| HS Code | 522474 |
| Productname | Diapolyacrylate Shinko-Lac® MABS U400B |
| Polymertype | MABS (methacrylate-acrylonitrile-butadiene-styrene) copolymer |
| Appearance | Pellets |
| Color | Natural/transparent (typical) |
| Density | 1.04–1.08 g/cm³ |
| Meltflowrate | 5–10 g/10 min (220°C/10 kg) |
| Tensilestrength | 40–50 MPa |
| Elongationatbreak | 30–60% |
| Flexuralmodulus | 1.8–2.3 GPa |
| Notchedizodimpactstrength | 80–150 J/m |
| Charpyimpactstrength | 8–15 kJ/m² |
| Heatdeflectiontemperature | 70–80°C at 1.82 MPa |
| Vicatsofteningtemperature | 90–100°C |
| Rockwellhardness | R95–R105 |
| Waterabsorption | 0.1–0.3% after 24 h |
| Moldingshrinkage | 0.4–0.7% |
| Processingmethod | Injection molding |
| Transparency | Transparent/translucent |
| Chemicalresistance | Good resistance to dilute acids, alkalis, alcohols, and aliphatic hydrocarbons; limited resistance to aromatic and chlorinated solvents |
| Electricalinsulation | Good |
| Uvstability | Moderate; UV stabilization may be required for outdoor use |
As an accredited Diapolyacrylate Shinko-Lac® MABS U400B factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Diapolyacrylate Shinko-Lac® MABS U400B is packaged in 20 kg net polyethylene-lined fiber drums for safe handling and storage. |
| Container Loading (20′ FCL) | Diapolyacrylate Shinko-Lac® MABS U400B, palletized and secured in a 20-foot FCL container, kept dry and handled per transport regulations. |
| Shipping | Diapolyacrylate Shinko-Lac® MABS U400B is shipped in sealed, properly labeled containers in accordance with applicable transport regulations. Transport and store in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Handle with care to prevent leakage or container damage. |
| Storage | Store Diapolyacrylate Shinko-Lac® MABS U400B in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers tightly closed, properly labeled, upright, and protected from physical damage. Use original or compatible containers, segregate from acids, bases, and reactive chemicals, and avoid temperature extremes. Follow the manufacturer’s SDS and local storage regulations. |
| Shelf Life | Typically 24 months from manufacture when stored unopened in a cool, dry, well-ventilated area, away from sunlight. |
Shinko-Lac® MABS U400B finds use in transparent in vitro diagnostic analyzer panels, sample tray windows and non-patient-contact microfluidic manifold retainers, where the part must survive repeated disinfection wiping without exhibiting stress crazing at gate bosses or molded-in insert corners. Material qualification for this sector includes IEC 61010-1:2010/AMD1:2016 for laboratory electrical equipment, ISO 10993-1:2018 for biocompatibility evaluation of limited-contact components, and ISO 10993-5:2009 using the MEM elution method for cytotoxicity screening. The resin is processed as the continuous phase at 100 parts by weight; color masterbatch is metered at 1.0–3.0 wt%, and external silicone lubricant is held below 0.05 wt% because higher concentrations migrate to the melt front and produce flow-line haze in polished window sections. Desiccant drying at 80°C for 3–4 h with a supply-air dew point of −30°C or lower reduces retained moisture below 0.05 wt%; insufficient drying produces splay on the cavity surface and reduces melt viscosity consistency required for manifold channel wall replication. Injection molding on a 120–180-ton clamp force hydraulic machine with a 20:1 L/D general-purpose screw and reverse-profile check ring should maintain melt temperature at 230–250°C, mold steel temperature at 50–70°C, and hydraulic holding pressure at 60–80 MPa for 0.5–1.5 s. A melt temperature excursion above 255°C causes surface plate-out and yellowing, so barrel residence time should be minimized and shot size held between 30% and 70% of machine capacity. Resin lot acceptance should include melt volume-flow rate testing under ISO 1133-1:2022 at 220°C and 10 kg, because lot-to-lot variance greater than 10% from the qualified value shifts fill time and haze in thin-wall areas. Mold cavities for optical sections are polished to SPI A-1 diamond finish, and ejection pins are positioned away from light-path zones. Terminal finished components include sample tray windows, cuvette holders, reagent level windows, and microfluidic manifold retainers. For prolonged patient contact or implant-adjacent use, published data for this specific configuration is limited and full ISO 10993-18 chemical characterization is required before final qualification.
