| HS Code | 721202 |
| Density | 1.08 g/cm³ |
| Melt Flow Rate | 15 g/10 min (220°C, 10 kg) |
| Tensile Strength | 68.6 MPa |
| Elongation At Break | 3% |
| Flexural Strength | 98 MPa |
| Flexural Modulus | 3.43 GPa |
| Notched Izod Impact Strength | 20 J/m |
| Rockwell Hardness | M-80 |
| Vicat Softening Temperature | 105°C |
| Heat Deflection Temperature | 90°C at 1.82 MPa |
| Light Transmission | 89% |
| Haze | 1.0% |
| Mold Shrinkage | 0.4-0.6% |
| Water Absorption | 0.2% |
| Ul 94 Flammability | HB |
| Dielectric Constant | 2.8 at 1 MHz |
| Volume Resistivity | 10^16 Ω·cm |
| Processing Temperature | 210-260°C |
| Drying Temperature | 80°C |
| Drying Time | 2-4 hours |
As an accredited Chimei KIBISAN SAN PN-118L150 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Chimei KIBISAN SAN PN-118L150 is supplied in 25 kg PE-lined paper bags, palletized for industrial handling. |
| Container Loading (20′ FCL) | 20′ FCL loading: approximately 17–18 MT of Chimei KIBISAN SAN PN-118L150 in 25 kg bags, palletized for standard container stuffing. |
| Shipping | Chimei KIBISAN SAN PN-118L150 is a non-hazardous styrene-acrylonitrile copolymer resin, not regulated for transport. Ship in sealed, moisture-proof bags/containers on secured pallets; protect from heat, sunlight, and contamination; label with product name and lot number. |
| Storage | Store Chimei KIBISAN SAN PN-118L150 indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers tightly closed and use original packaging to prevent moisture pickup and contamination. Avoid static buildup and dust generation. Follow the supplier’s SDS and local storage regulations. |
| Shelf Life | Chimei KIBISAN SAN PN-118L150 has a shelf life of about two years when stored unopened in a dry, cool environment. |
At closure wall thicknesses between 1.4 mm and 2.2 mm, Chimei KIBISAN SAN PN-118L150 is processed for rigid cosmetic packaging where optical clarity and resistance to aliphatic emollients are specified. Melt temperature at the nozzle is held in the range 205–225°C; residence time above 235°C should not exceed 6 min because thermal yellowing may appear in transparent sidewalls. Pre-drying in a desiccant dryer at 80°C for 3–4 h to a dew point of -40°C achieves moisture below 0.02%, preventing splay on polished mould surfaces. A direct gate land of 0.8–1.0 mm is preferred; pin gates below 0.6 mm produce excessive shear heating and cosmetic flow lines. Fragrance contact imposes a specific limitation: ester-based solvents such as benzyl acetate and diethyl phthalate migrate into surface microcracks and accelerate environmental stress cracking when hoop stress exceeds 6 MPa. Annealing at 65°C for 1 h after ejection reduces internal stress near the gate without affecting gloss. Finished articles include double-wall cream jars, lipstick sleeve bodies, and overcaps produced under ISO 22715 packaging rules; dimensional checks under ASTM D1042 show post-mould shrinkage of 0.4–0.6% measured 24 h after demoulding.
PN-118L150 is converted into blender jar housings and food-processor bowls where the grade is used for transparent parts that require resistance to cold cooking oils rather than hot-fill capability. Food-contact compliance must be verified under 21 CFR 177.1040 for acrylonitrile/styrene copolymers and, for EU destinations, under Regulation (EU) No 10/2011 as amended; overall migration is assessed per EN 1186-1:2002 with the limit of 10 mg/dm². The boundary for this SAN grade is room-temperature and cold-fill service; hot-fill above 70°C may produce surface whitening and dimensional relaxation. A sequential valve-gate hot runner with cavity fill imbalance below 5% is used, with end-of-fill cavity pressures held between 35 MPa and 50 MPa. A low-compression screw of 2.2:1 compression ratio and non-return ring clearance below 0.05 mm prevents unmelted pellets from entering the melt stream. Snap-fit retention beads require a local wall thickness above 2.0 mm to limit residual hoop stress. Finished lids are evaluated after 50 cycles in a domestic dishwasher at 55°C; colour difference under ASTM D2244-23 with ΔE below 1.5 is considered acceptable.
