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INEOS Styrolution Luran SAN 338L

    • Product Name: INEOS Styrolution Luran SAN 338L
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 306416
    Polymer Type Styrene Acrylonitrile (SAN) copolymer
    Density 1.08 g/cm³
    Bulk Density 0.65 g/cm³
    Melt Volume Rate 220 C 10 Kg 30 cm³/10 min
    Tensile Modulus 3700 MPa
    Tensile Stress At Yield 75 MPa
    Tensile Strain At Break 3.0%
    Charpy Notched Impact Strength 23 C 3 kJ/m²
    Charpy Unnotched Impact Strength 23 C 15 kJ/m²
    Vicat Softening Temperature B 50 106 °C
    Heat Deflection Temperature 0 45 Mpa 100 °C
    Heat Deflection Temperature 1 8 Mpa 90 °C
    Water Absorption 24 H 0.2%
    Volume Resistivity >10^15 Ω·cm
    Dielectric Constant 1 Mhz 2.9
    Ul 94 Flammability Rating HB
    Mold Shrinkage 0.4–0.7%
    Processing Melt Temperature 230–270 °C
    Processing Mold Temperature 50–80 °C

    As an accredited INEOS Styrolution Luran SAN 338L factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing INEOS Styrolution Luran SAN 338L is packaged in 25 kg bags, 40 bags per pallet (1,000 kg).
    Container Loading (20′ FCL) 20′ FCL dry container loaded with palletized, shrink-wrapped 25 kg bags of INEOS Styrolution Luran SAN 338L, secured for transport.
    Shipping INEOS Styrolution Luran SAN 338L is supplied as styrene-acrylonitrile copolymer pellets in moisture-barrier bags, octabins, or bulk containers. It is not classified as dangerous goods for transport (no UN number). Store dry, cool, and ventilated, away from ignition sources and direct sunlight; use normal industrial hygiene.
    Storage Store INEOS Styrolution Luran SAN 338L in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and strong oxidizing agents. Keep original containers closed to prevent moisture and dust contamination. Avoid excessive stacking and protect bags from damage. Maintain good housekeeping and control static where dust may form.
    Shelf Life INEOS Styrolution Luran SAN 338L has a typical shelf life of 24 months when stored dry, cool, and in unopened packaging.
    Application of INEOS Styrolution Luran SAN 338L

    Cold-flow geometry limits in transparent airless dispenser closures

    Transparent airless dispenser outer shells are produced from Luran SAN 338L where the moulding requires high flow length, low haze, and resistance to cosmetic formulation vapours without polycarbonate pricing or bisphenol-A monomer content. The grade is run in desiccant dryers at 80°C for 2–4 h to reduce residual moisture below 0.10% as measured by ISO 15512; the failure boundary is 0.15%, above which silver streaks and splay appear at the gate. In plants where ambient relative humidity exceeds 60%, drying time is extended to 4–6 h because the amorphous pellet surface adsorbs moisture quickly. Melt temperature is maintained at 235–250°C, and the nozzle zone is controlled at 240–250°C to prevent premature freezing in valve-gate systems. Mould temperature is held between 45°C and 65°C; a polished A1/A2 cavity surface is required for transparent high-gloss parts. Screw geometry on the injection unit is typically a general-purpose single-flight screw with an L/D of 20:1 to 25:1 and a compression ratio of 2.0:1 to 2.5:1. Holding pressure is set at 60–80 MPa as measured at the barrel, and clamp force is calculated at 1.0–1.3 kN/cm² of projected area. A thermal degradation cliff-edge exists above 260°C; nitrile side-group decomposition causes a measurable yellow shift and surface pitting. Colour formulation uses 0.5–2.0 wt% liquid dye or 1–3 wt% pellet concentrate; filler loadings above 3 wt% reduce transparency and increase mould-plate abrasion. Terminal articles include fragrance pump over-caps, cosmetic jar outer covers, lipstick sleeves and clear over-closures. Regulatory assessment for packaging falls under REACH Regulation (EC) No 1907/2006, with SVHC disclosure at 0.1 wt%, and packaging minimisation obligations under Directive 94/62/EC. Articles exposed to cosmetic emulsions are validated for environmental stress-cracking resistance using solvent screening protocols; alcohols above 20% aqueous concentration require part-level validation because SAN can exhibit craze initiation at surface stress concentrations.

