| HS Code | 147131 |
| Density | 1.04 g/cm3 |
| Melt Volume Flow Rate 220 C 10 Kg | 35 cm3/10 min |
| Molding Shrinkage | 0.4-0.7 % |
| Tensile Modulus | 2100 MPa |
| Tensile Stress At Yield | 45 MPa |
| Tensile Strain At Yield | 2.5 % |
| Charpy Notched Impact Strength 23 C | 20 kJ/m2 |
| Charpy Notched Impact Strength 30 C | 10 kJ/m2 |
| Vicat Softening Temperature B 50 | 98 °C |
| Heat Deflection Temperature 0 45 Mpa | 95 °C |
| Heat Deflection Temperature 1 8 Mpa | 83 °C |
| Ball Indentation Hardness | 95 MPa |
| Volume Resistivity | >1x10^15 ohm·cm |
| Dielectric Constant 1 Mhz | 2.9 |
| Water Absorption Equilibrium | 0.35 % |
| Ul 94 Flammability Rating | HB |
As an accredited INEOS Styrolution ABS TERLURAN GP-35N factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | INEOS Styrolution ABS TERLURAN GP-35N is supplied in 25 kg moisture-resistant paper sacks, palletized for industrial handling and storage. |
| Container Loading (20′ FCL) | INEOS Styrolution ABS TERLURAN GP-35N is bagged in 25 kg units, palletized, and securely loaded into a 20′ FCL container. |
| Shipping | INEOS Styrolution ABS TERLURAN GP-35N is shipped as non-hazardous ABS copolymer pellets and is not regulated for transport. Standard packaging is 25 kg moisture-barrier bags or octabins on pallets. Transport dry, away from excessive heat and direct sunlight, using covered commercial freight. |
| Storage | Store INEOS Styrolution ABS TERLURAN GP-35N in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and moisture. Keep in original, closed packaging to prevent contamination and moisture pickup. Protect from UV exposure and physical damage. Use first-in, first-out stock rotation and follow the SDS and local regulations. |
| Shelf Life | Typically 2 years from production date when stored dry, cool, and in unopened original packaging. |
In low-voltage electrical enclosure manufacturing, Terluran GP-35N, INEOS Styrolution's general-purpose ABS injection moulding grade, is processed as a high-flow styrenic feed for thin-wall housings where a UL 94 HB classification at 3.0 mm is accepted and no glow-wire ignition temperature above 650 °C is imposed by the end-product safety standard. Industry compliance for this segment is anchored to IEC 62368-1:2023 for fire and mechanical enclosure requirements, RoHS 2011/65/EU for homogeneous material heavy-metal limits, and REACH 1907/2006 SVHC disclosure; every shipment requires a certificate of analysis addressing lead, cadmium, mercury, hexavalent chromium, PBB, and PBDE below the directive's maximum concentration values. Typical addition ratios in the injection-moulding compound range from 98 wt% to 99 wt% virgin Terluran GP-35N with 1–2 wt% ABS-carrier colour masterbatch and up to 15 wt% closed-loop regrind recovered from sprues and runners, provided the regrind is pre-dried to <0.1% residual moisture. The downstream process uses a conventional single-screw injection-moulding machine with a screw L/D ratio of 20:1, barrel temperature profile from feed to nozzle 210/220/230/240 °C, nozzle melt temperature 230–250 °C, and mould surface temperature 50–70 °C; a back pressure of 5–10 bar is maintained for colour dispersion, screw rotation is kept at 60–100 min⁻¹, and injection speed is kept low to moderate to prevent jetting on polished cavity surfaces. Melt cushion is controlled at 3–6 mm, cooling time is 15–25 s for 2.0 mm nominal wall sections, and post-mould shrinkage of 0.4–0.7% is compensated in tool dimensioning. Terminal product types include wall socket faceplates, AC/DC adaptor housings, router bottom shells, and enclosure frames for handheld measuring instruments.
