| HS Code | 917209 |
| Manufacturer | Nippon A&L |
| Product Name | Nippon A&L ABS GH-100 |
| Material Type | ABS (acrylonitrile-butadiene-styrene) |
| Grade | GH-100 |
| Density | 1.04 g/cm³ |
| Melt Flow Rate | 15 g/10 min |
| Tensile Yield Strength | 44 MPa |
| Elongation At Break | 25% |
| Flexural Modulus | 2.30 GPa |
| Flexural Strength | 70 MPa |
| Notched Izod Impact Strength | 20 kJ/m² |
| Heat Deflection Temperature | 80 °C at 1.82 MPa |
| Rockwell Hardness | 105 R-scale |
| Molding Shrinkage | 0.4–0.6% |
| Ul 94 Flame Rating | HB at 1.5 mm |
As an accredited Nippon A&L ABS GH-100 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Nippon A&L ABS GH-100 is packaged in 25 kg moisture-resistant paper bags, stacked on pallets and shrink-wrapped for secure transport. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Nippon A&L ABS GH-100 resin, palletized, securely strapped, and moisture-protected for ocean freight. |
| Shipping | Shipping description: Nippon A&L ABS GH-100, non-hazardous ABS resin pellets, not regulated as dangerous goods for road, sea, or air transport. Supplied in sealed 25 kg bags or bulk containers. Keep dry, away from direct sunlight, heat, and ignition sources. Standard freight. |
| Storage | Store Nippon A&L ABS GH-100 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep original containers or bags tightly closed to prevent moisture and contamination. Avoid prolonged stacking or heavy loads. Separate from oxidizing agents and incompatible chemicals. Maintain good housekeeping and follow local regulations and the supplier’s safety data sheet. |
| Shelf Life | Typically 12 months from manufacture when stored in original, unopened packaging in a cool, dry, well-ventilated place away from sunlight. |
In portable audio charging-case base frames with nominal wall thickness of 1.2 mm, Nippon A&L ABS GH-100 is processed only after desiccant drying at 80 °C for 3–4 h. Target residual moisture is 0.05 % maximum by ISO 15512:2019. Higher moisture produces silver streaks at the flow front and reduces gloss on visible surfaces. The barrel temperature profile from feed to nozzle is 210/220/230/240/240 °C with melt temperature measured at the nozzle between 230 °C and 250 °C. Mold temperature for cosmetic surfaces is held at 50–60 °C. Injection speed is set at 80–140 mm/s. Packing pressure is 50–70 MPa for 0.4–0.6 s gate freeze on a 4 mm diameter cold sprue. For a four-drop hot runner with 1.0 mm valve-gate tips, sequential opening eliminates visible weld lines along the speaker grille rim. Color masterbatch with an ABS carrier is metered at 1.5–2.0 wt% through a gravimetric hopper loader. Liquid color is limited to 0.3–0.5 wt% and is accepted only when the carrier is mineral-oil-free and the dosing pump resolution is ≤0.01 g per cycle. Finished charging-case frames and speaker grille surrounds are evaluated under IEC 62368-1:2023 for audio/video equipment safety and RoHS Directive 2011/65/EU. The molder should confirm SVHC content below 0.1 wt% per REACH Regulation (EC) No 1907/2006 because pigment masterbatches can contribute residual substances. UL 94 classification is not assumed from the base resin data sheet; final part thickness, color loading, and processing temperature shift flammability results, and the classification must be re-confirmed on production-spec moldings.
Tooling for thin-wall filling includes a full-round cold runner of 6 mm diameter for natural and black lots. White lots use 7 mm diameter because titanium dioxide increases melt viscosity. Parting-line vents are 0.03 mm deep for the first 15 mm from cavity edge and are then relieved to 0.5 mm to atmosphere. Clamp force for a two-cavity tool with projected area 28,000 mm² at cavity pressure 40 MPa is 1120 kN; a 1300 kN hydraulic injection unit with a 36:1 L/D barrier screw is selected. Screw recovery time is kept at 4–6 s. Hopper throat bridging is avoided by using a 40° cone angle and a stick-slip coating on feed surfaces. The melt volume-flow rate certificate under ISO 1133-1:2022 Method A is recorded before production; lot-to-lot variation outside the supplier control range changes switchover position and short-shot pressure in 1.2 mm walls.
