| HS Code | 785382 |
| Density | 1.04 g/cm³ |
| Melt Flow Rate | 20 g/10 min at 220°C/10 kg |
| Tensile Strength At Yield | 430 kg/cm² |
| Elongation At Break | 25% |
| Flexural Strength | 700 kg/cm² |
| Flexural Modulus | 23000 kg/cm² |
| Izod Notched Impact Strength | 20 kg·cm/cm |
| Rockwell Hardness | R100 |
| Heat Deflection Temperature | 85°C at 1.82 MPa |
| Vicat Softening Temperature | 98°C |
| Flammability | UL94 HB |
| Processing Method | Injection Molding |
As an accredited Bhansali Engineering Polymers (BEPL) ABS ABS 100 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | BEPL ABS 100 is supplied in 25 kg bags, typically palletized and lined for safe industrial storage and handling. |
| Container Loading (20′ FCL) | Bhansali Engineering Polymers (BEPL) ABS 100 is loaded in a 20-foot FCL dry container, palletized and secured for ocean shipment. |
| Shipping | Bhansali Engineering Polymers (BEPL) ABS 100 is shipped as a non-hazardous thermoplastic resin, typically in 25 kg moisture-barrier bags or jumbo bags, palletized and stretch-wrapped. Keep dry and away from direct sunlight, heat, and contamination; handle as general industrial cargo under normal hygiene practices. |
| Storage | Store Bhansali Engineering Polymers (BEPL) ABS 100 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, flames, and oxidizing agents. Keep original bags/containers closed, palletized, and protected from moisture, dust, and contamination. Avoid excessive stacking or mechanical damage; use oldest stock first and follow the supplier’s SDS and local regulations. |
| Shelf Life | Shelf life is typically 12 months in original unopened packaging under dry, cool, ventilated storage, away from sunlight and moisture. |
ABS 100 is introduced as the base resin in unpainted automotive interior trim compounds for 2.0–2.5 mm nominal wall sections; batch-to-batch process records from molding shops show moisture splay and blemish formation become statistically significant when granulate moisture exceeds 0.08% at the feed throat. The material is ratioed at 100 phr virgin ABS 100, 15–25 phr clean-runner regrind, and 1–2 phr carbon black or color concentrate, with no additional external lubricant in textured-tool applications. Compliance for the terminal part follows FMVSS 302 and ISO 3795 burning-rate requirements, with a pass criterion not exceeding 100 mm/min; IMDS records are updated against ISO 11469 marking, and REACH Article 33 notifications under (EC) No 1907/2006 are triggered only when lot-specific SVHC concentrations exceed 0.1 wt%. Downstream, the material is dried in a desiccant-bed dryer at 80 °C for 3–4 h, injection molded on a 20:1 L/D general-purpose screw with a 2.2:1 compression ratio, melt temperature 220–240 °C, mold temperature 40–60 °C, and hydraulic hold pressure 50–70 MPa. Process limits emerge when residence time exceeds 15 min at 240 °C, producing yellowing at the sprue gate; mold temperatures below 30 °C reduce flow-line healing and raise weld-line visibility. Terminal finished components include air-vent surrounds, center console side panels, door handle escutcheons, and seat side shields.
The principal processing conflict in this sector is the interaction between low-gloss surface requirements and regrind addition. In-plant trials using a 1,200 kN clamp force machine and a 0.8 mm grain depth cavity showed that regrind fractions above 25 phr lowered melt viscosity sufficiently to alter textured surface replication, while higher melt temperatures required to restore flow produced liquid colorant migration to the part surface. Published independent data for ABS 100 in deep-grain interior trim with hot runner sequential valve gating is limited; therefore processors must validate surface appearance against a reference master plaque under D65 illumination rather than relying solely on melt flow ratio measurements.
