| HS Code | 135646 |
| Manufacturer | BASF |
| Productname | BASF 3D Ultrafuse PET Fused Filament |
| Material | Polyethylene Terephthalate (PET) |
| Filamentdiameter | 1.75 mm and 2.85 mm |
| Diametertolerance | ±0.05 mm |
| Netweight | 750 g |
| Density | 1.27 g/cm³ |
| Tensilestrength | 53 MPa |
| Tensilemodulus | 2100 MPa |
| Elongationatbreak | 5% |
| Flexuralstrength | 80 MPa |
| Flexuralmodulus | 2200 MPa |
| Charpynotchedimpactstrength | 4 kJ/m² |
| Heatdeflectiontemperature | 70 °C at 0.45 MPa |
| Printtemperature | 220-240 °C |
| Bedtemperature | 60-80 °C |
| Printspeed | 30-60 mm/s |
| Dryingtemperature | 60 °C |
| Dryingtime | 4-8 hours |
| Coloroptions | Black, White, Red, Blue, Green, Yellow, Orange, Natural |
As an accredited BASF 3D Ultrafuse PET Fused Fillament factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | One 750 g spool of 1.75 mm BASF 3D Ultrafuse PET filament, vacuum-sealed with desiccant inside a cardboard box. |
| Container Loading (20′ FCL) | Palletized BASF 3D Ultrafuse PET fused filament spools, shrink-wrapped and secured inside a 20-foot FCL container for ocean transport. |
| Shipping | BASF 3D Ultrafuse PET Fused Filament is not classified as dangerous goods for transport. It has no UN number, proper shipping name, hazard class, or packing group. Ship in original sealed packaging, protect from moisture, heat, and physical damage. No special transport precautions required. Consult SDS for details. |
| Storage | Store BASF 3D Ultrafuse PET Fused Filament in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and strong oxidizers. Keep it in original sealed packaging or an airtight container with fresh desiccant. Protect from moisture, dust, and physical damage. Recommended: 15–25°C, low humidity. Avoid prolonged humid-air exposure, which can degrade print quality. |
| Shelf Life | BASF Ultrafuse PET filament: 12-month shelf life when stored unopened, dry, cool, and protected from moisture, heat, and sunlight. |
BASF 3D Ultrafuse PET fused filament is introduced into downstream manufacturing as a 100 wt% polyester feedstock requiring no melt dilution or reactive compounding on the printing line. The material is supplied in 1.75 mm or 2.85 mm diameter with a ±0.05 mm tolerance and is processed through fused filament fabrication equipment with a 0.40 mm nozzle. Application development must treat the term “addition ratio” as the set of process ratios controlling mass per unit length—extrusion multiplier, layer height relative to nozzle diameter, perimeter count, and infill density—rather than as a melt formulation ratio. The following application scenarios are restricted to known deployment areas for extruded PET filament in manufacturing aids, prototypes, and low-temperature end-use parts.
| Parameter | Value | Test method / source |
|---|---|---|
| Extruder temperature | 230°C–250°C | Manufacturer processing specification |
| Build plate temperature | 70°C–80°C | Manufacturer processing specification |
| Pre-drying | 60°C for 4 h–6 h | Forced-air oven |
| Density | 1.27 g/cm³ | ISO 1183-1 |
| Tensile yield strength | 50 MPa | ISO 527-2 |
| Flexural modulus | 2000 MPa | ISO 178 |
| Heat deflection temperature B | 70°C | ISO 75-2/B |
Food-contact packaging prototypes and cold-fill line fixtures consume Ultrafuse PET at 100 wt% of the printed feedstock; no compatibilizer, filler, or recycled PET addition is performed on the production floor because the filament is supplied as a pre-compounded single-material feedstock with a melt mass-flow rate characterized under ISO 1133-1:2022. For prototypes intended to replicate polyethylene terephthalate bottle preforms, caps, and closure skirts, the extrusion multiplier is held at 1.00 while the layer height is set at 0.12 mm against a 0.40 mm nozzle, yielding a layer-to-nozzle diameter ratio of 0.30. Compliance for final food-contact parts is governed by Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm² for food simulants, and by FDA 21 CFR §177.1630 for PET polymers; however, the as-printed article is not automatically compliant because porosity, surface roughness, and residual moisture adsorption may alter migration behavior, and the manufacturer of the final article must conduct migration testing under the intended time–temperature food contact profile. Downstream production uses a heated build plate at 75°C, a nozzle temperature of 240°C ±5°C, and a closed chamber is unnecessary for small-section prototypes but a draft shield is advisable when cumulative build time exceeds 8 h in an air-conditioned assembly room. Terminal product types include bottle preform fit-function samples, cap torque-testing fixtures, cold-fill line changeover gauges, and low-temperature dairy container indexing fixtures, all of which operate below 60°C surface temperature to remain below the 70°C HDT B value.
