| HS Code | 689351 |
| Density | 1.04 g/cm³ |
| Melt Volume Rate | 18 cm³/10 min (220 °C/10 kg) |
| Tensile Modulus | 2100 MPa |
| Tensile Strength At Yield | 45 MPa |
| Elongation At Break | 15% |
| Charpy Notched Impact Strength | 18 kJ/m² at 23 °C |
| Vicat Softening Temperature | 98 °C |
| Heat Deflection Temperature A | 88 °C |
| Heat Deflection Temperature B | 80 °C |
| Rockwell Hardness | R 100 |
| Ul 94 Flammability Rating | HB |
| Water Absorption | 0.3% |
| Molding Shrinkage | 0.4–0.7% |
As an accredited INEOS Styrolution ABS TERLURAN 2822 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg polyethylene-lined paper sacks, palletized for safe handling and storage of INEOS Styrolution ABS TERLURAN 2822. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with palletized 25-kg bags of INEOS Styrolution ABS TERLURAN 2822, approx. 18–20 MT net, secured for export. |
| Shipping | INEOS Styrolution ABS TERLURAN 2822 is shipped as non-hazardous ABS thermoplastic pellets in moisture-resistant bags, octabins, or bulk containers. Keep dry, cool, and protected from direct sunlight and contamination. Under normal transport, it is not classified as dangerous goods; no UN number or hazard class applies. |
| Storage | Store INEOS Styrolution ABS TERLURAN 2822 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep containers tightly closed to prevent moisture pickup and contamination. Avoid dust generation and static buildup; ground equipment if handling fines. Protect from UV and follow the SDS and local regulations. |
| Shelf Life | Shelf life is typically 12 months when stored dry in original packaging below 30°C, protected from sunlight and moisture. |
Terluran 2822 is processed in automotive interior trim tools where nominal wall stock falls below 2.2 mm and flow length from a centrally located gate exceeds 180 mm. The grade’s melt-flow behaviour under ISO 1133-1:2022 at 220 °C/10 kg is used as input for pressure-drop simulation in multi-cavity tools, but lot-specific certificates of analysis should be used for production start-up because ash and residual acrylonitrile levels shift viscosity in the melt pool. Material is pre-dried in a desiccant dryer with air dew point below −30 °C at 80 °C for 3–4 h to reach residual moisture below 0.1%; at ambient relative humidity above 60%, drying time is extended to 4–6 h and the hopper loader is purged with dry air. Barrel temperatures are set in a straight profile between 230 °C and 250 °C, mould temperature between 50 °C and 65 °C. Injection velocity is increased to 80–120 mm/s to prevent premature freeze-off in grained ribs and bosses, while transfer from injection to hold is switched by cavity-pressure transducers at 35–40 MPa at the last point of fill. A projected part area of 0.08 m² at 35 MPa cavity pressure requires approximately 2,800 kN clamp force; smaller machines flash if the tool is not compression-clearanced. Automotive interior parts made from this grade must be tested to OEM-specific emission protocols, typically including gravimetric fogging according to DIN 75201 and odour assessment according to VDA 270; these are tool- and process-dependent outputs, not automatic product properties. When grained or acid-etched cavities are used, gloss levels measured to ISO 2813 on smooth skin should be established early because regrind content above 15 wt% and residence time beyond 8 min at 245 °C shift spectral reflectance before bulk mechanical properties degrade. Continuous-use temperatures above 85 °C require heat-ageing validation because ABS dimensional changes approach the published Vicat softening boundary when constraint stress is present.
A portable electronics rear cover moulded at 2.0 mm nominal wall thickness and weighing approximately 12 g is evaluated under IEC 60068-2-31 free-fall conditions from 0.5 m onto a steel plate at −10 °C. The limiting failure mode is not bulk tensile yield but brittle crack initiation at the weld line formed downstream of a speaker-grille core hole. To preserve impact resistance there, the melt temperature is maintained at 245–255 °C and the mould surface is held at 60–70 °C; a mould temperature below 50 °C raises the skin orientation layer and reduces notched impact energy near the flow-front junction. A sequential valve-gate programme is preferred over simultaneous edge gating because the meeting angle of the melt fronts determines the depth of the weld line. Hold pressure is set at 60–70% of the injection-pressure peak and held for 2–4 s to minimise cavity-pressure drop at the weld line. Notched Charpy impact measured to ISO 179-1/1eA on welded plaques is used as a gate-position screening test; a decrease in notched impact exceeding 25% relative to a single-gate plaque moulded to ISO 294-1 indicates an unacceptable gating arrangement. For final enclosures, UL 94 classification is thickness-dependent and must be verified at the thinnest wall with the actual colourant package, because ABS without flame-retardant additives usually obtains only an HB class under UL 94. Snap-fit bosses adjacent to the weld line should be moved at least 8 mm away from the flow-front junction to reduce local stress concentration. Solvent exposure from end-user cleaning agents is screened under ISO 175:2010 with 50% isopropanol for 24 h at 23 °C; parts that show gate-area crazing require a lower hold-pressure decay or a redesigned gate.
