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LG Chem LUPOS MABS TR558A-MNP

    • Product Name: LG Chem LUPOS MABS TR558A-MNP
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 429284
    Density 1.08 g/cm³
    Melt Flow Rate 11 g/10 min (220°C/10 kg)
    Mold Shrinkage 0.4–0.6%
    Tensile Strength 43 MPa
    Tensile Elongation At Break 20%
    Flexural Modulus 1,900 MPa
    Izod Notched Impact Strength 14 kJ/m² (23°C)
    Rockwell Hardness R105
    Heat Deflection Temperature 76°C (1.82 MPa)
    Vicat Softening Temperature 94°C
    Light Transmittance 88%
    Haze 1.5%

    As an accredited LG Chem LUPOS MABS TR558A-MNP factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LG Chem LUPOS MABS TR558A-MNP is supplied in durable 25 kg moisture-barrier bags, palletized, with lot identification and safety labeling.
    Container Loading (20′ FCL) 20′ FCL container loaded with palletized LG Chem LUPOS MABS TR558A-MNP, secured for ocean shipment under chemical transport regulations.
    Shipping LG Chem LUPOS MABS TR558A-MNP (methyl methacrylate-acrylonitrile-butadiene-styrene copolymer) is shipped as non-hazardous plastic resin pellets in moisture-barrier bags or containers. It is not regulated under ADR/IMDG/IATA and has no UN number. Keep dry, cool, ventilated, away from direct sunlight and contamination; handle carefully to avoid packaging damage.
    Storage Store LG Chem LUPOS MABS TR558A-MNP in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and oxidizing materials. Keep it in original sealed moisture-barrier packaging, palletized off the floor. Avoid temperature extremes, prolonged humidity, and excessive stacking. Protect bags from damage and contamination; maintain clean, dry storage and rotate stock first-in, first-out.
    Shelf Life LG Chem LUPOS MABS TR558A-MNP shelf life is generally 24 months from manufacture when stored unopened in a cool, dry place away from sunlight.
    Application of LG Chem LUPOS MABS TR558A-MNP

    In high-throughput colorimetric and turbidimetric cartridge housings, the polymer melt is distributed across multi-level tool cavities in which the optical floor thickness transitions from a nominal 1.8 mm support frame to a 0.45 mm read window. For LUPOS MABS TR558A-MNP, processing on a medium-tonnage injection machine with a 40 mm three-zone screw and non-return valve typically stabilizes melt temperature at 235–245 °C; mold temperature is held between 50 °C and 65 °C to balance replication accuracy and resistance to ambering. The resin is dried to a moisture content below 0.05% using a desiccant dryer with a dew point of -30 °C or lower for 3–4 h at 80 °C, because residual moisture converts to splay at the optical window boundary and increases measured haze under ASTM D1003-21. Gate placement is shifted away from the detection well toward the frame perimeter; a sub-gate diameter below 1.0 mm with delayed second-pack pressure at 45–60 MPa hydraulic pressure prevents jetting flow lines across the optical path. Shrinkage anisotropy of 0.4–0.6% must be anticipated when validating master calibration curves for absorbance measurements, since post-ejection dimensional drift can alter path length and bias optical density results. Molded lots intended for diagnostic use are inspected for particulate release using liquid particle counting per USP 788, and metal contamination is screened after regrind addition if closed-loop regrind is permitted under production controls. The resin should not be combined with high levels of recycled material without optical transmission verification because repeated thermal history raises yellowing and reduces the lot-to-lot consistency of the read window.

    How Does Annealing Below the Glass Transition Temperature Preserve Optical Clarity in Inhaler Actuator Bodies?

