| HS Code | 760475 |
| Density | 1.18 g/cm³ |
| Melt Flow Rate | 20 g/10 min (220°C/10 kg) |
| Tensile Strength | 50 MPa |
| Elongation At Break | 10% |
| Flexural Strength | 80 MPa |
| Flexural Modulus | 3000 MPa |
| Notched Izod Impact Strength | 15 J/m |
| Rockwell Hardness | R110 |
| Vicat Softening Temperature | 100 °C |
| Heat Deflection Temperature | 80 °C (1.8 MPa) |
| Ul 94 Flammability Rating | V-0 |
| Water Absorption | 0.2% |
| Mold Shrinkage | 0.4-0.7% |
| Dielectric Strength | 25 kV/mm |
| Volume Resistivity | >10^15 ohm·cm |
| Drying Temperature | 80 °C |
| Processing Temperature | 220-260 °C |
As an accredited Kumho Petrochemical SAN 330NI factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Kumho Petrochemical SAN 330NI is packaged in 25 kg net-weight moisture-resistant bags, palletized for safe industrial storage and transport. |
| Container Loading (20′ FCL) | Kumho Petrochemical SAN 330NI is loaded into a 20-foot FCL container under dry conditions, palletized, secured, and sealed for shipment. |
| Shipping | Kumho Petrochemical SAN 330NI is shipped as non-hazardous styrene-acrylonitrile copolymer resin pellets in sealed moisture-barrier bags or octabins. Transport in dry containers/trucks, avoid heat and moisture, and store in a cool, dry, ventilated area with packaging intact. |
| Storage | Store Kumho Petrochemical SAN 330NI in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, sparks, and open flames. Keep original containers tightly closed and palletized to prevent moisture ingress and dust accumulation. Avoid strong oxidizers, practice good housekeeping and static control, and follow local regulations and FIFO stock rotation. |
| Shelf Life | The recommended shelf life is typically two years in original unopened packaging, stored dry and cool away from direct sunlight. |
Clear outer shells for oil-in-water and water-in-oil cream formulations are produced from Kumho Petrochemical SAN 330NI as a direct replacement for general-purpose polystyrene in tools that require higher resistance to aliphatic cream bases and repeated cap tightening torque. The material is introduced at 100 wt% virgin pellet in high-gloss transparent jars and at 85–90 wt% virgin with 10–15 wt% regrind derived from sorted sprues, runners, and hot-runner drops in opaque inner collars or secondary caps. A SAN-carrier colour masterbatch is metered at 1.5–2.5 wt%; masterbatch loadings above 3.0 wt% raise injection-moulded haze from approximately 2.0% to 5.5–6.5% when tested per ASTM D1003-13, so side-feed gravimetric dosing is preferred over hand-mix additions. The moulding process is multi-cavity injection moulding on machines with clamp forces between 5,000 kN and 6,500 kN, reciprocating screw L/D ratios of 20:1–22:1, and non-return ring clearances held below 0.10 mm to prevent melt backflow and short-shot variability. Melt temperature is controlled at 230–250°C, mould temperature at 35–55°C, and holding pressure is profiled from 70% to 90% of peak injection pressure to suppress sink marks at hinge bosses and thread roots. Pre-drying in desiccant dryers at 80°C for 2–4 hours to a residual moisture level of ≤0.05 wt% per ISO 15512:2019 is required when ambient relative humidity exceeds 60%; batches left in open hoppers without drying exhibit splay and silver streaks in hot-runner tools. The relevant compliance assessment includes REACH Regulation (EC) No 1907/2006 substance screening, EU Packaging and Packaging Waste Directive 94/62/EC heavy metal limits with a total cadmium, lead, mercury, and hexavalent chromium sum below 100 mg/kg, and chemical compatibility testing of the moulded article under ISO 175:2010 using emulsion and alcohol-water simulants representative of the finished cosmetic formulation. Terminal finished product types include transparent cream jars, outer caps, lipstick tube casings, compact bases, and fragrance gift-set covers. On production floor data from multi-cavity tools, tunnel gates positioned in non-visible recesses below the base plate reduce gate blush at injection velocities below 45 mm/s; velocity settings above 50 mm/s are associated in high-flow SAN technical bulletins with increased melt-front turbulence, visual weld lines, and reduced clarity at the gate boundary.
