| HS Code | 254587 |
| Material Type | PCTG |
| Density | 1.27 g/cm³ |
| Tensile Strength | 50 MPa |
| Tensile Modulus | 1900 MPa |
| Elongation At Break | 120% |
| Flexural Strength | 75 MPa |
| Flexural Modulus | 2000 MPa |
| Notched Izod Impact Strength | 640 J/m |
| Heat Deflection Temperature At 0 45 Mpa | 75 °C |
| Heat Deflection Temperature At 1 82 Mpa | 65 °C |
| Glass Transition Temperature | 85 °C |
| Print Nozzle Temperature | 240-260 °C |
| Print Bed Temperature | 70-80 °C |
| Diameter | 1.75 mm |
| Diameter Tolerance | ±0.05 mm |
| Spool Weight | 0.75 kg |
| Chemical Resistance | Good |
| Layer Adhesion | Excellent |
| Warping | Low |
As an accredited Essentium PCTG-Z Additive Manufacturing Filament factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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Essentium PCTG-Z Additive Manufacturing Filament is an amorphous, glycol-modified copolyester feedstock for fused filament fabrication. The product is supplied as a natural transparent monofilament in 1.75 mm and 2.85 mm diameters on 750 g spools. The polymer backbone is a terephthalate copolyester containing cyclohexanedimethanol; this substitution inhibits crystallization and produces a material with lower retained residual stress than semicrystalline polyester alternatives. The amorphous morphology is relevant to part performance because it permits deep interlayer diffusion without the crystallization-rate limitations that affect PET and PLA. The glass transition temperature of PCTG-class resins places the service ceiling above PETG and below polycarbonate, while the melt viscosity remains low enough for use on conventional direct-drive and Bowden extruders.
Compared with PETG, the higher cyclohexanedimethanol content in PCTG shifts the glass transition and reduces the tendency for strain-induced crystallization at the nozzle. This difference is observed on large flat parts as reduced plate-side curl and as more uniform filament diameter after retraction. Published data for the exact Z formulation are limited; however, the manufacturer positions the Z designation as a processing variant with lower residual stress accumulation and improved interlayer fusion relative to standard PCTG. Operators should confirm the current datasheet for the specific lot because pigment and regrind levels can move the crystallization onset and melt flow rate.
Against unmodified PCTG, the primary practical difference claimed for the Z grade is a broader temperature window between the onset of melt flow and the onset of thermal degradation. In production terms, that window reduces the frequency of cold-layer delamination on thin-walled parts and permits higher volumetric throughput before the extruder motor current becomes unstable. The material should not be treated as a direct drop-in replacement for PETG in all fixtures, because its thermal expansion and solvent response differ enough to require revalidation of interference fits and chemical cleaning protocols.
Fluid-contact manifolds, valve bodies, and custom pump housings are prepared from PCTG-Z when service conditions include dilute acids, alcohols, or aliphatic hydrocarbons. The copolyester backbone exhibits better hydrolysis resistance than amorphous PLA and lower environmental stress cracking than acrylic in the presence of isopropanol. The upper continuous-use temperature remains below the glass transition; exposure above 65 °C under load can produce creep in threaded connections and compression fittings. Aromatic solvents, ketones, and chlorinated hydrocarbons may plasticize or craze the material, so compatibility testing according to ASTM D543 is required before any process fluid is approved.
Moisture absorption by PCTG is lower than that of polyamide but sufficient to generate hydrolytic degradation at melt temperature. Before processing, the filament should be dried at 65 °C for 4 h to 6 h in a forced-air or vacuum dryer. At ambient relative humidity above 60%, a dry-box feed with desiccant or an active dew-point controller set below -20 °C is recommended for continuous operation. Injection-molded copolyester data show that moisture contents above 0.03% by weight reduce melt strength and produce surface splay; in fused filament fabrication, the equivalent defects are bubble formation, nozzle drool, and weak layer boundaries.
Storage of partially used spools should be in sealed containers with fresh desiccant. If a spool has been exposed to ambient air for more than 24 h in an uncontrolled print cell, drying is repeated before returning to service. Drying temperature must not exceed 75 °C because spool deformation and filament tacking may occur above that range.
Extrusion of PCTG-Z is typically performed between 240 °C and 270 °C, with the higher end reserved for large nozzles and high volumetric rates. Build plate temperature is normally set at 70 °C to 80 °C on glass, polyetherimide, or carbon-fiber-reinforced build surfaces. Small sections below 100 mm may be printed on unheated flexible polyester build sheets if a copolyester-compatible primer is applied and the chamber is shielded from drafts.
