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Evonik Vestamid L1722P nf (as-conditioned) Nylon 12

    • Product Name: Evonik Vestamid L1722P nf (as-conditioned) Nylon 12
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 294017
    Density 1.02 g/cm³
    Melting Temperature 172 °C
    Tensile Modulus As Conditioned 400 MPa
    Tensile Yield Stress As Conditioned 30 MPa
    Tensile Yield Strain As Conditioned 25%
    Nominal Strain At Break As Conditioned >50%
    Charpy Notched Impact Strength At 23 C As Conditioned 15 kJ/m²
    Charpy Notched Impact Strength At 30 C As Conditioned 10 kJ/m²
    Heat Deflection Temperature Hdt B 0 45 Mpa 100 °C
    Water Absorption 24h 23 C 0.7%

    As an accredited Evonik Vestamid L1722P nf (as-conditioned) Nylon 12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied as conditioned Nylon 12 pellets in sealed moisture-protective packaging, in 25 kg bags, ready for processing.
    Container Loading (20′ FCL) Load 20′ FCL with Evonik Vestamid L1722P nf Nylon 12 in sealed, palletized bags; secure stowage, moisture protection, and contamination prevention ensured.
    Shipping Ship Evonik Vestamid L1722P NF (as-conditioned) Nylon 12 as non-hazardous polymer pellets. Protect from moisture, excessive heat, and contamination. Use clean, dry packaging; avoid sharp objects. Store upright in ventilated area. No special dangerous-goods requirements for standard transport.
    Storage Store Evonik Vestamid L1722P nf (as-conditioned) Nylon 12 in its original, tightly sealed container in a cool, dry, well-ventilated area. Keep away from direct sunlight, excessive heat, and oxidizing agents. Maintain low humidity to prevent moisture absorption, as the material is hygroscopic and its conditioned properties depend on stable moisture content.
    Shelf Life Store in original sealed packaging in a cool, dry place; shelf life is typically two years from manufacture date.
    Application of Evonik Vestamid L1722P nf (as-conditioned) Nylon 12

    In heavy-duty commercial vehicle braking circuits, polyamide 12 tubing is specified for compressed-air supply and control lines connecting the compressor, air dryer, reservoir, and brake chambers. The as-conditioned grade L1722P nf is melt-extruded into monolayer tubing with outside diameters from 6 mm to 16 mm and wall thicknesses from 1.0 mm to 2.0 mm. Compliance is evaluated against SAE J844 Type A and ISO 7628-2, including cold-temperature impact at −40 °C under ISO 7628-2, oil resistance, burst pressure retention, and UV exposure. The natural grade contains no carbon black; exposed installations require black pigmentation with a carbon black masterbatch at the compound supplier’s approved let-down ratio, because unfilled natural PA12 does not retain long-term UV resistance in under-hood or chassis locations. For extrusion, a single-screw extruder with L/D 30:1 to 36:1 and a barrier screw is operated with barrel temperatures from 210 °C to 240 °C, die temperature 220 °C to 250 °C, and vacuum calibration to hold ovality below 0.15 mm. The as-conditioned designation refers to the mechanical test state, not the recommended melt-processing moisture level; the resin is dried to 0.08 wt % or less in a desiccant dryer with dew point below −30 °C. Water-bath cooling at 40–60 °C minimizes residual stress. End products include tractor-trailer air brake harnesses, bus suspension leveling lines, and trailer ABS sensor tubing.

    Where Does L1722P nf Sit in Diesel Fuel Return Line Construction?