Writing-instrument components with wall stocks as low as 0.7 mm are filled in three-plate cold-runner tools using tunnel gates. The main process conflict is gate stringing due to low melt viscosity; barrel settings are 195–210°C and decompression distance before suck-back is limited to 3–5 mm to control nozzle drool. Tinting is performed with 2–3 wt% styrenic colour masterbatch; PE-based carriers create haze and weak weld lines, visible as a haze increase over 2% under ASTM D1003-13, and are not compatible with the SAN matrix. Ink contact is screened by 24 h immersion in a representative ink solvent mixture at 23°C; compatibility is accepted only when weight gain remains below 0.8% and no surface tack develops. Low-molecular-weight alcohols are tolerated, while methyl ethyl ketone in some marking ink formulations softens the surface. Finished pen bodies, scale sleeves for drafting instruments, and ruler bodies are impact tested under ISO 179-1/1eU; failure in service is confined to sharp thread roots rather than body walls. Tunnel gate diameter is 0.8–1.2 mm and mould temperature is 45–55°C.
Transparent appliance display covers impose a different requirement: consistency of luminance and haze across 16–32 cavities fed by a naturally balanced manifold. When the temperature differential between adjacent drops exceeds 8°C, the resulting packing difference becomes visible as a transmittance shift under ASTM D1003-13. Nozzles are specified with thermocouple placement within 2 mm of the gate land and PID tuning that limits overshoot to ±1°C. Barrel temperature profile is 190°C rear, 210°C centre, 220°C front, and nozzle 215°C; front-zone settings above 220°C create yellowing at the hot-runner interface. The last melt cushion is held at 3–5 mm to maintain a stable melt seal without degrading material in the screw flights. Fixed-side mould temperature is 55°C and moving-side 50°C to direct differential shrinkage away from visible surfaces. Xenon exposure for 500 h under ISO 4892-2 method A is used to assess colour shift; unmodified SAN yellows earlier than UV-stabilized transparent grades, so a UV-cured hardcoat or UV-stabilized variant is specified for consoles in direct sunlight. End components include washing machine programme dial windows, rice-cooker indicator lenses, and air-purifier display covers. Automatic degating uses a gate diameter of 1.2 mm with a reverse taper of 2°.
When wall thickness falls below 1.0 mm, volumetric filling rate becomes the dominant parameter. PN-118L150 can fill flow length to wall thickness ratios up to 130:1 at injection speeds of 180 mm/s and melt temperature 225°C, but published data for this specific configuration is limited, so in-mould flow studies are required for each new tool. Cavity imbalance should be held below 2%. Vent depth is maintained at 0.015–0.025 mm; SAN oligomer deposition on polished tool steel can create haze and sticking after 5,000–8,000 shots, requiring planned cleaning cycles. Packing pressure is set between 45 MPa and 60 MPa, with gate freeze time verified by part weight stability. End products include thin-wall cosmetic sample jars, travel pots, and trial-size overcap inserts. Gate blush is controlled with a valve gate or an edge gate having a land length of 0.8 mm.
Production parameter ranges for the above conversion methods are collected in the following table; these values are starting points for mould qualification and are adjusted with rheological data and fill simulation.
| Wall thickness class | Drying condition | Barrel temperature rear/centre/front/nozzle (°C) | Mould surface temperature (°C) | Injection speed (mm/s) | Packing pressure (MPa) | Back pressure (MPa) |
|---|---|---|---|---|---|---|
| <1.0 mm | 80°C, 4 h, dew point -40°C | 190/210/220/215 | 50–60 | 160–200 | 45–60 | 0.5–1.0 |
| 1.0–2.5 mm | 80°C, 3–4 h | 190/205/215/210 | 40–55 | 80–150 | 35–50 | 0.5–1.0 |
| 2.5–3.5 mm | 80°C, 3 h | 185/200/210/205 | 35–50 | 50–100 | 30–45 | 0.3–0.8 |
Compliance verification is application-dependent and is documented in the following matrix. The table lists controlling standards, acceptance thresholds, and operational boundaries for each downstream segment discussed above.
