| HS Code | 405386 |
| Density | 1.01 g/cm³ |
| Tensile Modulus | 1600 MPa |
| Tensile Strength | 50 MPa |
| Elongation At Break | 50% |
| Flexural Modulus | 1400 MPa |
| Charpy Impact Strength Notched | 10 kJ/m² |
| Heat Deflection Temperature Hdt 1 80 Mpa | 50 °C |
| Melting Point | 178 °C |
| Water Absorption 24h | 1.0% |
| Mold Shrinkage | 0.7% |
As an accredited EMS-Grivory Grilamid XE 3997 nat Nylon 12, Conditioned factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | EMS-Grivory Grilamid XE 3997 nat Nylon 12, Conditioned is supplied in sealed foil bags, 25 kg net each. |
| Container Loading (20′ FCL) | 20′ FCL loading of EMS-Grivory Grilamid XE 3997 nat Nylon 12, conditioned: sealed bags on pallets, secured and ventilated. |
| Shipping | EMS-Grivory Grilamid XE 3997 nat Nylon 12 (conditioned) is not regulated as dangerous goods for transport. Ship in sealed, clean, moisture-resistant packaging to prevent contamination and absorption. Avoid excessive heat, humidity, and dust formation. Handle with standard industrial hygiene practices. No special transport labeling or UN classification required. |
| Storage | Store Grilamid XE 3997 nat Nylon 12 (Conditioned) in its original, tightly sealed container in a cool, dry area away from direct sunlight, heat sources, and humidity. Keep at room temperature with moderate relative humidity to preserve the conditioned moisture level. Protect from dust and contamination, avoid stacking heavy loads, and use within two years. |
| Shelf Life | Store sealed in original packaging, away from moisture and heat, to preserve conditioned properties. Typical shelf life is two years. |
On multi-layer fuel-line lines running SAE J2260 constructions, EMS-Grivory Grilamid XE 3997 nat Nylon 12, Conditioned is introduced as the inner and outer polyamide layer adjacent to the EVOH barrier core. The material is supplied in natural pellet form conditioned to ISO 291 23 °C/50 % RH equilibrium moisture, which places the lot close to service moisture content and reduces post-extrusion tensile modulus drift. Industry compliance for tubular components in this sector is anchored to SAE J2260 for nonmetallic fuel system tubing, ISO 13775-1:2017 for thermoplastic automotive fuel tubing, ASTM D638-22 for tensile properties, ISO 527-1:2019 for tensile testing principles, ISO 1183-1:2019 for density, and ISO 1133-1:2022 for melt volume-flow rate during incoming lot verification. The addition ratio on a production scale is 100 parts by weight of XE 3997 nat, with 0.2–0.5 parts of an external lubricant masterbatch to reduce die build-up, and 0–2 parts of a colour masterbatch only where a non-natural outer layer is specified; the EVOH barrier layer is not part of this addition ratio and is metered separately in the multilayer head. In the downstream production process, the converter dries the pellets in a desiccant dryer to a residual moisture level below 0.10 % as verified by ISO 15512:2019, then processes the resin through a three-layer coextrusion head fed by PA12 extruders with L/D ratios of 24:1 to 30:1 and an EVOH extruder with L/D 24:1; melt temperature for the PA12 layers is held between 225 °C and 245 °C, vacuum calibration is maintained at −0.4 bar to −0.8 bar, and internal air pressure support is applied to prevent the PA12/EVOH interlayer from sagging. Terminal finished product types include fuel vapour return lines, onboard refuelling vapour recovery tubes, diesel fuel return lines, and quick-connector tubing for fuel-tank vent systems. Pre-drying interlocks are recommended when plant storage exceeds 60 % RH; the grade should not be combined with unapproved amine-based processing aids in colour masterbatches because this can shift melt viscoelastic response and produce unstable layer interfaces.
