Products

SABIC ABS MG47N

    VTB
    Specifications
    HS Code 901538
    Density 1.04 g/cm³
    Melt Mass Flow Rate 6.0 g/10 min (220°C/10 kg)
    Molding Shrinkage 0.50-0.70 %
    Tensile Strength At Yield 42 MPa
    Tensile Elongation At Break 20 %
    Flexural Modulus 2200 MPa
    Flexural Strength 65 MPa
    Notched Izod Impact Strength At 23 C 200 J/m
    Heat Deflection Temperature At 0 45 Mpa 90 °C
    Heat Deflection Temperature At 1 8 Mpa 80 °C
    Vicat Softening Temperature 96 °C
    Rockwell Hardness R105
    Ul94 Flammability Rating HB

    As an accredited SABIC ABS MG47N factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing SABIC ABS MG47N is supplied in 25 kg moisture-proof, polyethylene-lined paper bags, palletized for industrial handling and storage.
    Container Loading (20′ FCL) SABIC ABS MG47N resin packed in 25 kg bags, palletized and loaded into a clean, dry 20′ FCL container for export.
    Shipping SABIC ABS MG47N (acrylonitrile-butadiene-styrene copolymer) ships as non-hazardous solid resin pellets, not regulated for transport. Packed in moisture-proof bags or octabins, it should be kept dry, away from heat and direct sunlight, and handled as standard freight without puncturing packaging.
    Storage Store SABIC ABS MG47N indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, flames, and oxidizing agents. Keep in original sealed packaging on pallets to prevent moisture pickup, contamination, and deformation. Avoid prolonged high humidity/temperatures, follow manufacturer guidance, and use FIFO inventory rotation.
    Shelf Life Shelf life is 2 years when stored in original packaging at temperatures below 50°C, protected from moisture and direct sunlight.
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    Certification & Compliance
    More Introduction

    SABIC ABS MG47N is an amorphous acrylonitrile-butadiene-styrene injection-moulding grade positioned in the supplier’s high-flow general-purpose segment. The grade is specified for applications where melt fluidity, moderate notched impact, and dimensional stability are required in wall sections between 1.0 mm and 2.5 mm. Cavity-fill behaviour on hydraulic injection-moulding machines with clamp forces from 800 kN to 2,000 kN is differentiated from medium-flow ABS grades primarily by lower cavity-pressure demand at comparable notched Izod impact. Under ISO 1133-1:2022 at 220 °C with a 10 kg load, supplier literature places the melt volume-flow rate within the 20–28 cm³/10 min range. This flow range is approximately 1.5–2.5 times higher than many extrusion ABS grades, but the product is not a high-heat ABS and is not a high-impact ABS. The following sections define those boundaries and processing limits.

    What Distinguishes MG47N from High-Impact and High-Heat ABS Formulations?

    Relative to high-impact ABS, the main difference is a lower notched Izod impact plateau. High-impact ABS grades intended for interior automotive load-bearing parts frequently exhibit notched Izod values above 35 kJ/m² at 23 °C under ISO 180/1A, whereas MG47N is published in the 20–28 kJ/m² range. The reduction is a formulation trade-off intended to increase melt flow and shorten cycle time in multi-cavity tooling. Against high-heat ABS, MG47N is positioned at a Vicat B/120 of 96–101 °C under ISO 306 and an HDT/A at 1.8 MPa of 84–90 °C under ISO 75-2, while high-heat ABS grades commonly exceed 105 °C Vicat B/120 and 95 °C HDT/A. The grade therefore does not replace high-heat ABS in applications with continuous heat exposure above its thermal boundary without tooling thermal analysis and moulded-part validation.

    Against low-flow extrusion ABS grades, MG47N is distinguished by shear-thinning response at injection shear rates. Extrusion ABS with melt volume-flow rates near 8–15 cm³/10 min has higher molecular weight and higher melt strength, favouring sheet sag resistance and deep-draw thermoforming. MG47N is less suitable for those processes because retained melt strength is lower. The injection-grade advantage appears in thin-wall fill length below 1.0 mm wall thickness, where the higher flow rate reduces the pressure required to fill a fixed gate diameter. Published comparative data for this exact configuration is limited; however, capillary rheometry trends for unfilled ABS indicate that a shift from 10 cm³/10 min to 25 cm³/10 min MVR class can reduce spiral-flow pressure demand, although tool-specific validation is required.

    Melt Flow, Impact, and Thermal Property Benchmarks Under ISO Test Protocols

    A representative supplier-published property envelope is provided below. The values are not minimum or maximum specification limits and should be confirmed against the current certificate of analysis for the production lot.

