| HS Code | 890299 |
| Density | 1.01 g/cm³ |
| Tensile Modulus | 1700 MPa |
| Tensile Strength | 50 MPa |
| Yield Stress | 50 MPa |
| Elongation At Break | >50% |
| Charpy Impact Strength Notched | 5 kJ/m² |
| Charpy Impact Strength Unnotched | No break |
| Melting Point | 178 °C |
| Glass Transition Temperature | 45 °C |
| Water Absorption 24h | 0.25% |
| Water Absorption Saturation | 1.2% |
| Moisture Content | 0.10% |
As an accredited EMS-Grivory Grilamid L 25 W 20 Nylon 12, Dry factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied as dry nylon 12 granules in sealed moisture-proof packaging, typically 25 kg bags, ready for processing. |
| Container Loading (20′ FCL) | 20′ FCL: 25 kg bags of dry nylon 12 loaded on pallets, secured, moisture-protected, and container-ventilated. |
| Shipping | This nylon 12 resin ships as dry, solid pellets in sealed moisture-barrier bags, typically on pallets. It is non-hazardous and safe for standard freight. Protect from moisture, humidity, and prolonged heat during transit. Store in a cool, dry area, and handle with care to avoid bag rupture. |
| Storage | Store in its original, sealed container in a cool, dry, and well-ventilated area. Keep away from direct sunlight, heat sources, and high humidity to prevent moisture absorption and degradation. Ensure the container remains tightly closed when not in use. Under proper conditions, shelf life is typically 12 months from delivery. |
| Shelf Life | Shelf life is indefinite when stored dry, sealed in original containers, and protected from moisture, heat, and UV light. |
Because the grade is supplied dry, any open container residing more than 30 min in a plant with relative humidity above 60% must be returned to a desiccant dryer before feeding. Unsealed regrind from start-up purgings is dried separately and limited to a converter-validated percentage.
| Parameter | Setpoint | Verification method |
|---|---|---|
| Drying temperature | 80 °C | Desiccant dryer, dew point ≤ −40 °C |
| Drying time | 4–6 h | ISO 15512 moisture ≤ 0.10% |
| Barrel zone profile | 220–245 °C | Melt thermocouple |
| Adapter/die temperature | 230–245 °C | Melt thermocouple |
| Screw L/D | 30–36 | Barrier screw |
| Calibration vacuum | 0.4–0.7 bar | Pressure gauge |
At melt temperatures above 250 °C, visual surface degradation appears as yellowing and free plasticizer condensate at the calibrator entrance; the upper melt limit is therefore treated as a hard stop on multi-extruder lines. Start-up after purging with low-viscosity polyolefin is avoided because stagnant polyolefin residues contaminate the PA12 melt and produce delamination at the tie-layer interface. Line operators sample tube wall thickness at 30-minute intervals; wall-thickness drift greater than 0.03 mm triggers recalibration.
Truck and trailer air brake circuits built to ECE R13 or FMVSS 121 are filled with this grade in nominal 8 mm × 1 mm and 10 mm × 1.5 mm dimensions. Operating pressure at the compressor governor is 0.85–1.00 MPa; SAE J844 and ISO 7628 define minimum burst and leakage requirements. At −40 °C, unplasticized PA12 can retain pressure but may crack when the tube is flexed during fifth-wheel articulation. Plasticized L 25 W 20 moves the ductile-to-brittle response below the cold-soak floor. However, burst retention after heat ageing at 100 °C for 168 h depends on the plasticizer remaining homogeneously distributed. Separated plasticizer at the tube inner wall increases surface tack and can reduce fitting pull-out force. Fitting retention is measured by ISO 7628 or OEM-specific pneumatic impulse tests; validation includes pressure impulse cycling from 0 to 0.9 MPa at 2 Hz because plasticizer migration at the fitting contact surface can reduce pull-out force over time. The grade is not UV-stabilised in natural form; exterior chassis installations require a carbon-black or UV-stabilised outer layer or conduit. Pre-drying to 0.10% moisture before extrusion is mandatory because moisture above 0.12% lowers melt viscosity at the die and produces ovality above 0.10 mm, which compromises push-connect sealing.