The governing failure mode in SAE J844 air brake tubing is dimensional drift caused by incomplete post-crystallization shrinkage control when the tube exits the vacuum calibrator above 60 °C surface temperature. For this sector, XE 3997 nat is processed on single-screw extruders with L/D 30:1 and a barrier screw; the compression ratio is set at 2.5:1 and the screen pack is 60/80/40 mesh. The addition ratio is neat resin with up to 20 wt% in-house regrind, provided the regrind is dried to the same moisture specification and re-stabilized with 0.3–0.6 wt% processing stabilizer masterbatch; exceeding 20 wt% regrind is not recommended because burst-pressure retention under SAE J844 after heat aging at 100 °C becomes lot-dependent. Industry compliance standards are SAE J844, ISO 7628:2009 for thermoplastic tubing for air brake systems, FMVSS 571.106 for hydraulic and air brake hose, plus ASTM D638-22, ISO 527-1:2019, ISO 1183-1:2019, and ISO 188 for hot-air aging. The downstream production process uses melt temperature 240–260 °C, die land length to gap ratio 10:1, a vacuum calibration sleeve with closed-loop diameter control, and a two-stage cooling bath where the first stage is maintained at 40–50 °C to minimise thermal shock. Terminal finished product types are air brake tubing for heavy trucks, bus pneumatic door lines, rail brake control tubes, and trailer air-actuated suspension lines. Processing limitation: startup purging with low-viscosity LDPE should be avoided below 220 °C, because the viscosity mismatch can starve the screw feed section and produce melt-temperature oscillations visible as surface roughness.
| Sector | Regulatory/industry standard | Material test standard | Reported acceptance basis |
|---|---|---|---|
| Fuel vapour return tubing | SAE J2260 | ASTM D638-22, ISO 527-1:2019 | Conditioned tensile elongation at break |
| Air brake tubing | SAE J844, FMVSS 571.106 | ISO 188, ASTM D638-22 | Burst retention after 100 °C aging |
| Subsea pressure sheath | API Spec 17J, ISO 13628-2 | ASTM D638-22, ISO 9080 | Long-term hydrostatic strength |
| Industrial compressed-air liner | ISO 3949, SAE J517 | ISO 1817, ASTM D638-22 | Fluid resistance and pressure cycling |
| EV coolant loop | ASTM D3306, ASTM D6210 | ISO 1817, ISO 527-2 | Glycol aging and elongation retention |
| Optical cable tight buffer | IEC 60794-1-1, Telcordia GR-771 | ISO 1133-1:2022, ASTM D638-22 | Shrinkage and conditioned modulus |
For subsea pressure sheaths wound into unbonded flexible pipe per API Spec 17J / ISO 13628-2, XE 3997 nat is employed as an extruded polymeric barrier over the interlocked stainless-steel carcass. This application differs from automotive tubing because the polymer layer is thickened to 3–10 mm and must retain hydrostatic integrity after long-term exposure to seawater, sour gas, and production chemicals. Industry compliance is governed by API Spec 17J / ISO 13628-2 for unbonded flexible pipe, NORSOK M-710 for polymer qualification in aggressive fluid service, ASTM D638-22 and ISO 527-1:2019 for tensile properties, ISO 9080 for extrapolated stress-rupture data, and ISO 22088-2:2006 for determination of environmental stress cracking. The formulation addition ratio is 100 parts by weight of XE 3997 nat, 1–2 wt% of a hydrolysis-resistant stabiliser masterbatch, and 0.5–1.0 wt% of a drying-agent masterbatch used only in high-humidity coastal extrusion plants; the masterbatch carrier is PA12 to avoid splay. Downstream production process: the resin is pre-dried to 0.08 % maximum moisture per ISO 15512:2019 and fed to a single-screw extruder with L/D 30:1 and a grooved feed section, melt temperature is maintained at 230–250 °C, and the melt is crosshead-extruded over the carcass with a wall-thickness variation tolerance of ±0.5 mm; after sizing, the sheath is water-cooled at a controlled rate to limit internal voids. Terminal finished product types are pressure sheaths for unbonded flexible risers, hydraulic and chemical injection umbilical tubes, and flexible flowline liner stock. Published data for this specific grade in sour service is limited; qualification must include long-term ageing to ISO 9080 rather than short-term tensile retention.
The liner layer in ISO 3949 hydraulic hose assemblies is extruded from XE 3997 nat as a pin-mandrel tube before textile braiding. The addition ratio for industrial hose liner stock is 100 parts resin with 0.2–0.8 parts of an internal release agent masterbatch and, where UV or solvent-contact markings are specified, 2–3 wt% of carbon black masterbatch. Industry compliance standards include ISO 3949:2020 for plastic hoses and hose assemblies with textile reinforcement for hydraulic applications, SAE J517 for hydraulic hose, ISO 1817 for fluid resistance, ASTM D638-22 for tensile properties, and ISO 527-2 for molded or extruded specimen geometries. The downstream production process uses an extruder with L/D 25:1, a grooved feed throat, melt temperature 225–245 °C, and a pin-and-sleeve mandrel crosshead; downstream, a controlled stretch ratio of 0.5–1.5 % is applied before the tube enters the braider, and the liner is post-conditioned at 23 °C/50 % RH to stabilise moisture-dependent flexibility before crimping. Terminal finished product types include compressed-air hoses, hydraulic return-line hoses, and chemical transfer hoses for low-polarity fluids. A processing boundary is the use of flame-retardant masterbatches containing brominated diphenyl ethers; these are not permitted under RoHS Directive 2011/65/EU and may reduce weld-line strength at the pin mandrel split.
