| Код ТН ВЭД | 450208 |
Будучи аккредитованным заводом Lehvoss LUVOCOM 3F PAHT 9826 BK 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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Across automotive trim and body assembly lines, replacement of machined acetal and glass-filled nylon with Lehvoss LUVOCOM 3F PAHT 9826 BK is concentrated in end-of-arm tooling, sensor brackets, and dimensional holding fixtures where low-volume hard tooling cannot absorb long procurement lead times. The compound is used as a 100 wt% monofilament without downstream dilution; break-away support material is assigned to a separate extruder, and its mass fraction is geometry-dependent. Because the printed item is a production auxiliary rather than a vehicle component, quality control is governed by the plant's IATF 16949 control plan instead of UNECE type approval; dimensional capability is recorded on first-article fixtures and re-qualified after any chamber temperature adjustment or nozzle replacement. Mechanical acceptance specimens are printed flat in the same build orientation and tested to ASTM D638-14; short-term thermal screening uses ISO 75-1:2020 and ISO 75-2:2020 on flatwise and edgewise coupons because anisotropic heat deflection can shift the safe operating window depending on raster orientation. Production-scale FFF platforms with heated build chambers of 80–100 °C and nozzle diameters between 0.4 mm and 0.6 mm are used, with filament pre-drying in dry-air equipment at 80 °C for 4–6 h once storage RH has exceeded 60%. The terminal component categories typically encountered are bumper alignment fixtures, powertrain lifting aids, paint-shop masking templates, and sensor calibration mounts.
A selective soldering pallet printed from Lehvoss LUVOCOM 3F PAHT 9826 BK operates in a narrow thermal band where PEEK is often overspecified and POM is ruled out by mechanical relaxation after repeated wave contact. The printed carrier is produced at 100% infill in load-bearing areas and with a gyroid or cubic core cavity in non-load regions; no flame-retardant masterbatch or glass-fiber concentrate is added at the user site, which keeps the as-fed ratio at 0 wt% diluent and 100 wt% PAHT compound. Threaded brass or stainless steel inserts are installed post-build, and insert boss dimensions are adjusted by stepwise reaming rather than by changing polymer formulation. The process sequence includes FFF deposition at nozzle temperatures within the machine manufacturer's validated PAHT band, which is generally reported from 250 °C to 290 °C for high-temperature nylons; after build, pallet shells are annealed at 110 °C for 2 h in a circulating-air oven to reduce residual stress before first soldering trial. Compliance on the assembled carrier system is assessed under IEC 61340-5-1 for electrostatic discharge control, but the polymer itself is not regarded as ESD-active; grounding is provided by external copper tape or conductive inserts. Flame-retardant classification is not assumed from PAHT chemistry; if UL 94 documentation is required for an electronics enclosure, the converter must obtain a grade-specific statement from Lehvoss rather than cite general polyamide behavior. Final assemblies are evaluated under 2011/65/EU for the restricted substances inventory of the complete carrier. Terminal products include selective-solder pallet pockets, test-fixture baseplates, board handling end-effectors, and stencil cleaning jigs.
If packaging equipment runs without oil-based lubrication, printed Lehvoss LUVOCOM 3F PAHT 9826 BK chain guides and scraper blades reduce the requirement for machined acetal in low-volume aftermarket service. The material is fed as a 2.85 mm filament at 100 wt% virgin compound; when mass reduction is required, infill is lowered to 60–80% with 4 top and 4 bottom solid layers instead of introducing chemical blowing agents. FFF deposition takes place with a heated chamber above 80 °C, and post-processing is limited to abrasive blasting or vapor polishing only if the resulting dimensional tolerance holds at the wear-sensitive interface. Guarding components are documented against 2006/42/EC Annex I when integrated into a machine guarding system, and insulating regions are tested according to IEC 60243-1. Compatibility with cleaners and mineral oils is screened by ISO 175:2010 immersion tests; strong amine-containing cleaners should be avoided because polyamide molecular weight can degrade in aggressive amine service. Terminal part types are chain guides, timing-belt covers, scraper blades, vacuum gripper adapters, and cable drag-chain end brackets. Published data on this specific PAHT grade under continuous oil immersion is limited, so converter validation is required for each cleaner package.
