| HS Code | 888526 |
| Density | 1.08 g/cm³ |
| Melt Volume Flow Rate 220 C 10 Kg | 6 cm³/10 min |
| Molding Shrinkage | 0.4–0.7 % |
| Tensile Modulus | 2000 MPa |
| Tensile Stress At Break | 50 MPa |
| Tensile Strain At Break | 15 % |
| Charpy Notched Impact Strength 23 C | 12 kJ/m² |
| Vicat Softening Temperature B 50 | 98 °C |
| Heat Deflection Temperature 0 45 Mpa | 90 °C |
| Heat Deflection Temperature 1 8 Mpa | 80 °C |
| Light Transmission | 88 % |
| Haze | 2 % |
| Refractive Index | 1.57 |
| Water Absorption | 0.2 % |
As an accredited INEOS Styrolution Terlux® MABS HD 2822 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | INEOS Styrolution Terlux® MABS HD 2822 is supplied in 25 kg sealed bags, palletized for safe industrial transport and storage. |
| Container Loading (20′ FCL) | 20′ FCL loaded with 25 kg bags of INEOS Styrolution Terlux® MABS HD 2822, palletized, shrink-wrapped, and securely stowed for export. |
| Shipping | INEOS Styrolution Terlux® MABS HD 2822 is shipped as dry thermoplastic pellets in sealed moisture-barrier bags, octabins, or bulk containers. Keep dry and avoid prolonged heat or direct sunlight. Normally non-hazardous for transport; follow the SDS and local shipping regulations. |
| Storage | Store INEOS Styrolution Terlux® MABS HD 2822 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat sources, moisture, and ignition sources. Keep in sealed original packaging, protect bags from damage, and avoid incompatible chemicals. Follow supplier-recommended temperature and humidity limits. Use first-in/first-out rotation and maintain good housekeeping to prevent dust and static buildup. |
| Shelf Life | Shelf life is typically 12 months from delivery when stored dry in original sealed packaging at room temperature. |
In ambulatory infusion sets and diagnostic fluid handling, transparent connectors molded from Terlux HD 2822 are specified where the part must retain dimensional stability after ethylene oxide treatment and must not exhibit crazing during repeated Luer torque assembly. The resin is a methyl methacrylate-acrylonitrile-butadiene-styrene copolymer, which places it between transparent polystyrene and transparent ABS in terms of chemical tolerance and impact behaviour. The melt volume rate of the grade is confirmed against the supplier certificate using ISO 1133-1:2022 at 220 °C and 10 kg loading. For medical use, the grade cannot be treated as automatically compliant; each finished device must be validated under ISO 10993-1, with cytotoxicity testing to ISO 10993-5:2009 and irritation or sensitisation testing to ISO 10993-10:2010. Blood-contact applications additionally require haemocompatibility testing under ISO 10993-4:2017. The formulation used on a production medical line is typically 100% virgin resin; regrind is excluded unless a validated closed-loop regrind process is established. If a colourant is required, the most acceptable systems are acrylic-based or MABS-compatible masterbatches at addition levels between 1.0 wt% and 2.0 wt%, because PE- or EVA-carrier masterbatches reduce transparency and can delaminate at weld lines. Pre-drying is carried out in a closed-loop desiccant dryer at 80 °C for 4 h, targeting a moisture content below 0.08%; packaged material exposed to ambient air above 60% relative humidity for more than 30 min should be re-dried. An all-electric injection moulding machine with a screw diameter in the 30–50 mm range and a shot capacity using 40–70% of the barrel is preferred. Melt temperature is maintained between 235 °C and 250 °C, and the mould surface is kept between 40 °C and 60 °C; lower mould temperatures produce acceptable appearance but increase residual stress. Thin-wall Luer connectors with sections below 1.0 mm require injection velocities above 200 mm/s and hold pressures in the 60–80 MPa hydraulic equivalent range to prevent short shots and flow-front hesitation. A documented failure mode on production-scale tooling is brittle fracture at the gate-to-body junction when the melt cushion is allowed to drop below 3–5 mm because the butadiene phase can degrade in the hot runner and shift the impact behaviour toward brittle failure. Terminal components in this segment include needleless access valve housings, Luer lock hubs, Y-site bodies, and transparent syringe caps, all of which are assembled by thread or snap fits and must pass leak testing at pressures between 0.3 bar and 1.5 bar depending on the device class.
