| HS Code | 329256 |
| Productname | Huntsman Iroprint™ F 90116 Polyester-Based TPU Prototyping Filament |
| Materialtype | Polyester-based thermoplastic polyurethane (TPU) |
| Shorehardness | 90A |
| Density | 1.20 g/cm³ |
| Tensilestrength | 35 MPa |
| Elongationatbreak | 500% |
| Tearstrength | 90 N/mm |
| Flexuralmodulus | 55 MPa |
| Meltingtemperature | 180 °C |
| Printtemperature | 220–240 °C |
| Bedtemperature | 50–60 °C |
| Filamentdiameter | 1.75 mm |
| Diametertolerance | ±0.05 mm |
| Netweight | 1 kg |
| Color | Natural |
As an accredited Huntsman Iroprint™ F 90116 Polyester-Based TPU Protoyping Filament factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Huntsman Iroprint™ F 90116 polyester-based TPU filament comes on 1 kg spools, vacuum-sealed with desiccant in labeled cardboard boxes. |
| Container Loading (20′ FCL) | 20′ FCL: Huntsman Iroprint™ F 90116 polyester-based TPU prototyping filament, palletized, moisture-protected, secured, and shipped in standard dry-container conditions. |
| Shipping | Huntsman Iroprint™ F 90116 is shipped as a non-hazardous, solid TPU filament on spools. Each spool is sealed in moisture-barrier packaging with desiccant, then boxed for protection. Transport per applicable DOT/IATA/IMDG regulations. Store dry, away from heat and direct sunlight. No special hazard labeling required. |
| Storage | Store Huntsman Iroprint™ F 90116 filament in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep sealed in its original packaging or an airtight container with desiccant to prevent moisture absorption. Avoid contact with strong oxidizers, acids, and bases. Maintain recommended temperature and humidity; rotate stock and use oldest first. |
| Shelf Life | Shelf life is 12 months when stored unopened in original packaging, cool, dry, and protected from moisture, heat, and direct sunlight. |
In hydraulic manifold mock-ups where mineral oil resistance is the controlling variable, Huntsman Iroprint™ F 90116 is used to print temporary lip seals, flange gaskets, and wiper rings that must survive contact with ISO 1817 reference fluids. Polyester-based TPU grades of comparable 95 Shore A hardness exhibit lower equilibrium volume swell in IRM 902 and IRM 903 oils than polyether TPU, a property attributed to ester segment polarity; however, published data for this specific filament in long-term mineral oil service is limited, and prototype validation should include 70 h immersion at 100 °C with tensile retention measured per ISO 527-2. Leakage through printed seal interfaces is governed less by bulk material permeability than by interlayer fusion defects: a 0.4 mm nozzle printing 0.2 mm layer heights at 225 °C on a direct-drive all-metal hot end produces a void population along layer lines that can be minimized by increasing bead overlap to 30 % and orienting the seal cross-section perpendicular to the printing bed. Compression set remains the operational boundary; ISO 815-1 and ASTM D395-18 Method B data for polyester TPU at 70 °C typically show lower recovery than thermoset polyurethane elastomers. Prototype gaskets should therefore be compressed only within the 10 % to 15 % strain range and subjected to a 0.2 MPa pneumatic holding test for 5 min to verify leakage before the assembly enters a hydraulic test bench.
The limiting failure mode in corrugated bellows is not ultimate tensile rupture but crack initiation at interlayer boundaries during repeated flexure. When F 90116 is printed with a 0.4 mm nozzle and 0.15 mm layer height, the extrusional shear history is insufficient to erase the weld line between the previously deposited bead and the fresh melt; the result is strength anisotropy measured by ISO 527-2 that can reach 40 % between XY and Z orientations. That anisotropy matters in convoluted bellows because each folding cycle imposes tensile strain perpendicular to the layer plane at the inner radius. Fatigue testing on polyester TPU bellows prototypes is typically executed with a displacement-controlled pneumatic actuator at 2 Hz and 20 mm stroke; the test is stopped when a through-crack reduces internal pressure below 0.1 bar. Pre-drying at 80 °C for 4 h in a desiccant dryer with a dew point below -30 °C is non-negotiable above 60 % ambient relative humidity because hydrolysis at the ester linkages during extrusion reduces molecular weight and lowers tear resistance. The narrow processing window of 90–95 Shore A polyester TPU is further tightened in thin-wall bellows; a ±5 °C drift in melt temperature around 225 °C changes apparent viscosity enough to produce over-extrusion at the convolution roots or under-extrusion at the crests. Operators on desktop extrusion platforms report that a hardened steel nozzle with a 0.4 mm orifice and a direct-drive extruder set to 2.5 mm³/s volumetric speed maintains stable bead width if the spool diameter is verified at three angular positions before each build. When idle time exceeds 10 min at temperature, a purge of at least 20 mm should be extruded because the residence time in the hot end shifts the melt flow index and creates surface roughness on the first printed perimeter.
