| HS Code | 903443 |
| Productname | Ensinger TECAFIL PES natural - 1,75 mm - Filament Polyethersulfone |
| Manufacturer | Ensinger |
| Material | Polyethersulfone (PES) |
| Color | Natural |
| Filamentdiameter | 1.75 mm |
| Density | 1.37 g/cm³ |
| Glasstransitiontemperature | 225 °C |
| Heatdeflectiontemperature | 203 °C at 1.8 MPa |
| Continuousservicetemperature | 180 °C |
| Tensilestrength | 90 MPa |
| Tensilemodulus | 2700 MPa |
| Elongationatbreak | 20-30% |
| Waterabsorption | 0.7% after 24 h |
| Nozzletemperature | 350-390 °C |
| Bedtemperature | 160-180 °C |
| Dryingtemperature | 150 °C |
| Dryingtime | 4 h |
| Chemicalresistance | Good against acids, bases, and hydrocarbons |
| Flammability | UL94 V-0 |
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Ensinger TECAFIL PES natural – 1.75 mm – Filament Polyethersulfone is an unfilled polyethersulfone monofilament produced for fused filament fabrication of high-temperature thermoplastic components. The “natural” grade designation indicates an unpigmented, transparent amber appearance; the polymer backbone contains alternating ether and sulfone linkages, giving the material an amorphous morphology and a high glass-transition temperature. The filament is specified at a nominal diameter of 1.75 mm with a manufacturer datasheet diameter tolerance of ±0.05 mm. Published density for the PES grade is 1.37 g/cm³ to ISO 1183-1. Glass transition temperature is typically reported at 225 °C by differential scanning calorimetry to ISO 11357-2. Typical mechanical values reported for the base polymer or filament according to ISO 527-2 include tensile modulus near 2,800 MPa, tensile stress at break near 85 MPa, and elongation at break near 6%. Heat deflection temperature under 1.8 MPa is reported near 205 °C to ISO 75-2, and Vicat softening temperature is reported near 215 °C to ISO 306. The amorphous character reduces crystalline shrinkage relative to PEEK or polyamide, but melt processing must be controlled to avoid thermal degradation and residual stress.
Moisture absorption at saturation is approximately 2.1% by weight when tested to ISO 62 at 23 °C. The filament should not be considered process-ready from a newly opened spool unless the package contains desiccant and a vacuum barrier; after exposure to ambient air at relative humidity above 60%, pre-drying is required. Residual moisture above 0.02 wt% entering the hot end can hydrolytically degrade the sulfone backbone and produce gas voids, splay, and reduced interlayer weld strength. The glass-transition temperature of 225 °C defines the lower boundary for chamber and bed heating, while the upper boundary is set by discoloration, gel formation, and crosslinking when melt temperature exceeds 380 °C for extended residence. The unfilled grade has a reported tensile modulus near 2,800 MPa and tensile stress at break near 85 MPa to ISO 527-2; these values apply to conditioned test specimens and may shift downward in printed parts with incomplete interlayer fusion. Hardness, abrasion resistance, and long-term creep data for printed PES are less complete than injection-molded reference data, so load-bearing designs should use injection-molded PES datasheets as conservative starting points whenever printed-part validation has not been performed.
Because the material is amorphous, drying conditions must be more aggressive than those used for PLA or PETG but are comparable to PEI and polycarbonate. Water removal occurs by diffusion through the filament cross-section, so pre-drying at 150 °C for 4 h to 6 h in a desiccant dryer with a dew point below -30 °C is recommended for filament spools. Circulating-air ovens can be used only if the spool is loosely wound or if the spool is rotated to expose the filament surface uniformly; dense spools may require 6 h or longer because the diffusion path length is set by the winding depth rather than the 1.75 mm filament diameter. After drying, spools should be transferred to a sealed feed box purged with dry air or nitrogen and maintained below 20% RH at 25 °C during printing. A spool left in ambient air at 50% RH can regain enough surface moisture within a few hours to produce cosmetic splay and weak layer adhesion, which is a stricter handling requirement than for many lower-temperature filaments.
For PES, the processing window is narrow and thermal homogeneity across the build volume is critical. Extrusion-based FFF requires an all-metal hot end rated to at least 400 °C, with nozzle temperature set between 360 °C and 380 °C. Build chamber temperature should be held at 120 °C minimum, with 140 °C preferred for larger parts; bed temperature is normally 140 °C to 160 °C. Layer heights from 0.10 mm to 0.20 mm and print speeds from 20 mm/s to 40 mm/s are used, with volumetric flow limited to avoid excessive shear heating. At chamber temperatures below 120 °C, the high glass transition produces steep thermal gradients through the part, leading to edge lifting, corner curl, and interlayer delamination. In production-scale filament extrusion, the melt temperature profile is typically zoned from 340 °C at the feed throat to 360–370 °C at the metering zone and die, with melt pressure held stable by closed-loop diameter gauging and haul-off tension. On single-screw filament extrusion lines with L/D ≥ 24:1, melt-temperature overshoot or excessive backpressure can produce diameter wander and surface microvoiding; closed-loop laser diameter control is used to maintain ±0.05 mm tolerance.
