EMS-Grivory Grilamid® L 16 W 20 black 9995 PA12
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Product Name:
EMS-Grivory Grilamid® L 16 W 20 black 9995 PA12
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Factroy Site:
Yudu County, Ganzhou, Jiangxi, China
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Price Inquiry:
admin@ascent-chem.com
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Manufacturer:
Ascent Petrochem Holdings Co., Limited
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CONTACT NOW
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EMS-Grivory Grilamid® L 16 W 20 black 9995 PA12 is typically used in formulations when low-temperature impact strength and moisture absorption must be controlled within specific ranges.
Specifications
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HS Code
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160326
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| Material |
Polyamide 12 (PA12) |
| Product Name |
Grilamid L 16 W 20 black 9995 |
| Color |
Black 9995 |
| Density |
1.01 g/cm³ |
| Melting Point |
178 °C |
| Tensile Modulus |
300 MPa |
| Tensile Stress At Yield |
20 MPa |
| Elongation At Break |
>200 % |
| Flexural Modulus |
300 MPa |
| Charpy Impact Strength 23 C |
No break |
| Charpy Notched Impact Strength 23 C |
No break |
| Heat Deflection Temperature 1 80 Mpa |
40 °C |
| Heat Deflection Temperature 0 45 Mpa |
90 °C |
| Vicat Softening Temperature B 50 |
55 °C |
| Water Absorption 24h |
0.6 % |
As an accredited EMS-Grivory Grilamid® L 16 W 20 black 9995 PA12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
Packing & Storage
| Packing |
Supplied in 25 kg sealed, moisture-protective polyethylene-lined paper bags, clearly labeled with product name, black grade, and batch details. |
| Container Loading (20′ FCL) |
20′ FCL: Grilamid L 16 W 20 black 9995 PA12 securely packed on pallets, loaded in a full 20-foot container for transport. |
| Shipping |
This thermoplastic polyamide (PA12) is shipped as dry, sealed granules in moisture-proof bags or containers to prevent hydrolysis. Standard freight (truck, rail, sea) is suitable. Protect from extremes of heat and direct sunlight. No special hazard classification applies, though proper lifting and dry storage are required. |
| Storage |
Store Grilamid® L 16 W 20 black 9995 PA12 in its original, unopened packaging in a cool, dry, well-ventilated area. Keep away from direct sunlight, heat sources, and moisture to prevent degradation. Ensure containers remain tightly sealed when not in use. Under these conditions, shelf life is typically several years. |
| Shelf Life |
Store in a cool, dry place, protected from sunlight and moisture. Shelf life is approximately two years. |
Application of EMS-Grivory Grilamid® L 16 W 20 black 9995 PA12
# Grilamid® L 16 W 20 black 9995 PA12 — Downstream Application Configuration DataThe following technical documentation addresses extrusion and injection molding scenarios for EMS-Grivory Grilamid® L 16 W 20 black 9995. Processing parameter bands are drawn from publicly accessible PA12 extrusion literature and ISO annexes; where proprietary grade-specific data is not published, this is explicitly noted.## Fatigue-Resistant Air Brake Tubing in Heavy Commercial Vehicle Pneumatic SystemsPolyamide 12 compounds with medium relative viscosity (RV 1.6–1.7 in m-cresol) have been adopted for single-layer compressed air braking circuits because the polymer’s amide group spacing yields a low equilibrium moisture uptake of <0.75% at 23 °C and 50% RH, limiting dimensional excursion during dew-point cycling in pneumatic lines. Grilamid L 16 W 20 black 9995 is configured for vacuum-calibrated tube extrusion with a carbon black loading that confers UV screening sufficient for under-chassis exposure, as stipulated under ISO 7628-1:2016 for thermoplastic air brake tubing. Compliance verification for this scenario includes long-term heat aging at 100 °C ± 1 °C for 94 days, cold impact at −40 °C following ISO 7628-2 impact procedures, and resistance to zinc chloride solutions per OEM CVS-09100-type protocols applicable to road salt hydrolysis products.Formulation addition ratios for production of air brake lines using this compound follow a regrind ceiling of 20 wt% with 80 wt% virgin pellets, provided the regrind fraction is generated from clean, moisture-controlled sprues or tube scrap. Processing aids such as high-molecular-weight siloxane masterbatches may be introduced at 0.2–0.5 wt% only where internal surface roughness exceeds a melt-fracture threshold upon 50× magnification of microtome sections. Drying prior to extrusion is non-negotiable: residual moisture must be <0.10 wt% (Karl Fischer titration, ISO 15512:2019) to avoid hydrolytic viscosity loss at melt temperatures above 250 °C.Downstream manufacturing uses single-screw extruders with screw diameters from 45 mm to 75 mm and L/D ratios of 25:1–30:1. The