| HS Code | 477656 |
| Density | 1.01 g/cm³ |
| Melting Point | 178 °C |
| Tensile Modulus | 1200 MPa |
| Tensile Yield Stress | 45 MPa |
| Elongation At Break | 50% |
| Charpy Notched Impact Strength 23c | 10 kJ/m² |
| Charpy Unnotched Impact Strength 23c | no break |
| Water Absorption 24h | 0.2% |
| Water Absorption At 50 Percent Rh | 0.7% |
| Water Absorption Saturation | 1.5% |
| Heat Deflection Temperature A 1 8 Mpa | 45 °C |
| Heat Deflection Temperature B 0 45 Mpa | 100 °C |
| Vicat Softening Temperature B50 | 145 °C |
As an accredited Evonik Vestamid L1621 sw (dry properties) Nylon 12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Evonik Vestamid L1621 sw (dry properties) Nylon 12 supplied in sealed 25 kg polyethylene-lined bags, protected from moisture. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Evonik Vestamid L1621 sw nylon 12, dry granules, packed securely for safe transport. |
| Shipping | Vestamid L1621 sw Nylon 12 ships as a dry, moisture-sensitive powder. Use sealed, vapor-proof containers to prevent water absorption, which alters properties. Store in cool, dry conditions, away from heat and humidity. Avoid dust dispersion; ground equipment. Transport at ambient temperature. Protect from impact and contamination to ensure product integrity. |
| Storage | Store Vestamid L1621 sw Nylon 12 in its original, unopened packaging in a cool, dry, well-ventilated area away from direct sunlight and heat sources. Keep containers tightly sealed to prevent moisture absorption, as the resin is hygroscopic. Recommended storage temperature is below 30°C. Under these conditions, shelf life is typically 2 years. |
| Shelf Life | Shelf life is typically 2 years when stored dry, cool, and in original sealed packaging. |
In evaporative emission lines that carry oxygenated gasoline blends, a coextruded outer jacket made from Evonik Vestamid L1621 sw is processed in a dry-air hopper with a dew point of −40 °C and a residence time of 4 h at 80 °C. The jacket is not in direct fuel contact; it is positioned as the outermost layer over an EVOH barrier and an inner conductive layer, with each tie layer processed at a melt temperature deviation not exceeding ±3 °C across the annular die. The outer PA12 layer must retain impact strength after cyclic exposure to zinc chloride solution, road salt, and stone impingement at −40 °C. The qualification matrix applied to the jacket is shown below.
| Property or check | Standard | Condition | Acceptance criterion |
|---|---|---|---|
| Tensile properties after conditioning | ISO 527-2:2012 | 23 °C, 50 % RH | Report yield stress and elongation at break |
| Notched Charpy impact | ISO 179-1:2010 | −40 °C | No complete break in outer layer |
| Multi-layer fuel vapour line construction | SAE J2260-2004 | As specified in standard | No delamination at tie layers |
| Water absorption | ISO 62:2008 | Immersion at 23 °C | Record mass change |
| Chemical resistance to road deicing agent | DIN 73378 | Conditioned rod specimen | No surface cracking |
On production-scale lines the limiting factor is not the PA12 jacket itself but the EVOH tie-layer residence time. If the outer layer temperature drops below the upper limit of the tie layer at the die lip, interlayer adhesion at the weld line falls below the peel threshold required by SAE J2260-2004. A gear-pump controlled feed to the outer layer die mandrel reduces melt pressure fluctuation; local wall-thickness thinning under the clip area is monitored because a reduction below the specified minimum creates a stress concentration in the stone-impingement test. The outer jacket is also subjected to heat ageing at 100 °C for 1,000 h and then impacted at −40 °C; brittle fracture of the dry-as-molded compound during this sequence indicates excessive thermal oxidation or insufficient drying before extrusion.
