Products

Yuyao Weier ABS 603AB-45

    • Product Name: Yuyao Weier ABS 603AB-45
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 598068
    Product Name Yuyao Weier ABS 603AB-45
    Manufacturer Yuyao Weier
    Material Type ABS (Acrylonitrile Butadiene Styrene)
    Grade 603AB-45
    Density 1.05 g/cm³
    Melt Flow Rate 220 C 10 Kg 45 g/10 min
    Tensile Strength 45 MPa
    Elongation At Break 20%
    Flexural Modulus 2200 MPa
    Flexural Strength 70 MPa
    Notched Izod Impact Strength 15 kJ/m²
    Heat Deflection Temperature 1 82 Mpa 85 °C
    Vicat Softening Temperature 95 °C
    Rockwell Hardness 105 R
    Molding Shrinkage 0.4-0.6%
    Water Absorption 0.3%
    Flammability Rating UL94 HB
    Processing Method Injection molding
    Form Pellets

    As an accredited Yuyao Weier ABS 603AB-45 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing
    Shipping
    Storage
    Free Quote

    Competitive Yuyao Weier ABS 603AB-45 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

    Yuyao Weier ABS 603AB-45 is a pelletized acrylonitrile-butadiene-styrene copolymer supplied for injection molding and, where melt strength permits, profile extrusion. The manufacturer’s designation places the grade within the ABS 603AB family; the “45” suffix is a producer-specific marker and is not an ISO melt-flow-rate codification. Because no globally recognized public database publishes the certified property sheet for this exact formulation, the following statements distinguish between class-level ABS behavior and product-specific requirements. Lot-specific property values must be read from the certificate of analysis or the producer’s technical data sheet. Generic ABS grades of this type are designated under ISO 2580-1:2003, and test specimen preparation falls under ISO 2580-2:2003. Melt flow is reported under ISO 1133-1:2022 at a condition selected by the producer; common ABS conditions include 220 °C with 10.0 kg or 230 °C with 3.8 kg. Density is determined by ISO 1183-1:2019 method A. Tensile modulus, yield stress, and strain at break are determined by ISO 527-2:2012 using type 1A specimens at 50 mm/min. Flexural strength and modulus are determined by ISO 178:2019 at 2 mm/min. Notched Charpy impact is determined by ISO 179-1:2010/1eA; Izod impact is determined by ISO 180. Because the exact rubber phase content, SAN molecular weight, lubricant package, and antioxidant formulation are proprietary to the manufacturer, no numerical value for the 603AB-45 product should be inferred from class averages.

    Material Designation and Regulatory Baseline

    The material is a styrenic copolymer containing a dispersed polybutadiene rubber phase in a styrene-acrylonitrile matrix. The morphology combines rigid-phase hardness and processing ease with elastomer-phase impact absorption. That structure does not by itself confer regulatory approval. Under RoHS 2011/65/EU, including Annex II amendments from (EU) 2015/863, the ten restricted substances—lead, mercury, cadmium, hexavalent chromium, polybrominated biphenyls, polybrominated diphenyl ethers, and four specific phthalates—must remain below maximum concentration values in homogeneous materials. A producer declaration or IEC 62321 series test report is the typical enforcement document. Under REACH Regulation (EC) No 1907/2006, the supplier must communicate SVHC presence above 0.1 wt% in articles under Article 33. Food-contact use is not implicit: FDA 21 CFR 177.1020 applies to certain styrene-acrylonitrile copolymers, but a grade-specific migration study for monomers and processing aids is required before use in contact with food. For medical housings, ISO 10993-1 biocompatibility is not a property of the polymer alone; sterilization method, colorant package, and molding aids influence the assessment.

