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Ensinger TECAFIL PPSU natural - 1,75 mm - Filament Polyphenylsulfone

    • Название продукта: Ensinger TECAFIL PPSU natural - 1,75 mm - Filament Polyphenylsulfone
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
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    • Производитель: Ascent Petrochem Holdings Co., Limited
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    Код ТН ВЭД 842478

    Как аккредитованный завод Ensinger TECAFIL PPSU натурального - 1,75 мм - полифенилсульфона, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

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    Применение Ensinger TECAFIL PPSU натуральный - 1,75 мм - Нитка Полифенилсульфон

    For short-run custom surgical instrumentation and diagnostic device enclosure parts produced from TECAFIL PPSU natural 1.75 mm filament, the selection pathway depends on retention of interlayer adhesion after repeated steam sterilisation and on the absence of mineral fillers that could raise surface roughness in contact areas. The material composition in the final article is 100 % unfilled polyphenylsulfone by mass; no colourant, plasticiser, impact modifier, or processing aid is introduced downstream, and the only pre-build variable is residual moisture, which is driven below 0.05 % by drying at 150 °C for a minimum of 4 h in a closed-loop desiccant dryer. The relevant compliance framework includes ISO 17665-1:2006 for moist-heat sterilisation validation, ISO 10993-1:2018 for biological evaluation of limited-contact instruments, ISO 13485:2016 for quality management across the build record, and USP <88> Class VI where the manufacturer holds supporting data for systemic injection and intracutaneous reactivity of the base resin. A documented build specification for non-implantable instrument handles, retractor body shells, endoscopic camera adapters, and sterilisation tray dividers uses layer heights between 0.10 mm and 0.15 mm, 100 % solid infill, 4 perimeter walls, a nozzle temperature of 360–400 °C, a bed temperature of 160–190 °C, and an actively heated chamber held above 120 °C to suppress edge curl. The production process is FFF with a high-temperature all-metal hot end rated for continuous operation at 450 °C, a hardened steel nozzle aperture of 0.4 mm, and a direct-drive extruder mounted outside the chamber to avoid motor overheating. Post-print annealing at 170–200 °C in a circulating-air oven for 2 h and slow cooling at ≤0.5 °C/min through the 220 °C glass-transition region reduce residual stress and improve resistance to steam-penetration microcracking. The documented limiting condition is that repeated autoclave cycling above 134 °C may progressively release frozen-in orientation stresses if annealing is incomplete. Batch-to-batch filament ovality greater than ±0.05 mm around the nominal 1.75 mm diameter produces measurable melt-pressure fluctuation and localised under-extrusion in narrow-wall sections. No statements are made for permanent implantable use; components intended for long-term tissue contact require separate regulatory qualification under the intended device classification.

    What Changes When FFF PPSU Brackets Must Satisfy 14 CFR §25.853(a) and OSU 65/65 Heat Release Limits?

    In aircraft interior components printed from unfilled PPSU filament, the certifiable target is not merely short-term tensile strength but the combined response of low heat release and low smoke emission when the material is exposed to radiant heat. The feedstock utilisation ratio is 100 % PPSU by mass after breakaway support removal; the natural 1.75 mm filament contains no halogenated flame retardant, no antimony synergist, and no carbon filler, so the burn behaviour is a property of the polymer backbone rather than a formulated additive package. The relevant test matrix includes 14 CFR §25.853(a) vertical bunsen burner testing, ASTM E662 smoke specific optical density, and the OSU 65/65 heat release requirement under 14 CFR §25.853(d). The table below records the compliance parameters that downstream manufacturers must validate on representative printed panels because published data for this specific FFF configuration under aircraft-level thermal stress is limited; material approval in injection-moulded form does not transfer automatically to FFF parts.

