| HS Code | 420666 |
| Density | 1.01 g/cm³ |
| Melting Point | 178 °C |
| Glass Transition Temperature | -30 °C |
| Tensile Modulus | 1000 MPa |
| Tensile Strength | 55 MPa |
| Elongation At Break | 200 % |
| Flexural Modulus | 1000 MPa |
| Charpy Notched Impact Strength 23 C | No Break |
| Heat Deflection Temperature 1 80 Mpa | 55 °C |
| Vicat Softening Temperature | 160 °C |
| Water Absorption At Saturation | 1.5 % |
| Moisture Absorption At 50 Rh | 0.7 % |
As an accredited EMS-Grivory Grilamid XE 3817 black 9992 Nylon 12, Conditioned factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg sealed, moisture-proof bags. Conditioned black 9992 nylon 12 granules, ready for processing. |
| Container Loading (20′ FCL) | A 20' FCL of conditioned Grilamid XE 3817 Nylon 12 granules in sealed bags on pallets, ventilated to prevent moisture. |
| Shipping | Ship via sealed, moisture-resistant packaging to preserve conditioned Nylon 12. Protect from direct sunlight, extreme heat, and mechanical damage. Use sturdy containers with proper labeling for safe handling. Ensure ventilation and secure loading to prevent shifting. Follow applicable regulations for plastic granules; keep dry during transit and storage. |
| Storage | Store Grilamid XE 3817 black 9992 in its original sealed container in a cool, dry area, away from direct sunlight, heat, and moisture. Keep the environment well-ventilated and avoid exposure to humidity, which can affect conditioned properties. Protect from physical damage and contamination. Use within recommended shelf life, resealing promptly after each use. |
| Shelf Life | Grilamid XE 3817 has a shelf life of 5 years when stored sealed, dry, and cool. |
The conditioning state of EMS-Grivory Grilamid XE 3817 black 9992 at 23 °C and 50% RH alters room-temperature flexural modulus and low-temperature impact response in coiled air brake tube. Trailers and heavy-duty commercial vehicles require nylon tubing under SAE J844 and DIN 74324-1 to survive pressure cycling, longitudinal dimensional change after heat-ageing, and flex fatigue at -40 °C. At equilibrium moisture uptake of 0.6 wt% to 0.8 wt%, PA12 shows a measurable decrease in tensile modulus and an increase in notched impact strength, shifting cold spiral-coil failure mode from brittle fracture toward ductile yield. The extruder feedstock is not processed in the conditioned state; pellets are dried in a desiccant dryer at 80 °C for 4–6 h to residual moisture below 0.1%, because dissolved water above 0.15% generates surface roughening and microbubble formation in the sizing calibrator.
Production-scale single-screw extrusion with L/D 24:1 to 30:1 and a barrier compression section at 2.5:1 to 3.0:1 is typical for high-viscosity PA12 tube. Feed-zone temperature is held at 210 °C to 220 °C, the compression zone at 230 °C to 235 °C, the metering zone at 235 °C to 240 °C, and the die head at 235 °C ± 5 °C. Vacuum sizing operates at 0.02–0.06 MPa gauge and water temperature 20–30 °C, while haul-off speed is slaved to an ultrasonic wall-thickness gauge to maintain ±0.10 mm on 6.35 mm OD 1.0 mm wall tube. Final product forms include coiled 6.35 mm and 9.52 mm OD air brake lines cut to length and fitted with ISO 14743 push-in connectors. The principal batch-to-batch failures observed at the coiler are wall collapse during warm coiling when melt temperature drifts above 245 °C and flattened ovality when vacuum falls below 0.02 MPa.
In coextruded diesel fuel vapor return and tank vent tubing, EMS-Grivory Grilamid XE 3817 black 9992 acts as the inner contact skin and outer jacketing layer around a barrier core. This architecture is governed by SAE J2260, which evaluates layer adhesion, permeation resistance, cold impact, and thermal ageing of complete fuel line assemblies. A representative layer distribution for PA12/EVOH multilayer tube is outer PA12 0.25 mm, maleic anhydride-grafted tie resin 0.05 mm, EVOH 0.10 mm, tie resin 0.05 mm, and inner PA12 0.15 mm. Published data for Grilamid XE 3817 in this exact stack is limited, but the grade operates within the same extrusion-viscosity envelope as other high-viscosity PA12 coextrusion grades. The conditioned outer layer reduces rigid shrinkage stress after cooling, which lowers delamination risk at the tie-resin interface following post-extrusion moisture uptake.