    Household appliance control interfaces are moulded in Luran SAN 338L where backlit transparency, dimensional stability under moderate heat, and resistance to domestic cleaning detergents are specified. The application is limited to non-impact components; freezer and refrigerator door inserts, detergent drawer fronts, microwave control lenses and dishwasher indicator windows are produced. Drying follows the same desiccant profile, 80°C for 2–3 h, to a target residual moisture below 0.08%. Melt temperature is set between 225°C and 240°C, slightly lower than cosmetic moulding because appliance parts often have longer flow paths and residence-time exposure in hot-runner manifolds. The hot-runner manifold temperature is limited to 230–250°C; dead-spot stagnation above 260°C is avoided because discolouration appears in transparent lens edges. Mould temperature is controlled at 50–70°C with external thermolators; temperatures below 40°C produce visible flow lines at the gate radius and reduce gloss uniformity. Injection velocity is profiled from 30–60 mm/s at the gate to 80–120 mm/s through the mid-cavity to prevent hesitation marks. Holding pressure is 60–75 MPa and holding time is 8–12 s for wall thickness 1.8–2.5 mm. A pressure transducer near the gate is used to switch from velocity control to pressure control at a cavity pressure of 35–45 MPa. Shrinkage is typically 0.5–0.7% in flow direction and 0.6–0.8% transverse according to ISO 294-4; stringent dimensions on display windows require mould compensation. The Vicat softening temperature by ISO 306 method B50 is approximately 101–106°C, restricting continuous service to below 85°C. Flammability compliance for household appliances is assessed under IEC 60335-1 and UL 94 HB at a minimum thickness of 1.5 mm. The grade does not carry a UL 94 V-0 rating without flame-retardant modification, so it is excluded from proximity to uninsulated live parts. End articles include washing machine detergent drawer fronts, transparent microwave control lenses, dishwasher fascia windows and refrigerator shelf end-caps. Exposure to detergent concentrates and alkaline cleaning fluids is validated on finished parts because internal moulded-in stress governs environmental stress-cracking resistance; a cleaning protocol with 5% sodium carbonate solution at 60°C for 24 h is used as a screening procedure.

    SegmentRegulatory or safety referenceSpecific clause or test methodBoundary condition observed in practice
    Cosmetic packaging outer shellsREACH Regulation (EC) No 1907/2006SVHC disclosure threshold 0.1 wt%No SVHC above threshold declared in supplier SDS
    Household appliance transparent trimIEC 60335-1Subclause 30.2 glow-wire, end-product requirementSAN 338L limited to non-load-bearing, non-enclosure parts unless UL 94 HB at 1.5 mm is accepted
    Food-contact kitchenwareCommission Regulation (EU) No 10/2011; FDA 21 CFR 177.1040EN 1186-1, EN 13130-1, food simulant migrationFinished part must be tested under intended time/temperature; use with >20% ethanol requires validation
    Office machine glazingIEC 62368-1, RoHS Directive 2011/65/EUThermal heat accumulation, mechanical enclosure requirementsNot for outdoor UV exposure; not for safety-critical opaque enclosure flame barriers
    Analytical instrument coversRoHS Directive 2011/65/EU, REACH Regulation (EC) No 1907/2006ISO 10993-5 only where validatedGamma sterilisation above 15–25 kGy not recommended without colour validation
    LED optical diffusersIEC 62471, RoHS Directive 2011/65/EUASTM D1003 haze and transmittanceUV stabiliser required for continuous blue-pump LED exposure

    What Limits Solvent Resistance in Transparent Kitchenware Blender Jars?

