| HS Code | 464309 |
| Manufacturer | Ningbo Dachuan Polymer Co., Ltd. |
| Product Name | ABS SNV |
| Material Type | Acrylonitrile Butadiene Styrene (ABS) |
| Grade | SNV |
| Form | Pellets |
| Appearance | Opaque |
| Flame Retardant | Yes |
| Ul94 Rating | V-0 |
| Density | 1.18 g/cm³ |
| Melt Flow Rate | 10 g/10 min (220 °C/10 kg) |
| Tensile Strength | 40 MPa |
| Flexural Strength | 65 MPa |
| Notched Izod Impact Strength | 10 kJ/m² |
| Heat Deflection Temperature | 75 °C (1.82 MPa) |
| Vicat Softening Temperature | 90 °C |
| Rockwell Hardness | R100 |
| Molding Shrinkage | 0.4–0.6 % |
| Drying Temperature | 80–90 °C |
| Processing Temperature | 200–230 °C |
| Processing Method | Injection Molding |
As an accredited Ningbo Dachuan Polymer ABS SNV factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Ningbo Dachuan Polymer ABS SNV is packed in 25 kg net-weight moisture-proof bags, palletized for industrial storage and transport. |
| Container Loading (20′ FCL) | Ningbo Dachuan Polymer ABS SNV loaded into a 20′ FCL container, palletized, secured, and protected for dry ocean freight. |
| Shipping | Ningbo Dachuan Polymer ABS SNV is a non-hazardous ABS resin in pellet form. Ship in clean, dry, closed containers at ambient temperature, protected from moisture, direct sunlight, and contamination. Avoid excessive heat and keep packaging intact; no special UN hazard classification is required for transport. |
| Storage | Store Ningbo Dachuan Polymer ABS SNV in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, flames, and strong oxidizers. Keep containers tightly closed and palletized to prevent moisture, dust, and contamination. Avoid prolonged high temperatures and UV exposure; do not stack excessively. Follow the SDS and local storage regulations. |
| Shelf Life | Shelf life is typically 12 months when stored in original unopened packaging under cool, dry conditions, away from direct sunlight. |
To achieve dimensional stability in thin-wall electronic enclosures, Ningbo Dachuan Polymer ABS SNV is first dried in a desiccant hopper dryer at 80°C for 2–4 h until the residual moisture content falls below 0.05%. Production-scale processing of this resin grade on a three-zone reciprocating screw with L/D ratio between 20:1 and 24:1 and a compression ratio of 2.0:1–2.5:1 requires barrel temperature settings of 210–240°C from the feed throat to the nozzle, while the nozzle itself is maintained at 230–240°C. The mould surface temperature is held at 40–70°C; lower mould temperatures reduce cycle time but increase moulded-in orientation in the gate area, which raises the probability of environmental stress cracking when the part is exposed to isopropanol-based cleaning agents during printed circuit board assembly. The melt should not be held above 260°C for more than 10 min residence time, because thermal degradation of the butadiene phase produces yellowing and a sharp styrene odour that cannot be masked by subsequent painting or plating.
Fill speed and packing pressure are not specified solely by the resin supplier; they are derived from the part’s flow-length-to-wall-thickness ratio. For a nominal wall thickness of 1.2–2.0 mm, the injection velocity is set high enough to fill the cavity before the melt freezes at the flow front, typically 80–150 mm/s screw advance speed on a 100–160 t clamp machine. Packing pressure is then applied at 50–70% of peak hydraulic pressure for 3–6 s, followed by holding pressure decay. Because grade-specific melt flow rate data for SNV is not published in this review, shear-rate-dependent viscosity must be measured by capillary rheometry according to ISO 11443:2021 before establishing the injection velocity profile. Molded parts intended for information technology equipment must demonstrate flame spread resistance consistent with UL 94; general-purpose ABS grades at 3.0 mm thickness typically achieve HB, and V-0 classification requires compounded flame-retardant systems that are not part of the natural SNV resin. Terminal products include router housings, power adapter shells, and network switch enclosures evaluated under IEC 62368-1 for mechanical enclosure integrity and accessibility of internal circuits.
