| HS Code | 781366 |
| Polymer Type | Styrene Acrylonitrile (SAN) Copolymer |
| Density | 1.08 g/cm3 |
| Melt Flow Rate | 2.5 g/10 min (230°C/3.8 kg) |
| Tensile Modulus | 3800 MPa |
| Tensile Strength At Yield | 72 MPa |
| Tensile Elongation At Break | 3.0% |
| Flexural Modulus | 3700 MPa |
| Flexural Strength | 110 MPa |
| Notched Izod Impact Strength | 25 J/m (23°C) |
| Charpy Notched Impact Strength | 2.0 kJ/m2 (23°C) |
| Rockwell Hardness | M83 |
| Vicat Softening Temperature | 110°C |
| Heat Deflection Temperature At 1 8 Mpa | 94°C |
| Heat Deflection Temperature At 0 46 Mpa | 102°C |
| Molding Shrinkage | 0.4-0.7% |
| Water Absorption | 0.20% |
| Ul 94 Flammability | HB |
| Dielectric Strength | 20 kV/mm |
| Volume Resistivity | 1e15 ohm-cm |
As an accredited LyondellBasell Hiloy SAN 242 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell Hiloy SAN 242 is supplied in 25 kg polyethylene-lined paper bags, palletized and stretch-wrapped for secure industrial shipping. |
| Container Loading (20′ FCL) | 20′ FCL loading of LyondellBasell Hiloy SAN 242: palletized bags, uniformly stacked, shrink-wrapped, and secured for safe ocean transport. |
| Shipping | LyondellBasell Hiloy SAN 242 is shipped as solid styrene acrylonitrile copolymer pellets in sealed bags, boxes, octabins, or bulk containers. Keep dry and protected from heat, sunlight, and moisture. Handle with standard PPE and follow the SDS and transport documents for classification and requirements. |
| Storage | Store LyondellBasell Hiloy SAN 242 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and incompatible oxidizers. Keep containers/packages tightly closed and labeled to prevent moisture and dust ingress. Avoid generating dust and static discharge. Use original packaging, follow stacking limits, maintain good housekeeping, and keep away from food, drink, and animal feed. |
| Shelf Life | Typically 24 months when stored dry in original sealed packaging at moderate temperature, away from direct sunlight and moisture. |
On production-scale injection moulding lines for transparent appliance parts, LyondellBasell Hiloy SAN 242 is processed at melt temperatures of 210°C to 240°C, with mould surface temperatures maintained at 40°C to 70°C to balance flow length against frozen-in orientation. Converters running refrigerator crisper drawers and blender jars on hydraulic presses with clamp forces from 1,800 kN to 2,500 kN and screw L/D ratios of 20:1 to 24:1 observe that shot mass variability rises when the melt cushion falls below 3 mm; this condition prolongs residence time in the compression zone and accelerates yellowing of the acrylonitrile segment. Drying prior to moulding is set at 80°C for 2 h to 4 h when ambient relative humidity exceeds 60%, because free moisture above 0.08 wt% generates splay and weld-line haze measurable under ASTM D1003-13. For food-contact appliance parts, the compound is evaluated against FDA 21 CFR 181.32 for acrylonitrile copolymers and Commission Regulation (EU) No 10/2011, with overall migration determined according to the food simulant and declared contact ratio. The formulation is typically 100 wt% virgin SAN 242; where a tinted refrigerator drawer is specified, a styrene-based colour masterbatch is added at 0.5 wt% to 2.0 wt%, and total non-resin additives are held below 3.0 wt% because higher loadings reduce notched Izod impact strength when tested under ASTM D256-10(2018). Amine-based mould release agents and basic additives are excluded; residual amines at the moulding surface can accelerate nitrile hydrolysis at processing temperatures, producing colour drift and surface haze. Terminal products produced in this application segment include refrigerator crisper trays, transparent blender jars, food-processor bowls, mixer lids, and small-appliance measuring cups.
