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Guangdong YinXi ABS ABS313HL

    • Product Name: Guangdong YinXi ABS ABS313HL
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 564587
    Productname Guangdong YinXi ABS ABS313HL
    Manufacturer Guangdong YinXi Technology Co., Ltd.
    Polymertype ABS (Acrylonitrile Butadiene Styrene)
    Grade ABS313HL
    Form Pellets
    Color Natural
    Moldingshrinkage Percent 0.4-0.6
    Flammability UL94 V-0

    As an accredited Guangdong YinXi ABS ABS313HL factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Guangdong YinXi ABS ABS313HL is supplied in 25 kg woven bags, palletized for industrial shipment.
    Container Loading (20′ FCL) Guangdong YinXi ABS ABS313HL packed in 25 kg bags, palletized and loaded into a 20′ FCL dry container for export.
    Shipping Guangdong YinXi ABS ABS313HL is shipped as non-hazardous ABS thermoplastic resin, typically in sealed 25 kg bags. It is not classified as dangerous goods for transport. Store in a dry, ventilated area, away from direct sunlight, moisture, and contamination; avoid bag damage.
    Storage Store Guangdong YinXi ABS ABS313HL in a cool, dry, well-ventilated warehouse away from direct sunlight, heat sources, flames, moisture, and ignition. Keep original packaging sealed and palletized; avoid crushing or excessive stacking. Prevent contact with strong oxidizers and solvents. Maintain good housekeeping, dust control, and appropriate spill containment, following local regulations.
    Shelf Life Store Guangdong YinXi ABS ABS313HL sealed in a cool, dry, ventilated area; typical shelf life is 12 months.
    Application of Guangdong YinXi ABS ABS313HL

    Injection molding lines processing Guangdong YinXi ABS ABS313HL for automotive interior trim typically begin at the drying station rather than at the press feed throat. Desiccant-bed hopper dryers with closed-loop air dew point below -30 °C are set at 80 ± 5 °C for 2–4 h to bring residual moisture below 0.05 wt% before melt processing; conveying lines from dryer to press hopper are purged with dried air in plants where relative humidity exceeds 60%. The material is run as a natural or precolored injection-molding grade, with color metered at 2–4 wt% masterbatch at the feed throat when production requires rapid color change. Mold temperature is held at 40–60 °C for low-stress structural inserts and air-vent blades, while visible A-surface panels may require 60–80 °C to reduce flow-hesitation gloss variation and sink-mark contrast. Barrel temperature profiles from rear zone to nozzle are typically 190–210 °C, 210–230 °C, 220–240 °C, and 225–245 °C, with melt temperature measured by an insertion pyrometer between 225 °C and 245 °C; exposure above 255 °C or residence time above 8 min produces brown streak defects and a measurable drop in Charpy notched impact strength due to thermal degradation of the butadiene phase. Parts produced include steering-column lower shrouds, instrument cluster housings, door panel inserts, and HVAC vent assemblies. Lot acceptance testing follows ISO 1133-1:2022 for melt volume-flow rate, ISO 2580-2 for designation, and ISO 294-1 for specimen preparation; mechanical release documentation commonly requests ISO 179-1/1eA Charpy notched impact and ISO 527-2 tensile properties. For OEM interior programs requiring low volatile organic compound emissions, the molder must validate the supplied ABS313HL lot against the vehicle maker’s emission specification; where low-emission status is not explicitly documented in the batch certificate, VDA 277 headspace gas chromatographic total carbon emission data should be obtained before approving visible interior components.

    Why Does Plating Adhesion on ABS313HL Depend on Butadiene Etch Morphology?

