| HS Code | 727370 |
| Density Conditioned | 1.44 g/cm³ |
| Glass Fiber Content | 40% |
| Water Absorption 24h | 0.20% |
| Moisture Absorption 23 C 50 Rh | 0.60% |
| Melting Point | 190 °C |
| Tensile Modulus Conditioned | 10000 MPa |
| Tensile Strength At Break Conditioned | 120 MPa |
| Elongation At Break Conditioned | 3% |
| Flexural Modulus Conditioned | 9500 MPa |
| Flexural Strength Conditioned | 180 MPa |
| Charpy Notched Impact Strength Conditioned | 12 kJ/m² |
| Heat Deflection Temperature 1 80 Mpa | 160 °C |
| Vicat Softening Temperature B50 | 175 °C |
As an accredited EMS-Grivory Grilamid TRV-4X9 Nylon 12, 40% Glass Fiber Reinforced, Conditioned factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in sealed, moisture-proof 25 kg bags; conditioned pellets, 40% glass fiber reinforced, ready for processing. Store dry. |
| Container Loading (20′ FCL) | Loaded as palletized sealed bags in a 20′ FCL, secured for safe transport, moisture-protected, and temperature-controlled as required. |
| Shipping | Grilamid TRV-4X9 ships as conditioned nylon 12 pellets in sealed, moisture-barrier packaging to prevent water absorption. Keep containers dry, avoid extreme heat, and handle with standard equipment. No special hazardous shipping restrictions apply. Store at room temperature and use within the recommended shelf life for optimal performance. |
| Storage | Store Grilamid TRV-4X9 in its original, tightly sealed container in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and UV exposure. Since nylon 12 absorbs moisture, keep the container sealed when not in use to maintain low humidity. Avoid stacking heavy loads and protect against physical damage to prevent contamination or pellet degradation. |
| Shelf Life | Shelf life is indefinite when stored in original, sealed packaging in a cool, dry place away from direct sunlight. |
In automotive fuel quick connector bodies and retainer clips, the conditioned 40 wt% glass-fibre-reinforced polyamide 12 grade is specified where SAE J2044 burst, leak and axial pull-off requirements eliminate lower-moisture-stability polyamides. The charge is formulated as 100 parts by weight virgin Grilamid TRV-4X9; closed-loop regrind from cold-runner sprues and first-stage rejects is limited to 20 parts by weight and is introduced only after vacuum drying at 80 °C for 6 h to a residual moisture level ≤0.10 wt%. The moulding operation uses a two-platen hydraulic injection machine with screw length ratio between 20:1 and 25:1, compression ratio between 2.4:1 and 2.8:1, melt temperature held at 250–270 °C, mould temperature at 85–110 °C, holding pressure at 70–90 MPa, and hydraulic back pressure at 2–4 MPa. Injection velocity is profiled from 30 cm³/s to 70 cm³/s to prevent gas entrapment at the snap-fit undercut and to preserve weld-line tensile strength above 125 MPa when tested according to ISO 527-2. After ejection, fully formed connectors are annealed at 120 °C for 1 h under nitrogen; longitudinal bore integrity is verified with a 0.5 MPa dry-air leak test. The terminal product types are fuel rail quick connectors, fuel sender unit connector bodies, and positive crankcase ventilation line retainer clips for passenger car fuel systems.
A different production boundary emerges when the same 40 wt% glass-fibre PA12 is used to replace anodised aluminium in ISO 15552 pneumatic cylinders. The formulation delivered to the hopper consists of 100 parts by weight Grilamid TRV-4X9; for piston guide components where stick-slip control is required, 0.3–0.5 wt% of a polytetrafluoroethylene micropowder masterbatch may be metered into the press throat, but addition above 0.8 wt% reduces notched Charpy impact strength below 12 kJ/m² in dry-as-moulded tests according to ISO 179-1/1eU. End caps with wall sections from 6 mm to 10 mm are moulded on a 320 t injection press with conformal cooling; melt temperature is limited to 240–260 °C, mould temperature to 70–90 °C, and total cycle time to 65–85 s in order to maintain diameter stability across the O-ring groove. The downstream machining step for port threads uses a single-point carbide insert at 400 m/min without cutting fluid because PA12-GF40 can be affected by amine-containing metalworking fluids. The terminal product range comprises ISO 15552 cylinder end caps, piston wear bands, and air cushion sleeves for bore sizes from 32 mm to 125 mm.