Because low haze and resistance to ethanol, isopropyl myristate, and common cosmetic ester systems are specified for rigid cosmetic packaging, SAN 242 is injection moulded into jar bodies and overcaps using melt temperatures between 215°C and 235°C. The cavity must be polished to SPI A-2 or better to achieve surface gloss above 85 GU at 60° when measured under ASTM D2457-13; lower polish levels produce micro-flow marks that become visible after secondary decoration. Compliance for rigid packaging placed on the EU market requires conformity to Regulation (EC) No 1223/2009 for the finished cosmetic product, while the plastic material itself is assessed for substances of concern under REACH and, where reusable contact is claimed, Regulation (EU) No 10/2011. The addition level for colour and effect masterbatches is between 1.0 wt% and 3.0 wt%; for transparent components, no filler or impact modifier is used because the refractive index mismatch between styrenic matrix and conventional impact modifiers raises haze above 3.0% at 2 mm path length. Processing uses a two-plate, hot-runner multi-cavity tool with sequential valve gating; shot size and hold pressure are set to prevent gate blush, with hold pressures from 40 MPa to 60 MPa maintained until the gate freezes. Terminal product types include cream jars, cosmetic caps, compact bases, lipstick tubes, mascara overcaps, and fragrance caps.
The conversion of Hiloy SAN 242 into cuvettes and diagnostic sample cups is governed less by melt flow than by surface quality, wettability, and low extractables in the presence of assay buffers and alcohol-based reagents. Injection moulding is conducted in an ISO Class 7 cleanroom or local laminar-flow enclosure, with melt temperatures constrained to 210°C to 230°C and mould temperatures of 35°C to 50°C to reduce condensed-phase volatile deposition on cavity surfaces. The relevant compliance pathway for primary laboratory consumables is not a single resin certificate; the converter must qualify the finished component under ISO 10993-12:2021 for sample preparation and extractables, ISO 10993-5:2009 for cytotoxicity, and USP <661> for plastic packaging where applicable. Published grade-specific extractables data for SAN 242 in diagnostic reagent environments are limited; therefore, the burden of test data falls on the converter’s validated protocol. Formulation is kept at 100 wt% virgin resin with no internal release additive and no external silicone mould spray, because surface silicone migration changes reagent contact angle and meniscus geometry in optical cells. Cold-runner, two-plate tools with wedge gates are standard; hot-runner systems with exposed resin pools are avoided unless the manifold can be purged within 10 min at no more than 230°C, above which the resin fraction begins to develop free styrene and acrylonitrile decomposition products detectable as UV-absorbing extractables. Terminal outputs are spectrophotometer cuvettes, petri dishes, reagent reservoirs, sample transfer cups, and centrifuge tube outer sleeves.
Where transparency without polycarbonate cost is specified in water treatment sump housings, SAN 242 is moulded as unfilled resin, but the housing must survive cyclic hydraulic pressure without stress cracking. Potable water contact compliance is demonstrated under NSF/ANSI 61 for health effects and, where aesthetic clarity is marketed, NSF/ANSI 42 for particulate and turbidity reduction components; EU submissions rely on Regulation (EU) No 10/2011 with food-contact testing conducted in 10% ethanol and 3% acetic acid simulants for the intended service temperature. The formulation is 100 wt% SAN 242; no glass fibre is used because the resulting haze exceeds 30% at 2 mm thickness, and no elastomer impact modifier is added above 2.0 wt% because phase separation under high shear creates annular flow marks around the bowl threads. Moulders select compression screws with L/D 18:1 to 22:1 and back pressures of 3 MPa to 7 MPa to homogenise the melt without excessive shear heating; injection speed is profiled to maintain a flow-front velocity of 80 mm/s to 120 mm/s through the thread and sealing face. The process conflict is that high hold pressure can improve seal flatness but raises moulded-in stress at the thread roots; typical holding pressure is capped at 50 MPa, and stress relaxation is checked by annealing a sample at 70°C for 1 h and measuring diametric change. Terminal parts include clear overhead filter bowls, sediment sumps, flow-regulator windows, and pressure-differential gauge covers.