| Nominal wall thickness (mm) | Melt temperature (°C) | Mould temperature (°C) | Hold pressure (MPa hydraulic equivalent) | Back pressure (MPa) |
|---|---|---|---|---|
| 0.8–1.2 | 240–255 | 50–70 | 60–80 | 5–8 |
| 1.2–2.5 | 230–245 | 40–60 | 40–60 | 4–7 |
| 2.5–4.0 | 220–235 | 35–55 | 35–50 | 3–6 |
Heavy-wall caps and collars for fragrance and cosmetic packs are injection-moulded from HD 2822 because the butadiene-modified methacrylate-styrene matrix provides a higher resistance to ethanol-water mixtures than styrene-acrylonitrile or general-purpose polystyrene while retaining a surface gloss that can be polished to SPI A-1 finishes. The compliance framework is not food-contact driven; instead the packaging article must satisfy EU REACH 1907/2006 SVHC restrictions and, where the pack contacts cosmetic formulations, the packaging material must not introduce substances that compromise the cosmetic product under EC 1223/2009. The formulation on the shop floor commonly consists of 98.5–99.5 wt% virgin resin with 0.5–1.5 wt% of a transparent masterbatch using a PMMA or MABS carrier; solvent dyes are generally avoided because they reduce ejection consistency and can migrate when the cap is stored in contact with fragrance compounds. Where a UV absorber is specified, addition levels of 0.2–0.5 wt% using a benzotriazole or triazine chemistry in an acrylic carrier are typical, but the exact selection must be confirmed by migration testing using the intended fragrance formula. Processing of thick sections above 3.0 mm requires a deliberate reduction of melt temperature to 220–235 °C and mould temperature stabilisation between 35 °C and 55 °C to limit sink marks without creating excessive molecular orientation. Hot-runner systems are normally specified with internally heated or valve-gated nozzles sized for a 1.5–2.5 mm gate, and the runner manifold should be held 5–10 °C below the nozzle set point to reduce thermal history. Packing pressure is profiled in two stages: an initial hold at 45–60 MPa hydraulic equivalent for 2–4 s, followed by a lower hold at 20–30 MPa for 6–10 s to control gate freeze and prevent reflow marks. The stress-crack risk in this segment is driven by the fragrance and sunscreen constituents: HD 2822 is generally resistant to 30–50% ethanol-water mixtures at room temperature, but published data for specific configurations is limited when the formula contains high fractions of diethyl phthalate, ethyl acetate, or non-polar emollients such as isopropyl myristate. Concentrated terpenes and ketones should be treated as aggressive; a cap that performs acceptably with a hydroalcoholic formula may still craze after continuous contact with limonene-rich fragrance oil. Terminals produced in this segment include fragrance over-caps, cosmetic jar collars, serum dropper bodies, and heavy-wall tester closures, where the visual acceptance criterion is usually based on 100% inspection under polarised light for internal stress and a drop test at 0–4 °C after conditioning for 24 h.