    The selection of Luran SAN 338L for transparent blender jars, juicer bowls and coffee bean hoppers is driven by its clarity and resistance to fruit acids, but the conversion is constrained by thick-wall freezing behaviour and impact limitations. A blender jar has a nominal wall section of 4–6 mm, which demands a lower melt temperature of 220–235°C to limit residence-time degradation in front of the screw. The mould temperature is held at 45–55°C; this is a deliberate compromise because higher mould temperature improves surface replication but extends cooling time beyond 30 s. Drying before moulding is performed at 80°C for 3–4 h to reach residual moisture below 0.05%, because thick-wall parts amplify splay defects. The injection profile is staged with a slow initial velocity to prevent jetting at the gate, followed by a rapid fill phase to avoid premature edge freezing; typical fill time for a 1.5 L jar is 2.5–4.0 s. The gate is placed at the base centre with a shielded submarine diameter of 2.0–2.5 mm or a fan gate of 1.5–2.0 mm thickness to encourage plug flow. Holding pressure is 70–85 MPa and holding time is 10–15 s to minimise sink marks at the thread and base intersections. The clamp force is calculated at 1.3–1.6 kN/cm² projected area because thick-wall amorphous parts exert high peak cavity pressures. After demoulding, parts are annealed at 70°C for 30–60 min to reduce moulded-in stress before food-contact validation. Regulatory assessment for food-contact articles follows Commission Regulation (EU) No 10/2011 and FDA 21 CFR 177.1040 for styrene-acrylonitrile copolymers; the finished part must be tested in food simulants, including 10% ethanol and 3% acetic acid, at the intended hot-fill or ambient service temperature. The use limit is governed by impact behaviour, with a notched Charpy impact value of around 2 kJ/m² by ISO 179-1/1eA; blender jars are therefore not suitable for dry-blending ice or frozen fruit under repeated drop-load conditions. Chemical exposure to high-alcohol extracts above 20% ethanol is excluded without part-level stress-cracking validation. End articles include transparent mixing bowls, juice extractor bowls, coffee bean hoppers and spice-grinder transparent chambers.

    Process parameterRecommended bandFailure boundaryObserved defect
    Residual moisture0.05–0.10%>0.15%Silver streaks, splay, gate blush
    Melt temperature230–250°C>260°CYellowing, surface pitting, odour from nitrile degradation
    Mould temperature45–65°C<40°CFlow lines, poor gloss, internal stress
    Holding pressure60–80 MPa<50 MPaSink marks, vacuoles, poor dimensional stability
    Residence time2–5 min>8 minColour shift, molecular weight loss, surface defects

    When Dimensional Stability in Office Machine Glazing Outweighs Impact Toughness

    Office machine glazing and optical window applications specify SAN 338L where flatness, low particulate attraction, and resistance to cleaning wipes are more important than high impact toughness. Scanner document covers, printer output-tray windows, photocopier platen surrounds and control-panel glazing are moulded in wall thicknesses of 2.0–3.0 mm. The process window is narrow because the amorphous melt exhibits a steep viscosity-temperature response; melt temperature is set at 240–250°C, and mould temperature is maintained at 55–65°C with water-fed thermolators to stabilise cooling and minimise differential shrinkage. The injection fill time is kept between 0.8 s and 1.5 s for a flat rectangular part with a projected area of 0.06–0.12 m². Holding pressure is 50–70 MPa, and total cycle time is 35–50 s. The gate is a tab edge gate of 1.0–1.5 mm thickness, or a valve gate for hot-runner versions. Warpage control is critical for scanner cover flatness; local wall thickness variation is held to ±0.1 mm. Shrinkage according to ISO 294-4 is 0.5–0.7% in the flow direction and 0.6–0.8% transverse; the tool is dimensioned with differential shrinkage compensation. Residual stress is assessed with a polariscope; if optical retardation exceeds 100 nm, the part is annealed at 70°C for 60 min. Regulatory compliance is evaluated under IEC 62368-1 for audio/video and information technology equipment and Directive 2011/65/EU on the restriction of hazardous substances. The grade is not UV-stabilised for outdoor use, and impact-limited edge features should not be used for snap-fit latches without generous radii above 1.5 mm because notched impact performance is low. End articles include scanner copier platen surrounds, printer output tray transparent windows, operator panel lenses and document feeder cover windows.

    Analytical instrument housings, cuvette racks and non-patient-contact diagnostic equipment covers are moulded from Luran SAN 338L when clarity, low extractables in dry analytical environments, and resistance to intermittent alcohol cleaning are required. The resin is not selected for blood-contact or implantable applications; if a customer requests cytotoxicity testing under ISO 10993-5, the specific formulation must be validated because published biocompatibility data for this grade is limited. Moulding is performed with a general-purpose single-flight screw of L/D 20:1 to 25:1, melt temperature 230–240°C, and mould temperature 50–60°C. The process is optimised for dimensional control in multi-cavity racks: cavity-to-cavity weight variation is held to ±0.1 g on a 16-cavity tool, and holding pressure is 65–80 MPa. The gate diameter is 0.8–1.2 mm for pin-point gated cuvette racks; jetting is avoided by reducing injection velocity at the start of fill to 20–40 mm/s for the first 0.2–0.4 s. Cycle time for a 2.0–2.5 mm wall section is 25–35 s. The parts must be annealed at 70°C for 30–45 min if they will be exposed to alcohol-based wipes, because SAN 338L can exhibit environmental stress crazing at sharp corners and gate vestiges under repeated strain. Chemical resistance testing uses 70% isopropyl alcohol solution under a fixed-strain jig at 0.5% outer fibre strain for 24 h as a screening method. Compliance is assessed under RoHS Directive 2011/65/EU and REACH Regulation (EC) No 1907/2006. Sterilisation compatibility is limited: ethylene oxide cycles are the preferred method when required, whereas gamma irradiation above 15–25 kGy is not recommended without colour-shift validation because styrenic copolymers tend to yellow. End articles include transparent racks for automated analyser cuvettes, instrument display covers, pipette calibration stand housings and laboratory balance windows.