Clear sump bodies and filter bowls for point-of-use water treatment systems are moulded from transparent styrene-acrylonitrile copolymer when the housing must retain dimensional stability under intermittent hydrostatic pressure, resist mineral scale accumulation, and avoid stress whitening around threaded ports. For wetted pressure-bearing walls and threads, the polymer is used at 100 wt% virgin; regrind is excluded from these zones because the notch sensitivity of styrenic copolymers concentrates stress at weld lines and thread roots. Regrind may be introduced at ≤5 wt% only into non-wetted overmoulded knobs or external grips, and the recycled fraction must be dried to ≤0.03 wt% moisture before blending. Compliance for potable water contact is evaluated under NSF/ANSI 61 extraction testing, US FDA 21 CFR 177.1040 for acrylonitrile-styrene copolymers, and EU Regulation (EU) No 10/2011 with the overall migration limit of 10 mg/dm². Structural acceptance uses tensile yield strength measured per ASTM D638-14 and flexural modulus per ASTM D790-17 on dry-as-moulded specimens; hydrostatic burst validation is performed on complete housings after 1,000 h water contact at 23°C and after thermal cycling from 5°C to 45°C. The downstream production process is injection moulding with sequential valve-gated hot-runner manifolds, screw L/D of 20:1, shot size maintained between 30% and 70% of barrel capacity, melt temperature 240–255°C, and mould temperature 50–70°C to reduce residual orientation. Threads are formed by unscrewing cores or collapsible cores rather than thread splits to avoid flash at the sealing shoulder; hydraulic core pulls and position monitoring prevent mould damage during ejection. A 1.2 kg filter bowl in a 2,500 kN machine typically cycles at 60–90 s, with cooling time limited by the thickest thread boss rather than the bowl sidewall. Terminal finished products are clear filter sumps, replacement bowls for under-sink and countertop filtration units, and transparent housings for low-pressure point-of-use systems. SAN 330NI is not specified for continuous service above 70°C or for hot-water pressure vessels; polysulfone or polyamide 66 is required in those conditions. Assembly adhesives containing ketones, esters, or aromatic hydrocarbons are incompatible with SAN under hoop stress and cause environmental stress cracking in threaded regions, particularly when thread engagement torque exceeds 10 N·m on 50 mm diameter closures.
Transparent blender jars, juicer bowls, and refrigerator crisper drawers are moulded from SAN 330NI when food-contact clarity must be retained after repeated dishwasher exposure and low-temperature impact against ice or frozen fruit. The recommended formulation for a clear blender jar is 100 wt% virgin resin; regrind is limited to ≤10 wt% in transparent sidewalls and ≤20 wt% in opaque base adapters, provided the notched Izod impact strength measured per ASTM D256-10 remains within the supplier specification for the virgin lot. A food-contact-approved colour masterbatch is added at 1.0–2.0 wt% only when tinted jars are specified; pigments that increase haze above 4.0% per ASTM D1003-13 are rejected for transparent bowls. The production process is thick-wall injection moulding with wall sections between 4 mm and 6 mm, melt temperature 230–250°C, mould temperature 40–60°C, and valve-gated hot runner systems to eliminate sprue vestiges on the bowl interior. Screw L/D ratios of 20:1 with a compression ratio of 2.0–2.5:1 are used; shot weights are kept between 40% and 60% of barrel capacity to reduce residence time and yellowing. Post-mould annealing at 70–80°C for 1–2 hours reduces residual stress around thick bosses and thread starts, which is critical for blender jar bases where impact loads concentrate at transition radii. The terminal finished product types include clear blender jars, extractor bowls, coffee machine water reservoirs, refrigerator crisper drawers, and transparent storage containers for small household appliances. Compliance for repeated food contact requires US FDA 21 CFR 177.1040, EU Regulation (EU) No 10/2011, and GB 4806.7-2023 for plastic food-contact materials; appliance-level safety is evaluated under IEC 60335-1:2020. Operational boundaries are defined by the combination of low temperature impact and dishwashing chemistry: SAN 330NI is not microwave-safe and should not be exposed to dishwasher drying cycles above 65°C for extended periods because repeated thermal shock after aggressive detergent contact can initiate microcracks at gate vestiges and weld lines.
