| Код ТН ВЭД | 158334 |
Будучи аккредитованным заводом Lehvoss LUVOCOM 3F PAHT 9825 NT Nylon for Additive Manufacturing, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
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In underhood air-management applications where continuous air charge temperature after intercooler degradation reaches 120–140 °C, short-glass PA6 grades soften and lose clamp load retention in bolted flanges; the LUVOCOM 3F PAHT 9825 NT feedstock is therefore directed toward charge-air duct prototypes and low-rate spare parts rather than volume injection-molded components. Compliance for this segment is framed by ISO 16750-5:2010 for chemical and thermal loads, SAE J1455 for underhood electrical/mechanical exposure, and material property verification under ISO 527-2:2012 and ISO 75-2:2013. The formulation uses 100 wt% virgin natural compound; post-industrial regrind from failed build plates is limited to 10 wt% only for non-safety-related brackets after re-drying to residual moisture below 0.02 wt%. Downstream production on an industrial FFF platform requires desiccant drying at 80 ± 5 °C for 8–12 h, filament extrusion on a 25 mm twin-screw with L/D 40 and melt pump, printing with nozzle setpoint 310 ± 10 °C, build chamber 90 °C, and bed 110 °C; after extraction at 60 °C the parts are annealed at 130 °C for 1 h under forced air. On the filament extrusion line, barrel temperature excursions of ±5 °C at the metering zone produce ovality above 0.05 mm, forcing rejection on the laser micrometer. At ambient relative humidity above 60 %, drying time is extended to the upper 12 h limit and dry-air purge is maintained. Terminal parts include turbocharger inlet adapters, coolant reservoir flanges, mass air flow sensor mounts, and EGR cooler bypass brackets.
Published full-scale burn data for this specific unfilled natural grade in cabin air diffuser geometries is limited; the compound is therefore evaluated with printed coupons at worst-case flat and edge-on layer orientation before use in non-structural cabin interior parts. These are non-structural components only; primary airframe elements are outside the qualification envelope. Regulatory verification is anchored to 14 CFR 25.853(a) and Appendix F Part I vertical burn requirements, with smoke and toxic gas assessment under ATS 1000.001 and ABD 0031 where airframe OEMs require cabin interior material qualification. The feedstock is processed at 100 wt% virgin pellets without regrind, dried at 90 °C for 6 h, printed at nozzle 320 °C, chamber 100 °C, bed 120 °C, layer height 0.15 mm, then annealed at 120 °C for 2 h. Terminal parts include cabin air deflectors, PSU panel inserts, galley latch housings, and cable clamp blocks.
For low-voltage switchgear and relay sockets, the material's tracking resistance and glow-wire behavior are evaluated according to IEC 60112:2020 and IEC 60695-2-11:2021, with flammability classification under UL 94 at 0.8 mm thickness. Because the unfilled natural grade may exhibit orientation-dependent comparative tracking index, test coupons are printed in both flat and edge-on orientations. The formulation for this application is a 100 wt% unfilled natural compound; no anti-tracking additive or color masterbatch is compounded in the downstream process because particulate additives can increase leakage current scatter under DC bias. Amine-based antistatic and flame-retardant masterbatches are excluded because they alter the end-group balance of the polyamide during melt deposition. Production is performed on a high-temperature FFF cell with drying at 80 °C for 12 h, nozzle temperature 300–320 °C, chamber 85 °C, and layer height 0.2 mm; contact retention bores are reamed after printing to achieve H7 tolerance, and brass inserts are installed using controlled thermal insertion at 180 °C. Terminal products include relay sockets for 48 VDC bus systems, busbar support insulators, connector housings for under-bonnet HVAC actuators, and terminal block covers for frequency inverters.