For a 0.4 mm nozzle, the practical upper volumetric throughput is near 12 mm³/s. Above this rate, the residence time in the nozzle is insufficient for molecular diffusion across the layer interface, and the resulting part shows reduced transverse tensile strength. Wall thickness should be kept above 1.2 mm for pressure-bearing fluid parts; the perimeter count and infill density are then selected to maintain a continuous fused shell rather than a porous core. Layer heights from 0.10 mm to 0.25 mm are acceptable, but the deviation from nominal filament diameter should be monitored with a laser micrometer because ovality above 0.05 mm produces downstream flow-rate variation on Bowden systems.
Chemical resistance of PCTG is method-dependent rather than universal. In laboratory immersion tests, the material generally retains tensile strength after short-term exposure to dilute mineral acids and to aliphatic hydrocarbon fluids, but this does not imply compatibility with continuous solvent contact. Environmental stress cracking can occur when a stressed printed part is exposed to isopropanol, certain glycol ethers, or aggressive cleaning agents. Cracking is accelerated by residual stress at sharp corner radii and by excessive extrusion temperature that builds thermal contraction strain into the part.
Post-processing by machining is possible after printing, but the amorphous copolyester softens at relatively low cutting forces. Flood cooling should be avoided if the coolant contains ketones or aromatic solvents. Vapor polishing is not recommended because the solvent classes capable of smoothing the surface are also capable of inducing stress cracking. Annealing of PCTG-Z is generally less effective than annealing of PLA or semicrystalline polymers because the material does not crystallize to a significant extent; extended thermal cycling may only relieve a portion of the frozen-in orientation stress.
The following table summarizes manufacturer-published typical values for dried, unannealed PCTG-Z filament printed in the horizontal build orientation. Values are derived from a standard tensile bar rather than a production part geometry.
| Property | Test method | Typical value |
|---|---|---|
| Density | ASTM D792 | 1.23 g/cm³ |
| Tensile strength at yield | ASTM D638 | 50 MPa |
| Tensile modulus | ASTM D638 | 1600 MPa |
| Elongation at break | ASTM D638 | >150% |
| Flexural strength | ASTM D790 | 70 MPa |
| Flexural modulus | ASTM D790 | 1500 MPa |
| Notched Izod impact at 23 °C | ASTM D256 | 650 J/m |
| Heat deflection temperature at 0.455 MPa | ASTM D648 | 70 °C |
| Melt volume-flow rate at 230 °C, 2.16 kg | ASTM D1238 | 20 cm³/10 min |
| Water absorption, 24 h | ASTM D570 | 0.2% |
In production AM cells using direct-drive extruders with hardened steel nozzles, PCTG-Z runs at lower extruder motor current than polycarbonate and produces less plate-side curl than PETG on unheated perimeter zones. Batch-to-batch diameter variation is controlled through in-line laser measurement; operators should still verify ovality at spool changeover and record melt temperature during the first purge because thermistor calibration varies between printer brands. When a print farm transitions from PETG to PCTG-Z, the existing purge routine should be extended by at least 200 mm of filament or until the purge becomes optically clear, because cross-contamination with degraded PETG can create interfacial delamination in the next part.
Essentium supplies PCTG-Z with lot-level diameter and ovality data. For food-contact or skin-contact use, the base copolyester may meet certain requirements under FDA 21 CFR 177.1315 and EU Regulation No 10/2011, but the printed article must be evaluated separately. Fused filament fabrication introduces surface roughness, internal voids, and possible decomposition products at the nozzle; these factors are not addressed by raw-resin compliance statements.
Traceability documentation should retain the spool lot number, dryer temperature log, and hot-end temperature profile for each regulated part. If colorant masterbatch is added to natural PCTG-Z, the compliance status changes, and the full mixture must be reassessed under the intended use condition. Electrical and electronic applications are evaluated under RoHS 3 (EU 2015/863) for restricted substances, but the user is responsible for confirming that the final printed component meets any additional OEM-specific volatile organic compound limits.
The operational boundary for PCTG-Z is defined by temperature, solvent exposure, and sustained load. The material should not be used for load-bearing parts that exceed 60 °C in continuous service unless creep testing under ISO 899-1 has been performed. It is also unsuitable for direct contact with strong alkalis, ketones, esters, and chlorinated hydrocarbons. When a production application approaches these limits, published data for the specific configuration are limited and end-use validation under the relevant ASTM or ISO method is required.