| HS Code | 253825 |
| Material Type | MABS (methyl methacrylate-acrylonitrile-butadiene-styrene) |
| Filler Content | Unfilled |
| Density | 1.08 g/cm³ |
| Melt Volume Flow Rate | 11 cm³/10 min |
| Tensile Modulus | 2100 MPa |
| Tensile Strength At Yield | 45 MPa |
| Elongation At Break | 20% |
| Charpy Notched Impact Strength | 10 kJ/m² |
| Vicat Softening Temperature | 95 °C |
| Heat Deflection Temperature | 80 °C |
| Molding Shrinkage | 0.4–0.7% |
| Water Absorption | 0.2% |
| Processing Method | Injection molding |
| Color | Transparent/natural |
| Light Transmission | 88% |
| Haze | 2% |
As an accredited Polykemi AB POLYabs MABS T00 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polykemi AB POLYabs MABS T00 is supplied in 25 kg moisture-resistant polyethylene bags on pallets. |
| Container Loading (20′ FCL) | Polykemi AB POLYabs MABS T00 is securely loaded into a 20′ FCL container for dry, compliant bulk chemical transport. |
| Shipping | Shipping description: Polykemi AB POLYabs MABS T00 is a non-hazardous thermoplastic molding compound in granule form, not regulated for transport under ADR/IMDG/IATA. Ship in original sealed packaging at ambient temperature; keep dry, protect from moisture, heat, direct sunlight, open flames, and static. No special handling required. |
| Storage | Store Polykemi AB POLYabs MABS T00 in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and moisture. Keep in original, tightly closed containers/packaging to prevent contamination and dust accumulation. Avoid prolonged storage in high humidity or elevated temperatures. Follow local regulations and the manufacturer’s safety data sheet for safe handling and storage. |
| Shelf Life | Polykemi AB POLYabs MABS T00 typically has a 12-month shelf life when stored dry, cool, and in original sealed packaging. |
| Application sector | Standard or test method | Critical parameter / limit |
|---|---|---|
| Medical fluid management | ISO 10993-1:2018, ISO 10993-5:2009, USP <88> Class VI, ISO 10993-7:2008 | Regrind 0 wt% in fluid path; residual EtO below device-specific TCL |
| Cosmetic packaging | Regulation (EC) No 1223/2009, REACH Annex XVII, ISO 175:2010 | Regrind ≤ 20 wt% outer shell only; immersion testing 72 h at 23 °C and 40 °C |
| Optical covers and light pipes | IEC 62368-1:2018, Directive 2011/65/EU, UL 94 HB, ASTM D1003 | Luminous transmittance ≥ 88 % at 3 mm; hardcoat 5–15 µm |
| Diagnostic consumables | ISO 13485:2016, Regulation (EU) 2017/746, ISO 10993-1:2018 | Internal release ≤ 0.05 wt%; cavity pressure 35–50 MPa |
| Water-contact appliance reservoirs | IEC 60335-1:2020, Regulation (EU) No 10/2011, NSF/ANSI 51 | Overall migration ≤ 10 mg/dm²; regrind 0 wt% water-contact liner |
| Automotive interior backlit controls | FMVSS 302, ISO 3795, GADSL, Directive 2011/65/EU | T00 skin 0.8–2.0 mm; substrate surface ≥ 110 °C before overmould |
Competitive Polykemi AB POLYabs MABS T00 prices that fit your budget—flexible terms and customized quotes for every order.
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Polykemi AB POLYabs MABS T00 is a methyl methacrylate–acrylonitrile–butadiene–styrene terpolymer supplied as a transparent injection-moulding grade. The material is selected for moulded components where optical clarity, intermediate heat resistance, and higher impact toughness than standard acrylonitrile-butadiene-styrene are required. Typical conversion uses single-screw injection-moulding machines with screw L/D ratios between 20:1 and 25:1. Published lot-specific data for POLYabs MABS T00 in some specialised end-use tests remains limited, and the following values are class-level data from current supplier technical documentation and should be verified against the batch certificate.
