| HS Code | 387220 |
| Polymer Type | MABS (Methyl Methacrylate Acrylonitrile Butadiene Styrene) |
| Density | 1.08 g/cm³ |
| Melt Flow Rate | 20 g/10 min at 220°C/10 kg |
| Tensile Strength | 44 MPa |
| Elongation At Break | 30% |
| Flexural Modulus | 2000 MPa |
| Notched Izod Impact Strength | 14 kJ/m² at 23°C |
| Rockwell Hardness | R105 |
| Heat Deflection Temperature | 75°C at 1.82 MPa |
| Vicat Softening Temperature | 90°C |
| Mold Shrinkage | 0.4–0.6% |
| Light Transmittance | 85% |
| Haze | 3% |
As an accredited Chimei POLYLAC® MABS PA-758SR factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Chimei POLYLAC® MABS PA-758SR is packaged in 25 kg net paper sacks, palletized for industrial handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL: approximately 16,000–18,000 kg net of Chimei POLYLAC® MABS PA-758SR in 25 kg bags, palletized, subject to carrier weight limits. |
| Shipping | Chimei POLYLAC® MABS PA-758SR is shipped as non-hazardous polymer resin pellets, typically in 25 kg moisture-barrier bags on pallets. Transport in dry, covered conditions, avoiding direct sunlight, heat, and contamination. No UN number or dangerous goods classification applies; standard freight and customs documentation are required. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and ignition sources. Keep in original, tightly sealed containers/packaging to prevent contamination and moisture pickup. Avoid prolonged exposure to high temperatures and UV. Maintain good housekeeping to control dust; observe manufacturer’s SDS and local regulations. Use first-in, first-out stock rotation and keep containers closed when not in use. |
| Shelf Life | Chimei POLYLAC® MABS PA-758SR has a typical shelf life of 24 months when stored cool, dry, and sealed in original packaging. |
Deployment of Chimei POLYLAC® MABS PA-758SR in medical fluid management systems is driven by the combination of impact strength, optical clarity, and compatibility with solvent-based joining processes. Luer lock connectors and stopcocks manufactured to ISO 80369-7 require dimensional conformance across a 6% Luer taper with diametral tolerance of ±0.02 mm at the proximal orifice. This tolerance band translates directly to mold shrinkage control in the range of 0.4–0.6% along the flow direction (ISO 294-4), achieved through mold temperature maintained at 50–60°C and a barrel profile of 220°C at the feed zone, 235°C at the compression zone, and 245°C at the metering section. Production-scale injection molding machines with clamp forces of 80–120 tonnes achieve cycle times of 18–25 seconds on multi-cavity connector tools equipped with hot runner systems. Capillary rheometry (ISO 11443) at a melt temperature of 245°C demonstrates pseudoplastic flow behavior, with viscosity decreasing by approximately one order of magnitude between shear rates of 100 s⁻¹ and 10,000 s⁻¹, a response governed by the dispersed polybutadiene phase morphology.
Pre-drying is mandatory before plastication. Residual moisture exceeding 0.05 wt% measured by Karl Fischer titration per ISO 15512 hydrolyzes the acrylonitrile component during melting, producing surface splay and reducing molecular weight at the gate region. Desiccant dryers operating at 80°C for 3–4 hours with a dew point of -40°C or lower are specified on production lines. Drying hoppers must be insulated and purged to prevent moisture re-uptake where ambient relative humidity exceeds 60%.
Solvent bonding of MABS PA-758SR to rigid PVC tubing or to itself is performed with cyclohexanone or methyl ethyl ketone. The bonding mechanism relies on solvent diffusion into the amorphous polymer matrix, chain entanglement across the interface, and subsequent solvent evaporation. Capillary gap dimensions between mating surfaces must be controlled to 0.05–0.15 mm. Gaps below 0.05 mm produce insufficient solvent uptake and weak joints, while gaps above 0.15 mm risk solvent pooling and localized stress cracking. Post-bonding annealing at 55°C for 2 hours reduces residual solvent concentration below 500 ppm, as measured by headspace gas chromatography.
