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Kumho Petrochemical ABS HAG-7230

    • Product Name: Kumho Petrochemical ABS HAG-7230
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 264863
    Manufacturer Kumho Petrochemical
    Product Name ABS HAG-7230
    Material Type Acrylonitrile Butadiene Styrene (ABS)
    Grade HAG-7230
    Appearance Pellets
    Specific Gravity 1.04
    Melt Flow Rate 20 g/10 min (220°C/10 kg)
    Tensile Strength 450 kg/cm²
    Flexural Modulus 23,000 kg/cm²
    Rockwell Hardness 105 R-scale
    Heat Deflection Temperature 85°C
    Vicat Softening Temperature 98°C
    Molding Shrinkage 0.4–0.7%
    Flammability Rating UL 94 HB
    Processing Method Injection Molding

    As an accredited Kumho Petrochemical ABS HAG-7230 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-7230 is packaged in 25 kg moisture-resistant paper bags, palletized for safe industrial storage and transport.
    Container Loading (20′ FCL) 20′ FCL container loading: Kumho Petrochemical ABS HAG-7230, packed in 25 kg bags, palletized, approximately 20 MT net per container.
    Shipping Kumho Petrochemical ABS HAG-7230 is shipped as a non-hazardous thermoplastic resin, typically in 25 kg bags or jumbo bags on pallets. Keep dry, away from direct sunlight and excessive heat. Normal freight transport applies; no special UN hazard classification is required.
    Storage Store Kumho Petrochemical ABS HAG-7230 in a cool, dry, well-ventilated area at ambient temperature, away from direct sunlight, heat, sparks, flames, moisture, and strong oxidizers. Keep original containers tightly closed, labeled, and protected from physical damage. Avoid incompatible chemicals and prevent dust generation or static buildup. Maintain good housekeeping and comply with local storage regulations.
    Shelf Life Approximately two years when stored unopened in a dry, cool area away from direct sunlight and moisture.
    Application of Kumho Petrochemical ABS HAG-7230

    Injection molding of HAG-7230 into thin-wall monitor bezels, printer covers, scanner lids, and router housings starts with desiccant drying at 80 °C for 2 h to 4 h, with return-air dew point below −40 °C and pellet moisture below 0.05 wt%. When ambient relative humidity exceeds 60%, the drying time is extended to 4 h and the hopper receiver purge is verified. A general-purpose screw with 20:1 to 22:1 L/D and compression ratio of 2.0:1 to 2.5:1 is used. Barrel temperatures are set from 190 °C in the rear zone to 230 °C in the front zone, with the nozzle held at 240 °C to 250 °C. For wall thickness below 1.6 mm, the melt temperature is maintained at 230 °C to 250 °C and the mold surface at 50 °C to 70 °C. First-stage injection speed is profiled high through the runner and gate, then reduced before switchover; injection pressure peaks between 80 MPa and 120 MPa. Holding pressure is set at 50% to 70% of peak and maintained until gate freeze, with screw cushion kept at 3 mm to 5 mm. Failure modes observed on production machines include jetting from undersized gates, silver streaking when pellet moisture reaches 0.08 wt%, and gloss variation at end-of-fill when mold temperature drops below 50 °C. The final electrical enclosures are evaluated under IEC 62368-1:2023; tensile specimens are tested according to ISO 527-2/1A/50, and lot melt flow is checked by ISO 1133-1:2022 at 220 °C/10 kg.

    What Injection Window Prevents Silver Streaking in High-Gloss Vacuum Cleaner Shells?

    Silver streaking in vacuum cleaner canister bodies, dust chambers, hose exits, and wheel housings is typically produced by moisture vapor or gas release at the flow front. Drying is performed at 80 °C for 3 h to 4 h to a moisture target below 0.05 wt%; hot-air dryers are insufficient when ambient humidity exceeds 60%. The melt temperature is held between 240 °C and 250 °C, with the nozzle set 10 °C lower than the front zone to reduce drool. Mold temperature is elevated to 60 °C to 80 °C against SPI A-1 polished steel because gloss loss accelerates below 50 °C. Injection speed in the first stage is set to 100 mm/s to 150 mm/s and switched over at 95% to 98% of fill volume. Parting-line vents are cut to 0.02 mm to 0.03 mm depth and 4 mm to 6 mm width at last-fill locations, knit lines, and rib intersections. Back pressure of 0.8 MPa to 1.2 MPa is maintained to homogenize the melt. A valve-gated hot runner with sequential opening is preferred for large canister shells; this prevents visible weld lines at the hose exit and handle sockets. Holding pressure is stepped from 60% to 30% of peak injection pressure over 6 s to 8 s, and cooling continues until the average mold surface falls below 70 °C. Regrind use above 20% is not recommended for A-surface parts because oxidized rubber phase reduces gloss and shifts yellowness index. Surface acceptance is quantified at 60° using ASTM D523 or ISO 2813, with a typical target above 90 GU on the same mold finish. Thermal history above 250 °C for more than 6 min must be avoided. End products include canister bodies, motor covers, filter chambers, and wheel housings; mechanical integrity is confirmed per IEC 60335-1:2020 and restricted substances per RoHS 2011/65/EU with amendment (EU) 2015/863.

