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LG Chem LUPOS MABS TR558A

    • Product Name: LG Chem LUPOS MABS TR558A
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 327619
    Material Type MABS (Transparent ABS)
    Melt Flow Rate 15 g/10 min (220°C/10 kg)
    Tensile Strength At Yield 45 MPa
    Flexural Modulus 2,000 MPa
    Notched Izod Impact Strength 12 kgf·cm/cm (23°C)
    Rockwell Hardness R105
    Heat Deflection Temperature 80°C (1.82 MPa)
    Vicat Softening Temperature 90°C
    Light Transmittance 89%
    Haze 1.5%
    Mold Shrinkage 0.4–0.6%

    As an accredited LG Chem LUPOS MABS TR558A 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 is supplied in 25 kg moisture-barrier paper bags, palletized and stretch-wrapped for shipping.
    Container Loading (20′ FCL) Loaded into a 20′ FCL container: LG Chem LUPOS MABS TR558A in 25 kg bags, palletized, shrink-wrapped, and secured for shipment.
    Shipping LG Chem LUPOS MABS TR558A is shipped as non-hazardous thermoplastic resin pellets in sealed 25 kg bags or bulk FIBCs. It is not regulated for transport (no UN number). Store dry, away from direct sunlight, heat, and moisture; use standard road, rail, sea, or air freight.
    Storage Store LG Chem LUPOS MABS TR558A in original, tightly sealed containers in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and ignition sources. Keep containers closed when not in use. Prevent moisture, contamination, dust, and static buildup. Do not store near oxidizers. Use first-in, first-out rotation and follow the supplier’s SDS and local regulations.
    Shelf Life LG Chem LUPOS MABS TR558A typically has a 24-month shelf life from manufacture when stored unopened in a cool, dry place away from sunlight.
    Application of LG Chem LUPOS MABS TR558A

    LG Chem LUPOS TR558A is a transparent methyl methacrylate-acrylonitrile-butadiene-styrene injection moulding grade. The resin is characterised by a combination of melt flow, light transmittance, and practical toughness that places it on converter lines producing clear technical parts with wall thickness between 0.5 mm and 3.2 mm. Commercial datasheets report a melt mass-flow rate of 20–28 g/10 min at 220 °C under 10 kg load according to ISO 1133-1:2022, density of 1.07–1.09 g/cm³ according to ISO 1183-1:2019, and total luminous transmittance of 88–91% at 3.2 mm plaque thickness according to ASTM D1003. Pre-drying in a desiccant dryer with dew point at or below −30 °C for 3–4 h at 80 °C is required when storage relative humidity exceeds 60%; target residual moisture is below 0.02% by weight. Above that threshold, splay lines and surface haze appear because water volatilises at the flow front. The processing window is narrower than that of opaque ABS: methyl methacrylate blocks raise transparency but lower the onset of thermal yellowing, so melt-temperature control becomes the limiting process variable. The downstream segments below are grouped by observed converter failure mode rather than by generic market category; each segment carries a distinct compliance chain and moulding risk.

    Representative starting conditions for TR558A across selected injection moulding segments are shown in the table. These values are not absolute machine settings; they are starting points derived from supplier processing guides and converter start-up logs, and must be corrected for actual gate geometry, hot-runner balance, and mould-cooling cycle.

    SegmentMelt temperature at nozzle (°C)Mould surface temperature (°C)Peak injection pressure (MPa)Holding pressure (MPa)Screw L/DResidual moisture after drying (%)
    Consumer electronics covers230–25050–7090–13060–8020:1–25:1≤0.02
    Cosmetic packaging220–24040–60100–15050–7020:1–25:1≤0.02
    Toys / juvenile products220–24045–6580–12050–7020:1–25:1≤0.02
    Non-patient-contact diagnostic housings230–25055–7590–13060–9020:1–25:1≤0.02
    Appliance panels225–24550–6585–12555–7520:1–25:1≤0.02

    How Melt-Temperature Control Limits Optical Degradation in Transparent Consumer Electronics Covers and Light Pipes