    PropertyTypical rangeTest method
    Melt volume-flow rate, 220 °C, 10 kg20–28 cm³/10 minISO 1133-1:2022
    Density1.04 g/cm³ISO 1183-1
    Tensile stress at yield38–44 MPaISO 527-2/50
    Tensile strain at break10–25%ISO 527-2/50
    Flexural modulus1,900–2,300 MPaISO 178
    Flexural stress at yield55–65 MPaISO 178
    Notched Izod impact, 23 °C20–28 kJ/m²ISO 180/1A
    Notched Izod impact, −30 °C7–10 kJ/m²ISO 180/1A
    Vicat B/12096–101 °CISO 306
    Heat deflection temperature/Ae, 1.8 MPa84–90 °CISO 75-2
    Mould shrinkage, parallel/normal0.5–0.7%ISO 294-4

    The notched Izod value at −30 °C drops to 7–10 kJ/m², confirming that the ductile-to-brittle transition becomes significant below freezing. In sub-zero impact applications, MG47N is not a direct substitute for low-temperature ABS grades with additional impact modification. The flexural modulus of 1,900–2,300 MPa places it in the stiff unfilled ABS range, suitable for snap-fit geometries when the snap-beam strain is below the measured tensile yield strain.

    When Pre-Drying Is Insufficient in Humid Production Environments

    ABS does not undergo hydrolytic chain scission to the same extent as polyesters or polyamides, but pellet surface moisture vaporises during plasticating and causes splay marks, internal voids, silver streaking, and inconsistent shot weight. For MG47N, supplier processing literature recommends pre-drying in a dehumidifying dryer at 80 ± 5 °C for 2–4 h to reduce pellet moisture below 0.10 wt%. When ambient relative humidity exceeds 60%, or when regrind with high surface area is introduced, drying time should be extended to the upper limit or the hopper should be purged with dry air at a dew point of −30 °C or lower. The <0.10% moisture threshold is especially critical in hot-runner tools with small gate diameters, where moisture vapour is superheated during shear and visibly disrupts the part surface.

    Melt residence time is a critical control variable because the polybutadiene phase degrades through oxidation and crosslinking at elevated temperature. The supplier-defined melt window is 230–260 °C. Operation above 260 °C for more than 5 min residence time increases discolouration, free-rubber agglomeration, and notched Izod loss. Screw recovery should be set so that material does not remain in the barrel across more than 2–3 shots during interruption. In hot-runner systems, the manifold temperature should not exceed 250 °C, and gate temperature balance should be maintained within ±5 °C to avoid premature freeze-off in thin-wall sections.

    Processing parameterRecommended rangeCondition or equipment type
    Pre-drying time2–4 hDehumidifying dryer, 80 ± 5 °C
    Target moisture content<0.10 wt%Karl Fischer or loss-on-drying
    Melt temperature230–260 °CInjection barrel, front/middle/rear zones
    Mould temperature25–80 °CHigher range for gloss and lower residual stress
    Injection velocity50–150 mm/sWall sections below 1.5 mm
    Hold pressure40–70 MPaHydraulic pressure, adjusted to gate freeze
    Back pressure0.5–1.5 MPaHydraulic, to maintain melt homogeneity
    Screw speed30–80 min⁻¹30 mm general-purpose screw, L/D 20–22
    Maximum melt residence time<5 minAt melt temperature above 260 °C
    Hot-runner manifold temperature≤250 °CBalanced within ±5 °C

    Because the processing window is narrowest at the upper melt-temperature boundary, production monitoring should record actual melt temperature, hold-pressure integral, and screw-recovery time. When cycle interruptions exceed the maximum residence time, purging with a general-purpose ABS purge compound is required before restarting.

    Solvent Contact, UV Exposure, and Electroplating Boundaries

    Unmodified ABS is susceptible to stress crazing in ketones, esters, chlorinated solvents, and aromatic hydrocarbons. MG47N should not be specified for components in contact with methanol, acetone, methyl ethyl ketone, toluene, or trichloroethylene unless chemical compatibility is validated under ISO 22088 environmental stress-cracking methods at the service temperature and strain state of the part. For indoor appliance surfaces, the material is suitable when moulded with adequate venting and gate design. For outdoor UV-facing components, unpainted ABS undergoes photo-oxidative embrittlement and gloss loss. QUV accelerated weathering under ISO 4892-2 can produce visible colour shift and surface microcracking within 500–1,000 h; therefore, MG47N is not recommended for durable exterior unpainted parts without a protective capstock, paint, or UV-stabilizer masterbatch.

    Electroplating operations can use general-purpose ABS grades because the rubber phase is etched by chromic acid to form anchor sites for electroless nickel or copper. MG47N can be electroplated if etch bath temperature, agitation, and dwell time are adjusted to the grade’s rubber morphology; however, published data for this exact electroplated configuration is limited. Regulatory documentation from the supplier typically confirms compliance with EU RoHS Directive 2011/65/EU and REACH Regulation (EC) No 1907/2006, but a lot-specific certificate should be obtained for production release. No food-contact claim under FDA 21 CFR or EU 10/2011 is implied unless explicitly stated in a supplier compliance letter.

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