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LG Chem LUPOS ABS HI100X

    • Product Name: LG Chem LUPOS ABS HI100X
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 818926
    Manufacturer LG Chem
    Brand LUPOS
    Product Name ABS HI100X
    Polymer Type Acrylonitrile Butadiene Styrene (ABS)
    Grade HI100X
    Physical Form Pellets
    Color Natural
    Processing Method Injection Molding
    Density 1.04 g/cm³
    Melt Flow Rate 10 g/10 min
    Tensile Strength 44 MPa
    Flexural Modulus 2300 MPa
    Notched Izod Impact Strength 250 J/m
    Heat Deflection Temperature 85 °C at 1.82 MPa
    Vicat Softening Temperature 95 °C
    Rockwell Hardness 105 R
    Flammability Rating HB

    As an accredited LG Chem LUPOS ABS HI100X factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LG Chem LUPOS ABS HI100X is supplied in 25 kg moisture-resistant paper bags, palletized for safe industrial storage and handling.
    Container Loading (20′ FCL) LG Chem LUPOS ABS HI100X packed in 25 kg bags on pallets, shrink-wrapped and loaded into a 20′ FCL dry container.
    Shipping LG Chem LUPOS ABS HI100X is shipped as non-hazardous ABS resin pellets, typically in 25 kg moisture-barrier bags on pallets or in bulk containers. Keep dry, cool, and away from direct sunlight; avoid punctures and contamination. Use standard freight and follow the SDS and local transport regulations.
    Storage Store LG Chem LUPOS ABS HI100X in a cool, dry, well-ventilated area at ambient temperature, away from direct sunlight, heat sources, ignition, and oxidizing agents. Keep containers closed and in original sealed packaging to prevent moisture, contamination, and electrostatic buildup. Use stable stacking, avoid flame or prolonged high humidity, and follow local regulations plus the manufacturer’s safety data sheet.
    Shelf Life Shelf life is typically 24 months from manufacture when stored unopened in a cool, dry, well-ventilated area away from direct sunlight.
    Application of LG Chem LUPOS ABS HI100X

    Automotive interior lower garnish assemblies and glove-box backplates are first-tier candidate parts for LG Chem LUPOS ABS HI100X when the OEM specification prioritises cold-impact deformation over heat distortion. The grade is processed as natural or pre-coloured resin; black interior trim is generally produced with carbon-black masterbatch at a dose rate of 2.0–4.0 wt%, with the lower bound used for thin-wall B-pillar lower parts and the upper bound for glove-box outer shells where surface depth and scratch visibility control are tested. Compliance is determined under FMVSS 302 and ISO 3795 horizontal burn-rate methods, while VOC and odour are screened using VDA 278 thermal desorption analysis. REACH SVHC certification and EU ELV reporting are mandatory before shipment into EU assembly plants. Pre-drying is carried out in a desiccant dryer at 80 °C for 2–4 h, with dew point no higher than −30 °C and residual moisture below 0.05 wt%. The melt temperature is kept between 230 °C and 250 °C; hot-runner manifold temperatures must not exceed 250 °C because the butadiene phase begins to degrade and produces brown streaks. Injection speed is set from flow-length-to-wall-thickness ratio, with moderate velocities of 100–250 mm/s on barrel sizes up to 40 mm and higher velocities on thin walls. Packing pressure is tied to gate seal time and is usually 60–80% of peak injection pressure. Closed-loop regrind from sprues and rejected parts is capped at 15 wt% after six consecutive moulding trials demonstrate that the melt-flow ratio does not exceed 1.25 relative to virgin material. Published data for this specific configuration is limited; lot-specific melt flow and Izod impact values from the certificate of analysis must be approved before tool trials. Terminal parts include centre console side panels, glove-box outer shells, B-pillar lower garnishes and steering column shrouds where dimensional tolerance is controlled by mould temperature rather than annealing.

    Why does appliance facade tooling require elevated mould temperatures when using high-rubber ABS?