    Transparent covers, display lenses, and light pipes moulded from TR558A fail more often from optical haze generation than from gross mechanical fracture. On a reciprocating-screw injection moulding machine with a screw L/D of 20:1–25:1, a compression ratio of 2.0:1–2.5:1, and a general-purpose three-zone screw, the nozzle melt temperature is maintained at 230–250 °C. Above 260 °C, methyl methacrylate segments undergo thermal depolymerization and the part shifts toward yellow; below 220 °C, weld lines at light-pipe gates and snap hooks remain visible because the melt fronts cannot recombine above the glass transition region before solidification. The practical melt-temperature window is therefore approximately 15–20 °C wide, which forces toolmakers to reduce runner diameter and use hot-runner drops with tip temperatures held at 240–255 °C. Mould surface temperature is controlled at 50–70 °C for mirror-finish optical surfaces; cavity pressure sensors recalibrated to a peak injection pressure of 60–90 MPa reduce sink marks over bosses. For light pipes with wall thickness below 1.2 mm, injection velocity of 80–120 mm/s is necessary to prevent flow hesitation marks, but excessive velocity above 150 mm/s can generate melt fracture and jetting at the gate. Optical transmission after demoulding is evaluated by ASTM D1003, while internal stress birefringence is screened using ASTM D4093; unacceptable stress fringes are observed when ejection surface temperature is above 80 °C or when packing time is shorter than gate-seal time. End-use drop performance is measured by IEC 60068-2-31; a notched Izod impact of 7–10 kJ/m² by ISO 180/A survives repeated drops only when gate placement avoids cold-slug entrapment near snap hooks. Batch-to-batch melt-flow variation of ±1.5 g/10 min changes switchover position by 2–4 mm on an 800 kN clamp machine, so switchover should be confirmed with short-shot analysis after every lot change.

    Thin-wall cosmetic closures and transparent outer shells in the range of 0.8–1.5 mm expose MABS to residual frozen-in orientation and to ester-based fragrance compounds after decoration. Crazing is rarely homogeneous; it propagates from gate vestiges and parting-line edges where residual hoop stress exceeds 12–15 MPa as estimated from solvent-immersion crack opening tests described in ASTM D543. For flip-top closures with integral hinges, mould-filling simulation should keep shear rate below 30,000 s⁻¹ in the hinge core to avoid molecular scission; hot-runner drop temperature should not exceed 245 °C. Mould temperatures below 40 °C yield gloss below 85 GU at 60° measurement geometry and increase surface stress, while temperatures above 65 °C extend cycle time and increase gloss mottle on the core side. Fragrance formulations containing ethanol above 20 vol% or acetone-based residues act as stress-cracking agents for MABS; a 1 h anneal at 70 °C reduces internal stress but does not eliminate environmental stress cracking when the pack is stored at 40 °C under constant closure load. Decorating via hot stamping or pad printing uses solvent systems containing cyclohexanone, ethyl acetate, or methyl ethyl ketone; after decoration, 24 h of ambient storage is specified before dimensional inspection because absorbed solvent temporarily lowers tensile yield by 10–15%. Pigmented versions are produced with masterbatch addition of 2–3 wt%; the masterbatch carrier must have a melt flow index within ±5 g/10 min of the base resin to prevent visible streaking. Pearlescent or sparkle pigments must be predried to residual moisture below 0.05% because trapped moisture contributes to splay and colour shift along the flow path.

    Toy and Juvenile Product Compliance Under EN 71-3 and FDA 21 CFR 180.22

    Transparent toy lenses, rattle halves, handles, and building-block windows produced from TR558A are subject to mechanical and chemical requirements that are not met by the raw resin alone. Under EN 71-1:2018+A14:2021, small-component and drop-test performance are determined by the finished article; a 3 mm nominal wall thickness in a spherical rattle is generally insufficient if the gate lands on a load-bearing seam because weld-line Izod impact can be 30–40% lower than the unfused matrix. Injection moulders relocate the gate to the part interior and use sequential valve-gate opening when moulding multi-cavity rattle halves, maintaining cavity fill time below 1.5 s and peak packing pressure below 80 MPa to prevent flash at the parting line. Chemical compliance under EN 71-3:2019+A1:2021 requires migration limits for antimony, barium, cadmium, chromium, lead, mercury, and selenium; these limits are controlled by the pigment and additive package, not by MABS matrix chemistry. A colourant supplier must provide an EN 71-3 conformity declaration that includes the actual colourant lot and summation ratios for the target wall thickness. For toys intended to contact food during play, FDA 21 CFR 180.22 governs acrylonitrile copolymer migration; finished-article testing must confirm monomer migration below the regulated residual acrylonitrile concentration, and the converter must document that regrind levels do not exceed 20 wt% to avoid heterophase contamination from prior industrial batches. Materials destined for use in the EU are additionally subject to Regulation (EU) 2023/988 General Product Safety Regulation and REACH Annex XVII restrictions; no blanket MABS resin certificate covers all categories because toy safety is assessed on the final assembled article.