Thick-walled closures and overcap shells for prestige cosmetic packaging employ U400B at 100 parts resin, with color masterbatch added at 0.5–1.5 wt% and external mold release limited to 0.1 wt% maximum because higher release levels reduce hot-stamping adhesion and increase rejection under EU Packaging and Packaging Waste Directive 94/62/EC verification for total lead, cadmium, mercury and hexavalent chromium at a sum limit of 100 mg/kg. REACH (EC) No 1907/2006 SVHC screening applies to the finished article, and the package must not release substances into the cosmetic formulation in a manner that triggers migration concerns under EU Regulation (EC) No 1223/2009. Hot-stamping ink adhesion on the closure surface can be tested by the cross-cut method under ISO 2409:2013. Processing by injection blow molding on a reciprocating screw with melt temperature 225–240°C and parison die temperature 220–235°C is used for bottles and overcaps with 1.5–4.0 mm wall thickness; cooling is held until the part surface temperature drops to 60°C or below before ejection to avoid ovality and gate dimple. Terminal products include thick-walled cosmetic bottle overcaps, compact mirror covers, and fragrance bottle outer shells. Stress-cracking resistance must be validated against the specific fragrance or ester-based formulation because U400B may craze under hoop stress when exposed to ketones, esters or neat fragrance oils.
In refrigerated appliance water tank windows and clear detergent reservoir covers, wall thickness is limited primarily by sink-mark formation and cycle-time economics, not by melt flow restriction. U400B at 100 phr with antistatic masterbatch at 0.5–2.0 wt% and color masterbatch at 1–2 wt% is used; flame-retardant masterbatch is not recommended because the additive package can reduce light transmittance below the common specification of 88% at 3 mm. Safety compliance is assessed under IEC 60335-1:2020, and flammability classification is verified on the final part by UL 94 HB at 1.5 mm unless the end-product standard demands an alternative class. Tensile property verification for weld-line integrity may follow ISO 527-2:2012 using Type 1A specimens cut from molded plaques. Injection molding on a 250–400-ton machine with sequential valve-gated hot runner tips set at 230–245°C and melt temperature 235–245°C fills panels of 2.5–4.0 mm nominal thickness; holding pressure is profiled from 70 MPa to 35 MPa over 4–6 s to suppress sink at bosses. Terminal products include clear water tank side windows, laundry additive reservoirs, and transparent lid covers. For any direct potable water contact, migration testing under the applicable national regulation is required because the resin supplier does not provide automatic food-contact certification for U400B.