    Electroplating of ABS313HL is governed by the condition of the dispersed polybutadiene phase near the molded surface. The chemical etching step uses a chromic acid/sulfuric acid bath operating at 65–72 °C for 5–15 min, depending on rubber particle size and butadiene distribution; the etch dissolves surface butadiene domains and creates the micro-porous structure that anchors the metallic layer. ABS grades without controlled rubber morphology produce variable etch depth and low peel strength, so ABS313HL should be qualified for plating only after the batch certificate confirms that rubber content and particle size distribution fall within the plating-range specification. In plating-grade production, mold temperature is raised to 60–80 °C to minimize surface stress and orientational skin effects, and mold-release agents containing silicone or hydrocarbon waxes are eliminated from the production cell. Surface preparation practice follows ASTM B727-04(2019). After etching, parts pass through a palladium-tin colloid activator, an accelerator, electroless nickel or copper deposition, and then electrolytic copper, semi-bright nickel, bright nickel, and chromium plating sequences. Adhesion is checked by peel testing following ASTM B533-85(2019), with acceptance set by the automotive or sanitary OEM rather than by a universal minimum; decorative automotive trim, shower rings, and plumbing handle shells are the principal terminal products. Over-etching beyond the optimum creates brittle, weakly attached plate because mechanical interlock is undermined by excessive butadiene removal; under-etching leaves too few anchoring sites. The etch-rate window is narrow, and bath catalyst concentration, agitation, and racking density must be controlled so that temperature does not vary more than ±2 °C across the load. Plating line compliance with REACH authorisation for chromium trioxide in the etching step and the absence of hexavalent chromium in the final article must be documented before shipment. Published data for ABS313HL in commercial chrome-plated configurations is limited; adhesion must be validated on production tooling with molded parts from each lot.

    Thin-Wall Electronic Enclosures at 1.0 mm Nominal Wall

    When nominal wall thickness falls to 1.0 mm or below, the practical processing envelope for ABS313HL is constrained by two competing failure modes: short shots due to premature freeze-off and splay due to moisture or shear heating. Short-shot prevention requires nozzle pressures above 120 MPa, injection velocities of 120–180 mm/s, and a melt temperature at the upper end of the ABS window, typically 235–250 °C; however, this upper temperature is within 5 °C of the degradation onset for long hot-runner residence times. Thin-wall electronic enclosures are therefore produced on all-electric injection machines with screw L/D ratios of 18:1–22:1, shot capacities at 30–70% of barrel volume, and hot-runner manifolds designed for low dead-stop volume. Mold cooling is arranged so that cavity surface temperature stays at 50–70 °C, and conformal cooling is preferred for wall sections below 0.8 mm. The compound is pre-dried at 80 °C for 3–4 h to below 0.05% moisture; a dew point of -30 °C is maintained through the feed throat to avoid hydrolysis splay. Terminal products include laptop keyboard deck frames, router housings, USB hub shells, and handheld instrument cases. Compliance is evaluated against IEC 62368-1 for information technology equipment enclosures and the relevant UL 94 horizontal burn classification for unfilled ABS, unless a flame-retardant variant is used. Tensile modulus after molding is monitored per ISO 527-2/1A, and notched impact per ISO 179-1/1eA at 23 °C. Because published data for ABS313HL in this specific thin-wall configuration is limited, production tool trials with cavity pressure sensors are required to establish the lot-specific melt volume-flow rate and flow-length window.

    Wall thickness bandMelt temperatureNozzle temperatureMold temperatureInjection velocityHold pressure
    < 1.2 mm235–250 °C240–250 °C50–70 °C120–180 mm/s60–80 MPa
    1.2–2.5 mm225–240 °C230–245 °C40–60 °C60–120 mm/s45–65 MPa
    2.5–4.0 mm215–230 °C220–235 °C30–50 °C30–60 mm/s35–50 MPa

