Products

Kumho Petrochemical ABS HAG-7300

    • Product Name: Kumho Petrochemical ABS HAG-7300
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 992237
    Typical Density 1.05 g/cm³
    Melt Flow Rate 30 g/10 min (220°C/10 kg)
    Tensile Strength 45 MPa
    Elongation At Break 15%
    Flexural Modulus 2200 MPa
    Notched Izod Impact Strength 20 kJ/m² (23°C)
    Heat Deflection Temperature 85°C (1.82 MPa)
    Vicat Softening Temperature 95°C
    Rockwell Hardness 105 R
    Mold Shrinkage 0.4-0.7%
    Ul 94 Flammability HB

    As an accredited Kumho Petrochemical ABS HAG-7300 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Kumho Petrochemical ABS HAG-7300 is supplied in 25 kg moisture-proof bags, palletized and labeled for safe industrial transport.
    Container Loading (20′ FCL) Loading 20′ FCL container with Kumho Petrochemical ABS HAG-7300, 25 kg bags, palletized, shrink-wrapped, and secured for ocean transport.
    Shipping Kumho Petrochemical ABS HAG-7300 is shipped as non-hazardous ABS resin pellets, normally in 25 kg moisture-proof bags or bulk containers on pallets. It is handled as general cargo and should be kept cool, dry, ventilated, and protected from direct sunlight and heat. Follow the SDS and local transport regulations.
    Storage Store Kumho Petrochemical ABS HAG-7300 in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and oxidizing materials. Keep containers or bags closed to prevent moisture, dust, and contamination. Use clean, dry pallets, avoid crushing or stacking damage, and follow good housekeeping and static-control practices.
    Shelf Life Kumho Petrochemical ABS HAG-7300 typically has a 24-month shelf life when stored cool, dry, and away from direct sunlight and moisture.
    Application of Kumho Petrochemical ABS HAG-7300

    In display bezel and monitor housing production, Kumho Petrochemical ABS HAG-7300 is metered into the injection moulding cell at 100 parts per hundred resin (phr) base polymer; colour masterbatch dosage is held at 1.5 to 2.5 phr, carbon black for opaque black grades at 0.5 to 1.0 phr, and internal mould release at 0.2 to 0.4 phr. Clean regrind from sprue and runner systems may be incorporated up to 20 wt% for Class A visible surfaces when lot-to-lot melt flow index per ISO 1133-1:2022 remains within ±10% of the virgin value; beyond this threshold, surface bloom, gloss loss, and gate-area streaking become measurable. Compliance for this segment is anchored to IEC 62368-1:2018 for audio/video, information, and communication technology equipment enclosures, RoHS Directive 2011/65/EU Annex II, REACH Regulation (EC) No 1907/2006, WEEE Directive 2012/19/EU, and UL 94 where unfilled ABS of this type is typically classified as HB; any application requiring V-0, V-1, or 5VA must use a flame-retarded grade instead of HAG-7300. The moulding process uses a single-screw reciprocating injection unit with screw L/D of 20:1 to 22:1, compression ratio 2.2 to 2.5, and a shut-off nozzle to prevent drool at melt temperatures of 220 to 240°C. Pre-drying is conducted in a dehumidifying hopper dryer at 80°C for 2 to 4 h to reach residual moisture below 0.02 wt% with a dew point below -30°C; moulding floor storage above 60% relative humidity requires re-drying after bag opening beyond 4 h. Multi-cavity monitor-bezel tools with hot-runner thermal gates exhibit cavity-to-cavity fill imbalance above 0.15 to 0.20 s, which produces differential pack pressure and visible gloss banding near gate vestiges; balancing flow lengths, limiting decompression to 3 mm, and setting hold pressure at 60 to 80% of peak injection pressure suppresses this failure mode. Mould temperature is maintained at 40 to 60°C, and ejection is programmed only after gate freeze to avoid sink. Finished parts include monitor rear bezels, monitor front fascias, laptop lid-back panels, set-top box front faces, remote-control bottom shells, and desktop printer control-bezel frames.