| Parameter | In vitro diagnostic injection molding | Cosmetic injection blow molding | Appliance reservoir injection molding |
|---|---|---|---|
| Drying | 80°C for 3–4 h, dew point ≤ −30°C | 80°C for 3–4 h, dew point ≤ −30°C | 80°C for 3–4 h, dew point ≤ −30°C |
| Melt temperature | 230–250°C | 225–240°C | 235–245°C |
| Mold or parison temperature | 50–70°C | 220–235°C parison die | 50–65°C mold steel |
| Holding pressure | 60–80 MPa for 0.5–1.5 s | Not applicable | 70 MPa ramped to 35 MPa over 4–6 s |
| Regrind limit | Clean sprue/runner only, lot-controlled | Not recommended for hot-stamped surfaces | Clean regrind ≤ 15 wt% |
Within IEC 62368-1:2018 compliant AV/ICT equipment, display lenses and light-guide windows are produced from U400B at 100 parts resin, with optical diffuser masterbatch at 0.5–3.0 phr and anti-yellowing stabilizer at 0.2–0.5 wt% for indoor parts. Clean-sprue regrind is limited to 15 wt% because higher recycled content can increase microgel formation and optical light scattering. Antistatic performance may be specified as surface resistivity below 10¹² Ω/sq under IEC 61340-5-1 for static-controlled assembly environments. Thin-wall injection molding at 1.5–2.5 mm thickness uses melt temperature 235–250°C, mold temperature 55–70°C, and injection speed selected to keep cavity fill time below 0.8 s for parts smaller than 150 mm; screw back pressure is held at 0.4–0.6 MPa to avoid excessive shear heating. Terminal components include front panel display windows, infrared remote receiver lenses, and machine control indicator covers. The product must also satisfy RoHS Directive 2011/65/EU Annex II material restrictions. Long-term UV exposure should be avoided unless accelerated QUV testing under ISO 4892-3:2016 demonstrates acceptable color shift for the specified service life, because U400B is not a direct substitute for UV-stabilized PMMA in continuous outdoor light.
For non-invasive respiratory device subassemblies such as nebulizer upper shells, spacer bodies and mouthpiece retainers, U400B is selected where polycarbonate exhibits stress cracking after repeated disinfection and where PMMA lacks impact strength. Biocompatibility assessment follows ISO 10993-1:2018, with cytotoxicity by ISO 10993-5:2009 and sensitisation per ISO 10993-10:2010; supplier certification alone does not satisfy finished-device requirements. The formulation is 100 parts U400B, lubricant-free for fluid-path parts, with 0–20 wt% clean-room reprocessed material from the same grade when allowed by the device risk file; external release agents are not added. Injection molding is performed on an all-electric machine with a 30:1 L/D screw, melt temperature 230–245°C, mold temperature 45–65°C, and holding pressure 50–70 MPa. Leak-test fixtures extract parts after stabilization at 23°C ± 2°C and 50% ± 5% RH. Terminal components include compressor nebulizer upper enclosures, spacer bodies, and transparent mouthpiece retainers. For prolonged mucosal or fluid-path contact, published data for this specific configuration is limited; device manufacturers must conduct wear-particle and chemical characterization under ISO 10993-18 before claiming patient-contact compatibility.
Transparent document platens, media guides and scanner calibration strips use U400B at 100 phr with antistatic masterbatch at 1.0–2.0 wt% to limit dust attraction. Safety compliance for office equipment is assessed under IEC 62368-1:2018 and RoHS Directive 2011/65/EU. Processing by injection molding with melt temperature 230–245°C and mold temperature 50–65°C produces flat parts with 2.0–3.0 mm thickness; media guides with long flow lengths require sequential gating to prevent weld-line distortion. Terminal products include photocopier document glass supports, sheet-fed scanner media guides, and paper-path cover windows. Chemical resistance to cleaning solvents must be verified with the specific cleaner because repeated exposure to isopropanol can induce stress crazing in restrained transparent parts.
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Diapolyacrylate Shinko-Lac® MABS U400B is supplied as a transparent methyl methacrylate–acrylonitrile–butadiene–styrene copolymer in pellet form. The designation positions the product within the MABS class rather than standard ABS: methyl methacrylate and the diapolyacrylate modification raise light transmission and reduce the yellow undertone commonly observed in general-purpose acrylonitrile–butadiene–styrene, while the butadiene-rich impact phase retains low-temperature toughness. The U400B identifier denotes a specific viscosity, lubrication, and optical stabilisation package; exact melt viscosity and additive concentrations are lot-dependent and must be taken from the certificate of analysis generated by the producer. In injection moulding trials, the material is typically used for transparent covers, fluid-contact housings, diagnostic device windows, and consumer electronic casings where toughness is required at ambient and moderate sub-ambient temperatures. Because the material is not a general-purpose ABS, processing, drying, and tooling decisions should follow MABS-specific practice rather than ABS defaults.
