| HS Code | 871903 |
| Density | 1.05 g/cm³ |
| Melt Mass Flow Rate Mfr 220 C 10 Kg | 8 g/10 min |
| Tensile Strength | 45 MPa |
| Elongation At Break | 20% |
| Flexural Strength | 70 MPa |
| Flexural Modulus | 2200 MPa |
| Notched Izod Impact Strength | 16 kJ/m² |
| Heat Deflection Temperature Hdt 1 82 Mpa | 95 °C |
| Vicat Softening Temperature | 101 °C |
| Molding Shrinkage | 0.4–0.6% |
| Flammability Ul 94 | HB |
| Rockwell Hardness | 100 R |
As an accredited Qingdao Haier New Material ABS HR-1016 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Qingdao Haier New Material ABS HR-1016 is supplied in 25 kg moisture-proof paper sacks, palletized and stretch-wrapped for industrial shipment. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Qingdao Haier New Material ABS HR-1016, securely stowed and sealed for export shipment. |
| Shipping | Qingdao Haier New Material ABS HR-1016 is typically shipped as non-hazardous thermoplastic resin pellets in 25 kg moisture-barrier bags on pallets. Use covered, dry containers or trucks; avoid heat, sunlight, moisture, and sharp impact. No special dangerous-goods handling is required. Store cool and ventilated, keep packaging sealed, and follow local transport regulations. |
| Storage | Store Qingdao Haier New Material ABS HR-1016 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, flames, and moisture. Keep original packaging tightly sealed and protect from physical damage and contamination. Separate from strong oxidizers, acids, and solvents. Maintain clean handling areas, avoid dust/static accumulation, and follow first-in, first-out stock rotation. Use appropriate PPE and local regulations. |
| Shelf Life | Shelf life is typically 12 months when stored cool, dry, and well-ventilated in original unopened packaging, away from direct sunlight. |
Pre-dried ABS HR-1016 pellets entering a reciprocating screw injection unit should show residual moisture content not exceeding 0.05 % by ISO 15512:2019 Method B. Desiccant-bed dryers are set at 80 °C with a supply-air dew point no higher than -30 °C for a residence time of 2 h when ambient relative humidity is below 60 %; above 60 % RH or after winter warehouse storage, the residence time is extended to 4 h and dry-air flow rate is adjusted to maintain 0.9 m/s through the hopper bed. Melt temperature measured at the nozzle by immersion probe should be maintained between 230 °C and 250 °C; barrel zones from feed to metering are profiled 210/220/230/235 °C, with the nozzle set 5 °C below the metering zone to reduce drool and stringing. Mould surface temperature for refrigerator door end-caps and freezer drawer fronts is held at 40–60 °C; below 35 °C, pronounced flow lines propagate from the gate, while above 65 °C, cycle-time increase and post-ejection dimensional drift become measurable on 450 mm span parts. The grade-specific lot certificate governs where it differs from the general unmodified ABS processing ranges given in this section.
For a 2.4 mm nominal wall, hydraulic packing pressure is set between 40 MPa and 70 MPa, with hold time 0.3–0.5 s per millimetre of wall after gate freeze. Screw rotation speed should not exceed 80 min⁻¹ on a 35 mm diameter screw, corresponding to a circumferential screw speed near 55 m/min; higher rates induce frictional discolouration in the butadiene phase. Injection speed for large-area appliance covers is limited to 150–300 mm/s; sequential valve-gate systems with 4 drops are preferred over single edge gates to minimise knit lines around dispenser openings. When polished cavity steel is used for high-gloss surfaces, gate land length is increased to 0.8–1.2 mm and cold slug wells sized at 1.2 times the runner diameter are placed at each runner branch. Production-scale failure observations include gate blush at injection speeds above 350 mm/s, silver streaking from wet regrind or excessive screw compression ratio, and part warp exceeding 0.8 mm across a 450 mm span when cooling time is reduced below 15 s. Tensile yield stress should be checked on first-article samples per ASTM D638-14, notched Izod impact per ASTM D256-10(2018), and melt mass-flow rate per ISO 1133-1:2022; the gate region typically shows 8–15 % lower impact than the far-field due to molecular orientation. Dry in-plant regrind from sprues and runners may be reintroduced at a ratio no higher than 20 wt% after 3 mm screening and magnetic separation, because higher fractions lower weld-line impact and increase silver streak incidence. End products in this track include washing machine dispenser housings, refrigerator door end-caps, freezer drawer fronts, and air-conditioner control panel frames. Compliance is assessed under IEC 60335-1 clause 30 for resistance to heat and fire, and the substrate is expected to meet UL 94 HB at 1.5 mm when tested according to IEC 60695-11-10. REACH Regulation (EC) No 1907/2006 Annex XVII and RoHS Directive 2011/65/EU Annex II apply to homogeneous-material limits for lead, cadmium, mercury, hexavalent chromium, PBB and PBDE.