Trigger sprayer bodies, lotion pump closures, and dispensing heads for household and personal care liquids are moulded from SAN 330NI because the acrylonitrile component increases resistance to aqueous surfactant solutions and diluted glycol ether solvents compared with polystyrene. The resin is used at 100 wt% virgin in the primary chemical-contact body and nozzle housing; regrind is restricted to ≤10 wt% in non-contact external shrouds, colour-matched overmouldings, or dust caps. Colour concentrate based on a styrene-acrylonitrile carrier is metered at 1.5–2.0 wt% for opaque grades, while transparent sprayer bodies are processed without pigment to maintain visual inspection clarity. The downstream process is multi-cavity injection moulding on hot-runner tools with valve-gate control, melt temperature 235–250°C, mould temperature 40–60°C, and holding pressure maintained until gate freeze to prevent dimensional drift in snap-fit closure skirts. Screw L/D is typically 20:1 with a non-return ring clearance below 0.10 mm; injection speed is profiled to prevent jetting in elongated nozzle sections. Terminal finished product types include trigger sprayer bodies, lotion pump bases, dispensing caps, overcaps, and aerosol collar components. Compliance is assessed under REACH Regulation (EC) No 1907/2006, EU Packaging and Packaging Waste Directive 94/62/EC, and the heavy metal limits of 100 mg/kg total for lead, cadmium, mercury, and hexavalent chromium. Solvent compatibility is validated by immersion testing per ISO 175:2010 in representative surfactant systems containing 1–5 wt% non-ionic surfactant and 0.5–2.0 wt% glycol ether. The operational boundary is sharply defined: continuous contact with concentrated esters, ketones, or aromatic hydrocarbon-based cleaning solvents is not recommended because these media plasticise the SAN matrix and reduce hoop stress retention in threaded closure seals. Published data for this specific grade under aggressive solvent immersion is limited; each cleaning formulation should be tested in the finished closure geometry rather than on generic tensile bars.
| Production environment | Drying parameters | Residual moisture limit | Permitted regrind | Critical reference standard |
|---|---|---|---|---|
| Cosmetic packaging | 80°C 2–4 h | ≤0.05 wt% | ≤15 wt% in non-clarity zones | ISO 15512:2019 |
| Water filter housing | 80°C 4–6 h | ≤0.03 wt% | ≤5 wt% non-wetted only | NSF/ANSI 61 |
| Blender jar | 80°C 3–4 h | ≤0.05 wt% | ≤10 wt% transparent sidewall, ≤20 wt% opaque base | FDA 21 CFR 177.1040 |
| Trigger sprayer | 80°C 4 h | ≤0.04 wt% | ≤10 wt% non-contact | REACH (EC) No 1907/2006 |
| Food-contact tumbler | 80°C 2–3 h | ≤0.05 wt% | ≤20 wt% sorted regrind | EU No 10/2011 |
| Display glazing | 80°C 2–4 h | ≤0.05 wt% | ≤10 wt% non-visual ribs | UL 94 HB |
Two-piece transparent tumblers, salad bowls, and refrigerator storage containers are injection moulded from SAN 330NI when the part must resist staining from tomato oil, tea, coffee, and citrus juices while maintaining glass-like clarity at ambient food-service temperatures. The body is moulded at 100 wt% virgin resin for visible surfaces; sorted regrind from sprues and rejected pre-colour parts is added at ≤20 wt% in opaque bases, foot rings, or outer shells only after drying to ≤0.05 wt% moisture. Food-contact colour masterbatch is metered at 1.5–2.0 wt% in tinted versions, but transparent tumblers are typically produced without masterbatch to hold total luminous transmittance above 88% per ASTM D1003-13. The downstream process is high-cavitation injection moulding on stack moulds with 32–64 cavities, melt temperature 230–250°C, mould temperature 40–50°C, and cycle times between 15 s and 25 s depending on wall thickness and stack layout. Ejector pins are positioned in non-visual base rims to avoid push marks on the transparent sidewall; polishing of cavity surfaces to SPI A-1 finish is required for acceptable gloss. Terminal finished product types include stackable drinkware, serving bowls, refrigerator storage boxes, and clear compartments for domestic water dispensers. Compliance for food contact is based on US FDA 21 CFR 177.1040, EU Regulation (EU) No 10/2011, and GB 4806.7-2023; the product is not approved for microwave reheating or for continuous dishwasher drying above 65°C because repeated hot-air drying after alkaline detergent exposure can produce microcracking around injection gate remnants. Published data for SAN 330NI under repeated domestic dishwasher cycles is limited; processors supplying retail kitchenware typically validate one year of cyclical dishwasher simulation on production tooling before release.