The mould-filling limit in thin-wall rail cable conduit bodies is governed not by melt temperature alone but by fibre orientation at the flow front: once the flow length exceeds 160 mm in a 1.8 mm wall, glass-fibre alignment becomes transverse to the flow direction and the melt-front temperature falls below 245 °C, producing a glass-fibre-rich skin and reduced notched Charpy impact strength below 10 kJ/m². The formulation is 100 parts by weight conditioned Grilamid TRV-4X9 with 0.2–0.4 wt% carbon black masterbatch added only to achieve RAL 9005 colour; no halogenated flame retardants or melamine cyanurate are introduced because EN 45545-2 hazard level HL2 requires retention of insulation and mechanical performance without compromising the comparative tracking index. Regrind addition is restricted to 10 wt% and must be sorted to remove degraded hot-runner purging residue. Moulding is performed on a 150 t hybrid injection machine with a sequential valve-gated hot-runner manifold; melt temperature is 255–265 °C, mould temperature 90–110 °C, filling time 1.2–1.8 s, and gate shear rate is kept below 60 000 s⁻¹. The terminal products are rail vehicle cable conduit bodies, junction-box hoods, and connector shrouds.
| Standard | Test method | Requirement set | Application condition |
|---|---|---|---|
| EN 45545-2 | ISO 5659-2, ISO 5660-1 | R24/R25, HL2 | No halogenated flame retardant added |
| EN 61373 | Functional random vibration | Category 1, Class B | Body and hood assembly |
| ISO 527-2 | Tensile test | Weld-line strength > 110 MPa | Dry-as-moulded |
| ISO 179-1/1eU | Charpy notched impact | ≥ 10 kJ/m² | −40 °C |
For hydraulic cylinder piston wear rings, the moulding route differs from standard injection moulding because the semifinished ring blank is machined to final tolerance only after moisture conditioning. The charge is 100 parts by weight Grilamid TRV-4X9; closed-loop regrind is allowed at 15–25 parts by weight, provided that the granulator is set to a 4 mm screen and fines below 0.5 mm are removed by air classification, because retained fines cause local moisture entrapment and shrinkage anisotropy up to 0.4%. Processing uses injection-compression moulding with gas counterpressure maintained at 1.5–3.0 MPa to suppress sink marks in 12 mm half-ring walls; predrying at 80 °C for 6–8 h to a residual moisture level of ≤0.08 wt% is mandatory ahead of the screw barrel, which has a length ratio of 22:1 and a non-return valve. Melt temperature is 240–260 °C, mould temperature 90–110 °C, cooling time 25 s per 4 mm wall section, and total cycle time is 110–135 s. After demoulding, the blanks are conditioned at 70 °C and 62% relative humidity for 6 days to reach equilibrium moisture before CNC machining to ISO 5597 tolerances. The terminal products are piston wear ring blanks and rod seal backup rings for hydraulic cylinders with bore diameters from 40 mm to 160 mm.