    Starting injection-molding windows for HAG-7230 across three wall regimes; validate per ISO 1133-1:2022 and mold-flow simulation
    ParameterThin-wall electronics below 1.6 mmHigh-gloss appliance shells 2.0–2.8 mmFan blades 1.5–2.5 mm
    Drying temperature80 °C80 °C80 °C
    Drying time2 h–4 h3 h–4 h2 h–4 h
    Moisture targetbelow 0.05 wt%below 0.05 wt%below 0.05 wt%
    Melt temperature230 °C–250 °C240 °C–250 °C235 °C–250 °C
    Mold temperature50 °C–70 °C60 °C–80 °C55 °C–70 °C
    Injection speed80 mm/s–120 mm/s100 mm/s–150 mm/s60 mm/s–100 mm/s
    Holding pressure50%–70% of peak60%–30% stepped60%–70% of peak
    Back pressure0.5 MPa–1.0 MPa0.8 MPa–1.2 MPa0.5 MPa–1.0 MPa
    Screw cushion3 mm–5 mm4 mm–6 mm3 mm–5 mm

    Across forced-air cooling modules for air purifiers, humidifiers, and pedestal fans, HAG-7230 is selected for the combination of high melt flow and sufficient stiffness in thin airfoil sections. Blades are typically gated at the hub center with a hot-tip or three-plate cold runner to create balanced flow from the hub to the outer ring. Wall thickness ranges from 1.5 mm to 2.5 mm, and gate diameter is kept at 60% to 80% of the hub thickness to prevent jetting. Melt temperature is maintained at 235 °C to 250 °C, mold temperature at 55 °C to 70 °C, and holding pressure at 60% to 70% of peak for 4 s to 6 s. Shrinkage anisotropy between the flow and transverse directions is a primary defect source. Published shrinkage data for this exact radial flow configuration in HAG-7230 is limited; therefore, mold compensation factors should be derived from ISO 294-4 plaques molded with the identical gate geometry and process settings. Ejection should use a stripper plate or wide lifters rather than small pins, because pin marks on airfoil surfaces act as stress concentrators under cyclic loading. Parts are ejected after core surface temperature falls below 70 °C to reduce post-ejection warpage. Rotors are balance-checked to ISO 1940-1 G 6.3 and corrected by trimming at the blade tip; residual imbalance tolerance is set by the fan motor supplier. Continuous service in 65 °C ambient requires verification against heat deflection temperature measured by ISO 75-2/A at 1.82 MPa, which for unfilled high-flow ABS remains below 100 °C. End products are axial fan impellers, louvered front guards, motor mounting supports, and air-directing rings.

    When Cyclopentane-Based Blowing Agents Contact Refrigerator Door Caps

    Refrigerator door caps, handle trim, and rack retainers molded in HAG-7230 are exposed to cyclopentane or hydrofluorocarbon blowing agents during polyurethane foam filling. The foam exotherm plus chemical exposure can trigger environmental stress cracking at molded-in stress concentrations. Stress relief is performed before foam injection in a forced-air oven at 70 °C for 30 min to 60 min; this can alter gloss and must be validated on production fixtures. Mold temperature is raised to 60 °C to 80 °C to reduce surface stress during filling. Gates are positioned away from screw bosses, snap-fit hooks, and foamed-in features; all internal corners retain a minimum radius of 0.8 mm. Packing is held until gate freeze to avoid sink marks at boss bases and to reduce differential shrinkage. Environmental stress cracking is screened with ISO 22088-3 bent-strip specimens exposed to the same blowing agent used in foam production. Silicone-based mold release sprays are avoided because they interfere with polyurethane adhesion and can create peel failure at the foam-plastic interface. The ABS parts are not direct food-contact surfaces; they are retained behind the interior lining, so food-contact requirements are governed by the liner material. Flame retardance is documented to UL 94 HB at the specified thickness, and volatile substances are controlled under REACH EC 1907/2006. End products include door caps, handle trims, shelf retainers, and kick-plate covers.