    Standard / clauseTest conditionAcceptance thresholdDownstream print-control input
    14 CFR §25.853(a) Appendix F Part I60-s vertical Bunsen burner exposureAverage burn length ≤ 6 in; average flame time after removal ≤ 15 s; drips may not ignite cottonPrint solid wall thickness ≥ 2.5 mm; no uncontrolled voids; raster angle alternating ±45°
    ASTM E662NBS smoke chamber, non-flaming and flaming modeSuitable smoke density limit for large-area cabin materials where required, typically Ds ≤ 200 at 4 minVerify natural unfilled grade; pigmented polymer may shift smoke density
    14 CFR §25.853(d) OSU heat releaseRadiant heat flux 35 kW/m²Peak HRR ≤ 65 kW/m²; total HR ≤ 65 kW·min/m² in the first 2 minPost-print annealing at 180 °C to close surface microvoids; test after conditioning to fuselage service humidity

    The downstream production sequence is high-temperature FFF on a large-format platform with a cast aluminium build plate coated with a PPSU-compatible adhesion layer, a nozzle temperature of 380–400 °C, a build chamber held at 130–160 °C, and a bed setpoint of 180–210 °C. Support structures are generated as breakaway PPSU with a 0.2 mm offset, because soluble PVA cannot survive the chamber temperature and moisture-laden support material causes hydrolysis pits. Terminal components produced under this route include air-distribution duct clip bases, stowage bin latch brackets, cabin partition standoffs, and non-load-bearing wire harness standoff brackets. The operational boundary is that FFF layer interfaces may exhibit a Z-direction tensile strength reduction exceeding 25 % compared with XY strength; therefore, any bracket carrying flight-critical load or located in a primary cabin path must be tested at assembly level. Chemical incompatibility includes ketone-based cleaning solvents used in paint stripping; methyl ethyl ketone can stress-crack the as-printed surface, so ISO 22088-3 ESCR screening is required if maintenance protocols expose the part to such agents.

    Chlorinated Solvent Contact, Immersion Fixtures, and ESCR Behaviour of Polyphenylsulfone FFF Builds

    Immersion fixtures placed in chlorinated process streams subject polyphenylsulfone to solvent-induced plasticisation far earlier than thermal failure. The design-limiting parameter is typically environmental stress crack resistance under continuous load rather than heat deflection. The finished polymer mass fraction is 100 % unfilled PPSU; the application does not use blended polysulfone/PPSU ratios or fibre reinforcement because the natural 1.75 mm filament is selected specifically for chemical resistance and dimensional predictability after machining. Relevant compliance input includes ISO 22088-3:2006 bent-strip ESCR screening, ISO 175:2010 for absorption in liquid chemicals, and ASTM D543-20 for resistance to chemical reagents. The production process is FFF with 0.20 mm layer height, 6 external perimeter walls, 100 % solid infill in the wetted shell, and a 0.6 mm hardened steel nozzle. The part is then annealed at 190 °C for 2 h and machined on sealing faces using carbide end mills at 3,000–5,000 rpm without chlorinated cutting fluid. Terminal part types include acid pickling fixture holders, pump impeller cover housings, sensor immersion sleeves, and guided jig plates used in hot caustic washing stations. The material is resistant to many common acids and bases, but published data for this printed configuration is limited for short-chain chlorinated hydrocarbons; continuous immersion in methylene chloride or trichloroethylene is not recommended because these solvents can soften amorphous arylsulfone matrices and accelerate ESCR at sharp machined corners. A further operational boundary is that strong oxidising acids such as fuming nitric and oleum are outside the chemical-resistance envelope; any acid concentration above 15 % at elevated temperature requires ISO 175 soaking rather than spot testing before release.