For network router and set-top box lower shells with nominal wall thickness of 1.2–1.8 mm, the main process conflict lies between fill speed and surface gloss. Unmodified ABS HR-1016 is processed at the upper end of its melt temperature range to lower viscosity, but nozzle temperature above 250 °C accelerates thermo-oxidative degradation of the polybutadiene phase, producing yellowing and a notched Izod impact loss greater than 15 % after 20 min residence time. A practical melt-temperature limit is 240 °C, with hot-runner manifold set at 235 °C and nozzle tip temperature 245 °C. Injection speed is set at 180–280 mm/s; if flow length exceeds 180 mm from a single gate, the cavity should be rebalanced by changing to a fan gate with land length 0.6–0.8 mm or by adding a second gate, because end-of-fill cavity pressure below 35 MPa produces visible weld lines and micro-sink at rib intersections. Hydraulic packing pressure is limited to 50–80 MPa and hold time to 0.2–0.4 s per millimetre of wall; overpacking thin walls above 1.2 mm induces in-plane compressive stress that leads to delayed warpage after 48 h ambient storage. For a 1.4 mm wall, cooling time is generally 8–12 s with mould temperature 30–50 °C, but lowering mould temperature below 30 °C increases internal stress and solvent susceptibility in secondary painting. To maintain surface gloss above 85 GU at 60° incidence measured by ISO 2813:2014, cavity inserts should be polished to SPI A2 finish and parting-line venting depth should be no more than 0.02 mm; deeper vents allow flash, shallower vents trap air and produce diesel-effect burn marks at end of fill. The flame classification must not be assumed for thin-wall parts; a general-purpose unmodified ABS typically achieves UL 94 HB at 1.5 mm, but V-2 or better requires a flame-retardant ABS and must be assessed according to IEC 60695-11-10 on the actual thickness and colour. Electrical-safety enclosures assessed to IEC 62368-1:2023 require comparative tracking index and flame rating appropriate to the potential ignition source; if HR-1016 is supplied without a flame-retardant package, it is limited to low-current, low-voltage internal enclosures or non-primary enclosures. End products include network router lower shells, IoT gateway chassis, set-top box bottom covers, and Ethernet switch faceplates, where dimensional stability is checked after 24 h at 60 °C using a fixture gauge rather than free-standing measurement. Published data for HR-1016 in 0.8 mm wall sections is limited; mould-flow simulation should be calibrated with a spiral-flow test at 230 °C and 800 bar injection pressure before tool release.