    Compliance and test-method matrix for HAG-7230 downstream conversion
    RequirementStandard / test methodApplication note
    Melt volume-flow rateISO 1133-1:2022 at 220 °C, 10 kgVerify each lot before start-up
    Tensile propertiesISO 527-2/1A/50Specimen type 1A at 50 mm/min
    Flexural modulusISO 178:2019Three-point bending, data from material datasheet
    Notched impactISO 179-1/1eA or ISO 180/1A23 °C, record edgewise and flatwise if required
    Heat deflection temperatureISO 75-2/A at 1.82 MPaUse for service temperature limits
    Vicat softening temperatureISO 306/B50Report loading and heating rate
    Specular glossASTM D523 / ISO 2813 at 60°Reference SPI A-1 mold finish
    FlammabilityUL 94 HBThickness as marked on the material certificate
    Electrical enclosure safetyIEC 62368-1:2023Consumer electronics enclosures
    Household appliance safetyIEC 60335-1:2020Insulation and mechanical strength clauses relevant to plastics
    Restricted substancesRoHS 2011/65/EU, (EU) 2015/863, REACH EC 1907/2006Supply chain documentation required

    Countertop Appliance Structural Frames and Condensation Exposure Limits

    Stand mixer bases, food processor lower housings, blender motor covers, and electric kettle outer sleeves use HAG-7230 for high-flow filling of consolidated rib-and-boss geometries. Wall thickness from 2.0 mm to 2.8 mm demands two-stage holding to avoid sink marks on visible surfaces. Melt temperature is set at 220 °C to 240 °C, mold temperature at 50 °C to 70 °C, and back pressure at 0.5 MPa to 1.0 MPa. Gate thickness should be at least 60% of the adjacent wall, and a cold well is placed beyond the last cavity to trap degraded material. Condensation exposure on appliance bases requires that drains and weep holes prevent standing water accumulation; ABS is not hydrolytically degraded by short-term water contact but can stress-crack when cleaning agents penetrate stressed snap-fit regions. Ketones, esters, and aromatic hydrocarbons are incompatible with ABS and must not be used as assembly lubricants or cleaning solvents. Vegetable oil and citrus-based cleaners can also initiate environmental stress cracking at high residual stress; compatibility tests use ISO 22088-3 with the actual service fluid. Appliance safety testing follows IEC 60335-1:2020, and flammability classification is documented to UL 94 HB. End products include stand mixer bases, blender motor covers, food processor lower housings, and kettle outer sleeves; no direct food-contact claim is made unless a specific grade-specific certificate supports it.

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    Certification & Compliance
    More Introduction

    Kumho Petrochemical ABS HAG-7230 is a high-heat acrylonitrile-butadiene-styrene injection-molding grade positioned for thin-wall automotive interior and electrical enclosure components requiring dimensional stability during heat soak. Manufacturer technical literature characterizes the material as a rigid, opaque ABS with specific gravity near 1.05 g/cm³ under ISO 1183, Vicat softening temperature in the 95–99 °C range under ISO 306/B50, and melt volume-flow rate in the 9–13 cm³/10 min range at 220 °C/10 kg under ISO 1133-1. Lot-specific certification is required because polymerization and compounding shifts alter melt viscosity and pigment dispersion by up to 10%. Reported tensile yield strength falls in the 44–50 MPa range under ISO 527-2, flexural modulus in the 2,300–2,600 MPa range under ISO 178, and notched Izod impact strength at 23 °C in the 18–22 kJ/m² range under ISO 180/A. The grade is specified for instrument panel sub-structures, console side covers, air-outlet assemblies, glove-box surrounds, and painted or grained trim where general-purpose ABS exhibits excessive deflection or gloss loss after solar load.

    How Should HAG-7230 Be Dried and Melt-Processed on Reciprocating-Screw Injection Lines?