Thermoplastic coolant loops in battery-electric platforms require a polyamide with moisture-conditioned elongation above 150 % to survive clip-fit assembly at −20 °C and low electrical conductivity to avoid parasitic current paths. XE 3997 nat is processed as the inner and outer layers of a three-layer coolant tube, with a middle barrier polymer layer at 10–15 % of total wall thickness. Industry compliance is tested against ASTM D3306 for light-duty coolant formulations and ASTM D6210 for heavy-duty glycol coolants, while material testing follows ISO 1817 for fluid resistance, ISO 188 for hot-air aging, ASTM D638-22 for tensile properties, and ISO 527-1:2019 for specimen preparation. The addition ratio is 100 parts PA12, 1–2 wt% of heat stabiliser masterbatch for continuous service at 90–110 °C, and 0.5–1.0 wt% of colour masterbatch; the barrier layer is not included in the PA12 addition ratio because it is metered independently. Downstream production process: coextrusion through a spiral mandrel die, melt temperature 240–260 °C, downstream corrugating or 3D vacuum bending after the tube exits sizing; bend radii below 2.5× outside diameter require internal support air pressure to prevent kinking. Terminal finished product types are EV battery cooling hoses, power electronics coolant lines, and thermal-management connectors. Long-term coolant exposure beyond 110 °C is outside the recommended envelope unless the converter validates the specific coolant mixture under ISO 188.
In tight-buffer jacketing lines for IEC 60794-1-1 optical cables, XE 3997 nat is selected for its low post-extrusion shrinkage and conditioned tensile modulus, which reduces micro-bending attenuation in tight-buffered optical fibres. The addition ratio is neat resin with 0.3–0.6 wt% of an antioxidant masterbatch; no plasticizer is used to maintain kink resistance at low temperature. Industry compliance standards include IEC 60794-1-1 for optical fibre cable generic specification, Telcordia GR-771 for fibre optic component reliability, ASTM D638-22 for tensile properties, ISO 1133-1:2022 for melt viscosity lot release, and ISO 1183-1:2019 for density. The downstream production process uses a 24:1 L/D extruder with a melt pump, tube wall thickness 0.20–0.50 mm, line speed 150–600 m/min, vacuum sizing with closed-loop diameter gauge, and a post-extrusion annealing stage at 80–90 °C to control shrinkage below the cable specification. Terminal finished product types are optical fibre tight-buffer tubes, indoor/outdoor drop cable sheaths, and air-blown fibre microduct cores. The conditioned moisture state of the natural grade must be preserved during storage; if bags are left open above 60 % RH for more than 4 h, pre-drying is required to avoid splay and diameter variability.
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EMS-Grivory Grilamid XE 3997 nat is a natural-colour, short-glass-fibre-reinforced polyamide 12 injection-moulding compound. The material designation according to ISO 1043 can be expressed as PA12-GF30; the suffix “nat” indicates an unpigmented, natural base resin. In supplier literature, the term “Conditioned” refers to specimens brought to moisture equilibrium at 23 °C and 50 % RH under ISO 291 or by the accelerated procedure of ISO 1110, not to the moisture content of pellets at the point of supply. This distinction is necessary because the conditioned state changes the mechanical response in service: absorbed water acts as a plasticiser and lowers stiffness while improving ductility and room-temperature impact. The PA12 backbone provides lower equilibrium moisture uptake than PA6 or PA66, while the short-glass reinforcement increases modulus and reduces isotropic mould shrinkage relative to unfilled PA12. Components are specified in the conditioned state when they operate in humid air, enclosed housings, or under-hood environments and must retain dimensional stability, fuel and oil resistance, and low-temperature impact toughness. Because the grade is natural, colour concentrates can be added, but colourant effects on nucleation, crystallinity, and impact should be validated on production tooling before series release.