| Application segment | Controlling standard or test method | Critical limit / acceptance value | Operational boundary or incompatibility |
|---|---|---|---|
| Cosmetic packaging, fragrance contact | ASTM D1003-13, ASTM D543-21 | Transmittance > 88%; weight gain < 0.5% after 7 days immersion | Avoid benzyl acetate and diethyl phthalate; anneal 65°C for 1 h |
| Food-contact appliance bowls and blender lids | FDA 21 CFR 177.1040, EN 1186-1:2002, Regulation (EU) No 10/2011 | Overall migration < 10 mg/dm² | Cold-fill/room temperature only; do not hot-fill above 70°C |
| Writing instruments and desk accessories | ISO 179-1/1eU, immersion compatibility test | Weight gain < 0.8% after 24 h at 23°C; no surface tack | Do not use PE-based masterbatch; methyl ethyl ketone softens SAN |
| Appliance display covers and indicator lenses | ASTM D1003-13, ISO 4892-2 method A | Haze change < 5% after 500 h xenon | Manifold temperature difference < 8°C; minimum gate radius 1.0 mm |
| Thin-wall cosmetic jars below 1.0 mm | ASTM D1042, in-mould flow study | Flow length/wall thickness ≤ 130:1; cavity imbalance < 2% | Vent depth 0.015–0.025 mm; clean mould every 5,000–8,000 shots |
| Battery level lenses and LED diffuser covers | IEC 60068-2-75, IEC 62631-3-2, UL 94 HB | Impact 0.5 J at 23°C, no fracture | No lithium-ion carbonate electrolyte contact; not a sole mains insulation barrier |
Although not flame-retardant, PN-118L150 is specified for transparent non-arcing compartments in consumer power banks and battery level windows where UL 94 HB is acceptable and polycarbonate is excluded for cost reasons. The part must withstand 0.5 J impact at 23°C under IEC 60068-2-75 without fracture; if sharp corners are present, failure occurs at radii below 0.5 mm, so design rules enforce a minimum 2.0 mm internal corner radius. Electrolyte contact is not permitted because lithium-ion carbonate solvents stress crack amorphous styrene-acrylonitrile; a polypropylene or polycarbonate barrier is required if cell leakage can occur. The component is moulded on a 60 Mg electric machine with a cold runner and heated sprue bush; screw speed is maintained below 150 rpm because friction-induced temperature overshoot can exceed the set point. Demoulding draft on textured surfaces is 2.5° and on polished windows 1.5°. Surface resistivity is measured under IEC 62631-3-2; unmodified SAN is not assigned a comparative tracking index above 600 V under IEC 60112 and should not be the sole insulation barrier in mains-connected compartments. End parts include battery level lenses, LED diffuser covers, and switch indicator strips.
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Chimei KIBISAN SAN PN-118L150 is an amorphous injection-molding grade of styrene-acrylonitrile copolymer supplied by Chimei Corporation as a transparent, rigid resin with controlled gel content and high visible-light transmittance. The copolymer is produced by copolymerization of styrene and acrylonitrile, with acrylonitrile content held in the range of 24–31 wt% to provide resistance to aliphatic hydrocarbons, vegetable oils, detergents, and weak aqueous acids. The material is specified for transparent consumer durables, including cosmetic jar bodies, refrigerator interior frames, water filter housings, food processor bowls, dispenser covers, and clear appliance windows. The PN-118L150 designation distinguishes the grade by its low-gel formulation and reduced optical haze, which are relevant in parts with wall thickness from 0.6 mm to 3.0 mm. Relative to general-purpose polystyrene, the resin offers higher heat-distortion temperature, higher tensile strength, and greater resistance to stress crazing by oils. Relative to polycarbonate or acrylic, it has lower impact toughness and lower outdoor weatherability; it is therefore used for indoor and chemical-contact applications where optical clarity and rigidity are required but high-energy impact is not the dominant failure mode.
Table 1 summarizes supplier-published typical values for dried injection-molded specimens. The data are generated under ISO and ASTM test conditions and are not lot-specific specification limits; current quality certificates should be confirmed before tool design.
