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Kumho Petrochemical ABS KU-680

    • Product Name: Kumho Petrochemical ABS KU-680
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 304107
    Density 1.05 g/cm3
    Melt Flow Rate 5.0 g/10 min
    Tensile Strength 50 MPa
    Elongation At Break 20%
    Flexural Strength 80 MPa
    Flexural Modulus 2500 MPa
    Izod Notched Impact Strength 20 kJ/m2
    Rockwell Hardness 110 R-scale
    Heat Deflection Temperature 95 °C at 1.82 MPa
    Vicat Softening Temperature 105 °C
    Flammability Rating UL94 HB
    Mold Shrinkage 0.4-0.7%

    As an accredited Kumho Petrochemical ABS KU-680 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Kumho Petrochemical ABS KU-680 is supplied in 25 kg moisture-proof woven bags, palletized for industrial handling and storage.
    Container Loading (20′ FCL) Kumho Petrochemical ABS KU-680 loaded in a 20′ FCL container, palletized and shrink-wrapped for secure, dry ocean transport.
    Shipping Kumho Petrochemical ABS KU-680 is shipped as non-hazardous ABS copolymer pellets, typically in 25 kg woven bags or 500–1000 kg jumbo bags on pallets. Transport in dry, ventilated containers; keep away from moisture, direct sunlight, and excessive heat. Not classified as dangerous goods for transport.
    Storage Store Kumho Petrochemical ABS KU-680 in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, flames, and oxidizing agents. Keep original containers tightly closed and palletized off the floor to prevent moisture pickup and contamination. Avoid prolonged high humidity, maintain dry handling practices, and follow local storage regulations.
    Shelf Life Typical shelf life is 24 months when stored in original unopened packaging in a cool, dry, well-ventilated area away from direct sunlight.
    Application of Kumho Petrochemical ABS KU-680

    Miniature circuit breaker housings and terminal covers moulded from Kumho Petrochemical ABS KU-680 are processed on high-speed injection lines with clamp capacities between 80 t and 180 t; the limiting variable is not tonnage but the filling-phase pressure drop across a wall-stock reduction from 2.5 mm to 1.2 mm at the latch boss. When the melt front passes a gate land of 0.8 mm, the apparent shear rate at the runner wall exceeds 10,000 s⁻¹; above this threshold, viscous dissipation raises local melt temperature by 8–12 °C and accelerates oxidative yellowing if the granulate has not been dried to a residual moisture content below 0.02 wt%. Drying is performed in a desiccant hopper with air dew point below −40 °C and a residence time of 2–4 h at 80 °C; exceeding 90 °C can cause surface hydrolysis of the nitrile component, leading to silver streaks at the weld line. For electrical enclosures, the compound is processed at a melt temperature of 230–250 °C measured by an immersion thermocouple at the nozzle, with a mould temperature of 30–50 °C. Excessive melt temperature above 260 °C initiates depolymerisation, generating styrene monomer vapour that condenses on the cavity steel and causes delamination adjacent to the gate. Regrind is incorporated at a maximum of 20 wt%; beyond that level, the notched Izod impact under ISO 180/1A falls below 12 kJ/m², and the enclosure can crack during the terminal torque test. Compliance for unattended appliance circuit enclosures is assessed according to IEC 60695-2-11, with unfilled ABS grades typically achieving a glow-wire flammability index of 650 °C at 1.5 mm; for 850 °C requirements, the base resin is compounded with a brominated flame-retardant system rather than used neat.