    Residual moisture controls surface quality and melt stability. Desiccant pre-drying at 80–90 °C for 2–4 h to a pellet moisture content below 0.05 wt% is mandatory when ambient relative humidity exceeds 60% or when material has been stored in unlined silos. The dryer must deliver a dew point of -40 °C to -30 °C, and sealed hopper residence should be limited to 8 h; longer heating produces yellowing and variable melt viscosity. Wet pellets generate splay, silver streaks, and brittle weld lines that cannot be corrected by raising melt temperature without triggering butadiene-phase degradation.

    Melt processing on hydraulic or servo-driven reciprocating-screw machines with L/D 20:1–22:1 and compression ratio 2.5:1–3:1 uses barrel zones between 200 °C and 240 °C, with nozzle melt temperature held at 220–250 °C. Short-fill trials and pressure-drop studies should define the lower boundary for thin-wall filling; the upper boundary is set by rubber-phase thermal damage, visible as black specks, brown streaks, and a rise in yellowness index exceeding 2 units. Mold temperature is maintained at 50–80 °C to improve knit-line strength and grain replication. Injection fill time for wall stock of 2.0–2.5 mm is commonly 0.5–1.5 s, with pack pressure of 40–70 MPa and hold time set by gate-seal testing rather than cavity pressure peak. Hot-runner systems should avoid dead spots and shear imbalance above 100,000 s⁻¹ at the gate; residence time at melt temperature should not exceed 15 min.

    Process failure modes observed on production lines include gate blush when injection velocity is ramped too early, jetting when the gate is undersized, and delamination when the melt is contaminated with polycarbonate. Purging with general-purpose ABS or acrylic cleaning compound is suitable after processing polyolefins; purging with polycarbonate should be avoided because residual PC forms immiscible layers and weakens notched impact at -30 °C. Mold-release sprays containing silicone should not be specified because they migrate to the surface and alter paint adhesion after 24 h. Clean polypropylene or polyethylene purge pads are acceptable for shutdown, but long residence above 250 °C should be avoided.

    The shear-thinning response of HAG-7230 at typical melt temperatures means that filling pressure is more sensitive to gate diameter than to melt temperature within the recommended range. Increasing gate diameter from 1.0 mm to 1.5 mm can reduce injection peak pressure by 10–20% in thin-wall parts, while raising melt temperature by 5 °C reduces viscosity by 3–7%. Tool corrections should therefore prioritize gate land length and runner geometry before thermal adjustments. Spiral-flow data under ISO 1133-1 are not a substitute for cavity-filling simulation because high-heat ABS grades show pressure-dependent viscosity at pressures above 80 MPa. If recompounding with color masterbatch or additives is required, co-rotating twin-screw extruders with L/D 36:1–40:1 and mild shear screw elements are used. High-shear dispersion of pigments above 250 °C can lower impact by enlarging the dispersed rubber phase or crosslinking the butadiene; masterbatch letdown ratios above 4 wt% require validation by notched Izod and melt flow testing, not only colorimetric inspection.

    Mechanical and dimensional design data for HAG-7230 show the expected trade between heat resistance and low-temperature toughness. Mold shrinkage is generally 0.4–0.7% in flow and transverse directions, with higher values appearing in thick ribs and bosses. Post-molding shrinkage during heat soak is anisotropic; parts measured after 24 h at 80 °C can show an additional 0.05–0.15% loss in critical dimensions, so fixtures and locating holes should allow for this movement. Weld-line tensile strength in unfilled ABS typically retains only 60–75% of bulk tensile strength under ISO 527-2. Thin-wall connectors gated on multiple sides can fail at the knit line if mold temperature is below 50 °C or if packing pressure is removed before gate freeze. The material is not recommended for load-bearing threaded inserts in cyclic cold-temperature impact because localized stress concentration at the insert can reduce the effective impact threshold by 20–30% compared with unloaded sections. Published data for cyclic fatigue and long-term creep under thermo-oxidative aging for this specific grade is limited; component programs requiring plastic-strain or fatigue design values should commission grade-specific testing under ISO 527-2, ISO 899-1, or ISO 22088-2.

