| HS Code | 157619 |
| Flammability Rating | UL94 V-0 |
| Molding Shrinkage Percent | 0.4-0.6 |
| Processing Method | injection molding |
| Form | pellets |
As an accredited Guangzhou Kingfa Science & Technology ABS RS-830 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Guangzhou Kingfa Science & Technology ABS RS-830 is supplied in 25 kg paper bags, 40 bags per pallet (1,000 kg net). |
| Container Loading (20′ FCL) | 20′ FCL loaded with Guangzhou Kingfa ABS RS-830 in 25 kg bags, palletized, shrink-wrapped, and secured for ocean transport. |
| Shipping | Guangzhou Kingfa Science & Technology ABS RS-830 is a non-hazardous ABS resin, normally shipped as general cargo in dry, ventilated containers or covered trucks. Keep packages closed and away from moisture, heat, sunlight, and ignition sources; no special dangerous-goods classification is expected. Verify the current SDS and local regulations before shipment. |
| Storage | Store Guangzhou Kingfa ABS RS-830 in a cool, dry, well-ventilated warehouse, protected from direct sunlight, heat, flames, and moisture. Keep original bags or containers tightly closed, clean, and palletized; avoid crushing, tearing, and dust generation. Maintain good housekeeping and static control. Segregate from oxidizers, acids, alkalis, and solvents. Follow the SDS, observe shelf-life, and use first-in/first-out stock rotation. |
| Shelf Life | Shelf life is typically 12 months when stored in original, unopened packaging under dry, cool conditions away from direct sunlight. |
For electroplated ABS components based on Kingfa Science & Technology ABS RS-830, the first processing stage is not moulding but selective oxidation of the dispersed polybutadiene phase in a chromic acid–sulphuric acid etch bath. Production-scale ABS rack-plating lines typically maintain the etch solution at 350–420 g/L chromic acid and 180–250 mL/L sulphuric acid at 65–70°C for 5–15 min, depending on the moulding’s orientation and butadiene particle size distribution. Moulding parameters for plate-ready parts are constrained by the need to minimise frozen-in stress: melt temperature should be held at 230–250°C and mould temperature at 60–80°C, because lower mould temperatures and excessive shear create etch non-uniformity, micro-pitting, and premature plating peel. After rinsing and neutralisation, the etched surface is activated in a colloidal palladium-tin bath at 20–30°C for 1–3 min, then covered with electroless nickel to 1–5 µm as measured coulometrically per ISO 2177. Thermal-cycle adhesion is checked per ASTM B553, commonly with three cycles from -40°C to 90°C and a pass criterion of no blistering or loss of adhesion. The coefficient of linear thermal expansion mismatch between ABS and the electroplated metal layer, approximately 70–100 × 10⁻⁶ K⁻¹ for ABS versus 10–20 × 10⁻⁶ K⁻¹ for the metallic layer, is the underlying driver for this test. Users must verify that the specific lot of RS-830 is designated for electroplating; if Kingfa’s published grade documentation does not list plating-adhesion data, a full plating trial is required before series production.
| Electroplating stage | Control range | Verification or standard |
|---|---|---|
| Chromium-sulphuric acid etch | 65–70°C, 5–15 min, 350–420 g/L CrO₃, 180–250 mL/L H₂SO₄ | Visual surface inspection at 50× |
| Palladium-tin activation | 20–30°C, 1–3 min | Electroless copper strike surface conductivity |
| Electroless nickel thickness | 1–5 µm | ISO 2177 |
| Thermal-cycle adhesion | -40°C to 90°C, 3 cycles | ASTM B553 |
Thin-wall enclosures for routers, audio peripherals, and display bezels impose a narrow processing envelope in which melt viscosity, gate freeze-off, and venting interact to set the maximum flow length. A lot-specific melt-flow rate should be obtained per ISO 1133-1:2022 at 220°C and 10 kg; the value is a quality-control index rather than a direct predictor of flow in a 1.0–1.6 mm wall. If capillary rheometry data for RS-830 is not published, process validation should begin with short-shot studies on the production tool rather than extrapolating from a melt-flow value. On a 1,000–1,500 kN clamp injection machine, a 1.2 mm thick enclosure with a flow path of 150–200 mm may show filling pressures between 80–120 MPa at a melt temperature near 240°C; lowering melt temperature by 10°C can increase pressure demand by 10–15% while reducing yellowing. Shear rate in sub-runner and gate regions should remain below 50,000 s⁻¹ for unfilled ABS to avoid chain scission and surface blush. Weld lines formed at opposing melt fronts reduce local tensile strength to 60–80% of the parent value measured on a 3.2 mm specimen per ASTM D638-14. The practical lower melt-temperature limit is set by injection-pressure spikes and short shot, while the upper limit is set by volatile evolution above 260°C; the resulting window is narrower than general-purpose ABS literature often implies.
