| HS Code | 420168 |
| Product Name | Kumho Petrochemical ABS 770S |
| Manufacturer | Kumho Petrochemical |
| Material Type | Acrylonitrile Butadiene Styrene (ABS) |
| Grade | 770S |
| Processing Method | Injection Molding |
| Density | 1.04 g/cm3 |
| Melt Flow Rate | 2.5 g/10 min (220°C/10 kg) |
| Tensile Strength | 44 MPa |
| Flexural Modulus | 2200 MPa |
| Flexural Strength | 68 MPa |
| Izod Notched Impact Strength | 25 kJ/m2 |
| Rockwell Hardness | 105 R |
| Heat Deflection Temperature | 85 °C (1.82 MPa) |
| Vicat Softening Temperature | 98 °C |
| Mold Shrinkage | 0.4-0.7 % |
| Elongation At Break | 20 % |
As an accredited Kumho Petrochemical ABS 770S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Kumho Petrochemical ABS 770S is supplied in 25 kg moisture-resistant paper sacks, palletized for industrial handling and storage. |
| Container Loading (20′ FCL) | Kumho Petrochemical ABS 770S is loaded in a 20′ FCL container, securely packed in bags/pallets for safe chemical shipment. |
| Shipping | Kumho Petrochemical ABS 770S is typically shipped as thermoplastic resin pellets in 25 kg bags or 500–1,000 kg jumbo bags, palletized and shrink-wrapped. Transport in dry, ventilated containers protected from moisture, heat, and direct sunlight. It is non-hazardous under normal shipping conditions; follow applicable transport regulations. |
| Storage | Store Kumho Petrochemical ABS 770S in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and moisture. Keep in original sealed, labeled packaging on pallets; avoid crushing or stacking damage. Prevent dust and static buildup. Separate from oxidizing agents and incompatible solvents. Observe local regulations and the manufacturer’s SDS for safe storage and handling. |
| Shelf Life | Typically 12 months when stored in original unopened packaging under cool, dry conditions, away from direct sunlight and moisture. |
In automotive interior lower-stiffness trim applications, ABS 770S is processed as a neat injection-molding feedstock where the incoming resin lot is released against the manufacturer’s melt volume-flow rate specification under ISO 1133-1:2022 using 220°C and 10.0 kg. The formulation addition ratio for glove box bins and center console side panels is 100 phr virgin ABS 770S; reprocessed ABS 770S from sprues, runners, and rejected first-article parts is limited to 20 wt% of total shot mass, and the color package is added at 2 wt% using a carrier that does not shift linear mold shrinkage by more than 0.1%. Compliance requirements in this segment include horizontal burn-rate testing under ISO 3795:1989 or FMVSS 302, substance restrictions under EU 2011/65/EU as amended by (EU) 2015/863, and screening against REACH 1907/2006 Annex XVII and the SVHC Candidate List. On production lines, the material is processed in reciprocating-screw injection molding machines with screw diameter 45–70 mm, screw L/D 20:1–25:1, non-return valve, and clamp force from 5,000 kN to 12,000 kN. The barrel temperature profile is 220–240°C from feed zone to nozzle, the mold is held at 40–60°C, and the switch-over from injection velocity control to packing pressure occurs at 95–98% volumetric fill for 2.0–2.5 mm wall stock. Packing pressure is set at 50–70% of peak injection pressure, with hold time 8–15 s for 2.5 mm walls. Tools are normally valve-gated hot-runner systems with hardened P20 cavity inserts; gate orifice diameters below 1.5 mm are avoided because the high-flow front can shear-thin the melt sufficiently to produce jetting when injection velocity exceeds the gate-specific threshold established by mold-filling simulation. Terminal finished products include glove box bins, center console side panels, knee bolster covers, and lower B-pillar trim inserts. Operational boundaries are the melt-temperature ceiling of 260°C and total barrel residence time above 6 min, beyond which surface yellowing and notched impact loss become measurable under ISO 180; when ambient relative humidity exceeds 60%, drying at 80–85°C to below 0.05 wt% moisture is mandatory to prevent splay.