White and pastel rice cooker outer shells exhibit moisture-induced silver streaking that is not fully masked by raising mold temperature to 70 °C. When residual moisture exceeds 0.05 %, the flow front carries volatiles to the A-surface, and the defect remains visible as parallel streaks near the gate. Drying at 80 °C for 4 h in a desiccant dryer with dew point below -40 °C is therefore non-negotiable. White masterbatch based on titanium dioxide is metered at 3.0–5.0 wt%. This addition raises melt viscosity and reduces flow length; the rear barrel zone is reduced by 10 °C relative to unfilled natural material to prevent pigment-induced degradation. In-house regrind from rejected shells is blended at a maximum of 20 wt% after separate drying. Regrind above 20 wt% produces yellow shift and a drop in 60° specular gloss greater than 2 GU under ISO 2813:2014 on SPI A1 polished surfaces. The tool is a two-plate mold with 1.5° draft and stripper-plate ejection. Melt temperature at the nozzle is kept between 225 °C and 245 °C. Core temperature is 50 °C and cavity temperature is 55 °C to balance cooling and gloss. Finished outer shells are evaluated under IEC 60335-1:2020 for household appliance safety. Where the appliance standard requires glow-wire testing, the end product is tested under IEC 60695-2-11:2014 at a temperature defined by the product clause, typically 650 °C or 750 °C depending on the current and supervision category. ABS GH-100 is limited to external surfaces that are not in direct food contact and are not exposed to steam jets because continuous contact with wet heat above 75 °C can stress-crack the material.
A fan gate of 1.0 mm thickness across a 35 mm width is used at the top edge of the shell to minimize molecular orientation. Cavity-pressure transducers signal fill-to-pack switchover at 35 MPa or 3 mm before full fill. Holding pressure is 45 MPa for 2.0 s, then 20 MPa for 3.0 s. The profile reduces sink marks over internal ribs. If the skin freezes too early, internal voids form in sections thicker than 3.0 mm; ultrasonic inspection is used for those bosses. A 4-cavity tool with projected area 38,000 mm² requires a clamp force of approximately 1140 kN at average cavity pressure 30 MPa. Ejector pins are positioned behind ribs to prevent stress whitening on visible surfaces.
If the part is not subjected to high windscreen magnification and is located below the beltline, low-solar-load interior trim in seat side shields and glove-box outer doors is a permitted downstream use. Unlike exterior ABS grades, GH-100 is not specified for unpainted upper instrument panel skins. The material is pre-dried at 85 °C for 3–4 h. Carbon black masterbatch at 1.5 wt% is used for interior black parts; custom interior colors are adjusted through dry pigment or masterbatch but no more than 2.5 wt% total additive loading is recommended because impact strength falls as the additive phase increases. Injection molding uses in-mold grain textures equivalent to VDI 3400 SP-3 to reduce fingerprint visibility and hide minor flow scratches. Melt temperature is set between 230 °C and 250 °C. Mold temperature is 40–70 °C. Injection speed of 100 mm/s permits filling ribs as thin as 0.8 mm without short shots, but venting at the rib tip is required at 0.02 mm depth. The final product must meet FMVSS 302 / ISO 3795:1989 with burn rate below 100 mm/min. For German OEM specifications, VOC and SVOC are tested according to VDA 278:2011. Squeak and rattle against metal retainer clips is a known field complaint; a polyester felt tape or foam strip is inserted at the clip interface rather than increasing clip force, because high clip compression induces stress whitening in ABS.
The VDI 3400 SP-3 grain texture hides scratches on lower trim and seat side surfaces. If paint adhesion is specified for visible upper trim, the molded part is cleaned with iso-propyl alcohol after annealing, then an ABS-compatible adhesion promoter is applied. Baking is limited to 90 °C maximum to avoid warpage in large panels. Impact evaluation is performed at 23 °C using ISO 179-1/1eA Charpy notched specimens; low-temperature ductility below 0 °C is not claimed without a dedicated low-temperature ABS grade. Glove-box outer doors are designed with a minimum wall thickness of 2.0 mm for hinge load-bearing bosses; the hinge pin should not compress the boss side wall by more than 0.2 mm in assembly. Published data for GH-100 in painted upper dash substrates is limited; paint adhesion must be validated on production-textured parts.
