| HS Code | 383611 |
| Density | 1.07 g/cm³ |
| Melt Flow Rate 220 C 10 Kg | 15 g/10 min |
| Tensile Strength At Yield | 68.9 MPa |
| Elongation At Break | 3.0% |
| Flexural Strength | 103 MPa |
| Flexural Modulus | 3440 MPa |
| Izod Impact Strength Notched | 1.5 kJ/m² |
| Rockwell Hardness | M85 |
| Vicat Softening Temperature | 108°C |
| Heat Deflection Temperature 1 82 Mpa | 90°C |
| Mold Shrinkage | 0.4-0.7% |
| Light Transmittance | 88% |
| Haze | 2.0% |
| Ul 94 Flame Rating | HB |
| Water Absorption | 0.20% |
| Dielectric Strength | 20 kV/mm |
| Volume Resistivity | >10^15 ohm-cm |
| Refractive Index | 1.57 |
As an accredited Chimei POLYLAC SAN D-168 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Chimei POLYLAC SAN D-168 comes in 25 kg moisture-resistant paper bags, securely palletized and stacked for industrial storage and transport. |
| Container Loading (20′ FCL) | A 20-foot FCL dry container loaded with palletized bags of Chimei POLYLAC SAN D-168, securely stowed for standard ocean freight. |
| Shipping | Chimei POLYLAC SAN D-168 is a styrene-acrylonitrile copolymer resin supplied as pellets in 25 kg bags, jumbo bags, or octabins. It is non-hazardous and not regulated as dangerous goods. Ship in dry, ventilated conditions; protect from moisture, heat, and direct sunlight using standard land, sea, or air freight. |
| Storage | Store Chimei POLYLAC SAN D-168 in a cool, dry, well-ventilated area, away from direct sunlight, heat, moisture, and ignition sources. Keep containers tightly closed to prevent contamination and dust accumulation. Avoid contact with strong oxidizers. Use proper grounding to prevent static buildup. Maintain good housekeeping and follow local regulations for plastic resin storage. |
| Shelf Life | Shelf life is typically 24 months from manufacture when stored unopened in a cool, dry place, away from direct sunlight. |
In high-gloss cosmetic rigid packaging, Chimei POLYLAC SAN D-168 is specified for thick-walled jar bases, overcaps and airless pump collars where poly(methyl methacrylate) grades exhibit excessive melt viscosity during sequential valve-gated filling of multi-cavity tools. The resin is dried in a desiccant dryer with a dew point below -30°C at 80°C for 3–4 h, reaching residual moisture below 0.05 wt% before plasticization. Injection moulding uses a general-purpose screw with an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.2:1 to 2.5:1; back pressure is held at 0.5–1.5 MPa and screw speed at 40–80 rpm. Melt temperature is maintained between 225°C and 245°C, while the mould is kept at 50–65°C. Hot runner manifold settings above 250°C or residence times exceeding 5 min can cause light yellowing because of acrylonitrile thermal degradation.
Transparent colour in cosmetic packaging is achieved with solvent-soluble anthraquinone or azo dyes at 0.02–0.08 wt%, not with particulate pigments above 40 nm, because pigment agglomeration increases haze measured under ASTM D1003. For deep-draw inner cores and threaded overcaps, external silicone-free mould release is preferred over internal release additives that reduce light transmission at wall thickness above 3.0 mm. Tool surfaces are diamond polished to SPI A-1 finish on the transparent face; draft angles on inner cores are 1–2° to reduce ejection-induced microstress. Finished jar bases with wall thickness 2.5–6.0 mm retain total light transmission above 89% and haze below 2% when measured by ASTM D1003. Packaging compliance is documented through REACH SVHC content below 0.1 wt% and, where the same pack is dual-marketed for food-like products, 21 CFR 177.1040 and EU 10/2011 migration limits apply.