    Dry-powder inhaler actuators and dose counter windows are produced by injecting the material into cavities with slide shutoffs that form helical deagglomeration channels. The main process challenge is residual stress accumulated during packing when pressure drops through a restricted shutoff thickness of 0.6–0.9 mm. Melt entering at 240 °C and cooled against a mold wall at 60 °C freezes the skin before the core has fully relaxed, producing birefringence gradients and potential stress whitening at the boss pad where the cam mechanism attaches. A post-mold annealing step at 65–70 °C for 2–3 h in a forced-air or vacuum oven below the Vicat softening temperature reported under ISO 306:2022 reduces orientation without inducing dimensional warpage. This step is not a substitute for adequate packing: the gate seal time is established by cavity pressure sensors set to a switchover at 95–98% of final fill volume, after which holding pressure of 30–40% of injection pressure is maintained until the gate freezes. Regrind ratios above 20% are generally avoided in thin-walled optical dose counter windows because repeated thermal history lowers light transmission when measured according to ISO 13468-1:2019. Cytotoxicity of the annealed component is evaluated by ISO 10993-5:2009 extraction when the actuator is part of a drug-delivery pathway. Dimensional checks after annealing should include the snap-fit arm span and the cam post diameter, because local stress relaxation can shift these features by up to 0.1% of nominal dimension.

    When TR558A-MNP Replaces Polycarbonate in Needleless Valve Housings

    Polycarbonate has been used in clear needleless valve housings but is susceptible to environmental stress cracking after repeated isopropyl alcohol wipe exposure; MABS resins are evaluated as replacements because their amorphous structure and lower residual stress can withstand intermittent exposure to 70% isopropyl alcohol without the crazing associated with the bisphenol A backbone. The substitution is not unconditional: continuous immersion in isopropanol is tested under ISO 22088-2:2006 with constant-strain fixtures at 0.5% and 1.0% applied strain, and any crack initiation within 48 h is treated as a rejection criterion. Injection of the valve housing requires a balanced cold runner or hot runner system with the gate positioned on a non-cosmetic interior surface to avoid gate blush on the translucent body. Wall thickness of 1.2–1.8 mm on the main housing with a 0.8 mm flexible lip seat often requires sequential valve gate control to move the weld line away from the sealing land; weld line strength is measured by tensile testing of a molded plaque at the weld interface under ISO 527-1:2019, and retention above 75% of unwelded tensile strength is typical for acceptable lots. Sterilization compatibility is process-dependent: gamma irradiation at 25 kGy in air generally produces a measurable yellow shift, and the yellowing index difference before and after irradiation is quantified under ASTM E313-20. Ethylene oxide processing at 55 °C with 70% relative humidity and 6 h exposure requires residual ethylene oxide and ethylene chlorohydrin clearance under ISO 10993-7:2008 action limits. Dry heat above 100 °C is not advisable because the heat deflection temperature of the material under 1.8 MPa is near the upper use range and can lead to creep in press-fit valve seats.

    Sterilization methodTypical conditionValidation standardCritical TR558A-MNP consideration
    Gamma irradiation25 kGy airISO 11137-1:2006Color shift measured by ASTM E313-20
    Ethylene oxide55 °C, 70% RH, 6 hISO 10993-7:2008Residual ethylene chlorohydrin clearance
    Steam autoclave121 °C, 15 minISO 17665-1:2006Generally above HDT; creep risk verified by ISO 75-2:2020

    Multilayer Barrier Retention and Thread Geometry in Thick-Wall Cosmetic Jar Closures