Pre-drying is mandatory at 80°C for 2–4 h in a desiccant dryer with a dew point below -30°C; residual moisture above 0.1% produces silver streaks at the flow front. A hot runner manifold should be held at 230–250°C with total residence time no longer than 6 min. Venting is a critical downstream bottleneck: land widths below 0.02 mm and vent depths of 0.015–0.025 mm at the last-filled areas prevent air traps, because inadequate venting in thin-wall ABS appears as burn marks at end-of-fill and ejection issues. Gate geometry should avoid sharp transitions; edge gates or sub-gates with land length 0.5–1.0 mm and diameter 0.8–1.5 mm are typical, but simulation of shear heating is required to avoid gate blush.
| Process variable | Injection moulding envelope for unfilled ABS | Instrument or reference method |
|---|---|---|
| Drying temperature | 80°C | Desiccant dryer, dew point below -30°C |
| Drying time | 2–4 h | For initial moisture up to 0.3% |
| Residual moisture | below 0.1% | Gravimetric moisture balance |
| Melt temperature | 210–250°C | Nozzle melt pyrometer |
| Mould temperature | 40–80°C | Mould surface thermocouple |
| Hot runner manifold temperature | 230–250°C | Manifold thermocouple |
| Maximum melt residence time | 6 min | Shot weight × cycle time calculation |
In domestic appliance housings, control-panel carriers and internal structural brackets moulded from ABS RS-830 must pass repeated thermal and mechanical load cycling under safety standards such as IEC 60335-1. The material should be predried to 0.1% moisture or less before plastication; a closed-loop desiccant dryer set at 80°C for 2–4 h is standard for cold, unopened containers. Barrel temperatures from feed throat to nozzle are often profiled at 210°C, 220°C, 230°C, and 235°C for medium-flow ABS; injection speed is adjusted to fill 70–90% of cavity volume before transfer to holding pressure. Cavity pressure in sections with nominal wall 2.0–3.0 mm should be maintained at 30–50 MPa during packing, and gate freeze-off is confirmed by stabilised part mass rather than by timer alone. Heat deflection temperature is measured on 3.2 mm specimens under 1.82 MPa flexural stress per ASTM D648-16; this value is not a continuous-use limit. ABS RS-830 should not be used under sustained structural load above 70°C without creep data. For washing-machine control panels, drop-test impact at 23°C and -10°C should be evaluated on production tooling, because gate vestige and weld-line location dominate failure; standard Izod values from edge-gated test bars per ISO 180/A do not capture those tooling effects. Contact with amine-catalysed polyurethane foam systems, commonly used in refrigerator insulation, can cause environmental stress cracking on stressed ABS surfaces; this is a known incompatibility for unfilled ABS and must be addressed through barrier tapes or separate sealing profiles. Glow-wire testing per IEC 60695-2-11 at 550°C or 650°C may be required depending on carrier accessibility and current; ABS RS-830 in its general-purpose form is not inherently flame-retarded, so if a flame-retardant variant is supplied, that grade-specific data and additive loading must be confirmed.