Within automotive pre-series interior development, Ultrafuse PET is applied at 100 wt% of the fused filament feedstock; the process ratio of extruder temperature to build plate temperature is maintained at 240°C to 245°C against 75°C, and the extrusion multiplier is set at 0.98 for dense skins to avoid over-extrusion artifacts on visible A-surface prototypes. The material is characterized by ISO 527-2 tensile yield strength of approximately 50 MPa and an ISO 178 flexural modulus near 2000 MPa, but the limiting technical factor is the ISO 75-2/B heat deflection temperature of roughly 70°C, which restricts printed components to zones where continuous air temperature does not exceed 65°C and transient exposure remains below 80°C for under 10 min. Compliance in the automotive prototyping supply chain is typically governed by IATF 16949 for the development supplier and by REACH (EC) No 1907/2006 for substance registration, while the printed part itself is not a production product and therefore does not carry full PPAP documentation; dimensional acceptance follows the OEM’s internal reference standard, often derived from DIN EN ISO 527-2 and ISO 178 tensile and flexural data. The downstream manufacturing process involves fused filament fabrication with a 0.40 mm nozzle at 50 mm/s mean print speed, 0.15 mm layer height, and a 20% to 40% gyroid infill pattern for non-structural dashboard bezels and HVAC vent prototypes. Terminal products include dashboard trim prototypes, infotainment bezel click-in trial parts, HVAC vent louvers, and door panel switch bezels for pre-series fit verification, but not airbag covers, steering column cladding, or components in direct sunlight on parked vehicles due to long-term thermal creep above 70°C.
For machining cell fixture sets and soft-jaw covers, the process ratio of 0.20 mm layer height to 0.40 mm nozzle diameter is maintained at 0.50, with a four-perimeter wall stack and 50% to 70% triangular infill, while the filament remains at 100 wt% of the feed material without dilution. In production-scale machining cells, the typical failure mode observed is not tensile fracture but localized creep at brass heat-set insert bosses when fixture temperature exceeds 60°C during aggressive dry machining, which can be mitigated by increasing the wall count to 5 and embedding inserts with a 2:1 hole-depth-to-insert-diameter ratio. Drying at 60°C for 4 h in a forced-air oven is required if spool storage relative humidity exceeds 40% for more than 24 h, because PET undergoes hydrolysis during extrusion when moisture content in the filament exceeds 0.1 wt%; the resulting part shows latent layer adhesion loss, surface splay, and reduced Izod impact measured under ISO 179-1. Compliance for manufacturing aids is not regulated by a single ISO standard, but the material and its printed output should conform to the plant’s ISO 9001:2015 control plan, and where the fixture is used in food-processing adjacent areas, EU 10/2011 or FDA 21 CFR §177.1630 may apply if incidental contact is possible. Terminal part types include CMM fixture base plates, assembly pallet nest inserts, soft jaw covers for aluminium clamping on CNC vises, and go/no-go gauge housings, with the documented limitation that PET is not inherently static dissipative and should not replace ESD-safe polycarbonate or PEEK composites in charge-sensitive assembly lines.
