| HS Code | 456839 |
| Polymertype | Acrylonitrile-butadiene-styrene copolymer (ABS) |
| Appearance | Opaque thermoplastic pellets |
| Density | 1.05 g/cm³ (typical) |
| Meltflowrate | 2.5-3.0 g/10 min |
| Tensilestrength | 43-45 MPa |
| Elongationatbreak | 15-25% |
| Flexuralstrength | 65-70 MPa |
| Flexuralmodulus | 2000-2200 MPa |
| Notchedizodimpactstrength | 15-20 kJ/m² |
| Vicatsofteningtemperature | 95-100 °C |
| Heatdeflectiontemperature | 85-90 °C |
| Moldshrinkage | 0.4-0.7% |
| Rockwellhardness | 100-105 R scale |
| Processingmethod | Injection molding |
As an accredited PetroChina Daqing ABS 850 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packed in 25 kg moisture-resistant woven bags, PetroChina Daqing ABS 850 is palletized for safe industrial storage and transport. |
| Container Loading (20′ FCL) | PetroChina Daqing ABS 850 loaded in a 20′ FCL, palletized and shrink-wrapped, securely stowed for export ocean transport. |
| Shipping | PetroChina Daqing ABS 850 is shipped as non-hazardous acrylonitrile-butadiene-styrene copolymer resin, typically packed in 25 kg PP bags or jumbo bags. It is transported in dry containers as general cargo, kept dry, and protected from moisture, heat, and direct sunlight. |
| Storage | Store PetroChina Daqing ABS 850 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat sources, sparks, and open flames. Keep bags or containers tightly closed to prevent moisture and contamination. Avoid excessive stacking pressure that may deform pellets; use first-in, first-out stock rotation and maintain good housekeeping to limit dust and static. |
| Shelf Life | Typically 12 months from production when stored in a cool, dry, well-ventilated area away from direct sunlight and moisture. |
For lower-gloss automotive interior trim substrates such as door handle bezels, center console side panels and HVAC vent louvers, PetroChina Daqing ABS 850 is normally introduced into a single-screw injection molding machine with screw L/D ratio of 20:1–24:1 and compression ratio of 2.4:1–2.8:1 after dehumidifying-dryer treatment at 80–90°C for 2–4 h whenever ambient relative humidity exceeds 60%; residual moisture above 0.05% produces silver streaks and flow lines on textured grained surfaces. The melt temperature at the nozzle is held between 220°C and 250°C, while mold temperature is maintained at 40–80°C depending on wall thickness; parts with nominal wall thickness of 2.0–3.0 mm are preferred to avoid sink marks opposite bosses and ribs. At the dosing stage, regrind from sprue and runner systems is incorporated at 15–25 wt% after mechanical homogenization; higher regrind fractions above 30 wt% have been observed in production-scale runs to reduce notched Izod impact measured under ISO 180/1A by 10–15% and to shift surface gloss by more than 3–5 GU on grained surfaces, causing batch-to-batch visual mismatch. For emission-controlled interior parts, lot qualification under VDA 277 or ISO 12219-1:2021 is required; ABS 850 is not inherently low-volatile, so post-molding painting or soft-touch lamination must be validated for aldehyde and ketone release. Where unpigmented resin is used, a UV stabilizer masterbatch at 2–3 wt% is added to delay photodegradation of the butadiene phase on exposed upper instrument panel surfaces, but even stabilized ABS retains a boundary of 1,500–2,000 h in accelerated xenon-arc testing under ISO 4892-2 before gloss loss exceeds 20%. Finished components include door trim bezels, HVAC vent louver assemblies and seat side shields requiring matte grain retention and dimensional stability at 80°C continuous service.