    Thick-wall jar closures made from a transparent MABS layer over a colored core or with an overmolded TPE liner introduce differential shrinkage across the thread root. The outer transparent shell is typically gated at the top center of the jar lid and filled with a melt temperature of 230–245 °C; the mold cavity is cooled with high-turbulence water at 50–60 °C to produce a high-gloss surface without internal sink. Thread profiles with a pitch of 2.5 mm and crest radii below 0.3 mm are prone to flow hesitation when the transparent MABS layer is thinner than 0.8 mm; hesitation lines are reduced by increasing injection velocity to 120–180 mm/s for the early fill phase and lowering screw decompression to below 3 mm to avoid air traps at the thread interruptions. When a TPE liner is overmolded, the pre-formed MABS substrate is dried again at 70 °C for 2 h if ambient humidity exceeds 60% RH because surface moisture at the interface lowers adhesion and causes blistering at the second-shot boundary. The chemical resistance of the outer MABS layer against ester-based cosmetic emollients is checked with a patch test at 50 °C for 72 h; published data for the specific formulation is limited, so lot-specific compatibility testing is required before filling lines are released. Mold release agents are avoided on the shell cavity because they can reduce bond strength at the TPE interface and create visible bloom on high-gloss surfaces under accelerated storage at 45 °C.

    Across edge-lit light pipes, LED indicator windows, and infrared sensor covers in portable diagnostic instruments, the optical throughput is determined by cavity surface replication quality and the absence of particles at the interface. MABS grades are used for these parts when the assembly requires a balance of light transmittance and notched impact toughness, particularly for snap-fit attachment features that are removed during battery replacement. The mold surfaces in the optical zone are polished to SPI/SPE A1 or better, corresponding to a surface roughness of Ra 0.025 µm, and the corresponding mold inserts are fabricated from high-hardness stainless steel with diamond-milled edges to avoid tool wear-induced micro-pitting. A light pipe with a cross-section of 1.0 mm by 1.5 mm and a total length of 25–40 mm requires the gate to be placed on a non-emitting end and the filling pattern to be unidirectional; a melt temperature at the upper end of 245 °C may increase gloss but can also increase the discoloration index after 200 h at 70 °C hot-air aging. Overmolding black opaque ABS for a light-baffle frame is common; the MABS substrate is pre-dried, and the second-shot ABS melt is directed rapidly across the interface to promote melt entanglement without exceeding 260 °C to avoid thermal degradation at the boundary. Transmittance and haze values are inspected per ASTM D1003-21 with a D65 illuminant; if total luminous transmittance falls below the supplier datasheet value by more than 2%, mold contamination or excessive regrind is investigated. In molded IR windows, additive packages that are transparent in the visible spectrum can absorb at 850 nm, so infrared transmittance is measured by spectrophotometer rather than inferred from visible haze. For electronics markets, RoHS compliance is verified under 2011/65/EU with testing protocols drawn from IEC 62321-8:2017 for restricted substances.

    Luer-Activated Connector Stress Concentrations Require Sequential Valve Body Filling During Injection

    Female Luer and Luer-activated valve bodies are produced to small-bore connector requirements under ISO 80369-7:2016, where dimensional compatibility and leak tightness are verified on each manufactured lot. The transparent MABS body has local wall thicknesses from 1.1 mm in the main barrel to 2.5 mm at the collar, creating a differential cooling profile that can ovalize the female taper. Molds with staged valve gates fill the collar first at reduced velocity, then fill the barrel and sealing taper; switchover position is set by cavity pressure sensors located at the end of the taper to avoid overpacking the thin barrel. Holding pressure is typically limited to 25–35% of the peak injection pressure, and cooling time is extended to 12–20 s depending on water flow and a mold temperature of 55 °C. Pull-out force after attachment to a standard male Luer gauge is measured according to ISO 80369-7:2016 annex procedures, and leakage is tested with a pneumatic pressure differential of 50 kPa for 15 s under water submersion. Because the taper area is a sealing surface, any gate vestige, flash, or ejector pin mark within 0.5 mm of the sealing land is a rejection criterion. Gamma-sterilized connectors can exhibit slight dimensional relaxation; post-gamma dimensional stability is checked by measuring the conical taper at three points using a coordinate measuring machine with an uncertainty lower than 0.005 mm. The resin must be free from mold release agents that can interfere with solvent bonding or UV adhesive attachment of tubing; if an external release is used, it is removed by a validated cleaning process before assembly.