Solvent immersion testing of Ultrafuse PET printed walls indicates that the material retains practical resistance to dilute acids, aliphatic hydrocarbons, alcohols, and aqueous cleaning agents, but the printed wall is not equivalent to an injection-moulded PET surface because layer-boundary voids and edge pinning defects create capillary paths under prolonged liquid contact. The feedstock is therefore used at 100 wt%; no glass fiber or impact modifier is added, and the critical process ratio for fluid-contact parts is a 0.12 mm or 0.15 mm layer height against a 0.40 mm nozzle with 5 to 6 perimeter walls, producing a wall thickness of 2.0 mm to 2.4 mm that reduces through-wall porosity for low-pressure hydraulic experiments. A 100% solid infill is specified for any component holding liquid for more than 1 h, while 60% rectilinear infill is acceptable for structural racks without direct liquid contact. Extrusion is performed at 230°C to 245°C with a build plate at 75°C, and spool pre-drying at 60°C for 4 h to 6 h is mandatory before any fluid-tight prototype because moisture content above 0.1 wt% creates microvoids in weld lines that act as leak paths under 1.0 bar internal pressure. Compliance in the laboratory sector is anchored to ISO 175:2010 for chemical resistance classification, ISO 527-2 for tensile properties after immersion, and REACH (EC) No 1907/2006 for EU laboratory deployment; final end-use parts intended for aggressive solvent exposure outside the compatibility envelope must be qualified by ASTM D543 or ISO 175 testing on printed coupons, not on injection-moulded specimens. Terminal products include reagent bottle holders, wash bottle racks, pipette tip storage trays, and low-pressure solvent-carrier jigs for automated liquid handling workcells, with the boundary that ketones, strong alkaline solutions above pH 10, and aromatic hydrocarbons exceed the material’s chemical resistance and cause stress cracking or surface whitening.
Enclosed manufacturing and assembly cells that previously used ABS for low-stress housings and cable management parts substitute Ultrafuse PET at 100 wt% of the filament input, retaining an extrusion multiplier of 1.00 and a layer height of 0.15 mm on a 0.40 mm nozzle while setting infill density between 40% and 60% in a gyroid pattern to balance stiffness and print time. The driving technical requirement is low odour and reduced monomer emission during the melt deposition step; the filament is processed at 235°C to 245°C, below the upper limit at which PET degradation produces acetaldehyde, and the material does not emit styrene as with ABS, but the cell air exchange rate must remain at least 6 air changes per hour when a bank of four or more machines operates simultaneously in a sealed room. Compliance is assessed under REACH (EC) No 1907/2006 for substance exposure and under the RoHS Directive 2011/65/EU for restricted substances in electrical and electronic housings; flammability classification is not implicit, and any final electronics enclosure must be tested to UL 94 HB or the relevant appliance standard rather than assuming a V rating from the unfilled polyester. The downstream process may include tapping or heat-stake insert installation; because PET is notch-sensitive, threaded inserts with a 2.0 mm wall surrounding the boss and a hole diameter 85% of the insert outer diameter prevent circumferential cracking during installation. Terminal products include CNC control pendant housings, cable duct brackets, optical sensor mounts, and pneumatics manifold covers for low-temperature industrial automation cells, but the material is not substituted for polycarbonate in impact-loaded or high-voltage compartments.
In non-implantable medical device prototype construction, Ultrafuse PET is consumed at 100 wt% of the print feedstock, with the addition ratio for moulded-like surfaces set at 0.10 mm or 0.12 mm layer height on a 0.40 mm nozzle and 100% solid infill at 240°C nozzle temperature and 75°C build plate temperature. The downstream production route is short-run fused filament fabrication for pre-production anatomical fixtures, diagnostic instrument housings, and non-patient-contact tray inserts; patient-contact components are outside the reliable envelope unless the device manufacturer performs tissue-contact evaluation according to ISO 10993-5 and ISO 10993-10 because the filament supplier does not provide a positive cytocompatibility statement for as-printed surfaces. Compliance in this sector is structurally aligned to ISO 13485:2016 for the device manufacturer’s QMS and to Regulation (EU) 2017/745 for CE-marked devices; the raw polymer itself is registered under REACH (EC) No 1907/2006 but is not certified as medical-grade material. The process requires that all spools be dried at 60°C for 4 h before printing in a controlled environment with an ambient particle count below Class 100,000; after printing, parts intended for repeated handling may be coated with a biocompatible clear varnish only after evaluation of the coating–PET adhesion under ISO 2409 cross-cut testing. Terminal products include diagnostic device housing prototypes, non-contact surgical instrument nesting trays, and training simulators; porous printed surfaces must not be used without post-sealing in any environment where microbial contamination is a risk.