High-gloss fascia panels for small household appliances place simultaneous demands on mould finish, cleaning-agent resistance, and dimensional stability across 250 mm of unreinforced ABS. Terluran 2822 is dried to below 0.08% residual moisture before moulding; a dew-point meter on the dryer supply should read below −35 °C because moisture above this threshold produces surface splay on Class A polished cavities. A mould base with cartridge heating or oil circulation is set to 55–70 °C, and the polished cavity surface is periodically checked for micro-scratches that transfer to the part as visible haze. Panels are subjected to chemical-resistance screening under ISO 175:2010 using cotton-soak contact with 5% citric acid, 50% isopropanol, and 1% sodium carbonate solution for 24 h at 23 °C. Stress-cracking after this exposure is assessed visually at 10× magnification after no load; parts with residual moulded-in stress near the gate show radial crazing around the sprue when exposed to isopropanol. Aromatic and ketone solvents such as toluene and methyl ethyl ketone are incompatible and must be excluded from production-area cleaning routines. Dimensional stability is verified according to ISO 291 conditioning atmospheres, with post-mould shrinkage measured after 24 h and 48 h at 23 °C and 50% relative humidity. The injection unit should use a shut-off nozzle and a screw with L/D between 20:1 and 25:1 and compression ratio 2.2:1 to avoid unmelted granule passage that leaves surface pits. Regrind content is held below 15 wt% for high-gloss parts because repeated heat history shifts the melt-flow balance and can produce visible flow lines at the gate. External mould-release sprays are not used on polished cavities because stearate transfer lowers gloss by more than 5 GU measured to ISO 2813; ejection is handled by draft angles above 1.5° and stripper rings.
In distribution boxes with multiple core pins, cable-entry knockouts, and internal ribs, melt-flow fronts split and recombine at geometries where the local holding pressure decays before gate freeze. Charpy impact measured on injection-moulded plaques to ISO 179-1/1eU is used for incoming lot comparison, but component-level impact tests near the knockout membrane after conditioning at −5 °C for 16 h provide the relevant acceptance data. The dominant processing lever is not melt temperature alone but the combination of melt temperature 240–255 °C, mould temperature 60–75 °C, and hold-pressure time sufficient to keep cavity pressure above 40 MPa at the knit line until the gate seals. If cavity pressure drops below 20 MPa before freeze-off, the knit line remains as a surface notch and low-temperature impact values drop sharply. Gates are positioned to create a single flow front through high-stress zones, and overflow wells or locally thickened ribs are used to force the knit line into low-stress web areas. Electrical-safety testing of the final enclosure requires glow-wire performance under IEC 60695-2-11, but ABS grades without additional flame-retardant modification are generally limited to applications in which the final product passes the relevant end-product standard rather than carrying an independent high-temperature ignition rating. Post-mould annealing at 75 °C for 2 h can reduce residual surface stress and improve stress-crack performance against installation fluids, but it increases cycle time and can cause slight gloss reduction on textured surfaces. Regulatory compliance is documented under EU 2011/65/EU and REACH Regulation (EC) No 1907/2006 through supplier certificates; these are formulation-specific and must be requested for the actual colour and lot.