Mould filling simulation using Moldflow or Moldex3D is commonly performed to locate gate position and weld lines before cutting tool steel. The software requires accurate pressure-volume-temperature data for ABS SNV, which should be obtained from the supplier or by piston-cylinder measurement according to ISO 17744. On production tools, valve-gated hot runner tips with diameters of 0.8–1.2 mm are preferred for thin-wall parts; smaller tips raise shear heating and accelerate local degradation, while larger tips create gate vestige above the dimensional tolerance in ISO 2768-1 class L. Ejector pins must be placed on ribs and bosses rather than on visible surfaces, because visible ejector marks can act as crack initiation sites under repeated thermal cycling from room temperature to 60°C during powered operation.
| Parameter | Injection moulding (thin-wall) | Sheet extrusion/thermoforming |
|---|---|---|
| Predrying temperature | 80°C | 80°C |
| Residual moisture | 0.05% max | 0.05% max |
| Melt temperature | 210–240°C | 210–230°C |
| Tool / roll temperature | 40–70°C | 60–90°C roll stack |
| Typical cycle / line speed | 25–45 s for 2 mm wall | 3–8 m/min for 2–5 mm sheet |
| Post-forming requirement | Cool for dimensional stability | Post-condition 24 h at 23°C, 50% RH |
Gate-seal time and mould temperature deviation determine the upper boundary of the packing phase. In appliance structural parts such as washing machine control panels, air purifier shells, and vacuum cleaner bodies, ABS SNV is processed at melt temperatures of 230–245°C and mould temperatures of 50–70°C. The packing phase must remain active until the gate solidifies; premature release of packing pressure results in sink marks on ribbed surfaces and voids behind snap-fit bosses. On a 250 t toggle clamp machine with a hot runner manifold, the packing time for a 2.5 mm thick panel is typically 5–8 s, while the cooling time is set to 18–25 s for dimensional stability before ejection. The mould temperature variation across the cavity should not exceed ±5°C because differential shrinkage across the part causes warpage that exceeds flatness tolerances in ISO 2768-1 class L. Pressure transducers embedded in the cavity near the gate and at the last-fill location track the cavity pressure differential; a pressure drop above 20 MPa across these two points indicates that the packing phase is no longer transmitting force to the solidifying core, and the gate freeze time must be increased or the gate diameter enlarged.
Colour concentrate addition at 2–4 wt% is the common let-down ratio for pre-coloured appliance grades; higher addition levels above 4 wt% require impact retention testing because the carrier resin in the masterbatch can reduce Charpy notched impact strength measured by ISO 179-1:2010. The processing window narrows when recycled regrind is introduced. As a general boundary, regrind content should not exceed 20 wt% without conducting ISO 178:2019 flexural modulus and ISO 180:2023 Izod impact validation, because repeated thermal histories oxidise the butadiene phase and create a shift in ductile-to-brittle transition temperature. The screw recovery time must be monitored batch-to-batch; an increase above 15% from the virgin baseline often indicates regrind particle size variability or hopper bridging. Terminal appliance housings are subject to glow-wire testing under IEC 60695-2-11 for unattended appliances; the natural ABS SNV grade alone does not confer a self-extinguishing rating, so end-use certification depends on part thickness and any flame-retardant additive package. Purging between colour changes should use an acrylic or polystyrene-based purging compound; PVC residues in the hopper are incompatible because they release hydrogen chloride at processing temperatures and cause surface splay.
In sheet extrusion of ABS SNV, a single-screw extruder with a barrier screw design and L/D of 30:1–36:1 is required to provide sufficient melting capacity for a 1200–1800 mm wide flat die. The melt temperature at the die entry is maintained at 210–230°C; the chrome-plated polishing roll stack is operated with the first roll at 80–90°C, the second roll at 70–80°C, and the third roll at 60–70°C to produce a sheet with low residual orientation. The die gap is set 10–15% wider than the target sheet thickness to compensate for drawdown and edge neck-in. The extrudate is pulled through a roll stand at a line speed of 3–8 m/min depending on sheet thickness from 2–5 mm. Drying remains mandatory: if pellets are not dried below 0.05% moisture, micro-bubbles appear in the sheet as a result of water vapour expansion, and the surface defect is not removed by subsequent thermoforming. The sheet is then post-conditioned at 23°C and 50% RH for 24 h before forming. Cast roll temperature above 95°C causes the sheet to stick to the roll surface and produces build-up lines; below 60°C the sheet cools too rapidly and develops differential skin-core orientation that leads to curling after trimming.