screw geometry recommended for this grade is a three-zone barrier screw with a compression ratio of 2.4–2.7:1 and a mixing section of at least 4D length incorporating Maddock-style dispersive elements. Barrel zone settings from feed to metering are typically 220 °C / 235 °C / 245 °C / 250 °C with die head held at 250–255 °C. Vacuum calibration uses a closed-loop water temperature of 15–20 °C, and pneumatic sizing pressure is maintained at 0.02–0.05 MPa to prevent collapse of 8 mm OD × 1 mm wall tubing during the amorphous-to-crystalline phase transition.The terminal product profile concentrates on triple-coiled, heat-stabilized single-layer tubes in outer diameters from 6.0 mm to 16.0 mm for pneumatic circuits on tractor-trailer combinations and rigid trucks. Published data for this specific configuration for burst-pressure degradation after 1,000 h hot-oil exposure is limited; verification batches should therefore include burst testing at 23 °C and 100 °C against OEM-specific acceptance criteria rather than relying on extrapolated PA12 generic values.## Industrial Pneumatic Control Lines in Automated Assembly Cells and Semiconductor Cleanroom Sub-fab InfrastructureFor polyamide tubing destined for compressed air distribution in automation cells, the governing purchase specification is frequently ISO 14743:2004, which addresses push-in connector compatibility and defines dimensional limits for outside diameter and roundness under pressure cycling. Polyamide 12 is selected over PA6 or polyurethane where low water absorption is required to maintain a stable pressure drop across the line, and where zinc chloride or residual machining coolant mist is present in the working atmosphere.Readiness for this downstream field begins with pellet conditioning in a desiccant dryer at 80 °C for 4–6 h until residual moisture falls below 0.10 wt%, as determined by a dew-point transmitter on the hopper return air. Failure to observe this limit results in visible surface splay and volatile emissions at the die exit due to hydrolysis-induced molecular weight reduction. Where the production line runs continuously, hopper reload frequency should be matched to calculated residence time so that material in the throat does not exceed 15 min under ambient humidity above 40% RH.Formulation flexibility for this application is limited. Published processing guides for similar PA12 extrusion grades advise against the introduction of additional amide-based slip agents at levels above 0.1 wt% because the additive competes for hydrogen-bonding sites at the amorphous–crystalline boundary and can reduce long-term heat-aging resistance. If a higher surface gloss is specified for OEM cleanroom tubing, a silicon dioxide anti-block masterbatch at 0.05–0.10 wt% may be dry-blended at the machine throat, but only after trial-run verification confirms no change in OD ovality detected by dual-axis laser micrometers at a scanning rate of 20 Hz minimum.The extrusion process typically employs a 30:1 L/D single-screw unit with a decompression screw and a grooved feed section operating at 155–175 °C feed-zone temperature to maximize output stability. Melt temperature at the adapter is maintained between 235 °C and 245 °C to keep melt viscosity within the window required for thin-wall die flow. The draw-down ratio from die lip to final tube OD is held at 1.8:1 to 2.2:1 to minimize orientation-induced shrink at elevated service temperature. Post-extrusion conditioning for 48 h at 23 °C and 50% RH yields an equilibrium moisture level of 0.3–0.5 wt%, which improves push-in connector grip beyond the dry-as-extruded condition.Terminal products in this scenario include black 4 mm × 0.75 mm and 6 mm × 1.0 mm pneumatic tubes, cut to standard 50 m coils, with laser-marked traceability codes to satisfy ISO 9001 lot-level recall capability. The compound’s carbon black pigmentation permits direct printing of white part numbers using thermal transfer systems, eliminating a secondary cabling identification process on the end-user assembly line.## Monofilament Extrusion for Paper Machine Clothing and High-Abrasion Filtration FabricPA12 monofilament is produced in flat or round cross-sections for dryer screen fabrics in pulp and paper forming sections, where hydrolytic stability in saturated steam conditions at 110 °C is required. The low amide density of PA12 compared to PA66 yields reduced moisture regain and lower dielectrically measurable moisture-induced dimensional growth on the weaving loom.Published data specific to Grilamid L 16 W 20 black 9995 in monofilament yield is limited; however, generic PA12 extrusion literature establishes that a controlled viscosity of 1.60–1.70 relative viscosity supports orientation drawing after water quenching. The filament line must include a water bath at 55–65 °C followed by a two-stage hot-air oven with first-stage drawing at 80–100 °C and second-stage relaxation at 130–150 °C. Draw