| Compliance item | Reference method or directive | GP-35N condition at container level |
|---|---|---|
| Flammability classification | UL 94, 3.0 mm vertical specimen | HB; not V-0/V-2 |
| Melt volume-flow rate | ISO 1133-1:2022, 220 °C/10 kg | 35 cm³/10 min |
| Tensile yield stress | ISO 527-2:2012 | 45 MPa |
| Restricted substances | RoHS 2011/65/EU, REACH 1907/2006 | Supplier CoA per lot |
| Pre-drying moisture limit | EN ISO 15512 | <0.1% |
Uncoated automotive interior air vent louvres and centre-console trim rings pose a combination of low-temperature ductility and surface gloss stability demands that place Terluran GP-35N within a narrow processing window when in-plant regrind is introduced. In this segment, industry compliance starts with IATF 16949:2016 for control of externally provided materials and processes, while ELV 2000/53/EC and REACH Annex XVII restrict cadmium, lead, mercury, and hexavalent chromium in vehicle materials; component-level validation according to FMVSS 302 / ISO 3795 for interior material burn rate is mandatory before production release, and published data for GP-35N in this specific configuration is limited. Formulation addition ratios for these parts are typically neat resin with 2–4 wt% OEM-approved interior colour concentrate and a maximum 20 wt% recycled material recovered from the same production lot; higher regrind fractions cause visible gloss differential on textured surfaces because thermo-oxidative ageing shifts the rubber-phase crosslink density unevenly. The production process uses sequential valve-gated hot-runner injection moulding with melt temperature 240–260 °C, mould surface temperature 60–80 °C, and low injection velocity at gate entry to prevent free-jetting; core-pin degassing is applied where splay is observed on polished ribbed regions. Vent depth is held at 0.02–0.04 mm, and weld-line strength at gate junctions is verified by ISO 179-1/1eA notched Charpy testing before dimensional capability runs. Terminal product types include air vent grilles, infotainment panel trim frames, door handle recesses, and steering column shrouds; continuous service conditions above 80 °C are not recommended for load-bearing snap-fits unless additional heat ageing validation is performed.
When 25 wt% in-house regrind is blended into GP-35N for cordless stick vacuum cleaner dust cup shells, the practical problem is not melt flow but low-temperature impact retention after repeated processing cycles. Compliance for this application is defined by IEC 60335-1:2020 mechanical strength requirements, with ball-pressure testing conducted under IEC 60695-10-2:2014 at 75 °C for parts supporting live connections, plus RoHS 2011/65/EU and REACH 1907/2006; because the dust cup is not a current-carrying or flame-enclosing part, no UL 94 V-class rating is required, but the housing must pass a 0.5 J impact test if specified by the final appliance standard. The compound addition ratio is 73 wt% virgin GP-35N, 25 wt% post-industrial regrind produced from gate and edge trim, and 2 wt% colour masterbatch; the regrind fraction is pre-dried to <0.05% moisture and screened to ≤6 mm granule size before dosing. The downstream process is high-speed injection moulding on a machine with accumulator-assisted injection, melt temperature 240–250 °C, mould temperature 50–60 °C, injection pressure 900–1200 bar, and cooling time set to 12–18 s depending on wall thickness in the cyclonic cone; barrel residence time is held below 5 min and screw dosage stroke is limited to 40–70% of barrel capacity. Material exposed to ambient relative humidity above 60% is dried at 80 °C for 4 h in a desiccant dryer before processing. Terminal product types include opaque dust cup shells, cyclonic separator outer cylinders, and filter cover frames.
The injection moulding of keyboard top covers and monitor bezels from Terluran GP-35N demands reproducible melt flow to fill multi-cavity tools with 0.9–1.2 mm nominal wall thickness without short shots at low packing pressure. Regulatory compliance for computer peripheral housings falls under IEC 62368-1:2023 for fire and mechanical enclosure requirements, RoHS 2011/65/EU, and REACH 1907/2006; surface resistivity of natural GP-35N is in the order of 1015 ohm/sq, so static-dissipative protection requires an external antistatic additive or coating, not the neat resin. Formulation addition ratio is 98 wt% GP-35N plus 2 wt% custom colour concentrate; filler or flame retardant is omitted because UL 94 HB at 1.5 mm is accepted for these product categories. The downstream process uses a high-flow injection-moulding grade with melt volume-flow rate 35 cm³/10 min at 220 °C/10 kg, enabling filling at melt temperature 230–250 °C, mould temperature 45–65 °C, and hydraulic injection pressure 800–1100 bar; hot-runner systems with valve gates are preferred to eliminate cold sprue regrind and maintain surface gloss across large flat panels. Screw diameter is selected between 35–50 mm for shot weights of 80–250 g, dynamic holding pressure is maintained at 45–65 MPa, and hopper drying is applied when ambient relative humidity exceeds 55%. Terminal product types include keyboard upper housings, monitor bezels, mouse shells, and printer control panel frames.