Repeated heat histories from regrinding sprues, runners, and rejected parts alter the melt viscosity and colour stability of ABS RS-830 in non-cosmetic support brackets, mounting rails, and internal chassis. Plant-scale gravimetric dosing of 10–20 wt% clean in-house regrind is often acceptable when the regrind is sieved through a 4 mm screen and stored in sealed containers at 10–30% RH; higher regrind percentages can shift low-shear viscosity enough to change fill patterns and sink mark severity. Moisture management is more difficult for regrind because of increased surface area; open storage at 60% RH can raise moisture content to 0.3–0.5% within 48 h, requiring drying at 80°C for 4 h rather than the 2 h minimum that may suffice for compact virgin pellets. Impact strength of the blend is assessed on notched specimens per ISO 179-1/1eA:2023; when the regrind fraction exceeds 15 wt%, fractured test bars may show a transition from ductile yielding to brittle crack initiation at room temperature, although the exact threshold depends on the number of prior heat cycles. Yellowness index is measured per ASTM E313-20 under D65 illuminant; a ΔYI above 2.0 units after three heat histories can be detectable on light-colour or unpigmented parts, limiting regrind use to dark or hidden components. The plastication process must avoid stagnant melt zones in the check-ring clearance and hot-runner dead spots, which are sources of black specks and viscosity heterogeneity that cannot be corrected by downstream sorting.
On injection moulding machines processing regrind blends, screw compression ratio should remain in the low range of 2.0:1 to 2.5:1, and shear heating should be limited to a melt-temperature rise below 10°C between feed and nozzle. Lot-to-lot variation in virgin RS-830 and regrind particle size is a common cause of packing-pressure drift, so cushion position and transfer pressure should be monitored from shot to shot rather than adjusted only at setup. If the grade’s published certificate of analysis does not include regrind-ratio property retention, the values given here are to be treated as process-screening ranges from general unfilled ABS practice rather than lot-specific guarantees.
Because painted ABS RS-830 parts for exterior or semi-exterior use require a UV-stable topcoat, the moulded substrate and the coating system must be treated as a single failure mechanism rather than separate material properties. Unpainted ABS undergoes photodegradation, chalking, and loss of surface gloss under sunlight, so the substrate is cleaned with deionized water and dried at 50–60°C before a two-component acrylic or polyurethane primer is applied at 10–20 µm dry film thickness. Cross-cut adhesion testing per ISO 2409:2023 should achieve classification 0 or 1 on production-painted surfaces, with results evaluated on both flat areas and gate-adjacent regions where moulded-in stress is highest. Xenon arc weathering per ISO 4892-2:2013 using daylight filters at 0.35 W/m² at 340 nm and black-panel temperature 65°C is a common screening method; exposure of 2,000–3,000 h may be specified for automotive exterior painted ABS systems, but published data for this specific RS-830 configuration may be limited, and comparative testing on production parts is required. Solvent-based topcoat formulations containing toluene, xylene, or ketones can attack ABS moulded surfaces before the primer has fully cured; the incompatibility appears as microcracks and adhesion loss at high-stress points. Excessive melt temperature above 250°C or long residence time can generate carbonyl groups at the surface, which affect paint adhesion and long-term UV stability.
Moulded-in stress in painted ABS components should be checked before coating, because residual stress accelerates paint microcracking under paint-shop solvent exposure and thermal cycling. Higher mould temperature, lower injection speed near the end of fill, and generous rib radii reduce residual stress but may increase cycle time; none of these changes is detectable by standard tensile testing alone. If the paint supplier’s adhesion data for ABS RS-830 is absent, a pilot run with the exact production tool and painting line is the only reliable qualification path.