Appliance control panels and washing machine programme selector windows are moulded from SAN D-168 where a clear window must be integrated into an opaque ABS frame by insert moulding or two-shot moulding. Melt-flow hesitation occurs when the gate land thickness falls below 1.2 mm because the SAN melt exhibits an apparent viscosity increase under high shear; this is observed on production presses of 160–300 tonnes clamp force. A fan gate with land width 6–10 mm and land thickness 1.5 mm avoids jetting and free-surface roughness across the window. During moulding, barrel melt temperature is set at 235–250°C, mould temperature at 60–80°C, packing pressure at 55–70% of peak injection pressure, holding time 8–12 s and cooling time 15–25 s for a wall stock of 2.0–3.0 mm. Back pressure of 1.0–2.0 MPa is used to homogenize masterbatch and prevent surface streaking.
Weld-line haze around bosses and display windows is managed with sequential valve gating, where two nozzles open 0.3 s apart, or with overflow tabs of 0.3–0.5 mm thickness placed on the parting line to shift the weld line to a hidden edge. A mould venting depth of 0.02–0.03 mm is necessary on the parting line because gas entrapment generates burn marks at flow front convergence. When the finished window is exposed to domestic cleaning fluids, stress-crack resistance is evaluated by ISO 22088-3 at 0.5% flexural strain. If the appliance is used near UV light, a UV package of 0.3–0.5 wt% benzotriazole absorber and 0.2 wt% HALS is dry-blended into the SAN matrix; however, amine-based antistatic additives should be avoided because they can produce colour shift above 260°C melt temperature.
Representative processing windows reported across downstream SAN D-168 moulding trials are listed below; values are operational observations, not manufacturer specification limits.
| Downstream segment | Melt temperature | Mould temperature | Residual moisture before moulding | Reference test method |
|---|---|---|---|---|
| Cosmetic jar base | 225–245°C | 50–65°C | <0.05 wt% | ASTM D6869-17 / ISO 15512:2016 |
| Appliance control window | 235–250°C | 60–80°C | <0.05 wt% | ISO 15512:2016 |
| Medical diagnostic cover | 230–245°C | 45–55°C | <0.06 wt% | ASTM D6869-17 |
| Filter bowl | 225–240°C | 55–70°C | <0.05 wt% | ISO 15512:2016 |
Bench-top analyser covers and non-patient-contact diagnostic equipment housings are injection-moulded from SAN D-168 because the copolymer can be solvent-bonded to opaque ABS structural ribs using cyclohexanone or methyl ethyl ketone under controlled extraction ventilation. Before moulding, resin is dried at 80°C for 4 h to residual moisture below 0.06 wt%. Melt temperature is held at 230–245°C, mould temperature at 45–55°C, and the as-moulded cover is annealed in a forced-air oven at 70°C for 2 h with a heating rate below 0.5°C/min and cooling rate below 0.8°C/min to relax gate stress without inducing warpage.
Ethylene oxide sterilization at 50–55°C and 30–70% relative humidity does not produce measurable distortion in housing covers, but residual ethylene oxide levels must be aerated to satisfy ISO 10993-7:2008 limits. Steam autoclave exposure at 121°C is outside the operating window because Vicat softening onset is near 101°C, and load-bearing bosses distort under autoclave pressure. If gamma sterilization is requested, the dose should be limited to <15 kGy because higher absorbed dose produces visible yellowing and measurable notched impact loss; published data for this specific grade under gamma irradiation is limited. Material declarations for medical equipment housings are structured around ISO 10993-1:2018 when patient contact is intended, IEC 62321 methods for RoHS restricted substances, and REACH Annex XVII restrictions.
Chimei POLYLAC SAN D-168 is specified for transparent bowls in pneumatic lubricators, low-pressure hydraulic oil level gauges and filter bowls where fluid contact is limited to mineral oils, aliphatic hydrocarbons or dilute aqueous solutions at service temperature not exceeding 55°C.