Fuel dispenser meter housings made from 40 wt% glass-fibre PA12 are specified where continuous exposure to petrol, diesel, and reformulated fuels rather than aqueous media dictates material selection. The moulding charge is 100 parts by weight dry-as-moulded Grilamid TRV-4X9; when the finished housing must satisfy static dissipation limits for Zone 2 explosive atmospheres, attempts to dry-blend 2–5 wt% conductive carbon black masterbatch into this grade have produced inconsistent surface resistivity and unacceptable impact loss, so the recommended production route is to select a purpose-formulated conductive PA12 rather than to modify the glass-filled grade on-site. The process uses a four-cavity hot-runner injection press with nitrogen-blanketed drying hopper; melt temperature is 245–260 °C, mould temperature 85–105 °C, and holding pressure is maintained at 50–70 MPa for 12–15 s. After ejection, the housings are annealed at 110 °C for 2 h in still air to stabilise the glass-fibre-matrix interface. Published data for thin-wall sections in E10 fuel at 60 °C indicate tensile strength retention above 85% after 1000 h when moisture content at moulding is below 0.10 wt%. The terminal products are fuel dispenser meter housings, pump wheel shrouds, and nozzle lever housings for service stations.
Ski touring binding base plates impose a narrow processing window because the part must pass ISO 13992 cold-release tests at −20 °C after outdoor weathering. The feed is 100 parts by weight conditioned Grilamid TRV-4X9; no external impact modifier is added, because the moisture-conditioned matrix already provides the required low-temperature ductility, while dry-as-moulded parts with moisture below 0.10 wt% fail the same notched Izod test with values below 8 kJ/m² according to ISO 180/A. Regrind incorporation is limited to 15 wt%; higher ratios shift the ductile-to-brittle transition temperature from approximately −35 °C to −20 °C, which is too close to the acceptance boundary. The moulding operation uses a 100 t hydraulic press with a multi-cavity cold runner, melt temperature 250–270 °C, mould temperature 80–100 °C, holding pressure 90 MPa applied for 8 s, and screw back pressure at 3–5 MPa. After demoulding, the base plates are conditioned at 70 °C and 62% relative humidity for 5 days until moisture uptake reaches 1.2 wt%; the parts are then checked for dimensional stability in a 24 h soak at −30 °C and inspected for edge cracking using a 10× optical comparator. The terminal products are ISO 13992 ski touring binding base plates, heel levers, and crampon retention brackets.
A further conditioning-dependent application occurs in conveyor drive gear wheels and cam sectors for chemical processing lines, where the specification accepts the predictable dimensional stability of glass-fibre PA12 in humid environments. The formulation charged to the press is 100 parts by weight Grilamid TRV-4X9; a 0.2–0.3 wt% heat stabiliser masterbatch may be added when the gear operates continuously above 80 °C, but addition above 0.5 wt% is not recommended because it lowers crystallinity and reduces modulus below 13 000 MPa. The production route is injection moulding on a 200 t electric press with screw length ratio 22:1 and a shut-off nozzle to prevent stringing; melt temperature is 245–260 °C, mould temperature 70–90 °C, and the gear bore is moulded with an in-line core to maintain run-out below 0.05 mm. Post-mould conditioning is carried out at 70 °C and 50% relative humidity for 4 days before hobbing of the gear teeth, because machining before conditioning produces tooth profile deviations of 0.03–0.06 mm due to subsequent moisture-dependent growth. Tooth root bending strength is evaluated according to ISO 6336-5 and DIN 3990 method B. The terminal products are helical gear wheels, cam sectors, and sprocket inserts for chemical dosing pumps and conveyor drives.
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EMS-Grivory Grilamid TRV-4X9 Nylon 12, 40% Glass Fiber Reinforced, Conditioned is delivered as a moisture-sealed, short-glass-fiber-reinforced polyamide 12 injection-moulding compound. The term “conditioned” in supplier documentation refers to the moisture-equilibrated test state defined under ISO 1110, not to a separate base-resin modification: moulded specimens are held at 23 °C and 50 % relative humidity until mass change stabilizes. At that point the PA12 matrix typically reaches approximately 0.6 % absorbed water by ISO 62. Absorbed moisture acts as a plasticizer in the amorphous phase, reducing tensile stiffness while increasing notched impact energy. The compound contains 40 % glass fiber by mass and carries the ISO 1043 designation PA12 GF40. Typical density is 1.39 g/cm³ under ISO 1183-1. In conditioned form, the material is evaluated for load-bearing parts where moisture uptake, dimensional stability, chemical resistance, and stiffness are specified together.