For a PA12-GF30 compound, dry-as-moulded specimens are typically tested at a moisture content below 0.10 wt%. Conditioning at 23 °C/50 % RH raises the absorbed moisture to approximately 0.5–0.7 wt%; saturated water absorption is approximately 1.4 wt%. The plasticising effect reduces tensile modulus and tensile strength at break, while elongation at break and Charpy notched impact at 23 °C increase. Low-temperature impact may remain close to the dry value or decrease slightly because the moisture-related toughening mechanism is less effective below the β-transition of the PA12 matrix. Table 1 summarises representative values from current supplier technical literature. These are single-point data under ISO 10350-1 specimen preparation and are not design minimums.
| Property | Standard | Dry | Conditioned |
|---|---|---|---|
| Density | ISO 1183-1 | 1.23 g/cm³ | 1.23 g/cm³ |
| Tensile modulus | ISO 527-1/-2 | 6,600 MPa | 4,800 MPa |
| Tensile strength at break | ISO 527-1/-2 | 120 MPa | 75 MPa |
| Elongation at break | ISO 527-1/-2 | 3.5 % | 8 % |
| Charpy notched impact at 23 °C | ISO 179-1/1eA | 12 kJ/m² | 15 kJ/m² |
| Charpy notched impact at −30 °C | ISO 179-1/1eA | 8 kJ/m² | 7 kJ/m² |
| Heat deflection temperature at 1.80 MPa | ISO 75-1/-2 | 160 °C | 150 °C |
| Melting peak | ISO 11357-3 | 176 °C | 176 °C |
Tensile modulus is measured at 1 mm/min; tensile strength and elongation are measured at 5 mm/min for ISO 527-1/-2. Charpy specimens are edgewise notched according to ISO 179-1/1eA. Heat deflection temperature is determined at 1.80 MPa with a 120 °C/h heating rate. The melting peak is taken from the second heating cycle of ISO 11357-3. For design calculations, the conditioned tensile modulus and conditioned secant modulus at the service strain are more relevant than dry values when ambient humidity is uncontrolled.
Because the “Conditioned” designation applies to test specimens, not to pellet moisture content, melt processing requires the same drying discipline as any unfilled or reinforced PA12. Pellet exposed to ambient humidity should be dried to <0.10 wt% residual moisture before melting. Desiccant-wheel dryers are preferred; the dew point should not exceed −40 °C. Typical drying conditions for cold or damp material are 80 °C for 4–6 h. Hot-air dryers are not recommended because they cannot reach the required dew point in humid production areas. On a production-scale three-zone reciprocating-screw injection moulding machine with an L/D ratio of 20:1 to 25:1 and a compression ratio of 2.5:1, the barrel profile is normally set from 230 °C in the feed zone to 250 °C in the compression zone and 260 °C in the metering zone. The melt temperature measured by an insertion pyrometer should be kept between 240 °C and 270 °C; the upper limit is 280 °C for short residence. Mould temperature should be maintained between 60 °C and 90 °C. Table 2 consolidates the processing envelope.
| Parameter | Setpoint/Range | Unit |
|---|---|---|
| Residual moisture before melt | <0.10 | wt% |
| Desiccant dew point | ≤ −40 | °C |
| Drying temperature | 80 | °C |
| Drying time | 4–6 | h |
| Melt temperature | 240–270 | °C |
| Mould temperature | 60–90 | °C |
| Back pressure | 30–70 | bar |
| Screw speed | 80–150 | rpm |
| Hold pressure | 400–800 | bar |
| Maximum residence time at melt temperature | 15 | min |
Residence time is a threshold risk. In actual moulding trials, residence times below 5 min can produce melt-temperature variation and poor glass-fibre dispersion, whereas residence beyond 12–15 min can generate brown streaks, a drop in notched impact, and surface splay. When stoppages exceed the maximum residence time, the barrel should be purged with fresh feed at the lower melt-temperature limit. Reground sprues and runners may be introduced at up to 30 wt% if they are clean, dry, and not thermally degraded. For components used in fuel contact, pressure-bearing fluid handling, or safety-relevant bracketry, use of 100 wt% virgin compound is typical unless a controlled regrind study is available. The conditioned data in Table 1 should not be used to justify processing with wet pellets; residual moisture above 0.10 wt% during melting produces hydrolysis and lowers molecular weight even if the part is later conditioned after moulding.