Sterilization compatibility introduces specific design constraints. Gamma irradiation at 25 kGy produces a measurable yellow shift in MABS. The yellowness index (ASTM E313) typically increases by 2–5 units, depending on antioxidant package loading and oxygen exposure during irradiation. For applications requiring post-sterilization color stability, ethylene oxide sterilization at 55°C and 40–60% relative humidity for 2–4 hours is preferred, followed by aeration at 50°C for 12–24 hours to reduce residual ethylene oxide below the 4 mg/day limit specified in ISO 10993-7. Biocompatibility screening follows ISO 10993-5 for cytotoxicity and ISO 10993-10 for sensitization and irritation, with extractables testing conducted under exaggerated conditions per ISO 10993-12.
| Sterilization modality | Process parameters | Material response | Design boundary |
|---|---|---|---|
| Gamma (Co-60 source) | 25 kGy, ambient temperature | ΔYI of +2 to +5 units (ASTM E313) | Acceptable for single-use; color shift must be pre-specified |
| Ethylene oxide | 55°C, 40–60% RH, 2–4 hours | ΔYI below +1 unit (ASTM E313) | Preferred; 12–24 hours aeration at 50°C |
| Electron beam | 25 kGy, 10 MeV | ΔYI of +2 to +4 units (ASTM E313) | Wall thickness capped at 8 mm to limit thermal load |
| Steam autoclave | 121°C, 15 psi, 15 min | Dimensional distortion | Contraindicated; exceeds Vicat softening range of 95–100°C (ISO 306/B50) |
Transparent wearable electronics housings produced from MABS PA-758SR require a barrel temperature profile of 220°C at the feed zone, 235°C at the compression zone, and 245°C at the metering section. A mold temperature of 50–60°C is maintained to balance flow length against optical clarity. Mold temperatures below 40°C produce visible flow marks and weld-line haze on cosmetic surfaces, while temperatures above 65°C increase cycle time without measurable improvement in light transmission. Hot runner systems with full-round channels of 6 mm diameter are specified over cold runners for multi-cavity tools, as the melt at 245°C permits balanced fill without excessive shear heating. Screw configurations with L/D ratios of 20:1 to 24:1 and compression ratios of 2.5:1 are documented on production lines. Light transmission through a 2 mm plaque is approximately 88–90% at 550 nm (ASTM D1003), with haze below 1.5%. For device enclosures where stylus or fingernail contact is anticipated, scratch evaluation per ASTM D7027-13 indicates that abrasion whitening remains confined to the immediate scoring path without crack branching at loads typically encountered in consumer handling. Weld lines formed at mold insert boundaries or multi-gate intersections are visible under polarized light inspection and must be positioned away from cosmetic surfaces or eliminated through valve-gated hot runner sequencing.
Injection molding of thick-walled jar bodies and multi-start thread closures from MABS PA-758SR involves wall thicknesses ranging from 3 mm to 12 mm. The low thermal conductivity of approximately 0.17 W/m·K means that core sections remain above the glass transition temperature long after surface skin formation. Differential shrinkage between the frozen surface layer and the semi-molten core produces internal tensile stresses that increase environmental stress crack susceptibility when the component contacts aggressive media. The environmental stress cracking behavior of MABS in cosmetic formulations follows a critical strain model. Below a threshold strain of approximately 0.4% measured via constant-strain jig testing, crack propagation is negligible. Above this threshold, crack growth accelerates sharply. Post-molding annealing at 60°C for 1 hour relieves residual stresses. Comparative evaluations under ISO 22088-3 (bent strip method) document an upward shift in the critical strain threshold of 25–40% for annealed specimens relative to as-molded controls. Cosmetic formulations containing propylene glycol, ethanol, isopropyl myristate, or nonionic surfactants are the primary stress-cracking media encountered in this application sector.
Injection compression molding is preferred for thick sections exceeding 6 mm. The process maintains a controlled cavity pressure profile during packing, reducing molecular orientation in the core and minimizing birefringence, which would otherwise be visible as iridescent patterns under polarized light inspection. The compression stroke of 2–4 mm is applied after 85–95% volumetric fill, with cavity pressure held at 60–80 MPa during solidification. Production records from injection compression molding lines with 250–350 tonnes of clamping force indicate a 40–60% reduction in internal stress birefringence relative to conventional injection molding at equivalent wall thickness. Published data for this specific configuration is limited. The ranges cited derive from MABS material behavior documented in polymer processing literature and are not direct measurements from this grade.
Regulatory compliance for cosmetic contact includes EC No. 1223/2009 (Cosmetics Regulation) and GB 4806.7-2016 where applicable for food-contact-adjacent packaging. Extractable testing using 95% ethanol as a simulant at 40°C for 10 days per EN 1186-1 methodology is used to qualify the material for closure applications. Total migration limits are specified at 10 mg/dm² per EU Regulation 10/2011 for food-contact-adjacent packaging. Avoid combination with amine-based colorants or additives, as residual amines can accelerate environmental stress cracking in the presence of ester-containing cosmetic ingredients.