In appliance control panel production, the principal dimensional risk is anisotropic post-mold shrinkage; ABS 850 follows the typical ABS range of 0.4–0.7% in flow direction and 0.5–0.8% transverse to flow, with values determined according to ISO 294-4. Tooling for washing machine control panels is cut with mold dimensions offset by 0.5–0.6% from cold part dimensions, but local shrinkage near ribs and bosses can exceed 0.9% when wall thickness drops below 1.5 mm. A side-edge fan gate or a sequential valve-gated hot runner with nozzle tip temperatures of 230–250°C is used to avoid visible weld lines across display windows, and the holding pressure is set between 60 MPa and 80 MPa hydraulic-specific pressure for a shot size above 50% of barrel capacity. Cavity surface temperature is held at 50–70°C to produce sufficient flow front advance while maintaining grain transfer from textured cavity surfaces. White appliance parts are pigmented with titanium dioxide masterbatch at 3–5 wt%; loadings above 5 wt% reduce melt flow and can generate gate blush on polished display window surrounds. For compliance with IEC 60335-1 clause 30.2.3, parts forming enclosures for unattended appliances are tested at glow-wire temperature of 650°C when wall thickness exceeds 0.75 mm; ABS 850 generally passes this lower glow-wire condition but is not suitable for 750°C or 850°C glow-wire categories without flame retardant modification. Terminal applications include control panel bezels, detergent dispenser housings and control knob bodies, where foil hot stamping requires surface hardness and low retained stress; post-molding annealing at 70–80°C for 1–2 h reduces stress cracking around metal inserts and threaded bosses.
Electronic enclosure designs utilizing PetroChina Daqing ABS 850 are generally restricted to internal or consumer devices where UL 94 HB classification is acceptable; the material has no inherent V-2 or V-0 performance, and adding halogenated flame retardants to this grade usually reduces practical impact strength and may violate RoHS Directive 2011/65/EU or in-house halide-free policies. For power tool housings, thin-wall laptop accessories and desktop printer enclosures, the processing window depends on wall thickness: 2.0 mm walls require melt temperatures at the upper end of 230–250°C, while 3.0 mm walls can run at 210–230°C to reduce thermal degradation. Multiple surface-mount bosses and snap-fit features require exact dimensional control; mold shrinkage under ISO 294-4 should be revalidated when regrind content exceeds 20 wt%, because polybutadiene phase degradation in regrind raises melt viscosity variability and can widen shrinkage by 0.1–0.2%. Production-scale observation of multi-cavity tools has shown that unbalanced runner layouts create cavity-to-cavity fill pressure differences of 5–10 MPa, producing intermittent shorts and gloss differences. To reduce this, runner diameters should not fall below 4 mm for cold runner systems, and gate thickness should be 0.6–0.8 mm for subgates feeding non-appearance areas. Compliance under IEC 62368-1:2023 for audio/video and information technology equipment demands that internal polymeric parts maintain mechanical integrity after pre-conditioning; if a declared end product is used in elevated ambient up to 35°C, creep resistance of ABS 850 under load should be checked by ISO 899-2 at 40°C and 15 MPa flexural stress to estimate deflections. Because published multi-cavity comparative shrinkage data for Daqing ABS 850 is limited, initial production trials should hold the lower boundary of the pressure range and adjust after dimensional capability studies. End components include printer chassis brackets, power tool motor housings and telecommunications equipment enclosures where impact resistance rather than flame retardancy governs material selection.
| Sector | Standard / method | Representative ABS 850 boundary | Verification requirement |
|---|---|---|---|
| Automotive interior | VDA 277; ISO 12219-1:2021 | Not inherently low-VOC; painted or coated lots require aldehyde/ketone release testing | Lot-specific emission test after decoration |
| Appliance enclosure | IEC 60335-1 clause 30.2.3 | Glow-wire 650°C pass at > 0.75 mm wall; not for 750°C or 850°C | End-product glow-wire test at thinnest wall |
| Electronics enclosure | UL 94 HB; IEC 62368-1:2023 | HB only; no inherent V-2/V-0 performance | Flame class and creep data per final design |
| Toys / children’s products | EN 71-3:2019+A1:2021; 16 CFR 1501 | Element migration under 0.07 mol/L HCl at 37°C for 2 h; no small-part failure | Colorant migration certificates and finished-part dimensional check |
| Luggage shells | ASTM D648-18; ISO 1518 | HDT at 1.82 MPa typically 90–100°C; not for continuous load above 80°C | HPTP lot-specific heat deflection and scratch test |
| Office equipment | IEC 62368-1:2023 | Fire enclosure only if wall thickness and end-use conditions are validated; base resin is UL 94 HB | End-product fire enclosure simulation or component test |
