| HS Code | 562902 |
| Productname | Nanjing Lihan ABS S706 |
| Manufacturer | Nanjing Lihan Chemical Co., Ltd. |
| Materialtype | Acrylonitrile Butadiene Styrene (ABS) |
| Grade | S706 |
| Processingmethod | Injection Molding |
| Density | 1.05 g/cm3 |
| Meltflowrate | 20 g/10 min (220°C/10 kg) |
| Tensilestrength | 45 MPa |
| Flexuralmodulus | 2200 MPa |
| Heatdeflectiontemperature | 85°C (1.82 MPa) |
| Vicatsofteningtemperature | 95°C |
| Moldingshrinkage | 0.4-0.6% |
| Waterabsorption | 0.3% (24 h) |
| Flammabilityrating | HB (UL 94) |
As an accredited Nanjing Lihan ABS S706 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Nanjing Lihan ABS S706 is supplied in 25 kg moisture-proof paper-plastic compound bags, palletized for industrial transport and storage. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Nanjing Lihan ABS S706 chemical cargo packed and secured in a 20-foot full container load for shipment. |
| Shipping | Nanjing Lihan ABS S706 is generally shipped as a non-hazardous polymer resin in sealed bags or containers under general cargo conditions. Keep dry, ventilated, and away from moisture, heat, and ignition sources. It is not normally regulated as dangerous goods; follow local transport rules. |
| Storage | Store Nanjing Lihan ABS S706 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep containers tightly closed and labeled; prevent moisture and dust accumulation. Use grounding and bonding where appropriate to avoid static discharge. Follow local regulations and the supplier’s SDS for safe handling and emergency procedures. |
| Shelf Life | Store in a cool, dry, well-ventilated area away from moisture and sunlight; typical shelf life is 12 months unopened. |
Competitive Nanjing Lihan ABS S706 prices that fit your budget—flexible terms and customized quotes for every order.
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Nanjing Lihan ABS S706 is an acrylonitrile-butadiene-styrene terpolymer supplied as a medium-viscosity injection-molding grade. The material belongs to the general-purpose ABS class described by ISO 2580-1:2004, but the S706 designation is controlled through the lot certificate rather than through a single standardized property block. Because public datasheet values for this specific grade remain limited, incoming inspection should compare melt volume-flow rate, notched impact strength, tensile yield stress, Vicat softening temperature, and ash content against the supplier certificate of analysis. The three-phase morphology of the compound—SAN matrix, grafted polybutadiene rubber, and dispersed secondary rubber particles—governs the balance between processing flow and impact performance. On an FTIR scan, the nitrile absorption near 2244 cm⁻¹ and the butadiene trans-1,4 double-bond absorption near 967 cm⁻¹ confirm comonomer identity. A DSC scan typically shows the polybutadiene glass transition below −70 °C and the SAN glass transition near 105 °C. These characterization values are class-level observations and should not replace lot-specific certification.
Pre-drying is mandatory because ABS picks up moisture that produces splay and weld-line porosity. A desiccant-bed dryer with a dew point at or below −30 °C is specified. The resin is dried at 80 ± 5 °C for 2–4 h before processing. In production areas above 60% RH, dried material should not remain in an unheated open hopper for more than 30 min. Measured residual moisture below 0.05 wt% by Karl Fischer titration is the acceptance limit; loss-on-drying instruments used in production should be correlated with the supplier method before release.
Barrel temperature profiles from rear to nozzle are generally set from 200 °C to 230 °C, with the nozzle temperature not exceeding 240 °C. Melt temperature measured by an immersion probe should remain between 220 °C and 250 °C. Mold temperatures between 40 °C and 80 °C are applied; the lower region supports matte finishes and faster cycles, while the upper region improves knit-line strength and surface replication. General-purpose screws with L/D 20:1–24:1 and compression ratio 2.0:1–2.5:1 are acceptable. Back pressure is held at 0.5–1.5 MPa, and screw surface speed is maintained between 0.1 m/s and 0.3 m/s. Elevated back pressure raises plasticating work and can shift melt temperature toward the upper boundary, especially on older injection units with worn screws.