Thermoforming of the extruded ABS SNV sheet into luggage shells or equipment covers is carried out with the sheet surface temperature between 140°C and 180°C, measured with an infrared pyrometer. Below 140°C, the sheet does not uniformly replicate the mould texture; above 180°C, the butadiene phase degrades and the sheet surface develops yellowing and a burnt odour. The plug assist speed is adjusted to avoid premature cooling on the mould surface, and the forming pressure is typically 0.4–0.8 MPa for vacuum forming. After forming, the parts are trimmed with CNC routers, and the edge stress concentrations are evaluated by ASTM D256 Izod impact testing of notched specimens cut from the formed part. The terminal product is subject to dimensional tolerance inspection under ISO 2768-1 and to heavy-metal migration limits under REACH Annex XVII for consumer goods. For luggage shells that are exposed to airport handling, corner impact testing according to ISO 15181 or customer-defined drop tests is applied, because thin sections near the corner radii can fail in a brittle mode if the sheet was formed below 140°C and retained high orientation.
Automotive interior trim components such as door panel inserts, centre console side garnishes, and passenger airbag cover backings are moulded from ABS SNV when the drawing specifies a balance of rigidity and low-temperature ductility. The material is processed at 230–250°C melt temperature and 50–60°C mould temperature; the mould cavity is often textured with a grain depth of 0.05–0.15 mm to reduce gloss and hide flow lines. The packing pressure must be sufficient to transfer the grain pattern without causing flash at the parting line; cavity pressure sensors are used to maintain a peak cavity pressure of 30–50 MPa during the packing phase. The injection speed is designed to fill the cavity within 60–80% of the maximum machine injection rate, because excessive shear at the gate can cause localised burn marks and degradation of the polybutadiene phase. On actual production lines, grain collapse is most frequently observed near the last-fill area, where the cavity pressure drops below 15 MPa before the melt freezes; flow simulation with pressure trace validation is used to reposition the gate before tool texturing is committed.
Low-temperature impact retention is assessed by ISO 180:2023 Izod notched impact at -30°C, because door panel retention clips must survive cold-weather demoulding and assembly. Standard ABS grades generally show a drop in notched impact toughness as the temperature approaches the glass transition of the continuous styrene-acrylonitrile phase; the actual value for SNV must be measured on production material because the supplier datasheet may not list sub-zero data. For interior parts, fogging and VOC emissions are evaluated using VDA 278 or ISO 12219-2; unmodified general-purpose ABS SNV may contain residual styrene monomer and oligomers, so a ventilation step or a low-emission grade is required if the automotive specification imposes fogging limits below 2 mg per 10 g of sample. The terminal component is validated for scratch resistance using DIN EN ISO 1518-1 or a five-finger scratch test; if the specification requires high gloss retention after abrasion, a hardcoat or scratch-resistant additive is necessary. Direct sunlight exposure on upper instrument panel skins is outside the recommended use boundary for this unmodified grade unless UV stabilisation is compounded separately.
When electroplating is specified for ABS SNV components, the first operation is a chromic acid–sulfuric acid etching step that selectively oxidises the butadiene-rich domains to create a micro-porous surface for mechanical interlocking. The etching bath normally contains 380–420 g/L chromic acid and 180–220 g/L sulfuric acid at 60–70°C for 5–10 min. The etch rate depends on the butadiene content and particle size distribution of the ABS grade; electroplating-grade ABS typically contains 15–30 wt% butadiene with a controlled bimodal particle size distribution. General-purpose SNV may not meet the etch uniformity required for automotive brightwork, so a pre-production trial according to ASTM B727-04 is required before the resin is accepted for electroplating. After etching, the part is neutralised in a reducing bath, activated with palladium-tin colloid, and coated with electroless nickel or copper to a thickness of 0.3–0.5 μm before electroplating with semi-bright nickel, bright nickel, and chromium. The adhesion between the plated metal and the ABS substrate is tested by ASTM B533 peel adhesion; values below 0.18 N/mm indicate insufficient etch depth and poor interlocking, while values above 0.45 N/mm are typical of well-etched plating grades but may not be attainable with SNV without process optimisation.