    Representative verification matrix for unfilled ABS in switchgear enclosures
    Standard / methodCondition / specimenTypical acceptance
    IEC 60695-2-11Glow wire 650 °C, 1.5 mmNo ignition or self-extinguish within 5 s
    IEC 60068-2-30Damp heat, 40 °C / 93% RH, 48 hNo tracking, insulation resistance > 1 MΩ
    IEC 60112Comparative tracking index, solution ACTI ≥ 600 V
    ISO 180/1ANotched Izod, 23 °C≥ 12 kJ/m²

    Injection gate geometry for these enclosures uses a rectangular edge gate with a land length of 0.8–1.2 mm and a gate depth of 0.6–0.8 mm; the cold slug well is extended to 3 mm diameter to trap the solidified nozzle tip. Production-scale hot runner manifolds require thermal uniformity of ± 2 °C across the manifold, because local overheating in the runner channel promotes generation of free styrene and lowers the molecular weight of the regrind stream. Terminal blocks and distribution boxes produced from KU-680 are assembled with copper alloy inserts; the insert temperature before overmoulding is maintained at 90–110 °C to minimise hoop stress cracking at the plastic-metal interface.

    What Limits Flow Length in Thin-Wall Instrument Bezels?

    Flow-length-to-thickness ratio is the first-order constraint in automotive instrument cluster bezels, where nominal wall thickness has been reduced to 1.0–1.5 mm to control part mass. For hub-and-spoke bezel geometries, the melt flow path commonly exceeds 300 mm from a single valve-gated hot runner drop; under these conditions, the filling pressure rises above 140 MPa unless the melt volume-flow rate under ISO 1133-1 at 220 °C/10 kg is above 18 cm³/10 min. If the certificate of analysis for KU-680 shows lower flowability, the toolmaker must reduce the flow path by adding a second gate or increase wall stock to 1.8 mm; published data for this specific configuration is limited and must be validated on a moulding trial with pressure transducers installed in the nozzle and the end of fill. Weld lines generated at bosses and vent openings retain only 55–65% of the nominal tensile strength measured by ISO 527-2; therefore, gate sequencing and valve-pin delay are used to move the weld line into a low-stress zone rather than relying on melt temperature alone.

    For bezel applications, the mould temperature is held at 50–70 °C to improve grain reproduction on the textured surface and to reduce the depth of the frozen skin layer. Injection velocity is set to fill the cavity in 0.8–1.5 s; slower filling increases the risk of short shots at the far edge of the instrument cluster hood, while faster filling can entrain air at the parting line and produce burn marks at the last-filled rib. Packing pressure is limited to 60–80 MPa because higher packing intensifies sink marks over the screw bosses. Colour masterbatch loading is controlled at 1.5–2.5 wt%; if a carbon black masterbatch exceeds 0.5 wt% in the final part, the surface resistivity may shift, but the notched Izod impact under ISO 180/1A can fall below the interior trim requirement of 10 kJ/m². Compliance for automotive interior parts includes fogging under DIN 75201, odour evaluation under VDA 270, and xenon-arc ageing under ISO 4892-2; ABS grades without UV stabiliser packages show colour shift beyond ΔE 3 after 200 h of exposure and are therefore limited to interior zones with low solar load. Final parts include instrument cluster bezels, centre console trim plates, HVAC louvre assemblies, and steering column shrouds.

    Chrome-plated ABS components for sanitary and appliance trims depend on selective oxidation of the butadiene phase to create microcavities that anchor the electroless nickel deposit. In the etching bath, the polymer is immersed in a chromic acid solution of 380–420 g/L and sulphuric acid of 180–220 g/L at 65–70 °C for 5–10 min; the etching rate is sensitive to the volume fraction and domain size of the butadiene phase. ABS grades containing 15–25 wt% butadiene with a relatively coarse dispersion give higher peel strength, but published data for KU-680 in this specific electroplating configuration is limited and must be confirmed by scanning electron microscopy of the etched surface before production. After neutralisation in a reducing bath, the part is activated with a palladium-tin colloidal solution, followed by electroless nickel of 0.2–0.4 µm thickness, bright acid copper of 15–25 µm, semi-bright nickel of 8–12 µm, and chromium of 0.2–0.5 µm. Peel strength measured under ASTM B533 should exceed 0.8 N/mm on flat sections, and thermal cycling under ASTM B604 from −40 °C to 80 °C for 10 cycles must not produce blistering or loss of adhesion at edges.