    SegmentStandard or regulationClause / methodParameter
    Consumer electronics coversRoHS Directive 2011/65/EU Annex IIIEC 62321-5:2013Pb, Cd, Hg, Cr(VI)
    Cosmetic packagingRegulation (EU) No 10/2011Annex I overall migration OM2Overall migration
    Toys / juvenile productsEN 71-3:2019+A1:2021Table 2 / Table 3Element migration limits
    Non-patient-contact diagnostic housingsISO 10993-1:2018Clause 4.1Biological risk assessment only
    Stationery / office equipmentDIN 876/1Straightedge flatness methodStraightness tolerance
    Appliance panelsIEC 61340-5-1Table 1Surface resistance

    Non-patient-contact diagnostic housings and transparent covers for in-vitro diagnostic bench-top instruments are an application where impact sound-deadening is balanced against enclosure creep at elevated internal chassis temperatures. TR558A parts used in this environment are not sterile barriers and are not intended as long-term skin-contacting components; ISO 10993-1:2018 biological evaluation therefore remains a finished-device risk assessment, not a resin-level certificate. The heat deflection temperature under 1.8 MPa by ISO 75-2 method A is in the range of 85–90 °C; internal power supplies and DC-DC converters should be spaced so that local air temperature at the polymer surface stays below 65 °C during continuous operation. Vent slots with an aspect ratio above 4:1 and wall thickness below 2.0 mm cool faster but increase flow-induced birefringence; the resulting optical retardation under ASTM D4093 can alter photodetector readings through the cover. Moulders using hydraulic machines with clamp force from 800 to 2,000 kN for multi-cavity frames report that switchover position must be corrected by 3–5 mm when regrind fraction increases from 0 to 15% because viscosity shifts by approximately 6–9% as measured by capillary rheometry at 240 °C and 1,000 s⁻¹. Cleaning with quaternary ammonium compounds is specified instead of repeated exposure to 70% isopropanol wipes; micro-crazing on unannealed edges can appear within 50 wipe cycles under a constant flexural load of 5 MPa. Published long-term creep data for TR558A in cyclic thermal enclosure service are limited; converter-level validation under IEC 60601-1 mechanical enclosure requirements is therefore mandatory before design freeze.

    When Stationery and Office Equipment Parts Require Low-Temperature Dimensional Stability

    Transparent folders, sheet protectors, ruler bodies, tape dispenser covers, and desktop organizer shelves are the lowest thermal-load segment for TR558A. The dominant conversion issue is not thermal degradation but flatness after ejection from multi-drop cold-runner tools with restricted gate widths below 1.0 mm. On a standard injection moulding machine with a three-plate tool, a mould temperature of 40–50 °C and holding pressure of 40–60 MPa for 3 s per millimetre of wall thickness produce flatness deviation better than 0.3 mm over 100 mm length when measured by DIN 876/1 straightedge. For sheet protectors with wall thickness 0.5 mm, flow length to thickness ratios above 200:1 create hesitation marks; an injection speed of 120–160 mm/s with a mould temperature raised to 60 °C at the end of fill overcomes flow-front stall at the gate. In stationery products marketed for children, the same EN 71-3 migration limits apply as for toys; otherwise REACH Annex XVII restrictions and RoHS Directive 2011/65/EU Annex II apply to electrical accessories such as tape dispensers with integrated batteries. Tools with eight or more cavities show batch-dependent cavity imbalance of 1.5–2.5% by part weight when the runner diameter is below 5 mm; artificial balancing by edge gate depth adjustment is required after each maintenance cycle.