Acceptance matrix for printed electrical specimens:
| Standard designation | Test condition | Specimen orientation | Acceptance criterion |
|---|---|---|---|
| IEC 60112:2020 | Electrolyte A, 25 °C | Flat and edge-on | CTI ≥ 250 V |
| IEC 60695-2-11:2021 | Glow wire 850 °C / 0.8 mm | Flat | No ignition or flame ≤ 30 s after withdrawal |
| UL 94 | 0.8 mm thickness | Flat | V-0 or V-1 depending on connector current rating |
Large inspection fixtures and drilling jigs produced from LUVOCOM 3F PAHT 9825 NT are subjected to anneal cycles after deposition when dimensional stability after exposure to chilled coolant or freezing storage is required; the process is not a cosmetic post-treatment but a means of reducing locked-in orientation stress that manifests as post-process creep in Z-direction tensile specimens. The compliance framework is principally metrological: ISO 2768-1:1989 for general tolerances, ISO 1101:2017 for geometrical tolerancing, and ISO 178:2019 for flexural verification after heat treatment, while thermal transitions are screened under ISO 11357-3:2018. The material is used at 100 wt% as supplied pellets in large-format pellet-fed deposition; if the fixture requires higher compressive modulus, a carbon-fiber-filled LUVOCOM 3F grade is selected rather than blending fiber into the 9825 NT melt stream. On a single-screw deposition head with 30 mm screw diameter and L/D 30, uncontrolled fiber addition causes bridging at the vent port and feed-root plugging because the short-fiber reinforcement raises melt viscosity and reduces effective conveying angle; published data for this specific formulation under such loading is limited, so blending is not carried out on production cells. The pellet hopper is maintained at 80 °C with a -40 °C dew point air purge for 4 h before first deposition. Printing is conducted with a 0.4 mm layer height, nozzle temperature 340 °C, bed temperature 120 °C, and chamber temperature 90 °C; the printed fixture is ramped at 0.5 °C/min to a first hold at 90 °C for 30 min, then to 140 °C for 2 h, and cooled at 0.5 °C/min to minimize differential shell-to-infill shrinkage. If the ramp rate exceeds 1 °C/min, measurable Z-plane tensile failure in printed bosses is observed due to thermal expansion mismatch between the amorphous skin and semicrystalline core. Dimensional checks are performed after 24 h at 23 °C and 50 % RH according to ISO 291:2008. Terminal parts include CMM fixture plates, EDM electrode alignment jigs, composite trimming fixtures, and welding alignment frames for subassembly cells.
Chemical processing installations requiring short-run replacement components use the unfilled polyamide feedstock for trays and housings exposed to intermittent contact with hot aqueous glycol mixtures at temperatures below the polymer's continuous service limit. Compliance references include Regulation (EC) No 1907/2006 (REACH) for substances of very high concern, RoHS Directive 2011/65/EU for restricted substances, and ASTM D543-20 for chemical resistance screening; specific fluid immersion testing under ISO 175:2010 is required because published data for this exact formulation in concentrated organic acids is limited. The formulation is 100 wt% compound; no post-process sealant or adhesive is used at the tray wall joints, as weld lines must be eliminated by optimizing extrusion path rather than relying on chemical bonding. Moisture content above 0.02 wt% at the nozzle causes surface foaming, so the desiccant drying step at 80 °C for 10 h is treated as a release criterion, not a default setting. Downstream processing involves printing with a 0.25 mm layer height, nozzle temperature 310 °C, chamber temperature 80 °C, and bed temperature 100 °C; after printing, trays are heat-treated at 150 °C for 30 min to densify the outer shell and reduce microvoids. Terminal products include drying trays for laboratory-scale fluidized bed trials, filter press end housings, sight glass retainers for agitated reactors, and dip-pipe supports for chemical cleaning baths.
Large-format additive manufacturing work cells running pellet-fed extrusion of LUVOCOM 3F PAHT 9825 NT are used to produce thermoforming mandrels and composite layup tools that must tolerate autoclave cycles at 120–140 °C. Governing material acceptance requirements are drawn from ISO 75-2:2013 for heat deflection under 0.45 MPa, ISO 604:2002 for compressive strength, and ASTM E228-17 for coefficient of thermal expansion, while the production process itself is aligned with ISO/ASTM 52904:2019 for additive manufacturing process qualification. The feedstock is consumed at 100 wt%; reclaimed pellet regrind from failed tool blanks is limited to 20 wt% and is blended at the dryer inlet only after moisture content is verified below 0.02 wt% via Karl Fischer titration. Processing on a pellet-fed deposition head uses a 30 mm single screw with L/D 30, melt temperature 330–350 °C, bed temperature 120 °C, and layer height 0.4 mm; after deposition the tools are annealed at 150 °C for 2 h with ramping at 0.3 °C/min, then post-machined on 5-axis CNC equipment using carbide cutters with compressed air cooling, not liquid coolant, to avoid rapid moisture uptake at the machined surface. Terminal products include thermoforming molds for high-density polyethylene skin panels, composite layup mandrels for duct preforming, autoclave caul plates, and drill jigs for carbon-fiber-reinforced thermoplastic assemblies.