ratios for round PA12 monofilament generally fall between 3.8:1 and 4.6:1; higher ratios induce fibrillation at the black pigment agglomerate boundaries, a failure mode observed as micro-voids under 200× transmitted light microscopy.Drying specifications for this process are stricter than for tube because the melt residence time in the filament die is shorter, and small gas inclusions nucleate on carbon black particles. Moisture must be maintained at <0.08 wt% during extrusion. This is typically achieved using desiccant dryers with a −35 °C dew point air supply, regenerated in closed loop, and verified by on-line Karl Fischer moisture analyzers sampling at 10-min intervals.The downstream weaving operation uses high-speed air-jet or rapier looms; filament denier often ranges from 0.18 mm to 0.30 mm diameter. For black monofilament, online diameter measurement uses a single-axis gauging head cross-checked with a dual-axis unit at 15-min intervals; acceptable ovality shall not exceed 0.005 mm for filament destined for fine-mesh screen cloth. Tensile knots and splice failures are reduced when the as-spun filament is conditioned at 65% RH for 72 h before weaving, which increases elongation at break without compromising creep resistance at operating temperatures below 120 °C.## Unlabelled Application: Extended-Durability Gearbox Fluid Conduit in Agricultural MachineryUnder-chassis hydraulic control lines in combine harvesters and self-propelled sprayers expose polyamide tubing to sustained vibration amplitudes of 0.3–0.7 mm at 80–120 Hz from diesel engine harmonics, combined with oil mist and high ambient dust loads. The material selection for such conduits is based on PA12’s lower moisture absorption than PA6 and better resistance to zinc chloride from road de-icing agents that enter the machine bay during transport between fields. Grilamid L 16 W 20 black 9995 provides carbon black UV stabilization for segments routed outside the main body panel, eliminating the need for a secondary protective braid in low-pressure return lines.Processing for this conduit starts with pre-drying to <0.10 wt% moisture using a portable desiccant hopper on the extruder. The extrusion line uses a 38 mm single-screw extruder with 24:1 L/D ratio and a vacuum vent in the transition zone set to −0.08 MPa relative pressure to draw off residual monomers and processing volatiles, though the monomer content of this PA12 grade should already meet the OEM limit of <0.5 wt% caprolactam equivalent for this application. Melt temperature at the die is maintained at 240–255 °C with a pressure before the breaker plate of 15–20 MPa, monitored by a melt-pressure transducer with a high-low alarm to detect filter blockage from carbon black agglomerates.Formulation practice in this field frequently includes up to 15 wt% regrind but the regrind must be ground using a sieve screen of 3.0 mm to avoid unmolten particles at the screw root. The use of external lubricants is prohibited in hydraulic return lines because silicone-based processing aids can contaminate the fluid and generate foam in the reservoir. Barrel temperatures are profiled from 210 °C in the feed zone to 250 °C at the metering section to create a progressive melt without overheating the regrind fraction.Terminal products produced from this process are formed tubing assemblies with outer diameters of 10 mm to 20 mm and wall thicknesses varying from 1.0 mm to 2.0 mm. Final assembly includes crimped steel couplings and vibration-absorbing P-clips. Qualification testing for this application includes burst pressure retention after exposure to a hydraulic oil mixture at 100 °C for 168 h per OEM agricultural machinery specifications, though published data for this specific grade under these conditions is limited.## When PA12 Replaces PA6 in Engine Compartment Wire Jacketing with High-Temperature Cyclic ExposureSingle-layer polyamide 12 jackets on low-voltage electrical cables in engine compartments are specified where the continuous operating temperature does not exceed 125 °C and where short-term excursions to 150 °C are limited to 2 h cumulative over a service life. The black 9995 designation provides UV protection necessary for engine bay areas exposed to sunlight through grilles and undertray gaps.The cable jacketing operation uses a 60 mm 30:1 L/D single-screw extruder with a crosshead die and pressure tooling optimized for wall thicknesses from 0.25 mm to 0.50 mm. Melt temperature at the die exit is held within 235–245 °C to minimize thermal degradation of the semi-crystalline fraction. Wire preheating to 120–140 °C is applied using an induction heater before entering the crosshead die, which improves adhesion of the jacket to the wire bundle and eliminates internal voids at the interface.The formulation window for this scenario is narrow. Published processing literature for semi-rigid PA12 cable jackets indicates that the addition of copper-based