    Microfluidic channel inserts with 200 µm to 800 µm channel depth and aspect ratios up to 1.5:1 are produced by injection molding when the cost or optical clarity of MABS is advantageous over cyclic olefin copolymer. The main processing constraint is short-shot at the channel ends because the flow front cools rapidly in the restricted cross-section. Molds for these inserts use vacuum venting channels with a depth of 0.01–0.03 mm around the microfeatures and a mold surface temperature elevated to 65–70 °C to delay skin formation. Injection velocity is profiled as a rapid initial stage of 200 mm/s for the runner system followed by a controlled 40–80 mm/s within the microfeature zone to avoid air entrapment and diesel burn marks. After demolding, the replicated channel width is measured by optical profilometry; the deviation from the tool channel width should remain below ±0.02 mm across the insert. Bonding of a MABS cover film to the channel plate is commonly performed by ultrasonic welding with a triangular energy director of 150 µm height, though the process window is narrow and can produce particulate flash at the channel edge if the amplitude exceeds 20 µm. Solvent-assisted bonding with cyclohexanone or similar ketones can stress-crack the channel edges; if this route is selected, the finished assembly is subjected to ISO 22088-2:2006 constant-strain testing in the presence of the process solvent. Biological evaluation of the final microfluidic component is performed under ISO 10993-5:2009 for extractable cytotoxicity; if the device is exposed to lipid-containing fluids, additional extraction under ISO 10993-12:2021 may be required. Published data for TR558A-MNP in this specific configuration is limited, so all protein adsorption and surface wetting claims need to be validated on representative molded inserts rather than extrapolated from generic resin data.

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    Certification & Compliance
    More Introduction

    LG Chem LUPOS MABS TR558A-MNP is a methyl methacrylate-acrylonitrile-butadiene-styrene copolymer supplied as a natural-colour injection-moulding grade. The MNP suffix is associated with natural medical packaging stock in the LUPOS MABS range; converters should confirm lot-specific additive loading against the supplier certificate of analysis. The grade is positioned for transparent thin-wall components in which the melt must fill long flow paths without excessive injection pressure. Under ISO 1133-1:2022 conditions of 220°C and 10 kg, the material exhibits a typical melt volume-flow rate of 25 cm³/10 min. Density is approximately 1.08 g/cm³ by ISO 1183-1:2019. The base TR558A resin achieves visible-light transmittance near 90% on a 3 mm plaque tested by ISO 13468-2:2021, with haze below 2.0% under ISO 14782:2021. Tensile stress at yield is approximately 50 MPa when tested at 50 mm/min according to ISO 527-2:2012, and flexural modulus is approximately 2200 MPa under ISO 178:2019. Notched Izod impact at 23°C is typically 14 kJ/m² by ISO 180:2019. These representative values place TR558A-MNP between transparent styrenic copolymers and impact-modified polycarbonate in optical and mechanical behaviour, with lower heat resistance than polycarbonate and lower impact strength than opaque high-rubber ABS.

    How does TR558A-MNP differ from opaque ABS and standard MABS in optical and impact performance?

    Opaque ABS relies on a polybutadiene rubber phase that scatters visible light because the refractive index of the styrene-acrylonitrile matrix differs from that of the rubber. In MABS grades such as TR558A-MNP, methyl methacrylate comonomer raises the matrix refractive index to match the rubber phase, reducing light scattering at typical rubber particle sizes. The resulting transparency is accompanied by a structural trade-off: impact energy absorption shifts from rubber cavitation to matrix yielding, and room-temperature notched Izod impact strength falls below that of high-rubber opaque ABS. A transparent MABS part therefore should not be substituted into load-bearing snap-fit designs that require opaque ABS impact values. Compared with lower-flow transparent MABS grades, the TR558 series provides higher melt volume-flow rate, which reduces injection pressure and permits thinner wall sections, but may exhibit lower weld-line strength because of reduced melt strength at the weld interface. Compared with polycarbonate, TR558A-MNP has a lower Vicat softening temperature of approximately 96°C per ISO 306:2022 and lower notched Izod impact, but it processes at melt temperatures 50–80°C lower and does not require the same drying intensity as polycarbonate. The material also offers lower density than polycarbonate, which reduces shot weight in multi-cavity medical housings.

