| HS Code | 972005 |
| Density | 1.07 g/cm3 |
| Melt Flow Rate 200 C 5 Kg | 5.0 g/10 min |
| Tensile Strength At Yield | 73 MPa |
| Tensile Elongation At Break | 3.0% |
| Flexural Strength | 110 MPa |
| Flexural Modulus | 3.3 GPa |
| Izod Impact Strength Notched | 20 J/m |
| Rockwell Hardness | M85 |
| Vicat Softening Temperature | 110 °C |
| Heat Deflection Temperature 1 8 Mpa | 95 °C |
| Light Transmittance | 89% |
| Haze | 1.5% |
| Mold Shrinkage | 0.3-0.6% |
| Water Absorption | 0.2% |
| Dielectric Strength | 20 kV/mm |
| Volume Resistivity | 1e16 ohm-cm |
| Flammability | HB |
As an accredited Kumho Petrochemical SAN 326N A factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Kumho Petrochemical SAN 326N A is supplied in 25 kg multi-wall paper bags, palletized for industrial handling and storage. |
| Container Loading (20′ FCL) | Kumho Petrochemical SAN 326N A palletized in bags, loaded and secured in a 20-foot FCL container for export shipment. |
| Shipping | Kumho Petrochemical SAN 326N A is shipped as a solid styrene-acrylonitrile copolymer resin, typically in 25 kg bags or bulk containers. It is non-hazardous under normal transport regulations. Keep dry, avoid direct sunlight and excessive heat, and store in a cool, ventilated area. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep bags or containers tightly closed to prevent moisture ingress and contamination. Avoid dust generation and accumulation; use grounding/bonding where dust may form. Keep away from strong oxidizers and follow local regulations. |
| Shelf Life | Shelf life is typically 2 years from manufacture when stored cool, dry, and well-ventilated in unopened original packaging. |
High-cavitation cosmetic closure programmes generate rejection-rate data that is dominated less by raw resin lot variation than by the interaction between gate seal time and runner pressure decay in hot-runner tooling. Kumho Petrochemical SAN 326N A, an unfilled injection-molding SAN, is processed in this segment at melt temperatures of 220–245 °C. The lower boundary is determined by flow hesitation at polished cavity surfaces and by gate chill in multi-drop systems; the upper boundary is governed by oxidative yellowing when total barrel residence time exceeds 8 min. Before molding, the granules are dried in a desiccant dryer with an inlet-air dew point below −25 °C and a bed temperature of 80 ± 5 °C for 2–4 h. Residual moisture is held below 0.03 wt% as measured by Karl Fischer titration, because moisture above 0.05 wt% produces longitudinal silver streaking from hydrolysis of low-molecular-weight SAN fractions and increases part-to-part gloss scatter. Reciprocating-screw machines with screw diameters of 25–35 mm, L/D ratios of 20:1–22:1, compression ratios of 2.2:1–2.6:1, and non-return ring clearances below 0.03 mm are used to maintain shot-weight consistency in tools with 16–32 cavities. Back pressure is set at 0.5–1.5 MPa; screw surface speed is limited to 0.2–0.5 m/s to avoid frictional heating of melt above the degradation threshold.
Gate design in heavy-wall jars, caps, and vacuum-metallized collars is a primary process conflict. Valve-gated hot-runner drops of 1.0–1.5 mm diameter are positioned to place the gate vestige on non-cosmetic surfaces or under cap knurl. Mold temperature is maintained at 35–55 °C on the cavity side and 25–40 °C on the core side; this differential cooling assists ejection of deep-draw parts and reduces sidewall distortion. Peak injection pressure is 80–100 MPa, with transfer to hold phase at 95–98% of volumetric fill. Hold pressure is maintained at 55–70 MPa until gate seal, which is verified by plotting part mass against hold time; after gate freeze, additional hold time produces no measurable mass gain but increases cycle time. The final 2–5% of fill is decelerated to 30–50 mm/s to suppress jetting and reduce shear-induced gloss variation on the cavity surface. Perimeter vents are cut to a depth of 0.02–0.03 mm over a land length of 2–4 mm; core-pin vents are shallower at 0.015 mm to avoid flash while allowing gas escape at blind holes.