    Washing machine top decks and front facades are moulded in high-gloss, large-area tools where weld-line location overlaps mechanical latch bosses. In that geometry, the rubber phase in HI100X creates a flow front that is more elastic than a low-rubber ABS; therefore the mould temperature is raised to 60–70 °C to reduce frozen-layer growth and to improve replication of grain patterns. The material is dried at 80 °C for 3 h minimum. Melt temperature is held at 240 °C and must not exceed 250 °C for more than 8 min cumulative residence time. Colour masterbatch for appliance white or graphite silver is metered at 2–3 wt%; higher loading lowers notched Charpy results and increases the risk of visible pigment streaks along flow lines. Detergent-resistant stabilisation is validated by immersion in a 1% sodium carbonate solution at 40 °C for 72 h if the part will sit near dispenser overflow. Flammability is classified under UL 94 HB for appliance facades; structural integrity is assessed under IEC 60335-1 and relevant part-specific annexes. The weld line at the latch boss is the controlling failure mode. Charpy impact values must be generated on part-cut specimens with the notch positioned exactly on the weld line according to ISO 179-1. Bulk-spec sheet data are not sufficient; part-specific values are required because weld-line strength is a function of melt temperature, mould temperature, injection speed and flow-front meeting angle. Terminal products include front-load washer top decks, detergent dispenser housings, outer facades and control-panel frames. The process limitation is that mould temperatures below 50 °C may increase notch sensitivity at the weld line, while temperatures above 70 °C extend cooling time beyond cost targets and may cause ejection distortion in large flat sections.

    Screw bosses in electronic equipment housings are among the most narrowly constrained features when HI100X is selected for router and set-top box shells. The compliance chain for the sector is IEC 62368-1 for audio/video and information technology equipment, plus RoHS 2011/65/EU with supplier declarations from LG Chem. Flame classification is usually UL 94 HB at a final wall thickness of 1.8–3.0 mm, but the designer must verify the yellow-card thickness against the actual part drawing. For screw bosses, the resin is not compounded with glass fibre; the boss design therefore relies on surrounding wall stock and correct packing. Boss outer diameter is specified at 2.0 times the screw outer diameter, with wall thickness around 0.6–0.8 mm per boss wall to avoid sink marks. The gate is placed away from the boss where possible, or a dedicated flow leader is milled to force flow into the boss root. Melt temperature is held at 225–245 °C, with back pressure at 3–5 bar for homogeneous melt quality. Injection speed is set to fill the boss within 70–90% of total injection time, followed by a packing phase of 0.2–0.5 s per mm of wall thickness. Regrind is limited to 10 wt% in this sector because repeated heat history shortens molecular weight and reduces screw-pull-out resistance. Operators measure screw pull-out force on a dedicated fixture at three locations per cavity per shift; the pass/fail limit is set from the OEM drawing and correlated with residual moisture and pack pressure. Terminal parts include router lower shells, set-top box frames, UPS bezels and small control-room module housings. The boundary condition is that hot-runner temperatures above 250 °C produce visible splay and odour after momentary line stoppages, so the press control is interlocked to reduce the manifold setpoint automatically after 5 min idle.

    Application segmentCompliance standardTest condition or clause focusBoundary verification
    Automotive interior trimFMVSS 302, ISO 3795, VDA 278Horizontal burn rate, VOC/TVOC thermal desorptionLot CofA and OEM material approval required
    Appliance facadesIEC 60335-1, UL 94 HB, ISO 179-1Notched Charpy at −20 °C, ignitabilityWeld-line specimens to be cut from moulded parts
    Electronic enclosuresIEC 62368-1, RoHS 2011/65/EU, UL 94 HBSafeguard enclosure, restricted substances, flame class at final wallYellow-card thickness checked against drawing
    Outdoor telecom shroudsIEC 62262, EN 60529Mechanical impact rating, ingress protectionUV-stabilised formulation required for exposed skin
    Power tool housingsEN 62841, ISO 179-1Mechanical strength, Charpy on ribs and bossesLithium grease immersion test at 60 °C for 168 h

    When ABS HI100X is redirected from injection moulding to single-screw sheet extrusion