    Diesel fuel return lines operating under the hood and along the chassis require retention of burst strength after long-term exposure to petroleum fractions and biodiesel blends. L1722P nf is coextruded as the outer and inner layers of three-layer or five-layer fuel lines, with EVOH as the hydrocarbon barrier core and maleic-anhydride-grafted tie layers. The outer PA12 layer contributes abrasion resistance, low-temperature impact, and chloride stress-cracking resistance; the inner layer controls fuel swelling and prevents plasticizer extraction into the fuel stream. Typical tube dimensions are 8 mm OD with 1.0 mm wall; dimensional and permeation acceptance is established under SAE J2260 and ISO 19013-1 for diesel fuel hoses. Measured permeation depends on EVOH layer thickness and tie-layer continuity, not on the PA12 surface layers alone; published data for this specific multilayer configuration is limited and must be generated for the actual layer ratio. Processing requires coextrusion heads with spiral mandrels, individual extruder melt temperatures 200–230 °C for the PA12 layers, and vacuum calibration. The as-conditioned state of L1722P nf reduces the risk of brittle fracture when cold-formed into bundled chassis routings. End products include light-commercial diesel fuel return lines, auxiliary heater supply lines, and genset fuel tails.

    Pneumatic Control Tubing in Automated Assembly Cells

    Flexible pneumatic control circuits in industrial automation are built from PA12 tubing because of its fatigue resistance under high cycle counts and its dimensional stability in varying plant humidity. L1722P nf is extruded into OD sizes from 4 mm to 16 mm with tolerance class ±0.05 mm, then either straight-cut or coiled. Compliance with ISO 14743 for pneumatic fluid power tubes and ISO 4414 for system design; tubes are tested for burst at rated working pressure, typically rated at 0.4–1.0 MPa. The natural colour permits laser marking for circuit identification but offers no UV protection; indoor enclosures are therefore the dominant installation environment. The grade is supplied as-compounded without the need for external plasticizer addition; introducing low-molecular-weight plasticizer into the melt is not recommended because it shifts Shore D hardness and may create migration risk at connection points. Extrusion uses a single-screw extruder with a mixing section and an in-line gauge scanner; melt temperature is kept at 210–230 °C, with die-head pressure 15–25 MPa and haul-off speed adjusted to control residual draw ratio between 1.05:1 and 1.20:1. The as-conditioned moisture state minimizes post-extrusion dimensional change from water absorption; tubes are annealed at 80 °C for 2 h in some lines to stabilize crystallinity. End products include robotic end-effector air lines, valve-manifold jumpers, and bulk tubing for panel builders.

    Sheathing Low-Voltage Sensor Cables for Cold-Climate Wind Turbines

    Low-voltage sensor and control cables in wind-turbine nacelles require jackets that survive continuous flexing at low temperatures without plasticizer migration cracking. L1722P nf is used as a jacket compound either unmodified or with 2–3 wt % of a processing stabilizer masterbatch; the natural resin is not flame-retardant and must not be used in circuits requiring IEC 60332-1 flame propagation resistance unless compounded to a flame-retardant variant by a qualified compounder. Performance is assessed under ISO 6722 for abrasion and ISO 14572 for low-voltage cable sheathing; cold impact is verified at −40 °C using IEC 60811-506. Compound-level REACH and RoHS declarations are typically issued by the jacket compounder, not the neat resin. Pressure extrusion with a 90 mm single-screw extruder and a double-head crosshead is used to apply the jacket to shielded pairs; melt temperature at crosshead is 215–235 °C and screw speed is limited to avoid shear heating above 250 °C. The as-conditioned moisture state increases elongation at break; however, cable manufacturers dry the resin to 0.08 wt % immediately before extrusion to prevent foaming. Draw-down ratio is set between 1.5:1 and 2.5:1, with cooling troughs at 15–30 °C. End products include nacelle sensor harnesses, yaw-drive feedback cables, and tower lighting circuits.

    For low-pressure hydraulic return and lubrication circuits, conditioned L1722P nf provides a semi-flexible tube that withstands mineral oils, ester-based hydraulic fluids, and aqueous glycols at temperatures below 70 °C; the tube is not rated for high-pressure hydraulic service above 1.0 MPa working pressure. Extruded OD is 10 mm to 25 mm with wall thickness 1.0 mm to 2.5 mm. Compliance is normally established by supplier certification to ISO 15987 for PA12 moulding and extrusion materials and by end-product testing under ISO 1402 for rubber and plastics hoses. The material is processed on a grooved-feed single-screw extruder with heated feed throat at 60–80 °C, barrel zones 210–225 °C, and a spiral mandrel die to avoid weld lines. Because the feedstock is supplied in the as-conditioned state, the moisture level at the feed port determines whether additional drying is required; a desiccant hopper dryer at 80 °C for 4–6 h lowers moisture to <0.10 wt %. Finished tubes are cut into metre lengths and coiled; end products include machine-tool lubrication lines, low-pressure hydraulic tank return lines, and vacuum pump exhaust hoses.