    Flame-retardant compounding of ABS313HL for IEC 62368-1 information technology equipment enclosures is run on a co-rotating twin-screw extruder with 40:1 L/D ratio, side feeding for heat-sensitive additives, and vacuum venting at -0.08 MPa to strip residual styrene monomer and moisture. A common industrial starting formulation for an unfilled ABS compound targeting V-0 at 1.5 mm is brominated epoxy oligomer at 12–16 wt%, antimony trioxide at 4–6 wt%, and a phosphite-phenolic stabilizer at 0.1–0.3 wt%; however, the exact loading must be optimized for ABS313HL because the grade’s melt flow and rubber content influence both flame-retardant distribution and impact retention. The extruder barrel is profiled from 170 °C at the feed zone to 200–220 °C at the die, with melt temperature kept below 230 °C to avoid premature release of bromine species; screw speed is set between 300 rpm and 500 rpm on 32–45 mm diameter machines. Pelletized compound is re-dried at 80 °C for 2 h before injection molding into enclosure halves, cooling-fan frames, and power-supply housings. The finished enclosure is evaluated according to UL 94 vertical burn at the specified thickness and IEC 62368-1 clause 4.7 fire enclosure requirements; long-term heat aging is monitored under UL 746B where heat-aging indices are required by the end-user. Antimony trioxide is classified under EU CLP as H351; compounding lines must include local exhaust ventilation and the finished compound must be checked against the end-user’s regulatory list before export. Because ABS313HL is supplied as a general-purpose ABS injection grade, the compounding site must confirm that the selected flame-retardant package does not reduce Charpy notched impact below the mechanical design threshold; a formulation that achieves V-0 but falls below 8 kJ/m² at 23 °C may be unsuitable for snap-fit enclosure bosses. Published data for this specific ABS313HL formulation is limited, and optimum loading must be confirmed by UL 94 vertical burn tests on production-tool plaques.

    Downstream segmentRelevant standardTypical acceptance conditionPlant verification instrument
    Automotive interior trimISO 179-1/1eA, ISO 527-2, VDA 277Charpy notched at 23 °C ≥ 15 kJ/m², tensile yield 35–45 MPa, VOC below OEM capInstrumented pendulum impact tester, universal tensile tester, headspace GC/FID
    ElectroplatingASTM B727-04(2019), ASTM B533-85(2019)Adhesion peel above customer minimum after thermal cyclingPeel tester with 25 mm wide specimens, thermal shock chamber
    Thin-wall electronicsIEC 62368-1, UL 94UL 94 HB at 3.0 mm for unfilled or V-0 for FR compound; no distortion at 70 °CUL 94 flame chamber, IEC 62368-1 heat conditioning oven
    Flame-retardant compoundUL 94, IEC 62368-1, UL 746BV-0 at 1.5 mm compound, heat-aging index according to relayVertical flame chamber, oxygen index tester, aging oven

    Drainage Fittings Molded from ABS313HL Demand Low-Temperature Ductility Verification

    DWV fittings injection-molded from ABS313HL are processed at the lower bound of the melt-temperature window to minimize oxidative degradation during long hot-runner residence times in multi-cavity tools. Melt temperature is maintained at 215–230 °C for fittings with wall sections of 3–6 mm, while mold temperature is kept at 30–50 °C to permit a controlled freeze-off layer; higher mold temperatures can extend cooling time beyond 35 s per cycle in thick spigot sections and increase cycle cost. A desiccant dryer maintains residual moisture below 0.05% at 80 °C, because moisture above 0.10% produces splay and reduces hydrostatic burst resistance. Regrind from sprues and rejected fittings is reintroduced at 15–20 wt% only after screening, dedusting, and classifying to remove fines smaller than 0.5 mm; higher regrind fractions narrow the notched impact margin and raise the risk of brittle failure at pipe joints. The finished fittings—sanitary tees, 45° elbows, P-traps, and cleanout caps—are tested against ASTM D2661 for drainage waste and vent performance and NSF/ANSI 14 where plumbing code listing is required. Hydrostatic pressure testing and impact after water absorption are performed on lot samples because ABS drainage fittings must resist occasional mechanical contact during installation at temperatures down to 5 °C. The practical limit of ABS313HL in this application is not melt flow but low-temperature ductility; validation should use ISO 179-1/1eA at 0 °C and -20 °C, not only at 23 °C.