heat stabilizers above 0.3 wt% can interfere with the black pigment dispersion and lead to localized dielectric breakdown. Furthermore, lubricant packages containing ethylene bis-stearamide should be limited to 0.1 wt% or avoided entirely, as migration of the amide wax to the interface between cable jacket and connector seal surfaces reduces friction lock retention in automotive connector systems.Downstream process parameters must account for the lower melt strength of PA12 compared to PA6. The air gap between die exit and water trough inlet is minimized to 5–10 mm for thin-wall jackets to prevent draw-down instability. Screw speed is set to maintain a melt residence time of 4–6 s at maximum barrel temperature; longer residence at 245 °C causes measurable increases in yellowness index and a reduction in elongation at break from the as-received value, although published data for this specific black grade is limited beyond a reported elongation at break of >200% for typical PA12 extrusion grades.The terminal product applied in this sector is a single-conductor or multi-conductor automotive cable with black PA12 jacket for use in sensor, fuel injector, and EGR valve wiring. Compliance for such components typically falls under ISO 6722-1:2011 for single-core cables and ISO 14572:2011 for multi-core cables, with supplementary OEM standards requiring bending-stress resistance at −40 °C and no crack formation after aging at 125 °C for 3,000 h.## Extruded Air Induction System Components with High Resistance to Diesel Fuel CondensateCharge-air and crankcase ventilation lines on turbo-diesel light commercial engines subject polymer parts to continuous air flow at temperatures from −30 °C to 120 °C, with intermittent contact from acidic condensate containing nitric and sulfuric acid derived from exhaust gas recirculation mixtures. Polyamide 12 grades with heat stabilization, such as L 16 W 20 black 9995, provide the required sulfurous condensate resistance without the plasticizer migration associated with fully flexible PA11/12 formulations.The production process for these components typically proceeds by twin-screw compounding of a conductive carbon black variant, but for direct extrusion, single-screw profiles with grooved barrels are used. The groove angle is set at 45–60° and the axial length at 3D to maintain high feed rates without excessive pressure generation. A five-zone barrel profile of 215 °C / 225 °C / 235 °C / 245 °C / 250 °C is maintained, with the die temperature trimmed to 255 °C for glossy-surface requirement on visible under-hood sections. Vacuum calibration tanks are operated with water spray temperature at 12–16 °C and negative pressure of −0.03 MPa to keep the parison against the sizing die.Typical wall thickness for crankcase ventilation tubing is 1.5 mm, and the OD is sized to accept circumferential snap-fit connectors. Because of the acidic condensate exposure, additive packages in this application exclude magnesium-based acid scavengers at levels above 0.1 wt%. These compounds can form hygroscopic surface films when the tubing is cycled between high crankcase temperature and cold soak in winter, leading to a visible white efflorescence that is misinterpreted as polymer degradation. Where OEM specifications require improved surface conductivity, the addition of a PA12-based conductive masterbatch at 5–8 wt% is typical, yielding a surface resistivity in the range of 10^4–10^5 Ω/sq under 10 V DC test voltage.Terminal product categories include rigid charge-air tubes with a black exterior finish, crankcase ventilation lines, and diesel particulate filter differential pressure sensor hoses. Published data for this specific grade in compressible-gas crankcase applications with dynamic flex fatigue at 10 Hz is not publicly available; end-of-line validation relies on OEM-specific cyclic pressure pulsation tests at 0.1–0.4 MPa for a minimum of 500,000 cycles.## What Limits Post-Consumer Recyclate Inclusion in Structural Tubing for Cable Protection Conduits?Closed-cell corrugated conduit for cable protection in machine tools requires puncture resistance and flexibility across a service temperature range of −25 °C to 100 °C. PA12 has been used in this class because its notch sensitivity is lower than high-viscosity PA66 at subzero temperatures, and the black pigmentation provides UV stability for conduit routed outside machine frames. The L 16 W 20 black 9995 grade is an extrusion material for corrugated profiles manufactured on vacuum-forming corrugators after the melt exits a straight annular die.The extrusion-corrugation line combines a 50 mm single-screw extruder with a corrugator operating at mold block speeds from 1.5 to 4.0 m/s. Melt temperature is maintained at 240–255 °C and the die gap is adjusted to produce a parison wall thickness of 0.35–0.50 mm, which is thinned to 0.20–0.30 mm at the corrugation crests. The vacuum in the corrugator blocks