Pneumatic brake tubing with nominal dimensions of 8 mm outside diameter and 1 mm wall thickness is extruded on a grooved-feed single-screw line with a barrel L/D 30:1, a vacuum-sizing tank, and a four-point ultrasonic wall gauge. The drawdown ratio between the die gap and the final wall is treated as a critical parameter because excessive drawdown freezes in residual hoop stress that reduces burst pressure retention after thermal cycling. Hydrostatic testing is performed at 25 °C and 80 °C according to ISO 7628-1; the 80 °C burst requirement is the controlling acceptance limit because the tensile yield stress of PA12 declines with temperature. Low-temperature impact after heat ageing is evaluated at −40 °C per ISO 179-1/1eA; the dry-as-molded condition is relevant because the component is installed in a chassis location where moisture equilibrium is reached only slowly. The tube surface is imprinted with identification marks using hot-foil printing. If the foil tool exceeds the validated upper set point, local surface roughening acts as a notch and initiates brittle failure in the −40 °C impact test. On automatic coilers, the winding tension is limited because excessive coiling stress rearranges the residual hoop stress from sizing and increases ovality after the coil is relaxed.
Inside central loose-tube fibre buffers for outdoor optical cables, a thixotropic filling gel remains in continuous contact with the PA12 buffer tube wall. The buffer tube is chosen because the lower moisture absorption of PA12 compared with PA66 reduces tube tightening on the fibres after submersion and thermal cycling. The tube is commonly drawn to an outside diameter of 2.0 mm to 3.0 mm with a wall thickness of 0.15 mm to 0.25 mm; wall-thickness control is performed by a laser diameter gauge operating at a scanning frequency of 1 kHz. Gel compatibility is evaluated by ageing the buffer tube in the filling compound at 85 °C for 30 days and then checking outer diameter change according to IEC 60794-1-2. The extrusion line speed is constrained by melt fracture onset rather than by gel pick-up. A polished die land with a length-to-diameter ratio of 8:1 to 10:1 delays sharkskin, while an excessively short land generates surface roughness that increases optical attenuation because micro-bending is induced in the fibres. Dry-as-molded PA12 is dried to below 0.10 % moisture before extrusion; moisture above the set point causes surface splay on the buffer tube and a visible shrinkage variation after the water trough.
DEF dispensing hoses for agricultural and off-highway machines are constructed with an inner polyolefin, a PA12 barrier layer, and an outer elastomeric cover. The PA12 layer is selected because the urea solution in DEF is corrosive to many polyamide grades in the presence of heated return flow. The DEF chemistry is defined in ISO 22241-1 as a 32.5 % aqueous urea solution; the fluid is alkaline and promotes hydrolysis of condensation polymers under elevated service temperatures. A coextruded PA12 barrier layer of 0.05 mm to 0.15 mm thickness restricts ammonia and water transport sufficiently to maintain the conductivity of the contained fluid within the limits of ISO 22241-1 during recirculation. Compatibility of the complete hose is evaluated according to ISO 22241-3 by measuring extractable metals and aldehyde formation after hot fluid circulation. Processing the barrier layer is sensitive to melt temperature and screw shear; excessive residence time in the extruder produces thermal oxidation that appears as amber discoloration and a measurable reduction in elongation at break. The barrier layer must be continuous and free of pinholes. A pinhole density above the permitted action limit allows the urea solution to reach the outer cover and causes blistering. On production lines, the barrier layer is run with a barrier feedblock and a melt pump for thickness control; melt pressure is monitored because the thin film is less forgiving of flow variation than a thick-walled tube.
Because thin-wall catheter shafts are braid-reinforced and must resist kinking during insertion, the dry-as-molded flexural modulus of the PA12 jacket is used to predict kink radius before extrusion. The shaft is reinforced with a braid of 0.025 mm to 0.050 mm wire diameter, and the PA12 jacket thickness is normally 0.10 mm to 0.20 mm. If barium sulfate is let down at 20 wt% to 30 wt% for radiopacity, dispersion is checked by micro-CT or film radiography; agglomerates larger than 25 µm are rejected because they create weak points in the thin jacket. Published biocompatibility data for this specific configuration is limited; the finished device manufacturer must therefore perform biological evaluation according to ISO 10993-1:2018, including the endpoints listed in the table below. The extrusion melt temperature is set below the threshold at which the barium sulfate-filled compound begins to release acidic volatiles; the production line uses a vacuum vent on the extruder to remove trace volatiles and prevent voids in the catheter wall.
| Endpoint | Standard | Condition | Acceptance criterion |
|---|---|---|---|
| Cytotoxicity | ISO 10993-5:2009 | L929 cell line | No more than grade 2 reactivity |
| Sensitization | ISO 10993-10:2021 | Maximization method | No sensitization |
| Irritation | ISO 10993-23:2021 | Intracutaneous or dermal | No erythema or oedema above grade 1 |
| Leachables | ISO 10993-18:2020 | Extraction solvent | Report as device-specific evaluation |
Precision-machined push-in pneumatic fittings produced from extruded PA12 rod stock are stress-relieved at 80 °C for 4 h before final thread cutting; the threads are inspected to ISO 228-1 and the finished fittings are leak-tested at 10 bar with dry air.