Compressed-air control circuits in high-speed packaging machinery expose polyamide tubing to continuous flexure at the push-connect coupling. In these lines, 4 mm and 6 mm OD tube produced from Grilamid L 25 W 20 is cut to 500–2,000 mm lengths and fitted with nickel-plated brass or stainless-steel push-connect couplings. The material’s hardness after conditioning at 23 °C and 50% RH normally stabilises in the Shore D 55–65 range, which matches coupling grip-ring embedment without barb overtravel. Flexural fatigue performance is influenced by tube wall thickness uniformity; converters hold wall thickness to ±0.05 mm and use vacuum sizing with closed-loop water temperature of 40 °C. At 23 °C, a 6 mm × 1 mm tube operates at 1.0 MPa compressed-air supply with a 3:1 static safety factor. The limiting condition is cold-room cycling to 4 °C, where condensation introduces surface moisture and the moisture-affected surface can generate microcracks at the grip-ring edge. Lubrication of the coupling collet with silicone-free assembly fluid is allowed; hydrocarbon-based greases cause stress cracking at the flare. Leakage is tested after insertion in accordance with ISO 14743; production lots are dry-tested at 1.2 MPa for 5 s.
Wind turbine control cables installed in unheated tower sections require a jacket that survives continuous vibration and occasional 105 °C conductor fault temperatures. This PA12 grade is extruded as a 1.2–2.0 mm jacket over shielded twisted-pair bundles at line speeds of 20–50 m/min using a 60 mm single-screw extruder with a double-flighted screw and L/D 25–30. The melt is filtered through a 60/80 mesh pack to remove crosslinked particles larger than 100 µm. Cable manufacturers apply a proprietary adhesion promoter or use a foamed polyethylene separator to prevent the nylon jacket from bonding to the shield. After hot-air ageing at 100 °C for 3,000 h per IEC 60811-401, elongation at break of the jacket must remain above 150% and no visible crack may appear after a mandrel wrap at −25 °C. Plasticizer migration through the jacket thickness is monitored by Shore D ladder scans; a hardness increase greater than 8 points from the inner to outer surface indicates migration and is cause for lot rejection. The grade is not inherently flame-retardant; for installations requiring IEC 60332-1 flame spread, converters compound an FR masterbatch or specify an FR cable design. Because this specific grade is supplied as a dry natural resin, UV stabilisation and carbon black dosing are done at the cable extrusion line if outdoor or UV-exposed routing is required.
Subsea control umbilicals rated to API 17E and ISO 13628-5 use polyamide sheaths over steel tube bundles for dynamic service from topside hang-off to subsea termination. In this application, Grilamid L 25 W 20 is extruded after the steel tube stranding and fillers are bound; typical sheath wall thickness is 2.0–3.5 mm depending on bundle diameter. The melt is applied at 230–245 °C with a crosshead die and pressure tooling to avoid air pockets at the interstices. Because the cable is double-armoured in most dynamic sections, the PA12 sheath acts as a bedding and separation layer rather than as the primary water barrier. The grade’s low water absorption relative to PA6 reduces swelling-induced dimensional change in seawater, but the plasticizer package introduces a known operational boundary: continuous exposure to seawater above 50 °C in unarmoured sections can accelerate plasticizer extraction, causing the sheath to harden beyond design assumptions. Published data for this specific plasticized grade under 20-year subsea ageing is limited; therefore end users must run material-specific testing under API 17E qualification programmes before serial production. Buried static sections at 4 °C bottom water do not show this ageing acceleration. Pre-drying is critical; moisture content above 0.10% at the crosshead causes foaming at the die exit and reduces adhesion to the underlying bitumen-filled interstices.