SAN 330NI is selected for indoor point-of-sale display panels, audio equipment dust covers, vending machine display windows, and transparent electronics housings where impact load is low and PMMA price or processing stability is not acceptable. The compound is processed at 100 wt% virgin resin with 1.0–2.0 wt% antistatic masterbatch to reduce dust attraction on display surfaces; regrind is limited to ≤10 wt% in non-visual structural ribs or rear mounting bosses. Injection moulding is performed on polished cavity surfaces with surface roughness below Ra 0.05 µm, melt temperature 230–250°C, mould temperature 60–80°C, and low-to-moderate injection velocity to avoid silver streaks and flow lines across large flat windows. Hot-runner valve gates are positioned at the edge of the visible face, and holding pressure is ramped downward before gate freeze to prevent birefringence at the gate boundary. Terminal finished product types include transparent display glazing, dust covers for audio and laboratory instruments, vending machine front panels, and clear covers for low-voltage electrical enclosures. Compliance is assessed under UL 94 HB flammability classification, RoHS Directive 2011/65/EU, IEC 62368-1:2023 for audio/video and ICT equipment enclosures, and REACH Regulation (EC) No 1907/2006. The operational boundary is defined by surface durability: SAN 330NI does not match PMMA in Taber haze retention after 100 cycles under ASTM D4060-19, and it is not recommended for outdoor display glazing where ultraviolet exposure and windborne abrasion are continuous. Published comparative abrasion data for this specific grade under ASTM D4060-19 is limited; PMMA remains the reference material for high-clarity display applications requiring the lowest possible Taber haze increase.
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Kumho Petrochemical SAN 330NI is an unfilled, amorphous styrene-acrylonitrile copolymer supplied in natural pellet form for injection molding of transparent and opaque technical parts. The product belongs to the producer’s SAN 300 series; the 330 designation identifies an injection-class material, and the NI suffix is used in producer nomenclature for natural-color injection feedstock. Published compositional studies for commercial injection-grade SAN place the acrylonitrile weight fraction in the range 24–28%; this comonomer content increases resistance to aliphatic hydrocarbon oils, dilute acids, and alkaline cleaners relative to general-purpose polystyrene while retaining the dimensional stability of an amorphous styrenic resin. The amorphous character of SAN 330NI eliminates crystalline spherulitic haze and produces isotropic shrinkage, but it also means the polymer solidifies by vitrification rather than crystallization; therefore mold cooling time is controlled by glass transition rather than crystallization half-time. The glass transition temperature of commercial SAN is generally reported between 105°C and 110°C by differential scanning calorimetry or dynamic mechanical analysis. This thermal position supports higher service temperature than GPPS but imposes a higher mold temperature requirement. Grade-specific certificate-of-analysis values are reported under ISO 1133-1:2022 for melt mass-flow rate, ISO 527-2 for tensile stress, ISO 178 for flexural modulus, ISO 75-2 for heat deflection temperature, and ISO 1183 for density. Unfilled SAN mold shrinkage is typically 0.4–0.7% when measured in accordance with ISO 294-4 after 24 h, and lot-specific molecular-weight distribution can shift the balance between flow length and environmental stress-crack resistance.
The melt-flow position of SAN 330NI is typically higher than that of an extrusion-oriented SAN, which reduces injection pressure in thin-wall cavity layouts. Representative values for injection-optimized unfilled SAN grades are published in the region of 20–30 g/10 min under ISO 1133-1:2022 at 220°C and 10 kg; the exact producer lot value may be set within or near that band and must be obtained from the supplier’s current technical data sheet. Capillary viscometry of SAN shows pseudoplastic behavior with a power-law index commonly between 0.30 and 0.45 at shear rates from 102 s−1 to 104 s−1; filling pressure therefore rises less than proportionally with injection speed, and single-point melt mass-flow rate alone is insufficient to predict molding pressure on a multi-cavity hot-runner tool. In mold-filling simulation, a Cross-WLF or power-law model should be fitted to capillary data rather than using only melt mass-flow rate. For SAN melts, time-temperature superposition is often described by William-Landel-Ferry coefficients; commercial simulation packages accept viscosity coefficients in that form. If no 330NI-specific Cross-WLF coefficients are available, generic high-flow SAN coefficients should be calibrated with short-shot studies on the production tool.