| Wall thickness class | Melt temperature (°C) | Mold temperature cavity/core (°C) | Hold pressure (MPa) | Representative cooling time (s/mm) | Primary defect risk |
|---|---|---|---|---|---|
| 1.5 mm thin-wall jars | 235–245 | 45–55/30–40 | 65–75 | 2–3 | gate blush, jetting |
| 2.5 mm caps | 225–235 | 35–45/25–35 | 55–65 | 3–4 | sink marks, internal voids |
| 4.0 mm heavy bases | 215–225 | 30–40/20–30 | 50–60 | 5–7 | voids, gate cracking |
In-plane mold shrinkage is evaluated according to ISO 294-4 and falls in the range 0.3–0.7% depending on wall thickness and hold pressure. High-gloss cap surfaces are monitored with a 20° gloss meter per ASTM D523; readings below 80 GU initiate correction of mold temperature or fill rate. Tensile verification uses ISO 527-2 Type 5A specimens; flexural modulus is characterized by ISO 178. For cosmetic packaging, regulatory review includes REACH Annex XVII, heavy-metal migration under EN 71-3 where the package may be repurposed as a children’s article, and packaging waste requirements under 94/62/EC. The raw resin is not intended as a finished cosmetic-contact article; safety assessment under EU 1223/2009 is addressed at the level of the molded pack and the complete recipe, not at the level of the unfilled polymer.
During planar diagnostic tray qualification, the assumption that SAN 326N A can be substituted for polystyrene without altering gate-freeze or flatness constraints leads to warpage and closed-cell voiding in thin wells. The polymer is dried at 80 °C for 3 h in a closed-loop desiccant dryer to a residual moisture below 0.02 wt%. Melt temperature is held between 230 °C and 245 °C, and mold temperature is raised to 60–80 °C to reduce birefringence and frozen-in stress. For 1.0–1.5 mm nominal wall thickness, cycle times increase to 35–45 s; this slower cooling is unavoidable if flatness is required across the long axis of a 96-well tray. Tunnel gates of 0.8–1.2 mm diameter are preferred because edge gates generate visible blush on optical surfaces. Fill velocity is set at 60–80 mm/s; final packing velocity is reduced to 20–30 mm/s to avoid overpacking the gate region. Back pressure is kept below 0.8 MPa to limit frictional heat and molecular weight loss.
Warpage control in cuvette arrays and tube holders is driven by asymmetric cooling. Flatness tolerances of 0.05 mm over a 50 mm length are verified by coordinate measuring after 24 h of ambient conditioning. Post-ejection annealing at 70–80 °C for 1–2 h reduces residual stress, but annealing above 85 °C distorts ribs below 1.0 mm width. The SAN copolymer resists aliphatic alcohols, dilute saline, and phosphate buffer solutions; it is not compatible with ketone-containing adhesives, aromatic hydrocarbons, or chlorinated solvents. Solvent bonding with cyclohexanone causes microcrazing in 1.0 mm walls and must be replaced by UV-cure adhesive assembly. Repeated steam autoclave exposure at 121 °C exceeds the heat deflection temperature of unfilled SAN and creates permanent dimensional change; the material is therefore limited to non-autoclavable in vitro diagnostic components and non-invasive housings.
Biocompatibility and extractables requirements are addressed with ISO 10993-5 for cytotoxicity, ISO 10993-18 for chemical characterization, and USP 661.1 for packaging components. The material is not authorized for long-term implantable use or primary contact with parenteral pharmaceutical streams. Because acrylonitrile is a toxicologically controlled monomer, the injection molder must obtain a certificate of analysis for each lot and retain documentation that residual acrylonitrile is below the limit specified in the relevant packaging or device master file. Colorants and processing aids must be evaluated as part of the finished diagnostic assembly; silicone-based external mold releases are avoided because they migrate to the optical surface and interfere with reagent binding and photometric calibration.
Within domestic-appliance control-panel programmes, replacement of polycarbonate by SAN 326N A is feasible only where cumulative thermal load remains below the heat deflection temperature under 1.8 MPa stress as measured by ISO 75-2. The grade is suitable for washing-machine selector knobs, transparent program windows, decorative bezels, and non-current-carrying fascia; it is not suitable for oven doors, steam-sanitisation paths, or heated humidifier housings. Melt temperature is set at 220–240 °C, mold temperature at 50–70 °C to achieve high gloss on polished cavity inserts. Injection speed is kept at 40–60 mm/s with hold pressure of 50–60 MPa. Transparent amber or smoke tints are produced with solvent dyes at 0.02–0.08 wt%; opaque colours are generated with SAN-carrier masterbatch at 2–4 wt%. Polyethylene- or polypropylene-carrier masterbatches cause delamination at the gate and should not be used.