Interlayer failure in PES is primarily a consequence of insufficient local polymer diffusion across the weld plane. The weld temperature must remain above the glass transition for enough time to allow chain interdiffusion, but the high melt viscosity of PES limits molecular mobility at temperatures just above 225 °C. Raising nozzle temperature beyond 380 °C can reduce melt viscosity, but it also accelerates thermal degradation and crosslinking. The processing compromise is to operate at 360–380 °C, use a high-temperature chamber, and minimize layer cooling time by disabling part-cooling fans or by using a controlled low-volume fan only for small features. Residual stress is also influenced by part geometry: abrupt thickness changes, sharp corners, and large planar areas increase delamination risk because differential shrinkage concentrates tensile stress at the interlayer boundary. When PES is printed on open-bed machines without a chamber, published data for reliable large-part fabrication is limited because the required ambient temperature cannot be maintained.
Printing support structures for PES require separate consideration. Soluble supports that dissolve in alkaline water may not survive the 140 °C chamber temperature, and some support materials may be attacked by PES processing temperatures. Breakaway supports printed from PES or from a high-temperature modified polysulfone are generally more practical. If support material is left in place during annealing, thermal expansion differences can distort thin walls; supports should therefore be removed before post-printing thermal treatment unless the support material has been verified for matched thermal expansion.
Compared with polysulfone, TECAFIL PES natural raises the glass transition by about 35 °C and improves stiffness and high-temperature load-bearing capacity, but it also raises nozzle and chamber setpoints and reduces notched impact strength. Published PSU values typically place glass transition near 190 °C and heat deflection temperature near 170 °C, whereas PES is reported at 225 °C and 205 °C respectively. PPSU has a similar glass transition but significantly higher notched impact and better resistance to repeated steam autoclaving; PES may be selected when higher modulus or creep resistance is required, but sharp corners and notches should be designed with larger radii because PES is notch-sensitive. PEI is the closest processing analogue, with typical nozzle temperatures near 350–370 °C and chamber temperatures above 120 °C; PES offers a similar processing envelope and can replace PEI when sulfone-based chemical resistance or different transparency is required. Compared with PEEK, PES does not require crystallization management and can be processed at a lower nozzle temperature, but PEEK retains superior continuous-use temperature, fatigue resistance, and chemical resistance. The absence of a crystalline melting point in PES means that solidification occurs by vitrification rather than crystallization, so warpage is lower than PEEK but stress relaxation and solvent sensitivity must still be controlled.
Material substitution should be based on operating temperature, chemical exposure, mechanical load, and sterilization requirement. PES is a candidate for short-run high-temperature fixtures, autoclave-tolerant guides, electronic test sockets, and under-hood covers where printed geometry must retain stiffness above 150 °C. It should not be selected for applications requiring high notched impact at room temperature or for contact with polar aprotic solvents. When replacing PEI with PES, the chamber and bed settings are similar, but PES may require longer drying and more careful support removal because of its moisture uptake and notch sensitivity. When replacing PSU with PES, the higher glass transition extends the upper use temperature but narrows the processing window and increases the probability of stress-cracking if residual thermal stress is not annealed. Published data for this specific configuration in cyclic load-bearing FFF applications is limited; performance must be verified with printed test coupons under the expected thermal and chemical service conditions.
Printed PES parts can be annealed at 180 °C for 2 h in an air-circulating oven; the parts should be supported and heated slowly to avoid distortion. The grade has hydrolytic resistance at elevated temperature and is generally compatible with 134 °C steam autoclave cycles, but published data for the specific performance of FFF parts after repeated sterilization is limited. Microvoids and interlayer weld lines may reduce sterilization robustness compared with injection-molded PES, especially if the printed part contains under-extruded regions or poor layer bonding. The material resists many aqueous acids, bases, and aliphatic hydrocarbons, but polar aprotic solvents such as N-methyl-2-pyrrolidone, dimethylformamide, and dimethyl sulfoxide, chlorinated hydrocarbons such as methylene chloride, and ketones such as acetone and methyl ethyl ketone cause swelling or stress-cracking, particularly under residual thermal stress. PES should not be assembled with aggressive solvent-borne adhesives or cleaned with ketone-based solvents unless compatibility has been verified with the specific part geometry and loading.