mm apex height are positioned away from the optical window to prevent weld flash from entering the read path. Under ISO 13485:2016, the diagnostic cartridge manufacturer must validate that all mold-release agents and lubricants used in processing do not interfere with assay chemistry; silicone-based mold release is generally avoided because it migrates to the optical surface and reduces wettability.
Microfluidic cartridge bodies with channel depths of 0.1–0.4 mm demand polished core and cavity alignment within 0.01 mm to prevent cross-talk between adjacent channels. The polymer melt fills micro-features when mold temperature is kept at the upper end of the range, 70–80°C, and injection speed is sufficient to prevent premature solidification before feature replication. Vacuum venting of the microfeature cavity is required because trapped air in blind channels creates short shots and surface defects. After ejection, parts are annealed at 65°C for 2 hours to dimensionally stabilize the optical window before adhesive bonding. Laser welding through a transparent MABS cover to a black MABS base uses a diode laser wavelength of 980 nm and a clamp pressure of 0.2–0.5 MPa; the weld seam is placed at least 1.0 mm away from the optical read area to prevent heat distortion. The process is robust only when the natural absorption of the clear MABS is sufficient to transmit the laser wavelength without surface burn; published absorption data for TR558-CL are limited and require material-specific welding development. The regulatory context for European diagnostic devices is Regulation (EU) 2017/746, and the cartridge material is not cleared as a standalone material but must be supported by the manufacturer’s risk analysis, including leachables assessment and performance stability. For laboratory instruments outside the IVD directive, optical cuvette quality may be evaluated against ISO 15189:2012 laboratory quality system requirements. Published data specifically for TR558-CL in long-term wet reagent storage are limited; real-time aging must be performed with the actual assay matrix rather than accelerated substitution alone.
| Parameter | Method | Typical acceptance |
|---|---|---|
| Total luminous transmittance | ISO 13468-2:2021 | Report against material specification |
| Haze | ASTM D1003-13 | ≤ 2.0% at 2.0 mm for clear windows |
| Yellowness index | ASTM E313-20 | Lot-to-lot delta ≤ 0.5 |
| Optical window flatness | Non-contact profilometry | ≤ 0.05 mm across aperture |
| Contact angle after treatment | Sessile drop goniometer | ≥ 45 mN/m at 23°C |
Competitive PTS Trilac® MABS TR558-CL prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618005193850
Email: sales8@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
PTS Trilac® MABS TR558-CL is an amorphous methyl methacrylate-acrylonitrile-butadiene-styrene terpolymer supplied as pellets for injection moulding of transparent technical components. The methyl methacrylate comonomer shifts the refractive index of the styrene-acrylonitrile matrix closer to that of the dispersed butadiene-grafted rubber phase, reducing interfacial light scattering and producing total luminous transmittance values in the 88–90% range at 3 mm wall thickness when measured according to ASTM D1003-21. The TR558 designation identifies a medium-flow rheology package intended for thin-wall diagnostic, laboratory, and cosmetic housing applications; the CL suffix indicates a clarity-controlled formulation with rubber particle size distribution and gel count selected for reduced haze. The product is differentiated from general-purpose transparent ABS by lower haze, from polymethyl methacrylate by higher notched impact energy and lower surface hardness, and from bisphenol-A polycarbonate by lower processing temperature and different environmental stress-cracking response in alcohol-based disinfectant media.
Material is supplied in 25 kg moisture-barrier packaging. Incoming resin should be stored at 10–30 °C and opened only immediately before drying. Ambient humidity above 60% reduces the permissible open-container residence time for dried pellets to less than 30 min; moisture regain above 0.02 wt% is sufficient to produce surface splay in thin optical sections.
The comparative property set in Table 1 is based on typical values for natural, unfilled injection-moulded plaques. The TR558-CL value set positions the grade as a low-haze, medium-impact transparent resin with a Vicat softening temperature below that of polycarbonate and above that of standard transparent styrenics. Direct substitution without tooling modification is not implied because shrinkage, melt viscosity, and thermal conductivity differences require gate, venting, and cooling-channel adjustments.
| Property | TR558-CL typical | Unmodified MABS | PMMA | BPA-PC | Test method |
|---|---|---|---|---|---|
| Density | 1.08 g/cm³ | 1.08 g/cm³ | 1.19 g/cm³ | 1.20 g/cm³ | ISO 1183-1:2019 |
| Melt volume-flow rate 220 °C/10 kg | 20 cm³/10 min | 15 cm³/10 min | 8 cm³/10 min | 10 cm³/10 min | ISO 1133-1:2022 |
| Tensile yield stress | 46 MPa | 43 MPa | 72 MPa | 63 MPa | ISO 527-2:2012 |
| Flexural modulus | 2200 MPa | 2100 MPa | 3300 MPa | 2400 MPa | ISO 178:2019 |
| Charpy notched impact 23 °C | 10 kJ/m² | 8 kJ/m² | 2 kJ/m² | 60 kJ/m² | ISO 179-1:2023 |
| Vicat softening temperature B50 | 92 °C | 90 °C | 105 °C | 145 °C | ISO 306:2022 |
| Light transmittance 3 mm | 89% | 88% | 92% | 89% | ASTM D1003-21 |
| Haze 3 mm | 2.5% | 4.0% | 1.0% | 1.5% | ASTM D1003-21 |
The impact failure mechanism in MABS is rubber cavitation and multiple crazing. The clarity-controlled morphology limits rubber particle diameter to below the visible-light scattering threshold, but this constraint also bounds the upper impact response; a coarser particle size distribution would raise toughness at the expense of haze. TR558-CL is therefore specified for optical parts with moderate impact requirements, not for load-bearing structural components. Compared with an unmodified MABS grade of similar flow, the measurable optical difference is a haze reduction of approximately 1.5–2 percentage points at 3 mm thickness under ASTM D1003-21. Compared with PMMA, TR558-CL exhibits higher notched Charpy impact energy at 23 °C but lower pencil hardness; under ASTM D3363-22, pencil hardness for MABS typically falls in the F–H range, below PMMA at 2H–3H. Hard-coating remains necessary where repeated abrasive contact is expected. Compared with BPA-PC, TR558-CL processes at lower melt and mould temperatures, but its Vicat softening temperature is lower by more than 40 °C, limiting use in steam-sterilizable applications.