At 240°C melt temperature and 60°C mould temperature, injection-moulded plaques of ABS RS-830 retain measurable weld-line anisotropy that cannot be inferred from standard single-gate test specimens. Tensile specimens cut parallel and perpendicular to flow in a 2 mm plaque show different yield stress and elongation; the parallel-to-flow direction usually retains higher orientation, while the transverse direction fails earlier, and this difference is measurable per ISO 527-2:2012 with type 1A specimens. Weld-line tensile retention should be measured on a double-end-gated tensile bar, not inferred from a single melt-flow test; the reduction at the weld line is often 20–40% for unfilled ABS, but the exact value depends on melt temperature, fill speed, and gate distance. At 240°C melt temperature, the weld-line region may heal more completely than at 220°C because of increased molecular diffusion at the melt interface; however, higher temperature accelerates resin degradation and increases colour shift. The practical balance is a melt-temperature window of 230–250°C and a mould-temperature window of 40–80°C; higher mould temperatures improve weld-line knit strength but extend cycle time and may increase gloss variation on textured surfaces. Property values from standard plaques should be used only for quality assurance; part-level performance at weld lines must be tested on production tools with a falling-dart or tensile-pull fixture because gate position and part thickness dominate the local thermal history.
A mould-temperature differential of 5–10°C between core and cavity can shift the neutral axis and alter post-mould shrinkage, which in turn affects flatness and weld-line stress. Process capability studies should include at least 20 consecutive shots after steady state; short-shot studies and cavity-pressure sensors are more informative than laboratory test bars for weld-line validation. If specific weld-line retention data for Kingfa ABS RS-830 is not included in the published datasheet, only comparative in-house testing on the production tool is statistically meaningful.
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Guangzhou Kingfa Science & Technology ABS RS-830 is presented as a rigid amorphous acrylonitrile-butadiene-styrene terpolymer within the supplier’s designated ABS portfolio. The grade designation does not map directly to an ISO data block without consulting the supplier’s lot certificate. Published data for this specific configuration is limited; therefore, the property and process statements below are confined to class-level unfilled ABS behaviour referenced to ISO 2580-1:2002, ISO 1133-1:2022, ISO 527-2:2012, ISO 178:2019, ISO 179-1:2010, ISO 75-2:2013, and ASTM D638-14. No numerical value should be treated as an RS-830 specification unless confirmed by a dated certificate of analysis.
The grade name RS-830 is supplier-specific nomenclature. In commercial ABS slates, alphabetic prefixes often denote a flow class or end-use segment, while numeric suffixes separate impact, heat, or colour variants. However, no inference is made here because the manufacturer’s published technical datasheet for this specific configuration is not available in this document. Incoming inspection must use lot-specific release data.
| Property | Test method | Typical unfilled ABS class band |
|---|---|---|
| Density | ISO 1183-1:2019 | 1.03–1.07 g/cm³ |
| Melt volume-flow rate | ISO 1133-1:2022 220 °C, 10 kg | 5–40 cm³/10 min |
| Tensile yield stress | ISO 527-2:2012 | 40–52 MPa |
| Tensile modulus | ISO 527-2:2012 | 2100–2600 MPa |
| Flexural modulus | ISO 178:2019 | 2000–2800 MPa |
| Charpy notched impact, 23 °C | ISO 179-1:2010 | 10–30 kJ/m² |
| Heat deflection temperature, 1.8 MPa | ISO 75-2:2013 | 78–95 °C |
| Vicat softening temperature, B50 | ISO 306:2022 | 95–105 °C |
| Mould shrinkage | ISO 294-4:2018 | 0.4–0.7% |
| Moisture uptake, 23 °C, 50% RH | ISO 62:2008 | 0.2–0.3% |
The bands above are class-reference values drawn from ISO 2580-1 and general ABS technical literature. They are not RS-830 lot specifications and must not be used for tooling or part release without the supplier’s current certificate.
Within ABS grade slates, suppliers adjust three variables: melt volume-flow rate, notched impact strength, and heat resistance. A high-flow ABS typically exhibits melt volume-flow rate above 20 cm³/10 min at 220 °C/10 kg and reduced room-temperature Charpy notched impact relative to a high-impact grade. High-impact ABS grades often deliver Charpy notched impact values above 25 kJ/m² at 23 °C but sacrifice stiffness and flow. The RS-830 designation implies a specific position along this trade-off curve; the exact numerical position is supplier-controlled and must be read from the certificate of analysis.