The production of display bezels and business machine covers from ABS 770S is governed by thin-wall filling constraints because the melt must enter 1.0–1.5 mm cavities without exceeding the thermal degradation boundary of the styrene-acrylonitrile phase. Formulation addition ratio in this segment is commonly 97.5 wt% ABS 770S, 2.0 wt% color masterbatch, and 0.5 wt% internal mold release agent; external lubricants are omitted because they migrate to the cavity surface and reduce gloss uniformity measured under ISO 2813 at 60° geometry. Sector-level compliance comprises IEC 62321-5:2013 and IEC 62321-6:2015 for RoHS substance verification in electrotechnical products, UL 94 HB at the actual minimum part thickness, and ISO 11469:2016 polymer marking requirements. Downstream processing uses accumulator-assisted high-speed injection molding machines with barrel temperature 225–245°C, mold temperature 50–70°C, and cavity surfaces polished to SPI A1 or equivalent mirror finish. Long bezels above 600 mm require sequential valve gating to drive the flow front in a controlled direction; early or late valve opening by more than 0.2 s relative to the screw position can create hesitation lines at 1.0–1.5 mm wall thickness. The packing switch-over is set at 96–98% actual shot volume, packing pressure is 40–60 MPa, and cooling time for 1.2 mm walls is 8–14 s. Terminal finished products include monitor bezels, television front frames, router housings, and multifunction printer control-panel surrounds. Process limit: material exposed to melt temperatures above 250°C for more than 6 min begins to generate volatile degradation species that cause silver streaks and gloss differentials; drying at 80°C to below 0.05 wt% moisture is required before processing when the resin has been stored above 60% relative humidity.
The main restriction on hot-runner feed temperature in vacuum cleaner housing tools is not the barrel set point but the temperature history experienced by the melt in manifold channels during production interruption. Multi-drop hot-runner systems with 8 drops and valve pins show silver streaking at flow-front meeting lines when the manifold is held above 245°C and shot-to-shot pause exceeds 20 s; the defect is caused by volatile low-molecular-weight species from styrene-acrylonitrile thermal degradation. Formulation addition ratio for floor tool bodies and canister shrouds is 100 phr ABS 770S with up to 20 wt% clean in-line regrind; a phosphite antioxidant package is pre-compounded at 0.1–0.2 phr only when the regrind fraction approaches the upper limit. Compliance standards are IEC 60335-1 clause 30 for resistance to heat and fire, IEC 60695-2-11:2014 glow-wire testing at the relevant wall thickness, IEC 62321 RoHS substance screening, and REACH 1907/2006 SVHC restrictions. The downstream process uses injection molding machines with clamp force 3,500–8,000 kN, barrel temperature 215–235°C, mold temperature 45–60°C, and gas-assist molding in handle sections to eliminate sink marks at wall junctions between 2.5 mm and 3.5 mm. The hot-runner manifold is maintained at 235–245°C rather than the maximum permissible melt temperature; nozzle tips are insulated to prevent heat soak during tool changes. Terminal finished products include canister vacuum shrouds, cyclone dust-cup bodies, floor-head base plates, and extension-tube retaining clips. Operational limits: ABS 770S should not be exposed to manifold temperatures above 250°C for more than 10 min cumulative during production pauses; if a pause exceeds 20 min, the first shot should be purged and discarded to avoid carbonized deposits in the tool.