    When ABS313HL Is Used as the Base Resin in ABS/PMMA Coextruded Profiles

    Coextruded ABS/PMMA profiles use ABS313HL only as the inner high-flow tie layer, not as the exposed capstock, because the melt strength required for profile die stability under 1–2 m/s haul-off is supplied by a high-molecular-weight PMMA or a low-flow ABS layer, while ABS313HL contributes deep-draw thermoforming flow into bathtub edge profiles, appliance fascia extrusions, and point-of-sale rail profiles after the coextruded sheet is vacuum-formed at 150–175 °C; compliance for profile dimensional stability is checked under ISO 306 Vicat softening temperature and tensile properties under ISO 527-2, and the production line must verify that ABS313HL lot-to-lot MVR under ISO 1133-1:2022 does not exceed the die-swell tolerance of the downstream calibration tool.

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    Certification & Compliance
    More Introduction

    Guangdong YinXi ABS ABS313HL is an acrylonitrile-butadiene-styrene terpolymer positioned as a high-flow injection moulding grade within the manufacturer’s ABS313 series. The suffix combination is understood in industrial resin nomenclature as indicating high-lubricity/high-flow rheology, although the exact formulation difference is not disclosed in a public bilingual datasheet. Published data for this specific configuration is limited; therefore, class-typical ranges are used in this document and must be confirmed against lot-specific certificates of analysis before tooling release or part qualification.

    What Are the Core Specifications and Which Test Protocols Apply?

    ABS grades in this flow class are characterized by melt rheology under ISO 1133-1:2022, tensile properties under ISO 527-2:2012, flexural modulus under ISO 178:2019, notched impact under ISO 180:2023, and thermal deformation under ISO 75-2:2013 or ISO 306:2022. Table 1 compares the typical envelope for ABS-HL injection moulding grades with general-purpose ABS. The values are not lot-specific certificate values for ABS313HL.

    Property Test protocol ABS-HL class expected for ABS313HL General-purpose ABS comparison
    Melt flow rate ISO 1133-1:2022, 220 °C/10 kg 25–40 g/10 min 10–20 g/10 min
    Tensile yield stress ISO 527-2:2012 40–46 MPa 42–48 MPa
    Tensile modulus ISO 527-2:2012 2100–2400 MPa 2100–2500 MPa
    Flexural modulus ISO 178:2019 2200–2500 MPa 2000–2400 MPa
    Izod notched impact, 23 °C ISO 180:2023 14–25 kJ/m² 20–32 kJ/m²
    Vicat softening temperature B50 ISO 306:2022 92–98 °C 96–102 °C
    HDT at 1.8 MPa ISO 75-2:2013 82–88 °C 86–92 °C
    Density ISO 1183-1:2019 1.04–1.06 g/cm³ 1.04–1.06 g/cm³

    The melt flow rate is the principal differentiation marker. ABS-HL grades in the expected ABS313HL window fall between 25 g/10 min and 40 g/10 min at 220 °C under 10 kg load. This viscosity reduction is generally achieved through molecular weight adjustment, lubricant package modification, or both. It does not automatically preserve notched Izod impact; a shift from standard-flow ABS to a high-flow grade can lower 23 °C Izod impact by 15% to 30% at equivalent rubber content.

    Capillary rheometry under ISO 11443:2021 for ABS-HL class materials at 220 °C typically records an apparent shear viscosity of 80 Pa·s to 120 Pa·s at 1000 s⁻¹, compared with 150 Pa·s to 250 Pa·s for standard-flow ABS at the same shear rate. This viscosity differential increases at lower shear rates and narrows at high shear rates; therefore, thin-wall filling benefits are most visible in shear-thinning regions near gates and runners.