Moisture uptake in transparent MABS is lower than in polycarbonate but still high enough to cause splay and surface haze when pellets are processed above 0.10 % residual moisture. Drying should be carried out in a desiccant-bed or rotary-wheel dryer with inlet air dew point below -35 °C, at 80 °C for 4 h to 6 h. For humidity above 60 % RH, the drying time should be extended to 8 h and the hopper return-air dew point monitored. A sealed hopper with nitrogen or dried air purge is recommended to maintain pellet moisture below 0.05 % before the material enters the feed throat. Overdrying above 85 °C or residence times beyond 12 h can cause yellowing because the styrene-acrylonitrile segment and the optical stabiliser package undergo prolonged thermal exposure. Moisture measurement by ISO 15512:2019 or an equivalent loss-on-drying method is used for incoming raw-material audit; the tolerance for production use is 0.05 % maximum.
Thin-wall parts with flow length-to-thickness ratios above 150:1 require melt temperature at the upper end of the processing window, while mould temperature is selected for optical surface replication rather than merely for solidification speed. In transparent MABS of this class, the barrel profile is typically set from rear to nozzle as 220 °C, 235 °C, 245 °C, and 250 °C, with nozzle temperature not exceeding 260 °C. Melt temperature should be verified with a needle pyrometer because shear heating in the screw can raise actual melt temperature by 5 °C to 15 °C above the set value. Mold temperatures between 60 °C and 80 °C are preferred for transparent surfaces; at settings below 40 °C, rapid skin formation increases frozen-in stress, visible weld lines, and gate blush. The upper mold-temperature limit is governed by part ejection stiffness and cycle time; conformally cooled or high-conductivity tool steels are used where cycle time must be maintained. Published data for this specific U400B configuration is limited; the operating window should be confirmed with a grade-specific processing datasheet.
The table below gives the typical property envelope for transparent MABS grades of this class. Lot-specific certificates govern incoming acceptance and should not be replaced by generic values.
| Property | Test method | Typical range for MABS U400B class | Notes |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.08–1.11 g/cm³ | Measured at 23 °C |
| Melt volume-flow rate | ISO 1133-1:2022 | 8–16 cm³/10 min | At 220 °C/10 kg |
| Tensile stress at yield | ISO 527-2:2012 | 40–55 MPa | Test speed 50 mm/min |
| Tensile elongation at break | ISO 527-2:2012 | 5–20 % | Dependent on moisture and gating |
| Flexural modulus | ISO 178:2019 | 2000–2800 MPa | Test speed 2 mm/min |
| Charpy notched impact strength | ISO 179-1:2010 | 6–15 kJ/m² | 23 °C, type A notch |
| Vicat softening temperature | ISO 306:2013 method B50 | 90–105 °C | Load 50 N, heating rate 50 K/h |
| Light transmittance | ASTM D1003-13 | 87–91 % | 3 mm moulded plaque |
| Haze | ASTM D1003-13 | 1.5–3.5 % | 3 mm moulded plaque |
Lot acceptance should compare density by ISO 1183-1:2019 and melt volume-flow rate by ISO 1133-1:2022 against the supplier’s certificate of analysis. A density deviation greater than 0.005 g/cm³ or an MVR shift of more than ±2 cm³/10 min within the same grade indicates regrind contamination, incorrect resin handling, or lot mislabeling. Optical acceptance is performed on a 3 mm plaque using ASTM D1003-13; the plaque should be gated through a fan gate and moulded at the centre of the recommended processing window. Incoming visual inspection uses a light box with a daylight source to detect black specks, gels, and streaking; acceptable defect levels are use-specific and must be defined by the converter. Fourier-transform infrared spectroscopy against a retained reference spectrum can be used for resin fingerprinting when cross-contamination is suspected.