Surface texture is specified according to VDI 3400 texture cards; typical knob textures have a depth of 25–30 µm to reduce fingerprint visibility while preserving legibility of laser-etched icons. Laser marking is usually performed with 1064 nm fiber lasers at a power density that produces a contrast layer without burning the surface. Tensile and flexural data for validation are collected per ISO 527-2 and ISO 178. Snap-fit retention caps with arm lengths below 4 mm and deflection below 0.8 mm are acceptable; engagement cycles should be limited to 50 because SAN is more brittle than ABS. Chemical stress-crack resistance is evaluated with ASTM D543 at 0.5% applied strain using the exact detergent formulation; perfumed detergents containing terpenes have been observed to increase crazing. Flame rating of unfilled SAN 326N A is UL 94 HB. If IEC 60335-1 or product-specific clauses require V-0 or 5VA, flame-retardant modification is required and will generally reduce translucency; this change must be qualified before tooling approval.
Parts intended for direct contact with live terminals are excluded from the application envelope. Surface resistivity of the unfilled polymer is above 10^14 Ω/sq per ASTM D257, but dielectric strength is not a substitute for reinforced insulation. The comparative tracking index should be verified according to IEC 60112 if there is any assembly path to a printed circuit board or high-voltage lead.
Refrigerator shelf fronts, cold-use spice jar bodies, and transparent storage lids are molded from SAN 326N A only when the article is not intended for microwave, hot-fill, or heated dishwasher exposure. Food-contact compliance in the United States is evaluated under 21 CFR 177.1640 for styrene-acrylonitrile copolymers, with the end-use condition limited to cold contact. In the European Union, the finished article is tested under EU 10/2011 through overall migration per EN 1186 and specific migration per EN 13130; overall migration must remain below 10 mg/dm². Specific migration limits for styrene and acrylonitrile are 50 mg/kg and 0.01 mg/kg respectively. The molder must request a certificate of analysis for residual acrylonitrile from the resin producer; food-contact compliance is a compound-level property that can be lost by unsuitable colorants, mold releases, or blending with non-compliant recycled resin.
Cold-use storage lids with wall thickness 1.5–2.5 mm are processed at melt temperatures of 220–235 °C and mold temperatures of 35–50 °C. Ejection is delayed until the part surface is below 70 °C to prevent post-ejection warpage. Rectangular lids with aspect ratios above 3:1 are placed in static cooling fixtures immediately after ejection. Mold shrinkage is measured per ISO 294-4 and typically falls at 0.4–0.6% for this wall-thickness range. Living hinges are not recommended because SAN exhibits limited repeated flexural fatigue relative to polypropylene. Assembly by ultrasonic welding uses 20 kHz horns and energy directors of 0.2–0.4 mm height; solvent bonding is avoided to prevent adhesive residues and stress cracking.
Observed field failures in cold-use transparent articles occur when lids are placed in microwave ovens. Crazing and distortion appear above 85 °C, and migration testing at temperatures above the intended end-use condition can exceed the 10 mg/dm² overall migration limit. The material is not recommended for carbonated high-alcohol beverages or oil-containing foods above 5 °C without specific migration testing in 10% ethanol and olive oil simulants as prescribed by EU 10/2011.
Transparent paper-feed windows and scanner panels are typical office-equipment applications for SAN 326N A because the balance of transparency and stiffness is sufficient without the cost of polycarbonate. Unfilled SAN, however, exhibits surface resistivity above 10^14 Ω/sq per ASTM D257; that level permits dust adhesion and can contribute to paper jam sensor faults in dry office environments. If the equipment specification requires static-dissipative behaviour below 10^12 Ω/sq, a permanent antistatic additive is compounded at 0.5–1.5 wt%. This addition can raise haze from below 1.5% to 3–6% as measured per ASTM D1003 with a 2.0 mm polished plaque. The additive is predried with the base resin; melt temperature is reduced to 215–230 °C to avoid additive degradation, and mold temperature is set at 45–60 °C to control surface bloom. Published data for this specific configuration is limited; processors must validate additive migration against optical and tribological requirements before series production.
Ejector pin drag and vacuum release failures dominate textured cover scrap rates. Ejector pins of 6–10 mm diameter are placed on recessed surfaces; draft angles of at least 0.5° are used on textured ribs, and core-side EDM vents are added to reduce vacuum pull. Total luminous transmittance above 85% is generally required for scanner view windows, but surface haze above 5% can induce line-sensor image noise. Dimensional process capability for critical snap-fit dimensions is monitored with ISO 22514; a Cpk below 1.33 triggers tooling correction. Creep retention under constant latch load is evaluated per ISO 899-1; latch pre-load must remain below 2.0 MPa because SAN exhibits higher stress relaxation than polycarbonate in continuous service. Flame rating is UL 94 HB; if office-equipment enclosures require IEC 62368-1 fire-enclosure criteria, flame-retardant versions must be selected and optical clarity must be re-quantified.
