| HS Code | 885661 |
| Product | LG Chem SAN S80HFICELLHK |
| Material Type | Styrene Acrylonitrile (SAN) |
| Grade | S80HFICELLHK |
| Density | 1.06 g/cm³ |
| Melt Flow Rate | 8 g/10 min at 220°C/10 kg |
| Tensile Strength At Yield | 70 MPa |
| Tensile Elongation At Yield | 3.0% |
| Flexural Modulus | 3300 MPa |
| Notched Izod Impact Strength | 1.5 kJ/m² at 23°C |
| Vicat Softening Temperature | 106°C |
| Heat Deflection Temperature | 85°C at 1.82 MPa |
| Rockwell Hardness | M80 |
| Light Transmittance | 90% |
| Haze | 1.0% |
| Mold Shrinkage | 0.4-0.7% |
| Dielectric Constant | 2.8 at 1 MHz |
| Volume Resistivity | 1E15 ohm·cm |
| Flammability Rating | HB |
As an accredited LG Chem SAN S80HFICELLHK factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg moisture-resistant paper bags, 40 bags per pallet, totaling 1,000 kg net. |
| Container Loading (20′ FCL) | LG Chem SAN S80HFICELLHK chemical is packed in 25 kg bags, palletized, and loaded into a sealed 20-foot FCL container for export. |
| Shipping | LG Chem SAN S80HFICELLHK is a styrene-acrylonitrile copolymer in solid pellet form, non-hazardous and not regulated for transport. It is shipped in moisture-barrier bags or octabins by standard truck/container, kept dry and away from direct heat. |
| Storage | Store LG Chem SAN S80HFICELLHK in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers tightly closed to prevent moisture and contamination. Avoid dust generation and prolonged UV exposure. Use first-in, first-out rotation, bond/ground handling equipment as needed, and follow local regulations and the SDS. |
| Shelf Life | LG Chem SAN S80HFICELLHK typically has a 24-month shelf life when stored cool, dry, and protected from moisture and sunlight. |
A high-flow styrene-acrylonitrile copolymer grade such as LG Chem SAN S80HFICELLHK is introduced into cosmetic-packaging production primarily where sidewall sections fall below 1.2 mm, where multi-cavity flow-length-to-wall-thickness ratios exceed 180:1, and where screw-thread or snap-fit features demand repeated assembly. Melt-flow characterisation is performed to ISO 1133-1:2022 at 220 °C and 10 kg; the lot-specific MFR certificate must be checked because high-flow SAN grades in this class can vary from 25 g/10 min to 35 g/10 min, and a single hot-runner nozzle setting cannot compensate for that range. The relevant packaging-compliance framework is not the food-contact migration regime but the finished-article safety envelope under Regulation (EC) No 1223/2009, which requires that the packaging material does not transfer constituents that degrade the cosmetic formulation or cause sensitisation, together with REACH Annex XVII restrictions for residual monomers and processing aids, and ISO 22716:2007 for manufacturing hygiene. The formulation is set at 97.5–98.5 wt% virgin high-flow SAN, with a cosmetic-grade colour masterbatch at 1.5–2.0 wt% and an external mould-release additive at 0.2–0.5 wt%; regrind is limited to 10 wt% from the same production lot because wider regrind inclusion lowers thermal stability and increases black speck formation in transparent parts. At the injection-moulding stage, the material is dried in a desiccant hopper dryer with a dew point of −30 °C to −40 °C at 80 °C for 3–4 h, and residual moisture is verified below 0.05 wt% before barrel entry. Barrel temperatures are profiled from 210 °C in the rear zone to 235–250 °C at the nozzle, while the mould is held at 50–70 °C; raising mould temperature above 75 °C reduces frozen-in orientation but can extend cooling time by 20–30% on 1.2 mm shells and generate sink opposite thick thread profiles or hinge bosses. Injection speed is typically 60–120 mm/s, with pack pressure between 40 MPa and 70 MPa and a back pressure below 5 MPa to prevent additive exudation. The dominant process conflict is environmental stress cracking resistance against ester-based cosmetic formulations, especially isopropyl myristate and octyl palmitate; high injection speed improves minor-flow reproduction in thin ribs but increases residual hoop stress at gate areas. To prevent stress cracking, gates are positioned away from snap-fit undercuts and thread roots, and post-mould storage is maintained at 25 °C for at least 24 h before torque, drop-tension, or thermal-shock testing. Ketone-based wipe solvents must not be used on finished parts because acetone and methyl ethyl ketone promote crazing in SAN. Terminal product categories are lipstick inner shells and outer caps, compact powder trays, screw-thread cosmetic jars, mascara wand handles and closure rings.