Microfluidic cassette manufacture using MABS PA-758SR involves joining a precision-molded channel layer to a transparent cover film. Ultrasonic welding at 20 kHz with amplitudes of 20–40 μm generates localized frictional heating at energy directors, but the associated vibration can displace pre-loaded reagents or damage microchannel geometry with feature sizes in the 50–200 μm range. Laser transmission welding using diode lasers at 808 nm or 980 nm eliminates mechanical vibration, relying instead on a transparent upper layer and a laser-absorbing lower layer typically compounded with 0.1–0.3 wt% carbon black or near-infrared-absorbing additives. The weld interface temperature during laser transmission welding is controlled within a processing window bounded by the Vicat softening temperature of approximately 95–100°C (ISO 306/B50) and the onset of thermal degradation near 250°C. Effective joining is achieved at laser powers of 15–30 W, scan speeds of 5–20 mm/s, and clamping pressures of 0.3–0.8 MPa on production-scale workstations equipped with pyrometric closed-loop temperature control. Joint collapse of 0.1–0.3 mm is monitored as an in-process quality indicator. Weld seam width is controlled to 0.5–1.5 mm.
Optical requirements for diagnostic cassettes include high transmission in the visible range for fluorescent signal readout. MABS PA-758SR exhibits light transmission of approximately 88–90% through a 2 mm plaque at 550 nm (ASTM D1003), with haze below 1.5%. Weld seams introduced during laser transmission welding produce localized haze increases of 0.5–1.0% over the seam width. This zone must be positioned outside the optical readout path specified by the assay development team. For nucleic acid amplification devices operating with heated reaction zones at 65°C during annealing and 95°C during denaturation, the thermal profile of the material dictates that heated platens be isolated from load-bearing regions. Molded channel flatness is controlled to within 0.05 mm per 25 mm of channel length to ensure uniform laser clamping pressure across the weld interface.
Vacuum cleaner dust container bodies molded from MABS PA-758SR on standard reciprocating screw injection machines require no specialized screw metallurgy or surface treatments. The Izod notched impact strength exceeding 10 kJ/m² (ISO 180/A) at 2 mm wall thickness withstands routine end-use impact loading without crack propagation beyond the immediate impact site. Post-mold coating is not applied.
Edge-lit LED light guide plates in appliance displays and automotive interior ambient lighting utilize MABS PA-758SR for the combination of optical transmission and dimensional consistency. Laser-etched micro-prismatic dot patterns on the rear surface extract light perpendicular to the plate plane. The uniformity of this extraction depends on maintaining dot depth tolerance of ±5 μm. Fiber laser marking at 1064 nm produces adequate contrast without charring, provided pulse energy is capped below 0.5 mJ per pulse to avoid localized thermal degradation of the butadiene phase. Warpage of thin light guide plate sections between 1.5 mm and 3.0 mm after molding is controlled by maintaining uniform mold temperatures within ±3°C across the cavity surface and incorporating a flatness specification of 0.3 mm per 100 mm length.
Long-term optical stability under LED radiation is a design consideration. Accelerated aging at 80°C with 450–470 nm blue LED exposure at 50 mW/cm² for 1000 hours produces yellowness index shifts below 1.5 units in MABS containing hindered amine light stabilizers. Published data for this specific configuration is limited. Qualification testing per IEC 62722-2-1 for luminaire performance is recommended for commercial launch. For light guide plate dimensions exceeding 200 mm in length, mold flow analysis using Cross-WLF viscosity coefficients is performed prior to tool cutting to predict fill pressure, gate freeze time, and shrink-induced warpage. The butadiene phase in MABS contributes slight forward scattering that must be accounted for in edge emission uniformity calculations. Dot pattern density is adjusted at the mold design stage to compensate for this scattering contribution. Avoid exposure to ketone-based cleaning solvents during assembly, as residual ketones on the plate surface produce localized crazing under thermal cycling between -20°C and 60°C.
Competitive Chimei POLYLAC® MABS PA-758SR 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!