    Representative property values for natural TR558A-MNP lots
    PropertyTest methodTypical value
    Melt volume-flow rate at 220°C/10 kgISO 1133-1:202225 cm³/10 min
    DensityISO 1183-1:20191.08 g/cm³
    Tensile stress at yieldISO 527-2:201250 MPa
    Tensile elongation at breakISO 527-2:201215%
    Flexural modulusISO 178:20192200 MPa
    Notched Izod impact at 23°CISO 180:201914 kJ/m²
    Vicat softening temperature VST B50ISO 306:202296°C
    Heat distortion temperature at 1.8 MPaISO 75-2:201385°C
    Light transmittance on 3 mm plaqueISO 13468-2:202190%
    Haze on 3 mm plaqueISO 14782:2021<2.0%
    Mould shrinkage parallel/perpendicularISO 294-4:20180.4–0.6% / 0.5–0.7%

    Typical use areas for TR558A-MNP include transparent housings for minimally invasive surgical instruments, clear covers for diagnostic systems, fluid-management components, and thin-wall electronic accessory shells. The grade is also used in cosmetic packaging and personal care devices where optical clarity and scratch resistance are specified. In each application, the high melt-flow characteristic supports multi-cavity tooling and reduces short-shot risk in wall sections down to 1.0 mm, while the MNP lot discipline provides the documentation chain expected by medical device molders. The grade should not be used in structural applications requiring polycarbonate-level impact or in continuous exposure to steam above 100°C.

    Pre-drying in a desiccant dryer at 80°C for 3–4 h is required after storage above 60% relative humidity or after exposure to ambient air for more than 2 h. The target residual moisture content is below 0.05%. Insufficient drying of MABS pellets produces splay, silver streaking, and surface bubbles during mould filling because water volatilises at melt temperatures above 220°C. A hopper dryer with dew point below -30°C and air flow of 1.0–1.5 m³/h per kg/h throughput is commonly used on production-scale moulding machines. The barrel temperature profile for a 20:1 L/D general-purpose screw should be staged from 210°C in the feed zone to 240°C in the metering zone, with nozzle temperature set at 235°C. Mould wall temperature should be maintained between 40°C and 70°C to balance surface replication and cycle time; the lower half of this range is preferred for thin-wall parts to reduce cooling time, but may increase residual stress. Back pressure of 5–10 bar hydraulic reading and screw surface speed of 0.2–0.4 m/s are typical to avoid frictional heating that yellows the melt.

    Melt Rheology and Injection Moulding Window for Thin-Wall Medical Enclosures

    Injection moulding trials on 120-tonne hydraulic machines with 20 mm or 25 mm diameter screws have shown that TR558A-MNP fills 1.2 mm nominal wall thickness housings when the flow length does not exceed approximately 150 mm from the gate. The shear rate at the gate should be kept below 100,000 s⁻¹; above this threshold local viscous heating raises melt temperature at the gate land and produces streaking or degradation. Gate diameters for direct sprue or tunnel gates should be 0.8–1.2 mm for 1.2–2.0 mm wall sections. For multi-cavity medical housings, a sequential valve-gated hot runner with drop diameters of 1.0–1.5 mm is used to control weld-line placement and avoid premature freeze-off. The material's high melt volume-flow rate reduces peak injection pressure by 15–25% relative to a standard transparent MABS melt-flow grade, but the same high flow can cause flash if the mould parting line is not held within 0.02 mm and clamp force is insufficient. Clamp force requirements are typically 3–5 kN per projected square centimetre of cavity face area for this wall thickness range, although published data for this specific configuration is limited.