    Floor-care appliance shells, air-purifier inlet grilles, and dehumidifier panels represent a moulding family where HAG-7300 is selected for dimensional stability in multi-rib, multi-boss exterior parts rather than for load-bearing functions. The formulation runs at 100 phr HAG-7300; titanium-dioxide-based white masterbatch is added at 2.0 to 4.0 phr for white side panels, while permanent antistatic masterbatch is dosed at 0.8 to 1.5 phr where surface dust accumulation must be limited. Clean regrind is allowed up to 25 wt% for non-appearance internal supports and fan baffles, but white-lot colour drift is controlled by limiting regrind to 15 wt% for externally visible white parts. Compliance is evaluated under IEC 60335-1:2020 clause 21 for mechanical strength and clause 30.2 for glow-wire ignition behaviour; HAG-7300 is not a flame-retarded grade and must not be used for live parts or for enclosures requiring a GWFI of 750°C or 850°C unless product-specific testing demonstrates compliance. The production line typically employs a multicavity cooled-runner or hot-runner injection mould with clamp pressure calculated at 3 to 5 tons per in² of projected part area. Vacuum-cleaner cowls and dehumidifier side panels are filled with a two-stage injection profile—slow to fast—to avoid jetting around living-hinge bosses; pack pressure remains on until 1.2 to 1.4 times gate-freeze time, as determined by short-shot gate-freeze studies. Maintaining cooling-water delta below 3°C across stationary and moving halves reduces warpage in parts over 300 mm long. Terminal components include vacuum cleaner cowls, air purifier inlet grilles, dehumidifier shell panels, microwave door outer frames, and air-conditioner decorative end caps with integrated ventilation slots and snap-fit ribs.

    When grained automotive trim requires low-emission processing without structural load

    HAG-7300 is applied only to non-structural, low-heat automotive interior trim where load-bearing requirements do not exceed the capacity of an ABS grade; continuous-use temperature should remain below 70°C, and direct UV exposure requires a separate stabilisation review. The formulation starts at 100 phr HAG-7300; UV stabiliser masterbatch at 0.3 to 0.5 phr is used for parts receiving intermittent solar load through glazing, carbon black at 2.0 to 3.0 phr for black parts, and anti-scratch or slip additive at 0.5 to 1.0 phr to reduce surface marring on grained exterior surfaces. Clean closed-loop regrind is limited to 15 wt% because higher ratios can increase volatiles and odour in interior environments. Amine-based colour concentrates are excluded from the formulation; production-scale hot-runner trials have shown yellowing at hot-runner tips above 230°C when nitrogen-containing additives contact residual nitrile moieties under high shear. Compliance follows ISO 3795/FMVSS 302 for horizontal burn rate, VDA 270 for odour testing, VDA 278 for VOC and FOG, and REACH Regulation (EC) No 1907/2006 with OEM-specific reporting under IATF 16949 supplier manuals. Published data for this specific HAG-7300 grade under modern low-VOC automotive interior protocols is limited, so product-specific validation is required before program approval. The moulding process uses a grained cavity surface with texture depth 10 to 15 µm and minimum draft angle 1.5° per side. Sequential valve-gate hot-runner systems are used for long door-pull bezels to prevent weld-line visibility at gate boundaries. Melt temperature is kept at 220 to 230°C, with barrel residence time capped at 5 minutes to suppress thermal degradation and volatile generation. Ejector plates reduce white stress marks at textured ribs. Finished parts include door pull bezels, centre console side trim, seat side shields, quarter trim inserts, and non-airbag dashboard decorative strips.

    For toy and juvenile recreation product housings, the dominant requirement is substance migration compliance rather than mechanical specification alone. HAG-7300 is moulded at 100 phr; colorant masterbatch is dosed at 1.0 to 3.0 phr, and metallic or pearlescent pigment at 2.0 to 5.0 phr. No ortho-phthalate plasticiser is added because the application must satisfy the restriction framework for articles intended for children. Clean regrind is permitted up to 25 wt% only when the regrind stream is segregated and validated against the original migration certification. Migration kinetics in the polymer matrix become relevant at elevated storage temperatures above 40°C, where low-molecular-weight pigment carriers may migrate; this is controlled by specifying masterbatch carriers with molecular weight above 1,000 g/mol and testing per EN 71-10. Compliance includes EN 71-3:2019+A1:2021 for element migration, ASTM F963-23, CPSIA Section 108 for phthalate limits, and REACH Regulation (EC) No 1907/2006 Annex XVII entries 51, 52, and 66. This usage does not extend to direct food-contact or mouthing articles unless validated by specific food-contact migration testing. The process uses a polished A-2 mould finish for high-gloss toy shells; melt temperature is held at 230°C, and screw recovery time is monitored because high-aspect-ratio metallic flake increases viscosity and can extend recovery by 10 to 20%. Gate sizing is increased by 15 to 25% over standard ABS to avoid packing loss around the gate, and vent depth is maintained at 0.015 mm to prevent gas burn at filling end. Terminal components include toy vehicle body shells, building-block housing panels, electronic learning toy enclosures, action-figure accessory trays, and carnival-game plastic housings.