is held at −0.04 to −0.06 MPa to replicate the mold profile without creating thin spots at the root of the corrugation.The regrind fraction for this application is constrained by the black pigment’s effect on melt strength after repeated thermal histories. Published industrial practice for similar black PA12 grades indicates that post-consumer recyclate (PCR) loading should remain below 10 wt% when the regrind originates from mixed black conduit because pigment agglomeration and oxidative degradation products raise the melt flow index beyond the corrugator’s forming window. At 20 wt% PCR, batch-to-batch variance in corrugation geometry becomes detectable as a change in tensile ring stiffness along the conduit, leading to rejection at OEM incoming inspection.Compliance verification for this component class references IEC 61386-1:2008 for conduit systems for cable management, together with UL 1696 where North American approval is required. Testing includes compression resistance at 23 °C and after conditioning at 80 °C, tensile strength of the conduit joints, and resistance to impact at −25 °C. Because PA12 is not halogen-free, use in railway interiors or low-smoke compartments may be disqualified under EN 45545-2; this limitation must be verified before specifying black 9995 for rolling stock cable protection.End-product forms include corrugated conduit with outer diameters from 10 mm to 54 mm, in slit and unslit configurations, supplied in 25 m or 50 m coils. The black 9995 color supports direct marking with white ink-jet identifiers for batch, size, and material code without the need for a secondary label sleeve.## What Are the Practical Limits for High-Pressure Washer Spray Lance Tubes?Portable high-pressure washer lances and extension tubes have transitioned from brass to thermoplastics where weight reduction and thermal insulation at the operator grip are required. The PA12 grade under consideration is used for the inner tube portion that carries water at pressures up to 15 MPa in consumer and semi-professional pressure washers of up to 2.5 kW electric motor class. At higher pressure classes above 20 MPa, PA12 without fiber reinforcement does not maintain the hoop stress required, and published data for this specific configuration is limited.Direct extrusion of straight lance tubes uses a 45 mm single-screw extruder with a pin and spider die to produce 8 mm OD × 2 mm wall tubes, followed by cooling and straightening rolls. Melt temperature is held at 235–245 °C to permit a high back pressure of 18–22 MPa for homogenization of the black pigment and stabilization package without exceeding the thermal stability boundary. The spray water in use often contains dissolved calcium and magnesium carbonates; PA12’s low water absorption below 0.5 wt% at room temperature limits internal scaling compared to more hygroscopic polyamides.The formulation addition ratio includes a maximum 15 wt% regrind from in-house tube scrap, but the regrind must not contain silicone-based lubricant contamination from downstream assembly operations because even 0.05 wt% silicone contamination causes delamination at the weld line of the pin-and-spider die. Where greater UV resistance is required for outdoor storage of pressure washer units, a carbon black masterbatch at 0.5–1.0 wt% may be added, but the base grade’s black 9995 designation already includes sufficient carbon black for most consumer applications. Tensile impact strength at low temperature is measured per ISO 179-1:2010 Charpy impact testing on notched specimens, with acceptance values set by OEM rather than by ISO minimums.Terminal product types include straight extension lance tubes with quick-connect couplers at both ends, trigger gun inserts, and telescopic lance sections. The inner surface finish must achieve Ra <0.8 µm to prevent O-ring abrasion in dynamic sliding connections; this is achieved by polishing the die land to a mirror finish and maintaining die temperature above 250 °C.---### Comparative Processing Parameters for Reference Applications| Parameter | Air brake tubing | Monofilament | Corrugated conduit ||---|---|---|---|| Preheat drying moisture limit | <0.10 wt% | <0.08 wt% | <0.10 wt% || Melt temperature range | 235–255 °C | 235–245 °C | 240–255 °C || Screw L/D ratio | 25:1–30:1 | 24:1–30:1 | 25:1–30:1 || Regrind ceiling | 20 wt% | 15 wt% | 10–20 wt% || Calibration method | Vacuum sizing | Hot-air oven draw | Vacuum corrugator || Primary compliance standard | ISO 7628-1:2016 | ISO 179-1:2010 (impact) | IEC 61386-1:2008 |The table above summarizes process windows from publicly available PA12 extrusion literature. It is not a datasheet reproduction for Grilamid L 16 W 20 black 9995, as the manufacturer does not publish separate process data for each downstream configuration. End users must verify all parameters against the official EMS-Grivory technical datasheet and application-specific validation programs.