In transparent refrigeration and kitchenware components, the use of high-flow SAN is constrained less by melt viscosity than by the interaction between regrind content and overall migration testing. For food-contact articles intended for repeated contact with aqueous, acidic and fatty foods, the relevant compliance chain begins with 21 CFR 177.1040 for styrene-acrylonitrile copolymers when supplied under a food-contact-grade certification, continues through Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm², and includes GB 4806.7-2016 for articles placed on the Chinese market. Production formulation is run at 80–90 wt% virgin SAN plus 10–20 wt% closed-loop regrind from in-house runners, because external post-consumer SAN is excluded due to unknown additive content and the risk that migration limits cannot be upheld; the regrind is ground to a particle size of 3–5 mm and dosed gravimetrically with a tolerance of ±0.5 wt%. Food-contact colour masterbatch is added only at 1.5–3.0 wt% and must comply with 21 CFR 178.3297 for colorants and EU 10/2011 compositional requirements; low-molecular-weight lubricants and antistatic agents are excluded from this application unless migration evaluation demonstrates finished-article compliance. The downstream process is injection moulding of 2.5–4.0 mm thick parts such as refrigerator drawers and blender jars, using a melt temperature of 230–245 °C, a mould temperature of 45–60 °C, and a general-purpose screw with a compression ratio of 2.0:1 to 2.6:1. Vent depths are maintained between 0.02 mm and 0.03 mm to allow gas escape without flash; insufficient venting causes burning at the flow front and visible yellow streaks in transparent sections. Terminal products are refrigerator crisper trays, salad bowls, measuring cups, blender containers and coffee-grinder bowls. Published data for this specific high-flow grade in fatty-food migration tests is limited; therefore, migration validation is performed per finished-article geometry under EU 10/2011 Annex III and 21 CFR 177.1040 end-test protocols rather than extrapolated from resin-lot MFR certificates.
| Region | Standard or Regulation | Test Condition | Limit or Criterion |
|---|---|---|---|
| United States | 21 CFR 177.1040 | Finished article migration testing with food simulants | Compliance with applicable end-use extraction limits |
| European Union | Regulation (EU) No 10/2011 | Overall migration, aqueous/acidic/fatty simulants | 10 mg/dm² |
| China | GB 4806.7-2016 | Overall migration and residual monomer testing | Conformity with standard-specific limits |
| North America | NSF/ANSI 51 | Food equipment material evaluation | Material formulation and extraction compliance |
Point-of-use drinking water filtration systems place transparent styrene-acrylonitrile copolymer parts in sustained hydrostatic contact with chlorinated water; the dominant failure mode is not thermal distortion but circumferential weld-line splitting in threaded bowl geometries after repeated pressure cycles. The applicable standards are NSF/ANSI 61 for health effects of drinking water system components, NSF/ANSI 42 for aesthetic effects, and Directive (EU) 2020/2184 for materials in contact with water intended for human consumption in European installations. The moulding formulation is held at 100 wt% virgin high-flow SAN; no external release agent, anti-fog additive, or colour masterbatch is introduced unless pre-validated for drinking-water contact under NSF/ANSI 61, and if colour is required, drinking-water-grade masterbatch is limited to 2.0 wt% maximum. Injection moulding of transparent filter bowls and sumps is performed with wall thicknesses of 3–5 mm, a melt temperature of 230–240 °C, a mould temperature of 50–65 °C, and sequential valve gating to position weld lines away from O-ring grooves and thread roots. Post-mould annealing at 70 °C for 1 h reduces internal stress before hydrostatic cycling; the finished housing is then subjected to cyclic pressure between 0 bar and 6 bar for at least 100,000 cycles. Published cyclic test data for this specific grade in 6-bar water-filter housings is limited; the stated cycle condition derives from published SAN weld-line strength and hydrostatic pressure-test practice rather than a part-specific certification for the exact LG Chem grade. Terminal products are transparent filter sumps, reverse-osmosis storage tank heads, brine well caps, manifold covers and water softener control-valve housings.