Medical device shaft extrusion remains outside the standard certification boundary for this industrial grade. Catheter and endoscopic shaft developers sometimes evaluate plasticized PA12 for multi-lumen tubing because it offers lower flexural modulus than unplasticized PA12 and can be joined to polyether block amide or TPU segments by adhesive bonding. However, Grilamid L 25 W 20 is not supplied as an ISO 10993-1 biologically evaluated resin. Each final device must undergo cytotoxicity, sensitisation, and irritation testing according to ISO 10993-5, ISO 10993-10, and ISO 10993-23 on the sterilised finished construction. Extraction testing must include the specific plasticizer package and any processing aids introduced during melt extrusion. Steam autoclave at 121 °C or high-energy gamma sterilisation above 25 kGy may shift Shore D hardness and increase extractables; converters running 25 W 20 must validate post-sterilisation mechanical performance. The material is not supplied with a USP Class VI certificate as standard. For short-term patient-contact tools that do not require long-term implant classification, a 30-day extraction study is used as a screening method, but no claim of medical compliance can be transferred from the resin to a finished device. This boundary is stated because plasticizer migration in lipid-rich media is often higher than in saline; device developers cannot assume hydrolytic stability alone.
Flexible chemical transfer hoses use plasticized PA12 liners when the conveyed fluid is incompatible with polyurethane and requires a lower moisture-absorbing polyamide than PA6 or PA66. The grade is extruded as a 0.5–1.5 mm smooth-bore liner, often over a textile braid reinforced with a PVC or EPDM outer cover. For aqueous food-contact media, the final hose assembly must be verified by the converter under FDA 21 CFR 177.1500 for nylon resins and any applicable EU 10/2011 migration limits for the finished formulation. Plasticizer migration into food simulants, particularly 95% ethanol and olive oil, is typically higher than with unplasticized PA12. For industrial solvents, compatibility is evaluated by immersion in the specific fluid at 40 °C for 30 days, with measurements of Shore D change, tensile retention, and weight loss. The material’s low water absorption helps maintain coupling integrity in humid chemical plants, but strong mineral acids below pH 2 and phenols at elevated temperature degrade PA12 and are outside the service envelope. Continuous use with methanol or aggressive polar solvents may plasticize the surface and reduce burst pressure; written compatibility testing is required for each concentration and temperature combination. The dry feedstock must be processed at 0.10% maximum moisture, and liner thickness below 0.5 mm requires static mixing in the melt stream to avoid melt-temperature variation across the die.
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EMS-Grivory Grilamid L 25 W 20 Nylon 12, Dry is a plasticizer-modified polyamide 12 homopolymer supplied as moisture-controlled granules. The L prefix identifies the PA12 base chemistry in the EMS-Grivory material nomenclature; the W 20 suffix corresponds to a softened/plasticized modification, and the Dry designation indicates a controlled as-supplied moisture level rather than an unconditioned melt state. The PA12 backbone is synthesised from laurolactam or ω-aminolauric acid and carries an aliphatic segment of approximately 11 methylene groups between amide linkages. That structural feature lowers amide-group density relative to PA6 and PA66, reducing equilibrium moisture uptake to a typical range of 1.4 % to 1.6 % by mass for the unmodified base polymer under ISO 62 immersion. The plasticizer package modifies absolute mechanical values, so grade-specific data from the EMS technical datasheet must control final design calculations.
The dry supply condition is specified because PA12 is hygroscopic enough to require moisture control before melt processing. In sealed packaging, the residual moisture content is usually maintained below 0.10 % by mass. Once the package is opened at relative humidity above 60 % RH, the granules begin to reload moisture. Before extrusion or injection moulding, moisture should be reduced to 0.10 % or less; a desiccant dryer with a dew point of −30 °C or lower and an air temperature of 80 °C to 100 °C is used for 4 h to 8 h. Hot-air drying may be acceptable only in low-humidity plants when the granule bed depth does not exceed 50 mm and the hopper is covered.
Application context from EMS-Grivory technical literature includes flexible tubing, cable sheathing, pneumatic lines, and injection-moulded fasteners. The grade is typically selected for applications requiring low moisture uptake, lower density, and retention of ductility after conditioning; chemical exposure must be validated according to application-specific standards such as ISO 175 or automotive fuel-resistance test methods. The material is not a direct replacement for short-chain polyamides in load-bearing structural components unless the lower tensile modulus and plasticizer-modified strength values are explicitly included in the part calculation.