    When the same resin is evaluated on a single-screw sheet line for heavy-gauge thermoforming, the limiting variable shifts from weld-line integrity to gel count and melt-temperature control. This use is not the primary design envelope for HI100X, and published data for this specific configuration is limited. For short-run custom trays and prototype trim blanks, edge trim can be reintroduced at 5–10 wt% only if the shredded backbone is dust-free and dried to below 0.05 wt% moisture. Extrusion should run with a 30–40 L/D barrier screw and a closed-loop screen changer with a 60–80 mesh pack for pilot batches. Melt temperature at the die is kept between 210 °C and 230 °C; higher settings create die-lip drool and gel from butadiene degradation. The die gap is set at 1.2–1.5 times the intended final sheet thickness, and the vertical or inclined polishing roll stack is maintained at 60–80 °C. Compliance in this segment is driven by end-use packaging or material-handling specifications rather than electrical or appliance standards. If the formed part enters the EU as transport packaging, chemical safety is verified under REACH and, where applicable, heavy-metal restrictions under RoHS 2011/65/EU. Thermoforming results must be checked for part weight and wall-thickness distribution on a grid pattern; minimum wall thickness is set by the OEM drawing and is not a material property. The material should not be blended with amine-containing polyamide regrind because the combination can produce incompatible phases and yellowing at 220–240 °C. Products include heavy-gauge dunnage trays, prototype automotive trim blanks, and non-food industrial handling trays. The operational boundary is that HI100X should not be mixed with polycarbonate regrind of unknown source because phase separation produces surface delamination and reduces impact value. If the line has previously run PC sheet, the barrel and die must be purged with a suitable ABS transition material until melt pressure stabilises within ±5% of baseline before HI100X is introduced.

    Outdoor telecommunication pedestal shrouds and low-temperature impact retention

    Outdoor telecommunication pedestal shrouds expose the rubber phase to repeated low-temperature impact and ultraviolet irradiation, which means material selection must distinguish between as-moulded impact and impact retained after weathering. Bare HI100X is suitable for internal structural frames, but external shrouds require a UV-stabilised variant or post-mould coating; otherwise the surface yellows and loses gloss. The processing window for this sector is 230–250 °C melt temperature and 50–60 °C mould temperature. Pre-drying is 80 °C for 4 h before first use and 2 h after interruptions longer than 30 min if the dryer has no dew-point alarm. Wall thickness is generally 3.0–4.0 mm to meet mechanical impact under IEC 62262 at IK08 or above, but the actual rating depends on part design and internal reinforcement. Ingress protection is validated with the final gasket and cable glands according to EN 60529. Formulation for UV-stabilised black compounds uses carbon-black masterbatch at 1.5–2.5 wt%; for light grey pedestal shrouds a hindered-amine light stabiliser and UV absorber package is used at 1.0–2.0 wt%, but this must be sourced as a pre-compounded formulation to avoid dispersion defects. The risk in this application is internal voiding around thick bosses and ribs. Pack pressure is therefore maintained until gate freeze, and cooling time is verified by cavity-pressure sensors rather than timer only. If cavity pressure falls below 50% of peak at the gate before packing is terminated, short shots and voids will occur at the base of bosses. Regrind from rejected shrouds is capped at 20 wt% only when the regrind is free of weather-exposed skin and after physical property revalidation by ISO 179-1 notched Charpy at −30 °C. Terminal parts include ground-level utility boxes, pole-mount shrouds and remote terminal unit enclosures. The operational boundary is that prolonged ultraviolet exposure without stabilisation will reduce gloss retention and may lower impact after 12–18 months, so outdoor parts must not rely on unmodified HI100X as the final weatherable surface.

    Power tool housings require impact resistance at the intersection of manual drop, mechanical vibration and chemical exposure from gear lubricants and cleaning agents. HI100X is processed in tools with a melt temperature of 230–250 °C, a mould temperature of 40–60 °C, and a fill speed that avoids excessive shear heating at the gate. The sector’s compliance is anchored to EN 62841 for motor-operated hand-held tools and relevant clauses for mechanical strength, plus ISO 179-1 for Charpy values of the housing ribs. For gear-case covers, grease resistance is screened by contact with a lithium-based grease at 60 °C for 168 h; surface cracking, softening or delamination constitutes failure. The formulation is typically a carbon-black masterbatch at 2–3 wt% for black housings, with static-dissipative grades avoided unless the application requires it. Internal regrind is controlled at 10–15 wt% after moisture and dust checks, because higher ratios increase the brittle failure rate of snap fits and battery terminal bosses. Gate placement is chosen so that the flow front meets at low-stress regions rather than at screw towers. Rib-to-wall ratio is designed at 0.5–0.6 to reduce sink, and ejection pins are placed outside the visible surface. Terminal parts include drill motor housings, angle grinder gear-case covers, battery adapter shells and impact driver clamshells. The boundary condition is that impact-modified ABS should not be blended with stiff, low-impact recycled ABS unless the blend is re-certified for notched impact at −20 °C; the mixture can produce a sharp drop in ductile failure mode even when melt flow rate appears acceptable. Published data for HI100X in power-tool clamshells is limited, so part-specific impact and chemical-resistance trials are required before tool release.