Manufacturer-recommended melt temperature for POLYabs MABS T00 lies between 230 °C and 260 °C. Below 230 °C, homogenization of the acrylic-modified SAN phase and the butadiene rubber phase is incomplete; this may appear as visible gel particles at the gate when hot-runner drops are run below 235 °C. Above 260 °C, thermo-oxidative degradation of butadiene accelerates, and the CIELAB b* shift can exceed 1.0 unit after 20 min residence at 265 °C. Screw recovery should maintain shot capacity at 50–70 % of barrel volume. Lower utilization extends residence time; higher utilization reduces plasticating homogeneity. Back pressure between 5 bar and 15 bar hydraulic balances dispersion and shear heating. Hold pressure must not extend past gate freeze, because stress accumulation at the sprue can produce a visible white streak under transmitted light.
At melt temperatures above 260 °C, the butadiene phase undergoes autoxidation and crosslinking that proceed more rapidly than in styrene-acrylonitrile. Conjugated oxidation products increase yellowness index at an approximate rate of 0.05 YI units/min in a nitrogen-purged melt and faster in air-exposed material. Prolonged hold time in a hot runner above 250 °C can generate brown streaks at the gate even when the main melt stream remains within specification. After an interruption longer than 10 min, the barrel should be purged with a high-viscosity styrenic or acrylic purge compound until melt colour and clarity stabilise. When colour-compounded lots are processed, the masterbatch carrier must be verified for thermal stability above 240 °C; incompatible carrier resins can form black specks and deposit degradation products on the check ring.
Pre-drying at 80 °C for 3–4 h in a desiccant dryer with a dew point below −30 °C is required for optical surfaces. Residual moisture above 0.03 wt% causes splay, silver streaking, and localized gloss reduction at the end of flow. On a 12-cavity lens-housing tool, intermittent splay was traced to condensation at the dryer air line; a dew-point transmitter at the hopper throat read −20 °C until the flexible hose was insulated. If regrind is introduced at 20 wt%, drying time should be extended to 4–6 h unless the regrind is from sealed edge trim generated the same day. Vacuum dryers with inline moisture monitoring reduce oxidative exposure for medical and optical lots. Ambient-air hopper dryers are not sufficient when surface haze is controlled to 2–3 %.
| Parameter | Recommended value | Unit |
|---|---|---|
| Pre-drying temperature | 80 | °C |
| Pre-drying time | 3–4 | h |
| Residual moisture | <0.03 | wt% |
| Melt temperature | 230–260 | °C |
| Mould temperature | 40–70 | °C |
| Back pressure | 5–15 | bar |
| Injection speed | medium–fast | — |
| Screw L/D ratio | 20:1–25:1 | — |
Table 2 presents typical values obtained under ISO test geometry. These values are not design allowables and must be confirmed with lot-specific certificates for the exact colour and additive package.
| Property | Test method | Typical value | Unit |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.08 | g/cm³ |
| Melt volume-flow rate | ISO 1133-1:2022 at 220 °C/10 kg | 14 | cm³/10 min |
| Tensile modulus | ISO 527-1/-2 | 1900 | MPa |
| Tensile yield stress | ISO 527-1/-2 | 45 | MPa |
| Nominal strain at break | ISO 527-1/-2 | 20 | % |
| Charpy notched impact strength | ISO 179-1/1eA at 23 °C | 15 | kJ/m² |
| Vicat softening temperature | ISO 306/B50 | 96 | °C |
| Heat deflection temperature | ISO 75-2/Af at 1.8 MPa | 78 | °C |
| Light transmission | ISO 13468-1/A | 88 | % |
| Haze | ISO 14782 | 2.5 | % |
Optical parts moulded from T00 require polished tool steel with surface finish at least VDI 12 or equivalent diamond-polished roughness. Weld lines remain the dominant brightness defect in transparent MABS. In a two-gate cover with 2 mm wall thickness, raising mould temperature from 40 °C to 65 °C reduced weld-line haze from 6 % to 3 % when measured through a 1 mm aperture with a haze meter. The effect is attributed to delayed freeze-off and better interpenetration of melt fronts. Mould surface contamination or release-agent build-up can increase measured haze independent of polymer quality; tool maintenance cycles should therefore be defined by observed haze drift rather than shot count alone.