ABS 100 is compounded into appliance housing material with 100 phr resin, 2–4 phr white or metallic masterbatch, 0.2–0.5 phr internal mold release, and regrind limited to 20 phr because higher regrind fractions reduce notched Izod impact below the 10 kJ/m² threshold sometimes required by design verification. The governing standard is IEC 60335-1:2020, Clause 30.2, with glow-wire testing conducted at 550 °C for unattended appliance enclosures; a UL 94 HB rating at minimum thickness is used for North American export, and RoHS 2011/65/EU Annex II limits for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE must be satisfied by the pigment masterbatch and carrier resin. Drying uses a hopper dryer at 80 °C for 2–4 h to maintain moisture below 0.1%; injection molding is performed with melt temperature 230–250 °C, mold temperature 50–70 °C, injection speed 80–120 mm/s, and holding pressure 60–80 MPa. The main processing bottleneck is the formation of silver streaks when wet regrind enters the feed throat above 0.15% moisture; another incompatibility is observed when ABS 100 is dry-blended with polycarbonate regrind at more than 5 phr, causing delamination at the part surface. Terminal product types include mixer grinder bases, vacuum cleaner motor housings, and hand iron shells.
Production-scale data from a 450 kN clamp force molding line indicates that sink marks above internal bosses become unacceptable when pack pressure decays below 25 MPa within 2 s of gate freeze. The same line recorded batch-to-batch gloss variation of 1.5–2.0 GU when the colorant concentrate carrier resin was changed without re-qualification. For export markets requiring halogen-free documentation, the flame rating must be re-verified on the final pigmented compound because UL 94 HB classification is assigned to a defined thickness and color, not to the natural pellet alone.
In thin-wall networking device enclosures, ABS 100 is selected for dimensional consistency in 1.0–1.8 mm walls, and processor records show that holding pressure below 55 MPa produces sink marks over internal snap-fit bosses, while pressure above 85 MPa causes flash along the parting line because of the material’s medium viscosity. The blend is composed of 100 phr virgin ABS 100, 5–10 phr cold-runner regrind, and 1–3 phr black masterbatch; for lighter RAL colors the regrind fraction is reduced to 0–5 phr to avoid gloss variation. Fire enclosure compliance is assessed under IEC 62368-1:2023, with the material being a UL 94 HB grade at 1.5 mm; when end markets require V-0, this feedstock is not suitable without an FR additive package that must be re-qualified because ABS 100 is not supplied as a flame-retardant compound. Drying is performed at 80 °C for 3–4 h, and processing on 20:1 L/D screws uses melt temperature 230–250 °C, mold temperature 50–70 °C, fast injection velocity 200–300 mm/s, and back pressure 0.5–1.0 MPa. The critical limitation is gate blush in hot-tip valve-gated molds when the tip temperature exceeds the melt set point by more than 15 °C; published data for ABS 100 in valve-gated thin-wall tools with 0.8 mm wall stock is limited, requiring a process capability study. Terminal article types include router bottom covers, access point brackets, and set-top box front bezels.
In this application, the processing window is narrower than in thicker-wall automotive interiors because the ratio of gate diameter to part wall thickness strongly influences jetting. Molding trials with 1.2 mm nominal wall sections and a 0.6 mm valve-gate tip showed that injection speeds below 180 mm/s produced jetting streaks at the gate land, while speeds above 320 mm/s increased shear heating and caused material discoloration in the hot runner manifold. Moisture control is also more stringent because any moisture above 0.05% at the feed throat increases hydrolysis-induced surface haze in black parts, which is detectable under 60° gloss measurement but not always visible under diffused factory lighting.
ABS 100 is used as a base resin for injection molded drainage fittings where 3–8 mm wall sections must retain impact toughness after mold cooling. The formulation is 100 phr ABS 100 with 0.5–1.5 phr black masterbatch and 0.2–0.5 phr processing stabilizer; clean regrind from sprue and runner systems is accepted up to 25 phr, but lot-to-lot melt flow variation in regrind above 30 phr has been associated with short shots in multi-gated tees. Compliance is anchored to ASTM D2661 for Schedule 40 ABS DWV fittings in North America and ISO 3633:2002 for soil and waste discharge systems in international markets; for EU shipments, EN 1455-1 requirements for joint design and short-term hydrostatic pressure testing apply. Drying is performed at 80 °C for 2–3 h; injection molding uses a low-compression 2:1 screw, melt temperature 210–230 °C, mold temperature 40–60 °C, and hold pressure 70–90 MPa to prevent sink over thick hub sections. A hot-runner manifold is used only when the channel volume is less than 1.5 times the shot weight and residence time is below 12 min; exceeding these limits degrades resin at the manifold wall and lowers the acetone immersion resistance of the molded fitting. Terminal finished components are drain waste and vent couplings, p-traps, reducing tees, and wall bends.