Capillary rheometry at 220 °C, 230 °C, and 240 °C across apparent shear rates from 100 s⁻¹ to 5000 s⁻¹ is used to fit a Cross-WLF viscosity model for mold-filling simulation. For a medium-viscosity ABS such as S706, zero-shear viscosity at 220 °C is class-typically 1000–3000 Pa·s, with the transition to shear thinning occurring between 50 s⁻¹ and 200 s⁻¹. Simulation predictions that deviate from short-shot observations by more than 5% in flow-front position indicate incorrect viscosity parameters or incorrect heat-transfer inputs.
Appliance housings and consumer electronic enclosures are a primary application window for S706. On a 120-ton hydraulic injection molding machine with a 40 mm screw, vacuum cleaner canister shells molded at 2.3 mm nominal wall thickness typically require pack pressure from 55 MPa to 75 MPa and cooling time of 18–24 s, depending on gate geometry. Weld lines in ribbed sections are controlled by vent placement at the knit-line terminus; vent gaps below 0.02 mm prevent trapped gas and internal marking. Snap-fit bosses should preserve at least a 1.5:1 wall-to-boss thickness ratio to avoid sink marks. For occupant-facing automotive trim, the molder should verify lot-specific VOC, fogging, and odor results against the applicable OEM standard, because third-party data for this grade are not published.
The following comparison positions S706 within the ABS injection-molding portfolio using class-typical commercial ranges. The S706 column is an expected control band for a medium-viscosity general-purpose ABS; current public documentation is insufficient to certify every cell independently. All properties should be confirmed against the supplier certificate before tooling changes are made.
| Property and test method | S706 expected position | General-purpose extrusion ABS | High-flow ABS | Flame-retardant ABS |
|---|---|---|---|---|
| Melt volume-flow rate, ISO 1133-1:2022, 220 °C/10 kg | 10–18 cm³/10 min | 4–8 cm³/10 min | 25–35 cm³/10 min | 15–25 cm³/10 min |
| Notched Izod impact, ISO 179-1:2010, 23 °C | 15–25 kJ/m² | 30–45 kJ/m² | 8–14 kJ/m² | 8–12 kJ/m² |
| Tensile yield stress, ISO 527-2:2012, 50 mm/min | 38–46 MPa | 35–42 MPa | 37–44 MPa | 35–42 MPa |
| Vicat B50, ISO 306:2022, 50 N | 92–98 °C | 95–101 °C | 88–94 °C | 85–93 °C |
| Density, ISO 1183-1:2019 | 1.03–1.06 g/cm³ | 1.02–1.05 g/cm³ | 1.03–1.06 g/cm³ | 1.15–1.22 g/cm³ |
Differences from other products arise mainly from the flow-impact compromise. S706 is not a flame-retardant material. If UL 94 V-0 at 1.6 mm is required, a flame-retardant ABS or ABS-PC blend should be selected. Published documentation for S706 does not establish a UL 94 rating, so applications with regulatory ignition-resistance requirements should not proceed without supplier certification. Substitution of S706 for a high-flow ABS will reduce spiral flow by roughly 30–45% in a 2 mm wall-thickness spiral mold at 230 °C melt and 50 °C mold, based on class-typical medium-viscosity grades. The corresponding gain is higher low-temperature ductility and fewer brittle gate fractures. Substitution for an extrusion ABS will increase melt flow by a factor of two to three but reduce notched impact; thin snap-fit arms should be reviewed by finite-element analysis using ISO 527-2:2012 tensile data and ISO 179-1:2010 impact data.
Mold filling in thin-wall sections below 1.5 mm is controlled by the shear-thinning response of the SAN phase and the rubber-particle contribution to elongational viscosity. For a medium-viscosity grade positioned near 10–18 cm³/10 min, spiral-flow length in a 2 mm channel is commonly 450–550 mm at 230 °C melt and 60 °C mold. Supplier-specific data for S706 should be acquired from a spiral-flow mold before production tool release. When replacing a 10 g/10 min general-purpose ABS, fill pressure may decrease by 15–25% in identical tooling, while injection speed can be increased by 10–20% to retain frozen-layer control. Gate freeze time, however, is shortened; holding-pressure time should be adjusted using gate-sealing studies rather than historical values.