Processing of TR558-CL requires pre-drying in a desiccant dryer to a residual moisture content below 0.02 wt%. Supplier-recommended drying parameters are 80–85 °C for 3–4 h with a supply dew point of −30 °C or lower. Melt temperature during injection moulding is ordinarily set between 230 °C and 250 °C, and mould temperature between 40 °C and 70 °C. The lower mould-temperature boundary is controlled by surface replication and weld-line strength; the upper boundary is controlled by cycle-time extension and plate-out risk on polished cavity surfaces.
On a 25 mm reciprocating screw with an L/D ratio of 20:1 to 24:1 and compression ratio of 2.0:1, melt recovery below 8 s is attainable with back pressure in the range of 5–10 bar and screw rotation below 100 min⁻¹. Excessive shear heating above 250 °C accelerates butadiene-phase oxidation. Residence times above 5 min at melt temperature produce yellowing, silver streaks, and a drop in notched impact energy before optical clarity loss is observed. Hot-runner systems should be designed so that internal runner volume is below 30% of shot mass; higher ratios increase stagnation and gel formation in clear MABS grades.
Pre-drying is a boundary condition rather than a preparative step. MABS hydrolytic degradation of the nitrile and methacrylate groups releases ammonia and methanol at elevated temperature, causing splay and surface defects. Feed-throat temperature should be maintained at 40–60 °C, and insulated hoses are required when conveying dried pellets over distances greater than 10 m. If ambient relative humidity exceeds 60%, dried pellets should not remain in open hoppers for more than 30 min.
Flow haze in TR558-CL is usually shear-induced, not moisture-induced. When gate blush appears, reducing injection velocity through the gate below 300 mm/s and increasing melt temperature within the 230–250 °C window lowers the shear rate. Weld-line visibility cannot be eliminated solely by processing; it requires tooling changes such as sequential valve gating or overflow wells. Splay from moisture appears as fan-shaped silver streaks; splay from thermal degradation appears as brown striations near the gate.
In a diagnostic analyser housing with a 2.0 mm nominal wall and a 0.8 mm boss-to-wall ratio, packing pressure of 50–70 MPa and hold time of 5–8 s prevent sink marks while keeping cycle time below 35 s on a 100 t clamp machine. Lower packing pressure produces sink marks at rib intersections; higher packing pressure increases birefringence and gate stress. Lot-to-lot melt volume-flow rate variation for commercial MABS is typically within ±3 cm³/10 min; within this range, dimensional stability in a 2.0 mm wall diagnostic cover remains acceptable when the process is centered at 240 °C.
Repeated exposure to 70% isopropanol/water and quaternary ammonium compounds is a common acceptance criterion in diagnostic equipment housings. In MABS, the methyl methacrylate and acrylonitrile sequence distribution influences solvent uptake; lower equilibrium uptake of aqueous alcohol mixtures relative to bisphenol-A polycarbonate is documented in the literature, but the advantage is concentration-dependent. Testing according to ASTM D543-21 should be performed on injection-moulded plaques at the service strain because stress-crack initiation in MABS accelerates above 1.5% tensile strain in some alcohol solutions. Published data for TR558-CL in repeated disinfectant immersion is limited; production validation should include controlled strain jigs and wiper-contact protocols, not simple immersion coupons.
TR558-CL is not resistant to ketones, esters, or aromatic hydrocarbons. Methyl ethyl ketone, ethyl acetate, and toluene cause swelling, stress cracking, or partial dissolution. Strong oxidizing acids and continuous hot-water service above 60 °C are outside the recommended operational envelope.
The butadiene phase is unsaturated and undergoes photo-oxidation in continuous outdoor unpainted service. Yellowing and impact retention loss are expected under UV exposure unless a UV-stabilized grade is selected. Continuous service above 60 °C in air also reduces impact after ageing; design calculations should use aged data rather than as-moulded values for load-bearing snap-fits.
Certification status is resin-type specific and does not automatically transfer to finished devices. The supplier provides REACH and RoHS declarations for the resin as supplied; downstream converters are responsible for compliance of the final component with applicable device or packaging regulations.
| Requirement | Reference | Scope |
|---|---|---|
| REACH SVHC | Regulation (EC) No 1907/2006, Article 33 | Resin as supplied |
| RoHS | Directive 2011/65/EU, Annex II | Homogeneous material |
| Food-contact acrylonitrile copolymers | FDA 21 CFR 177.1030 | Grade-specific confirmation required |
| Biocompatibility | ISO 10993-5:2009 | Not conferred by resin grade alone |
| Flammability | UL 94 | Natural resin usually HB; colored or compounded variants require separate evaluation |
Regrind rates above 25 wt% degrade optical performance more than mechanical performance; recycled particulate contamination increases haze because scattering domains nucleate at polymer-polymer interfaces. The material is incompatible with amine-based additive packages because residual amines catalyze hydrolysis of the nitrile and methacrylate groups; lubricant and antistatic packages must be evaluated for clarity retention. Published data for repeated steam sterilization of TR558-CL with organic colorants is limited; autoclave validation on production-representative wall stock is required before specifying the grade for hydrogen peroxide plasma or steam-sterilizable device housings.