    Optical diffusion media and LED cover lens performance thresholds

    Light-emitting diode cover lenses, indicator lenses and diffuser plates use Luran SAN 338L as a carrier resin for light-diffusing additives where the application requires neutral light transmission, high surface hardness relative to acrylic, and lower processing temperature than polycarbonate. The compound is prepared with crosslinked PMMA microbeads at 1–3 wt% or with high-molecular-weight silicone powder at 0.3–0.8 wt% to achieve diffuse light distribution without unacceptable total luminous transmittance loss. A UV stabiliser package is added at 0.2–0.4 wt% when the LED source includes a blue-pump peak near 450 nm; the stabiliser is selected from hindered amine and benzotriazole classes supplied as SAN-compatible masterbatch. The base resin is pre-dried at 80°C for 2–3 h to a residual moisture level below 0.08%. Melt temperature is set at 230–250°C, and the hot runner is limited to 240–250°C; the screw is a low-shear general-purpose geometry with compression ratio 2.0:1 to 2.2:1. The mould temperature is held at 50–70°C with polished cavity surfaces to avoid micro-scratches that become visible in transmitted light. The gate design is a fan gate of 1.2–1.8 mm thickness or a hot-runner valve gate with a nozzle orifice of 1.5–2.0 mm. Holding pressure is 55–75 MPa, and total residence time is kept below 5 min because extended thermal exposure shifts yellowness index. Surface roughness of the cavity is specified at SPI A2 or finer; a textured surface at the exit side can be used as an alternative to additive diffusion but increases lamp image visibility. Photometric performance is validated on the final part by total luminous transmittance and haze measurement according to ASTM D1003. End articles include LED indicator lenses, appliance digital display windows, diffuser covers for linear luminaires and backlit control symbols. The product is not a substitute for PMMA in high-UV outdoor luminaires; long-term weatherability requires a co-extruded UV-protective layer or a different polymer.

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    Certification & Compliance
    More Introduction

    Luran SAN 338L is a styrene-acrylonitrile copolymer produced by INEOS Styrolution and positioned as an amorphous, transparent, easy-flow injection-moulding grade within the Luran family. The grade is intended for thin-wall technical parts where melt viscosity, optical clarity, and surface gloss are more decisive than high-energy impact resistance. The standard datasheet does not disclose a numerical acrylonitrile specification but classifies the grade as a medium-acrylonitrile SAN. The product is not automatically covered by a global food-contact statement; converters must obtain a specific compliance letter from the producer for EU Regulation 10/2011 or FDA 21 CFR applications before placing a finished article on the market.

    What Changes in Material Selection When 338L Is Compared with High-Viscosity SAN?

    The first selection variable is melt volume-flow rate. Under ISO 1133-1:2022 at 220 °C/10 kg, Luran SAN 338L is reported in the producer’s published datasheet envelope with a representative value of 29 cm³/10 min. High-viscosity SAN grades used for thicker-walled or impact-resistant mouldings typically report 8–14 cm³/10 min. This difference reduces injection pressure, shortens holding-pressure time, and lowers clamp-force demand in multi-cavity tools. The trade-off is a lower Charpy notched impact strength of 2.0 kJ/m² under ISO 179-1/1eA at 23 °C. If a product specification demands a notched impact value above 2.5 kJ/m², 338L is not the first candidate; a high-viscosity SAN or a clear acrylonitrile-butadiene-styrene grade must be evaluated instead.