Transparent water tanks and panel windows in espresso machines, garment steamers, and floor-care appliances are moulded from HD 2822 where the part must tolerate intermittent exposure to demineralised water at 60–85 °C, citric acid-based descalers, and weak detergent solutions without showing haze or stress cracks. The relevant appliance safety standard is IEC 60335-1:2020 with its material requirements for resistance to heat, fire, and tracking; the final part also falls under RoHS Directive 2011/65/EU for electrical and electronic equipment. A typical production formulation for this segment uses 100% natural transparent resin with no external mould release, because silicon-containing mould release agents can leave a surface residue that reduces adhesive bonding of silicone gaskets and promotes stress cracking in hot water. If a blue tint is required for water tanks, the masterbatch loading is held between 0.2 wt% and 0.8 wt%, and the carrier must be acrylic or MABS-based; styrene-based carriers can introduce a visible haze. Large flat reservoirs with planar surfaces above 150 cm² are particularly sensitive to flow hesitation and should be filled using sequential valve gates rather than a single edge gate. Melt temperature is set at 230–245 °C, but the lower half of that range is preferred for wall stocks above 2.5 mm to minimise thermal degradation of the butadiene phase. Mould temperature is maintained at 45–70 °C using pressurised water or oil heating, because the higher surface temperature improves hot-water resistance by reducing frozen-in orientation. The process window is constrained: at melt temperatures above 250 °C yellowing can occur in the clear material, while at melt temperatures below 220 °C the high melt viscosity of the MABS matrix produces excessive shear heating and visible gate blush. The critical performance limit for this application is not short-term exposure but repeated hot-cold cycling; a tank filled at 80 °C and then cooled to 5 °C can develop microcracks near weld lines if the packing phase is terminated too early. Published data for this exact grade under NSF/ANSI/CAN 61 or EU 1935/2004 food-contact certification is limited; therefore potable-water applications require grade-specific approval letters from the supplier before tooling is released. Terminals in this segment include coffee-machine water reservoirs, steam-iron fill tanks, extraction cleaner reservoirs, and transparent inspection windows.
The multi-cavity production of retractable pen barrels and marker bodies uses HD 2822 for a combination of low visible weld lines, alcohol-based ink resistance, and high flow that fills long, thin-walled core-and-cavity sets without excessive clamp force. The regulatory requirements are driven by the toy-like nature of some stationery: EN 71-3:2019 + A1:2021 restricts migration of heavy metals from accessible surfaces, and REACH 1907/2006 restricts certain phthalates and PAHs in polymers. The formulation for a stationery line usually contains 0.3–0.6 wt% of an internal mould release or lubricant masterbatch to improve ejection from textured grip surfaces; however, over-lubrication beyond 0.6 wt% produces surface defects and can reduce adhesion of pad-printed brand graphics. Colours are mixed at the press using transparent masterbatch at 1.0–2.0 wt%, because liquid colour can cause screw slippage on high-speed reciprocating screws. Drying follows the same desiccant protocol as other HD 2822 applications: 80 °C for 4 h, with a return-air dew point below -30 °C, to bring moisture below 0.1%. In multi-cavity hot-runner tools with 16–32 cavities, cavity-to-cavity fill imbalance above 5% by weight is a known source of variation in clip retention force; therefore the hot-runner balance must be verified with short-shot studies before production. Melt temperature is run at 230–250 °C, and the mould is held at 40–60 °C; for moulded threads and snap fits, the ejection temperature must be below 70 °C to prevent thread distortion. The main material-related failure mode in this segment is solvent stress cracking at the ink-fill end when ethanol-based inks contact a highly stressed gate region; secondary gates or tab gates located away from the thread area reduce this failure. Terminal parts include transparent pen barrels, cap bodies, marker reservoirs, and cosmetic pencil bodies, where dimensional checks are performed to ISO 2768-m tolerances and the surface is tested for alcohol resistance by 24 h contact with 70% ethanol at 23 °C.