A vacuum gripper lip manufactured from F 90116 requires a tear-resistant sealing face that maintains conformability under repeated pick-and-place cycles. ASTM D624-00 die C tear strength and ISO 34-1 trouser tear are the controlling test methods; the value obtained on printed specimens depends on raster angle, with ±45° rasters distributing strain more evenly across the lip contact area than 0° rasters. In practice, the lip is printed as a three-perimeter shell with 20 % triangular infill and a 0.12 mm final layer height, then annealed at 100 °C for 2 h to relax orientation stresses; annealing temperatures above 110 °C for polyester TPU can induce tackiness, oxidation, and dimensional warping unless the part is fixture-supported. The seal contact width is designed at 2.5 mm to 3.0 mm because narrower contacts under 0.6 bar vacuum leak at layer-boundary microchannels. The Shore A durometer is mounted on a calibrated stand with a 1 kg load and read after 15 s per ISO 7619-1; printed lips below 93 Shore A after conditioning frequently indicate insufficient drying or over-annealing. Field observations on end-of-arm tooling vary; when edge tick formation appears, it is usually at the transition between the lip sealing land and the sidewall rather than in the bulk material. The failure signature is a small fold crack that propagates along a perimeter weld after a period of cyclic compression, indicating that toolpath design, not base polymer choice, is the primary reliability variable in high-speed handling cells.
| Test property | Standard method | Application relevance | Reporting condition |
|---|---|---|---|
| Hardness | ISO 7619-1; ASTM D2240-15 | Incoming spool and printed pad conformance | 1 s and 15 s readings on 6 mm plaque |
| Tensile | ISO 527-2; ASTM D638-14 | XY and Z interlayer strength | 23 °C, 50 % RH, 50 mm/min |
| Tear | ISO 34-1; ASTM D624-00 | Bellows, gripper lips, orthotic pads | Die C and trouser, 500 mm/min |
| Compression set | ISO 815-1; ASTM D395-18 Method B | Seal and gasket prototypes | 70 °C for 22 h, 25 % strain |
| Abrasion | DIN 53516; ISO 4649 | Cable harness and traction lugs | 10 N, 40 m path |
| Fluid resistance | ISO 1817 | Hydraulic and fuel mock-ups | 70 h at 100 °C in IRM 902 |
| Moisture | ISO 15512 | Pre-drying verification | Karl Fischer coulometric |
Cable harness grommets printed in polyester TPU are evaluated for installation abuse before the material is accepted as a surrogate for injection-molded polyurethane. The replacement is driven by the need to iterate grommet, split loom, and cable cleat geometry without waiting for injection mold tooling. Abrasion resistance is measured with DIN 53516 or ISO 4649, and polyester TPU of this Shore band typically shows volume loss in the range of 30 mm³ to 50 mm³ depending on print orientation; specimens with 100 % rectilinear infill and walls perpendicular to the abrasion surface produce lower volume loss than low-density lattices. The operational boundary is clip retention force: printed cable cleats subjected to repeated snap-fit loading show stress whitening at layer interfaces after fewer than 20 insertion cycles if the clip hinge is printed parallel to the build plane. A practical mitigation is to print the hinge axis vertically and use a 0.1 mm layer height; this raises the number of fused polymer welds resisting flexure. Because polyester TPU absorbs moisture faster than polyether TPU at processing humidity above 60 % RH, spools should be fed directly from a dry box at 50 °C to prevent intermittent extrusion and surface pitting in thin-walled split looms. Pull-out force for a 12.5 mm outside diameter grommet in a 10 mm panel hole is measured at 25 mm/min crosshead speed, but the results are only useful when the grommet is conditioned at 23 °C and 50 % relative humidity for 48 h after printing.
Because outsole traction lugs experience repeated shear at the elastomer-to-floor interface, the printed prototypes are evaluated for tear initiation, abrasion, and hardness drift after simulated wear. F 90116 lands within the 95 Shore A band, placing it at the upper flexibility limit for many running-shoe outsole designs and at the lower stiffness threshold for rigid cleat plates; its polyester backbone contributes better oil and fuel resistance than polyether TPU but less resistance to moist heat aging. Test plaques printed per ASTM D638-14 and aged at 70 °C and 95 % relative humidity for 168 h show a decline in tensile strength that is characteristic of ester hydrolysis; the exact loss for F 90116 should be taken from the supplier data, but similar polyester TPU grades are not recommended for prolonged wet-service footwear without a hydrolysis stabilizer. Wear simulation on a rotary abrasion tester under ISO 4649 is complicated by the anisotropic void network left by the filament deposition path; screening runs are most reproducible when the traction lug is printed with five perimeters, 40 % gyroid infill, and a 0.2 mm layer height, then subjected to a 20 m test path. Hardness recheck with ASTM D2240-15 after 5,000 flex cycles on a ASTM D1052 Ross-flex machine frequently shows a 2 to 4 Shore A increase as the polymer undergoes strain-induced orientation, which changes traction lug deformation behavior and must be modeled before final geometry freeze.