    Injection moulding of electroplating substrates excludes external mould release agents and limits processing aids to below 0.1 wt%, because residual surface film disrupts the etch uniformity and produces skip plating on the back side of handles. Regrind is not permitted for Class A surfaces; any regrind generated from sprues and runners is segregated for non-plated structural parts. Mould temperature is raised to 60–80 °C to reduce birefringence and to promote a uniform surface skin that withstands the aggressive etch cycle. The final products include shower mixer bezels, door handle shells, automotive badges, and appliance control knobs; compliance is often stated against EN 248 for chromium plating adhesion and ISO 4527 for autocatalytic nickel-phosphorus coatings where a bright top layer is not used.

    Laser-Processed Housings Demand Controlled Moisture and Low Outgassing

    Laser-marked office-equipment housings require a moulding resin with low volatile emission and a consistent surface finish to maintain legibility of data matrix codes and regulatory markings. During laser marking, the near-infrared beam ablates pigment particles in the surface layer, generating local temperatures above 1,000 °C; if the resin contains excessive moisture or processing oils, the vaporised organics redeposit on the laser lens as a brown film and reduce mark contrast. KU-680 is pre-dried to a residual moisture concentration below 0.03 wt%, and the hot runner system is purged with 5–10 kg of fresh material after any colour or additive change. Melt temperature is held at 230–250 °C, mould temperature at 40–60 °C; a mould temperature above 70 °C increases gloss on untextured surfaces and can reduce the contrast of laser-marked characters to below the readability threshold for barcode scanners.

    Laser-sensitive additive masterbatch is added at 0.5–1.0 wt%; carbon black masterbatch is kept at 0.2–0.5 wt% to achieve a dark base colour without excessive soot loading that would reduce the notched Izod impact under ISO 180/1A. The housing wall thickness is typically 2.0–3.0 mm; below 1.5 mm, the laser pulse can perforate the surface and expose internal ribs, while above 3.5 mm, sink marks around bosses become visible after painting or pad printing. Compliance for office equipment housings includes UL 94 HB at 1.5 mm and IEC 62368-1 for information technology equipment; volatile organic emission is monitored by headspace gas chromatography against an internal specification of 50 µg/g total organic carbon from the moulded part. Final products include printer front covers, scanner bezels, multifunction control panels, and keyboard frames.

    When Flame-Retardant Masterbatches Shift the Process Window

    Compounding of a brominated flame-retardant system into ABS KU-680 alters the viscosity curve in the low-shear region and narrows the thermal processing window because the brominated aromatic species begin to liberate hydrogen bromide above 240 °C. A typical formulation for a UL 94 V-0 rating at 1.5 mm includes 12–18 wt% brominated epoxy or tetrabromobisphenol A derivative and 4–6 wt% antimony trioxide synergist; the exact loading depends on the bromine content of the masterbatch and the wall thickness of the power strip housing or charger shell. On a corotating twin-screw extruder with an L/D ratio of 40:1 and vacuum venting at −0.08 MPa, the compound is processed at a barrel set temperature of 180–220 °C with the die head held below 230 °C; screw speed is limited to 250–350 rpm to prevent excessive shear heating at the kneading blocks. The extruder barrel and screw elements are specified in a corrosion-resistant bimetallic alloy because free hydrogen bromide attacks nitrided steel and introduces iron contamination into the compound.

    The melt viscosity increase associated with flame-retardant loading has a measurable effect on injection pressure: at the same wall thickness of 2.0 mm, the filling pressure is 20–35% higher than for unfilled ABS. This pressure rise forces the processor to raise the clamp capacity for the same projected area or reduce the number of cavities on a multi-cavity tool. Flame-retardant ABS is also more sensitive to residence time; if the machine is stopped for more than 10 min at melt temperature, the material near the screw tip develops a red-brown degradation layer that must be purged with 15–20 kg of fresh compound. UL 94 vertical burning behaviour is highly composition-dependent: a 2 wt% shift in antimony trioxide loading can change the total flaming time from below 50 s to above 250 s and cause failure of the cotton indicator. The following matrix illustrates the sensitivity; actual KU-680 responses require laboratory confirmation on the production tool.