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BASF 3D Ultrafuse PET fused filament is a polyethylene terephthalate homopolymer monofilament produced for open-frame fused filament fabrication machines. The product is supplied in 1.75 mm and 2.85 mm diameters on 750 g net-weight spools, vacuum-sealed with desiccant to limit moisture uptake during storage. Published density under ISO 1183-1:2012 is 1.27 g/cm³. The thermal profile obtained by differential scanning calorimetry shows a melting onset near 238 °C and a melting peak near 245 °C under ISO 11357-3. The grade is intended for dimensionally stable technical parts, fixtures, covers, jigs, and functional prototypes where low warpage and moderate service temperature are more important than high-impact toughness. Unlike filled polyester compounds, this feedstock does not require an abrasive-resistant nozzle or a heated build chamber, although a heated platform is required to manage first-layer solidification strain.
Diameter control and spooling are critical because monofilament ovality above 0.05 mm can generate cyclic extruder flow fluctuations in a 0.4 mm nozzle at fixed feed rate. The manufacturer applies closed-loop dual-axis laser micrometry during winding to maintain dimensional consistency. A full-spool run with a 0.20 mm layer height and 40 mm/s print speed therefore produces a more uniform bead than unstabilized PET monofilament. On direct-drive printers, spool drag should remain below 2 N to avoid skipped steps in the extruder gear.
On a standard Cartesian or CoreXY printer with a 0.4 mm brass nozzle, the processing window typically spans an extrusion temperature of 235–250 °C and a build surface temperature of 60–80 °C. Direct-drive extruders can use retraction distances of 1–3 mm, while Bowden configurations may require 4–6 mm to reduce oozing without causing nozzle plugging. Layer heights between 0.10 mm and 0.20 mm with line widths of 0.38–0.45 mm are used for structural specimens. Build surfaces of PEI, polycarbonate, or coated glass at the upper bed-temperature limit improve first-layer peel resistance. On open-frame equipment, warping is lower than unfilled polypropylene or polycarbonate under identical bed adhesives, but published quantitative warp values for this specific filament configuration are limited. A closed chamber is not required, and ambient room conditions of 20–25 °C produce acceptable results when draughts are eliminated.
| Property | Test method | Typical value |
|---|---|---|
| Density | ISO 1183-1:2012 | 1.27 g/cm³ |
| Melting peak | ISO 11357-3 | 245 °C |
| Tensile modulus | ISO 527-2 | 2100 MPa |
| Tensile stress at yield | ISO 527-2 | 49 MPa |
| Nominal strain at break | ISO 527-2 | 16% |
| Flexural modulus | ISO 178 | 2000 MPa |
| Charpy notched impact strength | ISO 179-1 | 4 kJ/m² |
| Heat deflection temperature B | ISO 75-2:2013 | 75 °C |
| Vicat softening temperature A50 | ISO 306:2013 | 78 °C |
The load-bearing temperature boundary is governed by heat deflection temperature and Vicat softening data. Manufacturer-published typical values give heat deflection temperature of 75 °C under 0.45 MPa flexural stress using ISO 75-2:2013 method B and Vicat softening of 78 °C under method A50 of ISO 306:2013. As-printed PET homopolymer therefore should not be specified for continuous mechanical load above 60–65 °C, particularly when the part is constrained by metal fasteners with a higher thermal expansion coefficient. Recrystallization during annealing at 110 °C may raise dimensional stability but can embrittle the amorphous tie-chain network. This distinguishes it from polycarbonate and polysulfone grades, which retain load-bearing capacity above 100 °C under ISO 75-2 method A. Applications involving hot air ducts, underhood brackets, or steam-sterilized medical tools exceed the product’s thermal boundary.
The product also differs from carbon-fibre-reinforced PET grades in that no fibre reinforcement is present. This permits continuous printing with a standard brass nozzle and avoids severe abrasive wear, but it lowers stiffness and creep resistance. A fibre-filled PET filament would typically provide higher tensile modulus and lower thermal expansion, whereas the unfilled homopolymer remains more suitable for translucent parts and geometries where fibre orientation would introduce anisotropic shrinkage.
PET homopolymer is hydrolytically sensitive in extrusion. Moisture absorbed from ambient air reacts with ester linkages during heating, reducing melt viscosity and producing gaseous voids at the nozzle. The manufacturer’s handling instructions recommend drying at 60–65 °C for 4 h in a forced-air oven or filament dryer before printing if the spool has been removed from its sealed package for more than 24 h at 50% RH or higher. After drying, the filament should be held in a sealed desiccant box with a dew point below -30 °C or printed within 8 h in a conditioned room. Failure to dry manifests as intermittent extrusion, splayed first-layer lines, and a reduction in Z-axis tensile strength because vapour bubbles create microvoids between deposited beads. Storage at 15–30 °C and relative humidity below 20% is recommended for unopened spools. Visual transparency of the natural grade does not provide a reliable moisture indicator because haze often develops only after hydrolysis has begun.