    Biopharmaceutical clean utility prototypes require polymer surfaces that can withstand repeated caustic and acid washdown without leachable contamination of purified water or process intermediates. In this application, the filament is used as an unfilled, unpigmented 1.75 mm feedstock; the resin-to-filler ratio is 100/0, and no colour masterbatch is introduced because trace metal pigments would alter the extractable profile. Compliance documentation is governed by ISO 10993-1:2018 for indirect product-contact risk assessment, USP <661.1> for plastic materials of construction in pharmaceutical processing, and USP <88> Class VI where the supplier maintains biological reactivity data on the base resin. The downstream process starts with high-temperature FFF on a system fitted with a liquid-cooled hot end and a 0.4 mm stainless-steel nozzle operating at 365–395 °C; the bed is maintained at 170–200 °C and the chamber at 110–140 °C to reduce warping in flat plate prototypes. Components are printed at 100 % solid infill with 5 perimeter walls, then machined on sealing surfaces to an achieved arithmetic mean roughness of Ra 0.8 µm before cleaning in a washer-disinfector per ISO 15883-1. Terminal parts include prototype distribution manifolds, CIP nozzle adapter plates, filter housing prototypes, and single-use support trays for filling line validation. The main limitation is that as-printed FFF surfaces retain microscopic void networks and cannot be regarded as hygienic product-contact surfaces unless machined, chemically smoothed, or sealed with an approved cleanability treatment; direct contact with strong oxidisers such as hydrogen peroxide at concentrations above 10 % at elevated temperature should be validated by long-term exposure testing because oxidative degradation of the arylsulfone backbone may release oligomers.

    If Ionic Extractables Are Controlled Below Semiconductor Tooling Limits in FFF PPSU Fixtures

    Wet-bench tooling in semiconductor fabs is exposed to SC1 and SC2 cleaning solutions at controlled temperatures, making ionic extractables and outgassing the principal rejection criteria for polymer fixtures rather than thermal deformation alone. The filler loading in this application is 0 % conductive carbon or mineral reinforcement; the printed fixture is 100 % natural PPSU by mass, which avoids the uncontrolled leaching risk associated with carbon black but removes any static-dissipative function. The applicable standards are SEMI F57 for polymer materials and components used in ultrapure water and liquid chemical distribution systems and SEMI F104 or SEMI S2 where equipment safety and gas/chemical compatibility documentation is required; additional incoming-lot control uses ion chromatography of aqueous extraction after a 70 °C soak for 24 h. The downstream production route is FFF in a cleanroom annex on a high-temperature printer with a 0.4 mm nozzle, 0.15 mm layer height, 100 % solid infill, a bed of 175 °C, and a chamber temperature of 130 °C. Before fab entry, the completed fixture is ultrasonically cleaned in a mixture of 70 % isopropanol and 30 % deionized water, rinsed with ultrapure water meeting 18 MΩ·cm resistivity, and baked at 120 °C for 6 h to reduce volatile condensables. Terminal components include wet-bench cassette repair fixtures, CMP conditioner mounting brackets, buffer tank level-sensor holders, and splash guards for drain stations. The constraints are that PPSU fixtures must not be used in concentrated hydrofluoric acid immersion or plasma-exposed positions, and any batch-to-batch variation in low-molecular-weight oligomer content requires a certificate of conformance with stated ionic extraction limits because a colourant-free unfilled resin can still vary with polymerisation conditions.

    Repeated food contact at elevated temperatures in bakery, dairy, and beverage processing lines has driven replacement of short-run stainless steel components with FFF PPSU where the production line requires low thermal mass, steam compatibility, and dimensional stability in high-humidity air, though published data for this specific configuration is limited to indirect or splash contact rather than continuous product contact above 65 °C. The material formulation ratio is 100 % virgin polyphenylsulfone to 0 % filler by mass; no reclaimed PPSU regrind is introduced into the food-contact article, and infill density is fixed at 100 % on all wetted surfaces and 80 % in the core only when wall thickness exceeds 6 mm. The primary compliance references are FDA 21 CFR 177.2500 for polyphenylene sulfone resins used in repeated-contact food applications and NSF/ANSI 51 for food equipment materials where certification is required by the equipment assembler. The downstream production process starts with high-temperature FFF using a nozzle temperature of 360–400 °C, a bed temperature of 170–200 °C, and a heated chamber above 100 °C; the printed blanks are then machined on food-contact faces to remove layer ridges, followed by washdown testing at 85 °C with 1 % alkaline cleaner and rinse water. Terminal part types include oven door spacer blocks, steam nozzle adapters, separator cones, conveyor wear strips, and sanitary clamp shims. The operational incompatibility is with intense radiant heat above 180 °C because the material begins to creep near the 220 °C glass transition; dry heat above 180 °C is not recommended. Components should not be used with strong mineral acid cleaning concentrates above 10 % without controlled contact-time validation.