| Test method | Thin-wall network enclosure requirement | Large-area appliance cover requirement |
|---|---|---|
| ISO 527-2/1A/50 tensile yield stress | ≥ 38 MPa on 1.2 mm sections | ≥ 35 MPa on 2.4 mm sections |
| ISO 180/1A notched Izod at 23 °C | ≥ 14 kJ/m² after 24 h at 60 °C | ≥ 18 kJ/m² after 48 h at 40 °C and 60 % RH |
| ISO 306:2022 VST/B50 | ≥ 88 °C | ≥ 90 °C |
| IEC 60695-11-10 UL 94 at 1.5 mm | HB minimum | HB minimum |
In double-insulated rotary hammer motor cradle components, ABS HR-1016 is restricted to tool sections where the surface temperature remains below 65 °C during 240 min continuous operation. Typical applications are clamshell handle halves, motor cradle frames, gearbox isolation covers, and orbital sander dust ports, where the material is not in direct contact with gear grease or battery electrolyte. For a 2.0–2.8 mm nominal wall, screw bosses are designed with outside diameter 2 times the thread-rolling screw major diameter, and rib root thickness is held at 0.5–0.6 times the nominal wall to avoid sink marks. Moulded-in brass inserts should be preheated to 80 °C and inserted with a tolerance of 0.05 mm radial interference; cold inserts create residual tensile stress that later produces radial cracking at bosses under impact loading. Melt temperature is set between 230 °C and 240 °C, mould temperature at 40 °C, and hydraulic injection pressure between 100 MPa and 160 MPa. The process should use a screw with compression ratio 2.2:1 to 2.8:1 and length/diameter ratio 20:1 to 24:1; higher compression generates excessive shear heating in the butadiene phase and reduces notched impact. First-article notched Izod impact per ISO 180/1A should be checked at 23 °C and after 72 h at 70 °C; values below 12 kJ/m² in the gate region indicate excessive melt residence or moisture degradation. Environmental stress cracking is controlled by restricting production cleaning agents to isopropanol; ester-based or ketone-based cleaners, aromatic hydrocarbons, and strong alkaline solutions attack the polybutadiene phase and produce microcracking at screw bosses. Dry regrind ratio is limited to 15 wt% for visible tool housings because higher fractions increase gloss variation and impact scatter. Compliance is assessed under IEC 62841-1 for hand-held motor-operated electric tools, particularly creepage distances and mechanical strength after drop testing; the material is not a substitute for flame-retardant grades where a V-2 or better classification is required. End products include rotary hammer clamshell housings, angle grinder handle shells, orbital sander dust ports, and battery pack top covers only when the cell compartment is separated by a flame-retardant barrier.
Because gate-area delamination and weld-line strength loss occur with polyolefin-carrier masterbatches, appliance front-panel moulding with ABS HR-1016 uses an ABS-based masterbatch. Masterbatch is metered at a let-down ratio of 25:1, equivalent to 4.0 wt%, for dark high-gloss panels; for off-white and light-grey panels, a let-down of 50:1 (2.0 wt%) is used only when the masterbatch pigment loading is above 50 % and the injection unit is equipped with a static mixer of 6 elements. Below 2.0 wt%, lot-to-lot colour drift frequently exceeds ΔE*ab 0.8 under D65/10° observer compared against ISO 11664-4:2008. Tumble blending time is 15–20 min at 20 min⁻¹; longer blending at higher speed builds static charge on pellet surfaces and causes pigment segregation during hopper draw. Static mixing elements are placed between screw tip and nozzle, with pressure drop of 3–8 MPa at 240 °C; below 3 MPa, dispersion is insufficient and pigment agglomerates appear as dark specks under 10× inspection. The injection screw should be a general-purpose ABS screw with compression ratio 2.2:1 to 2.8:1 and L/D of 20:1 to 24:1; a high-shear mixing screw is not used because it overheats the polybutadiene phase and shifts the base resin colour. Melt temperature is controlled at 235–245 °C, mould temperature at 45–60 °C, and hydraulic packing pressure at 55–75 MPa to reproduce grained or polished front-panel surfaces without streaking. Injection speed for front panels is set between 120 mm/s and 220 mm/s, and screw-back pressure is maintained at 5 bar to 10 bar; excessive backpressure raises melt temperature and yellows the panel edge. In-line colour measurements are taken on a grained surface after 2 h of stable cycling, because initial shots contain purge contamination. Compliance for coloured appliance panels includes heavy-metal restrictions under RoHS Directive 2011/65/EU Annex II and REACH Regulation (EC) No 1907/2006 Annex XVII; pigment suppliers must provide declarations for cadmium, lead, hexavalent chromium, and mercury in the masterbatch. End products include refrigerator panel frames, washing machine control panels, air-conditioner front panels, and dishwasher fascia components.