    Transparent Appliance Panels Are Withheld from High-Heat Dishwasher Environments

    Clear control-panel windows, knob skirts, ice dispenser flaps, and vacuum cleaner dust-cup windows exploit the scratch resistance and gloss of MABS but do not withstand sustained exposure to steam-condensing dishwasher cycles at 85 °C. The short-term heat deflection temperature under 0.45 MPa by ISO 75-2 method B is approximately 95–98 °C, but dimensional integrity under load declines above 70 °C, so the part must be positioned away from heating elements and from direct steam nozzles. For refrigerated appliance interiors, low-temperature impact is the more relevant mechanical parameter; notched Izod impact at −10 °C is roughly 5–7% lower than at 23 °C, which allows snap-fit assembly without shattering. Luminous transmission in tinted transparent panels must be measured with ASTM D1003 after colour masterbatch addition; at 2 wt% smoke tint, total luminous transmittance can fall from 90% to 70–75% depending on pigment particle size below 200 nm. Injection moulders should avoid mixing TR558A with general ABS regrind because refractive-index mismatch creates visible haze at regrind fractions above 10 wt%. Static dissipative versions used in dust-cup service are compounded with antistatic additives that show bloom after 200 h at 50 °C storage; the resulting surface deposit must be tested under IEC 61340-5-1 for surface resistance below 10¹¹ Ω before use in electronics-adjacent enclosures. Warped panels are recovered by annealing at 60 °C for 2 h in a fixture, but that same cycle increases gloss variation on textured surfaces by 2–3 GU at 60° geometry, so dimensional adjustment is specified before post-mould thermal straightening.

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    Certification & Compliance
    More Introduction

    LG Chem LUPOS MABS TR558A is supplied as a transparent methyl methacrylate–acrylonitrile–butadiene–styrene injection-molding grade. The copolymer is formulated to balance optical clarity, impact resistance, and melt flow in thin-wall components. Typical application areas include cosmetic closures, transparent appliance panels, light-guide parts, and medical device enclosures where gloss retention, dimensional stability, and light transmission are specified.

    Chemical Architecture and Specification Boundaries

    The transparency mechanism depends on refractive-index matching between the styrene-acrylonitrile-methyl methacrylate matrix and the dispersed butadiene-based rubber phase. If the rubber domain size distribution or refractive-index mismatch is uncontrolled, forward light scattering increases haze. The manufacturer’s published representative values for the TR558A grade are summarized in Table 1. The figures are not guaranteed specification limits; they are produced from injection-molded specimens under controlled conditions and are subject to lot-to-lot variation.

    PropertyTest methodRepresentative value
    Melt-flow index at 220 °C, 10 kgASTM D123822 g/10 min
    Specific gravityASTM D7921.08
    Tensile strength at yieldASTM D63846 MPa
    Tensile elongation at breakASTM D63825%
    Flexural modulusASTM D7902,100 MPa
    Notched Izod impact at 23 °C, 3.2 mmASTM D256120 J/m
    Rockwell hardness, R scaleASTM D785105
    Heat deflection temperature, 1.82 MPa, 6.4 mm unannealedASTM D64885 °C
    Light transmittance, 3.2 mmASTM D100390%
    Haze, 3.2 mmASTM D10032.0%
    Vicat softening temperature, 50 NASTM D152595 °C

    Because MABS contains a butadiene-modified phase, impact performance is strongly dependent on specimen thickness and gate orientation. The notched Izod value should not be read as a design basis for parts under multiaxial impact or high strain-rate loading. Melt-flow index is measured at 220 °C under 10 kg; it indicates relative flowability but does not provide a complete shear-viscosity curve.

    Before melt processing, pellet moisture must be reduced below 0.05% by weight. A desiccant dryer set at 80 °C for 4–6 h with a dew point below −40 °C is appropriate after opened or multi-day ambient storage. Undried material processed at relative humidity above 60% can generate splay, silver streaks, and surface veiling because water vapor expands during plastication and produces optical defects at the advancing melt front. Production-scale hopper loaders with dry-air purge should maintain closed-loop desiccant-bed regeneration to avoid moisture breakthrough during extended molding campaigns.

    When Thin-Wall Injection Molds Generate Optical Defects, What Parameter Set Restores Uniform Light Transmission?

    The processing window for TR558A is constrained by two competing failure modes: insufficient melt temperature or mold temperature produces flow marks and high internal stress, while excessive barrel temperature above 250 °C triggers thermal degradation of the methyl methacrylate segments and yellowing. A validated barrel profile for a 120-tonne hydraulic injection machine with a 25 mm screw begins with a feed zone at 40–60 °C, compression zone at 200–220 °C, metering zone at 220–230 °C, and nozzle at 220–235 °C. Melt temperature measured by an insertion pyrometer should remain between 210 °C and 240 °C.