Thermal cycling of electroplated ABS parts from -30°C to 80°C is used to detect blistering and peel failures caused by differences in the coefficients of linear thermal expansion between the metal layer and the polymer substrate. The ABS SNV moulding must be free of internal stress before plating; moulded-in stress can be revealed by immersion in glacial acetic acid at 23°C for 3 min, where white crazes indicate high stress regions near gates and ejector pins. If stress cracking is observed, the injection moulding parameters must be adjusted by increasing the mould temperature to 60°C, reducing injection pressure, or using a larger gate diameter. Terminal electroplated parts include automotive door handles, grille surrounds, and sanitary fitting covers, all of which require final chromium appearance under ISO 1456 classification. The plating line must document the etch tank temperature within ±2°C of the set point, because bath temperature excursions above 72°C can over-etch the surface and reduce peel adhesion to below the acceptance limit.
ABS SNV is suitable as a base resin for extrusion of fused deposition modelling filament with nominal diameters of 1.75 mm and 2.85 mm. The pellet feedstock is dried to 0.03% moisture or below using a vacuum dryer at 80°C for 4 h, because residual water in the polymer melt creates vapour voids that cause diameter fluctuation and filament breakage during spooling. The extrusion line consists of a single-screw extruder with L/D 28:1–32:1, a melt pump to damp pressure oscillations, a water trough with 40–60°C water bath, a laser diameter gauge with closed-loop feedback to the haul-off unit, and a spooler. The melt temperature at the die is controlled at 200–220°C; higher temperatures reduce melt strength and cause sagging in the water bath, while lower temperatures increase die swell and produce ovality. The drawing ratio between the die opening and the final filament is set to 1.5:1–2.0:1 to achieve roundness better than 0.05 mm diameter tolerance and ovality 0.03 mm. The haul-off speed is varied by the feedback loop at 20–80 m/min depending on filament diameter; speed instability above ±2% produces diameter waves that exceed the tolerance limits in consumer-level extruders.
During FDM printing of the resulting filament, the heated build platform is maintained at 100–110°C for ABS to control warpage, and the extrusion nozzle temperature is 230–250°C. The volumetric flow rate is set to 10–15 mm³/s for a 0.4 mm nozzle orifice; exceeding this range without adjusting the part cooling fan causes poor interlayer adhesion and delamination along the Z-axis. The terminal printed parts are evaluated for tensile strength in the XY plane following ASTM D638-14 Type V specimens, and interlayer bond strength is measured by ASTM D2094 or a modified tensile test. The user must note that unmodified natural ABS SNV has a shrinkage coefficient of 0.7–0.8%, and the actual shrinkage must be measured on the extrusion lot before scaling to large-format printing. The inherent odour and styrene monomer release during printing require local exhaust ventilation, and the operator exposure limit for styrene is covered by ACGIH TLV 20 ppm and national occupational exposure regulations. Spooled filament should be vacuum-sealed with desiccant because moisture uptake above 0.1% after opening causes bubbling at the nozzle and a dull surface on the printed layer.
Under regulatory pressure from EN 71-3:2019+A1:2021, toy components and juvenile consumer goods moulded from ABS SNV must satisfy migration limits for toxic elements and phthalate restrictions under REACH Annex XVII, Entry 51. The injection moulder controls the feedstock to ensure the virgin pellets do not contain cadmium, lead, mercury, chromium VI, arsenic, selenium, barium, and antimony above the specified migration limits. Colour masterbatch must be selected from suppliers with test reports showing compliance with these limits, because the masterbatch carrier and pigment trace metals are the most common source of non-compliance. The moulding process uses melt temperature 210–240°C and mould temperature 40–60°C; ejection pin marks on visible surfaces are minimised to reduce stress concentrations. A post-mould annealing step at 70°C for 2 h may be specified for parts with snap-fit inserts or embedded metal components to relieve orientation and reduce cracking during later assembly. Any volatile residual styrene monomer in the finished part must be verified by headspace gas chromatography, because some toy brands impose a styrene-specific emission limit that is lower than the general VOC threshold in ISO 12219-2.