In edge-lit displays and control rings for consumer audio equipment, HD 2822 is used as a transparent light guide where polycarbonate would require a hard coat and PMMA would lack impact resistance during assembly snap fits. The regulatory basis for this segment is the EU RoHS Directive 2011/65/EU for hazardous substances and REACH 1907/2006 for SVHC reporting; electrical safety of the finished appliance is assessed under IEC 62368-1:2018. The optical formulation should avoid mineral fillers, reinforcing fibres, and high-loading colourants; if a neutral grey tint is required, masterbatch loading is held below 0.5 wt% and the pigment particle size must be below 1 µm to prevent light scattering. Ultraviolet stabilisers may be used at 0.2–0.4 wt%, but they can shift the colour coordinates of white LED light if overdosed. The moulding process uses a high-polish cavity with surface roughness below 0.05 µm Ra, and the tool requires adequate venting because MABS can generate gas at high melt temperatures that causes silver streaks on polished faces. Melt temperature is set from 240 °C to 255 °C for thin light-guide sections, and mould temperature is kept between 50 °C and 70 °C to replicate the polished mould surface. Injection speed is profiled to avoid jetting at the gate; a curved or tab gate is preferred over a direct pin gate. The total cycle time is often limited by the ejection temperature, which should not exceed 60 °C for parts below 1.5 mm thickness to prevent warpage. The main property cliff for this application is the combination of heat and load: HD 2822 has a Vicat softening point above 95 °C, but is not a substitute for polycarbonate in areas where the LED board can exceed 100 °C continuously. Published data for this exact configuration is limited, so end-product testing for colour shift after 1,000 h of LED exposure is required. Terminal components include light bars, control-knob light rings, display lenses, and backlit panels, where total luminous transmittance is verified to ISO 13468-1:2019 on a 2.0 mm plaque or on the finished part if surface curvature permits.
Reusable transparent housings and tray covers for dental or veterinary instruments may be produced from HD 2822 only when steam sterilisation is limited to defined conditions, because the copolymer is not an engineering polymer with unrestricted autoclave capability. The applicable standards for this segment are ISO 17665-1:2006 for moist heat sterilisation processes and, where the device contacts skin, ISO 10993-1 evaluation is required at the finished-device level. The formulation must avoid heat-sensitive dyes, metallic pigments, and external mould release, because surface residues can be extracted by steam and become visible as haze after repeated cycles. A typical pre-dried material is moulded at 240–255 °C with a mould temperature of 50–70 °C to reduce residual stress; after ejection, the parts are annealed in a forced-air oven at 65–75 °C for 2 h, which lowers internal stress but can produce a small dimensional relaxation that must be factored into tool dimensions. The critical design rule is to avoid sharp internal corners below 0.5 mm radius, because localised stress concentration at gate or ejector marks promotes steam-induced crazing. Published data for repeated steam cycles at 121 °C for this specific grade is limited; production qualification therefore requires a worst-case cycle matrix on finished parts, for example 50 cycles at 121 °C or 20 cycles at 134 °C, with inspection for haze, dimensional change, and loss of snap-fit force after each interval. The upper service limit is defined by the Vicat softening point and the autoclave pressure; if the part is clamped or loaded during sterilisation, distortion can occur even when the free-standing Vicat B50 is above 95 °C. Terminals for this segment include sterilizable transparent tray lids, protective covers for equipment controls, and reusable handling trays, all of which should be specifically designed with generous radii and uniform wall thickness.
Competitive INEOS Styrolution Terlux® MABS HD 2822 prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618005193850
Email: sales8@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Terlux® HD 2822 is a transparent methyl methacrylate-acrylonitrile-butadiene-styrene injection-molding grade supplied by INEOS Styrolution. The copolymer formulation is engineered to provide low haze and a melt viscosity suited to high-cavitation, thin-wall tooling. In polymer classification terms, the material falls under ISO 19062-2 as a MABS material and differs from opaque ABS grades because the refractive index of the grafted polybutadiene phase is matched to the continuous styrene-acrylonitrile-methyl methacrylate phase. The grade is intended for medical device housings, diagnostic cuvettes, transparent connectors, and other components in which visual inspection through the molded wall is an acceptance criterion. The paragraphs that follow define the specification envelope, processing thresholds, and material-selection boundaries using standardized data and production-scale injection-molding observations.