    When Peristaltic Pump Tubing Must Maintain Elastic Recovery After 107 Flex Cycles

    Peristaltic pump tubes in chemical dosing systems require repeated compression by rollers without permanent set or surface cracking. Conditioned L1722P nf is extruded into tubing with OD 6.0 mm to 12.0 mm and wall thickness 1.6 mm to 3.2 mm; the as-conditioned state contributes the required elastic recovery and tear propagation resistance. The tube is evaluated for tensile set under ISO 527-2 and for tear strength under ISO 34-1, though published cycle-life data for this specific grade in peristaltic service is limited and pump manufacturers perform application-specific endurance runs with the actual chemical media. The resin is used unfilled; if low extractables are required, a stabilizer masterbatch suitable for fluid-contact service is selected, but the natural grade is not automatically rated for potable water or food-contact use under FDA 21 CFR. Precision extrusion with vacuum sizing and ultrasonic wall-thickness measurement is required; melt temperature is 200–220 °C, and post-extrusion annealing at 80 °C for 2 h stabilizes hoop stress. End products include industrial chemical metering pump tubes, wastewater analyzer reagent lines, and ink-dosing pump elements.

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    Certification & Compliance
    More Introduction

    Evonik Vestamid L1722P nf (as-conditioned) is an unfilled polyamide 12 powder supply form based on the semicrystalline nylon 12 backbone. The product designation separates the L-series PA12 chemistry, the 1722 viscosity architecture, the P powder morphology, and the nf natural fine descriptor. The as-conditioned qualifier references test specimen conditioning under ISO 291 at 23°C and 50% RH, not dry-as-molded or freshly sintered states. This distinction is material because absorbed water acts as a plasticizer in polyamide 12, lowering tensile modulus while increasing chain mobility and notched impact response. The product is used in powder-bed additive manufacturing, and in some processing lines for thin-layer electrostatic or fluidized-bed coating. The low amide density of PA12 yields lower equilibrium moisture uptake than PA6 or PA66 and permits more stable dimensions in humid service. The powder is unfilled; it contains no glass or mineral reinforcement and therefore differs from filled compounds in recoater abrasion, elongation, and isotropy.

    The nylon 12 chain contains approximately one amide group per 12 methylene units, which reduces the concentration of hydrogen-bonding sites relative to PA6 or PA66. The resulting semicrystalline morphology exhibits a melting range controlled by the α- and γ-crystal forms. In laser sintering, the powder absorbs 10.6 µm CO2 laser radiation and undergoes rapid local melting without a solvent. The low water uptake of PA12 relative to short-chain polyamides reduces the dry-to-conditioned modulus shift but does not eliminate it. This is one reason the as-conditioned qualifier must be retained when comparing datasheet values across grades or when converting an injection-molded PA12 design into a laser-sintered part.

    What Does the nf Descriptor Change in Powder-Bed Processability?

    In powder-bed processes, the nf designation corresponds to a natural, fine particle size cut. This influences layer formation in SLS systems where powders are spread at typical layer thicknesses of 0.08 mm to 0.12 mm; a fine cut with a d50 in the lower micron range can reduce surface roughness but may increase electrostatic adhesion, reduce bulk flow, and require hopper agitation. Published data for this specific configuration is limited in open literature; therefore the d10, d50, d90, bulk density, Hausner ratio, and avalanche energy from each lot must be verified against the certificate of analysis. On production-scale SLS platforms using 30 W CO2 lasers emitting at 10.6 µm, PA12 absorbs the beam energy and melts the semicrystalline phase. The fusing window is set between the melting onset and the crystallization temperature; excessive bed temperature narrows the recrystallization boundary and promotes curl, while insufficient bed temperature increases part growth and warpage. Laser power, scan spacing, beam compensation, and refresh feed rate are machine-specific and are not transferred directly between equipment suppliers.