Small kitchen appliance motor housings present a non-food-contact enclosure case in which ABS 770S is specified for blender bases, hand mixer side covers, coffee machine lower shells, and stand-mixer trim rings. The formulation addition ratio is 100 phr ABS 770S; if surface scratch resistance is required by the OEM, an anti-scratch additive is included at 0.5–1.0 wt%, but fillers and glass fiber are omitted to preserve surface gloss and low warpage. Compliance in this sector is based on IEC 60335-1 clause 30 resistance to heat and fire, UL 94 HB at 1.5 mm, and OEM test specifications for resistance to household cleaning agents and repeated lid-closing impact. Downstream processing runs on conventional cold-runner injection molding machines with barrel temperature 215–235°C, screw back pressure 0.5–1.0 MPa, mold temperature 40–55°C, and decompression after screw recovery limited to 3 mm to prevent air aspiration that produces splay. Multi-cavity tools with 2–8 cavities use fan gates or tab gates to reduce jetting; when a textured cavity finish is specified, mold temperature is raised to 50–55°C to improve grain replication. Terminal products include blender base shrouds, hand mixer outer housings, coffee machine side covers, and planetary stand-mixer trim rings. Operational boundary: cleaning tests using ester-based solvents should not be conducted on parts above 60°C because stress cracking can occur in constrained snap-fit bosses; contact with polycarbonate components requires evaluation for environmental stress crack propagation under load.
When a high-flow ABS is specified for toy building-block multi-cavity tools, the process window is controlled by the sub-0.8 mm gate region where premature freeze-off leaves short shots at the last-filled cavity. The switch-over point is therefore set at 96–98% of actual shot volume, mold temperature is maintained at 50–60°C, and filling time is compressed to 0.3–0.5 s using accumulator-assisted injection. Formulation addition ratio is 100 phr virgin ABS 770S; color masterbatch is added at 1–3 wt% and is selected only from pigment preparations whose extractable elements comply with EN 71-3:2019+A1:2021; regrind is excluded unless the converter has full source traceability and phthalate-free documentation under REACH Annex XVII entries 51 and 52. Sector compliance also includes EU 2011/65/EU recast, ASTM F963 for the U.S. market, and pre-screening against the REACH SVHC Candidate List. The downstream production process uses high-cavitation cold-runner molds of 32–64 cavities, hold pressure 35–60 MPa, screw rotation speed 60–100 rpm, and cooling time 5–8 s for 1.0–1.5 mm wall sections. Venting depth is limited to 0.02–0.03 mm to prevent flash on the high-flow matrix. Terminal finished products include building blocks, toy gear components, game-board trays, and toy appliance shells. Operational boundary: blending with acetal or polyamide must be avoided because of gate-area delamination; storage in contact with certain low-molecular-weight polyolefin packaging can cause surface staining if external lubricants are present.
Compounding operations select ABS 770S as the styrenic base in polycarbonate/ABS alloys where the target market includes thin-wall automotive interior carriers, battery charging accessories, and laptop lower covers. The addition ratio in twin-screw compounding is typically 60–70 wt% ABS 770S, 30–40 wt% bisphenol-A polycarbonate, 2–5 wt% MBS or acrylic impact modifier, 0.1–0.3 wt% phosphite antioxidant, and 0.1–0.2 wt% mold release agent; the ABS 770S fraction is maximized within the range when flow-length-to-thickness ratios exceed 150:1 and minimized when low-temperature impact retention is the primary specification. Compliance standards include ISO 2580-1 for ABS designations, ISO 21305-1 for specification of PC/ABS molding materials, EU 2011/65/EU, REACH 1907/2006, and UL 94 HB at the final part thickness. The downstream process uses intermeshing co-rotating twin-screw extruders with L/D 36:1 to 44:1, barrel temperature profile 230–260°C from feed to die, melt temperature at the die plate 270–280°C, vacuum venting at -0.08 MPa, and strand pelletizing with water bath temperature below 40°C. Terminal finished products include laptop lower covers, automotive interior decorative carriers, battery charger housings, and thin-wall electronic enclosure frames. Operational boundary: PC/ABS compounds based on ABS 770S are not processed above 280°C for more than 5 min because polycarbonate hydrolysis and styrene-acrylonitrile degradation accelerate; polycarbonate moisture must be below 0.02 wt% before feeding, and the use of ABS 770S at below 50 wt% of the total polymer content may shift the phase morphology toward PC-matrix behavior and reduce chemical resistance.