    Compliance verification matrix for 603AB-45 when specified for electronic or industrial goods.
    Verification pointStandard or methodDocumentation basis
    Material designationISO 2580-1:2003Producer data sheet block code
    Test specimen preparationISO 2580-2:2003Lot certificate of analysis or producer internal specification
    Melt mass-flow rateISO 1133-1:2022Producer-specified condition and die size
    DensityISO 1183-1:2019Method A immersion at 23 °C
    Tensile propertiesISO 527-2:2012Type 1A specimen, 50 mm/min
    Notched impactISO 179-1:2010/1eA or ISO 180Certificate of analysis at 23 °C and -30 °C where applicable
    FlammabilityUL 94 or IEC 60695-11-10Final part thickness; generic resin test is not transferable
    Recycling markingISO 11469:2016Molded-in >ABS< per part geometry

    Before melt processing, pellet moisture content must be verified. ABS and rubber-bearing blends are moisture-sensitive enough to produce visible splay and reduced mechanical performance when moisture exceeds a critical threshold. A desiccant dryer with a dew point of -40 °C to -30 °C and a drying temperature of 80 °C for 2–4 h is the standard start-up condition for ABS-class materials. Hopper residence should be limited to avoid overdrying; temperatures above 90 °C for more than 6 h can cause pellet surface tack and feed-throat bridging. Dried resin should be conveyed in closed tubing. Storage at relative humidity above 60% should be assumed to require predrying unless hopper sensors record stable humidity. Hopper capacity should be matched to the number of machine barrel volumes consumed within the dried-resin shelf life of approximately 2 h from dryer discharge.

    Thermal exposure during melt processing is the primary process conflict. The polybutadiene phase undergoes thermo-oxidative degradation and can generate yellowing, black specks, plate-out on mold vents, and a measurable reduction in notched impact before the SAN matrix shows gross surface defects. Barrel settings from 200 °C to 240 °C, nozzle settings from 220 °C to 250 °C, and mold temperatures from 40 °C to 80 °C establish the initial window for many ABS grades. If melt temperature exceeds 260 °C or cumulative residence time exceeds 5 min, degradation byproducts may adhere to vents and alter part surface quality. Screw speed above 70 rpm and backpressure above 10 bar increase frictional heating and should be evaluated by melt-temperature measurement rather than barrel setpoint alone. A capillary rheometer equipped with a die of L/D 30:1 can detect lot-to-lot viscosity changes and degradation at 240 °C and 250 °C. On a production injection molding machine, the screw should not run excessively after reaching shot size; a cushion of 3–8 mm and a recovery time shorter than cooling time are common control targets.

    When Wall Thickness Falls Below 1.2 mm in Electrical Housings

    Thin-wall electrical enclosures impose high shear, fast injection, and early freeze-off. For these parts, melt-flow path and ductility must be validated at the actual cavity thickness; a generic 3.2 mm data-sheet specimen will not represent a 1.0 mm flow path. The molding trial should include short shots to map the flow front from 60% to 95% fill volume. Injection pressure of 100–140 MPa and hold pressure at 60–80% of peak injection pressure may be necessary, depending on part length-to-thickness ratio. Clamp force for a thin-wall tool is commonly assessed at 3–5 kN/cm² of projected area, but molded-part stress, flash, and breathing must be confirmed on the specific press. A mold temperature of 80 °C often improves flow length and surface gloss in ABS but increases cooling time. If the conversion uses a hot runner, the runner thermal profile should be checked for dead spots at 260 °C or above. Published data for the thin-wall electrical-housing performance of 603AB-45 is limited; class-level ABS design values cannot be used to certify creep, impact, or dielectric performance.

    Potential application areas for a controlled-viscosity ABS of this class include low-voltage switchgear covers, business machine housings, domestic appliance bezels, automotive interior trim clips, and point-of-sale terminal enclosures. The resin may also be considered for painted or coated parts if adhesion testing is performed on the final molded substrate. Solvent-based paints can interact with the polybutadiene phase and cause stress cracking, so a paint adhesion and embrittlement protocol under ISO 2409 or ISO 16276-2 is advised. For plated parts, the producer must confirm etchability; otherwise, a plating-grade ABS should be specified. If UL 94 V-0 at 1.5 mm is required, a designated flame-retardant grade is necessary unless the producer documents flame-retardant performance for 603AB-45.

    What Distinguishes the 603AB Series from General-Purpose ABS Molding Grades?