Competitive Kumho Petrochemical SAN 326N A prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618005193850
Email: sales8@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Kumho Petrochemical SAN 326N A is a pelletised styrene-acrylonitrile random copolymer formulated for high-flow injection moulding. The bound acrylonitrile fraction is typically held within 24–26 wt%, which shifts the property envelope away from general-purpose polystyrene and toward a stiffer, more chemically resistant thermoplastic. Melt flow behaviour is specified by ISO 1133-1:2022 at 220 °C under a 10.0 kg piston load, with a representative high-flow envelope of 18–30 g/10 min. Density falls between 1.07 g/cm³ and 1.08 g/cm³ when tested to ISO 1183-1. The material is supplied as cylindrical or lenticular pellets with a bulk density suitable for hopper-equipped injection moulding machines, and the A designation is used on lot certificates to identify the natural, lubricated specification intended for multicavity tools and thin-wall parts where gloss and dimensional consistency are critical.
The high-flow envelope of SAN 326N A is most relevant when wall stock drops below 1.5 mm and flow-path-to-wall-thickness ratios exceed 120:1. In such cavities, the melt pressure at the gate may need to reach 80–120 MPa, while cavity sensors at the flow front can record 30–50 MPa during the packing transition. On production lines, multicavity tools for cosmetic packs or electronic housings are frequently run on electric or hydraulic machines with clamp force above 1,200 kN because the projected area filled at high packing pressure can generate cavity-opening forces that exceed the clamp margin of smaller presses. The screw configuration should use a general-purpose polyolefin/styrenic profile with a compression ratio near 2.0:1 and an L/D of at least 20:1; excessive low-shear zones produce unmelted granules in high-output cycles, while overly aggressive shear can raise melt temperature beyond the recommended 220–260 °C window. Rheological data for the grade indicate that melt viscosity drops strongly between 200 °C and 240 °C, which makes holding-pressure time and gate freeze time the controlling variables for sink-mark avoidance. When rib thickness exceeds 60% of adjacent wall thickness, gate seal should be confirmed by cavity-pressure decay rather than by a fixed timer, because premature screw-return can pull material back from the gate and produce microvoids at the rib base.
Moisture uptake in high-flow SAN is lower than in polycarbonate or polyamide, but storage in relative humidity above 60% can introduce enough surface moisture to cause silver streaking in thin-wall parts. Pre-drying in a desiccant hopper dryer at 80 °C for 2–4 h with a dew point of -30 °C or lower is therefore required before processing when sacks have been open for more than one shift or when ambient RH exceeds 60%. Drying beyond 4 h provides no measurable gain and risks pellet yellowing if dryer temperature control oscillates above 85 °C.
Because the acrylonitrile comonomer raises the glass transition and reduces free volume, high-flow SAN 326N A retains a useful thermal resistance despite its elevated melt flow. Heat deflection temperature under a 1.82 MPa flexural stress is typically reported in the range of 86–91 °C when measured by ASTM D648-16, while Vicat softening temperature at 50 N is commonly 104–108 °C under ISO 306. Mould shrinkage is anisotropic and depends on gate type and wall thickness, but a representative range of 0.2–0.6% can be expected using ASTM D955-08. The thermal stability of the styrene-acrylonitrile backbone is sufficient for continuous service in warm environments that would soften general-purpose polystyrene, but the material is not a high-heat engineering resin. Long-term exposure above 85 °C can produce post-mould shrinkage in constrained parts, and dimensional checks on critical snap-fit bosses should be taken after 24 h conditioning rather than immediately after ejection. The coefficient of linear thermal expansion is in the range of 6–8 × 10⁻⁵ K⁻¹, which is lower than that of polyolefins but higher than that of glass-filled SAN grades. Tool designers should therefore anticipate thermal expansion in assembled parts where the housing and bezel are made from dissimilar polymers.