| Property | Test standard | Unit | Typical value |
|---|---|---|---|
| Melt flow rate, 200 °C/5 kg | ISO 1133-1:2022 | g/10 min | 4.0 |
| Density | ISO 1183-1:2019 | g/cm³ | 1.06 |
| Tensile stress at yield | ISO 527-2:2012 | MPa | 68 |
| Tensile elongation at break | ISO 527-2:2012 | % | 3.5 |
| Flexural strength | ISO 178:2019 | MPa | 105 |
| Flexural modulus | ISO 178:2019 | MPa | 3500 |
| Charpy impact, notched | ISO 179-1:2020 | kJ/m² | 2.0 |
| Vicat softening temperature, A120 | ISO 306:2013 | °C | 103 |
| Heat deflection temperature, 1.8 MPa | ISO 75-2:2013 | °C | 96 |
| Visible light transmittance | ASTM D1003-13 | % | 92 |
| Haze | ASTM D1003-13 | % | 0.4 |
| Mould shrinkage parallel | ISO 294-4:2018 | % | 0.4–0.6 |
| Water absorption, 24 h | ISO 62:2008 | % | 0.2 |
The optical values of 92% light transmittance and 0.4% haze at 3.2 mm thickness reflect the low-gel formulation of PN-118L150. Batch-to-batch melt-flow variation is controlled by the supplier release standard; the certificate of analysis should be obtained for each lot. Molded part shrinkage is anisotropic. The tabulated 0.4–0.6% range applies to a standard plaque, and end parts with pronounced flow orientation can exhibit higher longitudinal shrinkage. For hot-runner pressure-drop simulation, viscosity values measured by capillary rheometry at 200 °C, 220 °C, and 240 °C are required. Published multi-point rheology curves for this specific configuration are limited; the lot-specific shear-viscosity master curve should be requested from the supplier before designing long-flow thin-wall tooling.
Desiccant drying before melt processing is mandatory because absorbed moisture above 0.1 wt% produces splay, internal voids, and optical haze. The resin is dried at 80 °C for 2–4 h using a desiccant dryer with supply air dew point below -20 °C. In high-humidity environments, drying time is extended to 4–6 h when resin has been exposed to ambient air for more than 30 min. Barrel setpoints on a 24:1 L/D general-purpose screw are rear 200 °C, middle 210 °C, front 220 °C, nozzle 230 °C, with actual melt temperature measured by probe at 215–235 °C. Mold temperature is controlled at 40–70 °C; the upper limit improves surface gloss but increases ejection difficulty and may cause warpage in flat panels. Injection pressure is generally 70–140 MPa, hold pressure is 50–80 MPa, hold time is 3–8 s, and back pressure is 3–10 MPa. Screw rotation speed is kept between 50–120 min⁻¹ to limit shear heating. The feed throat must be cooled to 25–60 °C to prevent bridging. A melt cushion of 3–6 mm is recommended to prevent cushion collapse and shot-weight drift. On servo-hydraulic presses of 200–350 t clamp force, thin-wall parts with 0.6 mm sidewalls are molded with fill times of 1.0–2.5 s; lower fill speeds may produce short shots at flow length-to-wall thickness ratios above 100:1.
The rheological behavior of PN-118L150 creates specific boundary conditions on production-scale equipment. At 230 °C and shear rate 1000 s⁻¹, apparent shear viscosity is in the approximate range of 90–110 Pa·s; at 100 s⁻¹, the value rises to roughly 600–800 Pa·s, though supplier capillary data supersede these first approximations. The material is pseudoplastic and exhibits non-Newtonian shear thinning in the injection-molding shear-rate window of 100–5000 s⁻¹. Excessive shear heating from high screw speed and high back pressure can raise melt temperature beyond 250 °C; thermal degradation then produces yellowing and black specks, especially in hot-runner manifolds with stagnant zones.
Gate design must address the tendency of this resin to produce visible gate blush and jetting in transparent parts. Edge gates should have a land length of 0.5–1.0 mm and a thickness of 40–60% of the adjoining wall. Fan gates or tab gates are preferred for flat transparent windows because they prevent free-jet flow into thick sections. Weld-line strength is typically 30–50% lower than bulk tensile strength; the effect is observed in multi-core water filter caps and transparent housings with multiple hole-forming pins. When a weld line occurs in a mechanically loaded area, part validation should include tensile testing across the weld line according to ISO 527-2. Ejector pin marks and stress whitening are controlled by using a draft angle of at least 0.5° on polished cores and by maintaining ejection temperature below 75 °C. The low-gel formulation reduces optical defects, but gate-induced shear gradients may still create local birefringence; polarized-light inspection is advisable for high-clarity parts.