The structural consequence of higher butadiene content is a two-phase morphology of rubber particles dispersed in a styrene-acrylonitrile copolymer matrix. This morphology influences crazing and shear yielding, which are the primary toughening mechanisms in ABS. As butadiene content increases, tensile stress at yield and flexural modulus decrease, while notched impact and paint adhesion may increase. These property shifts are measured by ISO 527-2:2012 and ISO 178:2019. A grade comparison therefore requires parallel evaluation of melt viscosity, mould shrinkage, and thermal distortion, not a single data point.
Moisture control is the first boundary condition. ABS resins absorb atmospheric moisture; at 23 °C and 50% RH, equilibrium moisture uptake for unfilled ABS can reach 0.2–0.3%. For injection moulding, residual moisture above 0.05% causes splay, surface clouding, and loss of impact. The resin should be dried in a desiccant dryer with dew point below −30 °C, hopper inlet air temperature 80–85 °C, and residence time 2–4 h. Drying for more than 8 h at elevated temperature is not recommended because prolonged heat exposure can yellow the polymer. These are class-level recommendations; the supplier’s drying curve for RS-830 may narrow the window.
Barrel zone settings for unfilled ABS are commonly arranged from 210 °C near the feed throat to 250 °C at the nozzle, with melt temperature measured by an air-shot pyrometer at 230–250 °C. If melt temperature exceeds 260 °C, thermal degradation of the butadiene phase accelerates, generating odour, yellowing, and reduced toughness. If melt temperature is below 210 °C, high viscosity produces uneven filling, gate freeze-off, and residual stress. On production-scale injection moulding machines, the screw should have a low-compression design with compression ratio 2.0–2.5:1 and L/D ratio 18–22:1; these values are typical for ABS and not RS-830-specific.
Back pressure of 0.3–0.7 MPa and screw surface speed 0.2–0.5 m/s are class reference points. Excessive shear heating from high back pressure may degrade the butadiene phase; too little back pressure may leave unmelted granules. Mould temperature is maintained between 40 °C and 80 °C. Lower mould temperatures improve cycle time but increase moulded-in stress; higher mould temperatures improve gloss and impact retention but lengthen cooling.
Injection velocity should be selected to avoid jetting and dark specks. Gate shear rate is a practical control variable; typical unfilled ABS moulding avoids prolonged shear rates above 50,000 s⁻¹ in thin gates. Hold pressure of 50–70% of peak injection pressure and hold time determined by gate-seal studies are used to control sink and warpage.
Tool design interacts with the amorphous structure of ABS. Wall-thickness transitions should not exceed 25% of the adjacent wall to avoid sink marks and voids. Gate dimensions for unfilled ABS are typically designed with land length 0.5–1.0 mm and gate diameter not less than 50% of wall thickness. Weld-line strength in unfilled ABS is often 60–80% of the base tensile strength, but weld-line performance for RS-830 must be evaluated on a moulded plaque before production. Mould shrinkage for unfilled ABS is typically 0.4–0.7% after 24 h, depending on wall thickness and mould temperature. Higher mould temperature increases shrinkage and reduces post-mould dimensional change. Measurement according to ISO 294-4:2018.
Substitution between ABS and high-impact polystyrene is a common cost-reduction exercise. HIPS has lower density, usually 1.03–1.06 g/cm³, but inferior heat resistance, chemical resistance, and notched impact. The heat deflection temperature of HIPS under 1.8 MPa is often 70–85 °C, while unfilled ABS class data range from 78 °C to 95 °C. ABS provides better resistance to oils, greases, and dilute acids, but it is more sensitive to ketones, esters, and aromatic hydrocarbons. If RS-830 is specified for an enclosure, the economic comparison must include density, mould cycle time, painting or plating requirement, and impact at sub-zero temperatures; the supplier’s certificate should be used for grade-specific values.
Compared with PC/ABS blends, unfilled ABS has a lower heat distortion temperature and lower low-temperature toughness. PC/ABS melts are processed at 260–280 °C and require drying at 100–110 °C. ABS processes at lower melt temperature and lower mould temperature, which reduces energy consumption and cycle time. The trade-off is reduced notched impact at −30 °C and lower maximum service temperature.