Drying is governed by residual moisture threshold rather than fixed time alone. Although SAN absorbs less water than ABS, moisture levels above 0.05–0.10% by weight can hydrolyze nitrile groups at melt temperatures above 240°C, producing surface splay, haze, and reduced optical clarity. Water absorption of unfilled SAN after 24 h immersion at 23°C is typically 0.2–0.3% under ISO 62; regrind from humid storage can therefore carry more moisture than virgin pellets. A desiccant hopper dryer with delivered-air dew point at or below -30°C is standard. Pellets exposed to relative humidity greater than 60% typically require 2–4 h pre-drying at 80°C; longer drying is permissible if the manufacturer’s specified maximum temperature is not exceeded. Lot-specific residual moisture should be verified with an automatic Karl Fischer moisture analyzer rather than inferred from storage time alone, especially when recycle content exceeds 20% by weight.
On a servo-hydraulic injection machine with 1,800 kN clamp force and a 25 mm diameter barrier screw having L/D 20:1, melt temperature is normally controlled between 230°C and 250°C, and mold temperature is set between 45°C and 65°C. The injection profile is adjusted to keep flow-front velocity in 1.2–2.0 mm wall sections within 200–350 mm/s; lower velocities can produce flow lines, while higher velocities may generate jetting and gate blush. Barrel residence time above 250°C should be kept below 10–15 min to limit thermo-oxidative yellowing, although producer-specific yellowing kinetics for SAN 330NI are not fully published and must be confirmed during production-scale purging trials. Hot-runner manifolds should avoid dead spots, and any color masterbatch should be polymer-compatible to reduce light-scattering inclusions when optical parts are inspected under ASTM D1003 haze measurement. A two-plate cold-runner mold with cavity pressure sensors is preferable for qualification; cavity pressure at the end of fill should be kept below 60–80 MPa for semi-transparent parts to reduce molded-in stress and orientation birefringence. Gate dimensions should be adjusted so that gate freeze-off occurs after hold pressure has compensated for volumetric shrinkage; typical edge-gate diameter in a 2.0 mm wall is 0.8–1.2 mm. Vent depth for SAN is usually 0.02–0.03 mm; insufficient venting can produce burn streaks and mold deposit. If hot runners are used, externally heated manifolds with thermal uniformity of ±5°C across the nozzle tip are recommended because local overheating above 260°C accelerates yellowing and can create black specks even when the barrel setpoint is lower.
Substitution of GPPS with SAN 330NI in transparent enclosures is usually evaluated when the part contacts aliphatic oils, dilute acids, alkaline cleaning agents, or short-term ethanol during service. Under ASTM D1003, unfilled GPPS typically transmits 89–91% visible light through a 3.0 mm plaque, while SAN injection grades typically transmit 88–90%; the small transmission difference is offset by higher mechanical strength. Tensile strength of unfilled SAN is commonly 60–75 MPa under ISO 527-2, compared with 40–60 MPa for GPPS. Heat deflection temperature under ISO 75-2 method A at 1.82 MPa is typically 95–100°C for SAN injection grades and 75–85°C for GPPS.
The conversion from GPPS is not a drop-in substitution because melt viscosity is higher and the thermal diffusivity through the solidified layer differs. Tooling developed for GPPS with wall thickness below 1.0 mm may require increased gate diameter, revised runner balance, or additional mold cooling before SAN 330NI can be qualified. Capillary rheometry under ISO 11443 should be compared with the existing mold-filling simulation; if the available simulation database does not contain grade-specific 330NI viscosity, a measured shear-viscosity curve across 100–10,000 s−1 is required. Published data for this exact grade-simulation configuration is limited. Optical haze is influenced by gel particles and unconverted monomer residues; transparent parts should therefore be molded with controlled residence time and measured after 24 h conditioning at 23°C and 50% relative humidity under ASTM D1003 because moisture uptake can produce a temporary haze bloom in thin plaques.
SAN is attacked by concentrated oxidizing acids, ketones such as acetone and methyl ethyl ketone, esters, chlorinated solvents, and aromatic hydrocarbons such as toluene; these media can produce swelling, haze, or sudden environmental stress cracking under molded-in stress. The 330NI grade should not be selected for continuous contact with such solvents unless the final part is tested under the intended stress state. Environmental stress-cracking resistance is assessed using bent-strip methods derived from ISO 22088-2 or tensile-creep methods under ISO 22088-1; a reagent that is aggressive to GPPS is often less aggressive to SAN because the acrylonitrile phase reduces solvent uptake, but this advantage narrows at elevated temperature and in thick sections with high residual stress. The environmental stress-cracking mechanism in SAN involves solvent diffusion into the surface layer, plasticization, and craze initiation at stress concentrations such as weld lines, sharp corners, or over-tightened inserts. Molding conditions that reduce molecular orientation and frozen-in stress therefore improve chemical resistance even without changing the base resin; the same 330NI part may pass a chemical rub test when molded with high mold temperature and adequate packing pressure but fail when molded at low mold temperature and short hold. Chemical resistance data from a neat resin plaque does not automatically apply to a molded part with orientation and weld lines.