The PA12 matrix of Grilamid XE 3997 nat gives resistance to mineral oils, greases, aliphatic hydrocarbons, engine coolants, and zinc chloride solutions. Zinc chloride resistance is one reason PA12 is selected over PA6 or PA66 in automotive under-hood applications where road-salt and galvanic corrosion products generate zinc chloride. Glass-fibre reinforcement can reduce apparent chemical resistance at cut edges because fibre wicking creates a capillary path for fluid entry into the part. For sealed or welded housings this effect is mitigated. Stress-cracking resistance in chloride-containing environments should be evaluated with constant-strain fixtures according to ISO 22088 or the relevant OEM method, using moulded plates with the same fibre orientation and weld-line condition as the final part. Continuous exposure to hot water above 80 °C requires hydrolysis-resistance validation, since PA12 can undergo molecular-weight reduction in aqueous service over extended time. Published data for this specific formulation under long-term hot-water exposure are limited. The material should not be used with strong mineral acids, oxidising agents, or polar solvents that dissolve or swell PA12; methanol and ethanol can cause surface attack at elevated temperature. For natural-grade parts, outdoor UV exposure without a stabilised black or UV-stabilised colour package is not recommended for long-term aesthetic retention.
In the form supplied, EMS-Grivory typically declares conformity to Directive 2011/65/EU RoHS and Regulation (EC) No 1907/2006 REACH for this natural compound. Converter-created colour concentrates, processing aids, or post-moulding coatings require separate compliance confirmation.
In direct comparison with PA6-GF30, Grilamid XE 3997 nat absorbs roughly one-quarter of the equilibrium moisture at 23 °C/50 % RH, which produces less stiffness loss between dry and conditioned states and better dimensional stability in humid air. Compared with PA66-GF30, the PA12 grade has a lower density, improved zinc chloride stress-cracking resistance, and lower heat deflection temperature; PA66-GF30 remains stiffer and more heat-resistant in dry and conditioned states. Against unfilled PA12 grades such as Grilamid L 20, the 30 wt% short-glass reinforcement in XE 3997 nat raises the tensile modulus from the range of 1,000–1,500 MPa to more than 6,000 MPa dry and reduces linear mould shrinkage, but it also introduces anisotropic flow-direction properties and lower elongation at break. Against PA11-GF30, the PA12 grade offers broadly similar low moisture uptake and chemical resistance, with a slightly lower melting peak; field selection is usually determined by regulatory, supply-chain, or supplier-specific testing rather than by a single property. Compared with the black version of the same base compound, the natural grade may have different colourant package and therefore different UV ageing behaviour; carbon-black grades are preferred for outdoor parts unless secondary painting or UV-stabilised colour concentrates are used.
Rheological characterisation for this specific grade should be performed by capillary rheometry according to ISO 11443 if gate-pressure calculations are required. Published data for the complete shear-rate and temperature matrix are limited, so fill simulations should be calibrated with measured melt-pressure data from short-shot trials on the intended mould.
Typical uses include under-hood clips, quick-connector housings, pneumatic valve bodies, filter housings, cable-conduit fittings, and enclosures exposed to mineral oil or fuel vapour. In these service conditions, the conditioned mechanical data are used for deflection and snap-fit calculations because the part is not dry. Snap-fit design should use the conditioned secant modulus at the expected strain, and the maximum snap-fit strain should remain below the conditioned yield strain; using dry tensile modulus can produce brittle snap-fit failure. For glass-fibre-reinforced PA12, the mechanical response is anisotropic. Tensile modulus and strength along flow are higher than across flow, and weld lines can reduce impact strength by more than 50 % compared with a simple ISO bar. Gate location and venting should be determined by short-shot studies on production tooling; a fill simulation alone is not sufficient. Moulded parts should be tested at −30 °C or −40 °C with the actual gate and weld-line configuration, because laboratory ISO bars overstate the toughness of complex moulded geometries. For continuous hot-air exposure above 120 °C, the natural PA12-GF30 grade may embrittle over time unless a heat-stabilised variant is validated. Fibre attrition during melt processing reduces the number-average fibre length and lowers tensile modulus and impact; screw speed, back pressure, and shot-to-barrel-volume ratio should be set to minimise this attrition. The processing window in Table 2 is therefore a boundary condition for preserving the property set reported in Table 1.
Incoming material should be monitored for moisture content and melt volume-flow rate according to ISO 1133-1:2022 at a specified condition; lot-to-lot variation in natural PA12-GF30 can affect filling behaviour. The supplier certificate of analysis should be retained for traceability. Post-moulding conditioning may be accelerated by warm-air or water immersion, but through-thickness moisture distribution differs from standard ISO 291 equilibrium; parts should be allowed to equilibrate before dimensional inspection.