    Representative published values for INEOS Styrolution Luran SAN 338L
    PropertyStandardValueUnit
    DensityISO 1183-11.08g/cm³
    Melt volume-flow rateISO 1133-129cm³/10 min
    Tensile modulusISO 527-1/-23600MPa
    Tensile stress at yieldISO 527-1/-272MPa
    Nominal strain at breakISO 527-1/-22.5%
    Charpy notched impact strength at 23 °CISO 179-1/1eA2.0kJ/m²
    Vicat softening temperature B/50ISO 306101°C
    Heat deflection temperature AISO 75-1/-296°C
    Water absorption, saturationISO 620.20%
    Light transmission, 2 mmASTM D100390%
    Moulding shrinkageISO 294-40.4–0.7%

    The table is transcribed from the producer’s current standard datasheet for natural transparent resin and should not be treated as release limits. Lot-specific certificates of analysis control the actual values supplied to a converting site.

    Pellet handling before moulding begins with a dehumidified-air dryer rather than a simple hot-air hopper. The target residual moisture is <0.10%; typical conditions are 80 °C for 2–4 h with a dew point not higher than −18 °C. If the plant ambient relative humidity exceeds 60% or regrind exceeds 30 wt%, drying should be extended because SAN uptake at high humidity can generate silver streaks and surface splay. Barrel setpoints from feed to nozzle are normally profiled between 220 °C and 260 °C; the nozzle is maintained at 250–260 °C and the mould at 40–70 °C. On a reciprocating-screw injection machine with 25 mm screw and L/D 20, medium-to-high injection velocity is used to exploit the shear-thinning response. Back pressure is controlled between 0.5 MPa and 1.5 MPa. Higher back pressure adds shear heating and can discolour the melt during long screw-recovery delays. Shot volume should remain between 50% and 80% of barrel capacity; longer residence at high temperature lowers the effective processing window.

    Runner balancing in multi-cavity tools is critical because the lower melt viscosity of 338L does not compensate for uneven shear heating in the runner system. Shear-induced melt temperature differences of 10–20 °C between inner and outer cavities can shift fill time and cause flash on fast cavities while others remain short. Tooling should use shear-balanced runner cross-sections or a hot runner with individual cavity balancing rather than natural balancing. Cavity pressure sensors are recommended for settings transfer between machines with different screw diameters.

    Lot-to-lot melt viscosity variation is controlled by the producer within the datasheet specification, but regrind history is an additional variable. Under repeated moulding passes, SAN undergoes molecular-weight reduction and viscosity drift; converters running hot-runner tools report that gate-freeze time can change when the regrind fraction exceeds 30 wt%. The gate-freeze test should be performed by incremental hold-pressure staging on the production tool and correlated with part weight under ±0.5% of the filled part mass. This is more reliable than a laboratory melt-flow measurement alone for setting holding-pressure time.

    Mould-Filling Pressure and Gate Design in Thin-Wall Transparent Mouldings

    Transparent SAN parts with wall sections below 1.5 mm require a calculated filling-pressure margin. The apparent viscosity of 338L decreases under injection shear, but the pressure drop across pin gates smaller than 0.8 mm can still exceed available machine pressure. Gate size, gate location, and runner balance are therefore set so that the flow-front velocity at the gate does not exceed the critical value for jetting; for unfilled SAN, a gate velocity above 150 mm/s is often associated with jetting and splay defects in multi-cavity tools. The tool surface should be polished along the flow path because SAN replicates tool finish and any roughness appears as haze. Mould temperature uniformity is held within ±5 °C across the cavity block to avoid differential shrinkage. Published data for 338L-specific weld-line strength reduction is limited, but as a general SAN rule, weld-line strength decreases as melt temperature falls below 240 °C. Weld-line evaluation should follow ISO 527-1/-2 tensile bars moulded with and without interrupted flow.

    Shrinkage anisotropy is a further tool-design constraint. Moulding shrinkage of 0.4–0.7% under ISO 294-4 is directional; lower shrinkage commonly occurs along flow, with higher transverse shrinkage. Rib-to-wall ratio should not exceed 0.6–0.8 because thicker intersections extend cooling time and worsen sink marks. Post-moulding annealing at 70 °C for 2 h reduces residual stress and improves dimensional stability in high-aspect-ratio parts; published data for 338L-specific annealing response is limited.