The multilayer process uses separate extruders for each polymer. The PA12 stream is maintained at 230 °C to 245 °C melt temperature, tie resin at 200 °C to 215 °C, and EVOH at 210 °C to 230 °C depending on ethylene content. Coextrusion die manifold temperature is set at 235 °C, and vacuum sizing follows with 0.04–0.07 MPa vacuum to maintain roundness. Final product lengths include 6.0 mm OD 1.0 mm wall and 8.0 mm OD 1.0 mm wall fuel vapor lines terminated with quick-connect couplings. Mismatch in melt viscosity across the manifold is the variable most often correlated to layer-displacement scrap, appearing as longitudinal adhesive striping at the EVOH/tie boundary under 100× optical inspection.
The question is relevant because corrugated tube tooling applies cyclic vacuum and mechanical forming force that is sensitive to melt strength rather than only melt viscosity. Under IEC 61386-23, corrugated conduit for protected automotive cable routing is tested for impact resistance at -25 °C, compression strength, and low-temperature flexibility after heat-ageing. The conditioned PA12 part exhibits lower flexural modulus than the dry-extruded component; dynamic mechanical analysis at 1 Hz under ISO 6721-4 commonly shows a 30–50% reduction in storage modulus when moisture content reaches 0.6 wt%. This property shift does not directly enter the corrugator, because feedstock must be dried below 0.1% moisture, but it affects downstream installation. After field conditioning at 23 °C/50% RH, the conduit is more resistant to brittle fracture during harness routing at subzero cabin conditions.
Corrugated production uses a downstream mould-block corrugator after a L/D 25:1 extruder. Melt temperature is kept between 230 °C and 245 °C, and corrugator moulds are held at 60–80 °C to control surface replication without blocking. Vacuum at each corrugator block segment is pulsed, with pressure differential of 0.01–0.03 MPa sufficient to draw the PA12 tube wall into the mould cavities before cooling. Finished corrugated conduit with internal diameters of 10 mm to 20 mm and wall thicknesses of 0.5–0.8 mm is used in engine-compartment harness protection. The dominant reject mode is mould-block gap flash when melt temperature exceeds 250 °C, and surface pockmarks when residual moisture exceeds 0.15% at die entry.
During dynamic submarine umbilical service, a polyamide 12 outer sheath must tolerate continuous seawater immersion, bending cycles, and potential contact with hydraulic control fluids. ISO 13628-5 sets requirements for thermoplastic sheathing used in subsea production control umbilicals. PA12 is selected where low water absorption and hydrolysis resistance reduce void formation and stress-cracking compared with PA6. In outer sheath extrusion, Grilamid XE 3817 is dried to 0.08% moisture or less and processed at melt temperature 220 °C to 235 °C. The low processing temperature limits thermal degradation in long-run extrusion through a pressure die. Single-screw extrusion with L/D 30:1, a mixing head, and a melt pump provides steady volumetric output for consistent wall thickness over continuous steel tube bundles.
The final sheath wall thickness typically ranges from 2.0 mm to 4.0 mm. The conditioned state at seafloor ambient 4 °C to 6 °C water reduces modulus sufficiently to permit low-temperature bending during installation over chute radii. The critical manufacturing defect is sag-induced eccentricity when melt temperature exceeds 240 °C in vertical down-extrusion. Die-head land length is therefore optimized for high-viscosity PA12, and haul-off speed is locked to melt-pump output. The product is not used in direct contact with high-pressure methanol injection streams without permeation testing, because PA12 is not a universal barrier under all umbilical chemical service conditions.
Burst performance of a PA12 control line is calculated from hoop stress with a service safety factor, not from a single fixed wall property. For DIN 73378 polyamide tubing in mobile hydraulic and pneumatic systems, an 8.0 mm OD tube with 1.0 mm wall has a standard dimension ratio of 8:1. Permissible working pressure is then set by burst pressure at maximum operating temperature. The conditioned PA12 tube at 23 °C has lower tensile yield stress than the dry part, and burst pressure follows the same downward shift. Designers apply conditioned tensile values from ISO 527-2 for ambient burst calculations and dry aged values for high-temperature derating. For field-conditioned PA12, burst margin at 23 °C is commonly kept above 4:1 relative to peak surge pressure, but this margin is not a grade property and must be validated per line batch.