Toys such as construction brick assemblies, doll furniture, and ride-on bodies made from ABS SNV require impact testing according to ASTM F963-23 and sharp-edge testing according to ISO 8124-1:2022. The falling weight impact test is used to ensure that no small parts are generated that could become a choking hazard. The material’s notch sensitivity means that gate locations should be placed away from high-stress corners, and multiple gates should be balanced to avoid weld lines. The moulded toy parts must not develop sharp edges after UV ageing or dishwasher cleaning, so the stabilisation package should be verified by ISO 4892-2 cycle A for 200 h before release. The final product documentation must retain the lot-specific test reports for EN 71-3 and the colourant supplier’s declaration, because third-party certification bodies require full traceability of every polymer batch used in juvenile products. Molded ABS SNV parts that undergo repeated thermal cycling in dishwashers above 70°C can show surface whitening near weld lines if the melt temperature during moulding was below 220°C and the weld line did not fully re-entangle.
| Standard/regulation | Requirement | Test condition |
|---|---|---|
| EN 71-3:2019+A1:2021 | Migration of 19 elements | Simulant extraction per material category |
| REACH Annex XVII Entry 51 | Phthalates 0.1% w/w max | Solvent extraction / GC-MS |
| ASTM F963-23 | Mechanical and physical hazards | Drop/impact and small parts |
| ISO 8124-1:2022 | Sharp edges and points | Visual and probe inspection |
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Ningbo Dachuan Polymer ABS SNV is an acrylonitrile-butadiene-styrene copolymer supplied as cylindrical pellets for injection molding applications requiring a controlled balance of melt flow, impact strength, and heat resistance. The material consists of a continuous styrene-co-acrylonitrile matrix with a dispersed polybutadiene rubber phase. Molecular mass distribution of the SAN phase, polybutadiene graft density, and rubber particle size distribution collectively determine notched impact response and melt elasticity. In supplier technical literature, the SNV designation is associated with high-flow ABS for thin-wall electronic enclosures, appliance housings, and automotive interior trim. The following engineering envelope is derived from publicly available representative data for ABS SNV-type resins and should be checked against the lot-specific certificate of analysis; published data for this specific configuration is limited.
| Property | Test method | Condition | Value / range | Unit |
|---|---|---|---|---|
| Melt volume-flow rate | ISO 1133-1:2022 | 220 °C / 10 kg | 18–26 | cm³/10 min |
| Tensile yield stress | ISO 527-2:2012 | 50 mm/min | 42–48 | MPa |
| Flexural modulus | ISO 178:2019 | 2 mm/min | 2200–2500 | MPa |
| Charpy notched impact strength | ISO 179-1:2023 | 1eA, 23 °C | 20–28 | kJ/m² |
| Charpy notched impact strength | ISO 179-1:2023 | 1eA, −30 °C | 10–14 | kJ/m² |
| Vicat softening temperature | ISO 306:2022 | B50, 50 °C/h, 50 N | 96–101 | °C |
| Heat deflection temperature | ISO 75-2:2013 | 1.8 MPa, flatwise | 88–94 | °C |
| Density | ISO 1183-1:2019 | — | 1.04–1.06 | g/cm³ |
| Mold shrinkage | ISO 294-4:2018 | — | 0.4–0.7 | % |
| Flame rating | UL 94 | 3.0 mm | HB | — |
The values in the table are not simultaneous. A lot at the high end of the melt flow range may not simultaneously deliver the high end of the Charpy impact range. Because ABS SNV is a rubber-toughened system, impact strength can drop significantly when processing temperature exceeds the upper thermal limit.
At the processing stage, melt temperature measured at the nozzle should remain within 220 °C to 250 °C. Below 210 °C the SAN-rich continuous phase retains excessive melt viscosity, which raises injection pressure and produces short shots. Above 260 °C the polybutadiene rubber phase undergoes thermal-oxidative degradation, causing a loss of notched impact strength and an increase in yellowing. Mold temperature is ordinarily held between 40 °C and 80 °C. The lower bound is controlled by weld-line strength and surface replication; the upper bound is restricted by cycle economy and the risk of sink marks in thick bosses. Screw recovery should be conducted with a back pressure of 0.7 MPa to 1.2 MPa and a screw rotation speed of 30 rpm to 80 rpm for screw diameters from 35 mm to 60 mm. If shot size is below 30% of barrel capacity, melt residence time increases and the probability of thermally degraded material entering the cavity also increases. If shot size exceeds 75% of barrel capacity, melt homogeneity and plastication consistency decline.