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Vestamid L1621 sw is a plasticized polyamide 12 (PA12) injection-moulding compound supplied in black. The suffix “sw” denotes black pigmentation; “dry properties” refers to the reference state obtained after drying to a moisture content below 0.1 wt% and verified by Karl Fischer titration according to ISO 15512. Dry as-moulded data represent the upper stiffness boundary for design because absorbed water in PA12 acts as a plasticizer. The inherent low moisture uptake of PA12—typically 1.0 % to 1.5 % at saturation under ISO 62—limits the dimensional and mechanical shift between dry and conditioned service compared with PA6 or PA66. The grade is not a glass-filled or impact-modified system; it is a plasticized PA12 with a reduced tensile modulus and a ductile low-temperature failure mode.
The values in Table 1 are representative dry as-moulded results and should be confirmed against the current manufacturer data sheet and lot-specific certificate of analysis.
| Property | Test method | Typical dry value |
|---|---|---|
| Density | ISO 1183-1 | 1.01 g/cm³ |
| Tensile modulus | ISO 527-1/-2 | 400 MPa |
| Tensile stress at yield | ISO 527-1/-2 | 25 MPa |
| Tensile strain at yield | ISO 527-1/-2 | 30 % |
| Tensile strain at break | ISO 527-1/-2 | >200 % |
| Charpy notched impact strength, 23 °C | ISO 179-1/1eA | No break |
| Charpy notched impact strength, −30 °C | ISO 179-1/1eA | No break |
| Ball indentation hardness | ISO 2039-1 | 25 MPa |
| Shore D hardness | ISO 868 | 55 |
| Melting temperature | ISO 11357-3 | 172 °C |
| Vicat softening temperature, B50 | ISO 306 | 140 °C |
| Water absorption at saturation, 23 °C | ISO 62 | 1.0–1.5 % |
The dry condition should not be confused with conditioned values obtained after ISO 1110 accelerated moisture conditioning; conditioning lowers modulus and often raises notched impact response.
Polyamide 12 is produced from laurolactam by ring-opening polycondensation. The longer alkane segment between amide groups reduces density and moisture affinity compared with PA6 and PA66. L1621 sw compounds a plasticizer phase into the PA12 matrix, disrupting interchain hydrogen bonding and lowering dry tensile modulus from unplasticized-PA12 levels near 1,400 MPa to approximately 400 MPa. The plasticizer phase also depresses the brittle-ductile transition and contributes to the no-break Charpy response at −30 °C. The carbon-black pigment serves principally as an ultraviolet screening agent; it does not act as a reinforcing filler, so the low modulus of L1621 sw should not be corrected upward for pigmentation. Compared with impact-modified PA12 grades, L1621 sw achieves flexibility through plasticization rather than elastomer toughening; plasticizer migration behaviour must therefore be considered in hot or solvent-contact service.
Selection of L1621 sw over an unplasticized PA12 grade changes dry tensile modulus from approximately 1,400 MPa to 400 MPa and yield stress from approximately 40 MPa to 25 MPa. The trade-off is intentional: snap-fit assemblies that would crack after repeated engagement in unplasticized PA12 can accept the lower load-bearing capacity because the plasticizer phase increases elongation at break to >200 % and suppresses brittle fracture. Against short-glass PA12 compounds, L1621 sw sacrifices modulus and creep resistance; glass-filled grades can exceed 2,000 MPa in dry tensile modulus, but they produce higher abrasive wear in screw and barrel components and exhibit notch sensitivity. Against PA66, the PA12 backbone of L1621 sw reduces saturation water uptake from 8–9 % to 1.0–1.5 % under ISO 62, which reduces the shift in dimensions from dry to conditioned service in humid environments. The black pigmentation in L1621 sw also provides opacity and ultraviolet screening, but unpigmented PA12 grades are preferred where colour-neutral translucency is required.