Chemical compatibility is confirmed by immersion in the service fluid at 60°C for 7 days under 0.5% flexural strain, followed by craze assessment according to ISO 22088-3. The grade is not recommended for continuous contact with aromatic hydrocarbons, esters, ketones, chlorinated solvents, or methanol and ethanol blends above 20 vol%; hydraulic fluids containing phosphate ester friction modifiers produce environmental stress cracking at threads and sealing bosses. For injection moulding, wall thickness is set at 3.0–6.0 mm and the gate is positioned at the base flange to avoid a knit line in the pressure-containing sidewall. A two-stage injection speed profile is used: 55–75 mm/s initial fill for the flange, then 25–35 mm/s across the sidewall to reduce gas traps and flow hesitation. Melt temperature is 225–240°C, mould temperature 55–70°C, and packing pressure is maintained until gate freeze.
Thread-capped bowls are assembled with a calibrated torque screwdriver set to 1.5–2.5 N·m; higher tightening torque creates microcrazing at the sealing boss after mineral oil contact under cyclic pressure between 0.1 MPa and 0.6 MPa. Sealing surfaces must not be flame polished, because local thermal stress above 100°C initiates microcracking in SAN. Finished sight glass components are pressure tested at 0.8–1.0 MPa pneumatic pressure with dry air after 24 h annealing at 70°C to stabilize residual stress. For regulatory documentation, the material requires REACH SVHC declaration and RoHS compliance by IEC 62321 screening; potable water contact requires additional certification against local standards such as NSF/ANSI 61 and BS 6920 when the filter bowl is used in drinking water systems.
Office equipment clear covers for scanner glass surrounds, point-of-sale terminal windows and laser printer paper cassettes are injection-moulded from SAN D-168 where cleaning protocols use quaternary ammonium compounds or hydrogen peroxide-based disinfectant wipes at 30–40°C service temperature. Unlike polycarbonate, SAN D-168 shows less environmental stress cracking under alcohol and quaternary ammonium solutions, but validation is required by ISO 22088-3 with the specific disinfectant at 0.5% applied strain. Moulding uses a melt temperature of 235–245°C, a mould temperature of 60–75°C, and a parting-line vent depth of 0.02–0.03 mm to prevent burn marks in flat clear panels of approximately 150 mm × 250 mm.
Surface hardness and scratch resistance are increased with a UV-curable acrylate topcoat applied after moulding; coating adhesion is checked by ASTM D3359-17 cross-hatch tape test to a rating of 5B. The transparent cover must retain light transmission above 88% and haze below 2% when measured under ASTM D1003. If the equipment is installed near windows, a stabilizer package of 0.3–0.5 wt% benzotriazole UV absorber and 0.2 wt% HALS is compounded into the SAN matrix; indoor-only parts do not require this addition. Regulatory documentation for office equipment covers is limited to RoHS 2011/65/EU Annex II and REACH SVHC screening. If a V-2 rating is required, a flame-retardant additive must be selected and validated for transparency, because many brominated flame retardants increase haze and reduce light transmission.
In dry-goods chutes, closure caps and shallow clear lids for food processors, SAN D-168 is specified for transparency, gloss and food-contact compliance, not for impact-bearing jar bodies. Melt temperature is maintained at 220–235°C and mould temperature at 50–60°C. The gate is placed on the sidewall rim with tab thickness above 1.5 mm to avoid jetting into the transparent panel; cycle time for a 2.5–3.5 mm wall lid is 30–45 s on a 180–250 tonne injection press.
Food-contact compliance is established under 21 CFR 177.1040 and EU 10/2011; overall migration into food simulants is below 10 mg/dm², and acrylonitrile-specific migration must meet the relevant Annex I limit for the intended food category. Only food-grade external silicone release is used during moulding; internal release additives that are not listed for the target regulatory region must be excluded. The finished lid is not suitable for bottom-rack dishwasher exposure above 75°C or for microwave reheating because thermal distortion occurs near the SAN Vicat softening range. Repeated exposure to 0.5% sodium hydroxide solution in alkaline dishwasher detergents can cause surface haze on unpolished sidewalls; polished transparent faces show less change but require validation by immersion testing for 130 cycles at 65°C. Snap-fit hinges should be replaced with living hinges only after prototype flex testing, because SAN notch sensitivity causes hinge fracture under repeated loading.