Floor-care tool housings moulded from Terluran 2822 are assembled by self-tapping screws into bosses and by vibration welding along a perimeter bead. The screw bosses require pilot holes with an internal diameter equal to 70–80% of the screw outer diameter to limit hoop stress below the threshold at which ABS environmental stress cracking begins; assembly torque is controlled at 1.2–1.8 N·m for 3 mm screw diameters, but fastener supplier data takes precedence. Vibration-welding joints use a 1.0–1.5 mm bead height and a melt-down of 1.0–1.3 mm; welding amplitude and frequency are selected after evaluating the cleaning-solution compatibility of the final part because residual fluid inside the weld joint can accelerate crack growth. The main processing risk in floor-tool housings is high clamp force induced by long projected areas, so cavity-pressure sensors are installed in the end-of-fill location and used to switch from injection to hold phase at 30–35 MPa cavity pressure rather than by timer. Barrel residence time is kept below 8 min at 245 °C because extended residence increases the yellowness index of natural material and shifts notched impact performance before the part exceeds visual acceptance limits. Surface hardness and scratch resistance are evaluated with ISO 1518-1 or the OEM-specific Erichsen scratch-tip method, but ABS is not generally scratch-resistant enough for unpainted high-traffic surfaces without texture. Textured surfaces with a typical surface roughness of Ra 6.3–12.5 µm hide abrasive marking longer than polished surfaces, but texture depth must be validated for ejection because deeper textures increase release force and can cause ejection pin marks.
Snap-fit retention in ABS depends on flexural modulus measured to ISO 178:2019 and on the strain level at the undercut. For an unreinforced ABS housing rib with a cantilever length of 12 mm, thickness of 1.5 mm, and undercut depth of 0.6 mm, the calculated outer-fibre bending strain should remain below 2.0% to avoid stress-whitening and creep relaxation. The use of Terluran 2822 in snap-fit closures requires a mould temperature high enough to reduce frozen-in orientation near the hinge root; a mould temperature of 55–65 °C is typical. Moulded-in residual stress is checked on a polariscope or by the immersion method described in ISO 175:2010 using n-propyl acetate, but exposure time must be limited to 3 min to avoid solvent absorption at the surface. The grade is not recommended for integrally moulded living hinges because ABS has limited repeated flexural fatigue strength compared with polypropylene; if a living hinge is required, the part should be redesigned to use a metal pin or snap fit. For snaps assembled into a painted or electroplated housing, plating adhesion is measured by the OEM cross-cut test to ISO 2409, but ABS electroplating systems are based on a butadiene-rich surface etch and should be qualified with the specific Terluran 2822 lot because rubber-particle distribution alters etch depth. Published data for this specific electroplated configuration is limited, so adhesion and thermal-cycle testing must be performed on moulded plaques before production approval. Repeated snap engagement is tested to 5,000 cycles under 23 °C and 50% relative humidity; retention force loss beyond 15% at cycle 1,000 indicates excessive root strain or over-filled material at the snap base.
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Introduced under the TERLURAN product family, INEOS Styrolution ABS TERLURAN 2822 is classified as a high-flow acrylonitrile-butadiene-styrene injection molding resin. The material’s published melt volume-flow rate is 22 cm³/10 min when measured at 220 °C under 10 kg piston load according to ISO 1133-1. Density is 1.04 g/cm³ per ISO 1183-1, and tensile modulus is 2300 MPa per ISO 527-2. These values place the grade in the easy-flow segment of the TERLURAN range while retaining sufficient butadiene rubber content for notched impact strength of 19 kJ/m² at 23 °C under ISO 179/1eA.
Unlike purely heat-resistant or high-impact ABS grades, TERLURAN 2822 is formulated around a continuous styrene-acrylonitrile matrix and a dispersed polybutadiene graft-rubber phase. The SAN matrix controls melt viscosity, modulus, and solvent resistance; the rubber phase controls crack propagation and low-temperature ductility. The molecular weight distribution in the SAN phase is tailored toward rapid mold fill without extreme loss of entanglement, so that environmental stress cracking resistance remains usable for unpainted enclosures. The grade is supplied as natural or colored pellets. Masterbatch carriers, internal lubricants, and color concentrates must be dry and viscosity-matched to avoid delamination or weld-line weakening.
Under ISO 1133-1, the MVR test uses a capillary die of 2.095 mm diameter and 8.000 mm length. The test temperature of 220 °C is below typical processing melt temperatures of 240 °C; therefore, the MVR ratio does not directly predict injection pressure at manufacturing shear rates. It does provide a reproducible lot-release parameter. For process simulation, capillary rheometry at 240 °C and 1000 s⁻¹ is more relevant than MVR because the ABS melt is pseudoplastic and viscosity declines with shear rate.