| Scenario | Standard or Method | Condition / Application | Verification Focus |
|---|---|---|---|
| Transparent appliance parts | FDA 21 CFR 181.32, Regulation (EU) No 10/2011 | Food-contact drawers, blender jars | Overall migration, sensory, nitrile residue |
| Cosmetic rigid packaging | Regulation (EC) No 1223/2009, REACH | Cream jars, caps, compacts | Substance restrictions, packaging safety |
| Diagnostic consumables | ISO 10993-5:2009, ISO 10993-12:2021 | Cuvettes, specimen cups, petri dishes | Cytotoxicity, extractables profile |
| Water filter housings | NSF/ANSI 61, NSF/ANSI 42 | Potable water sumps, filter bowls | Leachate, turbidity reduction, structural integrity |
| Thin-wall housewares | FDA 21 CFR 181.32, Regulation (EU) No 10/2011 | Food storage trays, organisers | Migration, warpage, filling consistency |
| Writing instruments | REACH, EN 71-3:2019+A1:2021 | Pen barrels, rulers, correction-tape casings | SVHC, element migration for children’s articles |
In thin-wall transparent housewares such as storage trays and food containers, the limiting factor is not plastication but the balance between mould filling and shear-induced degradation of the acrylonitrile segment. At wall thicknesses from 0.8 mm to 1.2 mm, flow-length-to-wall-thickness ratios exceeding 120:1 require melt temperatures at the upper end of the SAN processing window, 230°C to 240°C, and injection velocities from 70 mm/s to 110 mm/s; above 110 mm/s, shear rates at the gate can exceed 10⁵ s⁻¹, causing melt fracture and visible surface defects at the gate area. Process engineers use ISO 1133-1:2022 melt mass-flow rate data to establish lot-to-lot consistency but then verify filling in a spiral-flow tool with a 2 mm cavity depth, because spiral-flow length correlates inversely with mould fill pressure. Compliance for food storage trays is established under FDA 21 CFR 181.32 and Regulation (EU) No 10/2011, with the converter completing migration testing using food simulants matched to the declared contact temperature and time. The formulation is 100 wt% SAN 242 for maximum transparency; if multicavity release is insufficient, 0.1 wt% to 0.3 wt% of a saturated fatty acid release agent is added, but levels above 0.5 wt% produce plate-out on polished cores and should be avoided. Production tools are high-cavitation two-plate moulds with full hot-runner systems and valve pin sequencing; hold pressure is kept at 25 MPa to 40 MPa for 0.5 s to 1.2 s to reduce post-mould shrinkage variation without introducing gate blush. Terminal outputs include food storage boxes, refrigerator organisers, serving trays, cup racks, and modular drawer inserts.
Writing instrument barrels, transparent rulers, and correction-tape bodies made from SAN 242 are produced by injection moulding with melt temperatures of 210°C to 230°C and mould temperatures of 30°C to 50°C. The critical requirement is resistance to inks, marking solvents, and cleaners; compatibility is assessed by immersion testing in ethanol and methyl ethyl ketone according to ASTM D543-20, with the component inspected for cracking after 24 h at 23°C. Regulatory compliance for the European market is mainly under REACH and, when the article is intended for children’s use, EN 71-3:2019+A1:2021 migration limits; the resin supplier’s safety data sheet and food-contact status are not sufficient for children’s categories. Formulation is normally 100 wt% virgin resin; only masterbatches with a styrene-based carrier are used, at 0.5 wt% to 2.5 wt%, because incompatible polyolefin carriers create visible delamination streaks at high shear during filling. Production tooling uses small-diameter gates with reverse taper to reduce gate vestige on pen barrels; screw L/D is 20:1 and back pressure is limited to 2 MPa to 5 MPa to maintain melt homogeneity without excessive residence. Terminal product types include ballpoint pen barrels, rollerball pen bodies, mechanical pencil barrels, transparent rulers, geometry instruments, and correction-tape casings.