Weld-line strength remains the main risk in substitution. Because lower melt viscosity reduces the elapsed time for interpenetration at the melt front, weld lines in S706 may show 10–20% lower notched impact than the 10 g/10 min reference when both are molded at the same mold temperature. Raising mold temperature to 70–80 °C and increasing hold pressure to 60–70% of peak injection pressure recovers some of the loss. Vacuum vents at the flow-front junction are required. Processors should verify weld-line properties using ISO 179-1:2010 Charpy or ISO 180:2019 Izod specimens cut from the weld-line position rather than relying on laboratory plaque values.
Laboratory plaques injection-molded according to ISO 294-1:2017 and conditioned at 23 ± 2 °C and 50 ± 10% RH for 16 h are used for property certification. Tensile specimens per ISO 527-2:2012 Type 1A are tested at 50 mm/min. Notched Izod values are tested at 23 °C and, where relevant, at −30 °C for low-temperature behavior. For unfilled ABS of this class, tensile modulus is generally between 2000 MPa and 2600 MPa; lot-specific secant or chord modulus values require supplier confirmation. Heat deflection temperature under 1.8 MPa load per ISO 75-2:2013 is typically below the Vicat value, and both should be reported with specimen conditioning details.
Regrind addition affects melt viscosity and color shift. A 20 wt% regrind fraction is common for non-appearance parts. For high-gloss white parts, regrind is either excluded or limited to 10 wt% because repeated heating oxidizes the butadiene phase and shifts yellowness. Pellet size distribution should be monitored; feed variability on gravimetric dosing units increases when regrind bulk density falls below 550 kg/m³. Color-stabilized lots should be purged with a transition material of similar melt viscosity before shutdown. Polystyrene is not recommended as a purge because of phase incompatibility with ABS.
On short cycle times below 15 s, screw recovery may exceed cooling time if the plasticating capacity of the machine is marginal. For medium-viscosity ABS, specific plasticating capacity is typically 0.1–0.2 kg/h per cm³/min of screw volume. A machine with a 40 mm screw and recovery capacity below 25 g/s will limit thin-wall output. Raising barrel temperature reduces melt viscosity and improves recovery, but only until the degradation boundary at 250 °C melt is approached. In this situation, back pressure can be increased moderately to 1.5 MPa and screw speed reduced to 80 rpm to limit shear heating. The adjustment may add 0.5–1.5 s to recovery time but prevents thermal damage.
Hot-runner manifolds impose additional residence-time exposure. For a medium-viscosity ABS, maximum residence time in a hot runner at 240 °C is generally 5–8 min before yellowing and free styrene increase. Manifold channels below 6 mm diameter create shear rates above 1000 s⁻¹, which lower viscosity but may increase melt-temperature heterogeneity. Melt-temperature spread across hot-runner tips should be maintained within ±3 °C; wider spreads produce variable gate freeze and dimensional variation in multi-cavity tools.
Matte-textured surfaces formed from unfilled S706 are sensitive to mold temperature and texture depth. Pencil hardness according to ASTM D3363-20 for unfilled ABS typically falls between 2B and HB; lot-specific values depend on surface gloss, texture, and pigment loading. Scratch resistance in automotive interior applications is often evaluated by PV3952 or equivalent OEM mar tests, not by a single ASTM method. For electronic enclosures, a Taber abrasion test under CS-10 wheels with 500 g load may be used as a pass/fail comparator, but the result is influenced by mold texture replication. High-gloss black surfaces show visible micro-scratching earlier than low-gloss textured surfaces; therefore, texture specification is a physical mitigation rather than a property of the base resin.
| Test or compliance item | Standard or reference method | Typical role |
|---|---|---|
| Melt volume-flow rate | ISO 1133-1:2022 | Lot release and process stability |
| Tensile yield stress | ISO 527-2:2012 | Design verification |
| Notched Izod impact | ISO 179-1:2010 | Toughness certification |
| Vicat softening temperature | ISO 306:2022 | Heat resistance ranking |
| Density | ISO 1183-1:2019 | Material identity check |
| Residual moisture | Karl Fischer titration | Drying verification |
| REACH SVHC | Regulation (EC) No 1907/2006 | Substance declaration |
| RoHS restricted substances | Directive 2011/65/EU Annex II | Electrical and electronic conformity |