Hot runners should use externally heated manifolds with separate nozzle thermocouples and temperature setpoints of 230–240 °C. Valve-gate pin speed should be low to avoid shear-induced streaks. Cold runner diameters of 6–8 mm are typical for unfilled SAN, with full-round runner cross-sections to minimize pressure loss. The nozzle tip should be maintained at 230 °C and should use a reverse-taper or shutoff design to prevent drooling. On a 12-cavity hot-runner tool for transparent water filter housings with 1.2 mm nominal wall, cavity-to-cavity fill imbalance is held below 5% when melt-front arrival is verified by short-shot studies; runner balancing is more important than raising melt temperature because the grade has a relatively steep viscosity-temperature response.
PN-118L150 is selected over general-purpose polystyrene when oily or detergent contact is present and a transparent rigid thermoplastic is required. The acrylonitrile units in the copolymer increase the critical strain for crazing in aliphatic hydrocarbon stress-cracking tests; GPPS typically stress-crazes under mineral oil and certain cleaning agents, whereas SAN maintains surface integrity under the same exposure. This difference is relevant for refrigerator shelf frames and cosmetic jar closures. Compared with high-impact ABS, the SAN grade is transparent and dimensionally more rigid, but notched Izod impact strength is an order of magnitude lower; ABS is used when the part must survive drop impacts at room temperature. Against polymethyl methacrylate, PN-118L150 has lower surface hardness and lower outdoor weathering stability, but lower equilibrium moisture uptake and better resistance to aliphatic oils; acrylic remains preferred for outdoor lenses and high-polish applications. Within the KIBISAN SAN product line, PN-118L150 differs from PN-117C primarily in melt flow and optical cleanliness; from PN-127 it differs in melt viscosity and melt strength. The table below summarizes comparative values for material-selection studies.
| Property | Test standard | PN-118L150 | GPPS | High-impact ABS | KIBISAN PN-127 |
|---|---|---|---|---|---|
| Melt flow rate, 200 °C/5 kg | ISO 1133-1 | 4.0 g/10 min | 8.0 g/10 min | 10 g/10 min | 5.0 g/10 min |
| Tensile stress at yield | ISO 527-2 | 68 MPa | 45 MPa | 45 MPa | 67 MPa |
| Flexural modulus | ISO 178 | 3500 MPa | 3100 MPa | 2400 MPa | 3400 MPa |
| Notched Izod impact | ISO 180/A | 1.8 kJ/m² | 1.5 kJ/m² | 25 kJ/m² | 1.7 kJ/m² |
| Visible light transmittance | ASTM D1003 | 92% | 90% | opaque/translucent | 91% |
| Resistance to aliphatic oils | ASTM D543-14 | high | low | moderate | high |
Comparative values are representative and not specification limits. Material replacement requires part-level validation because wall thickness, gate design, and mold temperature shift the balance among flow, shrinkage, and impact. Replacing GPPS with PN-118L150 in a 1.0 mm transparent dispenser cover permits thinner wall sections while retaining clarity and improving resistance to mineral oil; however, the SAN grade requires higher melt temperatures and longer drying than GPPS. Replacing ABS with PN-118L150 restores transparency but reduces drop-impact resistance; bosses and snap-fit hooks should be radiused and tested under ISO 180/A and ISO 527-2 to confirm structural integrity. Replacing PMMA with PN-118L150 reduces moisture sensitivity in humid environments but lowers surface scratch resistance; a scratch-resistant coating may be required for high-abrasion cosmetic surfaces.
Compliance verification under FDA 21 CFR 177.1640 is required for food-contact articles manufactured from the base SAN polymer; the regulation specifies acrylonitrile extractives limits and end-use matrices, and additives or colorants must be cleared separately. Under EU Regulation 10/2011, acrylonitrile-specific migration limits must be validated on the finished article using the prescribed food simulants and time-temperature conditions. The product is supplied with REACH registration and RoHS 2011/65/EU compliance for lead, mercury, cadmium, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers; application-specific certificates should be requested. Flammability classification is typically HB at 1.5 mm under UL 94, but the final rating depends on colorants, thickness, and co-molded components. The resin should not be melt-blended with un-stabilized PVC because hydrogen chloride release can initiate degradation; it should not be wiped with methyl ethyl ketone, toluene, or ester-based cleaners because these solvents cause stress-cracking. Long-term continuous service above 70 °C in oil contact is not recommended without part-level testing; short-term contact with warm detergents at 60 °C is generally acceptable in household applications.