For toy housing compounds based on ABS 850, masterbatch and processing aids must be screened against EN 71-3:2019+A1:2021 migration limits for nineteen elements; ABS 850 itself contains no intentionally added heavy-metal stabilizers, but colorants must be selected from suppliers with migration certificates for the finished compound. The migration kinetics of residual colorant species are evaluated under 0.07 mol/L hydrochloric acid at 37°C for 2 h, and any batch exceeding the specified element release limits is rejected before molding. In injection molding of small toy vehicle bodies and building blocks, melt temperature is set at 220–240°C and mold temperature at 40–60°C to maintain acceptable cycle times between 25 s and 35 s for wall thicknesses of 1.5–2.5 mm. Gates must be positioned outside the primary tactile surface because EN 71-1 restricts sharp edges and protrusions; gate vestiges are typically trimmed and polished. Pigment masterbatch is used at 2–4 wt%, with soluble organic colorants avoided because they can migrate under saliva-simulant conditions and cause lot rejection. Mechanical strength of snap-fit joints in toy assemblies is validated by ISO 527-2 tensile testing and ISO 180/1A notched impact at 23°C; for small play items intended for children below 36 months, the U.S. 16 CFR 1501 small parts regulation additionally requires that the assembled unit must not fit through a 31.7 mm cylinder. ABS 850’s surface quality and processability make it suitable for opaque toy bodies where the end product is not subjected to prolonged outdoor UV exposure; for outdoor toys, UV-stabilized ABS or ASA should replace unmodified ABS 850 because the butadiene phase undergoes rapid loss of impact after 800–1,200 h of xenon-arc weathering under ISO 4892-2. Finished products include toy vehicle bodies, building block housings and handheld game shells requiring high-flow balance and notch resistance under repeated drop loading.
After pre-drying at 85–95°C for 3–4 h, sheet extrusion of ABS 850 for hard-side luggage shells begins with resin plastication in a single-screw extruder with 30:1–36:1 L/D and a barrier screw design; moisture in the sheet causes pinholes and bubble defects during subsequent thermoforming. The melt is delivered through a flat die with die gap of 0.8–1.2 mm for sheets of 1.5–3.0 mm final thickness, and melt temperature at the die entry is maintained at 200–230°C. Polished three-roll stack temperatures are set at 80–100°C to control shrinkage and surface gloss. In subsequent vacuum forming or pressure forming, sheet surface temperature is brought to 140–170°C; lower temperatures produce cracking in corner draw areas, while higher temperatures cause sagging and wall thinning below 0.5 mm on deep-draw luggage shells. Recycled trim from edge trim and rejected parts is incorporated at 20–30 wt% after cryogenic grinding; beyond 30 wt%, the butadiene rubber phase in regrind has been observed on industrial lines to reduce dart impact of formed shells by approximately 10–15% and increase variability in corner thickness. Compliance for luggage is frequently driven by airline handling and dimensional durability rather than chemical safety, but the finished shell must meet ISO 1518 scratch resistance tests and ASTM D648-18 heat deflection temperature; unreinforced ABS 850 typically exhibits HDT at 1.82 MPa in the range of 90–100°C, which is sufficient for short-term exposure in vehicle trunks but not for continuous loads above 80°C. Terminal products include hard-side suitcase shells, protective equipment cases and instrument carrying enclosures formed from coextruded or monolayer sheet.
For printer chassis and document handling components, ABS 850 can be employed where high-flow injection filling and moderate heat resistance are required; it is not a high-heat ABS and should not be selected for fuser frame components that operate above 85°C or for parts in direct contact with heated rollers. Molding of large flat chassis parts with ribs and bosses requires melt temperature 230–250°C, mold temperature 50–70°C, and holding pressure 70–90 MPa for shot weights within 70–80% of machine barrel capacity. The occurrence of sink marks opposite bosses is controlled by limiting rib-to-wall thickness ratio to 0.5–0.6:1 and boss-base wall thickness to 0.8:1 relative to nominal wall. Regrind levels for office equipment enclosures are typically maintained at 15–20 wt% after dust removal and magnetic separation; metal contamination from printer inserts must be kept below 0.1 wt% to avoid nozzle wear and black specks. The global safety standard IEC 60950-1 or its successor IEC 62368-1 may apply, and if the enclosure is used as a fire enclosure, the minimum wall thickness must be validated against the applicable standard; without flame retardant modification, ABS 850 only meets UL 94 HB. Dimensional stability of long chassis parts after ejection is improved by post-molding fixturing at 60–80°C for 30–60 min; this reduces warpage of parts longer than 300 mm from internal residual stress. Finished components include printer side panels, paper tray side frames and scanner housing bases where vibration damping and screw boss strength are primary requirements.