Melt viscosity is characterized by melt volume-flow rate under ISO 1133-1:2022 at 220°C with a 10.0 kg load. Mechanical data are obtained according to ISO 527-1/-2:2012; notched impact data are obtained according to ISO 179-1/1eA:2010. The table records indicative values for the grade; molded-part values will vary with gate position, orientation, and thermal history.
| Property | Standard and condition | Indicative value for HD 2822 |
|---|---|---|
| Melt volume-flow rate | ISO 1133-1:2022, 220°C, 10.0 kg | ≈22 cm³/10 min |
| Density | ISO 1183-1:2019, 23°C | ≈1.08 g/cm³ |
| Tensile modulus | ISO 527-1/-2:2012, 1 mm/min | ≈1,900 MPa |
| Tensile stress at yield | ISO 527-1/-2:2012, 50 mm/min | ≈42 MPa |
| Notched Charpy impact | ISO 179-1/1eA:2010, 23°C | ≈4 kJ/m² |
| Vicat softening temperature VST/B/50 | ISO 306:2022, 50 N, 50°C/h | ≈88°C |
| Light transmittance | ISO 13468-1:2019, 3 mm | ≈89% |
| Haze | ISO 14782:2021, 3 mm | ≈1.0% |
| Water absorption | ISO 62:2019, 24 h, 23°C | ≈0.2% |
Table values are drawn from manufacturer literature and class-typical data for transparent MABS; they are not batch certificates. The product-specific datasheet should be requested from the supplier before setting inspection limits.
For processors running high-cavitation tooling, the melt-temperature window is narrow at high screw speeds because the butadiene phase is thermally sensitive. The supplier recommends barrel settings from 180°C in the feed zone to 240°C at the nozzle, with an air-shot melt temperature of 230°C ± 10°C. Mold surface temperature is maintained at 40–70°C. Pre-drying is mandatory at 80°C for 4 h in a dehumidified-air dryer with a dew point of -30°C or lower. If ambient relative humidity exceeds 60% or regrind fraction exceeds 20%, drying time is extended to 6 h. Residual moisture above 0.03 wt% can cause splay, silver streaks, and loss of notched impact strength. On a three-zone reciprocating screw with L/D ratio 20:1, screw speed is set so that dosage remains 65–75% of barrel capacity; back pressure of 5–10 bar hydraulic is sufficient to remove unmelted resin without excessive shear heating. Injection pressures at the screw tip typically range from 80–120 MPa for thin-wall filling; pressure-limited fill indicates a need to raise melt temperature within the allowable ceiling or to enlarge gate diameter.
Mold temperature control units are operated with supply pressure 2–4 bar and turbulent flow in cooling channels; laminar flow reduces heat removal and produces uneven shrinkage. For optical surfaces, mold inserts are polished to Ra 0.05 µm or better. Surface roughness above Ra 0.2 µm increases measured haze, and gas entrapment creates dark specks at the end of fill. Venting depth at the parting line should not exceed 0.03 mm for this low-viscosity melt because larger vents flash.
Hot-runner processing introduces additional thermal history. Externally heated manifolds with temperature variation ±1°C across nozzle tips are used to avoid local overheating. At melt temperatures above 250°C, total residence time is kept below 5 min. Evidence of thermal degradation appears as a shift in yellowness index measured under ASTM E313-20; an increase of more than 2 units relative to virgin pellets indicates throughput interruption or poor manifold thermal control. Gate shear rates above 100,000 s⁻¹ may cause melt fracture; increasing gate diameter from 0.8 mm to 1.2 mm or reducing injection velocity restores surface quality.