    Pre-drying of ABS313HL is a non-negotiable stage before injection moulding. The polymer phase is hygroscopic to the extent that surface moisture above 0.08% by mass produces splay, jetting, and loss of impact resistance at the gate. A desiccant dryer with a dew point of -20 °C or lower is used, with inlet air temperature set at 80 °C for 2 h to 4 h. The dried resin should be fed through a closed hopper to maintain moisture below 0.05% as measured by ISO 15512:2019. Moisture above 0.05% can reduce tensile yield stress by 3% to 5% and notched Izod impact by 10% to 15% through secondary reactions in the rubber phase.

    On a 120-ton hydraulic injection moulding machine equipped with a 20:1 L/D general-purpose screw, ABS-HL grades process best when the melt temperature is maintained between 220 °C and 250 °C. Barrel profile from rear to nozzle is typically 200 °C, 220 °C, 230 °C, 240 °C, and 240 °C; the hot runner or nozzle is set at 235 °C to 245 °C. Residence time above 250 °C should be limited to 5 min or less because polybutadiene rubber-phase oxidation and chain scission accelerate, causing yellowing, black specks, and a drop in notched Izod impact exceeding 20% in thin-wall parts. Thermal degradation of ABS313HL is dominated by polybutadiene-phase oxidation rather than SAN matrix chain scission alone. At melt temperatures above 250 °C, discoloration and reduced impact are observed before significant molecular weight loss of the SAN phase occurs. Thermogravimetric analysis of ABS under nitrogen shows mass loss beginning near 350 °C, but this is not a processing temperature; it defines purge and shutdown limits. During extended downtime, the barrel should be purged with a thermally stable polymer such as high-density polyethylene, and screw temperatures reduced to 180 °C to avoid stagnation degradation.

    Processing variable ABS-HL class window Control limit / observed failure
    Pre-drying 80 °C, 2–4 h, desiccant dryer Moisture above 0.08% causes splay, jetting, weld-line weakness
    Melt temperature 220–250 °C Above 250 °C or residence above 5 min accelerates rubber degradation
    Mould temperature 40–80 °C Below 30 °C increases frozen-in stress and gloss variation
    Injection pressure 70–120 MPa hydraulic Higher values indicate gate freeze or undersized runner
    Screw geometry L/D 20:1–24:1, compression ratio 2.0:1–2.5:1 High-compression screws may over-shear, causing black specks
    Nozzle Open nozzle or reverse-taper shutoff Dead spots cause black specks and brown streaks
    Back pressure 0.5–2.0 MPa Excessive back pressure raises melt temperature and degrades rubber

    Back pressure is normally held at 0.5 MPa to 2.0 MPa. Excessive back pressure raises melt temperature through shear heating, which increases the probability of rubber-phase degradation. Screw recovery speed should be set so that recovery is completed before the cooling time expires, without exceeding a screw surface speed of 0.3 m/s in low-viscosity ABS-HL melt. Gate and runner dimensions should be adjusted only after fill studies. Typical gate land length is 0.5 mm to 1.0 mm, and cold runner diameter should be at least 2.5 mm for unfilled ABS-HL, depending on part weight. Direct gates on thin-wall covers often require a gate diameter of 0.8 mm to 1.2 mm; smaller gates freeze before packing is complete, producing sink marks and poor dimensional stability.

    When Thin-Wall Mould Filling Replaces Standard Flow Requirements

    The primary justification for selecting ABS313HL over standard ABS313 is the filling of parts with nominal wall thickness below 1.2 mm or with flow-length-to-thickness ratios above 120:1. Spiral-flow testing according to ASTM D3123-09 on ABS-HL grades commonly shows flow lengths of 700 mm to 900 mm at 1.5 mm thickness and 220 °C melt temperature, but comparable published data for this specific grade is limited. Injection speed must be raised to 120 mm/s to 200 mm/s at the screw, depending on part geometry; slow injection in thin sections causes hesitation marks and weld-line weakness.