    The ABS family includes general-purpose injection molding grades, high-gloss grades, electroplating grades, high-heat grades, flame-retardant grades, and controlled-viscosity variants. Without the producer’s certificate of analysis, the 603AB-45 designation cannot be assigned to one of these subclasses. Differentiation from another ABS product should be performed through a comparative test matrix: melt flow rate under identical ISO 1133-1:2022 conditions; notched Charpy impact at 23 °C and -30 °C; tensile yield stress and modulus by ISO 527-2:2012; and dynamic viscosity at 220–250 °C over shear rates from 100 to 10,000 s⁻¹. If the product is claimed to replace a plating-grade ABS, the evaluation must include chromic acid etch adhesion, electroless copper deposition, and surface roughness development; matching melt flow alone is insufficient. If the product is claimed to offer lower emissions for automotive interiors, the relevant test is VDA 278 or ISO 12219-1 depending on the target market. Published data for the specific 603AB-45 configuration in these comparative protocols is limited; third-party testing is required to demonstrate equivalence.

    Processing Reference Limits for Drying and Melt-Delivery Equipment

    Reference limits for ABS-class drying and injection-molding processing; producer lot-specific settings may vary.
    ParameterReference rangeEquipment or measurement basis
    Pellet moisture after drying0.05 wt% maximumKarl Fischer or moisture analyzer, desiccant dryer with dew point -40 °C to -30 °C
    Predrying temperature80 °C for 2–4 hTray or hopper dryer with closed conveyance
    Barrel temperature profile200 °C to 240 °CThree-zone general-purpose screw, compression ratio 2.5:1 to 3.0:1
    Nozzle/melt temperature220 °C to 250 °CMelt pyrometer or nozzle probe
    Mold temperature40 °C to 80 °CTurbulent-water thermolator
    Backpressure3–7 barHydraulic injection unit
    Screw rotation30–70 rpmGeneral-purpose 20:1–22:1 L/D screw
    Cushion3–8 mmInject position and screw recovery control
    Critical residence limit5 min maximum at melt above 240 °CShot-to-barrel-capacity ratio and cycle time

    The processing window is not a single setpoint but a tolerance band that depends on molecular weight and additive package. If the lot contains a lower-viscosity grade, the lower barrel temperatures and backpressure should be used. If the lot contains a higher-viscosity grade, molding may require a more aggressive screw-recovery profile, but the degradation limit should not be crossed. Production-line variation in drying hopper airflow and mold-water line scale can shift the practical window by 5–10 °C; a process-capability study should track melt temperature, fill time, and part weight to detect drift.

    Splay, silver streaking, or surface delamination in molded parts generally indicates moisture, trapped gas, or degradation. The response sequence is to verify dryer dew point and airflow, lower barrel temperatures in 5 °C steps, and inspect the screw and non-return valve for degraded material. If splay persists after drying and temperature reduction, a general-purpose styrene-based purge compound with a similar melt-flow index can be used. Flow marks near the gate may be caused by jetting; increasing gate size or reducing injection velocity may convert the flow front to a laminar fill. If the part is a heat-resistant or electrical housing, reprocessed material content should be agreed with the molder. General ABS grades retain a practical regrind proportion of 10–20 wt%, but the specific 603AB-45 allowance must be stated by the producer because rubber-phase degradation can lower impact retention.

    For applications exposed to ultraviolet radiation or elevated service temperatures, long-term performance should be tested on the formulated product. ISO 4892-2 xenon-arc exposure with daylight filters and a black-standard temperature of 65 °C is a common accelerated weathering method for plastics. ABS resins without high levels of UV stabilization can show gloss loss, chalking, and embrittlement within a few thousand hours; the presence of carbon black or a light-stable pigment system may improve this behavior. Long-term heat aging at 85 °C or 95 °C in air can be evaluated by tracking notched impact retention and surface oxidation. Published data for the specific outdoor weathering or long-term thermal aging performance of Yuyao Weier ABS 603AB-45 is limited; the end user should not extrapolate from a general ABS weathering curve.

    Top