    Moisture conditioning retains sufficient absorbed water in PA12 to suppress glass transition response and enhance notched impact relative to dry samples. Typical moisture uptake for PA12 at 23°C and 50% RH is approximately 0.5 wt% to 0.7 wt% per ISO 62, whereas water saturation is near 1.5 wt%. Drying is mandatory when storage exceeds 60% RH or when open-air exposure has been prolonged; typical powder drying conditions for PA12 are 80°C to 90°C for 4 h to 6 h in a desiccant dryer, but the time–temperature profile must avoid sintering at particle contacts. Agglomerated particles larger than the recoater gap produce streaks and short feeds in powder-bed machines. Storage under nitrogen or sealed moisture-barrier containers is used on production lines to cap moisture absorption and reduce thermo-oxidative aging during idle periods. Batch-to-batch variance in residual moisture after conditioning is small when the same conditioning protocol is enforced, but part thickness and crystallinity shift the time to equilibrium.

    Thermal and Mechanical Response Under As-Conditioned Equilibrium

    The following typical values consolidate laser-sintered test bar data for unfilled PA12 conditioned per ISO 291. They are process-dependent indications rather than a material specification. Build orientation, laser energy density, and powder reuse state can move tensile elongation and notched impact more than the conditioning state itself.

    PropertyTest methodTypical value
    DensityISO 1183-11.01 g/cm³
    Tensile modulusISO 527-1/-21500 MPa
    Tensile strengthISO 527-1/-245 MPa
    Elongation at breakISO 527-1/-220%
    Flexural modulusISO 1781400 MPa
    Charpy notched impactISO 179-1/1eA4.5 kJ/m²
    HDT B at 0.45 MPaISO 75-2155°C
    Melting peakISO 11357-3178°C

    The as-conditioned tensile modulus falls below dry injection-molded PA12 because water plasticizes amorphous regions. Notched Charpy impact improves under the same plasticization. Build orientation exerts a stronger influence on elongation than does moisture content; parts built in the z-axis show lower interlayer elongation due to incomplete interlayer coalescence at the energy floor. The melting peak near 178°C is characteristic of the α/γ crystal population in PA12; laser sintering from a heated bed yields a slower cooling path than injection molding, producing different lamellar thickness distribution and a different balance of elastic modulus and yield stress. Porosity remaining after sintering is a function of energy density, scan strategy, and layer thickness, and is not represented in the table. For applications where pressure tightness or fatigue resistance is required, the porosity distribution must be characterized by micro-CT or optical cross-section.

    Lot-to-lot variability in the powder is managed through melt volume rate, particle size distribution, and bulk density release limits. Incoming inspection on production lines typically includes sieve analysis, apparent density, and moisture content. If the d50 shifts upward, the minimum layer thickness may need to increase and the laser energy density may require adjustment to achieve the same part density. If the d10 fraction increases, fines can accumulate on heat shields and beam windows, causing thermal drift in the build chamber. These operating observations are not unique to any single SLS platform; they arise from the powder’s cohesion and particle size distribution.

    When Reuse Cycles Increase Melt Viscosity and Reduce Recrystallization

    Powder reuse is the largest source of drift in SLS production. Virgin L1722P nf powder is mixed with refurbished powder at ratios set by the build chamber fill factor, part packing density, and measured melt flow rate. After successive cycles, polyamide 12 undergoes thermo-oxidative chain extension and branching; the melt flow rate measured under ISO 1133-1 falls, and the viscosity rise reduces the ability of the melt to heal interlayer interfaces. A drop in melt flow rate below the lot-defined floor changes the fusing behavior and can produce lower notched impact and greater interlayer porosity. Oxygen uptake also shifts the crystallization exotherm and can widen or narrow the processing window depending on the dominant degradation pathway. Production lines monitor melt flow rate, bulk density, and yellowness after each build; when the melt flow rate falls below the supplier’s minimum tolerance, virgin material is blended to restore process stability. The exact refresh ratio cannot be fixed generically. It depends on laser energy density, bed temperature, part surface-to-volume ratio, and chamber packing density. High bed occupancy at high energy density consumes more antioxidant and accelerates molecular weight growth; low bed occupancy may not age the powder as quickly but can produce more waste.