Tubing is produced by high-viscosity single-screw extrusion at L/D 27:1 with melt temperature 230 °C to 245 °C and vacuum sizer operating at 0.03–0.05 MPa. Dimensional ovality is held below 0.15 mm on 8.0 mm OD by controlling vacuum and water bath temperature at 25 °C to 35 °C. A closed-loop laser diameter system monitors OD and wall. The finished product is used for low-pressure hydraulic pilot circuits and air-over-oil control lines in agricultural machinery, where operating temperature remains below 80 °C. Above that temperature, creep rupture behaviour of unconditioned PA12 under constant internal pressure, evaluated according to ISO 1167, becomes the limiting design criterion.
| Application segment | Standard designation | Test condition relevant to conditioned state | Typical production control limit |
|---|---|---|---|
| Air brake tubing | SAE J844, DIN 74324-1 | Low-temperature impact at -40 °C | Residual moisture < 0.1% before extrusion |
| Fuel vapor return | SAE J2260 | Layer adhesion after thermal ageing | PA12 melt 230–245 °C |
| Corrugated conduit | IEC 61386-23 | Impact at -25 °C | Melt temperature < 250 °C |
| Subsea umbilical sheathing | ISO 13628-5 | Seawater ageing and bending | Melt temperature 220–235 °C |
| Hydraulic control line | DIN 73378, ISO 1167 | Burst at 23 °C; creep at 80 °C | Ovality < 0.15 mm |
| Pneumatic control line | ISO 14743 | Pull-out force after pressure cycling | OD tolerance ±0.10 mm |
Factory automation networks and robotic end-of-arm pneumatic systems consume large volumes of black PA12 tubing in 4.0 mm, 6.0 mm, and 8.0 mm external diameters. ISO 14743 covers requirements for push-in connectors and thermoplastic tube assemblies in pneumatic systems, including pull-out force, leakage, and pressure cycling. In this application, the conditioned state is the normal in-service condition. Compressed air at dew points below 3 °C does not saturate the tube, but ambient humidity brings the outer surface to approximately 0.6 wt% moisture uptake, which stabilizes flexibility and reduces stress-cracking around barbed fittings. The compound is extruded as round single-layer tube. Drying follows the same 80 °C for 4 h procedure, and extrusion melt temperature is held at 235 °C to 245 °C with L/D 28:1 and a compression ratio of 2.5:1.
Final cut-length tube is coupled to nickel-plated brass or stainless steel push-in fittings. Retention force depends on surface hardness and moisture-conditioned modulus. Production-scale batch testing includes pull-out force per ISO 14743, and occasional failure occurs when tube OD falls below the lower tolerance limit of -0.10 mm due to sizer wear, causing incomplete gripping and line blow-out during pressure cycling. The carbon-black filled black 9992 coloration provides ultraviolet resistance for outdoor pneumatic control lines, but the grade is not specified for food-contact compressed air lines unless the complete system is validated against the relevant food-contact compliance code.
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EMS-Grivory Grilamid XE 3817 black 9992 is a semi-crystalline polyamide 12 (PA12) grade supplied with heat stabilisation and impact modification. The black 9992 colour code is produced with a carbon black masterbatch that provides ultraviolet absorption and uniform pigmentation; the material is not reinforced with glass fibre or mineral filler. In the conditioned state, moisture content has been brought to equilibrium with 23 °C and 50 % relative humidity according to ISO 291, or accelerated to an equivalent level by ISO 1110. Conditioning is not an indication of hygroscopic saturation; it is a controlled water absorption step intended to produce reproducible toughness data. The material density is approximately 1.02 g/cm³ by ISO 1183, and saturation water uptake in water at 23 °C is approximately 1.4 % by ISO 62. Because the polymer backbone is polyamide 12, water absorption is lower than that of PA6 and PA66, and dimensional changes in humid service are correspondingly reduced.
PA12 occupies a specific position among engineering polyamides because the amide group concentration is lower than in PA6 or PA66. The lower amide concentration reduces hydrogen bonding sites for water and produces a material with lower density, lower equilibrium moisture content, and lower notch sensitivity at low temperature. The impact modifier in XE 3817 forms a dispersed elastomeric phase that increases energy absorption during crack initiation, but also lowers tensile modulus and hardness relative to an unmodified PA12. These are not processing defects; they are intended changes in the molecular and morphological balance. The grade is used in injection-moulded clips, cable ties, snap-fit fasteners, and extruded corrugated or smooth tubing. A conditioned PA12 grade such as XE 3817 provides lower moisture uptake than PA6 and retains measurable notched impact resistance at -30 °C.