Decorator wall plates and junction-box covers show a processing-sensitive failure mode at the screw boss. Without annealing, parts molded at high injection speed develop residual stress that concentrates at the boss root. Field assembly with screw torque above 0.4 N·m initiates radial cracking after temperature cycling from -20 °C to 60 °C. A post-mold annealing step at 70 °C for 2 h reduces the crack incidence in production trials. Annealed parts are then cooled on a flat fixture to prevent warpage below 0.3 mm across a 120 mm span. Drying is at 80 °C for 3 h to 0.05 % moisture. External mold release agents are prohibited because they interfere with pad printing and paint adhesion; ejection is achieved through draft of 1° and a 0.02 mm parting-line vent depth. If flame retardancy is required for a V-0 wall plate, GH-100 is not processed with halogenated additives in-house; a dedicated FR ABS grade is selected instead because additive compatibility, plate-out on the mold, and UL 94 color stability must be validated separately. Finished wall plates are evaluated under UL 514D for cover plates and IEC 60670-1:2015 for boxes and enclosures. Surface resistivity is not specified for standard decorative plates; static-dissipative requirements are outside this grade’s typical use.
A tab gate of 0.7 mm thickness is placed at the non-visible rear edge. Shear rate at the gate is kept below 50,000 s-1; above this value, the material discolors and gloss bands appear. Screw back pressure is 5–10 bar, screw speed 120 rpm, and melt cushion is 3–5 mm. For a 12-cavity wall-plate tool, cooling uses spiral channels of 8 mm diameter. Water temperature is 25 °C on the non-cosmetic side and 45 °C on the cosmetic side to control warpage. Zinc-plated screws are not used at installation because metallic marks on the boss seat are visible under oblique light. Torque is applied with a calibrated torsion screwdriver and recorded for lot audits.
A consolidated compliance matrix for the downstream segments discussed above is provided below. The table includes only finished-part standards; material-level mechanical property standards are not duplicated here.
| Downstream segment | Product safety and performance standard | Ignition or burn-rate assessment | Environmental or marking requirement |
|---|---|---|---|
| Portable audio charging-case base / speaker grille | IEC 62368-1:2023 | UL 94 classification on production-spec molding at final wall thickness | RoHS Directive 2011/65/EU; REACH Regulation (EC) No 1907/2006 |
| Rice cooker outer shell / household appliance panel | IEC 60335-1:2020 | IEC 60695-2-11:2014 glow wire, temperature per product clause | SVHC confirmation below 0.1 wt% |
| Seat side shield / glove-box outer door | FMVSS 302 / ISO 3795:1989 burn rate below 100 mm/min | VDA 278:2011 VOC/SVOC | ISO 11469:2016 material marking |
| Decorator wall plate / junction box cover | UL 514D; IEC 60670-1:2015 | Glow wire not applied unless product listing requires | REACH SVHC disclosure |
| Office automation side panel / paper tray / scanner chassis | IEC 62368-1:2023 | UL 94 HB final part | ECMA-74; ISO 11469:2016 |
When an office automation enclosure is classified as PS1 or PS2 under IEC 62368-1:2023 and the flammability requirement is limited to UL 94 HB, ABS GH-100 can be considered for side panels, paper trays, and scanner lower chassis. The material is pre-dried at 80 °C for 4 h. Melt temperature is 230–250 °C. A four-point sequential valve-gate system is used for panels with projected area above 80,000 mm². Melt cushion is maintained at 5–8 mm. Screw recovery time is kept below the cooling time to limit melt residence to 5 min; residence beyond 8 min generates black specks and gloss variation in natural or light grey parts. For static-dissipative internal paper-path covers, conductive carbon black masterbatch is added at 6–8 wt% to reach surface resistivity below 109 Ω under IEC 61340-2-3 at 12 % RH. This loading reduces notched impact and ductility, so the grade is not used for thin snap-fit arms requiring high elongation. Parts with mass above 100 g are marked with >ABS< per ISO 11469:2016. Environmental declarations follow ECMA-74. Direct contact with fuser heat or waste toner is excluded because heat deflection under 1.8 MPa is below 90 °C for typical ABS grades in this class.