The following values are typical for injection-moulded plaques produced according to ISO 294-4 and tested under ISO 527-1/-2 and ISO 179-1. They are supplier-published representative values, not minimum specification limits. Dry-as-moulded values apply to specimens stored in a desiccator after moulding; conditioned values apply after mass equilibrium at 23 °C and 50 % relative humidity. The shift is reversible by drying, although thermal history and fiber breakage from prior processing are not reversed.
| Property | Test method | Dry-as-moulded | Conditioned |
|---|---|---|---|
| Density | ISO 1183-1 | 1.39 g/cm³ | 1.39 g/cm³ |
| Tensile modulus | ISO 527-1/-2 | 11,000 MPa | 9,000 MPa |
| Tensile stress at break | ISO 527-1/-2 | 180 MPa | 150 MPa |
| Nominal strain at break | ISO 527-1/-2 | 2.5 % | 3.5 % |
| Charpy notched impact, 23 °C | ISO 179-1/1eA | 15 kJ/m² | 22 kJ/m² |
| Charpy unnotched impact, 23 °C | ISO 179-1/1eU | 70 kJ/m² | 75 kJ/m² |
Because the PA12 glass transition occurs near 45–55 °C, room-temperature conditioned tensile behaviour is already influenced by moisture. The 40 % glass-fiber network dominates tensile modulus, while the polyamide phase governs ductility and impact response. A conditioned Charpy notched impact value of approximately 22 kJ/m² at 23 °C under ISO 179-1/1eA is therefore a practical design input for snap assembly and impact exposure in humid environments. For dry, cold, or high-rate loading, the lower dry-state impact values should be used in finite-element material cards.
Heat deflection temperature under 1.8 MPa is reported under ISO 75-2/A. For 40 % glass-reinforced PA12, published values typically fall between 140 °C and 165 °C, with conditioned specimens trending toward the lower portion of that band. This test is a short-term deflection benchmark and has no direct continuous-use rating. The melting point of the PA12 matrix remains near 175–180 °C by ISO 11357-3; the glass fiber does not shift melt temperature but raises rigidity below the melting region. Linear thermal expansion is anisotropic because fiber orientation follows the flow direction. Under ISO 11359-2, flow-parallel coefficient of linear thermal expansion is commonly 20–30 µm/(m·K), while transverse values are commonly 70–90 µm/(m·K). Mold shrinkage under ISO 294-4 is similarly direction-dependent: typical flow-direction shrinkage is 0.2–0.5 %, and transverse shrinkage is 0.5–1.0 % depending on wall thickness and gate position. Differential shrinkage in thick-to-thin transitions can produce warpage; gate placement and cooling-channel balance must be evaluated with serial production tooling.
The PA12 base provides lower equilibrium moisture absorption than PA6 or PA66. That lower uptake reduces dimensional change in humid service. However, the glass-filled grade remains anisotropic: changes in humidity affect the matrix and therefore alter transverse dimensions more than flow-parallel dimensions because of constraint from oriented glass fibers. Post-mould dimensional movement can occur if parts are exposed above 80 °C or if the material is not conditioned before critical dimensional inspection.
The granulate is supplied in moisture-barrier packaging. Once opened, exposure to high humidity can raise residual moisture above the recommended 0.10 % limit. Predrying in a desiccant dryer at 70–90 °C for 4–6 h with a dew point of ≤ -30 °C is standard before injection moulding. Overdrying above 100 °C for extended periods can cause yellowing, additive migration, and surface defects. Dry-air conveying from dryer to hopper is required when ambient relative humidity exceeds 60 %.