The operational boundary in DWV fitting molding is determined by the need to retain solvent-cement compatibility after long barrel residence periods. If the melt temperature is kept above 230 °C for longer than 20 min, the parts may pass dimensional checks but fail subsequent acetone immersion because the surface becomes more susceptible to stress whitening. Published independent data for ABS 100 in ISO 3633:2002 fitting configurations is limited; molders should qualify each cavity geometry with a 20-cycle purge procedure and verify that the purged material does not show more than 0.5 g/min mass loss under the fitting manufacturer’s thermal stability protocol.
ABS 100 is formulated for precision toy molding at 100 phr base resin with 1–2 phr organic pigment masterbatch and regrind not exceeding 5 phr because higher regrind percentages reduce color repeatability and complicate traceability under toy safety documentation. The relevant compliance framework includes EN 71-3:2019+A1:2021 for migration of certain elements, ASTM F963-17 for soluble heavy metal extraction, and CPSIA Section 101 for lead content in accessible substrates at a limit of 100 ppm. In this sector the main processing challenge is not high-temperature stability but dimensional precision: molding is performed on a 20:1 L/D screw with melt temperature 220–240 °C, mold temperature 50–70 °C, injection velocity 150–250 mm/s, and holding pressure 65–85 MPa, with cushion maintained below 1.0 mm to avoid uneven packing of multi-cavity brick molds. Terminal product types include construction bricks, toy vehicle bodies, and hobby structural frames.
An additional constraint is the selection of non-heavy-metal pigment systems. Cadmium- and lead-based masterbatches that might pass process trials are incompatible because they introduce migration risk beyond the toy standard matrix; the same applies to recycled-feedstock contamination. Finished parts are subjected to an extraction test under EN 71-3 using 0.07 mol/L hydrochloric acid, and release is permitted only when the analytical detection limit for lead is below 0.01 mg/kg in the final pigmented part, not merely in the natural resin certificate. Cavity-to-cavity weight variation above 0.15% on a 16-cavity construction brick mold has been associated with measurable differences in clutch force retention, making shot volume control more important than melt flow index alone.
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Bhansali Engineering Polymers (BEPL) supplies ABS 100 as an unfilled acrylonitrile-butadiene-styrene injection-moulding grade for general-purpose technical components. The product designation ABS 100 identifies the standard general-purpose resin within the BEPL ABS range; it is not a flame-retardant grade, an electroplating grade, or a long-term outdoor weathering grade. The resin comprises a rigid styrene-acrylonitrile matrix with a dispersed polybutadiene rubber phase. The rubber phase is grafted to the matrix at the particle interface, which provides the characteristic balance between room-temperature impact resistance and stiffness. The material is supplied in pellet form, and the lot-specific certificate of analysis is the controlling specification for melt volume-flow rate, tensile yield stress, notched Izod impact resistance, and heat deflection temperature. The current public datasheet should be retrieved from the supplier before tool design because revisions may alter lot-average values and colour-specific data.
Incoming resin from BEPL should be dried and then verified against ISO 1133-1:2022 for melt volume-flow rate, ISO 527-2:2012 for tensile yield stress, ISO 180:2019 method A for notched Izod impact, and ISO 306:2013 method A50 for Vicat softening temperature. The density of unfilled general-purpose ABS of this class is measured at 23 °C under ISO 1183-1:2019. Moisture content in undried pellets exposed to high-humidity conditions can exceed 0.10% by mass and should be checked by ISO 15512:2019 when splay or surface veining appears on moulded parts.
ABS 100 is positioned as the general-purpose injection-moulding grade. Compared with BEPL high-heat ABS grades, ABS 100 exhibits a lower deflection temperature under load and a lower Vicat softening temperature. Under sustained mechanical load, a maximum continuous-use temperature in the region of 65 °C to 80 °C may be appropriate for unstressed or lightly stressed parts, but part validation under ISO 75-2:2013 method A is required for load-bearing applications. Compared with BEPL high-flow ABS grades, ABS 100 has a more viscous melt; this can raise injection pressure demand and may require larger runners, gates, or vents, but it often helps retain impact toughness in thick-walled sections where melt flow length is less critical. Compared with BEPL flame-retardant ABS grades, ABS 100 is normally considered UL 94 class HB at minimum material thickness, not V-0, unless final-part testing demonstrates otherwise. Compared with BEPL electroplating grades, ABS 100 is not specifically formulated for etch-sensitive plate adhesion; plating trials are necessary before specifying the grade as a plated substrate.