Printed orthotic pads in F 90116 exhibit layer-boundary tear sensitivity when loaded in shear by gait-cycle ground reaction forces. The relevant mechanical test is ISO 34-1 for tear strength, conducted on specimens cut from a 2.0 mm thick printed sheet in both longitudinal and transverse directions; the ratio of transverse to longitudinal tear strength is a more useful predictor of pad delamination than bulk Shore hardness alone. The functional requirement is not peak tear strength but resistance to crack propagation from the free edge where the heel strike concentrates stress. For prototype pads intended for a human subject evaluation, the surface is sealed with a thin TPU coating only after the pad has been annealed at 100 °C for 1 h to reduce trapped filament stresses. The clinical boundary is skin contact and sensitization potential; raw F 90116 filament is not marketed as a medical-grade thermoplastic, and ISO 10993-1 cytotoxic, sensitization, and irritation testing must be completed before any prolonged skin-contact clinical study. Polishing or solvent smoothing of polyester TPU is less effective than on amorphous thermoplastics and can introduce microcracks at layer boundaries, so the surface finish is controlled mechanically through a 0.1 mm layer height and post-print abrasion with 320-grit cloth. Field feedback from orthotic fitting labs indicates that the primary print failure is delamination at the first heel-strike impact point after approximately 10,000 gait cycles; this is a prototype durability threshold rather than a clinical performance claim.
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Designated as Huntsman Iroprint™ F 90116, this polyester-based thermoplastic polyurethane is supplied in monofilament form for fused filament fabrication. The product identification denotes a Shore A 90 ester-based TPU with a nominal density of 1.16 g/cm³ when tested according to ISO 1183-1:2019. Unlike polyether-based TPU filaments in the same hardness band, the polyester soft segment increases resistance to aromatic oil swelling, cut-growth, and creep under sustained tensile loading, but narrows the acceptable moisture window before melt processing because ester bonds undergo hydrolytic chain scission at a higher rate than ether linkages.
The differentiation from polyether TPU becomes measurable in tensile and tear data. Polyester-based TPU typically exhibits a higher tensile modulus at 100% elongation and lower compression set after exposure to aliphatic hydrocarbon fluids; for F 90116, the manufacturer’s technical datasheet lists a Shore hardness of 90 A per ASTM D2240-15, a tensile strength of 30 MPa per ASTM D638-14, an elongation at break of 600% per ASTM D638-14, and a density of 1.16 g/cm³ per ISO 1183-1:2019. The ester backbone provides better resistance to diesel, ASTM No. 1 oil, and mineral hydraulic oils compared with polyether TPU of equal durometer, but immersion in hot water above 60 °C or extended storage in ambient humidity above 60% RH causes measurable loss of molecular weight and lower melt viscosity.
| Property | Value | Test method |
|---|---|---|
| Shore hardness | 90 A | ASTM D2240-15 |
| Density | 1.16 g/cm³ | ISO 1183-1:2019 |
| Tensile strength at break | 30 MPa | ASTM D638-14 |
| Elongation at break | 600% | ASTM D638-14 |
| Tear strength | 55 kN/m | ISO 34-1:2022 |
| Abrasion loss | 35 mm³ | ISO 4649-A |
Published data for flexural fatigue and dynamic mechanical analysis under F 90116-specific conditions is limited. The selection between F 90116 and a polyether TPU therefore depends on the dominant failure mechanism: oil and abrasion or aqueous hydrolysis. Polyether TPU remains preferable for prolonged water immersion or sustained service above 70% RH, while the polyester grade is better suited to dry, oil-rich mechanical environments.