    Office automation covers and flat document trays enter the moulding cell with strict flatness and snap-fit fatigue requirements, and HAG-7300 is processed for thin-wall enclosures where dimensional consistency determines acceptance. The formulation runs at 100 phr HAG-7300; black masterbatch at 1.0 to 2.0 phr, scratch-resistant additive at 0.3 to 0.6 phr, and clean regrind at 20 to 30 wt% is acceptable for internal non-Class A structures but not for outer covers. The compliance set is IEC 62368-1:2018 for ICT/AV enclosure safety, UL 94 at HB for non-current-carrying covers, RoHS Directive 2011/65/EU Annex II, and REACH Regulation (EC) No 1907/2006. Moulding uses large platens with hot-runner valve gates; thin-wall document feeder trays at 2.0 mm nominal wall demand high injection velocity, but velocity above the critical shear threshold causes jetting at gate lands. Melt temperature is set at 230 to 240°C, mould temperature at 45 to 55°C, and hold pressure at 50 to 70 MPa for parts up to 450 mm length. Flatness is held to 0.35 mm per 100 mm when cooling-water delta across cores is below 2°C, and conformal cooling is required at deep boss features to avoid sink-induced warp. Terminal products include printer front covers, scanner lids, multifunction-device control-panel housings, document feeder input trays, and copier output-sorter facias.

    Is low-current electrical accessory cladding compatible with standard ABS stabilisation packages?

    For non-energised electrical accessory dress plates and surround frames, HAG-7300 is used as a dimensional-stable cladding resin, not as an electrical insulator for live contacts. The formulation ratio is 100 phr HAG-7300; titanium dioxide white masterbatch at 3.0 to 5.0 phr for colour saturation, and clean regrind is limited to 10 wt% because wall-plate tolerances of ±0.1 mm are sensitive to shrinkage variation from repeated heat history. Compliance is assessed under IEC 60669-1 for electromechanical switch and plate assemblies, RoHS Directive 2011/65/EU Annex II, and REACH Regulation (EC) No 1907/2006; any live-contact enclosure or terminal carrier must satisfy a higher glow-wire or V-0 requirement that may fall outside HAG-7300 capability. The moulding process uses a cold-runner edge gate to avoid hot-runner colour streaks in white parts; mould temperature is kept at 55 to 65°C to stabilise post-mould shrinkage. Ketone-based cleaning solvents are excluded from post-mould wiping because they stress-crack ABS at gate and weld-line regions; purging for changeover uses acrylic or HDPE rather than PVC. Terminal parts include switch surround plates, socket dress frames, dimmer knob covers, and surface-mounted trunking accessories.

    Free Quote

    Competitive Kumho Petrochemical ABS HAG-7300 prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618005193850

    Email: sales8@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Kumho Petrochemical ABS HAG-7300 is an injection-molding acrylonitrile-butadiene-styrene grade positioned for visual components requiring controlled surface appearance. The HAG-series designation indicates high-appearance gloss optimization rather than a flame-retardant, heat-stabilized, or plating-specific formulation. Procurement specifications for this grade should require the following test methods: ISO 1183-1:2019 for density, ISO 1133-1:2022 for melt volume-flow rate at 220 °C under 10 kg, ISO 527-1/-2:2019 for tensile properties, ISO 178:2019 for flexural modulus, ISO 180/A:2019 for notched Izod impact, and ISO 75-2:2013 for deflection temperature under load at 1.82 MPa. The material is supplied as cylindrical pellets, and lot-specific color stability is conventionally monitored by pellet and molded-plaque spectrophotometry under ASTM D6290.