Against non-ABS thermoplastics, the distinction is mainly one of property balance. Relative to high-impact polystyrene, ABS 100 provides better notched impact at 23 °C and improved environmental stress-cracking resistance under ASTM D256-10 or ISO 180:2019 method A. Relative to polypropylene, ABS 100 offers higher tensile modulus, greater surface hardness, and lower mould shrinkage but lower resistance to concentrated acids, chlorinated solvents, and some hydrocarbon environments. Relative to polycarbonate and PC/ABS blends, ABS 100 has lower multi-axial impact at sub-zero temperatures and lower 1.80 MPa heat deflection temperature, but it can be processed at lower melt temperatures and generally has lower melt viscosity at the same shear rate.
Published third-party data for this specific BEPL formulation is limited. The following table is therefore a class reference for unfilled general-purpose ABS injection-moulding resins, not a substitute for the BEPL ABS 100 datasheet or the lot-specific certificate of analysis. When the supplier COA conflicts with these ranges, the COA controls.
| Property | Test condition | Test method | Class reference envelope | Unit |
|---|---|---|---|---|
| Density | 23 °C | ISO 1183-1:2019 | 1.03–1.06 | g/cm³ |
| Melt volume-flow rate | 220 °C / 10 kg | ISO 1133-1:2022 | 5–25 | cm³/10 min |
| Tensile yield stress | 50 mm/min | ISO 527-2:2012 | 35–50 | MPa |
| Tensile modulus | 1 mm/min | ISO 527-2:2012 | 1800–2500 | MPa |
| Notched Izod impact | 23 °C, notch A | ISO 180:2019 | 18–35 | kJ/m² |
| Flexural modulus | 2 mm/min | ISO 178:2019 | 1700–2400 | MPa |
| Vicat softening temperature | 50 °C/h, 50 N | ISO 306:2013 method A50 | 95–105 | °C |
| Heat deflection temperature | 1.80 MPa, 120 °C/h | ISO 75-2:2013 method A | 85–98 | °C |
| Flammability class | 1.6 mm thickness | UL 94 | HB | class |
Rheological behaviour of unfilled general-purpose ABS of this class is strongly shear-thinning. Apparent shear rates in injection moulding range from roughly 100 s⁻¹ at the flow front to above 10 000 s⁻¹ in thin gates. Mould-filling simulation should use viscosity model parameters generated from lot-specific capillary rheometry or MVR data rather than assuming Newtonian flow. Residual moisture shifts the apparent MVR, so pellets must be dried before rheological testing.
Long-term creep testing should be performed under ISO 899-2:2003 or ASTM D2990-17 when sustained tensile or flexural stresses exceed 10 MPa at service temperatures above 40 °C. Creep in screw bosses and snap-fits can relax clamp force and is a known failure mode in ABS enclosures if the boss is too thin or if the screw is over-torqued. Chemical stress-cracking resistance should be evaluated under ASTM D543-20 or ISO 22088-3:2006 for any application involving oils, greases, cleaning agents, or plasticizers that may migrate from wiring insulation or gaskets.
Pre-drying of ABS 100 is mandatory, not optional. The material should be dried in a desiccant dryer at 80 °C to 90 °C for 3 h to 4 h, with a drying air dew point of −30 °C or lower. The maximum residual moisture before moulding should be 0.10% by mass. At moisture levels above 0.20%, production-scale moulding of ABS commonly shows splay at the gate, surface veining, jetting, and local loss of gloss as steam is generated at the melt front. When ambient relative humidity is above 60%, dried resin should be consumed within 4 h unless the hopper is purged with dry air, and open handling of pellets should be minimized.
Melt temperature measured at the nozzle should be maintained from 230 °C to 250 °C. Sustained melt temperatures above 260 °C, particularly with residence times longer than 5 min, can produce yellowing, black specks, and thermal degradation of the butadiene rubber phase. Mould temperature should be held at 40 °C to 70 °C; at the lower end, flow lines and weld lines become more visible and weld-line impact falls. At the upper end, gloss and knit-line strength improve but cycle time increases and mould release may degrade in deep-draw or textured tools. For high-gloss appliance surfaces, the tool surface temperature should be controlled by pressurised water or oil units rather than relying on melt heat alone.