Melt pressure at the gate is limited by apparent viscosity, runner diameter, and the time required for the gate to freeze. With an MVR of 22 cm³/10 min under ISO 1133-1, the melt temperature envelope for injection molding is 220 °C to 260 °C, and the mold temperature is maintained between 40 °C and 80 °C. The lower mold-temperature boundary is set by surface replication and residual stress; the upper boundary is set by cycle length and sink-mark control in ribbed sections. In tools with wall stock of 1.0 mm to 1.5 mm, injection speed must be sufficient to prevent premature flow-front solidification. Published processing guidance for high-flow ABS in this MVR class recommends moderate-to-high injection velocity, but no single velocity setting is valid across all screw diameters and gate configurations.
Shear rates above 10,000 s⁻¹ in restricted gates or hot-runner tips can create viscous heating that degrades the polybutadiene phase and forms yellowed streaks. A cold-runner system should be balanced by volume and, where feasible, use free-flowing gate geometries with orifices not smaller than 0.8 mm for unpigmented material. On high-cavitation tools with hot-runner systems, the most frequent molding defect observed for this MVR class is gate blush from excessive shear heating in needle-valve hot drops. Correction requires reducing injection acceleration and increasing gate diameter rather than raising mold temperature.
Contrary to the assumption that higher MVR automatically permits lower clamp force, the clamping requirement is governed by projected area and peak cavity pressure. High-flow grades shorten fill but do not reduce peak cavity pressure by more than the viscosity ratio suggests. In multi-cavity tools, filling imbalance is often amplified by temperature differences between the nozzle-side and ejector-side mold halves. A difference of 5 °C to 10 °C between the halves can change flow-front velocity and shift the weld line. Mold temperature control with independent circuits and a flow-regulation manifold is required for appearance parts.
| Property | Test Method | Published Value |
|---|---|---|
| Density | ISO 1183-1 | 1.04 g/cm³ |
| Melt volume-flow rate, 220 °C/10 kg | ISO 1133-1 | 22 cm³/10 min |
| Tensile modulus | ISO 527-2 | 2300 MPa |
| Tensile yield stress | ISO 527-2 | 45 MPa |
| Charpy notched impact, 23 °C | ISO 179/1eA | 19 kJ/m² |
| Charpy notched impact, -30 °C | ISO 179/1eA | 7 kJ/m² |
| Vicat softening temperature VST/B50 | ISO 306 | 96 °C |
| Heat deflection temperature, 1.8 MPa | ISO 75-2 | 79 °C |
| Mold shrinkage | ISO 294-4 | 0.4–0.7% |
| Water absorption, 24 h | ISO 62 | 0.3% |
The notch sensitivity of this grade is moderate. The 19 kJ/m² Charpy value at 23 °C exceeds that of ultra-high-flow ABS grades but remains below medium-impact general-purpose grades. At -30 °C, the value falls to 7 kJ/m², indicating that the ductile-brittle transition has occurred. Components with snap-fits, screw bosses, or living hinges subjected to impact during freezing conditions should be evaluated in molded plaques rather than from raw material datasheets. The Vicat softening point of 96 °C supports short-term contact with warm surfaces, but continuous structural loads above 75 °C are not recommended for unfilled ABS. The heat deflection temperature under 1.8 MPa load of 79 °C limits high-tolerance dimensional stability in hot environments.
For high-gloss applications, mold surface preparation and process control are as important as resin selection. A polished tool surface with Ra below 0.05 µm promotes gloss retention; a mold temperature below 40 °C produces flow marks and blush at the gate. Packing pressure between 50% and 70% of peak injection pressure is used to compensate shrinkage in thick ribs. Gate freeze must be confirmed by weight stabilization; premature gate freeze leads to voids and sink marks, whereas excessive hold time increases cycle time and residual stress.