    Illustrative formulation sensitivity matrix for brominated FR/ABS systems
    Brominated FR loadingSb₂O₃ loadingVertical burn, 1.5 mmNotched Izod ISO 180/1A
    12 wt%4 wt%V-2 or V-1; afterflame clear10–12 kJ/m²
    15 wt%5 wt%V-0; total flaming < 50 s8–10 kJ/m²
    18 wt%6 wt%V-0; char layer dense6–8 kJ/m²

    Final flame-retardant components include power strip housings, wall adapter shells, and uninterruptible power supply terminal covers. Compliance is assessed under UL 94 V-0 at the minimum production wall thickness, IEC 60695-11-10, and IEC 62368-1; halogenated formulations must also satisfy RoHS limits for polybrominated diphenyl ethers below 1,000 ppm and for antimony trioxide as an indirect article 33 candidate list substance under EU Regulation 1907/2006 where applicable. Because the flame-retardant package reduces weld-line strength, the gate position is moved away from snap-fit arms and screw bosses; the packing time is shortened by 20–30% compared with unfilled ABS to reduce residual stress at the flame-retardant particle-matrix interface. Incompatibility with amine-based stabilisers should be noted, because basic amines accelerate decomposition of brominated flame retardants and generate a dark, odorous deposit on the mould surface.

    In diagnostic device enclosures moulded from unfilled ABS, the primary process limitation is not mechanical performance but the retention of mould release agents and volatile oligomers after repeated steam or hydrogen peroxide sterilisation. The mould is therefore run without external release agents; ejection is achieved with a draft angle of 1.5–2.0° and a polished core surface with a draw polish in the ejection direction. Hot runner channels are specified with a minimum radius at every melt turn and are kept below 250 °C to reduce residence-time degradation. The granulate is dried to 0.02 wt% moisture or lower in a desiccant dryer with validated lot-to-lot verification; a single lot with higher moisture can shift the melt viscosity and produce dimensional variation outside the ±0.05 mm tolerance allowed for snap-fit assembly of two housing halves. Melt temperature is maintained at 220–240 °C, mould temperature at 40–60 °C, and cushion distance is held at 2–4 mm to ensure consistent packing pressure without overfilling the cavity.

    Biocompatibility evaluation for non-implant device enclosures is performed according to ISO 10993-5 for in vitro cytotoxicity, ISO 10993-10 for sensitisation and irritation, and USP <87> for biological reactivity. If gamma sterilisation is specified, the total absorbed dose is limited to 25 kGy; above this level, the styrene-acrylonitrile matrix yellows and the notched Izod impact under ISO 180/1A declines by more than 20%. Ethylene oxide sterilisation is less aggressive toward ABS but leaves an absorbed gas residue that must be desorbed at 40–50 °C for 24–48 h; the part design must include venting channels in the shipper carton to prevent ethylene oxide entrapment. Final products include handheld blood glucose meter housings, portable diagnostic reader shells, and ultrasonic nebuliser enclosures; all exposed edges are radiused to 0.5 mm minimum to prevent crack initiation during repeated drop testing under IEC 60601-1.