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Lehvoss LUVOCOM 3F PAHT 9825 NT is an unfilled, natural-colour nylon feedstock developed specifically for fused filament fabrication and direct extrusion additive manufacturing systems. The PAHT portion of the designation identifies a heat-stabilised high-temperature polyamide matrix, while the 9825 NT suffix identifies the natural unfilled grade within the LUVOCOM 3F melt-processed thermoplastic portfolio. The product is supplied as a monofilament in nominal diameters of 1.75 mm and 2.85 mm, with controlled ovality and diameter tolerance for consistent volumetric feed in Bowden-drive and direct-drive toolheads. Published manufacturer data describe the base polymer as a polyamide 6/66-based system; the formulation contains heat stabilisers intended to extend melt residence time and reduce oxidative chain scission during hot-end hold at temperatures between 250 °C and 280 °C. Because the material is unfilled, nozzle abrasion is lower than with carbon-fibre-reinforced polyamides, but the stiffness is correspondingly lower and the printed part remains electrically non-conductive.
Before extrusion, the filament should be dried in a forced-air or vacuum dryer at 80 °C for 4–8 h. Target residual moisture is below 0.05 wt%; drying air with a dew point of −30 °C or lower is preferred. Moisture above this threshold produces steam porosity at the nozzle, reduces melt viscosity, and weakens interlayer boundaries. The heated build plate should be held at 80–100 °C, with a chamber temperature of 40–60 °C to reduce residual stress on large flat sections. Initial parameter development on a 0.4 mm hardened steel nozzle at 30–60 mm/s and layer heights of 0.15–0.25 mm provides a stable starting envelope for XY-plane tensile specimens. Z-axis interlayer strength must be developed separately because semicrystalline solidification and chain orientation create anisotropic mechanical behaviour in thin walls.
| Processing variable | Initial validation range |
|---|---|
| Drying temperature and time | 80 °C, 4–8 h |
| Residual moisture target | <0.05 wt% |
| Extruder temperature | 250–280 °C |
| Build plate temperature | 80–100 °C |
| Chamber temperature | 40–60 °C |
| Print speed | 30–60 mm/s |
| Layer height | 0.15–0.25 mm |
| Nozzle diameter | 0.4 mm hardened steel |
Melt residence time is a critical variable because the amide linkage in polyamide 6/66 undergoes hydrolytic and oxidative degradation when heated in the presence of water or oxygen. The heat-stabiliser package in PAHT 9825 NT shifts the onset of measurable degradation, but it does not eliminate the requirement for dry feedstock. Degradation proceeds by two competing pathways. Hydrolytic chain scission dominates when moisture is present; random amide bond cleavage lowers number-average molecular weight and weakens interlayer adhesion. Oxidative degradation dominates in dry but oxygen-rich hot ends above 260 °C, producing chromophores and, eventually, gel particles. The stabilised formulation suppresses the oxidative pathway but cannot protect against grossly wet feedstock. Processing with a dew-point-controlled dryer and an inert feed path is therefore a process control rather than a material property.
At a setpoint of 260 °C, moisture levels above 0.10 wt% can produce hydrolytic chain scission and lower molecular weight sufficiently to reduce weld-line strength at the interlayer boundary. The maximum continuous hot-end residence time should be kept below 15–20 min during stable extrusion. After a pause longer than 10 min, a purge of 20–30 mm of material should be completed before deposition resumes. On production-scale direct-drive systems with all-metal hot ends, intermittent clog formation during extended runs is commonly associated with degraded polymer residue at the heat break or with spool moisture reintroduced after drying. A sealed dry spool holder with desiccant and a hygrometer reading below 10 % RH is an effective control for long builds. Shear thinning behaviour typical of polyamide 6/66 allows deposition through a 0.4 mm nozzle at moderate backpressure. If nozzle pressure becomes unstable, the first troubleshooting step is verification of residual moisture and filament diameter, not increasing extruder temperature beyond 280 °C, because excessive temperature accelerates degradation and increases emission of low-molar-mass volatiles.
On manufacturing lines using a 0.6 mm nozzle and 0.25 mm layer height, unsupported overhangs begin to show surface defects above 45° unless support structures and cooling fan speeds are adjusted for the hotter processing window. A 0.3 mm Z-gap is typically used for breakaway support interfaces to balance support removal force against underside surface finish. Batch-to-batch feedstock variation in the filament diameter beyond ±0.05 mm is a more common cause of under-extrusion than hot-end temperature error when the spool is stored outside a dry box. For unfilled polyamide FFF parts, Z-direction tensile strength is often 50–70 % of XY-direction strength because polymer diffusion across the weld plane remains incomplete. Published data for this specific configuration on overhang fatigue and long-term chemical exposure are limited; application validation is required.