    Autoclave Cycling Tolerance for Printed Dental Splints and Try-In Frames

    Dental try-in frames printed from PPSU are autoclaved repeatedly in clinical and laboratory environments, subjecting the FFF layer interfaces to moist heat, pressure swings, and the mismatch in thermal expansion between the polymer and embedded steel inserts. The formulation addition ratio is 100 % PPSU by mass; the component is printed directly from the natural 1.75 mm filament without diluent or filler, and a 0.08–0.12 mm layer height is used for occlusal features to limit staircase error. Compliance documentation should include ISO 10993-1:2018 for short-term mucosal contact, ISO 17665-1:2006 for moist-heat sterilisation validation in the dental practice, and ISO 13485:2016 for laboratory quality records; the part is not intended as a definitive intraoral prosthesis under dental device classification because FFF PPSU does not hold a universal regulatory clearance for permanent mucosal use. The downstream production route is high-temperature FFF with a 0.4 mm hardened nozzle, a nozzle setpoint of 370–400 °C, a bed temperature of 160–200 °C, and a chamber maintained at 100–130 °C; support material is breakaway PPSU and is removed with diamond-coated rotary tools before the trial frame is polished to a high gloss with pumice-free acrylic finishing wheels. After printing, the part is annealed at 180 °C for 1.5–2 h and then subjected to 10 mock autoclave cycles at 134 °C to verify dimensional stability before clinical issue. Terminal product types include edentulous try-in frames, implant verification jigs, transfer templates, and orthodontic model verification bases. The component is not warranted for an unlimited autoclave cycle life; after the initial 10-cycle verification screen, periodic dimensional inspection on a defined interval is required because published data for this FFF configuration under repeated moist-heat exposure is limited. After any refurbishment that involves sandblasting or machining, the component must be re-annealed and re-verified for fit because surface compressive stress introduced by FFF cooling gradients can be removed abruptly.

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    Ensinger TECAFIL PPSU natural is an unfilled polyphenylsulfone monofilament supplied at a nominal diameter of 1,75 mm for fused filament fabrication. The product designation in manufacturer documentation is TECAFIL PPSU natural – 1,75 mm – Filament Polyphenylsulfone. The base polymer is amorphous, so it does not show a melting endotherm; the processing window is instead controlled by the glass transition. Representative datasheet values include density 1,29 g/cm³ under ISO 1183-1, tensile strength 70 MPa and tensile modulus 2,3 GPa under ISO 527-2, elongation at break above 60 %, Charpy notched impact 30 kJ/m² under ISO 179-1/1eA, flexural modulus 2,4 GPa under ISO 178, and heat deflection temperature HDT/A 214 °C under ISO 75-2. Glass transition is reported at 220 °C. The natural grade is unpigmented, which removes colourant-related nucleation effects and retains the amber transparency typical of polyphenylsulfone.

    Because no melting point is present, dimensional change is governed by the coefficient of linear thermal expansion of approximately 55 × 10⁻⁶ K⁻¹ up to the glass transition. The density of 1,29 g/cm³ differs from the typical values for PEEK at 1,32 g/cm³ and PEI at 1,27 g/cm³, which affects spool weight and printed mass. During cooling from the forming temperature to ambient conditions, the part shrinks by thermal contraction rather than by crystallization volume loss. This behaviour reduces some warpage mechanisms associated with semi-crystalline materials but does not eliminate residual stress in thick cross-sections.

    Why is pre-drying and high-temperature hardware non-negotiable for this material?