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PetroChina Daqing ABS 850 is a high-impact acrylonitrile-butadiene-styrene resin produced by Daqing Petrochemical Company, a subsidiary of PetroChina. The grade is positioned for sheet extrusion, thermoforming, and thick-section injection moulding. Distributor documentation places it in the low-melt-flow, high-impact ABS family, with a dispersed polybutadiene rubber phase grafted to a styrene-acrylonitrile matrix. The material is available as natural or batch-coloured pellets, and its mechanical response is governed by rubber-phase volume fraction, graft ratio, and SAN molecular weight distribution.
The consolidated property envelope in Table 1 follows ISO and IEC methods. Values should be confirmed against the current producer certificate of analysis because lot-to-lot shifts in rubber morphology can alter low-temperature impact by more than 10%.
| Property | Method | Representative range |
|---|---|---|
| Melt flow rate, 220°C/10 kg | ISO 1133-1:2022 | 5–8 g/10 min |
| Density | ISO 1183-1 | 1.04–1.06 g/cm³ |
| Tensile yield stress | ISO 527-1/-2 | 43–47 MPa |
| Tensile elongation at break | ISO 527-2 | 15–30% |
| Flexural modulus | ISO 178 | 2100–2500 MPa |
| Notched Izod impact, 23°C | ISO 180/1A | 30–45 kJ/m² |
| Vicat softening temperature, B50 | ISO 306 | 96–100°C |
| Rockwell hardness, R scale | ISO 2039-2 | 105–110 |
| Flammability class, 3.0 mm | IEC 60695-11-10 | HB |
The high impact is not obtained by merely increasing rubber content. The graft efficiency of SAN onto polybutadiene determines whether the rubber particles transmit stress through cavitation or debonding. In Daqing ABS 850, the notched Izod range of 30–45 kJ/m² at 23°C under ISO 180/1A is consistent with a rubber particle size distribution centred near 0.3–1.0 μm and a gel content sufficient to prevent particle coalescence during melt processing. Capillary rheometry at 220°C shows pronounced shear-thinning behaviour typical of ABS: apparent viscosity drops from approximately 1200 Pa·s at 100 s⁻¹ to 300 Pa·s at 1000 s⁻¹. The power-law index is near 0.3 over this interval. This strong shear-thinning allows filling of medium-flow injection tools despite the low ISO melt flow rate, while the extensional viscosity of the high-rubber phase remains high enough to stabilise sheet and parison formation.
On single-screw extruders with L/D ratios from 30:1 to 36:1 and barrier mixing sections, throughput is limited by melt temperature at the adapter and by moisture-driven splay rather than by screw torque. Pellets require drying at 80°C for 2–4 h to reduce moisture to below 0.05 wt%; post-drying moisture should be verified by ASTM D7191 or ISO 15512. Feed-throat dew point should remain below -30°C. Barrel temperatures from 190°C in the feed zone to 230°C in the metering zone keep the melt at 210–230°C. Above 250°C, the butadiene phase undergoes thermo-oxidative degradation, producing colour shift from natural to yellow and a measurable drop in melt strength. On a 90 mm single-screw line running 2.0 mm sheet, throughput is commonly observed in the 250–400 kg/h range when the roll stack is maintained at 70–85°C; published data for this specific configuration is limited.
Thick-wall injection moulding requires lower screw speed and back pressure than general-purpose grades to avoid shear heating. Mould temperatures between 30°C and 70°C are used; the upper end improves knit-line strength in parts with multi-gate geometry but increases cycle time. Injection pressures of 70–120 MPa are typical, and hold pressure should be adjusted until part mass stabilises because packing behaviour of the high-rubber grade differs from low-rubber injection ABS. Clamp force can be estimated from projected area at 0.4–0.6 tons/cm², but actual settings must follow part geometry and wall thickness. Process conflict occurs at high back pressure above 10–15 bar: plasticisation becomes more uniform, but shear heating can raise melt temperature 5–10°C above barrel set point. The operator must record melt temperature at the nozzle and reduce barrel set points accordingly. In extruders with residence times longer than 5 min, melt temperature should be kept below 240°C to avoid gel particles from crosslinked butadiene rubber.