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Kumho Petrochemical ABS 770S is an injection-moulding grade acrylonitrile-butadiene-styrene terpolymer, supplied in pellet form and specified for high-flow, medium-impact applications in thin-wall industrial housings and interior components. The unfilled grade has a density of 1.04 g/cm³ determined under ISO 1183-1. Melt volume-flow rate is reported in supplier datasheets under ISO 1133-1 at 220 °C and 10 kg; values for the high-flow 770S are generally positioned above conventional general-purpose ABS grades and below super-high-flow ABS used for complex multicavity tooling. Processing is performed on reciprocating-screw injection moulding machines with a barrier or general-purpose screw having L/D of 20:1 to 24:1 and compression ratio 2.2:1 to 2.6:1. The polybutadiene dispersed phase contributes impact energy absorption but requires controlled shear and melt residence time to prevent yellowing, gloss shift, and generation of odour compounds. Published data for exact spiral-flow performance of this specific supplier configuration is limited; tool-specific pressure-loss measurements are required to validate fill velocity at the gate.
Moisture absorption in ABS pellets is moderate, but the acrylonitrile sequences are hygroscopic enough to cause hydrolytic surface defects when melt residual moisture exceeds 0.05 wt%. Pellets exposed to 23 °C and 50 % RH reach equilibrium moisture content in the 0.2–0.35 wt% range; at warehouse conditions above 60 % RH, pre-drying is mandatory because moisture uptake accelerates and may exceed the process limit within 6–12 h of opened bag exposure. Desiccant dryers with an air dew point below -40 °C, drying temperature of 80 °C, and residence time of 2–4 h reduce residual moisture below the threshold. The dew-point sensor must be installed at the drying hopper return, not only at the dryer outlet. In satellite dryers, a dry-air flow rate of 1.0 m³/h per kg/h of resin throughput is a minimum commissioning check. Residual moisture is best verified by loss-in-weight or Karl Fischer titration according to ISO 15512, not by drying time alone. Pellet surface temperature must remain below 95 °C to prevent sintering at the hopper cone; radial air distributors with the same outlet temperature are preferred.
Vacuum dryers operating below 30 kPa can shorten drying cycle but require pellet fines removal to avoid carryover into the vacuum pump.
The melt temperature window for unfilled ABS 770S is typically bounded by 210 °C and 240 °C at the nozzle, with rear zone 180–200 °C, middle zone 200–220 °C, front zone 210–230 °C, and nozzle set point 210–240 °C. For thin-wall parts of 1.2 mm nominal wall thickness in a 16-cavity tool, hydraulic injection pressure frequently falls between 80 MPa and 120 MPa depending on runner balance. Hold pressure should be set at 50–70 % of peak injection pressure, with hold time initially derived from gate freeze analysis. Screw speed should remain within 40–80 rpm, back pressure at 0.5–1.0 MPa, and cushion position at 3–6 mm to maintain shot-to-shot consistency. The use of hot runner systems is permitted if manifold and nozzle tip temperatures do not exceed 240 °C; local shear heating in narrow valve-gate clearances can produce effective melt temperatures above 260 °C, at which ABS degradation accelerates. Thermal decomposition onset in open-air thermogravimetry is normally observed near 260 °C; sustained operation above 250 °C is therefore outside the processing boundary. Melt residence time above 240 °C should not exceed 8 min; if a stoppage exceeds 15 min, purging with a rigid PVC or polypropylene transition material is required before restarting ABS feed.