Edge trims from sequential valve gates are reground and blended at 15 wt%. Regrind is dried separately and fed through a second gravimetric hopper. If a paper tray requires label adhesion, corona treatment is carried out at 2.0 kW for 1.0 s before pressure-sensitive adhesive application; surface energy after treatment is checked by dyne pens at 50 mN/m minimum. Paper tray flexural modulus increases when carbon black is present, and warpage is minimized by placing ejector pins at 6 mm intervals along the long axis. Customer acceptance testing for office automation parts usually includes drop test, vibration test, and label adhesion; these are product-specific and are not covered by base-resin datasheet values.
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Acrylonitrile-butadiene-styrene compound Nippon A&L ABS GH-100 is part of the manufacturer’s short-glass-fibre-reinforced Absolac product line, where the GH prefix denotes glass reinforcement for elevated flexural modulus and reduced mould shrinkage relative to unfilled ABS. The supplier’s current technical data sheet and lot certificate are controlling; however, the grade is generally associated with a nominal glass fibre content of 10 wt%, a melt volume-flow rate measured under 220°C/10 kg conditions in the range expected for medium-flow injection-moulding grades, and a recommended pre-drying schedule of 80°C to 85°C for 2 h to 4 h in a desiccant-bed hopper dryer. Applications include printer chassis, office automation frames, electrical enclosures and automotive interior brackets where unfilled ABS lacks dimensional stability under load and where PC/ABS or reinforced PBT is not required by thermal or impact specifications. Compared with unfilled medium-impact ABS, GH-100 provides higher tensile strength and flexural stiffness, lower notched impact strength, and lower coefficient of linear thermal expansion. Compared with a 20 wt% glass-filled ABS grade in the same series, GH-100 retains better flow length and lower compound density but sacrifices modulus and creep resistance.
Compounding of short-glass ABS is performed on a co-rotating twin-screw extruder with length-to-diameter ratio of 40 to 48; glass roving is fed downstream into the polymer melt to limit fibre fracture. Vacuum venting at approximately −0.08 MPa gauge pressure removes moisture and size volatiles, while die pressure is maintained below 8 MPa to avoid excessive shear heating. The median fibre length in moulded parts is typically 200 µm to 400 µm, with fewer than 10% of fibres longer than 600 µm after injection moulding. Progressive fibre attrition reduces tensile strength and notched impact but can improve surface appearance and reduce moulded-in stress. Regrind levels above 20 wt% can increase viscosity variability and should be evaluated against first-crop mechanical data.
Short glass fibre reinforcement of an amorphous styrene-acrylonitrile matrix changes the tensile failure mode from matrix yielding to fibre–matrix debonding and fibre pull-out. In conditioned specimens prepared and tested according to ISO 527-2, tensile stress at break for a 10 wt% glass-filled ABS is generally reported between 65 MPa and 80 MPa, while unfilled medium-impact ABS typically falls between 40 MPa and 50 MPa. Flexural modulus determined under ISO 178 is in the 3,500 MPa to 4,500 MPa range, approximately twice that of unfilled ABS. Notched Izod impact at 23°C under ISO 180/1A is commonly reduced to 8 kJ/m² to 12 kJ/m² from the 18 kJ/m² to 30 kJ/m² range typical of unfilled grades. The heat deflection temperature under a 1.8 MPa load, measured according to ISO 75-2, is typically 10°C to 15°C higher than unfilled ABS, although ABS remains amorphous and does not display a sharp crystalline melting point. Colourant packages and glass sizing chemistry can shift notched impact and melt flow by 5% to 10%, so supplier certificates should be obtained for the specific colour lot.