Conditioning alters the mechanical response in two directions: absorbed water reduces stiffness and yield stress, and it increases notched impact strength. In dry-as-moulded condition, tensile modulus is typically in the upper part of the range 800–1000 MPa; after conditioning, the value drops to approximately 600–800 MPa when tested by ISO 527-1/-2. The yield stress moves from roughly 30–35 MPa to 22–28 MPa, while nominal strain at break remains above 50 %. This shift must be accounted for in snap-fit design; a clip designed only on dry modulus can lose insertion force or become under-constrained after moisture uptake. Notched Charpy impact strength by ISO 179-1/1eA at 23 °C is commonly reported in the range 25–45 kJ/m² after conditioning, and the material retains a notched impact value above 6 kJ/m² at -30 °C. The heat deflection temperature under 1.8 MPa load by ISO 75-1/-2 remains in the region of 45–55 °C, which places the grade below glass-filled PA12 and PA66 for elevated-temperature load-bearing service.
| Property | Test standard | Typical conditioned range |
|---|---|---|
| Density, 23 °C | ISO 1183 | 1.01–1.03 g/cm³ |
| Water absorption, water 23 °C saturation | ISO 62 | 1.3–1.6 % |
| Tensile modulus | ISO 527-1/-2 | 600–800 MPa |
| Yield stress | ISO 527-1/-2 | 22–28 MPa |
| Nominal strain at break | ISO 527-1/-2 | >50 % |
| Charpy notched impact, 23 °C | ISO 179-1/1eA | 25–45 kJ/m² |
| Charpy notched impact, -30 °C | ISO 179-1/1eA | 6–12 kJ/m² |
| Melting point, DSC | ISO 11357-1/-3 | 174–178 °C |
| Vicat softening temperature, VST/B50 | ISO 306 | 125–140 °C |
| Heat deflection temperature, 1.8 MPa | ISO 75-1/-2 | 45–55 °C |
| Melt volume-flow rate, 275 °C/5 kg | ISO 1133-1 | 15–25 cm³/10 min |
| Mould shrinkage, flow direction | ISO 294-4 | 0.7–1.1 % |
For the black 9992 variant, carbon black content can slightly reduce surface resistivity and alter thermal conductivity. If static dissipation is required, surface resistivity must be confirmed by IEC 60093 or ASTM D257 rather than assumed from pigmentation. The mould shrinkage range of 0.7–1.1 % in flow direction by ISO 294-4 is close to unfilled PA12, and differential shrinkage between flow and transverse directions can produce ovality in thin-walled circular parts if the gate is not centrally located. Parts with press-fit inserts should be assembled only after conditioning because the lower modulus reduces hoop stress and the risk of stress cracking. In dry-as-moulded condition, the same interference fit may produce cracks at the insert edge when the part is later exposed to road salt.
Melt temperature control is the principal processing constraint. The grade is processed by injection moulding and extrusion with a melt temperature between 210 °C and 250 °C; operation above 250 °C for more than 10 min residence time can initiate thermal chain scission and black speck formation in carbon black-loaded PA12. A desiccant dryer should reduce moisture to ≤0.10 % before melting. Drying at 80 °C for 4–6 h with a dew point below -30 °C is typical; drying above 110 °C is not recommended because oxidation can shift colour and reduce impact resistance. In injection moulding, mould temperature should be held at 30–60 °C. The lower end produces faster cooling and higher skin orientation, which raises flow-direction modulus but increases frozen-in stress; the upper end improves crystallinity and dimensional stability at the expense of cycle time. A uniform mould temperature across the cavity is required because a thermal gradient greater than 10 K between opposing surfaces can cause bowing in clips longer than 80 mm.
On a hydraulic injection machine with clamp force between 600 kN and 1500 kN, a screw with L/D ratio from 20:1 to 25:1 and compression ratio 2.0:1–2.5:1 is used. Back pressure is typically 30–60 bar, and screw speed is set to avoid shear heating above 250 °C; melt temperature should be monitored at the nozzle because the shear heating contribution from a worn check ring can be 5–10 K higher than the barrel set point. If the non-return valve leaks, cushion instability and part mass variation exceed 0.5 %, and dimensional acceptance in snap-fit engagement features is lost. A recommended barrel profile for a 25 mm diameter screw is feed zone 200–210 °C, compression zone 220–230 °C, metering zone 230–240 °C, and nozzle 230–245 °C. Hot-runner manifolds should be kept below 250 °C and purged at start-up because PA12 can discolour at dead spots.