Where lower B-pillar trim, seat side shields, and seatbelt retractor covers are specified without post-moulding annealing, automotive interior moulding with ABS HR-1016 is confined to low-load areas below 70 °C in normal use. The governing flammability test is FMVSS 302, equivalently ISO 3795, with a horizontal burning rate limit of 100 mm/min on specimens 100 mm long and 13 mm wide cut from the thinnest grained section; many OEM interior specifications tighten this limit to 80 mm/min. For unmodified ABS at wall thickness below 1.8 mm, first-article flammability testing is mandatory because the burning rate is thickness-dependent and surface grain depth may accelerate flame propagation. The tool should position the gate in a non-visible lower edge to allow packing pressure of 60–80 MPa and hold time 0.4 s/mm without gate blush on visible grain. Melt temperature is held at 235–245 °C, mould temperature at 50–70 °C to improve knit-line strength and reproduce grain depth 0.5–1.0 mm; lower mould temperatures create gloss difference across the grained area and increase residual stress. Injection speed is limited to 100–180 mm/s for grained surfaces; higher speeds cause grain micro-tearing at the base of grain peaks and produce a whitish appearance. Regrind ratio is limited to 15 wt% because higher recycled content raises residual styrene and acrylonitrile release and increases visible flow lines. Published data for ABS HR-1016 under automotive low-emission protocols is limited; VDA 278:2011 thermodesorption screening should be run on first-article parts, with special attention to styrene, acrylonitrile, toluene, and ethylbenzene, and the result compared with the OEM volatile organic compound and fogging limits. GADSL screening is performed on the safety data sheet and supplier declaration, not on the moulded part alone; any reportable substance above 0.1 wt% must be disclosed through the IMDS. EU ELV Directive 2000/53/EC Annex II restricts lead, cadmium, mercury, and hexavalent chromium in homogeneous materials, with cadmium below 0.01 wt% and the others below 0.1 wt%. End products include lower B-pillar trim, seat side shields, seatbelt retractor covers, and steering column lower shrouds, provided that post-moulding annealing is not required; if a moulder anneals parts at 80 °C for 2 h, the resulting dimensional change exceeds the typical clip-position tolerance of ±0.3 mm and creates squeak-and-rattle risk in the interior system.
| Regulation / standard | Requirement | HR-1016 application note |
|---|---|---|
| FMVSS 302 / ISO 3795 | burning rate ≤ 100 mm/min | verify on thinnest grained section and after weathering |
| EU ELV Directive 2000/53/EC Annex II | Cd ≤ 0.01 wt%, Pb/Hg/Cr⁶⁺ ≤ 0.1 wt% | require lot certificate and IMDS entry |
| REACH Regulation (EC) No 1907/2006 Annex XVII | substance restrictions apply by national deviation | confirm with downstream automotive OEM |
| GADSL | declarable substances only | supplier SDS screening before production |
| VDA 278:2011 | VOC/SVOC release limits per OEM | first-article parts from production tooling, not lab plaques |
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Qingdao Haier New Material ABS HR-1016 is supplied as a pelletized acrylonitrile-butadiene-styrene terpolymer produced by Qingdao Haier New Material Co., Ltd. The grade is positioned in the injection-molding ABS category, but the producer’s published datasheet for HR-1016 is not reproduced in this technical note. Where grade-specific values are unavailable, the engineering data below refer to class-typical medium-flow ABS behavior and are identified as such. The material consists of a continuous styrene-acrylonitrile copolymer matrix with a dispersed butadiene-based rubber phase. Grafted SAN chains at the rubber-matrix interface contribute to interfacial adhesion, impact energy absorption, and melt stability. The balance among rubber content, SAN molecular weight, grafting density, and rubber particle size determines the difference between general-purpose, high-impact, heat-resistant, and high-flow ABS grades.