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    Certification & Compliance
    More Introduction

    Kumho Petrochemical ABS KU-680 is a pelletized acrylonitrile-butadiene-styrene graft copolymer supplied for sheet extrusion and thermoforming operations in which heat deflection under load, low-temperature ductility, and melt strength during calender roll processing are critical. The grade designation KU-680 identifies a high-impact extrusion resin within the manufacturer’s ABS portfolio; it is differentiated from higher-flow injection molding grades by a lower melt flow rate of approximately 7 g/10 min at 220 °C/10 kg per ASTM D1238-20 and by controlled rubber-phase grafting that raises melt viscosity while maintaining thermoforming draw. Representative manufacturer-published values include a notched Izod impact strength at 23 °C of 350 J/m per ASTM D256-23, a heat deflection temperature under 1.82 MPa of 89 °C per ASTM D648-18, and a Vicat softening temperature of 100 °C per ISO 306:2022. Principal application areas include refrigerator inner liners, automotive interior panels, luggage shells, sanitation components, and industrial covers. The resin is supplied in natural and precolored pellet form, and its representative property profile is evaluated using ASTM and ISO methods described in the comparative data section below.

    Does KU-680 Require Different Drying and Screw Conditions Than Injection-Grade ABS?

    Processing behavior differs from injection-grade ABS because sheet extrusion demands uniform melt temperature, low moisture, and sufficient melt strength at the die lip. Dehumidifying hopper drying is required before extrusion; the resin should be dried to a moisture content below 0.05 % using a dew point of -30 °C or lower. A typical drying schedule is 80 °C for 2–4 h, with the upper time limit extended only when ambient relative humidity exceeds 60 %. Overdrying above 85 °C for more than 4 h can produce pellet yellowing and surface splay due to thermal oxidative degradation of the polybutadiene phase. Single-screw extruders with L/D ratios from 24:1 to 33:1 and compression ratios of 2.5:1 to 3.0:1 are preferred; a barrier screw with Maddock mixing elements improves melt homogeneity and reduces gel fisheyes. Barrel temperature profiles typically increase from 180 °C in the rear zone to 210–220 °C at the metering section, with an adapter temperature of 210 °C and a slot die temperature of 220–235 °C. Melt temperature should not exceed 240 °C for residence times longer than 30 min, because polybutadiene oxidation accelerates and reduces notched Izod performance per ASTM D256-23. These conditions are derived from production-scale sheet equipment with polished chrome rolls and top/bottom roll temperatures maintained between 70 °C and 110 °C depending on sheet thickness.

    Representative manufacturer-published property data for KU-680 are tabulated below. Values are typical and are not specification limits; process-specific colorants, regrind, and sheet thickness can shift the measured values by several percent. Published data for application-specific configurations such as coextruded structures or high-gloss film lamination are limited, and preliminary trials are required for those end-uses.

    PropertyTest methodRepresentative value
    Melt flow rate at 220 °C/10 kgASTM D1238-207 g/10 min
    Specific gravityASTM D792-201.04 g/cm³
    Tensile strength at yieldASTM D638-2244 MPa
    Tensile elongation at breakASTM D638-2225 %
    Flexural strengthASTM D790-1762 MPa
    Flexural modulusASTM D790-172,200 MPa
    Notched Izod impact at 23 °C, 3.18 mmASTM D256-23350 J/m
    Notched Izod impact at -30 °C, 3.18 mmASTM D256-23130 J/m
    Rockwell hardnessASTM D785-23105 R-scale
    Heat deflection temperature at 1.82 MPa, annealedASTM D648-1889 °C
    Vicat softening temperature at 1 kgISO 306:2022100 °C
    Mold shrinkage, flow direction, 3.2 mmASTM D955-210.4–0.6 %

    Gel Content, Rubber Grafting, and Low-Temperature Ductility in Sheet Thermoforming

    The melt-phase architecture of KU-680 is produced with a controlled graft copolymerization route that disperses polybutadiene-based rubber particles within a styrene-acrylonitrile matrix. The product’s low gel count is intended to reduce undispersed crosslinked rubber specks on sheet surfaces, a defect that becomes visible in high-gloss refrigerator liners after thermoforming. Low-temperature ductility is verified through notched Izod testing at -30 °C; a representative value of 130 J/m per ASTM D256-23 supports deep-draw freezer liner applications, but the processor must confirm the relationship between sheet thickness and formed-part impact because thermoforming-induced molecular orientation can reduce edge ductility in corners. Rubber particle size distribution and grafting efficiency also affect melt elasticity and sheet sag resistance. During thermoforming, sheet surface temperatures should be maintained between 150 °C and 180 °C with aluminum mold temperatures of 60–80 °C; below this range, incomplete replication of embossed textures occurs, and above this range, excessive sheet thinning and surface rubber degradation can produce gloss shifts.