Water absorption in polyamides is governed mainly by hydrogen bonding at amide sites. Because PA12 contains fewer amide groups per unit chain length than PA6 or PA66, its saturated moisture content under ISO 62 is approximately 1.4 % to 1.6 %, whereas PA6 typically absorbs 9 % to 10 % and PA66 approximately 8 % to 9 % by mass. The lower moisture loading produces a smaller shift in tensile modulus from the dry-as-moulded condition to the conditioned state. For PA6 and PA66, tensile modulus according to ISO 527-1:2019 can fall from roughly 3,000 MPa dry to below 1,500 MPa after conditioning at 50 % RH; the PA12 class moves through a narrower band. For a plasticized grade such as L 25 W 20, the absolute modulus is lower, but the moisture-induced shift remains smaller than for short-chain polyamides.
The practical result is more predictable dimensional integration in humid service. Tubing, clips, and cable jackets made from PA12-based material exhibit lower longitudinal growth and less stiffness loss after water exposure. That does not eliminate the need for conditioning-sensitive tolerance studies on the final extruded profile; radial wall-thickness changes and residual stress relaxation still require validation under the end-use humidity and temperature cycle.
A direct comparison of polymer-class reference values shows why the material is specified for moisture-sensitive and low-density applications. The table below uses dry-state values for the unmodified base polymers; the exact W 20 grade data must be obtained from the EMS-Grivory datasheet because plasticizer content shifts mechanical and rheological values.
| Material | Water absorption at saturation, ISO 62 (%) | Density, ISO 1183-1 (g/cm³) | Melting point, ISO 11357-3 (°C) |
|---|---|---|---|
| PA12 base (unmodified) | 1.4–1.6 | 1.01–1.02 | 176–180 |
| PA11 base | 1.6–1.9 | 1.03–1.05 | 185–189 |
| PA6 | 9.0–10.0 | 1.13–1.14 | 220–225 |
| PA66 | 8.0–9.0 | 1.13–1.15 | 260–265 |
Those values explain the selection logic. Grilamid L 25 W 20 is preferred over PA6 or PA66 when the application must maintain ductility after humid ageing and when part mass and moisture-induced dimensional movement are constrained. It is preferred over PA11 when the PA12 chemical resistance profile, lower density, or specific extrusion rheology is required; PA11 may be selected when a partly bio-based feedstock is a decisive requirement. The comparison against unmodified PA12 is equally important: the W 20 plasticizer modification trades off tensile modulus and hardness for higher elongation, lower flexural stiffness, and improved low-temperature impact behaviour. Published data for the exact plasticizer content and the resulting notched Charpy values under ISO 179-1:2010 should be consulted; generic PA12 class values cannot be substituted for design checks.
For applications involving fuel or oil contact, PA12-based grades are usually evaluated by volume and mass change after immersion under ISO 175 or by retention of tensile properties after fuel exposure under automotive standards. The lower amide density gives polyamide 12 a different polarity balance than PA6 or PA66, which can reduce the driving force for polar-fluid absorption. However, the plasticizer package in the W 20 grade may be partially extractable in some fluid formulations, so compatibility testing must be performed on the finished extruded tube or injection-moulded component with the actual service fluid. Published data for this specific configuration is limited when aggressive blends containing biodiesel or ethanol are involved.
On production-scale single-screw extruders with L/D ratios of 30:1 to 36:1 and compression ratios of 2.5:1 to 3.0:1, the melt temperature for Grilamid L 25 W 20 is normally controlled between 210 °C and 240 °C. Barrel profiles are ramped in three or four zones from a feed zone at 180 °C to 200 °C, through compression at 220 °C to 240 °C, to metering at 230 °C to 250 °C. Melt temperatures above 270 °C increase the risk of thermo-oxidative chain scission, yellowing, and loss of melt strength; total barrel residence time should be kept below 15 min. In injection moulding, barrel temperatures of 220 °C to 260 °C and mould temperatures of 40 °C to 80 °C are typical for PA12-based grades. Lower mould temperatures may be used for fast cycle times, but they can increase the frozen-in stress level and reduce the ductility of thin-wall sections.