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Chimei POLYLAC SAN D-168 is a styrene-acrylonitrile copolymer supplied as pellets for injection molding, thin-wall extrusion, and selected co-extrusion operations in which clarity, chemical resistance, and high melt flow are simultaneously specified. The grade is produced within the POLYLAC SAN D-series by continuous mass polymerization; its acrylonitrile content is typically in the range of 24–28 wt%, with the balance styrene. Density at 23°C is 1.08 g/cm³ measured according to ISO 1183-1:2019 or ASTM D792. Because open data sheets for this specific D-168 configuration are limited, the numerical ranges cited in this document are representative of high-flow SAN D-series benchmarks and should be verified against the lot-specific certificate before mold design, regulatory testing, or process validation.
Storage and handling conditions influence process stability. Pellets should be kept in sealed containers at temperatures below 30°C and protected from UV exposure. Moisture uptake follows Fickian diffusion; at 23°C and 50% RH, equilibrium moisture content of SAN is typically 0.15–0.25 wt%. Above 60% RH, pre-drying becomes mandatory because excess surface moisture contributes to surface splay, hydrolysis-induced molecular weight reduction, and melt instability during processing.
Rheological screening under ISO 1133-1:2022 at 220°C using a 10 kg load places D-168 in the high-flow segment, with melt flow rate values commonly in the range of 28–38 g/10 min, corresponding to melt volume rates near 30–40 cm³/10 min. Medium-flow SAN grades often fall below 15–20 g/10 min, while low-flow extrusion SAN may fall below 5–8 g/10 min. The high melt flow of D-168 allows thin-wall fill sections below 1.5 mm and reduces injection pressure compared with medium-flow SAN at identical wall thickness; the exact reduction depends on gate geometry, runner length, and mold temperature. The trade-off is lower melt strength, lower strain at break, and reduced notched impact resistance. The lower molecular weight required for this melt flow also means D-168 is not specified where weld lines experience high tensile stress or where long-term creep resistance under load is critical.
Differences from POLYLAC ABS are structural. D-168 contains no polybutadiene rubber phase, so it appears transparent and exhibits higher surface hardness, while ABS is opaque and ductile. Notched Izod impact measured under ISO 180/1A at 23°C is typically 2.0–3.0 kJ/m² for D-168, whereas general-purpose ABS grades typically exceed 15 kJ/m². Compared with general-purpose polystyrene, D-168 offers higher tensile strength, better resistance to aliphatic hydrocarbons and cooking oils, and a Vicat softening temperature approximately 10–15°C higher. Compared with PMMA, D-168 has lower light transmittance and higher haze, but better resistance to alcohol-based cleaners and lower equilibrium moisture uptake.
Pre-drying is required for D-168 when handling humidity exceeds 60% RH. A desiccant dryer with a dew point below −30°C and hopper residence time of 2–4 h at 80–85°C reduces moisture content below 0.05%. Barrel profiles from rear to nozzle are typically 190–210°C, 210–230°C, 220–240°C, and 225–240°C; measured melt temperature should remain between 200°C and 230°C. Residence time at melt temperature above 260°C should be limited because acrylonitrile degradation produces yellowing, black specks, and surface splay. Mold temperature from 40°C to 80°C controls surface gloss, cooling stress, and knit-line strength. A general-purpose injection screw with an L/D ratio of 20:1–25:1 and compression ratio of 2.0:1–2.5:1 is adequate for homogeneous melt. Hot runner systems with valve gates should avoid sharp restrictions that generate adiabatic shear heating above 1000 s⁻¹; thermocouple placement in the nozzle and hot runner manifold is necessary to detect local temperature overshoot.