    Comparative processing behavior against high-impact polystyrene and injection-grade ABS is governed by differences in melt strength, polarity, and chemical resistance. High-impact polystyrene typically has lower notched Izod impact, often below 120 J/m at 23 °C, while KU-680’s representative notched Izod value of 350 J/m permits reduced wall thickness for equivalent impact. The density of KU-680 at 1.04 g/cm³ is comparable to many HIPS grades, so direct part-weight comparisons must account for wall-thickness reduction and flexural modulus. Stress-cracking resistance to fats, oils, and cleaning agents is higher in ABS than in HIPS; however, KU-680 remains susceptible to ketones, esters, aromatic hydrocarbons, and concentrated acetic acid. Compared with a general-purpose injection-grade ABS with melt flow rates above 20 g/10 min per ASTM D1238-20, KU-680’s lower flow improves die-lip stability and calender roll release but requires higher melt pressure and extruder torque. Compared with ASA or AES grades, KU-680 is not intended for unpainted outdoor exposure because the polybutadiene phase has limited UV stability; outdoor weatherable parts require a coextruded ASA cap layer or UV-stabilized color system.

    When KU-680 Is Selected for Food-Contact or Automotive Interior Applications

    For food-contact uses, the finished article must meet the extractives and residual acrylonitrile monomer limits established in 21 CFR 177.1020. Compliance cannot be inferred from the resin grade alone; migration testing under the intended food type, contact time, and temperature is required. For automotive interior applications, low odor and low VOC performance may require selection of controlled lubricant packages and optional vacuum stripping; odor evaluation under VDA 270:1992 is commonly applied to interior trim components. Regulatory compliance is formulation-specific. The natural resin is typically assessed under REACH Regulation (EC) No 1907/2006 for SVHC content below 0.1 % w/w and under RoHS Directive 2011/65/EU for restricted heavy metals; color concentrates, regrind, and processing aids may alter the final compliance status. Flammability is rated according to UL 94; the natural grade is typically HB at a thickness of 3.0 mm, but the final part must be evaluated in its finished thickness and color.

    Standard or directiveRelevant scopeApplication condition
    ISO 2580-1Designation system for ABS extrusion and molding materialsUsed for grade specification and material designation
    ASTM D4673-16Classification system for ABS plastics and alloysBasis for property group and specification coding
    21 CFR 177.1020Acrylonitrile copolymers for food contactResidual monomer and extractives limits must be verified
    REACH (EC) No 1907/2006SVHC and Annex XVII restrictionsNatural resin declaration required; additives assessed separately
    RoHS Directive 2011/65/EUPb, Cd, Hg, Cr(VI), PBB, PBDE restrictionsFinal article assessment required
    UL 94Flammability of plastic materialsNatural grade typically HB at 3.0 mm; final color and thickness must be tested

    Field observations from sheet extrusion lines indicate that the most common failure modes are moisture-induced splay and gel-related surface defects when drying and screw mixing deviate from the stated ranges. Regrind levels above 20 % may increase yellowing and reduce notched Izod impact per ASTM D256-23; any regrind stream should be free of PVC, acetal, and polyolefin contamination. Purging between color changes should be performed with SAN-based or acrylic-based purge compounds; PVC purges must be avoided because thermal degradation releases hydrogen chloride and accelerates chain scission in ABS. The operational ceiling of 240 °C should be regarded as a limit, not a target, and startup at the lower end of the temperature profile is recommended to minimize edge tear and reduce die-lip buildup.

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