For HR-1016, the producer should be consulted for the certificate of analysis, lot-specific melt flow rate, impact strength, and thermal deformation values. The following sections provide processing thresholds, property envelope comparisons, and chemical compatibility boundaries that apply to medium-flow ABS injection-molding grades. They should not replace lot-specific validation on production tooling.
Pre-drying is mandatory for ABS HR-1016. A closed-loop desiccant dryer with a dew point below -40°C is required. Drying at 80°C for 2–4 h is standard for medium-flow ABS to reduce residual moisture below 0.05% by weight. At ambient relative humidity above 60%, moisture uptake accelerates, and hopper dryers with dew points above -20°C may fail to remove surface moisture and absorbed water. Moisture above 0.1% produces splay, silver streaks, weak weld lines, and an increased tendency toward delamination at the gate. The dried pellets should be conveyed with dry air and should not remain exposed to plant air for more than 15–30 min before entering the feed throat.
Melt temperature measured by a needle pyrometer should remain between 220°C and 250°C for standard medium-flow ABS. Above 260°C, the polybutadiene phase undergoes thermal-oxidative degradation, leading to yellowing, loss of impact strength, and generation of low-molecular-weight volatiles. During production interruptions, melt residence time above 240°C should not exceed 6 min. A barrel profile of rear 190–210°C, middle 210–230°C, front 220–240°C, and nozzle 220–250°C is common for medium-flow ABS, but the actual set points depend on screw geometry, shot size relative to barrel capacity, and screw speed.
Mold temperature is a critical boundary. Below 40°C, the frozen layer thickens, surface gloss declines, and flow length shortens. Above 80°C, cooling time increases, and ejection scuffing or sticking may occur. A mold temperature of 50–70°C is typically selected for appliance housings and interior trim. Hot runner systems require independent zone control with temperature variation held within ±2°C to avoid imbalance and shear heating in small gates.
On single-screw reciprocating injection machines, a general-purpose ABS screw with an L/D ratio of 20:1 to 25:1 and a compression ratio of 2.0:1 to 2.5:1 is used. The non-return valve should seal consistently, and screw surface speed should remain between 0.2 and 0.5 m/s. Screw speeds above 0.7 m/s can generate shear heating that raises the melt above 260°C at the screw tip. Back pressure of 0.5–1.5 MPa supports melt homogenization without excessive temperature rise. Injection pressure at the nozzle commonly falls between 60 and 120 MPa, depending on flow length, wall thickness, and gate size. Holding pressure is typically applied at 50–70% of peak injection pressure until gate freeze. A cushion of 2–5 mm should be maintained to provide consistent packing pressure.
Flow length to wall thickness ratio should be kept below 250:1 for thin-wall ABS parts. Below 1.2 mm wall thickness, short shots and gate jetting become more probable unless high injection speed, heated molds, and optimized gate geometry are used. Production failures recorded on ABS lines include gate blush, sink marks over bosses, jetting, and warpage from differential shrinkage. Unfilled ABS shrinkage is generally in the range of 0.4–0.7% according to ISO 294-4, but HR-1016-specific shrinkage must be obtained from the producer.