Screw design for extrusion should use a three-zone screw with a mixing section when colourants or stabiliser masterbatches are added. For tubing and cable sheathing, filtration through a breaker plate with screen packs of 60/80/100 mesh is common; the pressure must be monitored to avoid exceeding the barrel flange and gearbox rating. Melt pressure on a 45 mm single-screw line at moderate throughput typically remains in the 150 bar to 250 bar range for PA12-based tubing compounds, but this range is not a product specification and must be verified on the actual line. Because PA12 has a coefficient of linear thermal expansion of approximately 110 × 10⁻⁶ K⁻¹ to 130 × 10⁻⁶ K⁻¹ under ISO 11359-2, tooling dimensions for injection moulds and calibration sleeves must allow for greater shrinkage than PA6 or PA66.
The process control envelope for the dry material is summarised below. The values are not grade-specific moulding recipes but are the control limits used in production planning; actual settings must be established on the production machine and recorded in the process sheet.
| Parameter | Extrusion | Injection moulding |
|---|---|---|
| Residual moisture target | <0.10 % by mass | <0.10 % by mass |
| Drying temperature | 80–100 °C | 80–100 °C |
| Drying time, desiccant dryer | 4–8 h | 4–8 h |
| Melt temperature | 210–240 °C | 220–260 °C |
| Mould/tool temperature | not applicable | 40–80 °C |
| Moisture verification method | ISO 15512:2019 | ISO 15512:2019 |
At the upper end of the melt-temperature range, residence time becomes the controlling variable. On a 30 mm laboratory extruder, short hold-up times may permit 250 °C without visible degradation, whereas a large accumulator head on a production line can hold material for longer than 10 min and should operate at the lower end of the temperature envelope. The difference is not a material inconsistency but the expected behaviour of a polyamide with a melt viscosity that depends on both thermal history and shear history.
Under ISO 1133-1:2022, the melt volume-flow rate of plasticized PA12 grades is higher than that of unmodified PA12 base polymer at the same load because the plasticizer reduces chain friction and free volume. The exact MVR value for L 25 W 20 should be taken from the supplier’s certificate of analysis, but the increased flowability permits thin-wall injection filling and high-speed extrusion of small-diameter tubing. However, the same flowability narrows the processing window for vertical walls: excessive melt temperature or excessively long residence time can produce flow marks, jetting, and dimensional instability in moulded parts.
If the sealed package is opened or damaged, moisture uptake begins immediately at a rate that depends on ambient relative humidity, temperature, and granule surface area. At 23 °C and 80 % RH, open-stored pellets can reach process-relevant moisture levels within several hours. Processing wet PA12 produces splay marks, surface roughness, and hydrolysis-induced viscosity loss; at die temperatures above 240 °C, dissolved water accelerates chain scission and can reduce extrudate burst strength. The corrective action is not to increase barrel temperature, because this worsens hydrolysis and thermal degradation. The material should be redried in a desiccant dryer at 80 °C to 100 °C for 4 h to 8 h. The drying air should have a dew point of −30 °C or lower and the moisture content should be confirmed at 0.10 % or less using ISO 15512:2019 or an equivalent calibrated Karl Fischer method. If the material has been stored in an open silo for more than 24 h, drying time may need to be extended to 8 h to 12 h; this is not a universal correction because hopper geometry, airflow distribution, and ambient load vary between plants.
Sealed packaging of the dry grade should be stored at temperatures between 10 °C and 30 °C and protected from direct sunlight and precipitation. Under those conditions, the manufacturer’s unopened shelf life is normally stated on the lot certificate; a period of at least 24 months is common for PA12 compounds, but the lot-specific document controls the actual limit. Opened bags should be reclosed immediately after transfer and purged with dry nitrogen when the remaining material will be stored longer than one shift. Storage should avoid direct contact with concrete floors because migration of alkaline ground moisture can contaminate the granulate surface, and strong oxidising agents or solvent vapours should not be stored in the same cabinet.
Chemical incompatibilities include hot concentrated mineral acids, phenols, cresols, and concentrated formic acid, which dissolve or severely degrade PA12. Chlorinated solvents may induce environmental stress cracking in moulded parts with high residual stress. Continuous exposure to hot water above 90 °C requires long-term hydrolysis, creep, and extraction data on the actual part geometry because plasticizer migration can alter flexibility and surface properties over time. Food-contact, potable-water, medical, and flame-retardant compliance is not automatically conferred by the PA12 polymer family; the specific EMS-Grivory commercial item, colour, and lot-specific regulatory documentation must be checked before such use.