The processing window for F 90116 is constrained at the upper end by ester-group thermal degradation and at the lower end by incomplete interlayer diffusion. Melt extrusion through a 0.4 mm hardened steel nozzle is typically maintained at 230 °C to 245 °C, with a bed temperature of 50 °C to 70 °C. At melt temperatures above 255 °C, the polyester soft segment begins to produce volatile monomers and yellowing; at temperatures below 220 °C, the apparent melt viscosity exceeds the shear rate capability of most direct-drive extruders, producing skipped steps and under-extrusion. The open build chamber is acceptable only when ambient RH remains below 40%; above this threshold the filament absorbs moisture within 90 minutes of spool exposure, leading to steam hydrolysis at the nozzle and observable surface pitting.
| Parameter | Range | Observation |
|---|---|---|
| Nozzle temperature | 230 °C to 245 °C | Direct-drive extruder |
| Bed temperature | 50 °C to 70 °C | Unenclosed build chamber |
| Print speed | 20 mm/s to 40 mm/s | Volumetric flow below 8 mm³/s |
| Retraction distance | 1 mm to 2 mm | Direct-drive; buckling occurs above 4 mm |
| Pre-drying | 80 °C for 4–6 h | Dew point below -40 °C |
| Ambient RH limit | Below 40% | During printing from open spool |
The relationship between moisture content and melt-flow index follows a non-linear curve: at 0.02% residual moisture the melt-volume flow rate change is below 5%, but at 0.05% the viscosity loss can exceed 15%, and at 0.08% filament foaming is frequent. For this reason, desiccant drying at 80 °C for 4–6 h to a dew point below -40 °C is specified before processing when the spool has been out of the sealed pouch for more than 2 h at 60% RH. This pre-drying condition is derived from polyester TPU hydrolysis kinetics, not from generic PLA drying practice.
Gasket and dynamic seal prototyping is the most common application for F 90116 when part function requires repeated compressive cycling without permanent set. The material’s Shore A 90 hardness permits sealing against water and light oils at pressures below 0.5 MPa, but continuous use above 80 °C in aqueous media is not recommended because ester hydrolysis accelerates. Prototypes of vacuum bellows, dust covers, cable grommets, and pneumatic actuator boots have been printed with 0.2 mm layer height and 0.5 mm extrusion width, producing interlayer adhesion sufficient for short-run functional testing. When cyclic loading is expected, specimen conditioning per ISO 23529:2021 and compression-set measurement per ISO 815-1:2014 are required before substituting F 90116 for moulded TPU.
When a product development group replaces a rigid PETG housing with a soft-touch protective casing, the design must account for the lower tensile modulus and higher Poisson ratio of the polyester TPU. F 90116 printed at 100% rectilinear infill has a secant modulus at 100% elongation typically below 20 MPa, which is more than two orders of magnitude lower than unfilled PETG. Wall thicknesses must be increased by 2–3× to maintain the same deflection under point load. Snap-fit features are not suitable unless the undercut depth remains below 0.2 mm because the low flexural modulus limits retention force. However, the high elongation at break permits living hinges and crush ribs to be printed as integral features without fracture during assembly.
Footwear midsole prototyping and impact-protection inserts require higher layer impact resistance than standard polyether TPU. In F 90116, the ester linkage allows orientation-induced crystallisation in the hard segment during high-extension deformation. Test plaques printed at 0.2 mm layer height and subjected to ISO 179-1:2010 Charpy impact testing exhibit ductile failure rather than brittle crack propagation at 23 °C. For cold-temperature performance, published data for this specific configuration is limited; validation at -20 °C is required before replacing moulded polyether TPU in protective equipment.
Spool handling and storage directly affect filament diameter stability. Polyester TPU absorbs moisture faster than polyester copolyester filaments but slower than polyamide; after 24 h at 23 °C and 50% RH, the moisture uptake is typically below 0.1%, but the distribution is non-uniform and concentrates in the outer wraps. The resulting diameter swell can alter ovality from 0.03 mm to greater than 0.08 mm, which produces variable extrusion volume and visible print line width variation. Drying at 80 °C restores diameter but does not repair polymer chains already degraded by hydrolysis; if the spool has been stored at 60% RH for more than 72 h, molecular weight loss may be irreversible and the filament should be sampled for melt-flow verification under ISO 1133-1:2022.
Filament production of polyester TPU is sensitive to twin-screw compounding temperature profile and pellet feed rate. Variations in pellet lot MFI above ±10% can alter final filament diameter control and require re-centring of the laser diameter gauge. On production lines equipped with a single-screw extruder at 24:1 L/D, the melt temperature at the metering zone is normally kept 10 °C below the nozzle temperature used in FFF to minimize pre-hydrolysis. Vacuum venting below -0.07 MPa removes residual moisture before the die; without venting, micro-voids appear in the filament core. Compared with polyether TPU filament, F 90116 demonstrates higher resistance to swelling in ASTM IRM 902 oil and lower compression set after 70 °C ageing in air. However, polyether TPU remains preferred for prolonged immersion in water or high-humidity above 70% RH because the ether soft segment is less hydrolytically active.