Transmission and haze are measured on injection-molded plaques rather than raw resin. A 3 mm plaque shows transmittance of approximately 89% and haze of approximately 1.0% under ISO 13468-1:2019 and ISO 14782:2021. These values are reduced by surface roughness, weld lines, excessive mold-release agents, and contamination. In medical device housings, secondary operations such as ultrasonic welding and adhesive bonding alter local residual stress. Solvent-based adhesives containing methyl ethyl ketone or ethyl acetate are incompatible because they induce environmental stress cracking in stressed MABS. Cleaning protocols using isopropanol should be validated at molded strain levels because the grade exhibits limited alcohol resistance. Ethylene oxide sterilization, gamma irradiation, and e-beam sterilization require device-level qualification; published data for repeated sterilization cycles for HD 2822 are limited, and color shift may occur under gamma doses above 25 kGy.
Regulatory documentation is product-specific. A raw-material statement of compliance to USP Class VI or ISO 10993-5 does not replace final device testing under ISO 10993-1:2018 and regional medical device regulations. For food-contact or drug-packaging use, the converter must verify whether HD 2822 is listed under applicable 21 CFR sections and whether migration testing under EU 10/2011 is required. The grade is supplied for industrial transformation; no statement in this paragraph constitutes regulatory clearance.
The difference between HD 2822 and opaque high-impact ABS is primarily optical phase compatibility. Opaque ABS contains polybutadiene particles with a refractive index difference sufficient to scatter visible light; HD 2822 reduces that difference by incorporating methyl methacrylate in the continuous phase and selecting a grafted rubber morphology that preserves transparency. The trade-off is lower impact strength. Opaque high-impact ABS can show notched Charpy values of 20–30 kJ/m² at 23°C, whereas HD 2822 is specified at approximately 4 kJ/m². Against polycarbonate, HD 2822 has a Vicat softening temperature of 88°C versus approximately 145°C for a medium-viscosity polycarbonate, but the melt volume-flow rate of HD 2822 at 220°C/10 kg is ≈22 cm³/10 min, permitting lower injection pressure and shorter cycle time in thin-wall tools. Against PMMA, HD 2822 has lower elastic modulus and lower surface hardness; PMMA retains greater ultraviolet stability, while HD 2822 offers higher notched impact and flowability. Within the Terlux platform, HD 2822 is selected over lower-flow transparent MABS when pressure-limited filling occurs in multi-cavity tools or when wall thickness falls below 1.5 mm. The high-flow behavior is obtained through molecular-weight control and not through external plasticizers; published side-by-side grade comparison data are limited. These comparisons are material-class indicators and not direct engineering substitutes; part-level validation is required for any material substitution.
For thin-wall diagnostic components such as transparent cuvettes and instrument windows, HD 2822 is processed with sequential valve gating to move weld lines out of the optical path. A filling time of 0.3–0.5 s for a 1.0 mm wall section minimizes freeze-off and orientation. Packing pressure is set at 60–80% of peak injection pressure and held for 2–4 s. Venting depth at the parting line is limited to 0.02–0.03 mm to prevent flash while allowing air displacement. After ejection, parts are placed on non-abrasive fixtures; handling with bare metal tools can create micro-scratches that scatter light. For optical parts with tight birefringence limits, annealing at 70°C for 2 h may reduce molded-in stress, but part dimensions can shift by 0.1–0.3%; production experience with HD 2822 in this configuration is limited and should be confirmed by dimensional capability studies.
Production-scale failure modes observed in transparent MABS include gate blush due to excessive shear rate at valve-gated tips, black specks from degraded material accumulating in hot-runner dead spots, and splay from incomplete drying. Screw-recovery time should not be extended more than 10 s beyond the cooling time required for part ejection; prolonged residence in the barrel promotes oxidation and yellowing. Material changes from pigmented ABS to HD 2822 on the same machine require purging with a low-viscosity clear styrenic purge compound because contaminated dead spots produce visible specks. For a projected area of 200 cm² in a multicavity medical housing, clamp force of 800–1,000 kN is typically required to prevent mold deflection. Mold deflection above 0.05 mm in optical zones generates differential shrinkage and birefringence.