Injection speed should be profiled so that 60% to 80% of cavity volume is filled before switch-over, with packing pressure held at 50% to 70% of peak injection pressure. Back pressure from 0.5 MPa to 1.5 MPa assists homogenisation of colour masterbatch and prevents free pellet slip along the screw but should not be raised to the point at which screw recovery time becomes excessive. A cushion of 3 mm to 6 mm should be maintained for shot-to-shot consistency. The following processing window is a class guideline; the BEPL lot-specific datasheet and mould-flow study may require narrower limits for a given tool.
| Parameter | Recommended setting | Unit |
|---|---|---|
| Desiccant dryer temperature | 80–90 | °C |
| Drying time | 3–4 | h |
| Maximum residual moisture | ≤0.10 | % by mass |
| Melt temperature at nozzle | 230–250 | °C |
| Mould temperature | 40–70 | °C |
| Back pressure | 0.5–1.5 | MPa |
| Cushion | 3–6 | mm |
| Switch-over position | 60–80 | % of shot volume |
On production-scale injection-moulding machines, screws with length-to-diameter ratios of 20:1 to 24:1 and compression ratios of 2:1 to 2.5:1 are representative for ABS. The screw should be free of dead spots; degraded ABS from previous runs can accumulate behind check rings and later release as brown or black contamination. Hot-runner manifolds and drops should be set to 230 °C to 250 °C, and flow channels should be streamlined to avoid stagnant zones. Melt pressure loss across the hot runner should be recorded during tool trials because transfer fill imbalance can appear when cavity count exceeds 8. Gate dimensions should be selected for volume fill and shear rate: for unfilled ABS of this class in thin-wall sections, a gate diameter of 0.8 mm to 1.5 mm may be a starting point, but the final gate size must be confirmed by short-shot and pressure-drop studies.
Regrind use should be limited to 20% by mass unless a full property-retention study is performed. Dried regrind should be blended with virgin resin, free of fines, and protected from moisture. Purging between colours or resin families should follow the purging compound supplier’s procedure; ABS 100 should not be processed in barrels containing PVC, acetal, or polycarbonate residues without intensive purging because thermal degradation products can contaminate the styrene-acrylonitrile matrix and lower weld-line strength.
Electrical enclosures and switchgear covers manufactured from ABS 100 are normally specified where the end-use standard permits UL 94 class HB at the minimum part thickness. Glow-wire testing under IEC 60695-2-12 is part-specific and cannot be guaranteed by the material grade alone; ribs, bosses, metallic inserts, and wall thickness transitions alter local ignition behaviour. Mould inserts for screw bosses should avoid sharp internal corners because production failures in ABS enclosures commonly occur at weld lines around openings and at the junction between thick bosses and thin walls.
Appliance housings, control panels, and consumer-durable covers use ABS 100 for the balance of stiffness, dimensional stability, and surface finish. Mould temperature should be held at the upper end of the processing envelope to reproduce fine-grained texture and reduce sink marks. Solvent wiping and adhesive bonding require compatibility testing: methyl ethyl ketone, acetone, and ester-based cleaning agents can promote environmental stress cracking in stressed ABS parts under ASTM D543-20 or ISO 22088-3:2006.
Automotive interior trim parts such as pillar covers, glove box liners, and console components may be moulded from ABS 100 when service temperatures do not exceed the validated continuous-use limit and when colourfastness is accepted by the OEM. Long-term UV exposure without paint, capstock, or ultraviolet stabilization is not recommended. Thermoforming is not the primary conversion route for this grade; it is configured for injection moulding and should not be substituted into sheet extrusion without BEPL approval.
Chemical and thermal operational boundaries must be defined before substituting ABS 100 into an existing tool. The grade should not be specified for continuous immersion in concentrated acids, chlorinated solvents, aromatics, esters, or ketones. Stress-cracking resistance under ASTM D543-20 or ISO 22088-3:2006 should be evaluated for any gasket, lubricant, or adhesive that contacts the part under stress. Continuous service above 85 °C under mechanical load is not recommended without part-level testing; short-duration excursions are less severe than sustained load, but the part geometry and ribbing determine the actual limit. BEPL ABS 100 should be dried after any storage period exceeding the supplier’s shelf-life guidance, and lot-specific certificates of analysis should be retained as part of the quality record because melt viscosity, colour, and notched impact may shift across production lots.