Actual injection pressure required on a typical 100–150 ton machine falls between 70–100 MPa hydraulic, depending on wall thickness, gate design, and melt temperature. Hold pressure should be profiled to compensate for shrinkage without overpacking. Packing at pressure above 80 MPa can produce stress birefringence around the gate, which reduces transparency in natural D-168 parts. Short-shot defects in core-pin areas have been observed when mold temperature falls below 40°C; raising mold temperature to 60°C or increasing melt temperature to 230°C improves knit-line strength in such zones.
The representative values in the following table are derived from test plaques conditioned at 23°C and 50% RH in accordance with ISO 291. Lot-specific certificates may differ because of colorants, lubricants, or mold release agents. The data are not guaranteed specification limits but provide a technical baseline for material selection and mold-filling simulation.
| Property | Test Method | Condition | Representative Value |
|---|---|---|---|
| Melt flow rate | ISO 1133-1:2022 / ASTM D1238 | 220°C, 10 kg | 28–38 g/10 min |
| Density | ISO 1183-1:2019 / ASTM D792 | 23°C | 1.08 g/cm³ |
| Tensile strength at break | ISO 527-2 / ASTM D638-14 | 23°C, 50 mm/min | 68–75 MPa |
| Tensile modulus | ISO 527-2 / ASTM D638 | 23°C, 1 mm/min | 3600–3800 MPa |
| Flexural strength | ISO 178:2019 / ASTM D790-17 | 23°C, 2 mm/min | 100–115 MPa |
| Flexural modulus | ISO 178:2019 / ASTM D790-17 | 23°C | 3400–3700 MPa |
| Notched Izod impact | ISO 180/1A | 23°C, edgewise | 2.0–3.0 kJ/m² |
| Rockwell hardness | ASTM D785 | M scale | 78–84 |
| Vicat softening temperature | ISO 306 / ASTM D1525 | B/50, 50°C/h | 104–108°C |
| Heat deflection temperature | ISO 75-2/Af / ASTM D648 | 1.82 MPa, flatwise | 88–93°C |
| Light transmittance | ASTM D1003 | 3.2 mm natural | 88–90% |
| Haze | ASTM D1003 | 3.2 mm natural | <2.0% |
| Mold shrinkage, flow direction | ISO 294-4 / ASTM D955 | 60 × 60 × 2 mm | 0.4–0.7% |
| Water absorption after 24 h | ISO 62 / ASTM D570 | 23°C | 0.15–0.25% |
Specimen geometry matters in comparative testing. ISO 527-2 type 1A tensile bars injected at a mold temperature of 60°C show less frozen-in orientation than edge-gated specimens from cold molds. HDT values measured under ISO 75-2/Af are sensitive to cooling rate during plaque molding; rapid cooling increases free volume and can lower HDT by several degrees. The Vicat softening temperature under ISO 306 method B/50 uses a 50 N load and heating rate of 50°C/h, and therefore should not be confused with method A/120. Light transmittance and haze are measured on natural unpigmented plaques; addition of colorants, regrind, or external lubricants shifts optical values.
The thermal and mechanical performance envelope creates a narrow processing window. Increasing melt temperature to 240°C improves flow length and knit-line strength but reduces permissible melt residence time, accelerates nitrile degradation, and increases yellowness index. Lowering mold temperature below 40°C shortens cycle time but freezes in orientation and raises chemical stress cracking risk in detergent or oil exposure. A property cliff-edge occurs at wall sections below 0.8 mm, where high shear rates in the gate produce localized melt temperatures above 250°C even when the barrel set point is 220°C. In such cases, larger gates or multiple gates are required rather than increasing barrel temperature.