When colour consistency in high-gloss pen barrels becomes a process parameter, Terluran GP-35N is selected for its 35 cm³/10 min melt volume-flow rate under ISO 1133-1:2022, which reduces the residence time needed for thin-wall filling in multi-cavity tools. Compliance for writing instruments marketed to adults is primarily chemical-safety based: REACH Annex XVII entries for benzene and eight polycyclic aromatic hydrocarbons in accessible plastic parts must be met, and where products are supplied to educational or children's markets, EN 71-3:2019+A1:2021 migration limits for nineteen elements apply; ASTM D4236-94(2021) is used for chronic hazard labelling in art and writing materials. The formulation addition ratio in opaque high-gloss pen barrels is 99 wt% virgin GP-35N and 1 wt% solvent-dye or pigment ABS masterbatch; pearlescent or metallic versions use 2 wt% masterbatch, while regrind is excluded from visible gloss surfaces because gel bodies and black specks are visible under high polish. The downstream process uses polished hardened steel moulds with surface roughness <0.05 µm Ra, melt temperature 230–240 °C, mould surface temperature 55–65 °C, and injection speed below 120 mm/s to prevent gate blush and melt fracture. Sub-gate diameter is held at 0.8–1.2 mm, holding pressure is set at 55–75 MPa, and cooling time is 6–10 s for 1.0 mm wall sections. Terminal product types include pen barrels, cap bodies, mechanical pencil clutch housings, and marker shell components.
Constructional toy components moulded above 1.5 mm wall thickness use GP-35N as a high-flow ABS base, provided the compounder and brand owner obtain EN 71-3:2019+A1:2021 migration test results for all colour masterbatches and final pigmented compounds; the neat resin itself is not a food-contact or mouth-contact material and must not be represented as FDA 21 CFR compliant without separate formulation-specific evaluation. The EU Toy Safety Directive 2009/48/EC imposes chemical and physical safety obligations on the finished article rather than on the resin alone, and REACH 1907/2006 SVHC declarations are required from each compound supplier. Addition ratios in this segment are typically 96–98 wt% GP-35N, 1–3 wt% masterbatch, and up to 2 wt% processing lubricant or mould-release concentrate only where ejection force on deep ribs exceeds 40 kN; external impact modifier is introduced only when customer specifications demand notched Charpy impact above 25 kJ/m², which neat GP-35N does not supply at 23 °C according to its typical datasheet value of 19 kJ/m² under ISO 179-1/1eA. The injection-moulding process uses positive shut-off nozzles to prevent drool, melt temperature 230–250 °C, mould temperature 40–60 °C, and cooling time based on wall thickness; post-moulding adhesion of waterborne decorative inks requires corona or plasma surface activation because the polybutadiene-rich surface has low surface energy. Mould release taper is set at 1° minimum on deep ribs, draft angle at 0.5° on textured surfaces, and melt decompression at 3–5 mm after plastication. Terminal product types include building block base plates, constructional model frames, and hobby organizer trays.
For non-patient-contact housings of diagnostic devices, Terluran GP-35N is considered only when the device risk assessment does not require biocompatibility evaluation under ISO 10993-1:2018 and no cleaning agent compatibility beyond 70% ethanol or mild detergent is demanded. This application segment is governed by IEC 60601-1:2005+A1:2012+A2:2020 for basic safety and essential performance of medical electrical equipment, with fire-enclosure requirements depending on energy sources; RoHS 2011/65/EU and REACH 1907/2006 apply to devices placed on the European market. The formulation addition ratio is conservative: 98–99 wt% virgin GP-35N with 1–2 wt% medical-equipment grey or white masterbatch, and no post-industrial regrind unless the device manufacturer has conducted cleaning-agent exposure and impact ageing studies on the regrind fraction; gamma and ethylene oxide sterilisation are not qualified for GP-35N and would require full mechanical property revalidation. Downstream processing is standard injection moulding with melt temperature 230–250 °C, mould temperature 50–70 °C, and dedusting of granules before hopper loading to reduce black-spec formation in visible enclosures. Melt residence time is kept below 8 min, shot sizing is limited to 60% of barrel capacity, and material lot traceability is maintained according to ISO 13485:2016 where the device manufacturer's quality system requires supplier lot linkage. Terminal product types include ultrasound cart console covers, laboratory analyser side skirts, and non-load-bearing IV pole caddies; the material is not intended for fluid-contact components, respiratory accessories, or implant housings.