| Property | Test standard | Representative 10 wt% glass-filled ABS range | Unfilled medium-impact ABS reference |
|---|---|---|---|
| Density | ISO 1183-1 | 1.12 g/cm³–1.16 g/cm³ | 1.04 g/cm³–1.07 g/cm³ |
| Tensile stress at break | ISO 527-2 | 65 MPa–80 MPa | 40 MPa–50 MPa |
| Flexural modulus | ISO 178 | 3,500 MPa–4,500 MPa | 2,000 MPa–2,600 MPa |
| Notched Izod impact, 23°C | ISO 180/1A | 8 kJ/m²–12 kJ/m² | 18 kJ/m²–30 kJ/m² |
| Heat deflection temperature, 1.8 MPa | ISO 75-2 | 95°C–108°C | 88°C–95°C |
| Mould shrinkage, flow direction | ISO 294-4 | 0.1%–0.3% | 0.4%–0.6% |
| Coefficient of linear thermal expansion, parallel | ISO 11359-2 | 4 × 10⁻⁵ K⁻¹–6 × 10⁻⁵ K⁻¹ | 7 × 10⁻⁵ K⁻¹–9 × 10⁻⁵ K⁻¹ |
Before melt processing, moisture uptake in glass-filled ABS must be reduced to below 0.05 wt% because residual water at melt temperature hydrolyses the styrene-acrylonitrile phase, produces surface splay, and increases glass-fibre agglomeration at the screw root. In production-scale desiccant dryers operating with a dew point below −30°C, the resin bed is held at 80°C to 85°C for 2 h to 4 h; residence beyond 6 h can yellow natural grades and oxidise butadiene segments at the pellet surface. Transfer lines from the dryer to the machine throat should be sealed, and machine hoppers should not be left open at ambient relative humidity above 60%. Batch-to-batch variability in drying is frequently observed on central vacuum conveying systems when the receiver volume is oversized; pellets cool below 60°C and re-adsorb surface moisture during short interruptions. A desiccant-bed regeneration cycle of 4 h at 150°C to 180°C is normally sufficient for the dryer, but dew-point monitoring rather than time-based replacement is the reliable process control. Hydrolytic degradation of the SAN phase is accelerated above 260°C; melt residence time should therefore be kept below 10 min during emergency stops.
The processing window is bounded at the lower melt-temperature limit by viscosity increase and at the upper limit by thermal degradation of the styrene-acrylonitrile phase and glass-fibre sizing. For short-glass ABS grades in the GH-100 class, barrel settings are typically profiled from rear to nozzle as 210°C / 220°C / 230°C / 240°C, with nozzle temperature held at 240°C to 250°C. Melt temperature measured by air-shot pyrometer should remain between 230°C and 260°C. Mould surface temperature is held at 60°C to 80°C to develop weld-line strength and reduce exposed-glass surface roughness. Injection velocity is set to fill the cavity in 0.5 s to 1.5 s for wall sections of 1.5 mm to 2.5 mm; hold pressure is commonly maintained at 50% to 70% of peak injection pressure for 6 s to 10 s. Back pressure during screw recovery is limited to 0.5 MPa to 1.0 MPa because excessive back pressure increases fibre attrition. Screw surface speed should not exceed 0.3 m/s on a 40 mm diameter reciprocating screw; higher speeds reduce fibre length and lower final flexural modulus. Clamp-force requirements are similar to unfilled ABS at equal wall thickness, but the higher cavity pressure can raise clamp demand by 10% to 20%; multi-cavity tools for GH-100 are frequently run on 80- to 150-tonne injection moulding machines with shot sizes occupying 60% of barrel capacity.
Spiral flow testing of glass-filled ABS grades shows that a 10 wt% glass loading reduces flow length by 15% to 30% compared with unfilled ABS at the same melt temperature and injection pressure. The flow-length reduction is not linear with wall thickness; sections below 1.2 mm show disproportionately greater reduction because glass fibres orient in the thickness direction and increase apparent viscosity. Gate freeze time is slightly shorter due to higher thermal conductivity of the glass-filled compound. Hold-pressure time must therefore be set by gate-seal study rather than transferred from unfilled ABS. Pressure-specific volume behaviour changes with fibre content, so cavity pressure sensors provide more reliable switch-over than timer-based control. On hot-runner systems, the internal runner diameter should be at least 5 mm to avoid fibre plugging at tips; valve-gate tips with 2.5 mm orifice are preferred over thermal gate tips.