The intervals in Table 1 are class-typical values for medium-flow ABS injection-molding grades. They are preliminary design boundaries, not producer-certified HR-1016 data. Conformity to a specific lot should be established using the certificate of analysis and, where necessary, parallel testing under identical specimen preparation and test conditions.
| Property | Test standard | Unit | Typical envelope |
|---|---|---|---|
| Melt mass-flow rate at 220°C/10 kg | ISO 1133-1 | g/10 min | 15–30 |
| Density | ISO 1183-1 | g/cm³ | 1.04–1.07 |
| Tensile yield stress | ISO 527-2 | MPa | 40–50 |
| Flexural modulus | ISO 178 | MPa | 2100–2600 |
| Charpy notched impact strength at 23°C | ISO 179-1/1eA | kJ/m² | 15–30 |
| Vicat softening temperature, 50 N, 50°C/h | ISO 306/B50 | °C | 95–108 |
| Heat deflection temperature under 1.8 MPa | ISO 75-2/A | °C | 75–85 |
| Water absorption after 24 h immersion | ISO 62 | % | 0.2–0.4 |
| Molding shrinkage | ISO 294-4 | % | 0.4–0.7 |
| Rockwell hardness, R scale | ISO 2039-2 | R | 100–110 |
Differentiation from other ABS sub-classes must be confirmed by direct testing. High-flow ABS grades are produced by reducing SAN molecular weight or adding flow promoters; their melt mass-flow rate at 220°C/10 kg can reach 40–60 g/10 min, but tensile yield stress and impact strength are lower than those of medium-flow grades. High-impact ABS grades increase rubber content to around 20–25 wt% or use a wider rubber particle size distribution; Charpy notched impact can reach 30–50 kJ/m² at 23°C, while tensile modulus and melt flow decrease. Heat-resistant ABS grades incorporating alpha-methylstyrene or N-phenylmaleimide raise the Vicat softening point to 105–115°C, but require melt temperatures 10–20°C higher and exhibit reduced flow. Flame-retardant ABS grades containing brominated or phosphorus-based systems can achieve UL 94 V-0 at 1.5 mm or less, but they show higher density, narrower processing temperature windows, and lower melt stability. Published data for HR-1016-specific differentiation from these sub-classes are limited; parallel injection molding and mechanical testing remain the controlling comparison method.
ABS resins are susceptible to environmental stress cracking under residual molded-in stress in the presence of aromatic hydrocarbons, ester-based plasticizers, ketones, and certain chlorinated solvents. The stress cracking resistance of HR-1016 should be assessed under ISO 22088-1 or ISO 22088-2 using the actual service fluid and strain level. Ketones such as acetone and methyl ethyl ketone can soften the SAN matrix, while aromatic solvents can initiate crazing at stressed gate areas and weld lines. Contact with PVC gaskets containing migratory plasticizers can also cause surface microcracking over time. For applications requiring chemical resistance, the part should be annealed or redesigned to reduce tensile residual stress, and the producer should be asked whether the HR-1016 formulation has been modified for chemical resistance.
Regulatory compliance must be verified with the producer for the exact grade, colorant package, and production site. Typical documentation includes RoHS Directive 2011/65/EU conformance, including Delegated Directive 2015/863 for phthalates, and REACH Regulation 1907/2006 SVHC declarations. For food-contact applications, compliance with FDA 21 CFR 180.22 or EU Regulation 10/2011 must be established for the specific grade and processing history. Grade classification under GB/T 12672-2009 may be relevant for domestic Chinese ABS shipments, and the producer should confirm the designated designation and inspection lot requirements.
Typical downstream uses for medium-flow ABS grades include appliance control panels, refrigerator interior trim, vacuum cleaner housings, office equipment enclosures, and automotive interior components. In these applications, the molder should monitor batch-to-batch variation in melt flow rate and moisture content. A melt flow shift of 5–10% can alter fill pattern and packing behavior. Regrind addition up to 20 wt% is practiced for non-appearance parts; for glossy surfaces, regrind ratio should be reduced to avoid color shift and surface defects. Weld-line strength can decline by 30% or more when melt temperature falls below 210°C or mold temperature falls below 40°C. Gate locations should avoid impact-critical zones. Cavity pressure during packing for medium-flow ABS is commonly 30–50 MPa, and clamping force selection uses a first estimate of 0.4–0.7 t/cm² of total projected shot area. Published data for HR-1016-specific performance in these downstream configurations is limited; processor validation on production tooling remains the controlling step.