    Water uptake in polyphenylsulfone is sufficient to create visible and mechanical defects if the filament is not dried. Conditioning under ISO 62 gives water absorption at saturation around 1,1 %. Amorphous sulfone extrusion practice requires residual moisture below 0,03 %. Drying is performed in a dry-air oven at 150 °C for at least 4 h, with spool orientation allowing air circulation between flanges. If drying is omitted, steam expansion at the nozzle produces splay, microbubbles, and reduced interlayer fusion. Storage must be maintained in a desiccated cabinet or sealed bag with a dew point below −20 °C. Published processing data for this specific filament configuration are limited; the drying condition is the commonly used safe threshold for unfilled PPSU feedstock.

    The hot end must sustain continuous operation above 350 °C. PTFE-lined hot ends are unsuitable because the continuous service limit of PTFE is ordinarily 260 °C, and decomposition products can form above 350 °C. The nozzle can be brass, plated copper, or hardened steel for this unfilled grade; abrasive-resistant tool steel is not required unless filled variants are used. An all-metal heat break with a polished internal path reduces dead zones and polymer stagnation.

    Build plate temperature is typically set between 130 °C and 160 °C, depending on the build surface. A heated chamber is required. Operation below 80 °C produces non-uniform cooling and frozen-in stress. Raising chamber temperature to 80–120 °C reduces the temperature gradient between the formed layer and the surrounding air, but motion components and toolhead electronics may require active cooling if chamber temperature approaches 100 °C.

    Rheology of unfilled PPSU is shear-thinning. Melt flow rate is commonly reported around 15 cm³/10 min at 365 °C and 5 kg under ISO 1133-1. Higher molecular weight grades may show lower melt flow and higher impact retention. In filament extrusion, melt temperature is maintained above 330 °C and below 400 °C to avoid thermal degradation. Because the polymer is amorphous, no crystallization plateau exists in the hot end, which simplifies residence-time management relative to semi-crystalline PEEK. Degradation is observed as a shift in melt pressure and as a drop in notched impact of printed specimens tested under ISO 179-1/1eA.

    Dimensional control of the 1,75 mm filament is measured with closed-loop laser gauges and melt-pump control in filament manufacture. Short-term diameter variance is maintained within ±0,05 mm. In direct-drive feed systems, the filament path from spool to hot end should remain straight. Poorly wound bobbins that impose lateral force can cause buckling inside the heat break. This failure mode is more likely with 1,75 mm feedstock than with 2,85 mm feedstock because the smaller cross-section reduces critical buckling load. Diameter variance greater than ±0,10 mm alters volumetric drag flow at constant motor steps and can produce alternating over- and under-extrusion. No published coefficient of variation is available for the Ensinger product.

    Property boundaries that separate PPSU from PSU, PEI, and PEEK in high-temperature service

    Compared with polysulfone, the PPSU grade shifts the service boundary upward. Polysulfone has a glass transition near 185 °C and an HDT/A near 174 °C. PPSU increases those values to 220 °C and 214 °C while retaining higher notched impact after repeated steam exposure. Compared with polyetherimide, PPSU has lower tensile strength but greater resistance to hot water and steam-induced stress cracking. Polyetherimide can be more notch-sensitive and may embrittle after repeated sterilization. Compared with PEEK, PPSU processes at lower melt temperatures because PEEK requires melting around 343 °C; however, PEEK retains a higher continuous-use temperature because of its semi-crystalline microstructure. PPSU is therefore positioned above polycarbonate and polysulfone, but below PEEK, for continuous thermal resistance.

    Comparative reference values for unreinforced high-temperature thermoplastics in fused filament fabrication
    PropertyTECAFIL PPSU naturalPSUPEIPEEK
    Density, g/cm³1,291,241,271,32
    Glass transition, °C220185217143, melting 343
    HDT/A, °C214174200152 amorphous
    Tensile strength, MPa7070105100
    Charpy notched, kJ/m²306–105–86–8

    The notched impact of PPSU at 30 kJ/m² is approximately three to five times higher than the typical values listed for PSU, PEI, and PEEK. The trade-off is tensile stiffness. PPSU is more ductile, which can support thin snap-fit features but can reduce dimensional fidelity on unsupported overhangs if the feedstock is not dry and the chamber is too cool. For applications requiring higher tensile modulus at the same approximate glass transition, PEI may be selected. For applications requiring dry heat resistance above 200 °C, PEEK remains the more appropriate choice. For steam-exposed fixtures and medical housings, PPSU offers a balance of impact retention and processing temperature below PEEK.