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    Certification & Compliance
    More Introduction

    LG Chem LUPOS ABS HI100X is a high-impact acrylonitrile-butadiene-styrene terpolymer positioned within the LUPOS ABS portfolio for injection moulding and extrusion applications. The grade is supplied in pellet form and is specified where low-temperature impact retention, dimensional stability, and melt processability must be balanced in rigid parts. HI100X is not a single-phase resin but a multiphase system in which grafted polybutadiene particles are dispersed in a styrene-acrylonitrile matrix. Rubber particle size distribution, graft density, and dispersed-phase volume govern the low-temperature impact response and melt elasticity. Grade-specific values are controlled by the manufacturer under the ISO 2580-2 data-block framework. The following engineering statements are restricted to class-wide high-impact ABS behaviour unless otherwise noted; users should obtain the released-lot technical data sheet for HI100X because colourant packages, regrind fraction, and moulding temperature strongly influence final properties.

    What Limits the Processing Window for HI100X During Drying and Melt Plastication?

    Moisture absorption in ABS is lower than in polyamide 6 or polycarbonate, but the pellet surface remains hygroscopic. Residual moisture above approximately 0.05 wt% contributes to splay, silver streaks, and reduced weld-line strength because water expands in the melt during decompression and gate passage. Class-wide ABS practice is to dry in a dehumidifying hopper dryer with a dew point of −40 °C or better for 2–4 h at 70–80 °C; high-humidity warehouse conditions may require an extended residence time of 6–8 h. Melt temperature should not exceed 240–250 °C for an unfilled high-impact ABS grade because the polybutadiene phase degrades by oxidation-accelerated crosslinking and chain scission, producing brown streaking and loss of impact retention. Barrel profile on a three-zone general-purpose screw with L/D ratio between 20:1 and 25:1 is typically set from 200 °C at the feed throat to 230 °C at the nozzle. Actual settings must be corrected for shear heating in small-diameter screws, especially when screw speed exceeds 100 min⁻¹.

    On multicavity tools with extended flow length-to-wall-thickness ratios above 150:1, high-impact ABS such as HI100X exhibits a viscosity plateau that controls both peak injection pressure and flow-induced skin orientation. When a hydraulic injection moulding machine with a 22 mm diameter screw and a clamp force of 1200 kN is used, the recommended decompression distance is 2–4 mm to prevent nozzle drool without cavitating the melt cushion. Gate freeze-off in cold-runner systems becomes the limiting factor when the gate diameter is below 1.0 mm, because the styrenic melt front solidifies before the required packing time is complete. In such geometries, a valve gate or heated needle shut-off is required to maintain a packing pressure of 40–60 MPa for 0.5–1.5 s beyond volumetric fill. On production-scale tools, failure modes observed include jetting from undersized tunnel gates, non-uniform packing in finger-like flow fronts, and high scrap rates from weld-line and gate-blush regions when the melt cushion is less than 3–6 mm. Tensile properties measured on moulded plaques according to ISO 527-2 and flexural properties measured according to ISO 178 are strongly influenced by gate location and fill orientation; charpy or Izod impact values measured on weld-line specimens are class-wide lower than bulk values because butadiene domains orient parallel to the weld plane. Published data for HI100X in quantitative weld-line impact retention is limited and should be generated on the production tool rather than extrapolated from edge-gated specimens.

    When Electroplating Replicates Rubber Particle Distribution Across HI100X Surfaces

    Electroplating and vacuum metallisation on HI100X depend on residual butadiene surface distribution and the oxidative etch profile. In ABS electroplating, chromic-sulphuric acid etching selectively attacks butadiene domains and produces mechanical interlock. For a high-impact grade with larger dispersed rubber domains, etch depth and crater diameter may be greater than on medium-impact ABS, which can improve adhesion but may increase surface roughness if the etch time exceeds 5–8 min at 65–70 °C in a hexavalent chromium-free process. The subsequent electroless nickel or copper deposition creates a conductive layer; adhesion is assessed by cross-cut peel according to ISO 2409 or tape pull using ASTM D3359. Etch penetration is not uniform across gated and weld-line areas because rubber particle deformation varies with flow-induced strain. Production platers report delamination at gate-blush zones and low peel strength at knit lines when rack current density deviates beyond the qualified range. Published adhesion data for HI100X in hexavalent chromium-free etch systems is limited, and the etch line must be qualified through peel-force testing on production-gate and weld-line regions. Solvent-borne polymer coatings and in-mould decoration films should be checked for solvent compatibility because ketones and esters attack the SAN matrix and may cause stress cracking in moulded-in residual stress zones.