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Certification & Compliance
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EMS-Grivory Grilamid® L 16 W 20 black 9995 PA12 is manufactured under an ISO 9001 quality system and complies with relevant regulatory requirements.
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COA, SDS/MSDS, and related certificates are available upon request.
For certificate requests or inquiries, contact: admin@ascent-chem.com.
More Introduction
EMS-Grivory Grilamid® L 16 W 20 black 9995 PA12 is an unreinforced, plasticized polyamide 12 injection moulding and extrusion grade in the EMS-Grivory L series. The L prefix identifies the PA12 family, which is synthesized from laurolactam or ω-aminolauric acid and carries eleven methylene units between amide linkages. The numerical 16 code denotes a low-to-medium melt-viscosity class within the L series; the W suffix identifies plasticizer modification; the 20 extension is interpreted as a nominal plasticizer level of roughly 20 parts per hundred resin by weight, although the exact plasticizer chemistry is not disclosed in public datasheets. The black 9995 code corresponds to a carbon-black masterbatch that supplies opacity and ultraviolet screening. Under ISO 1043-1, the material is designated PA12 and contains no glass or mineral reinforcement.
The long aliphatic repeat unit reduces the amide-group concentration relative to PA6 and PA66. This structural feature is responsible for density close to 1.01 g/cm³ when measured per ISO 1183-1, saturation water absorption of approximately 1.4% per ISO 62, and a melting temperature of 172–178°C per ISO 11357-1/-3. The dry-as-moulded tensile modulus is in the order of 240–300 MPa under ISO 527-1/-2; yield stress is 15–20 MPa, and nominal elongation at break exceeds 50%. Notched Charpy impact at −30°C is typically reported in the range 10–15 kJ/m² per ISO 179-1/1eA. These are typical values for dry-as-moulded injection moulded specimens and are not specification minima.
Typical comparative property profile: dry-as-moulded values, not guaranteed limits.
| Property | Test method | Unit | Typical value |
| Density | ISO 1183-1 | g/cm³ | 1.01 |
| Water absorption, saturation at 23°C | ISO 62 | % | 1.4 |
| Tensile modulus | ISO 527-1/-2 | MPa | 240–300 |
| Yield stress | ISO 527-1/-2 | MPa | 15–20 |
| Nominal elongation at break | ISO 527-1/-2 | % | >50 |
| Charpy notched impact at −30°C | ISO 179-1/1eA | kJ/m² | 10–15 |
| Melting temperature | ISO 11357-1/-3 | °C | 172–178 |
| Vicat softening temperature B50 | ISO 306 | °C | 80–90 |
The plasticizer in W 20 lowers the glass transition temperature and disrupts intermolecular hydrogen bonding between amide groups. As a result, yield stress and flexural stiffness decrease, while elongation and sub-ambient impact increase. This property balance is intended for flexible snap-fit components, clips, cable ties, and thin-walled geometries that require repeated flexure at low temperature. The low modulus also limits load-bearing capacity in gear-like or creep-sensitive applications; long-term creep data for this specific grade are limited, and creep-sensitive parts should be validated under ISO 899-1 with the actual load and temperature.