    On production lines, thin-wall ABS-HL parts exhibit lower orientation stress than standard ABS at the same injection pressure. However, this advantage is lost when the mould temperature falls below 30 °C; frozen-in stress increases, and post-mould shrinkage measured after 24 h at 23 °C can vary by more than 0.2% between near-gate and end-of-fill regions, causing warpage in flat covers. Valve-gated hot runner systems are preferred for ABS-HL to prevent drool; open hot runners may exhibit gate stringing due to low melt viscosity.

    High-Flow Rheology Does Not Automatically Preserve Impact Performance

    A common substitution error is to replace a standard ABS grade with ABS313HL in a part exposed to 0 °C or lower temperatures. The high-flow modification can reduce low-temperature notched Izod impact by 15% to 30% because the rubber-phase particle size distribution and molecular weight distribution are tuned for viscosity rather than energy absorption. Parts must be revalidated by ISO 180:2023 at the intended operating temperature; the 23 °C value alone is not sufficient. For machine guarding or power-tool housings that must sustain multiple-impact events, a medium-flow ABS or ABS/PC alloy may be more appropriate. If the application requires low-temperature ductility below -20 °C, ABS313HL should not be selected without instrumented puncture testing or Charpy impact data specific to the lot.

    Comparison with ABS313 Standard Flow and ABS/PC Alloy Grades

    For thin-wall parts, ABS313HL provides a measurable processing advantage over ABS313 standard flow: lower melt viscosity reduces injection pressure by 10% to 25% in comparable tooling, shortens fill time, and permits greater cavitation on the same clamp force. The trade-off appears in impact and thermal stability. ABS/PC alloys can deliver notched Izod impact at 23 °C of 35 kJ/m² to 60 kJ/m² and heat deflection temperatures above 100 °C, but they require higher melt temperatures and are more sensitive to moisture and mould release chemistry. ABS313HL remains easier to process for unfilled thin-wall enclosures where thermal load is below 80 °C and impact exposure is limited to ambient-temperature impact without retained notch.

    Unfilled ABS resins in this class are typically classified as HB under UL 94, not V-0. Flame-retardant versions require halogenated additives, intumescent phosphorus systems, or bromine-antimony synergists that alter flow, impact, and colour stability. For electrical enclosures, glow-wire ignition temperature measured according to IEC 60695-2-11:2021 and comparative tracking index per IEC 60112:2020 must be evaluated on the final compound. The base ABS313HL grade should not be inferred to carry UL Recognized Component status without the manufacturer’s UL Yellow Card, and compliance under REACH and RoHS 2011/65/EU must be established from lot-specific documentation because colour masterbatches and external lubricants are not captured by generic ABS data.

    Chemical resistance of ABS313HL follows the same solvent sensitivity profile as general-purpose ABS. Immersion tests under ISO 175:2010 show significant attack by ketones, esters, aromatic hydrocarbons, and chlorinated solvents, with stress cracking more likely when moulded-in stress is high. Aqueous acids, alkalis, and aliphatic hydrocarbons are tolerated in short immersion periods. For appliance housings exposed to cleaning agents such as isopropanol or quaternary ammonium disinfectants, compatibility testing must be conducted on the actual part because moulded-in stress and flow orientation dominate environmental stress cracking. External lubricants used in high-flow ABS can migrate and alter paint adhesion or ultrasonic welding performance.

    Because ABS313HL is a commercial resin supplied with lot-level variation, final process validation should be based on the manufacturer’s certificate of analysis, which reports melt flow rate, tensile properties, Izod impact, Vicat softening temperature, and moisture level. Incoming resin should be inspected for pellet colour consistency and foreign matter. If regrind is used, the ratio should not exceed 20% by mass in thin-wall applications unless the manufacturer’s technical support has validated higher levels; regrind reduces melt viscosity slightly and may lower notched Izod impact by 5% to 10% per reuse cycle. Published data for this specific configuration is limited; process windows should therefore be tested on the intended mould with the actual lot, not transferred directly from generic ABS processing guides.

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