In aircraft maintenance and repair organizations, drill templates and inspection gauges are exposed to hot engine oil, repeated oven cycles, and direct handling around engine bays. If machined aluminum or carbon-fiber-filled nylon is replaced by Lehvoss LUVOCOM 3F PAHT 9826 BK, the as-fed ratio remains 1.0 undiluted monofilament, but moisture control before extrusion controls the entire build. Unsealed spools are dried at 80 °C in a desiccant dryer for 6–8 h; Karl Fischer verification should show residual moisture below 0.03 wt% because higher water content reduces interlayer adhesion and creates microvoids in vertical walls. The production workflow on high-temperature FFF platforms specifies alternating ±45° raster layers in load-bearing regions, with extra perimeters around hole locations that receive drill bushings. A post-build anneal at 120 °C for 1–2 h under nitrogen or vacuum is applied to reduce crystallinity gradients and improve dimensional stability during subsequent hot-tool contact. Compliance is governed by the MRO quality system under AS9100D clause 8.5.1 for control of production and service provision; first-article verification follows AS9102, and mechanical anisotropy is measured using ASTM D638-14 specimens printed flat, edge, and vertical. The operational boundary for this service is continuous exposure above 130 °C or direct hydraulic fluid contact above 80 °C; both require validation on printed specimens before release. Terminal deliverables include drill plates, trim templates, engine borescope guide tools, and wheel-well protective covers that remain non-flight shop aids rather than certified airframe components.
The dominant process conflict in MRO tooling is not extrusion temperature but shape distortion from differential melt crystallization after high-temperature exposure. A fixture printed with 0.4 mm layers on a cartesian FFF machine with 300 × 300 × 300 mm build volume can show residual stress concentrated at the interface between the heated bed plane and upper layers; this is observed on production lines as radius elongation in drill bushings and hole-to-hole pitch drift after the first oven cycle. To control it, the build is started with a raft-free solid base of 4 layers, and the chamber is held at 90–100 °C while the bed is maintained at 100–110 °C. Batch-to-batch filament moisture variation on 2.85 mm spools is a common bottleneck; converters that do not verify Karl Fischer values before loading can experience interlayer delamination on vertical specimen walls. These effects are not cosmetic and are detected by ASTM D638-14 vertical-direction tensile retention below the flat-direction value; published data for this exact PAHT grade at 120 °C annealing in nitrogen is limited, so MRO shops run a first-article validation on every spool lot.
Where gas processing operators need non-sparking inspection mounts and valve-position indicators, Lehvoss LUVOCOM 3F PAHT 9826 BK is printed as a replacement for acetal and glass-reinforced epoxy laminates. The polymer is not compounded with conductive carbon black at the user site; it is processed at 100 wt% black PAHT, and anti-static performance, if required, is achieved through printed post-build copper grounding pathways inserted into tool channels rather than through modification of the polymer formulation. Service printing uses nozzle temperatures in the 260–290 °C band and a heated chamber held near 90 °C; warpage on long thin instrument mounts is reduced by orienting the part along the X-Y diagonal and increasing the bed adhesion area by a geometry-dependent margin determined from the machine's thermal offset tables. Chemical resistance is screened with ISO 10468 on printed coupons, but because polyamides are attacked by strong amines and some sour-gas corrosion inhibitors contain amine species, direct immersion testing is required before production use. The assembled device may be assessed for equipment category under IEC 60079-0 only if the printed housing is not expected to serve as an explosion-proof enclosure. Terminal products include gas turbine borescope alignment mounts, valve stem indicators, instrument tag plates, and flange face measuring fixtures. Published data for this specific PAHT grade in sour-gas atmospheres is limited; converter validation is mandatory.
Development shops and chemical equipment builders employ Lehvoss LUVOCOM 3F PAHT 9826 BK for low-pressure manifold prototypes, pump impeller masters, and tank-farm pipe fitting trial pieces. The filament is consumed at 100% PAHT monofilament; when a printed form is used as a sacrificial lost-polymer pattern, the shell investment sequence is adjusted to the thermal expansion profile of the pattern rather than to a fixed mass ratio. High-temperature FFF machines with hardened steel nozzles of at least 0.4 mm diameter are used, and pressure-holding prototypes are built at 95–100% infill with extra perimeters rather than a single dense wall. Before sealing or coating, the PAHT part is dried to 0.03 wt% moisture; solvent-free epoxy or ceramic slurry sealing is used after build to close surface pores where low-pressure fluid tightness is required. Compliance for temporary piping prototypes is evaluated according to ISO 15493:2003 for plastics piping systems in industrial applications, while chemical resistance is screened per ISO 175:2010. If a trial part enters a food processing washdown zone, the compliance file should not assume FDA 21 CFR 177.1500 clearance without a migration study on the printed finished article, because surface porosity and post-processing can alter the residue profile. Terminal product types comprise pump impeller patterns, chemical dosing manifold trials, CIP nozzle brackets, and temporary bypass pipe fittings. Continuous contact with hot strong acids or hot ethylene glycol above 80 °C is not recommended without validation.