For domestic appliance transparent parts, the production problem is balancing high-speed injection economics against optical clarity, detergent resistance, and dimensional stability at continuous operating temperatures between 40 °C and 65 °C. The compliance baseline is IEC 60335-1:2020 for general household appliance safety, IEC 60335-2-2:2022 for vacuum cleaner requirements, and UL 94 HB for horizontal burn classification of thin sections; colourfastness and detergent resistance are verified to ISO 4892-2:2013 for xenon-arc exposure where parts are visible in service. The formulation is 85–100 wt% virgin high-flow SAN, with in-house regrind limited to 15 wt% from the same appliance production programme; colour masterbatch is added at 2–3 wt%, and a UV absorber package is introduced at 0.2–0.5 wt% only for components exposed to sunlight or high-intensity retail lighting. Moulding is performed on hydraulic or hybrid machines with screw diameters of 30–50 mm, melt temperatures of 235–245 °C, and mould temperatures of 55–80 °C. Injection speed is set between 80 mm/s and 150 mm/s to reproduce optically polished surfaces, with pack pressure maintained at 40–70 MPa for 2–4 s per 2.5 mm wall thickness. The ejection temperature is held below 65 °C; premature ejection above 70 °C leads to claw deformation in vacuum dust-cup engagement ribs and ovality in steam-iron tank threads. Post-mould annealing at 65 °C for 1 h is used for clear tanks and dust cups before ultrasonic welding or screw-cap assembly. Terminal product categories include transparent vacuum cleaner dust cups, steam-iron water tanks, washing machine detergent drawers, and refrigerator door bins where chemical resistance to cleaning formulations is required.
Unlike cosmetic-packaging mouldings, personal-care attachment parts are subjected to intermittent heat pulses, high humidity, and periodic cleaning with ethanol, isopropanol, or hair-conditioning residues. The compliance framework is IEC 60335-2-23:2019 for skin and hair care appliances, RoHS Directive 2011/65/EU as amended by (EU) 2015/863 for restricted substances, and ISO 4892-3:2016 for accelerated ageing under artificial weathering. The injection formulation is approximately 98–100 wt% high-flow SAN, with colour masterbatch at 0.5–1.5 wt% and no impact modifier because impact-modifier addition above 2.0 wt% reduces transparency below the optical acceptance limit for clear diffusers. Moulding uses a melt temperature of 230–250 °C, a mould temperature of 50–70 °C, and wall thicknesses of 1.5–2.5 mm; texture is applied to cavity surfaces where surface scratching is a field-return issue. Terminal products are hair dryer diffuser nozzles, curling-iron handles, electric shaver body shells and transparent storage caps for personal-care devices.
Transparent covers and windows in electrical measurement equipment use high-flow SAN where polycarbonate would add unnecessary cost and where the service environment is indoor and below 50 °C. The governing safety and materials framework is IEC 62368-1:2018 for audio/video and information technology equipment, RoHS Directive 2011/65/EU, and ASTM D638-22 for tensile property verification on moulded specimens; surface scratch resistance is assessed to ISO 1518-1:2019. The moulding formulation contains 98.5–99.5 wt% virgin high-flow SAN and 0.5–1.5 wt% antistatic or colour masterbatch, with the antistatic package required only where dust accumulation on transparent windows would obscure indicator LEDs. Injection moulding is performed on a 25–40 mm screw with a compression ratio of 2.0:1 to 2.5:1, melt temperature of 230–245 °C, mould temperature of 50–65 °C, and optically polished mould steel with SPI A-1 finish. The ejection temperature is held below 65 °C because hot ejection above that threshold creates micro-ripples on flat optical surfaces and increases birefringence under polarised light inspection. Terminal products are energy meter covers, circuit breaker windows, test instrument display screens and thermostat cover lenses.
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Within the styrenic polymer portfolio supplied by LG Chem, the grade designation LG Chem SAN S80HFICELLHK identifies a high-flow acrylonitrile–styrene random copolymer supplied as cylindrical pellets for thin-wall injection moulding. The material is an amorphous copolymer with a density in the range 1.07–1.08 g/cm³ when measured to ISO 1183-1:2019. The product differs from general-purpose SAN grades by a rheology package that lowers melt pressure loss in restricted gates and by a stabilisation/release system configured for high-cavitation tooling. The exact sub-designation carries application-specific documentation; published data for this specific configuration is limited, and the values below are read from the S80 SAN family as comparative bands rather than guaranteed specification limits. The material should not be assumed to carry universal food-contact or medical approval. Where regulatory status is required, the finished article must be evaluated under EU 10/2011, FDA 21 CFR 177.1640, or the relevant regional standard, including the effect of masterbatch, regrind, and surface coating.