Mould shrinkage anisotropy, rather than absolute shrinkage, is the primary dimensional risk in moving from unfilled ABS to GH-100. Flow-direction shrinkage is reported as 0.1% to 0.3%, while transverse shrinkage can reach 0.3% to 0.5% because fibre orientation restricts longitudinal contraction but not matrix-dominated transverse relaxation. This anisotropy causes edge lifting and hole-position drift in flat parts when gates are located at one end. To reduce differential shrinkage, the filling pattern should be balanced so that the flow front advances at approximately 1:1 in the two principal cavity axes, and gate location should be moved away from thin unsupported regions. Tool steel for glass-filled grades requires nitriding or hardened inserts of 52 HRC to 56 HRC; ejector pins and shut-off faces wear rapidly under glass-fibre abrasion when tool hardness is below 45 HRC. Venting depth must be kept below 0.02 mm to 0.03 mm to prevent flash while allowing volatiles to escape. For components subjected to sustained load, published data for this specific configuration is limited, and creep modulus should be obtained from the supplier for the intended stress and temperature.
In service, the lower coefficient of linear thermal expansion of glass-filled ABS reduces misalignment in electronic chassis assembled with metal heat sinks. The coefficient of linear thermal expansion for a 10 wt% glass-filled ABS is typically between 4 × 10⁻⁵ K⁻¹ and 6 × 10⁻⁵ K⁻¹, compared with 7 × 10⁻⁵ K⁻¹ to 9 × 10⁻⁵ K⁻¹ for unfilled ABS. Creep modulus under a sustained tensile stress of 20 MPa at 23°C is higher than unfilled ABS, but published data for this specific configuration is limited when service exceeds 60°C; creep rupture properties should be obtained from the manufacturer. Exposure to ketones, aromatic hydrocarbons and strong acids causes environmental stress cracking in ABS, and glass reinforcement does not remove this limitation. Outdoor weathering of natural grades causes yellowing and surface embrittlement unless UV-stabilised or painted variants are specified.
Substitution of unfilled ABS with GH-100 is not a direct drop-in because the glass-filled material shows reduced flow length at equal wall thickness and increased demand on gate and runner dimensions. A bracket originally designed with 2.5 mm wall thickness may require a gate diameter increase from 1.0 mm to 1.5 mm and a cold runner diameter from 4 mm to 5 mm to avoid short shots. The hold-pressure window narrows: insufficient hold produces sink marks at bosses and rib intersections, while excessive hold increases flash at the parting line and changes fibre orientation near the gate. Weld lines are the most significant mechanical limitation; glass fibres at the weld interface reduce weld-line strength by 20% to 40% compared with the bulk property, so weld lines should be relocated to low-stress areas through multiple gates or sequential valve-gate timing. Compared with PC/ABS, GH-100 offers lower heat resistance and lower notched impact, but it provides lower density, simpler drying, and generally better flow in thin sections. The selection is therefore driven by stiffness-to-cost and dimensional stability rather than by maximum toughness or maximum heat resistance.
Regulatory and supply-chain documentation for electrical enclosure grades is governed by the end-use specification rather than by the polymer grade alone. Flame-retardant classification is evaluated under UL 94 at the thickness and colour actually used, and the exact rating for GH-100 must be obtained from the supplier’s UL Yellow Card. RoHS compliance is assessed against Directive 2011/65/EU and its delegated amendments, including restriction of lead, mercury, cadmium, hexavalent chromium, and specific brominated flame retardants. REACH compliance is declared through the supplier’s safety data sheet and substance-of-very-high-concern notification. ISO 9001 or IATF 16949 batch certificates should be retained for moulded parts supplied into automotive programmes, and the glass-fibre sizing may be subject to specific food-contact or medical restrictions if the application requires USP Class VI or food-contact listings. The processor should verify that regrind limits, lot traceability, and colourant approvals are stated in the purchase specification.