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Lehvoss LUVOCOM 3F PAHT 9826 BK is a black high-temperature polyamide (nylon) feedstock formulated for extrusion-based additive manufacturing, specifically fused filament fabrication (FFF/FDM). The material is part of the LUVOCOM 3F family, in which the 3F designation separates filament-fed additive manufacturing compounds from injection-moulding or conventional extrusion grades. The PAHT segment indicates a high-temperature polyamide base intended to extend the thermal service range of nylon components produced on desktop or industrial FFF platforms. In contrast to general-purpose PA6 or PA66 filaments, a high-temperature polyamide of this class is specified where short-term heat exposure, creep resistance, and retention of stiffness above 100 °C are relevant design inputs. The BK designation indicates a black final filament, but the presence and type of pigmentation or filler must be confirmed against the batch certificate because black colour alone does not identify the filler system. Relevant property tests include tensile testing under ISO 527-2, flexural testing under ISO 178, heat deflection under ISO 75-1/-2, melt volume-flow rate under ISO 1133-1:2022, and density under ISO 1183-1.
Published numerical data for this exact LUVOCOM 3F PAHT 9826 BK configuration are limited in publicly available industrial documentation. The following processing and verification framework therefore relies on class-level behaviour of high-temperature polyamide FFF feedstocks and on the standard methods required to generate product-specific values. The material must be evaluated in the intended build orientation because FFF tensile and flexural properties are anisotropic. A specimen printed flat in the XY plane typically produces higher tensile strength than a Z-oriented sample owing to layer-interface weakness. Comparative data should therefore report orientation, raster angle, layer height, extrusion temperature, chamber temperature, and part conditioning with each data set.
Compared with PA12 filament, the high-temperature polyamide class generally shifts the heat deflection temperature upward and improves stiffness retention in hot environments, but the processing window is narrower and drying is more critical. Compared with PA6 or PA66 filaments, the high-temperature backbone may reduce moisture uptake and raise the continuous use ceiling, although nylon chemistry still requires active moisture control. Compared with PEEK or PEI filaments, a PAHT grade of this type is processed at lower hot-end temperatures and does not require the 400 °C class hot ends and chamber temperatures used for polyetheretherketone. However, it also does not inherit the same chemical resistance, flame resistance, or long-term thermal oxidative stability as PEEK or PEI. These comparisons are class-level and must be verified against product-specific ISO datasets rather than assumed from nomenclature. The material is not a powder-bed nylon and is not an SLS grade; it is supplied for filament-fed AM systems. Selection between PAHT, PA12, PA6/66, PEEK, or PEI is therefore determined by the load case, service temperature, chemical exposure, and acceptable failure mode, not by a single thermal property.
Before melt processing, the filament is dried to reduce residual moisture because polyamide melts undergo hydrolytic chain scission when water is present above critical limits. For high-temperature polyamides of this class, moisture should be reduced below 0.10 wt% before extrusion. Moisture content is measured by Karl Fischer titration according to ISO 15512:2019 or ASTM D6869-17. A desiccant dryer with a dew point below -40 °C and air temperature in the 80–100 °C range for 4–12 h is a common class-level protocol. Dried filament should be transferred directly to a heated or sealed hopper, and open spool residence in ambient air should be limited if relative humidity exceeds 60%. Moisture uptake is rapid; nylon filaments can re-absorb moisture within hours under humid plant conditions and produce surface splay, reduced melt strength, and dimensional variation in the printed part.
Melt processing is controlled by the viscosity of the high-temperature polyamide and the thermal stability of the melt. The melt volume-flow rate is checked according to ISO 1133-1:2022 using the loading condition specified in the manufacturer’s datasheet; for high-temperature polyamides, this is frequently reported at 275–300 °C with 2.16 kg or 5 kg applied mass. A change in MVR greater than 10% across lots may indicate moisture, chain scission, or masterbatch variation and requires adjustment of extrusion temperature or drying before production. On FFF equipment, direct-drive all-metal hot ends rated for continuous operation at or above 300 °C are used, with hardened steel or nickel-plated brass nozzles selected for abrasion resistance if the grade is filled. The extrusion window is typically narrow; nozzle temperatures below the required melt range produce under-extrusion and poor interlayer strength, while excessive residence time above the upper limit can generate oxidative degradation products and discolouration. Print-speed and nozzle-orifice combinations are selected to maintain shear rate within the stable, melt-fracture-free range, but published data for this specific configuration are limited.