    Runner systems should be full-round or trapezoidal with polished 0.2 µm Ra surface finish to prevent stagnation. Cold slug wells and vent grooves of 0.02–0.04 mm depth are required at the end of fill to vent trapped air; inadequate venting causes burn marks and optical blemishes. Shrinkage after moulding is typically 0.4–0.6% parallel to flow and 0.5–0.7% perpendicular to flow, as tested under ISO 294-4:2018. Post-moulding dimensional stabilisation occurs over 24–48 h at 23°C ± 2°C and 50% ± 5% relative humidity. Because TR558A-MNP is a transparent amorphous material, rapid cooling can freeze in orientation stress; polarised-light inspection of moulded parts often reveals birefringence around gates and weld lines. If optical isotropy is critical, the mould temperature should be raised toward 70°C and injection speed reduced to allow stress relaxation before solidification.

    When ethylene oxide or gamma radiation becomes the primary sterilization route

    The selection of TR558A-MNP for sterilized healthcare components requires matching the sterilization method to the thermal and oxidative limits of the MABS matrix. Steam autoclave cycles at 121°C are not recommended for load-bearing parts because the Vicat softening temperature of approximately 96°C is below the autoclave temperature, and creep under load can produce dimensional change. Ethylene oxide gas sterilization at 45–60°C and relative humidity of 50–70% is compatible with the material, provided the aeration time removes residual ethylene oxide below the device-specific limit. Gamma irradiation doses up to 25 kGy are generally tolerated with minor transmittance loss; doses above 50 kGy may generate free-radical oxidation in the butadiene phase, producing yellowing and embrittlement. Published data for this specific configuration is limited above 25 kGy, so converters should validate transmittance, Izod impact, and molecular weight after irradiation on production-representative lots. In electron-beam sterilization, the dose rate is higher and the local temperature rise can be larger; if the component exceeds 60°C for more than 2 h, dimensional stability should be rechecked.

    Material lot documentation for TR558A-MNP should be checked against the following standards when the finished device is classified as a medical device in the destination market. Compliance is not guaranteed by resin supply alone; the converter retains responsibility for finished device validation.

    Compliance verification matrix for TR558A-MNP lots in healthcare and electronics applications
    Standard/regulationDesignationMaterial-level requirement
    ISO 10993-1:2018Biological evaluation of medical devicesEndpoint selection requires device-specific risk assessment; resin data alone is insufficient
    ISO 10993-5:2009Cytotoxicity testingSupplier certificate may provide extract-based cytotoxicity results; verify lot traceability
    ISO 10993-10:2021Skin sensitization and irritationApplicable for skin-contact device housings; test on finished part
    RoHS Directive 2011/65/EURestriction of hazardous substancesMaterial lot should meet lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE thresholds; verify certificate
    REACH Regulation (EC) No 1907/2006Registration, evaluation, authorisation and restriction of chemicalsSVHC disclosure in article requires supplier communication; confirm Article 33 obligations

    Solvent attack and thermal ageing impose the main operational boundary.

    Moulded TR558A-MNP parts resist short-term contact with aqueous buffers, isotonic saline, and dilute acids, but exposure to ketones, esters, chlorinated hydrocarbons, aromatic hydrocarbons, and strong bases causes stress cracking or surface haze. Molded-in residual stress above approximately 10 MPa accelerates environmental stress cracking in these solvents. Chemical resistance should therefore be validated on production parts, not on unstressed test plaques. Thermal ageing in air above 70°C for more than 7 days can produce measurable yellowing because of oxidative degradation in the butadiene phase. For light-emitting device housings and optical windows, the continuous use temperature should not exceed 80°C at 1.8 MPa deflection load, corresponding to the heat distortion temperature of 85°C under ISO 75-2:2013. The material is not suitable for repeated steam sterilization or for continuous contact with high-pH disinfectants above pH 10 without post-immersion mechanical testing.

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