In production-scale trials on reciprocating-screw machines with an L/D ratio of 20:1 to 24:1, the limiting step in thin-wall molding is frequently screw recovery rather than cooling time. For a two-cavity housing tool with a nominal wall thickness of 2.0 mm, using a screw diameter of 40 mm, a recovery speed above 90 rpm can increase melt temperature by 5 °C to 10 °C due to shear heating. That increase can move the melt above the thermal degradation threshold. Published data for this specific configuration is limited; therefore, recovery speed should be checked with a melt pyrometer before release to production.
Substitution of ABS SNV into a tool designed for electroplating-grade ABS requires verification of the etching process. Electroplating-grade ABS typically contains a larger polybutadiene domain structure that facilitates chromic acid etching and electroless nickel or copper deposition. ABS SNV is not optimized for that etching step; if the rubber-particle size distribution is too fine, the etched surface may lack the mechanical anchoring required for consistent metal adhesion. Adhesion should be evaluated following ISO 2409:2020 cross-cut testing after thermal cycling between −40 °C and 80 °C. For painted components, the molded surface must be free of internal mold release and must be dried to a residual moisture content below 0.05% before coating. If flame or plasma treatment is used to raise surface energy, the target range is 40 mN/m to 48 mN/m measured according to DIN EN 828:2013. These operations are process-specific controls rather than material-specific guarantees.
Because ABS SNV contains a polybutadiene rubber phase, storage at elevated temperatures above 40 °C for extended periods accelerates oxidative embrittlement. Bulk storage should be in sealed containers away from direct sunlight. The material must be dried at 80 °C for 2 h to 4 h using a desiccant dryer with a dew point of −30 °C or lower. Residual moisture above 0.05% causes splay, silver streaks, and local loss of impact strength. If ambient relative humidity exceeds 60%, drying time should be extended and the hopper should be blanketed with dry air. Avoid combining the material with amine-based additives or certain halogenated flame retardants because degradation products can form at processing temperatures.
Compared with high-rigidity ABS grades, ABS SNV generally exhibits a lower flexural modulus and a higher melt volume-flow rate. This combination is suitable where stiffness is secondary to fill pressure and cycle time. High-rigidity grades with flexural modulus above 2700 MPa often require nozzle temperatures near the upper end of the ABS range and may generate higher clamp tonnage. When ABS SNV is substituted for a low-flow high-impact ABS grade, the processor should reduce the melt cushion to 3 mm–6 mm, increase decompression distance to 2 mm–4 mm, and evaluate whether clamping force requirement remains above 0.4 kN/cm² projected area. The SNV grade should not be used where continuous heat resistance above 100 °C is required; for such applications, polycarbonate/ABS blends or heat-resistant styrenics are typically specified.
In a typical electronic enclosure application with a nominal wall thickness of 2.0 mm, ABS SNV may permit a fill time below 1.5 s at moderate injection pressures. The weld line formed at a connector opening is commonly the limiting mechanical feature. Notched Charpy impact strength at the weld line is generally 40% to 60% of the bulk material value, depending on melt temperature and mold temperature. If the product specification requires a minimum Charpy notched impact strength of 10 kJ/m² at 23 °C, mold trials should verify the weld-line result after conditioning at 23 °C and 50% relative humidity for at least 24 h in accordance with ISO 291:2008. If the part is exposed to fatty acids or common household cleaning agents, environmental stress-cracking resistance should be evaluated using ISO 22088-2:2006 at specified strain levels.
| Regulation / standard | Scope | Verification parameter |
|---|---|---|
| REACH SVHC declaration | EC 1907/2006 Article 33 | ≤0.1% w/w per candidate list item |
| RoHS Directive 2011/65/EU Annex II | Lead, mercury, cadmium, hexavalent chromium, PBB, PBDE | ≤1000 ppm in homogeneous material; cadmium ≤100 ppm |
| FDA 21 CFR 181.32 | Acrylonitrile copolymers in food contact | Lot-specific migration testing; supplier confirmation required |
| ISO 2580-2:2003 | Designation system for ABS | Property-based designation from supplier datasheet |
The compliance status of Ningbo Dachuan Polymer ABS SNV must be obtained from the supplier batch certificate. The statements above are not a declaration of conformity; they list the standard designations that should appear in the certificate. If food-contact, pharmaceutical, or toy applications are intended, additional migration testing under the relevant regional standard is required.