The black 9995 carbon-black system improves outdoor weathering relative to natural PA12, but carbon black can reduce surface resistivity and should not be assumed to provide the same insulation values as unpigmented PA12. If electrical insulation is critical, surface and volume resistivity should be measured per IEC 62631-3-1 and IEC 62631-3-2 on the finished part. The grade is supplied as standard black pellets; lot-to-lot variation in carbon black dispersion can influence surface appearance and notched impact.
The stress-strain curve of L 16 W 20 differs from unmodified PA12 in the position of the yield point. The plasticizer allows chain segments to slip at lower stress, so yield stress is reduced and the post-yield plateau is longer. This behaviour is measured at 23°C and 50% relative humidity after conditioning, but the dry-as-moulded condition gives slightly higher stiffness. When parts are exposed to moisture, PA12 undergoes limited plasticization relative to PA6; the change in tensile modulus from dry to conditioned is smaller than in short-chain polyamides. This is one reason why the grade is used for snaps that must maintain assembly force in humid air.
The crystallinity of PA12 is another controlling variable. Cooling from the melt creates spherulites whose size and perfection depend on mould temperature and cooling rate. A mould temperature below 40°C produces smaller, less-perfect crystallites and generally yields tougher parts but lower creep resistance. A mould temperature of 60–80°C promotes more complete crystallisation, reducing post-mould shrinkage and improving chemical resistance. The black pigment may act as a nucleating agent, shifting crystallization to higher temperatures and reducing cycle time compared with natural PA12; this effect is tool-dependent.
How Does L 16 W 20 Compare with PA6, PA66, PA11 and Unplasticized PA12?
The primary practical difference arises from water uptake. PA6 and PA66 can absorb about 9.5% and 8.5% water at saturation under ISO 62, while PA12 L 16 W 20 absorbs roughly 1.4%. This reduces the dimensional and mechanical property shift in humid environments and in parts exposed to intermittent condensation. It also reduces the risk of hydrolysis in hot-water contact, although the grade is not intended for continuous hot-water pressure service.
Compared with unplasticized PA12, the W 20 modification lowers tensile modulus from the typical unplasticized PA12 range of 1400–1600 MPa to below 300 MPa. Yield stress and hardness fall, while elongation and cold impact rise. The trade-off is increased susceptibility to creep and plasticizer extraction. Unplasticized PA12 is more suitable for rigid clips, fasteners, and structural brackets; L 16 W 20 is more suitable for parts that must bend, snap, or absorb impact without fracture.
Compared with PA11, both polymers are long-chain aliphatic polyamides with low water absorption and low density. PA11 may have a higher bio-based carbon fraction depending on the monomer source, while PA12 typically has a slightly lower density and a melting point approximately 10°C lower. Selection between PA11 and PA12 frequently turns on pipe or cable specifications, fuel resistance requirements, and the specific plasticizer package rather than on a single property.
Compared with elastomer-modified PA12, the plasticizer route can offer lower melt viscosity and easier thin-wall filling, but it has a clearer service ceiling because plasticizers may migrate under high heat or be extracted by hot oil, fuel, or polar solvents. Elastomer-modified systems may retain low-temperature impact with less plasticizer loss, but they are typically more expensive and may display higher melt viscosity. Chemical compatibility should be checked per ISO 175 when any fluid contact is expected.
Compared with acetal copolymer and thermoplastic polyurethane elastomers, PA12 L 16 W 20 has a lower density than acetal and better dimensional stability than many TPU grades, but it does not replace acetal where low wear and high stiffness are required, nor TPU where very high elongation and tear strength are required. The grade should be specified on the basis of the entire mechanical, thermal, and chemical environment rather than a single comparative property.
In automotive clips and industrial fasteners, the grade is used where low force-to-assemble and resistance to hydrocarbon fluids, road salt, and low-temperature impact are required. Typical designs include hinge-like snap arms, cable ties with live hinges, closure clips, and pneumatic connector bodies. The black 9995 colour is commonly selected for underhood and exterior parts where ultraviolet exposure and aesthetics require a stable black surface. Field failures in such parts are usually associated with excessive strain at sharp internal radii or plasticizer extraction after long hot-oil exposure; design strain should remain below the yield elongation, and notched impact should be considered at stress concentrations.