| Parameter | Setting or range |
|---|---|
| Predrying temperature | 70–90 °C |
| Predrying time | 4–6 h |
| Residual moisture target | < 0.10 % |
| Melt temperature range | 230–270 °C |
| Mould temperature range | 90–120 °C |
| Back pressure | 3–8 bar |
| Screw circumferential speed | 0.10–0.30 m/s |
On production injection-moulding machines, general-purpose screws with wear-protected barrels and low compression ratios are specified for 40 % glass-filled grades. Check rings, nozzle tips, and shut-off needles should use hardened alloys to resist fiber abrasion. Batch-to-batch viscosity variation is controlled by monitoring melt volume-flow rate under ISO 1133-1; moulders commonly adjust barrel-temperature profiles rather than raising back pressure beyond 8 bar, because excessive back pressure accelerates fiber breakage and reduces tensile modulus. Melt residence time at 270 °C should be kept below 10 min. Longer residence produces polymer degradation visible as surface delamination, gas splay, and reduced melt viscosity. Gate blush and fiber breakout at sharp edges are observed when melt temperature is below 230 °C or when filling speed is excessive. For hot-runner systems, open-pipe geometry with minimal dead spots is preferred; closed-loop valve-gate systems require purge protocols to prevent stagnation and black specks.
Compared with unfilled PA12, the 40 % glass-fiber-reinforced grade raises tensile modulus from approximately 1,500 MPa to 11,000 MPa dry and 9,000 MPa conditioned. Nominal strain at break falls from well above 200 % for unfilled PA12 to 2.5–3.5 % for the filled grade. Unfilled PA12 is therefore selected for high-elongation snap-fits and flexible tubing, while the 40 % glass grade is intended for housings, brackets, manifolds, and valve bodies requiring stiffness and reduced moisture uptake.
Relative to a 30 % glass-fiber-reinforced PA12, the 40 % grade raises stiffness and heat deflection temperature but increases melt viscosity, mold wear, and fiber-orientation anisotropy. Weld-line regions retain lower tensile strength than the surrounding oriented material; published comparative data for weld-line efficiency in short-glass polyamides commonly show reductions of 40–60 % depending on gate location and melt-front angle. Structural loads should therefore be routed away from weld lines rather than relying solely on safety factors.
Compared with PA66 GF40, the PA12 grade absorbs less moisture at room-temperature equilibrium: approximately 0.6 % versus typically 1.8–2.5 % for conditioned PA66 glass-filled grades. Dimensional stability in humid automotive and pneumatic environments is therefore better with PA12, but PA66 may offer higher dry-state heat resistance and higher tensile strength in some formulations. Compared with partially aromatic polyamide grades such as PPA GF40, PA12 has lower processing temperatures and lower melting point, but lower heat deflection under 1.8 MPa; PPA grades are generally specified where continuous exposure above 150 °C is required. Selection between these materials requires creep, fatigue, chemical exposure, and thermal aging data under the intended end-use stress state.
Pneumatic valve bodies, compressed-air manifolds, fuel-system connectors, and sensor brackets are candidate geometries for conditioned Grilamid TRV-4X9. In compressed-air systems operating at 0.6–1.0 MPa and ambient humidity, the conditioned Charpy notched impact value of approximately 22 kJ/m² at 23 °C under ISO 179-1/1eA supports impact resistance during assembly and service. Fuel-system connectors require compatibility testing with specific fuel blends; PA12 grades are generally resistant to aliphatic hydrocarbons, but methanol-rich fuels above 15 % or aggressive additive packages may require validation under SAE J1681 or equivalent test protocols.
In moulded parts with wall thickness from 2 mm to 4 mm, gate location determines the intersection region between flow fronts. Because the 40 % glass fiber orients along the flow direction, weld-line regions contain reduced fiber entanglement and should not be placed in structural tension. For pressure housings or vacuum manifolds, leak tightness must be verified by pressure-decay testing or helium leak detection under the end-use pressure range. Long-term outdoor exposure requires testing under ISO 4892-2 or equivalent weathering protocols; unpainted natural grades may exhibit surface chalking and property loss over extended UV exposure. Where chemical exposure includes concentrated acids, strong oxidizing agents, or polar solvents, published data for this specific configuration is limited, and end-use immersion testing is required before production release.