The most common substitution within the TERLURAN line is between TERLURAN 2822 and TERLURAN 2802. The following comparison is based on manufacturer-published typical values.
| Property | TERLURAN 2822 | TERLURAN 2802 |
|---|---|---|
| Melt volume-flow rate, 220 °C/10 kg | 22 cm³/10 min | 8 cm³/10 min |
| Charpy notched impact, 23 °C | 19 kJ/m² | 26 kJ/m² |
| Vicat VST/B50 | 96 °C | 98 °C |
| Tensile modulus | 2300 MPa | 2200 MPa |
| Mold shrinkage | 0.4–0.7% | 0.4–0.7% |
The MVR ratio of 22/8 gives TERLURAN 2822 a lower viscosity under standardized capillary conditions. The practical benefit appears in thin-wall housings, controller front panels, vacuum cleaner body shells, and small appliance covers where wall stock is below 1.2 mm and flow length-to-thickness ratio exceeds 120:1. Reducing melt viscosity permits lower injection pressure and better replication of textured surfaces. However, the Charpy notched impact at 23 °C declines from 26 kJ/m² to 19 kJ/m². This loss becomes greater at low temperature and in sharp notches. If a part is designed with an impact-absorbing snap-fit, TERLURAN 2802 may be preferred. Where the design is stiffness-dominated and impact events are rare, TERLURAN 2822 reduces fill-related rejects. Published data for direct cycle-time reduction in a specific injection molding machine configuration is limited because cooling time depends on wall thickness and molding tolerance more than on melt viscosity.
In comparison with higher-flow grades in the same supplier portfolio, TERLURAN 2822 occupies an intermediate position: it provides a substantial reduction in melt viscosity over general-purpose grades without falling to the lower notched impact values characteristic of ultra-high-flow ABS. This placement is quantifiable only when Charpy values, MVR, and Vicat temperature are examined together. Material substitution based solely on MVR can produce parts that fill successfully but fail low-temperature impact tests.
Pre-drying is mandatory before injection molding. At relative humidity above 60%, surface moisture can produce splay and silver streaks, although ABS does not undergo true hydrolytic backbone scission. Dry the resin at 80 °C for 2–4 h in a dehumidifying dryer with a dew point below -30 °C. Residual moisture should be below 0.1% by weight. The use of a closed feed throat and temperature-controlled hopper reduces re-moistening in production lines operating above 60% ambient humidity. During start-up, purge with a general-purpose ABS of similar viscosity.
The barrel profile is typically staged from 210 °C near the feed throat to 245 °C at the nozzle, with a maximum melt temperature of 260 °C. Residence time is a critical boundary. At a melt temperature of 240 °C, the melt should not remain in the barrel for more than 8 minutes. At 260 °C, residence time should be shortened to below 5 minutes to avoid gel particles, yellowing, and the formation of black specks from polybutadiene degradation. Accumulation in hot runners, nozzles, and check-ring dead spots can create the same effect even when the barrel timer is short.
General-purpose screws with L/D ratios of 20:1 to 24:1 and compression ratios of 2.0:1 to 2.5:1 are acceptable. High-shear mixing elements, high-compression barrier flights, and back pressure above 15 bar can add heat and should be used only after a thermal audit of the melt stream. Regrind use introduces an additional variable. Up to 20 wt% regrind is typically allowed for unpainted, non-appearance parts, provided the regrind is dried and dust-free. Higher levels tend to increase melt viscosity and reduce gloss. For white or high-gloss moldings, regrind levels above 30 wt% shift color and create visible splay, weld lines, and flow marks. Reprocessing the same material more than three times is not recommended because cumulative thermal history degrades the polybutadiene phase and reduces notched impact.
The material’s resistance to chemicals follows the general ABS class. Dilute mineral acids, alkaline cleaners, and aqueous salt solutions at ambient temperature are tolerated; however, ketones, esters, aromatic hydrocarbons, and chlorinated solvents cause environmental stress cracking. Molded-in stress from overcooling or aggressive packing amplifies stress cracking. Adhesives, paint solvents, and electroplating pre-treatments must be validated with prototype parts because solvent-based systems can attack the SAN phase. Ultrasonic welding energy directors with heights of 0.3 mm to 0.5 mm are generally feasible with TERLURAN 2822, but thin-wall collapse must be controlled by reducing amplitude and hold time.
The grade is cited in manufacturer literature for household appliance housings, vacuum cleaner bodies, electrical junction boxes, toys, sanitary fittings, and thin-wall enclosures. In each case, selection logic is based on wall thickness, fill length, impact requirement, and surface appearance rather than heat resistance. Applications requiring continuous use above 80 °C, flame retardance, or high impact below -20 °C should use other TERLURAN grades. The material is UL 94 HB rated at 1.5 mm, subject to color and thickness. RoHS 2011/65/EU and REACH registration are documented; final-article conformity depends on pigments, flame retardants, and processing aids. Food-contact status under Regulation (EU) No 10/2011 must be verified for the specific grade and color.