When the Grade Is Processed on General-Purpose Three-Zone Screws
Before melt processing, the pellets must be dried in a desiccant dryer at 80°C for 4–6 h to a residual moisture content below 0.10%. If bags have been opened in a plant with relative humidity above 60%, drying times of 6–8 h are often required. A hot-air hopper dryer is not sufficient because it cannot reliably achieve a dew point below −20°C; moisture present at levels above 0.15% causes hydrolysis of the amide linkages in the melt. Production symptoms include splay marks, gas streaks, nozzle drool, reduced melt viscosity, and a loss of Charpy impact after moulding. The hopper should be sealed and the dry-air supply maintained at the hopper inlet during production.
Residual moisture should be confirmed by a calibrated moisture analyzer or Karl Fischer titration; lot-to-lot variation can occur after transport. Incoming resin should also be checked for melt volume-flow rate per ISO 1133-1 if a change in molecular weight due to repeated heat histories is suspected. Published melt-flow data for this exact grade are limited, but the plasticizer modification reduces viscosity compared with unplasticized PA12 of the same melt-viscosity class.
For a 40 mm general-purpose three-zone screw with L/D 20–25 and compression ratio 2.5:1–3:1, barrel temperatures are typically set from 210°C in the feed zone to 240°C at the nozzle. Melt temperature should remain below 250–260°C; above this range, the plasticizer can volatilize, causing deposits on vents and cavity surfaces, and the carbon black can produce local overheating. Start with a low back pressure of 0.5–1.0 MPa and moderate screw speed; excessive shear heating can drive plasticizer to the surface and produce streaks or gate blush. Injection pressure is generally lower than for unplasticized PA12, with a starting injection pressure of 40–80 MPa and hold pressure of 60–80% of injection pressure.
Mould temperature may be set between 20°C and 80°C. Lower mould temperatures shorten cycle time but produce lower crystallinity and may increase post-mould shrinkage and warpage. Higher mould temperatures, particularly 60–80°C, improve dimensional stability and crystallinity but increase cycle time. The optimum depends on wall thickness and required tolerances. For parts that must meet tight dimensional limits after humid service, a post-mould conditioning period at standard atmosphere per ISO 291 is recommended before final inspection.
In production-scale moulding, the grade flows well through restricted gates because of its low melt viscosity, but the same characteristic makes flash control more dependent on clamp force and tool fit. A worn non-return valve can produce shot weight variability because the plasticized melt leaks backward during screw recovery; if cushion stability drops below 2 mm or screw recovery time becomes inconsistent, the check ring and screw tip should be replaced. Regrind from sprues and runners is generally acceptable at 20–25% by weight if the material is dried and not contaminated; repeated heat histories increase viscosity and reduce low-temperature impact, so the regrind fraction should be kept constant in production.
The plasticized grade should not be considered for continuous hot-air service above approximately 80°C. Peak exposure up to 100°C for short cycles may be acceptable, but plasticizer migration and oxidative embrittlement become more probable. Contact with hot oil, fuels, and polar solvents should be tested because plasticizer extraction causes the part to stiffen, shrink, and lose elongation. Dimensional testing after fluid exposure should follow ISO 175 with the actual service fluid at the intended temperature, and mechanical re-testing should follow ISO 527-1/-2 and ISO 179-1/1eA because the dry-as-moulded values will not represent aged parts.
Regulatory statements should be confirmed for the exact grade and colour. The base PA12 may be covered by generic listings such as FDA 21 CFR 177.1500 for nylon resins, but black 9995 carbon-black masterbatch can contain additives that require separate confirmation for food-contact or drinking-water use. RoHS recast Directive 2011/65/EU Annex II restrictions on lead, cadmium, mercury, hexavalent chromium, PBB, and PBDE apply to electrical and electronic equipment; typical black 9995 coloration does not intentionally employ these restricted substances, but the moulder should request supplier declarations for the specific purchase lot.
Observed failure modes in production include splay and gas streaks from wet pellets, streaking from excessive screw speed, and short shots from worn non-return valves. These are controlled by moisture below 0.10%, screw speed below the point of surface defect formation, and a maintained cushion. Published data for this specific configuration are limited; process limits should be verified on the production machine rather than transferred from unplasticized PA12 settings.