Typical mechanical response for the high-flow S80 family falls within a tensile stress at yield of 66–72 MPa under ISO 527-2:2012, flexural modulus of 3,300–3,700 MPa under ISO 178:2019, Charpy notched impact of 2.0–2.5 kJ/m² under ISO 179-1:2010, and Vicat softening temperature of 104–108°C under ISO 306:2022 method B50. Heat deflection temperature under 1.8 MPa load is expected in the range 86–90°C under ISO 75-2:2013 method A. These bands are intended for material selection, not for drawing-level guarantees.
The processing window is bounded primarily by melt temperature, residence time, and shear heating. A nozzle melt temperature of 210–240°C is generally applicable. Mould surface temperature is typically maintained at 30–60°C; the lower portion is used for cycle-time-sensitive packaging and housings, while the upper portion reduces visible flow marks and improves dimensional precision. For sections below 0.8 mm, melt temperature must not be raised above 250°C to cure short shots. Above that threshold, the random styrene–acrylonitrile backbone can undergo discoloration, molecular-weight reduction, and volatile residual formation. Instead, short-shot correction in thin ribs and bosses is normally achieved by increasing injection velocity or by adjusting gate geometry.
Plasticising units with 20:1–25:1 L/D and compression ratios of 2.2–2.8:1 are suitable for the grade. Back pressure is maintained at 5–15 bar hydraulic, and screw speed is usually set between 50–100 rpm to limit frictional superheat. The metering zone is set 10–20°C below the nozzle temperature to stabilise pellet feed. In high-speed injection, apparent viscosity becomes strongly shear-thinning, which is the functional basis for selecting this grade over a standard-flow SAN. Exact viscosity curves should be requested from the supplier because the shear-thinning slope varies with lot-to-lot molecular-weight distribution.
Injection pressure is tool-dependent. The high-flow modification may allow a reduction in cavity pressure of approximately 10–20% compared with a general-purpose SAN at the same wall thickness, but this value is geometry-dependent and cannot be transferred from one mould to another without pressure-transducer validation. In thin-wall multi-cavity tools, fill time is commonly targeted at 0.5–1.5 s. Pressure-limited filling below 1,000 bar hydraulic or below the machine’s specific maximum should be confirmed with short-shot studies.
Hot-runner manifolds should have free-flow channels of 4–6 mm diameter and no dead spots or abrupt right-angle transitions. Valve-gate systems are preferred over thermal sprue tips for high-cavitation cosmetic parts because they reduce gate blush and improve gate-freeze consistency. In direct-gated parts below 1.0 mm wall thickness, gate-freeze studies should define holding-pressure time; premature gate freeze produces sink marks, while excessive hold time increases residual stress near the gate.
Drying is mandatory under ambient conditions exceeding 60% RH. The pellet should be dried in a desiccant dryer at 75–85°C for 3–4 h to achieve residual moisture below 0.05 wt%. Drying air dew point should be -20°C or lower. Hot-air hopper dryers alone are insufficient at high humidity because equilibrium moisture may remain above 0.10 wt%, producing splay at the gate and surface defects along flow fronts. In central drying systems, hopper capacity should be matched to consumption so that dried pellet residence time does not exceed 4 h. Prolonged hopper residence at drying temperature can shift the melt into a lower-viscosity condition and increase volatiles.
Barrel residence time is the binding operational limit. At 240°C, total residence time should not exceed 8 min. If shot size is below 30% of barrel capacity, residence time increases; barrel temperature should then be reduced or a smaller plasticising unit should be used. During interruptions longer than 10 min, the melt should be held at 180°C or lower before restart. Degradation by-products from excessive residence time reduce translucency, increase yellowing, and may leave mould deposits on polished cores.
Regrind may be used up to 20 wt% in non-critical appearance parts if the regrind is free of fines and dried to the same moisture specification as virgin pellet. Higher regrind levels alter the viscosity distribution, increase the probability of gloss variation, and reduce weld-line strength. The use of 100% regrind in thin-wall electronic housings is not recommended without separate thermal-stability and impact validation. Melt blending with polyoxymethylene, polyvinyl chloride, or olefinic residues should be avoided unless dedicated purging is performed, because decomposition products from incompatible residues can cause gas marks and surface contamination.