    The base polymer is a polybutadiene-rubber-modified styrene-acrylonitrile terpolymer. Generic ABS composition ranges—styrene 40–60 wt%, acrylonitrile 15–35 wt%, and polybutadiene 5–30 wt%—define the structural envelope but are not a substitute for a lot-specific certificate. The continuous mass polymerization route typically used for this class yields a narrower rubber particle size distribution and lower gel content than many emulsion-polymerized ABS grades used for extrusion or calendering. Published data for this specific configuration is limited in secondary literature; incoming inspection should therefore be built around a traceable sequence comprising resin lot number, bag moisture exposure, dryer dew point, melt temperature, and shot-to-shot cushion stability.

    What Injection Molding Parameters Are Required to Preserve Gloss and Notched Izod Impact?

    Pre-drying is performed in a desiccant dryer with a dew point no higher than −30 °C, an inlet air temperature of 80–90 °C, and a residence time of 2–4 h. Residual moisture at the machine throat should remain below 0.05 wt%. When moisture exceeds 0.07 wt%, volatilized water at the melt front creates splay and reduces 60° gloss as measured under ASTM D523. The plasticating unit should use a general-purpose three-zone screw with L/D ≥ 20:1 and compression ratio 2.2:1–2.8:1. A barrel profile from 190 °C at the feed section to 230 °C at the nozzle is a representative starting point; measured melt temperature should lie between 220 °C and 250 °C. Operation above 260 °C accelerates polybutadiene degradation and shifts the molded part toward lower impact and yellowing.

    Injection velocity should be set to fill a 2 mm nominal wall section in 0.4–1.0 s. Transfer to holding pressure is normally set at 95–98 % of complete fill, because late transfer produces overpacking and residual stress at the gate. Hydraulic hold pressure in the range 40–80 MPa is a starting reference for accumulator-assisted machines; electric machines require plastic-pressure integration rather than hydraulic gauge correlation. Mold temperature at the cavity surface should be controlled between 40 °C and 80 °C. For high-gloss surfaces, a mold temperature of 60–70 °C is used to delay skin solidification and replicate the tool finish.

    Hot-runner channel diameters should be sized to keep shear rates below 20,000 s⁻¹ in the gate land to reduce melt fracture and gate blush. The gate tip temperature should not exceed 260 °C, and valve-gate sequencing should be tuned to avoid hesitation lines. When throughput increases by more than 20–30 % of the initial validation window, a revalidation run is required because shear heating in the runner changes effective melt viscosity and can create gloss bands on the final surface.

    On production-scale electric injection molding machines with clamp force between 1,500 kN and 4,000 kN, gloss failure frequently appears as a localized defect at the gate blush or on the rib-opposed surface rather than as a global loss. The spatial pattern indicates that moisture nucleates at the end of fill, not that bulk thermal degradation has occurred. A 25 kg bag stored at 25 °C/70 % RH for 24 h can take up sufficient water to exceed 0.3 wt%. Therefore closed-loop vacuum conveying with dry-air purge is preferred. The dryer exit dew-point monitor should be data-logged, and regeneration cycle maintenance should be scheduled by temperature set-point verification rather than visual inspection of desiccant color alone.

    Drying, Melt Temperature, and the Onset of Volatile Defects in High-Shear Runner Systems

    Volatile defects are most probable when melt temperature, gate shear rate, and residual moisture interact. At a hot runner gate shear rate above 20,000 s⁻¹, local viscous dissipation can raise the melt above 260 °C even when the nozzle set point is 230 °C. This produces low-boiling degradation products from the polybutadiene phase and creates brown streaks. To isolate thermal from moisture-related defects, a two-level drying experiment is used: one lot is dried to 0.03 wt% residual moisture and a second is exposed to 0.08 wt%. If defect density is equivalent under the same injection conditions, the source is thermal; if the higher-moisture lot shows splay while the dry lot does not, dryer performance is limiting.

    Pressure diagnostics provide additional resolution. A cavity-pressure sensor behind the last fill point should record a repeatable peak within 10 % lot-over-lot. If peak pressure rises by more than 15 % without a recipe change, melt viscosity has shifted, often due to high residual moisture or a molecular-weight distribution change. In high-gloss parts, such shifts are visible before mechanical property failure occurs, making cavity-pressure curves a more sensitive quality indicator than melt-volume-flow-rate testing alone.