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INEOS Styrolution TERLURAN GP-35N is an unfilled acrylonitrile-butadiene-styrene injection-molding grade positioned in the medium-impact, high-flow segment of the Terluran GP product family. The grade is intended for thin-wall technical components where a melt volume-flow rate of 35 cm³/10 min at 220 °C and 10 kg per ISO 1133-1:2022 reduces filling pressure in multi-cavity tools and in parts with long flow-length-to-wall-thickness ratios. Representative mechanical properties obtained on dry, injection-molded specimens include a tensile modulus of 2400 MPa and yield stress of 45 MPa per ISO 527-2:2012, Charpy notched impact strength of 21 kJ/m² at 23 °C and 8 kJ/m² at -30 °C per ISO 179-1/1eA, and a Vicat softening temperature of 96 °C per ISO 306 A50. Mold shrinkage is typically 0.3–0.7 % per ISO 294-4:2018, and the material is classified UL 94 HB at 1.5 mm. These values place GP-35N one flow class above standard lower-flow ABS grades such as Terluran GP-22, with a corresponding reduction of roughly 20–25 % in room-temperature notched impact strength.
Because the property profile favors melt flow over energy absorption, GP-35N is used in electrical and electronic housings, appliance fascia, thin-walled furniture connectors, and small consumer goods where mold fill is the dominant constraint. The grade should not be used as a direct substitute for high-heat ABS in continuously load-bearing parts above 90 °C or in thick safety-relevant brackets requiring ductile crack propagation under high-speed loading. Published data for this specific configuration is limited beyond the supplier datasheet; field validation is required for snap-fit and ultrasonic-welding applications.
At the lower end of the supplier-recommended melt-temperature window, the shear-thinning response of the ABS matrix is not sufficient to prevent short shots in ribs, bosses, and end-of-fill features. Processing guidelines for high-flow Terluran grades specify a melt temperature range of 220–260 °C and a mold temperature range of 40–80 °C, with the upper half of the range required for polished cavity textures and wall stocks below 1.5 mm. In spiral-flow evaluations on a 25 mm reciprocating screw and a 2 mm test channel, flow length increases by approximately 30–40 % across the 220–260 °C melt-temperature window, but the exact value is gate- and tool-specific. A 10 °C drop in nozzle set temperature can increase the cavity pressure required to maintain constant fill time by 5–15 % depending on gate geometry, producing flow hesitation marks and local differences in gloss. Nozzle temperature is not used as a substitute for a correct barrel profile because the material experiences only limited conductive heating in the nozzle body.
Thermal stability of the butadiene phase becomes limiting above 250 °C. Residence times longer than 8 min at 260 °C produce yellowing, surface splay, and low-molecular-weight volatile compounds. Injection units with large shot-to-barrel ratios are therefore operated at the lower end of the melt-temperature range, especially when cycle times exceed 60 s or when hot-runner channels create additional residence time. Capillary rheometry per ISO 11443 is recommended for molders requiring exact shear-viscosity input for flow simulation at wall thicknesses below 1.0 mm.
Pre-drying is performed in dehumidifying dryers with a dew point below -30 °C at 80 °C for 2–4 h when residual moisture exceeds 0.1 wt%. Undried material exposed to ambient humidity above 60 % RH can hydrolyze during plastication, forming splay, bubbles, and weakened weld lines. The effect is more severe when regrind fractions exceed 20 wt%, because recyclate carries higher surface moisture and dust. Injection pressure is typically set between 70 MPa and 120 MPa, with holding pressure between 50 MPa and 80 MPa. Back pressure is maintained between 5 bar and 10 bar, and screw rotation speed is controlled between 30 min⁻¹ and 60 min⁻¹ to limit frictional heating and yellowing. At mold temperatures below 40 °C, knit-line visibility increases and surface gloss drops. Above 80 °C, cycle time increases without equivalent improvement in impact performance, and ejection sticking can occur on highly polished cores unless draft angles exceed 1.0 °. Regrind addition up to 30 wt% is possible if the material is cleaned and dried, but each 10 wt% regrind fraction can increase melt volume-flow rate by approximately 1–2 cm³/10 min because of molecular-weight reduction.