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LyondellBasell Hiloy SAN 242 is a general-purpose injection-moulding grade of styrene-acrylonitrile copolymer supplied as pelletised feedstock. The grade contains a nominal acrylonitrile segment of 24 wt%, placing it in the mid-range of SAN copolymer formulations. Under thermal analysis the material behaves as a rigid amorphous thermoplastic. The supplier technical datasheet identifies the product through rheological, mechanical, optical, and thermal values rather than by polymerisation route. The melt phase is transparent with a faint yellow cast at moderate wall thickness. Because the polymer backbone does not contain a dispersed polybutadiene rubber phase, the article remains transparent under normal use conditions, unlike medium-impact ABS, which is opaque or translucently hazy depending on rubber particle size and processing history.
The following table lists representative values from the LyondellBasell technical datasheet for Hiloy SAN 242. These are typical lot-release values, not minimum or maximum specifications. Incoming quality control should compare dried-pellet values against the supplier release sheet using the same test method and conditioning state.
| Property | Representative value | Test method |
|---|---|---|
| Melt mass-flow rate at 230 °C with 3.8 kg load | 3.0 g/10 min | ISO 1133-1 |
| Density | 1.08 g/cm³ | ISO 1183-1 |
| Tensile stress at yield | 68 MPa | ISO 527-2 |
| Tensile strain at break | 2.5 % | ISO 527-2 |
| Flexural modulus | 3600 MPa | ISO 178 |
| Notched Izod impact at 23 °C, type A notch | 2.0 kJ/m² | ISO 180/A |
| Vicat softening temperature, load 50 N, rate 50 °C/h | 106 °C | ISO 306/B50 |
| Heat deflection temperature at 1.80 MPa | 98 °C | ISO 75-2/A |
| Mould shrinkage, parallel and transverse | 0.4–0.7 % | ISO 294-4 |
| Water absorption, 24 h immersion | 0.20 % | ISO 62 |
For applications requiring optical comparison, total luminous transmittance is typically reported in the range of 88–90 % at 2 mm wall thickness under ASTM D1003. Haze measurements on moulded plaques should be based on the same thickness, because increasing wall section reduces transparency and shifts the visual colour from colourless to light yellow.
On a production floor, the first variable requiring attention is not melt temperature but pellet moisture. Hiloy SAN 242 absorbs moisture from ambient air. Residual moisture above 0.05 % vaporises inside the plasticating unit and produces surface defects because the melt is processed above 200 °C. A desiccant-bed dryer with a dew point of -30 °C or lower is used at 80 °C for 2–4 hours. In plants where relative humidity exceeds 60 %, hopper lids are kept closed and transfer lines are purged with dry air. Failure to maintain these conditions results in silver streaking on flat cosmetic panels and loss of optical continuity at weld lines.
For cold-runner injection tools, barrel settings from feed throat to nozzle are normally maintained at 200 °C, 210 °C, 215 °C, 220 °C, and 220 °C. The melt temperature measured at the nozzle is kept between 220 °C and 240 °C. Hydraulic back pressure is set at 50–100 bar to stabilise screw recovery and improve dispersion of colour concentrate. Screw surface speed is limited to 0.15–0.25 m/s. Co-rotating twin-screw compounders used for masterbatch dilution employ L/D 32–40 and temperature profiles from 190 °C to 230 °C. Holding pressure is selected from 60–80 MPa cavity pressure at the gate for amorphous solidification. Mould temperature is controlled by water units to 40–70 °C; higher mould temperature increases clarity but raises cycle time and may prolong sink-mark formation in thick bosses.
Tooling for Hiloy SAN 242 requires generous cold-runner drops and continuous vent channels of 0.02–0.04 mm depth. Venting along weld lines must not be interrupted; insufficient venting causes burn marks at the end of fill and deposit formation on cavity surfaces. For multicavity tools, geometrically balanced runners are required because the melt viscosity is more shear-sensitive than that of high-flow grades. Clamp force is calculated from projected area and a specific cavity-pressure assumption of 25–35 MPa. On hydraulic toggle machines in the 1000–1500 kN class, cavities are filled with a screw cushion of 2–4 mm and decompression of 2–3 mm to avoid nozzle drool. Regrind fractions above 20 wt% produce a measurable increase in melt mass-flow rate and a decrease in tensile strain at break; higher regrind use should not be permitted without re-validation of mechanical performance.