On production-scale FFF lines, the primary processing bottleneck is frequently batch-to-batch filament diameter variation rather than melt temperature. A laser micrometer with ±0.01 mm resolution should be used to log diameter along each spool. Ovality above 0.05 mm on a 1.75 mm filament can cause under-extrusion or stripping in direct-drive extruders. Filament buckling in Bowden feed systems occurs if the feed path contains sharp bends or if the filament is softened by preheat; direct-drive configurations are preferred for high-temperature polyamides. If moisture is reintroduced before printing, the extrudate develops splay marks and the melt viscosity drops due to hydrolysis. This is indistinguishable from thermal degradation by appearance alone, so moisture measurement must be used to separate the two causes before adjusting processing parameters.
For semi-crystalline high-temperature polyamides, interlayer adhesion depends on the thermal history after deposition. Differential scanning calorimetry according to ISO 11357-3:2018 identifies the melting endotherm and recrystallization onset. If the build chamber is maintained below that onset, each deposited layer may cool below the effective glass transition before the next layer is placed. That quench reduces polymer chain diffusion across the interface and produces low weld-line strength in the Z direction. An enclosed chamber held in the class-level range of 70–110 °C is therefore used to slow solidification and allow consolidation. Part-cooling fans should be disabled or limited to a duty cycle below 20% unless overhang quality requires intermittent cooling. The bed is typically maintained at 70–110 °C with a polyamide-specific or PEI build surface to control first-layer shrinkage and lift-off. Large flat parts may require sacrificial brims or adhesion promoters because the differential shrinkage between the initial layer and upper layers creates residual stress concentrations that can exceed the bed adhesion force and produce corner delamination.
Application evaluation for LUVOCOM 3F PAHT 9826 BK includes functional tooling, jigs, fixtures, brackets, housings, and other components exposed to moderate mechanical load and elevated temperature. For creep-limited applications, long-term deformation should be measured under ISO 899-1 at the actual service temperature, not inferred from short-term tensile data. Chemical resistance to oils, greases, cleaning agents, and fuels is class-typical for polyamides but must be tested according to ISO 175:2010 using the actual contact medium and temperature. The material is not presumed to be food-contact, medical, or flame-retardant certified unless those certifications appear in the supplier batch documentation or regulatory status certificate. For automotive or industrial applications above continuous 100 °C, oxidative aging, creep, and fatigue must be validated on the actual printed part and not on injection-moulded proxies. If post-printing annealing is used to increase crystallinity and reduce internal stress, dimensional change and shrinkage must be characterized. Typical class-level annealing for high-temperature polyamides is conducted at 100–150 °C for 2–4 h with fixturing, but published data for this specific grade are limited.
Because FFF properties are orientation- and processing-dependent, an injection-moulding datasheet cannot replace a filament-specific validation package. The following verification matrix identifies the minimum documentation required for engineering use of LUVOCOM 3F PAHT 9826 BK.
| Parameter | Standard or method | Purpose in AM validation |
|---|---|---|
| Residual moisture | ISO 15512:2019, ASTM D6869-17 | Confirm drying below 0.10 wt% before extrusion to limit hydrolytic degradation. |
| Melt volume-flow rate | ISO 1133-1:2022 | Detect lot-to-lot viscosity drift and set extrusion temperature. |
| Tensile properties | ISO 527-2 | Measure orientation-dependent modulus, yield, and break values in XY and Z. |
| Flexural properties | ISO 178 | Assess rigidity for brackets and housing ribs. |
| Heat deflection temperature | ISO 75-1/-2 | Compare short-term thermal resistance under specified stress; report method and specimen orientation. |
| Impact strength | ISO 179-1/1eU or ISO 179-1/1eA | Evaluate notch sensitivity and effect of layer-interface direction. |
| Density | ISO 1183-1 | Verify filler content and void content after printing. |
| Thermal transitions | ISO 11357-1/-3 | Measure melting and recrystallization behaviour to set chamber and annealing conditions. |
| Chemical resistance | ISO 175:2010 | Generate media-specific property retention data. |
The operational boundary for this material includes drying discipline, chamber temperature, and exposure limits. Filament should not be stored open in uncontrolled ambient air above 60% relative humidity after drying. The material should not be blended with general-purpose nylon feedstock unless compatibility has been verified by MVR and tensile data. For EU market placement, current REACH and RoHS declarations must be obtained from the supplier because thermal data do not establish regulatory compliance. Validation of this grade for long-term service above 100 °C, for safety-critical load cases, or for contact with aggressive process chemicals requires application-specific testing on printed parts, not reliance on class-level comparisons.