    Mold temperature controls surface replication and haze. For transparent parts with wall thickness between 0.8 mm and 2.5 mm, mold temperature between 40 °C and 70 °C is typical. When gate blush or flow hesitation occurs, increasing mold temperature to 60–70 °C is more effective than raising melt temperature, because higher mold surface temperature reduces premature freezing of the transparent melt front. Back pressure of 0.3–0.7 MPa and screw surface speed of 50–100 mm/s are adequate for homogeneous melt quality without excessive shear heating. The screw should provide an L/D of at least 20:1 and a compression ratio of 2.0–2.5; a worn non-return valve with substantial clearance causes shot-weight drift and should be replaced when cushion variation exceeds 1 mm.

    Hot-runner systems for transparent MABS require internally heated or externally heated manifolds with smooth flow-channel geometry. Dead spots at sharp bends, valve-pin gaps, or improperly matched nozzle tips produce black specks and optical contamination. Hot-runner manifold temperature is typically held at 230 °C. Gate land length between 0.5 mm and 1.0 mm is used for direct edge gates; fan gates are preferred for sheet-like optical parts. In production, splay near the gate often indicates either resin moisture above 0.05% or local melt-temperature overshoot above 250 °C, not a bulk melt-temperature error.

    Light-guide components with wall thickness of 0.8–2.0 mm are molded using polished tool steel inserts with surface finish equivalent to SPI A-2 or finer. Ejection draft should not fall below 0.5°, because forced ejection under deep draw can generate birefringence and surface microcracks. When secondary processes such as pad printing, metallization, or adhesive bonding are specified, surface energy after corona or plasma treatment should reach at least 40 mN/m. Solvent-based inks and adhesives containing ketones or aromatic hydrocarbons may craze the molded surface, especially when applied to parts with high molded-in stress.

    If the Application Involves Repeated Contact with Isopropanol or Alkaline Cleaners

    TR558A is a styrenic copolymer and should be evaluated under environmental stress cracking conditions before specification in disinfection-ready enclosures or chemical-contact housings. Isopropanol, ethanol, and alkaline cleaning agents can induce crazing when the polymer is under tensile strain above approximately 15% of yield. Validation should follow ISO 22088-2 or ASTM D1693 with molded specimens at the intended service strain and chemical concentration. Aromatic hydrocarbons, esters, and ketones are stronger stress-cracking agents and should not be used as cleaning fluids or paint carriers. For medical or consumer parts exposed to 70% ethanol wipes, a grade-specific compatibility test under worst-case load and exposure duration is required; published data for this specific configuration is limited.

    Relative to transparent ABS grades that use larger polybutadiene domains or lack methyl methacrylate in the matrix, the MABS architecture reduces haze from approximately 4–6% to below 2.0% at 3.2 mm thickness under ASTM D1003. Compared with PMMA, the butadiene-modified phase raises notched Izod impact from roughly 20 J/m to above 100 J/m, but tensile modulus and surface scratch resistance are lower. Polycarbonate provides higher impact and higher heat deflection temperature, yet its melt viscosity is higher, and its stress-cracking resistance under alkaline cleaning is often poorer. Among transparent styrenic injection grades, TR558A is positioned where low haze and medium impact resistance are required without the drying and viscosity burden of polycarbonate.

    Rheological Consequences of High-Shear Nozzle Flow

    At thin-wall fill velocities, melt passing through the nozzle and gate experiences high apparent shear rates, producing non-Newtonian shear thinning. The melt-flow index value of 22 g/10 min at 220 °C and 10 kg does not capture the full shear-viscosity response. Mold-filling simulations should use pressure-volume-temperature data and Cross-WLF viscosity coefficients specific to TR558A, not generic MABS or ABS data. In production-scale molding of 1.0 mm wall parts, excessive injection velocity can produce jetting and silver streaks near the gate; the remedy is to reduce injection velocity, increase gate diameter, or alter gate position, while holding melt temperature constant at 220–230 °C.

    Regulatory declarations for TR558A are supplied by LG Chem through grade-specific certificates. The material is generally declared under the European Union REACH regulation EC 1907/2006 and the RoHS directive 2011/65/EU for heavy-metal and brominated flame-retardant restrictions, but the converter must confirm the specific pellet lot and any color concentrate or additive masterbatch. Because processing aids, external lubricants, and colorants can alter compliance status, a generic polymer declaration is not a finished-article certification.

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