    When repeated steam autoclave exposure is the governing specification

    Saturated steam sterilization in pharmaceutical and medical fixtures is routinely performed at 134 °C for 3 min or at 121 °C for 20 min under ISO 17665-1. The PPSU glass transition of 220 °C provides a substantial margin above the 134 °C plateau. By contrast, polycarbonate with a glass transition near 145 °C has a narrow thermal margin and is more prone to stress relaxation and surface haze after repeated cycles. The dominant failure mode in printed PPSU autoclave fixtures is not polymer meltdown but interlayer delamination caused by residual stress and moisture re-absorption. Parts should be produced with high chamber temperature and dense wall loops, and should be given slow venting cycles during sterilization. Rapid venting can create differential pressure within trapped porosity and promote layer separation.

    Injection-molded PPSU shows high retention of notched impact after 100 steam cycles at 134 °C; no identical published dataset exists for FFF parts with controlled raster orientation. The limiting condition is the printing process itself. Sparse infill and under-extruded boundaries create moisture ingress paths that reduce steam-cycle durability. The user is responsible for validating the specific printed geometry under the same wrapping, loading, and sterilizer ramp conditions as production.

    Chemical resistance of PPSU derives from the sulfone backbone. The material resists aliphatic hydrocarbons, alcohols, dilute mineral acids, and common disinfectants. It is not recommended for continuous contact with chlorinated solvents such as dichloromethane or with ketones under stress because environmental stress cracking can occur. Concentrated nitric acid and strong oxidizing acids are incompatible. The base polymer can support medical device and food-contact assessments, but compliance statements require lot-specific documentation. Relevant biological evaluation standards may include ISO 10993-1 for evaluation planning, ISO 10993-5 for cytotoxicity, and ISO 10993-10 for irritation and sensitization. For polysulfone resin formulations, FDA 21 CFR 177.2440 may be referenced. The natural unfilled grade is generally preferred for regulatory dossiers because it avoids pigment extraction and simplifies additive review. Published data for this specific filament configuration under biological reactivity testing are limited.

    Storage boundaries are dry and cool. Exposure to ambient humidity above 60 % RH without desiccation can return the spool to a moisture level that requires re-drying. A sealed bag with fresh desiccant or a dry cabinet is sufficient for room-temperature storage. If the spool is opened in a non-conditioned room and left on the printer for more than 24 h, printing defects may appear unless a heated dry-feed system is used. Field experience with twin-screw compounding of amorphous sulfone materials shows uncontrolled moisture as the most frequent cause of poor interlayer strength and surface splay.

    Model designation differences within the Ensinger TECAFIL family include diameter and colour variants. The 1,75 mm diameter is typically used with direct-drive or short Bowden feed systems, while 2,85 mm feedstock is used where higher feed force is available and where longer Bowden tubes are acceptable. Colour variants and filled materials are not equivalent to natural PPSU. Glass-filled or carbon-fiber-filled PPSU increases tensile modulus, reduces impact, and changes thermal expansion and abrasion behaviour. The natural unfilled grade should therefore be specified only when the application requires the base polymer’s ductility, transparency, and simpler chemical profile.

    Processing hardware for PPSU is in the same class as PEI and PEEK, but PPSU does not require the upper melt temperature of PEEK. Hot ends rated for 380 °C may be sufficient, while PEEK often requires hardware rated for 450 °C. The trade-off is chamber cost. A chamber temperature of 80–120 °C remains high enough to require active toolhead cooling and thermal isolation of belts, fans, and electrical connectors. Users must verify the extruder’s maximum continuous temperature and the chamber’s temperature uniformity before starting a print campaign with this material.

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