    Comparative Profile: HI100X Versus High-Flow ABS and PC/ABS Blends

    The following table summarises class-wide property ranges for high-impact ABS, high-flow ABS, and PC/ABS blends. It is not a product data sheet for HI100X and should not be used for final part design. HI100X-specific values must be obtained from the manufacturer’s released technical data sheet.

    AttributeTest methodHigh-impact ABS classHigh-flow ABS classPC/ABS class
    DensityISO 1183-11.04–1.07 g/cm³1.05–1.08 g/cm³1.10–1.17 g/cm³
    Tensile yieldISO 527-235–45 MPa40–48 MPa50–60 MPa
    Flexural modulusISO 1781700–2200 MPa1900–2400 MPa2100–2500 MPa
    Notched Izod impact at 23 °CISO 180/A25–40 kJ/m²12–20 kJ/m²40–60 kJ/m²
    Heat deflection temperatureISO 75-2, Method A94–102 °C88–96 °C105–125 °C
    Melt volume-flow rate at 220 °C/10 kgISO 1133-1:202215–40 cm³/10 min40–80 cm³/10 min5–15 cm³/10 min

    Sheet extrusion of HI100X requires a vented barrier screw with L/D ratio of 32:1 to 40:1 and a melt pump to damp pressure oscillations from regrind fraction changes. On a 900 mm sheet line with three-roll polishing stack, roll temperatures are typically set between 80–100 °C for high-impact ABS to control sheet shrinkage and surface replication. Chill-roll temperature below 70 °C can freeze residual orientation and produce higher longitudinal shrinkage after trimming. Edge trim and skeletal scrap from thermoforming are frequently reintroduced at levels up to 20 wt%; above this level, the MFR window can narrow because repeated heat history increases the crosslinked fraction of the polybutadiene phase. Dimensional change of thermoformed parts depends on sheet gauge, plug speed, and plug temperature. For amorphous ABS, free shrink measured on a 100 mm disc after 10 min at 120 °C is the usual internal control, but published data for this specific configuration in HI100X is limited. Extruders should not rely on colourless pellet appearance to judge contamination; recycled sheet produced from printed or coated parts carries high risk of SAN-matrix incompatibility and plate-out on the die lip.

    Compliance Boundaries Are Not Transferable Across Colourant Packages

    Regulatory compliance is not assigned to a base resin alone. HI100X may be supplied with pellet-level colourants, processing aids, or mould-release packages that alter the final compliance status. A raw-material compliance checklist should be rebuilt for every final formulation and colourant lot. The matrix below summarises typical assessment frames for unfilled ABS compounds; the user must obtain the supplier’s Safety Data Sheet and product compliance statement for the specific HI100X commercial grade.

    RequirementDesignationAssessment basis
    Restriction of hazardous substancesRoHS 2011/65/EU with (EU) 2015/863Lead <1000 ppm, mercury <1000 ppm, cadmium <100 ppm, hexavalent chromium <1000 ppm, PBB and PBDE <1000 ppm
    REACH candidate listEC 1907/2006, Article 33Supplier SVHC declaration required for each lot
    Food contactFDA 21 CFR 177.1020Applicable only where the specific ABS grade and colourant package are cleared; not inferred for HI100X without confirmation
    Flammability ratingUL 94, vertical burnUnfilled ABS is generally HB at 1.5 mm; any V-class claim requires a specific FR formulation

    Solvent resistance limits for HI100X follow the class-wide behaviour of ABS: aromatic hydrocarbons, ketones, esters, and chlorinated solvents can cause surface softening, swell, and environmental stress cracking under external load. In service temperatures above 60 °C, continuous exposure to cutting oils and some plasticising fluids should be validated because low-molecular-weight additives migrate into the SAN phase and reduce the glass transition temperature. If the part is assembled with metal inserts, an interference fit near a knit line should be avoided unless the specimen has passed a thermal-cycling qualification from −30 °C to 80 °C at 85% RH. Processing with moisture-sensitive polycarbonate residues in the same machine should include full purging because PC degradation can generate carbon dioxide and alter HI100X melt quality. The operational boundary is not solely thermal: screw recovery time must be monitored when regrind fines accumulate in the feed throat, because bridging can create intermittent feed starvation and shift the melt cushion, causing critical dimension drift in downstream assembly.

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