    When HAG-7230 Replaces General-Purpose ABS in Instrument Panel and Trim Components

    In elevated-temperature interior applications, the difference between HAG-7230 and general-purpose ABS is first thermal. General-purpose grades with Vicat softening temperatures of 90–95 °C may deflect at air-vent or top-pad locations where solar soak raises surface temperature to 100–110 °C; HAG-7230 has a Vicat advantage of 2–8 K, placing it above typical short-term solar soak limits but below most PC/ABS grades. The second difference is melt flow; high-heat ABS typically sacrifices flow by 20–35% compared with general-purpose ABS of similar rubber content, which can reduce the number of cavities that can be filled on a given press or require an increase in melt temperature of 5–10 °C. The third difference is impact distribution: notched Izod values are adequate for short-rib loading, but below high-impact or low-gloss grades. Selection is therefore a balance of heat, processability, and low-temperature impact.

    PropertyTest standardHAG-7230 high-heat ABSGeneral-purpose ABSPC/ABS typical
    DensityISO 11831.05 g/cm³1.04–1.06 g/cm³1.12–1.15 g/cm³
    Vicat softening temperatureISO 306/B5095–99 °C90–95 °C105–130 °C
    Melt volume-flow rateISO 1133-19–13 cm³/10 min at 220 °C/10 kg15–30 cm³/10 min at 220 °C/10 kg8–20 cm³/10 min at 260 °C/5 kg
    Notched Izod impact at 23 °CISO 180/A18–22 kJ/m²20–30 kJ/m²45–60 kJ/m²
    Flexural modulusISO 1782,300–2,600 MPa1,900–2,300 MPa2,200–2,500 MPa
    Heat deflection temperatureISO 75-1/A89–94 °C82–88 °C95–115 °C

    The values are representative industry ranges; lot-specific certificates govern because compounding additives and rubber-particle size distribution shift measured results. HAG-7230 should not be specified as a direct substitute for PC/ABS where low-temperature ductility or high-energy impact absorption is required, because the notched Izod gap is large and becomes more pronounced below -20 °C under ISO 180/A.

    Chemical compatibility boundaries are narrower than for semi-crystalline olefins. Dilute acids, aliphatic hydrocarbons, and aqueous detergent solutions at low temperatures are generally tolerated, while esters, ketones, aromatic hydrocarbons, and polar solvents attack the styrene-acrylonitrile matrix. In-cabin cleaners containing ethanol or isopropanol may cause stress crazing on molded-in tabs or snap-fits if residual stress exceeds 20 MPa. Continuous wet-heat exposure below 70 °C is accepted in HVAC ductwork, but intermittent condensation and dry-heat cycling can reduce notched impact by 10–15% after 1,000 h; this must be considered for warranty durability. Unpainted exterior use is limited because UV exposure degrades the butadiene segment, causing surface chalking and gloss loss under ASTM D523 within 500–1,000 h of accelerated weathering. Painted or film-laminated surfaces require adhesion promoters and topcoats that do not contain aggressive solvents.

    Electrical enclosure and office equipment applications use the grade where dimensional stability under moderate heat load is required. Because ABS is inherently insulating but not a high comparative tracking index material, tracking resistance should be verified under IEC 60112 before specifying HAG-7230 for printed-circuit-board retainers or terminal guards. Flame-retardant behavior is not automatically implied by the HAG designation; unfilled ABS typically does not carry a UL 94 V-0 rating unless a flame-retardant additive system is selected. For interior components requiring low smoke or low toxicity, grade-specific data should be obtained from the supplier.

    Regulatory compliance for automotive interior polymers is commonly evaluated against REACH 1907/2006/EC, RoHS 2011/65/EU Annex II, and OEM-specific emission requirements under VDA 278. The grade is supplied as a thermoplastic resin without intentionally added lead, cadmium, mercury, hexavalent chromium, or polybrominated biphenyls, but compliance must be verified from the supplier's material declaration because compounding additives vary with color. Food-contact status is not implied unless the specific colored compound is tested and listed under the relevant jurisdiction. For underhood or exterior painted parts, specification engineers should confirm heat aging performance under ISO 188 and paint adhesion under ISO 2409.

    Storage in unopened, moisture-proof packaging below 30 °C and below 60% relative humidity is recommended; opened gaylords should be sealed or dried before use. Recycled sprues and runners may be reintroduced up to 20 wt% when the regrind is dry, unpainted, and free of oil. Repeated thermal cycling of regrind above 250 °C reduces butadiene-phase impact performance and should be validated by melt flow and Izod testing under ISO 1133-1 and ISO 180/A. Lot-to-lot variation in high-heat ABS is an operational boundary that molding shops manage by maintaining drying records, shot-weight logs, and cavity-pressure curves rather than by relying on a single melt temperature setting.

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