Chimei POLYLAC® MABS PA-758SR is a transparent methyl methacrylate–acrylonitrile–butadiene–styrene copolymer supplied by Chimei Corporation. The grade belongs to the POLYLAC MABS segment, in which a fraction of styrene in the styrene-acrylonitrile matrix is replaced with methyl methacrylate to narrow the refractive-index mismatch between the continuous phase and the grafted polybutadiene rubber phase. The PA-758SR designation identifies a flow-modified variant within the PA-758 transparent MABS series. The material is specified for injection molding of thin-wall transparent parts requiring a balance of melt flow, impact resistance, and visible-light clarity. Its supplied pellet form is amorphous; therefore, thermal softening occurs gradually and a defined crystalline melting point is absent. Lot-specific certificates of analysis should govern production release because generic datasheet values are representative rather than release limits. Published data for the precise SR-modifier chemistry or its numerical delta relative to PA-758R is limited; the suffix should not be interpreted as an independent chemical identity without confirmation from Chimei technical documentation.
Incoming-lot qualification is recommended where optical specifications are tight. Batch-to-batch variation in rubber particle size distribution can shift haze by 0.5–1.0 % even when the refractive-index mismatch remains unchanged. For cosmetic packaging or diagnostic windows with a haze requirement below 3 %, a standard step plaque should be molded and measured under ASTM D1003. Pellet transparency alone is not a reliable release criterion because molded-surface orientation, packing pressure, and thermal history contribute to final optical performance. The resin is amorphous and should be purged from the barrel and hot-runner system when changing from opaque ABS or high-temperature engineering polymers. Residual contamination from polycarbonate or flame-retardant grades can generate visible specks and reduce transmittance in transparent sections.
Opaque ABS grades scatter visible light because the polybutadiene domains in the graft copolymer have a refractive index different from that of the styrene-acrylonitrile matrix. In MABS, the matrix refractive index is shifted toward that of the rubber by incorporation of methyl methacrylate. When the domain-matrix refractive-index difference falls below approximately 0.005, forward scattering is reduced sufficiently for the molded part to appear transparent. Class-typical total luminous transmittance for transparent MABS is 88–90 % at 3.2 mm thickness under ASTM D1003, with haze in the range of 2–4 %. General-purpose opaque ABS does not meet these optical values, while PMMA commonly transmits 92 % or more under the same standard. The tradeoff is impact resistance: class-typical notched Izod values for transparent MABS are generally above 10 kJ/m² under ISO 180/A, whereas general-purpose PMMA is frequently below 5 kJ/m².
Against polycarbonate, PA-758SR offers lower melt viscosity and lower density, but its upper service temperature is lower. Class-typical heat-deflection temperature for transparent MABS at 1.82 MPa is 84–89 °C, while polycarbonate can exceed 125 °C. The transparent MABS grade is therefore selected where thin-wall filling, short cycle time, or reduced clamp force is limiting, and where sustained mechanical stress above about 60–70 °C is not expected. Within the PA-758 series, the SR suffix indicates a flow modification, but the exact concentration and molecular-weight effect are not fully disclosed in published literature. Comparative screening against PA-758R should be conducted with the same mold and processing conditions because flow length and impact retention may diverge only under high-shear or low-temperature molding.
Table 1 consolidates class-typical property ranges for the PA-758 transparent MABS series. The values are engineering reference data, not lot release criteria. Melt-flow and impact balance can vary with the SR modifier package, regrind content, and moisture state. Production trials should use the certificate of analysis for the specific lot and should not rely on property tables for final part approval.
| Property | Test method and condition | Typical range |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 / ASTM D1238, 220 °C, 10 kg | 22–30 g/10 min |
| Density | ISO 1183-1:2019 / ASTM D792 | 1.08–1.10 g/cm³ |
| Tensile stress at yield | ISO 527-2:2012, 50 mm/min / ASTM D638-14 | 38–44 MPa |
| Tensile elongation at break | ISO 527-2:2012 / ASTM D638-14 | 12–20 % |
| Flexural modulus | ISO 178:2019 / ASTM D790-17 | 2,000–2,300 MPa |
| Notched Izod impact, 23 °C | ISO 180/A:2019 / ASTM D256-10, 3.2 mm | 10–16 kJ/m² |
| Rockwell hardness | ASTM D785, R scale | 110–115 |
| Vicat softening temperature, B50 | ISO 306:2022 / ASTM D1525, 50 N | 98–104 °C |
| Heat-deflection temperature, 1.82 MPa | ISO 75-2:2020 / ASTM D648-18 | 84–89 °C |
| Luminous transmittance, 3.2 mm | ASTM D1003-13 | 88–90 % |
| Haze, 3.2 mm | ASTM D1003-13 | 2–4 % |
| Molding shrinkage | ISO 294-4:2018 | 0.4–0.6 % |
Rheologically, the PA-758 series is pseudoplastic. Melt-flow rate alone under-predicts injection pressure requirements because the material exhibits shear-thinning behavior at gate shear rates. Processing on a conventional single-screw injection molding machine with an L/D of 20:1–24:1 and a compression ratio of 2.5:1 is generally sufficient for homogenization. A shut-off nozzle is required to prevent drool when melt temperatures exceed 230 °C. Hot-runner systems should be fully divided and free of dead spots; stagnant resin degrades to yellow-brown oxidation products that reduce transmittance and increase haze. Gate design should avoid excessive shear heating because high gate-shear rates can locally reduce molecular weight and produce visible flow lines in transparent parts.