Substitution scenarios require technical review of load-bearing, chemical exposure, and thermal sterilization conditions. D-168 is specified in transparent stationery, cosmetic containers, household appliance lenses, food processor bowls, small appliance housings, and similar rigid parts where moderate impact loads and detergent or oil resistance are required. In food processor bowls, the high melt flow permits filling of complex lids and snap-fit undercuts without excessive clamp force; however, the low notched Izod impact value means the part must avoid sharp internal corners and high gate stress. For PMMA replacement, D-168 offers lower density and better resistance to alcohol-based cleaners, but it has lower light transmittance and lower continuous-use temperature. For ABS replacement, D-168 provides transparency and higher surface hardness, but loses the ductile failure mode of ABS and may be unsuitable for drop-impact components.
In production-scale injection molding on fast cycling machines, D-168 exhibits sensitive gate vestige quality under high holding pressure. Holding pressure above 80 MPa can produce stress birefringence around the gate; pack pressure should be profiled to compensate for shrinkage without overpacking. Batch-to-batch variation in melt flow rate for high-flow SAN D-series grades can reach ±3 g/10 min. Processors should request melt flow and Vicat data from each lot and adjust holding pressure and cushion position accordingly. On a 120-ton injection molding machine producing cosmetic containers, transfer by screw position rather than hydraulic pressure reduces gate blush and improves dimension stability.
Published data for D-168 in blow molding and thick-sheet extrusion is limited. The low melt strength makes these processes difficult; D-168 is not specified where parison hang strength or sag resistance is critical. For thin-sheet extrusion, melt temperature should remain near 210–230°C, and polished roll temperatures should be maintained above 70°C to minimize surface haze. Excessive regrind addition above 30 wt% can reduce light transmittance and increase haze; regrind must be dried to the same moisture target as virgin pellet.
Food-contact compliance for D-168 is not intrinsic to the base resin alone. For natural resin in food-contact articles, the relevant FDA citation is 21 CFR 177.1040 for acrylonitrile/styrene copolymers; migration of residual acrylonitrile monomer must be controlled below the regulatory limit. In the European Union, plastic materials and articles intended for food contact must satisfy Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm² and specific migration limits for monomers. Compliance of pigmented D-168 requires validation of each colorant package because heavy-metal pigments may alter RoHS and food-contact status.
The regulatory matrix in the following table summarizes the usual status for natural D-168 resin. End users are responsible for validating the final article under intended use conditions, including temperature, time, and food simulant type.
| Regulation or Standard | Requirement | Typical D-168 Status |
|---|---|---|
| RoHS Directive 2011/65/EU incl. (EU) 2015/863 | Pb, Hg, Cd, Cr(VI), PBB, PBDE threshold 0.1 wt% per homogeneous material | Natural resin normally conforms; pigmented grades require documentation |
| REACH Regulation (EC) 1907/2006 | Candidate List SVHC below 0.1 wt% in article | Supplier SDS and REACH declaration required |
| FDA 21 CFR 177.1040 | Acrylonitrile/styrene copolymers for food-contact articles | Lot-specific migration validation required |
| Regulation (EU) No 10/2011 | Overall migration limit 10 mg/dm²; specific migration limits for styrene and acrylonitrile | Food simulant testing on final article required |
| UL 94 HB | Horizontal burn classification | Typically HB at 1.5 mm and 3.0 mm without flame retardant |
| ISO 11469:2021 | Marking of plastics for identification | Identification as >SAN< unless filled or modified |
At production scale, D-168 should not be combined with copper-based colorants under long residence times because copper ions accelerate thermal degradation. The material is also incompatible with amine-based additives that discolor at processing temperatures. For hot runner systems with valve gates, periodic purging with a medium-flow SAN purge compound at 200°C is used to remove oxidized residue and prevent black speck contamination. Clean, dry regrind may be incorporated into D-168 at levels up to 30 wt% provided optical performance remains within specification; higher regrind fractions require additional testing for light transmittance, haze, and notched Izod impact.