In injection-moulding operations, three processing boundaries determine part quality. First, pre-drying in a desiccant dryer at 80 °C for 4 h to 8 h to a dew point of −30 °C or lower is required when regrind content exceeds 20 wt% or storage relative humidity is above 60 %; failure to dry plasticized PA12 can generate surface splay and shot-weight variation. Second, melt temperature should be maintained between 210 °C and 250 °C; barrel residence above 260 °C increases plasticizer volatilization and black-speck formation. Third, mould surface temperature should be held between 20 °C and 60 °C for moderate crystallinity and dimensional stability; lower mould temperatures reduce cycle time but increase frozen-in stress in thick sections. On production-scale toggle-clamp machines with general-purpose screws in the 18:1 to 22:1 L/D range, the lower melt viscosity of L1621 sw relative to unplasticized PA12 permits gate pressures approximately 15–25 % lower for identical wall-stock geometries. The low-shear melt is prone to drool with open nozzles; positive shut-off nozzles are recommended for hot-runner systems. Mould shrinkage after 48 h at 23 °C and 50 % RH generally falls between 1.0 % and 1.5 % when measured per ISO 294-4, but shrinkage is strongly dependent on gate freeze time and cavity thickness, so a prototype cavity trial is required for tolerance-critical features.
Capillary rheometry according to ISO 11443 shows pseudoplastic flow; at shear rates above 100 s⁻¹ the shear-thinning effect becomes pronounced. The Cross-WLF parameters supplied with commercial flow-simulation databases should be used for gate-pressure prediction. The plasticizer phase reduces die swell relative to unplasticized PA12, but also reduces screw friction; low back pressure in the 30–60 bar range is typical, and screw recovery time should be monitored to detect feed-throat bridging or screw slippage.
Automotive snap-fit clips and cable retainers use L1621 sw where installation in an engine compartment combines low-temperature assembly and vibration. For these parts, low-temperature impact is assessed with Charpy notched specimens at −30 °C per ISO 179-1/1eA; the grade typically records no break. The same ductility supports living-hinge designs in industrial enclosures where repeated flexural cycles at 23 °C and 50 % RH are specified. Fluid-contact applications are limited primarily to fuels and aliphatic hydrocarbons because plasticizer extraction in polar solvents or strong alkaline media can reduce low-temperature ductility; published data for this specific configuration in methanol or glycol-based fluids is limited, and compatibility testing under ISO 175 is required. Applications in medical device housings may require grade-specific confirmation against ISO 10993-1, because the plasticizer system and carbon black pigment are part of the biocompatibility package. Regulatory status under FDA 21 CFR 177.1500 for nylon resins is available only if the supplier issues a grade-specific compliance statement; the base PA12 chemistry should not be assumed to cover the plasticizer package.
Thermal-ageing behaviour for L1621 sw is governed by plasticizer retention rather than oxidation induction. Long-term heat ageing should be assessed under ISO 188 at candidate service temperatures; continuous use above 90 °C can accelerate plasticizer migration and surface tack. The black grade is not inherently flame-retarded; any flame-class claim requires grade-specific testing under IEC 60695-11-10 or UL 94. Electrical connectors using this grade should be qualified on the finished assembly, because comparative tracking index and volume resistivity values are geometry- and processing-dependent.
Because PA12 contains amide groups, moisture uptake shifts dry-property data to conditioned values. After accelerated conditioning under ISO 1110 at 70 °C and 62 % RH, the tensile modulus of plasticized PA12 can decrease by 10–30 % relative to the dry condition, while notched impact strength often increases. Dry-property data should therefore be used for initial snap-fit design only with a moisture correction, or conditioned values supplied by the manufacturer should be requested. For dimensional analysis, the water-absorption value under ISO 62 remains the critical input; changes in relative humidity from 20 % to 80 % can produce measurable width changes in long, thin sections. The grade is not recommended for continuous use above 90 °C without additional ageing data from the manufacturer, because plasticizer migration kinetics accelerate with temperature and can lead to embrittlement over time.