Moisture absorption in MABS is lower than in polycarbonate or PMMA, but uncontrolled moisture above approximately 0.05 % by weight is a consistent source of splay, vacuoles, and loss of transparency. In plants where relative humidity exceeds 60 %, pre-drying is not optional. The resin should be dried in a desiccant dryer at 80 °C for 3–4 h, with a drying-air dew point of -30 °C or lower. Hopper residence time should be kept below 4 h unless the hopper is insulated and dry-air-purged. Failure to maintain the dry-air dew point below -20 °C can produce intermittent splay that appears only after several hours of molding because pellet-core moisture diffuses slowly during melting.
Melt temperature should be maintained between 200 °C and 240 °C, with a short-residence maximum of 250 °C. Mold temperature should be set between 40 °C and 70 °C. Lower mold temperatures reduce cycle time but increase orientation-induced birefringence and may produce visible flow lines. Higher mold temperatures above 70 °C improve surface smoothness and optical uniformity but increase cooling time and sink-mark risk. Injection speed should be moderate to high, with short hold time. Excessive hold pressure can create gate stress and microcracks that appear later after chemical exposure. Chemical incompatibility is pronounced with ketones, esters, aromatic hydrocarbons, and some amine-containing additive concentrates. These chemicals soften or craze the MABS surface. When molding after PVC compounds, the barrel and hot-runner should be purged thoroughly because residual vinyl chloride-derived materials can contaminate the melt and produce black specks.
Thin-wall cosmetic packaging such as lipstick cases, compact housings, and personal-care closures is a common application for PA-758SR because the material tolerates high-speed multi-cavity filling while retaining visible clarity. Stress-crack resistance should be evaluated under ASTM D543 or ISO 4599 using the relevant formulation; published data for this specific grade in contact with ethanol-based systems or micellar water is limited. Medical device enclosures and diagnostic housings can be considered only after device-level evaluation under ISO 10993-1:2018, because raw-material compliance alone does not establish biocompatibility. Household transparent parts and toys require national-market certification, such as EN 71-3 migration testing for elements, and the processor must verify that colorants and additives do not raise heavy-metal content above the applicable limit.
Food-contact and medical uses require grade-specific regulatory confirmation, not merely polymer-family compliance. The following matrix lists the standards most frequently cited in supplier documentation for the POLYLAC MABS series. A grade-specific letter from Chimei should be obtained before PA-758SR is used in food-contact or medical devices.
| Regulatory/standard | Scope | Typical condition or citation |
|---|---|---|
| 21 CFR 177.1020 | Acrylonitrile-butadiene-styrene copolymers for food-contact use | Residual acrylonitrile and styrene monomer limits; extractives limits apply |
| REACH Regulation (EC) No 1907/2006 | Registration, SVHC communication, restrictions in Annex XVII | Article 33 notification may apply if SVHC content exceeds 0.1 % w/w |
| RoHS Directive 2011/65/EU as amended by (EU) 2015/863 | Electrical and electronic equipment | Lead, mercury, cadmium, hexavalent chromium, PBB, PBDE, and four phthalates below threshold limits |
| ISO 10993-1:2018 | Biological evaluation of medical devices | Device-level testing required; raw-material grade alone is not sufficient |
| USP Class VI | Plastics in contact with parenteral or tissue preparations | Confirm supplier certificate for the specific lot; not automatic for all MABS grades |
| ASTM D1003-13 | Haze and luminous transmittance | Optical QC for transparent molded specimens |
For all regulated applications, the converter must maintain incoming resin certificates, process contact declarations, and when necessary carry out extraction or migration testing on the finished article. No material-family statement replaces lot-specific written certification from the supplier for the intended use and regulatory market.