Comparisons against general-purpose ABS, polymethyl methacrylate, and polycarbonate are made on the basis of notched Charpy, haze, and Vicat data. Diapolyacrylate Shinko-Lac® MABS U400B shows higher light transmittance and lower haze than general-purpose ABS at equivalent wall thickness because the methyl methacrylate phase reduces the refractive-index mismatch at the polybutadiene interface. Compared with PMMA, the impact strength is generally higher but the surface hardness and weatherability are lower; PMMA remains the material of choice for long-term outdoor optical exposure, whereas MABS is limited to indoor or UV-screened environments. Compared with polycarbonate, MABS processes at lower melt temperature with lower drying energy, but it does not reach the heat-distortion performance or the extreme notched impact values of PC. For applications requiring gamma or electron-beam sterilisation, PC or radiation-stabilised materials may be preferred; MABS can exhibit colour shift if radiation dose and dose totals are not validated.
| Material class | Optical character | Notched Charpy, 23 °C | Vicat B50 range | Typical predrying condition |
|---|---|---|---|---|
| Diapolyacrylate MABS U400B class | Transparent | 6–15 kJ/m² | 90–105 °C | 80 °C, 4–6 h |
| General-purpose ABS | Opaque | 15–25 kJ/m² | 95–108 °C | 80 °C, 2–4 h |
| PMMA | Transparent | 2–3 kJ/m² | 95–112 °C | 80 °C, 2–4 h |
| Polycarbonate | Transparent | 25–45 kJ/m² | 140–155 °C | 120 °C, 4 h |
Transparent MABS is degraded or stress-crazed by ketones, esters, chlorinated solvents, and aromatic hydrocarbons. Brief contact with isopropanol, ethanol, and diluted household detergents is commonly tolerated at ambient temperature, but load-bearing parts should be evaluated by controlled-strain environmental stress-cracking tests such as ISO 22088-2:2006 before release. The butadiene-rich phase swells in aliphatic oils and can cause haze or microcrack formation if stressed above approximately one-third of the yield stress. For disinfectant-wiped device housings, repeated exposure to quaternary ammonium compounds, alcohol blends, or hydrogen peroxide-based cleaners may produce surface stress whitening; the converter is responsible for validating chemical compatibility under the end-use load and wipe frequency. Incompatibility with primary amine-containing additives is not a universal restriction for MABS, but formulations containing primary amines should be avoided because they can accelerate thermo-oxidative degradation and increase yellowing at melt temperatures above 250 °C.
Gate design and vent placement have a direct effect on optical quality in U400B. Submarine gates and restricted pin gates can generate shear heating above 1000 s⁻¹; at these shear rates, local melt temperature may exceed the stabiliser threshold and create silver streaks or brownish degradation specks. Direct edge gates or fan gates with a land length of 0.8–1.0 mm and a gate thickness of 50–70 % of the nominal wall are preferred for optical-grade plaque or window moulding. Vent channels should be cut to a depth of 0.015–0.025 mm on the core side, with full perimeter venting and vent width of at least 3 mm. Clamp force on equipment used for multi-cavity tools is based on an injection pressure of 50–90 MPa; for a projected shot area of 250 cm², a clamp force of 125–225 tonnes is a practical starting point.
Regrind addition up to 20 % is common in non-optical MABS applications, but for U400B transparent parts the amount must be lower and the regrind must be free of dust, mixed resin, and moisture. Regrind increases the yellowing index and reduces light transmittance because each heat history consumes the optical stabiliser package. A limit of 10 % to 15 % and a maximum of 3 processing cycles is technically justified for non-appearance-critical areas; validated colour stability should be checked against a yellowness-index method. Pellet-to-regrind ratio should be controlled gravimetrically because volumetric blending produces composition drift.