    For transparent components, haze and yellowing are controlled by the thermal history rather than the grade alone. The light-transmission value of 90% under ASTM D1003 is obtained on a clean, dry material processed with a short thermal history. If the melt is held above 250 °C for longer than 10 min, the yellowness index under ASTM E313 can drift upward, and the part may shift from water-white to slightly yellow. Moulders should purge after every machine stop and avoid overlarge barrels; a barrel capacity below 50% of shot size may also expose the melt to excessive residence time.

    When Hot-Runner Residence Time Approaches the SAN Degradation Envelope

    Hot-runner systems require stricter control than cold-runner tools because melt is held at processing temperature across the entire production window. The producer’s processing guidance for Luran SAN grades limits melt temperature to 260 °C; above this temperature, styrene-acrylonitrile copolymers undergo thermal degradation that appears as yellowing, viscosity drift, and surface degradation. In valve-gated hot runners, the local melt temperature at the gate insert can exceed the barrel setpoint by 10–20 °C during high-speed filling. Therefore, hot-runner zones should be profiled with the gate zone no higher than 260 °C and the manifold at 230–250 °C. Residence time above 250 °C should be kept below 10 min during interruptions; after longer stoppages, the system must be purged with a commercial SAN or GPPS purge compound. Dead spots, sharp transitions, and poorly heated gate tips are the most common causes of black specks in transparent mouldings. Published kinetic data for 338L-specific discolouration is limited.

    Check-ring and screw wear are common process drift sources in unfilled SAN. A worn check ring creates backflow and requires longer screw recovery; on a 25 mm screw, a check-ring clearance above 0.05 mm can make cushion control unstable and create short shots in multi-cavity tools. Preventive maintenance should include measurement of the non-return valve clearance every 250,000 shots or at the first sign of cushion drift. Hot-runner gate-tip heaters should be replaced if the thermocouple reading oscillates more than ±3 °C, because transparent SAN magnifies small gate-temperature differences as stream lines or blush.

    Typical conversions for 338L include transparent housings, cosmetic packaging, office-equipment lenses, domestic-appliance windows, sanitary components, and technical knobs or handles. Chemical resistance to aliphatic hydrocarbons, paraffinic oils, diluted acids, and many household detergents is consistent with the styrene-acrylonitrile polymer class and is assessed under ISO 175 immersion tests; aromatic hydrocarbons, ketones, esters, and chlorinated solvents are excluded because they cause stress cracking or dissolution. The material is not suitable for continuous exposure to hot water above 70 °C under stress, and it is not recommended for thin-wall pipe or sheet extrusion because melt strength is insufficient. Dry blending with colour concentrate should be performed in a low-shear tumble mixer for 10–15 min and fed through a gravimetric dosing unit; high-speed dry blending can generate fines that later appear as surface defects.

    The Substitution Boundary Is Defined by Notched Impact and Heat Distortion

    Compared with glass-fibre-reinforced SAN, 338L retains optical clarity and lower density but exhibits lower modulus and creep resistance. The tensile modulus of 3600 MPa under ISO 527-1/-2 is appropriate for unfilled transparent applications; filled SAN grades are typically above 6000 MPa but are opaque. Compared with high-viscosity Luran SAN grades, 338L fills longer flow paths and reduces clamp-pressure demand but is less tolerant of snap-fit strains and low-temperature impact. If the product must survive repeated snap-fit assembly at 0 °C, a high-viscosity SAN or clear polycarbonate blend is preferred. Compared with ABS, 338L offers transparency and lower density but has lower notched impact strength. The substitutability is therefore limited to applications where the specification sets an ISO 179-1/1eA requirement at or below 2.0 kJ/m² and an HDT/A requirement at or below 96 °C.

    Compliance Verification Matrix for 338L

    The following matrix identifies the relevant regulatory frameworks; it does not replace a supplier declaration for the final article.

    Compliance verification matrix
    Regulation or standardScopeCondition
    REACH (EC) No 1907/2006Polymer registration and SVHC communicationConfirm via current safety data sheet; no SVHC above 0.1% w/w in substance/mixture as supplied is declared.
    RoHS 2011/65/EURestricted substances in homogeneous materialsThe converter must verify final article compliance; the resin does not inherently contain Pb, Hg, Cd, Cr(VI), PBB, or PBDE above the standard thresholds.
    FDA 21 CFR §181.32Styrene-acrylonitrile copolymers for food contactThe standard 338L datasheet does not provide a direct global food-contact statement; a lot-specific supplier letter is required.
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