Semicrystalline solidification shrinkage for polyamide 6/66 is typically in the range of 1.0–1.5 % linear. On large flat parts, shrinkage anisotropy between the build plate, chamber, and free surfaces creates residual tensile stress at the part edges. A heated plate above the glass-transition temperature and slow cooling after build reduce warp-induced delamination. For parts thicker than 6 mm, reducing infill density from 100 % to 40–60 % may be necessary to limit internal shrinkage voids.
Representative dry-state mechanical and thermal values reported under standard polyamide test protocols are summarised in the following table. Conditioned values at 50 % RH will show lower modulus and higher elongation because absorbed water acts as a plasticizer. Lot-specific values should be verified against the current manufacturer datasheet before tooling dimensioning.
| Property | Test method | Dry-state typical value |
|---|---|---|
| Density | ISO 1183-1 | 1.12 g/cm³ |
| Tensile strength | ISO 527-2 | 67 MPa |
| Tensile modulus | ISO 527-2 | 2,500 MPa |
| Elongation at break | ISO 527-2 | 8–12 % |
| Flexural modulus | ISO 178 | 2,300 MPa |
| Charpy notched impact strength | ISO 179-1/1eA | 5 kJ/m² |
| Heat deflection temperature HDT/A | ISO 75-2/A | 125 °C |
| Heat deflection temperature HDT/B | ISO 75-2/B | 180 °C |
| Vicat softening temperature B50 | ISO 306 | 200 °C |
| Water absorption, saturation | ISO 62 | 2.2 % |
Compared with unfilled PA12, PAHT 9825 NT has a higher dry-state heat distortion temperature and tensile modulus, but higher moisture uptake. Typical unfilled PA12 HDT/B values are around 90 °C, while PAHT 9825 NT is reported near 180 °C under ISO 75-2/B. The difference is significant for underhood housings or process equipment covers that see short-term temperature excursions. Compared with short-carbon-fibre polyamide compounds, the unfilled PAHT 9825 NT has lower stiffness, lower abrasion resistance, and higher elongation; it also avoids the galvanic coupling and conductive path that carbon fibre can introduce in metal assemblies. Density is lower than carbon-filled grades, which often exceed 1.20 g/cm³. Against an impact-modified PA6, the PAHT grade shifts service temperature upward but may have lower notched impact toughness at sub-zero conditions; the specific grade selection should be made with conditioned impact data from notched Charpy tests.
Within the LUVOCOM 3F range, the PAHT 9825 NT material occupies the unfilled high-temperature nylon position. Glass-fibre-reinforced grades provide higher flexural modulus and lower thermal expansion, but increase nozzle wear and produce rougher side-wall surfaces. Carbon-fibre-reinforced grades provide higher stiffness and electrostatic discharge characteristics, but they reduce elongation and require hardened steel or ruby nozzle bores. The unfilled natural grade is therefore selected when thermal resistance, moderate stiffness, and non-conductive behaviour are required together.
Typical use cases include functional prototypes, bracketry, covers, and tooling fixtures that require better elevated-temperature resistance than PA12 but do not require the stiffness of a fibre-filled grade. The material is also used for short-run production of non-conductive housings where carbon-fibre grades are excluded because of electrical or galvanic concerns.
For brackets, sensor housings, and underhood fixtures that must survive short-term temperature excursions above 150 °C, the unfilled PAHT 9825 NT grade is a candidate only when the applied tensile stress remains below the temperature-dependent yield envelope. The dry-state HDT/B value near 180 °C is a short-term thermal deformation indicator, not a continuous load-bearing limit. Creep testing according to ISO 899-2 at the intended service temperature and load percentage should be performed. Published data for continuous use above 150 °C in a load-bearing configuration for this exact grade are limited; a prototype programme using specimens from at least three production lots is recommended to quantify batch-to-batch variation in creep modulus and interlayer fracture energy. The absence of carbon fibre avoids galvanic coupling in aluminium assemblies and permits radio-frequency transparency in sensor or radar brackets, but the unfilled grade does not provide the stiffness of a fibre-filled polyamide.
Printed parts made from PAHT 9825 NT are not supplied with a blanket food-contact approval. If repeated food-contact service is intended, migration testing under Regulation (EU) No 10/2011 or FDA 21 CFR 177.1500, as applicable, must be conducted on the finished printed part because porosity, colourants, and post-processing agents influence compliance. REACH and RoHS conformity should be confirmed with the manufacturer for the specific spool lot. The material should not be combined with acidic or amine-based cleaning agents at elevated temperature without compatibility testing, because polyamide 6/66 can undergo environmental stress cracking or accelerated hydrolysis in acidic media above 80 °C. The spools should be returned to sealed containers with desiccant immediately after use; prolonged exposure to ambient humidity above 60 % RH can raise moisture content to levels that require re-drying before the next build.