Heat-resistant ABS grades use alpha-methylstyrene or N-phenylmaleimide co-monomers to increase heat deflection temperature to 95–110 °C; flame-retardant ABS grades typically reduce melt-flow rate and tensile yield stress. If RS-830 is a general-purpose or high-gloss grade, these modified families are not direct drop-in replacements. Differences must be evaluated by thermal analysis and complete mechanical testing.
Potential application sectors for an unfilled ABS grade of this type are appliance housings, electrical enclosures, automotive interior trim, consumer electronics, small appliance bodies, vacuum cleaner housings, toys, and office equipment. The actual suitability of RS-830 for any application depends on the grade-specific datasheet, regulatory approvals, and end-use testing. Unfilled ABS is not recommended for external load-bearing parts exposed to direct sunlight without UV stabilisation, continuous hot-water contact above 70 °C, or solvents such as ketones and esters.
Regulatory boundary conditions for ABS RS-830 must be confirmed from the supplier’s current compliance certificate. Many unfilled ABS grades in the Kingfa portfolio are supplied as RoHS-compliant under Directive 2011/65/EU and REACH-compliant under EC 1907/2006, but such statements are product-grade-specific. UL yellow card data, when applicable, is published by the supplier under a specific file number and should not be inferred from similar grades. If flame-retardant performance is required, RS-830 should be compared with the supplier’s FR ABS grades, which contain halogenated or phosphorus-based systems and may exhibit lower tensile strength and lower flow than unfilled general-purpose ABS.
Grade verification should be performed on each lot. The certificate of analysis typically reports melt volume-flow rate, density, tensile properties, impact strength, and thermal properties according to ISO methods. Incoming inspection should include melt flow rate by ISO 1133-1:2022, density by ISO 1183-1:2019, and colour by spectrophotometer. Mechanical specimens should be injection-moulded under a defined mould temperature and conditioning protocol, typically 23 °C and 50% RH for at least 24 h before testing according to ISO 527-2:2012 or ISO 179-1:2010.
Lot-to-lot variability in compounded ABS can arise from rubber particle size distribution, graft ratio, and styrene-acrylonitrile copolymer molecular weight. These are not typically certified but affect impact and flow. For production-scale trouble-shooting, a two-lot comparison of capillary rheometry at 230 °C and 250 °C is more informative than a single melt-flow value.
| Check | Test method | Typical action basis |
|---|---|---|
| Moisture content | ISO 15512:2019 or Karl Fischer | Below 0.05% before moulding |
| Melt volume-flow rate | ISO 1133-1:2022 | Supplier specification window |
| Density | ISO 1183-1:2019 | Supplier specification window |
| Tensile yield stress | ISO 527-2:2012 | Supplier minimum value |
| Charpy notched impact | ISO 179-1:2010 | Supplier minimum value |
| Vicat softening temperature | ISO 306:2022 | Supplier minimum value |
| Visual appearance | Supplier inspection plan | No contamination, pellet size deviation, or foreign resin |
The action basis is derived from generic ABS practice. Lot-specific limits should be taken from the Guangzhou Kingfa Science & Technology certificate of analysis and raw-material inspection plan.
Thermal degradation failure modes in ABS are progressive. The butadiene phase begins to oxidize at elevated melt temperatures, causing yellowing, reduced impact, and generation of volatile decomposition products. Splay or silver streaks on the part surface can be mistaken for moisture but are often thermal degradation if the melt temperature exceeds 260 °C or if residence time exceeds 10–15 min at typical processing temperatures. The failure can be confirmed by differential scanning calorimetry or by lower injection speed trials. If black specks appear, the barrel or hot runner may have dead spots; purging with a commercial ABS purging compound is required.
Dimensional variation may arise from irregular packing if the melt viscosity changes due to degradation or if the check ring leaks. Regular check-ring seal testing on the injection unit is part of process capability control. Mould-filling variation between lots can also appear if pellet bulk density differs, altering feed-screw conveying and plasticating stability. Published data for this specific configuration is limited; production trials should establish the residence time and temperature boundary for RS-830 on the target machine.