    In service, unfilled PA12 sintered parts exhibit ductile yielding under slow tensile loading and brittle fracture under high-rate or notched loading. The notched Charpy test under ISO 179-1/1eA is particularly sensitive to interlayer voids and residual porosity. A part with acceptable tensile strength can still fail notched impact if the z-axis interfaces are not fully healed. Consequently, build orientation is not a secondary variable; the datasheet value for notched impact is useful only when the specimen orientation and notch plane are reported. This is a common qualification gap when moving from material datasheet to part design.

    Compared with glass-filled or carbon-filled PA12 powders, the unfilled nf grade provides lower stiffness when tested under ISO 527-1/-2, lower density, and higher elongation, but it sacrifices modulus and creep resistance at elevated temperature. Compared with PA11 powder, PA12 exhibits a lower melting peak and lower water uptake per ISO 62; PA11 may provide higher elongation in impact-dominated parts. Compared with PA6 and PA66, PA12’s longer methylene sequence reduces equilibrium moisture uptake, which supports dimensional stability in humid operating environments. The L1722P nf is not interchangeable with extrusion-grade or injection-molding-grade PA12 pellets; the powder particle size distribution and surface chemistry are controlled for powder-bed spreading rather than screw feeding. It also differs from coarse coating powders because the fine cut promotes film levelling in electrostatic spray and fluidized-bed coating but may require flow aids to maintain consistent powder pickup. For metal coating applications, substrate pretreatment and cure temperature must be matched to the PA12 melt rheology; the same grade can flow out to a continuous film only above the crystalline melting range.

    After SLS, parts are depowdered, bead blasted, and optionally dyed or vibratory finished. The as-conditioned state is established after the part reaches moisture equilibrium; freshly sintered parts removed from the build cake may be dry and stiffer. Dyeing in acid or disperse dye baths raises moisture and can plasticize the surface; dimensional changes may occur depending on wall thickness and dye chemistry, but published data for this specific grade and dye chemistry is limited. Sealing with acrylic or polyurethane coatings closes residual porosity and changes the moisture uptake rate, so mechanical testing should be performed on finished parts rather than uncoated test bars when the coating is part of the design.

    Regulatory Qualification Is Triggered by End-Use, Not by Base Resin

    The base polyamide 12 resin does not automatically transfer compliance from one application to another. The following matrix identifies the minimum qualification routes used in downstream manufacturing.

    Framework or standardScopeQualification requirement
    REACH (EC 1907/2006)Resin and article importVerify SVHC status and lot SDS; restriction list applicable to end-use
    RoHS 2011/65/EURestricted substancesUnfilled PA12 typically below thresholds; test colored or dyed final parts
    FDA 21 CFR 177.1500Nylon resins for food contactEnd-use restrictions and migration testing apply; resin compliance alone is insufficient
    ISO 10993-1:2018Medical device biocompatibilityCytotoxicity, sensitization, and irritation assessment on final device configuration
    ISO 527-1:2019Tensile testingCondition per ISO 291; report build orientation and test speed
    ISO 1133-1:2022Melt flow rateMonitor powder reuse drift and incoming lot acceptance

    Storage and handling boundaries are governed by the powder’s fine particle size and semicrystalline thermal profile. The product should be kept sealed below 60% RH and below 40°C to limit moisture pickup and premature thermo-oxidative aging. Open-air handling should be minimized in high-throughput powder-bed machines; where conveyors and sieving stations are used, dust extraction and antistatic grounding must be installed to prevent combustible dust accumulation. The powder is not a finished medical device or food-contact article. Application-specific validation under device or food-contact regulatory frameworks is mandatory and must include final-part testing rather than resin certification alone. In laser-sintered production, requalification is required when the powder supplier, machine manufacturer, or refresh ratio changes, because mechanical values shift with those variables. Published data for this specific configuration is limited for highly filled, colored, or chemically post-treated parts; processors should generate their own design allowables using the relevant ISO or ASTM method before committing to lot-specific process parameters.

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