Extrusion of tubing requires a reverse temperature profile from the feed zone to the die, with maximum die head temperature 230–250 °C, and a polished calibrating die with vacuum sizing. A melt pump is recommended for wall thickness tolerance below ±0.05 mm. Moisture above 0.10 % causes splay, microvoids, and reduced burst pressure in pneumatic tubing; if ambient relative humidity exceeds 60 %, the dryer hopper should not be left open. Venting is critical because PA12 carbon black grades can generate volatile residuals; vent depths of 0.02–0.05 mm are common in injection moulds. If the vent is too deep, black flash occurs; if too shallow, burn marks form at the fill end. Reground XE 3817 black 9992 can be used, but the addition rate should not exceed 20 % if impact and surface finish requirements are tight; carbon black agglomerates from repeated processing can produce visible surface pitting and lower notched impact at -30 °C.
At a wall thickness below 1.5 mm, rapid cooling in a cold-runner mould suppresses PA6 and PA66 crystallinity and can produce brittle fracture at sub-zero temperatures. PA12 retains ductility at lower temperature because its glass transition is lower and its methylene-rich chain reduces moisture sensitivity. XE 3817 in the conditioned state typically retains a notched Charpy impact value of 6–12 kJ/m² at -30 °C, whereas an unmodified PA6 conditioned at the same temperature may fall below 4 kJ/m² depending on molecular weight and mould temperature. In addition, PA12 withstands zinc chloride solutions and many automotive road salts, whereas PA6 and PA66 are susceptible to stress cracking in zinc chloride at concentrations as low as 30 %. This difference is used in wire clips and fuel-line retainers exposed to underbody conditions.
| Property | Grilamid XE 3817 conditioned | PA6 conditioned | PA66 conditioned |
|---|---|---|---|
| Equilibrium moisture at 23 °C, 50 % RH | 0.5–0.8 % | 2.5–3.0 % | 2.0–2.5 % |
| Saturation water absorption, 23 °C water | 1.3–1.6 % | 9–10 % | 8–9 % |
| Tensile modulus conditioned | 600–800 MPa | 1200–1600 MPa | 1600–2000 MPa |
| Charpy notched impact, -30 °C | 6–12 kJ/m² | 3–5 kJ/m² | 3–5 kJ/m² |
Compared with an unmodified PA12 such as Grilamid L 25, XE 3817 has a lower tensile modulus and higher notched impact strength. The trade-off is a reduction in hardness and abrasion resistance; a sliding wear application requiring high surface hardness should use a glass-filled or higher-viscosity PA12 grade. Compared with a 30 % glass-fibre-reinforced PA12, XE 3817 is not a structural replacement: typical reinforced grades exhibit tensile modulus above 7000 MPa, while XE 3817 conditioned remains below 800 MPa. The selection logic is therefore reversed: XE 3817 is chosen when the part must flex, snap, or absorb impact rather than carry high sustained loads.
Differences from PA66 also appear in thermal properties. PA66 has a melting point near 260 °C, requiring higher processing temperatures and creating greater energy input; XE 3817 melts at 174–178 °C, allowing lower mould temperatures and reduced cycle time. However, the PA12 base has a lower heat deflection temperature than a 30 % glass-filled PA66, which can exceed 240 °C. Therefore XE 3817 is not used under continuous load above 60 °C where creep or creep rupture may control design. In hot water or humid environments, PA12 typically retains a higher fraction of tensile strength than PA66 after extended exposure, but the lower stiffness of XE 3817 means that creep deformation can occur at lower stress than in reinforced polyamides.
Operational boundaries include the following: continuous service above 60 °C under mechanical load should be verified by creep testing because heat deflection temperature is below 55 °C; exposure to strong acids, phenol, cresol, or formic acid should be avoided; the black pigmentation may restrict food-contact use unless specific migration testing is performed under EU 10/2011 or FDA 21 CFR; the grade is not flame retardant and is typically classified as UL 94 HB at test thickness. For automotive fuel vapour applications, no single PA12 grade provides universal resistance to all oxygenated fuels; compatibility testing should follow SAE J2260 or ISO 7628 for tubing systems. Published data for this specific colour and lot combination in long-term hydrolytic ageing is limited, so end-users should request test reports from the compounder before specifying the material in safety-critical fluid handling.