| Stage | Parameter | Set-point range |
|---|---|---|
| Pre-drying | Dryer dew point | -40 °C to -30 °C |
| Pre-drying | Drying temperature | 78 °C to 82 °C |
| Pre-drying | Minimum residence time | 2 h to 4 h |
| Melt | Nozzle temperature | 210 °C to 240 °C |
| Melt | Melt temperature measured by air shot | 215 °C to 240 °C |
| Injection | Injection pressure, hydraulic | 80 MPa to 120 MPa |
| Injection | Hold pressure ratio | 50 % to 70 % of peak |
| Recovery | Screw surface speed | 0.15 m/s to 0.30 m/s |
| Recovery | Back pressure | 0.5 MPa to 1.0 MPa |
| Tool | Mould temperature | 40 °C to 60 °C |
Comparative tensile and flexural behaviour is determined on injection-moulded Type 1A specimens under ISO 527-2 and ISO 178. The high-flow 770S grade typically exhibits tensile yield stress in the 40–48 MPa range and flexural modulus between 2.1 GPa and 2.5 GPa. Because notched impact values are sensitive to notch radius and temperature, direct comparisons between ISO and ASTM data are invalid; the relevant notched Izod testing uses ISO 179-1/1eA at 23 °C. Table 1 lists the standard designations and representative published ranges for unfilled ABS of this flow class.
| Property | Test standard | Unit | Representative range |
|---|---|---|---|
| Density | ISO 1183-1 | g/cm³ | 1.04–1.06 |
| Melt volume-flow rate, 220 °C/10 kg | ISO 1133-1 | cm³/10 min | 18–24 |
| Tensile yield stress | ISO 527-2 | MPa | 40–48 |
| Flexural modulus | ISO 178 | GPa | 2.1–2.5 |
| Notched Izod impact, 23 °C | ISO 179-1/1eA | kJ/m² | 20–30 |
| Vicat softening temperature, B50 | ISO 306 | °C | 94–99 |
| Heat deflection temperature, 1.80 MPa | ISO 75-2 | °C | 82–88 |
| Flammability class at 1.5 mm | UL 94 | — | HB |
For appearance-critical surfaces, mould temperature variation of more than ±5 °C across the cavity creates visible gloss differences; cartridge heater zones should be individually controlled and the return side temperature set within 2 °C of the cavity side.
Substitution of ABS 770S for a lower-flow high-impact ABS grade shifts the process envelope toward shorter fill time and lower pressure loss. Spiral-flow mould testing generally shows that high-flow ABS fills 10–20 % longer at constant injection pressure, but the dispersed rubber concentration is lower than in a high-impact grade, reducing notched Izod and Charpy values. The difference arises from polybutadiene content and graft morphology; higher rubber content increases impact absorption but raises melt viscosity and reduces melt venting tolerance. When a tool is transferred, clamp force requirement may fall, but screw recovery time and hold-pressure decay must be re-established from short-shot studies. Mould shrinkage for unfilled ABS is generally 0.4–0.7 %, with transverse shrinkage 0.1–0.2 % higher than flow-direction shrinkage. Dimensional approval for snap-fit and bearing seats should require process capability index Cpk greater than 1.33 across 30 consecutive shots. Weld-line tensile strength in multi-gate tools is typically 60–70 % of un-welded strength under ISO 527-2; gate placement studies should therefore avoid weld lines in load-bearing ribs. Compared with semicrystalline competitors, ABS 770S provides lower mould shrinkage anisotropy but lower chemical resistance to organic solvents; compared with amorphous engineering resins such as PC/ABS, the grade offers easier flow but a lower heat deflection limit.
Continuous service temperature for unfilled ABS 770S under no external load is typically limited to 60–70 °C. Short-term heat resistance is bounded by the Vicat softening temperature of 94–99 °C and HDT-A of 82–88 °C under 1.80 MPa. The resin is susceptible to photolytic oxidation; unpigmented natural material must not be used for outdoor weatherable parts without addition of carbon black or organic UV absorbers. Contact with ketones, esters, aromatic hydrocarbons, and chlorinated solvents causes environmental stress cracking, especially at moulded-in residual stress levels above 5 MPa. Dilute acids and alkalis are tolerated at room temperature, but concentrated oxidizing acids and strong alkaline solutions are incompatible. The material carries UL 94 HB at 1.5 mm; applications requiring V-0 must use a flame-retardant ABS grade instead of 770S.
Regrind usage above 20 wt% increases melt-flow variation and can reduce impact strength; first-quality production should limit regrind to 20 % and verify MVR shift after each 500 kg of reclaimed material.