In twin-sheet and single-sheet thermoforming, the material should be heated to a surface temperature of 140–170°C before forming. The high rubber content extends the elastic plateau, so sagging of the sheet across the clamp frame occurs earlier than with lower-impact grades. This requires higher vacuum or plug-assist actuation rates to avoid webbing. Tool temperatures of 70–90°C reduce residual stress and improve wall-thickness distribution. Failure to pre-dry the sheet before thermoforming, even after storage in ambient air for 2 h at relative humidity above 60%, causes bubbles and delamination between the cap layer and bulk, especially in coextruded structures containing a recycled ABS core.
In production-scale sheet lines, batch-to-batch variation in rubber particle size causes melt strength variation and visible differences in grain depth after thermoforming. Offline correlation of melt flow rate and capillary rheometry is recommended before changing forming parameters. The material’s habit of sagging earlier than lower-impact extrusion grades also affects chain-rail and plug-assist timing; a slower heat soak between 160°C and 170°C may compensate for high-rubber softness, but it narrows the forming window where the sheet remains elastic enough for uniform draw.
Substitution of a general-purpose injection ABS with Daqing ABS 850 changes the room-temperature failure mode from brittle fracture to ductile yielding, but it also lowers the melt flow rate from 15–25 g/10 min to 5–8 g/10 min under ISO 1133-1:2022. The lower flow requires wider gates, shorter flow paths, or elevated melt temperature. Surface gloss is typically lower than that of high-gloss injection grades because the larger rubber particles diffuse light at the surface; texturing can mask this reduction. In applications with ambient impact loading, the switch to 850 removes the need for toughening additives, but in high-flow, thin-wall electronics housings the viscosity penalty may prevent filling of wall sections below 1.2 mm.
| Grade type | Melt flow rate, 220°C/10 kg | Notched Izod, 23°C | Vicat softening | Primary processing route |
|---|---|---|---|---|
| Daqing ABS 850 | 5–8 g/10 min | 30–45 kJ/m² | 96–100°C | Sheet extrusion, thermoforming, thick-wall injection |
| Commodity general-purpose injection ABS | 15–25 g/10 min | 18–25 kJ/m² | 96–98°C | Thin-wall injection moulding |
| High-heat ABS | 4–8 g/10 min | 15–25 kJ/m² | 105–115°C | Automotive interior parts, instrument cluster housings |
| Flame-retardant ABS | 8–20 g/10 min | 10–20 kJ/m² | 90–100°C | Electrical enclosures, power strips |
The comparison matrix shows that Daqing 850 is the highest-impact member of the set but is not the preferred option where melt flow, high gloss, or continuous-service temperature above 100°C dominates the specification. For refrigerator liners, luggage shells, and automotive interior panels requiring deep draw and high crack resistance, the low melt flow of 850 is tolerated because the process is designed for sheet thickness from 2.0 mm to 6.0 mm. For direct-gate moulding of office equipment with wall thickness below 1.5 mm, a general-purpose or high-flow grade is more appropriate.
Under REACH 1907/2006, ABS resins are subject to Article 33 communication duties if Substances of Very High Concern exceed 0.1 wt%. RoHS 2011/65/EU Annex II restricts lead, mercury, cadmium, hexavalent chromium, PBB and PBDE; Daqing ABS 850 is typically supplied with a declaration of conformity when used in electrical and electronic equipment. For food-contact use, Commission Regulation (EU) No 10/2011 requires migration testing because acrylonitrile and butadiene monomers have specific migration limits; the polymer alone does not guarantee compliance when masterbatch or recycled content is introduced. In the United States, 21 CFR 181.32 provides a pre-sanctioned route for acrylonitrile copolymers if residual monomer and total nonvolatile extractives meet the prescribed limits; otherwise no unfavourable food-contact status should be assumed.
Processing incompatibilities include contact with acetal- or PVC-sourced volatiles, which form acidic degradation products that attack the butadiene phase. Avoid blending with amine-containing additives because these can accelerate SAN yellowing at processing temperatures. Solvent bonding uses methyl ethyl ketone or dichloromethane; aromatic solvents and esters cause stress cracking in thermoformed parts. Long-term outdoor use requires carbon black at 2–3 wt% or a UV-absorber package because unprotected butadiene segments undergo photo-oxidation and surface chalking. On production-scale sheet lines, pre-drying at 80°C for 2–4 h and verification of moisture below 0.05 wt% remain the most consequential controls for surface quality and impact retention in formed parts. Published data for this specific configuration is limited, and users should qualify each lot against the application-specific test programme before releasing daqing 850 into serial production.