    Tool surface condition is a first-order variable. For SPI-A1 or SPI-A2 finish replication, the cavity should be polished to Sa ≤ 0.012 µm. Chromium or nickel plating thickness between 0.025 mm and 0.075 mm should be uniform over the entire cavity surface. Mold release should be avoided; if external release is unavoidable, a silicone-free evaporative release that does not accumulate on textured surfaces is preferred because any mold deposit changes surface energy and alters the 60° gloss reading.

    Molding shrinkage for this class of ABS is usually 0.4–0.7 % in the flow direction and 0.4–0.6 % transverse, depending on wall thickness and packing. Toolmakers should not use a single isotropic shrinkage factor for a visible part with ribs and bosses; a linear shrink gauge under ISO 294-4 is used to generate cavity-specific corrections. For automotive interior components with high appearance, dimensional stability is often measured after 24 h at 23 °C/50 % RH; unannealed parts can continue moisture-equilibrated dimensional drift if packed under high stress.

    The grade is used in injection-molded visual housings and non-structural trim: small appliance fascia panels, vacuum cleaner body components, audio/video front frames, and cosmetic packaging. Typical part wall thickness is 1.5–3.0 mm, and the primary acceptance criterion is often absence of sink, knit-line visibility, and gloss differential. In these applications, destructive fitting or drop-weight tests such as ASTM D2463 on the assembled article are more meaningful than the notched Izod value alone because the load path includes ribs, snap fits, and ultrasonic weld lines. HAG-7300 is not positioned for thick-wall extruded profiles, calendered sheet, or foam structures; if extrusion is attempted, melt strength and draw-down behavior must be obtained from the vendor because injection-molding grades do not typically certify these values.

    Compared with high-flow general-purpose ABS, HAG-7300 typically has a lower melt-volume-flow rate and a tighter surface appearance specification. Compared with high-impact ABS, notched Izod impact under ISO 180/A at 23 °C is lower because gloss optimization generally requires a smaller and more uniform polybutadiene rubber particle size distribution. Compared with high-heat ABS, deflection temperature under load at 1.82 MPa is lower; therefore continuous exposure to forced-air temperatures above 85 °C should not be specified without direct measurement of part-surface temperature and confirmation from the vendor’s heat-ageing data.

    For mold-filling simulation, viscosity coefficients should be derived from capillary rheometry under ISO 11443:2021 at 220 °C, 240 °C, and 260 °C. Generic ABS coefficients may underpredict pressure drop in sequential hot-runner systems by 8–15 % when melt temperature falls below 230 °C. Pressure-volume-temperature data should be entered for the grade because specific volume changes during packing control sink and warpage. Simulations that ignore pressure-dependent viscosity may underappreciate gate freeze time and underfill thin-wall regions.

    When Finished Articles Are Shipped to EU and North American Electrical/Electronic Markets, a Supplier Certificate Checklist Applies

    Compliance positions are product-specific and should be obtained from the resin supplier’s product stewardship statement; material-type inference is not accepted in a technical file. The matrix below defines the minimum documentation set for a typical molded housing application. Absence of a statement for any category should trigger a supplier change or additional analytical verification.

    Framework Relevant Scope Documentation Required
    RoHS 2011/65/EU + (EU) 2015/863 Pb, Hg, Cd, Cr(VI), PBB, PBDE, DEHP, BBP, DBP, DIBP in homogeneous material Supplier certificate per batch or lot; no greater than maximum concentration values
    REACH 1907/2006 Candidate List SVHC > 0.1 wt% in each article Written confirmation or Section 15 of SDS
    WEEE 2012/19/EU Electrical and electronic equipment marking For the finished assembly, not the resin alone
    ISO 2580-2 ABS designation and test basis Certificate of analysis with lot number

    The certificate should also specify whether the grade carries a California Proposition 65 listing; no such statement can be inferred from the polymer backbone. No food-contact or medical-grade claim should be made for HAG-7300 unless the supplier provides a specific written approval. For export to markets requiring ASTM materials, data generated under ASTM D638-14 for tensile and ASTM D256-10 for Izod impact should be requested rather than converting ISO values through unverified correlation.

    Top