Tensile and flexural properties reported by the manufacturer under ISO 527-2 using dried specimens include tensile modulus of 2100 MPa, tensile stress at yield of 49 MPa, nominal strain at break of 16%, flexural modulus of 2000 MPa under ISO 178, and notched Charpy impact strength of 4 kJ/m² under ISO 179-1. These values refer to bulk or well-fused XY-plane samples and do not transfer directly to the interlayer interface. In fused filament fabrication, Z-axis tensile strength is commonly 40–60% of the XY-plane value because incomplete polymer chain diffusion across the weld interface limits the through-thickness load path. Users who require Z-axis certification should generate specimens according to ISO 527-2 type 1BA at the intended layer height, print speed, and chamber conditions, since published data for this specific configuration is limited.
When layer welding is optimized, the natural grade can produce translucent sidewalls, though printed translucency declines with layer height and moisture. Interlayer weld strength is rate-dependent: higher extrusion temperature and lower print speed increase polymer chain interdiffusion across the interface. A nozzle temperature of 250 °C at 30 mm/s generally yields better through-thickness strength than 235 °C at 60 mm/s, but stringing and dimensional softening may increase. Operators should validate the weld factor using a flat tensile bar printed in the Z orientation rather than relying on visual sidewall quality.
The homopolymer backbone differs from glycol-modified PET copolyesters in crystallinity, fusion behaviour, and impact response. PETG filament grades typically incorporate cyclohexanedimethanol at 15–30 mol%, which suppresses crystallinity and produces notched Charpy impact values in the 8–10 kJ/m² range under ISO 179-1. BASF Ultrafuse PET reports a notched Charpy impact average near 4 kJ/m², reflecting the more ordered microstructure. The same ordering gives the homopolymer a higher modulus and better surface hardness after annealing, but it reduces tolerance to sharp radius changes, threaded inserts, and snap-fit deflection. Designers moving from PETG to this product should increase minimum wall thickness or reduce local strain at bosses and living hinges. Conversely, when the design priority is dimensional accuracy across a print run, the homopolymer’s lower die swell and stable viscosity at 235–250 °C tends to produce more consistent bead width than PLA or PETG on open-frame printers.
| Property | BASF Ultrafuse PET | PETG copolymer filament | PLA filament |
|---|---|---|---|
| Tensile modulus | 2100 MPa | 1800–2000 MPa | 3000–3500 MPa |
| Notched Charpy impact | 4 kJ/m² | 8–10 kJ/m² | 3–5 kJ/m² |
| Heat deflection temperature B | 75 °C | 70 °C | 55 °C |
The comparative table lists typical unfilled filament property ranges reported in supplier datasheets. Differences in specimen preparation, printing orientation, and moisture condition prevent direct substitution of these values into finite-element models without converter-specific validation.
Chemical contact data for the BASF Ultrafuse PET grade should be verified using ISO 175:2010 or ASTM D543 immersion protocols, particularly when the printed article is exposed to ketones, chlorinated solvents, concentrated alkalis, or acidic solutions above 40 °C. Polyethylene terephthalate homopolymer generally withstands dilute mineral acids, aliphatic hydrocarbons, and many alcohols at room temperature, but stress cracking can occur in aromatic solvents and strong caustic environments. For food-contact printed parts, converter validation is required because the filament’s raw-material compliance does not automatically extend to the final layer-porous surface. Relevant regulatory frameworks include FDA 21 CFR 177.1630 for PET homopolymers and Regulation (EU) No 10/2011 for plastic food-contact materials; migration testing and cleaning validation must account for layer lines, internal voids, and printer-specific contaminants.
In comparison with ABS, BASF Ultrafuse PET does not generate styrene monomer odour and has better resistance to oils and many weathering agents, but its dry-bed requirement and lower notched impact place it closer to PLA in toughness. Operators should not select this filament for high-speed tooling parts that require service above 80 °C or repetitive impact loading. For such conditions, polycarbonate, ASA, fibre-filled polyamide, or impact-modified copolyester grades may be required depending on the thermal and mechanical demand.