At melt temperature above 260 °C, the acrylonitrile-rich chain segments undergo thermal decomposition. This produces yellow-green chromophores and reduces melt viscosity, leading to flash in tools designed for fresh pellets. If melt is retained in the barrel for more than 5 minutes at 230 °C, periodic purging is required. Machines with long nozzle shutdowns or hot-runner manifolds without balanced thermal control may generate black specks after 8–10 minutes. Interrupted cycles retain melt in the barrel and can create shot-to-shot variability that is not inherent to the resin lot. Short shots must not be repeatedly recovered without purging the barrel with an acrylic or styrene-based purge compound.
Repeated processing also shifts molecular weight distribution. Injection-moulding shops should perform melt mass-flow rate by ISO 1133-1 per shift on dried pellets and compare against the supplier lot value. A deviation greater than 15 % from the fresh-pellet value usually indicates retained residence time, excessive shear, or contamination. If hot-runner tooling is used, manifold and nozzle zones are controlled individually at 220–230 °C; dead zones in the manifold should be eliminated through balanced flow-channel geometry and valve-gate actuation.
Flexible transparent packaging is not the primary conversion route for Hiloy SAN 242. Transparent housewares, cosmetic closures, appliance lenses, dials, indicator windows, and filter housings are more representative applications. High optical clarity and surface modulus are primary requirements; impact strength is secondary. The notched Izod impact value of 2.0 kJ/m² excludes load-bearing snap-fit structures, self-threading closures without metal inserts, and thin-wall battery housings subject to drop loading. The flexural modulus difference of 1200 MPa relative to medium-impact ABS contributes to lower deflection under equivalent short-term load.
For cosmetic and detergent contact, the resin is resistant to mineral oil, many ester-based emollients, and dilute detergents at ambient temperature. Solvent-based nail lacquers, chlorinated cleaning agents, and high-solvent hair sprays can produce environmental stress cracking. When chemical exposure is suspected, validation follows ISO 4599 using a constant-strain bent-strip jig and the specific contact medium. Medical component use outside the body may require cytotoxicity assessment under ISO 10993-5 and sensitisation assessment under ISO 10993-10; published data for this specific product’s biological classification is limited.
| Property | Hiloy SAN 242 | General-purpose polystyrene | Medium-impact ABS | Test method |
|---|---|---|---|---|
| Density | 1.08 g/cm³ | 1.04 g/cm³ | 1.04 g/cm³ | ISO 1183-1 |
| Tensile stress at yield | 68 MPa | 46 MPa | 45 MPa | ISO 527-2 |
| Flexural modulus | 3600 MPa | 3200 MPa | 2400 MPa | ISO 178 |
| Notched Izod impact at 23 °C | 2.0 kJ/m² | 1.2 kJ/m² | 20 kJ/m² | ISO 180/A |
| Heat deflection temperature at 1.80 MPa | 98 °C | 75 °C | 95 °C | ISO 75-2/A |
| Total luminous transmittance | 88–90 % | 90 % | opaque | ASTM D1003 |
At equal wall thickness, Hiloy SAN 242 has higher stiffness and heat resistance than general-purpose polystyrene and lower notched impact strength than ABS. The differentiating feature is the combination of transparency and moderate chemical resistance absent in ABS. It is not a direct replacement for polycarbonate in transparent impact applications, because the notched impact value remains more than an order of magnitude lower.
At the regulatory interface, the grade is evaluated on an article-specific basis. Food-contact assessment in the United States is not a generic material approval; the final article is evaluated against 21 CFR 177.1040 for styrene-acrylonitrile copolymers. In the European Union, migration testing for specific food simulants under Regulation (EU) No 10/2011 is required on the finished part. For electrical and electronic components, RoHS 2011/65/EU restrictions are normally met by the base polymer, but flame retardants, colourants, and processing aids used downstream may alter the article classification. REACH (EC) No 1907/2006 compliance is maintained through the supplier safety data sheet and is not an article-level indication unless SVHC content is assessed. Strong acids, aromatic hydrocarbons, ketones, and chlorinated solvents remain the primary incompatibility boundaries; article-level validation is required.