| Property | Test Method | Typical Value or Range | Unit |
|---|---|---|---|
| Melt flow rate | ISO 1133-1:2022, 220 °C, 10.0 kg | 18–30 | g/10 min |
| Density | ISO 1183-1 | 1.07–1.08 | g/cm³ |
| Tensile yield stress | ASTM D638-14, 50 mm/min | 65–72 | MPa |
| Tensile elongation at break | ASTM D638-14 | 2–4 | % |
| Flexural strength | ASTM D790-17 | 100–110 | MPa |
| Flexural modulus | ASTM D790-17 | 3.2–3.5 | GPa |
| Notched Izod impact, 23 °C | ASTM D256-10 | 1.0–2.0 | kJ/m² |
| Heat deflection temperature, 1.82 MPa | ASTM D648-16 | 86–91 | °C |
| Vicat softening temperature, 50 N | ISO 306 | 104–108 | °C |
| Mould shrinkage, flow direction | ASTM D955-08 | 0.2–0.6 | % |
When SAN 326N A is substituted for a medium-flow SAN grade with an MFR near 8–12 g/10 min, the increase in melt flow shortens fill time and permits lower barrel temperatures, but it also reduces the molecular weight fraction that contributes to craze resistance. The practical consequence is that snap-fit arms and weld lines may exhibit lower load-bearing capacity under repeated assembly, so design verification should follow ISO 179-1 or ASTM D256-10 rather than relying on resin-supplier single-point data. Against rubber-modified ABS, SAN 326N A replaces the polybutadiene rubber phase with higher optical clarity and higher modulus. The absence of a discrete rubber phase reduces notched impact by an order of magnitude relative to high-impact ABS and eliminates the phase-separation haze that limits ABS in transparent applications, but also removes the toughening that prevents crack propagation in living hinges and under-the-hood clips. Compared with glass-reinforced SAN, the neat grade gives higher surface gloss and lower abrasion on tooling, while flexural modulus is roughly 3.3 GPa versus 7–9 GPa for glass-fibre-reinforced SAN. Mould shrinkage is therefore higher in neat SAN 326N A, and post-mould warpage is more sensitive to gate location and fibre-free orientation. In thin-wall transparent parts, glass-fibre grades are unsuitable because of translucency loss; in dimensionally stable structural brackets, glass-filled grades are preferred.
In appliance and cosmetic-packaging cavities, SAN 326N A is selected where high-gloss sidewalls, low haze, and resistance to household oils or detergents are required simultaneously. Surface gloss retention after moulding is influenced by mould temperature; a tool surface maintained at 40–70 °C using water-circulating temperature control units improves replication of polished cavity surfaces. Chemical resistance to dilute aqueous acids, alkalis, alcohols, and aliphatic hydrocarbons is adequate for cleaning-agent housings, but ketones, esters, chlorinated solvents, and aromatic hydrocarbons attack the resin and should be excluded from contact. Published data for this specific configuration is limited for aggressive solvent exposure; therefore, immersion testing by ISO 175 or ASTM D543-21 is required when a new fragrance, solvent-based adhesive, or cleaning concentrate is introduced. Because the resin is a styrene-acrylonitrile copolymer, stress cracking can occur under simultaneous load and chemical contact, particularly around moulded-in inserts and rivets.
Compliance records for SAN 326N A must include the styrene-acrylonitrile copolymer clearance under FDA 21 CFR 177.1040 where food-contact use is claimed, subject to end-use extraction limits and total non-volatile extractives specified by the regulation. Electrical and electronic applications are assessed against RoHS Directive 2011/65/EU as amended by EU 2015/863 for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE restrictions, plus the four phthalates DEHP, BBP, DIBP, and DBP. Flame classification is commonly UL 94 HB at a thickness of 1.5 mm or 3.0 mm, which limits use in load-bearing electrical enclosures requiring V-0 performance unless flame-retardant modification is validated by the end-user. The grade does not rely on bisphenol A chemistry, and does not contain intentionally added phthalate plasticisers. REACH registration under EC 1907/2006 is managed by the manufacturer, but downstream converters remain responsible for substances introduced through masterbatch, mould release, or post-mould coating.
| Standard or Regulation | Scope | Typical Basis for Claim |
|---|---|---|
| FDA 21 CFR 177.1040 | Styrene-acrylonitrile copolymer food contact | Resin composition and extraction testing under conditions of use |
| RoHS 2011/65/EU amended by EU 2015/863 | Restricted hazardous substances | Supplier declaration and analytical screening for 10 restricted substances |
| REACH EC 1907/2006 | Registration and SVHC communication | Article-level declaration when SVHC concentration exceeds 0.1 wt% |
| UL 94 HB | Horizontal burn rate | Flame test at 1.5 mm or 3.0 mm thickness |
| ASTM D543-21 | Chemical resistance | Comparative immersion or contact testing for specific service fluids |
A maximum melt residence time of 5 min should be observed when barrel temperatures exceed 260 °C, and thermal excursions beyond 280 °C degrade the molecular weight distribution and release volatiles. Purging after heat-sensitive masterbatch or after PVC contamination requires 3–5 barrel capacities of purging compound to remove acidic residues, because chlorinated polymer residues accelerate discolouration in the SAN melt. Strong bases, concentrated oxidising acids, and polar solvents degrade surface gloss and may craze moulded parts, so such contact should be excluded from service conditions or limited to short-term intermittent exposure with validated extraction testing.