The differentiation of GP-35N from general-purpose ABS grades is defined by the inverse relationship between melt volume-flow rate and Charpy notched impact strength. The high-flow formulation is achieved through a shifted molecular weight distribution, which reduces melt viscosity but also reduces energy absorption under high-speed loading. Table 1 summarizes representative values from supplier datasheets; colorants, regrind, and moisture content shift the values toward the lower end of the stated ranges. GP-35N is therefore specified for thin-wall housings where the dominant load is static or low-velocity, while lower-flow grades are retained for thick structural parts requiring ductile crack propagation resistance.
| Property | Test Method | TERLURAN GP-35N | Lower-Flow ABS Reference |
|---|---|---|---|
| Melt volume-flow rate at 220 °C, 10 kg | ISO 1133-1:2022 | 35 cm³/10 min | 18–20 cm³/10 min |
| Tensile modulus | ISO 527-2:2012 | 2400 MPa | 2500 MPa |
| Tensile yield stress | ISO 527-2:2012 | 45 MPa | 48 MPa |
| Charpy notched impact strength at 23 °C | ISO 179-1/1eA | 21 kJ/m² | 27–30 kJ/m² |
| Charpy notched impact strength at -30 °C | ISO 179-1/1eA | 8 kJ/m² | 11–13 kJ/m² |
| Vicat softening temperature A50 | ISO 306 | 96 °C | 100 °C |
| Density | ISO 1183-1:2019 | 1040 kg/m³ | 1040 kg/m³ |
Chemical resistance follows the general ABS pattern. The butadiene phase is swollen by aromatic and aliphatic solvents, while the styrene-acrylonitrile matrix is attacked by esters, ketones, and chlorinated solvents. Environmental stress-cracking evaluation per ISO 22088-2 is required for contact fluids such as cutting oils, brake fluids, and plasticizer-containing PVC gaskets because higher residual orientation in high-flow parts can reduce stress-cracking resistance relative to lower-flow ABS. GP-35N is not considered a plating-grade material; for electroplated components, a specialty Terluran or Novodur grade with controlled butadiene particle size and etch morphology is preferred. Painting, in-mold labeling, and laser marking are feasible, but cleaning solvents containing MEK or methylene chloride can induce surface crazing and must be removed before molding or assembly. From a regulatory perspective, the base polymer can be evaluated for food-contact use under 21 CFR 177.1020 for acrylonitrile-butadiene-styrene copolymers and under EU Regulation 10/2011 with end-use migration testing. Supplier declarations for RoHS Directive 2011/65/EU and REACH Regulation (EC) No 1907/2006 must be requested for the specific color and lot before commercial release.
When the nominal wall is below 1.2 mm, the flow-length-to-wall-thickness ratio is verified against cavity layout, gate position, and available nozzle pressure. GP-35N can fill flow-length-to-wall-thickness ratios of approximately 120:1 to 150:1 from a direct edge gate at 240 °C and 80 MPa injection pressure, but textured surfaces, narrow ribs, and multi-gated tooling reduce the achievable ratio. Weld-line strength in high-flow ABS is typically 50–70 % of the parent Charpy notched impact value, and the reduction is non-linear when knit lines form at the end of fill where melt pressure and temperature are lowest. For snap-fit geometries, assembly strain is kept below 0.8 % when molded-in stress is unknown. Photoelastic inspection or solvent-jet tests with isopropyl alcohol can identify high-orientation zones. Mold shrinkage ranges from 0.3 % to 0.7 %, with anisotropic variation of 0.1–0.3 % between flow and cross-flow directions, requiring tooling dimensions to be corrected by differential shrinkage measurements after first-article inspection.
| Processing or Compliance Parameter | Setpoint or Classification | Reference Basis |
|---|---|---|
| Drying temperature | 80 °C | Supplier processing guide |
| Drying time | 2–4 h | Supplier processing guide |
| Dryer dew point | < -30 °C | Dehumidifying dryer specification |
| Melt temperature | 220–260 °C | Supplier processing guide |
| Mold temperature | 40–80 °C | Supplier processing guide |
| Back pressure | 5–10 bar | Injection molding practice for ABS |
| Flammability classification | UL 94 HB | UL 94 |
Published data for specific hot-runner configurations and sequential valve gating with GP-35N is limited. Molders are advised to generate in-house shear-viscosity data using capillary rheometry per ISO 11443 before committing to stack molds or thin-wall tools with wall sections below 0.8 mm. Processing with moisture above 0.1 wt% or with melt residence times beyond 8 min at 260 °C is outside the established operating boundary and invalidates representative mechanical property expectations.