The primary differentiation against standard transparent ABS is the methacrylate comonomer content. This reduces refractive index mismatch between the matrix and the butadiene rubber phase, lowering haze while retaining notched impact strength in the 12–18 kJ/m² range. By contrast, PMMA of comparable optical quality typically shows notched Charpy values of 2–4 kJ/m², so T00 is chosen when snap-fits, clips, or drop-tested housings are specified. Against polycarbonate, T00 has lower Vicat softening and lower as-moulded impact; however, MABS flows at 230–260 °C versus polycarbonate melt temperatures above 300 °C, and it can fill thin walls without the same drying and screw-wear demands. Surface hardness is lower than PMMA. Resistance to boiling water and autoclave cycles is lower than polycarbonate.
In thin-wall control-panel and electronic housing moulds, wall thickness reductions from 2.5 mm to 1.8 mm require melt temperature to be raised from 235 °C to 255 °C and injection velocity increased to keep fill time below 1.5 s. The melt volume-flow rate of 14 cm³/10 min at 220 °C/10 kg supports filling of ribs with width-to-thickness ratio up to 0.8, but not micro-moulded features below 0.5 mm. Spiral-flow data for this exact material in the published datasheet is limited; tool trials should confirm flow length under the specific injection pressure and wall thickness. Mould temperature should be held at 60–70 °C for transparent parts because cold mould surfaces freeze weld lines and reduce impact at the knit line by more than 30 % compared to the bulk material.
Shrinkage of MABS T00 class material is typically 0.4–0.7 % in the flow direction and 0.5–0.8 % transverse, depending on wall thickness and mould temperature. Post-mould warpage in large flat lenses arises from differential shrinkage between gate and end-of-fill regions. A gate-to-end temperature gradient above 15 K can produce residual stress measurable as a path difference of 20–30 nm in polarized light. To reduce birefringence, mould temperature should be made uniform within 5 K across the cavity, and hold pressure should follow a two-stage profile with a short first stage at 50–60 MPa and a longer second stage at 30–40 MPa. Annealing at 70 °C for 2 h after moulding reduces residual stress but may increase haze slightly if the part is exposed to humid air during cooling.
Chemical compatibility data for MABS class materials shows sensitivity to aromatic hydrocarbons, ketones, esters, and chlorinated solvents. Contact with isopropanol, ethanol, or hand sanitizer can cause environmental stress cracking under moulded-in stress; transparent covers should therefore be annealed at 70 °C for 2 h before field deployment if repeated disinfectant exposure is anticipated. Steam autoclaving at 121 °C is outside the continuous use limit and typically produces warpage and surface haze. The product should not be compounded with certain amine-based colorants or flame retardants that accelerate thermo-oxidative degradation of the butadiene segment. Regulatory compliance under REACH and RoHS 2011/65/EU Annex II must be confirmed from the supplier’s lot certificate for the exact colour and additive package. Food-contact status under FDA 21 CFR 175.300 is not automatically assigned to pigmented or compounded variants; verification against the specific formulation is required.
On a 1200 kN injection-moulding machine using a 35 mm screw with 22:1 L/D, batch-to-batch melt viscosity variation for T00 can be held below 5 % when melt temperature is controlled at 245 °C and cushion is kept between 3 mm and 5 mm. Clamp force calculations for transparent medical housings often assume cavity pressure of 35–45 MPa; insufficient clamp generates parting-line flash, which appears as a bright edge under transmitted light. Screw recovery time should be 0.8–1.2× the injection time to avoid starved feeding. In multi-cavity tools with geometrically balanced runners, natural T00 can produce cavity-to-cavity weight variation of ±0.3 % when cavity pressure sensors are used for process control. Polished tool steel of VDI 12 or finer is required for low-haze surfaces; rough tool surfaces scatter light and add to measured haze beyond the polymer intrinsic value.