Flammability data are conditional ratings rather than material properties. A typical SAN of this family is rated UL 94 HB in natural colour at a thickness of 3.0 mm. Thickness below 1.5 mm may require separate UL evaluation, especially in pigmented or regrind-containing compounds. The UL file for the specific grade, not the generic SAN family, must be referenced on the finished article.
The primary difference from a general-purpose SAN grade is the high-flow rheology package and an external/internal release system intended for high-cavitation moulding. In replacement trials, the high-flow material can fill thinner wall sections at the same injection pressure or reduce the cavity pressure required for a given wall thickness. The pressure reduction is not a universal transfer function; it must be verified with cavity-pressure transducers on the target tool. The high-flow character also changes the molecular-weight distribution and may reduce notched impact relative to a standard-flow SAN at the same acrylonitrile content. Weld-line tensile strength should be revalidated when the material is used in load-bearing snap-fits or living hinges.
Because the backbone composition remains acrylonitrile–styrene, chemical resistance to dilute acids, bases, alcohols, and aliphatic hydrocarbons is similar to standard SAN. Aromatic hydrocarbons, ketones, esters, and chlorinated solvents remain aggressive and should not be considered for long-term contact without immersion testing. The high-flow modification may reduce knit-line visibility in some translucent parts, but it can also produce gate blush if the gate diameter is below 0.8 mm or if injection velocity is excessive.
In high-cavitation tooling, the practical advantage is the ability to fill a 0.7–1.2 mm nominal wall at moderate clamp force. The limiting variable is usually post-moulding shrinkage anisotropy around gate regions; a mould temperature above 50°C and a holding pressure of 40–60% of injection pressure are used to control sink marks. Multi-cavity layouts should balance runner lengths to within 5% of the longest path; otherwise the low-viscosity melt preferentially fills the shortest cavities and produces cavity-to-cavity mass variations exceeding 0.5% in small parts.
The comparative data below are intended for material-selection screening. They are not specification limits, and lot certificates from the supplier govern the actual values. The high-flow character is most visible in melt volume-flow rate and in practical cavity-pressure or spiral-flow trials; mechanical properties remain within the same broad SAN family, but the sacrifice in impact is a processing trade-off that must be assessed for snap-fit geometries.
| Property | Standard | Unit | S80HFICELLHK comparative band | General-purpose SAN band |
|---|---|---|---|---|
| Melt volume-flow rate | ISO 1133-1:2022 | cm³/10 min | 15–30 at 220°C/10 kg | 6–12 at 220°C/10 kg |
| Density | ISO 1183-1:2019 | g/cm³ | 1.07–1.08 | 1.07–1.08 |
| Tensile stress at yield | ISO 527-2:2012 | MPa | 66–72 | 68–74 |
| Flexural modulus | ISO 178:2019 | MPa | 3,300–3,700 | 3,200–3,600 |
| Charpy notched impact | ISO 179-1:2010 | kJ/m² | 2.0–2.5 | 2.0–2.8 |
| Vicat softening temperature B50 | ISO 306:2022 | °C | 104–108 | 105–109 |
| HDT-A | ISO 75-2:2013 | °C | 86–90 at 1.8 MPa | 88–92 at 1.8 MPa |
Incoming-lot verification should include melt volume-flow rate, moisture, and visual colour after moulding a standard plaque. A practical acceptance window for melt flow rate is typically ±10% of the supplier’s nominal value for the lot. Moisture above 0.05 wt% should trigger additional drying. Ash content above 0.05 wt% may signal contamination or additive segregation. These controls are especially relevant when the grade is used in translucent refrigerator drawers, cosmetic closures, charger housings, and thin-wall electronic ancillary parts, where surface defects and colour drift are directly visible.
For dimensionally stable articles, specimens should be conditioned and tested according to ISO 291:2008 or the equivalent atmospheric conditioning standard referenced in the drawing. Shrinkage is tool-dependent and is influenced by wall thickness, gate type, mould temperature, and holding pressure. Published data for this specific configuration is limited; therefore, the correct shrinkage factor must be determined from a moulded trial on the production tool rather than from a general SAN handbook value.
Chemical resistance should be tested according to the relevant end-use immersion or stress-cracking protocol, such as ISO 22088-2:2006 for environmental stress cracking. The grade should not be specified for continuous outdoor UV exposure unless a separate UV-stabilised formulation or secondary coating is selected. Continuous service above 75°C should be assessed for creep and load-bearing deformation under the specific part load, because amorphous SAN loses stiffness as the glass transition region is approached.