Repeated contact with isopropanol or ethanol is tolerated better by SAN than by GPPS, although amorphous polyamide or polycarbonate remains more resistant. For UV-exposed service, unpigmented natural 330NI requires a UV absorber package matched to wall thickness; accelerated weathering is normally measured under ASTM D4459 or ISO 4892-2. Purging before processing should eliminate polyacetal or PVC residues because their acidic decomposition products can catalyze chain scission and generate surface defects.
The table below summarizes representative published ranges for unfilled injection grades; these are not lot-specific acceptance limits and must be checked against the producer’s certificate of analysis for the actual shipment.
| Property / standard | Unfilled injection SAN class | GPPS | ABS |
|---|---|---|---|
| Tensile strength at 23°C, ISO 527-2 | 60–75 MPa | 40–60 MPa | 35–50 MPa |
| Tensile modulus, ISO 527-2 | 3.3–3.8 GPa | 3.0–3.5 GPa | 2.0–2.5 GPa |
| Notched Izod impact, ISO 180/1A | 1.5–2.5 kJ/m² | 1.0–2.0 kJ/m² | 10–25 kJ/m² |
| Heat deflection temperature at 1.82 MPa, ISO 75-2 | 95–100°C | 75–85°C | 85–105°C |
| Light transmittance, 3.0 mm plaque, ASTM D1003 | 88–90% | 89–91% | opaque to translucent |
Compared with a lower-flow general-purpose SAN grade, 330NI is positioned to favor shorter filling time and lower hydraulic pressure, while notched impact may be slightly lower due to reduced molecular weight. Compared with ABS, SAN 330NI offers higher transparency and usually lower part density, but it does not provide the low-temperature impact resistance or ductility of the polybutadiene phase; under ISO 180/1A, a specification requiring notched Izod impact above 10 kJ/m² at -30°C should be directed away from SAN. Compared with GPPS, the SAN grade provides better resistance to oils and dilute reagents, but it requires more rigorous drying and higher processing temperature. These comparisons are only valid when test specimens are prepared under identical conditions per ISO 294-1 and conditioned according to the relevant ISO test method before mechanical loading.
Compliance documentation for Kumho Petrochemical SAN 330NI normally addresses EU REACH registration and candidate-list screening, RoHS Directive 2011/65/EU Annex II heavy-metal restrictions, and may include statements on persistent organic pollutants. The following matrix identifies the minimum lot-verification points for incoming quality control.
| Assessment area | Standard/regulation | Data source |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 | Lot certificate of analysis |
| Tensile and flexural properties | ISO 527-2 / ISO 178 | Producer technical data sheet |
| Heat deflection temperature | ISO 75-2 | Producer technical data sheet |
| Optical transmittance and haze | ASTM D1003 | Internal molded plaque test |
| Density and water absorption | ISO 1183 / ISO 62 | Producer technical data sheet |
| RoHS restricted substances | Directive 2011/65/EU Annex II | Supplier declaration |
| REACH candidate-list screening | Regulation (EC) No 1907/2006 | Supplier declaration |
Food-contact and medical use are not assumed; specific migration limits under EU Regulation (EU) No 10/2011 or FDA 21 CFR sections applicable to styrene-acrylonitrile copolymers must be verified for the final compounded and colored article. For electrical enclosure applications requiring comparative tracking index, testing under IEC 60112 should be performed on the final colored compound because additives can alter surface tracking resistance. The unfilled 330NI resin is not inherently flame retardant; a UL 94 rating above HB requires a qualified flame-retardant compounded version, and long-term heat aging is evaluated under UL 746B or IEC 60216. The producer’s safety datasheet should be reviewed for decomposition products formed during purging and for workplace exposure limits to residual monomers. Lot-to-lot melt-flow drift greater than 10% from the qualified baseline can require barrel-temperature or injection-speed adjustment; color measurements for transparent parts are typically performed on molded plaques under D65 illumination and 10° observer geometry using ASTM E313 yellowness index. Any production-scale substitution of regrind should be validated for optical haze shift because thermal history accumulates during multiple resin dryings.