| HS Code | 239776 |
| Density | 1.10 g/cm³ |
| Water Absorption 24h 23 C | 0.3 % |
| Tensile Modulus Conditioned | 1800 MPa |
| Tensile Stress At Break Conditioned | 50 MPa |
| Nominal Strain At Break Conditioned | 20 % |
| Charpy Impact Strength Notched 23 C Conditioned | 6 kJ/m² |
| Charpy Impact Strength Unnotched 23 C Conditioned | No break |
| Melting Temperature | 178 °C |
| Heat Deflection Temperature 0 45 Mpa | 145 °C |
| Heat Deflection Temperature 1 80 Mpa | 55 °C |
| Vicat Softening Temperature B50 | 160 °C |
| Mold Shrinkage | 0.4 % |
As an accredited EMS-Grivory Grilamid L XE 4074 black 9225 Nylon 12, Glass Bead Filled, 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 to prevent moisture pickup, labeled with product details and lot number. |
| Container Loading (20′ FCL) | 20′ FCL of Grilamid L XE 4074 black 9225 nylon 12, glass bead filled, conditioned, loaded in sealed containers on pallets. |
| Shipping | Ships in sealed, moisture-resistant packaging to protect the conditioned nylon 12 pellets. Standard ground freight is available; no hazmat designation applies. Keep dry and avoid extreme heat during transit. Delivery typically within 3–5 business days. |
| Storage | Store Grilamid L XE 4074 in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and oxidizing agents. Keep the original container tightly sealed to prevent moisture absorption, which can affect performance. Avoid exposure to excessive humidity or condensation. Ensure proper labeling and segregation from incompatible materials. |
| Shelf Life | Store sealed in cool, dry conditions away from sunlight. Shelf life typically two years from date of manufacture. |
EMS-Grivory Grilamid L XE 4074 black 9225 Nylon 12, Glass Bead Filled, Conditioned is used as supplied at 100 wt% in low-permeation fuel line quick connectors for gasoline, ethanol-blended fuel, and diesel return systems because the glass bead filler reduces isotropic mould shrinkage to 0.5–0.9 % after moisture conditioning at 23 °C and 50 % RH, while the PA12 matrix limits equilibrium moisture uptake to roughly 0.7 % in the same environment. Converters introducing in-house regrind into the feed stream should cap the regrind fraction at 20 wt% for connectors that must retain snap-fit engagement force after 1,000 h of fuel immersion; higher regrind fractions in this geometry reduce cold-temperature engagement tab recovery below -30 °C. Injection moulding of connectors with wall sections between 1.2 mm and 3.5 mm uses a melt temperature of 240–270 °C, tool temperature of 60–90 °C, screw L/D ratio of 20:1–25:1, and compression ratio of 2.0–2.5:1. Pre-drying at 80 °C for 4–6 h is required when opened containers exceed 0.1 % moisture, although the conditioned state for final part validation is reached separately after demoulding. Compliance is verified against SAE J2044 for quick-connect coupling performance, SAE J2260 for non-metallic fuel system components, and ISO 175 for volume and mass change after immersion in Fuel C and E85. Terminal parts include fuel line quick connectors, evaporative emission canister connectors, fuel sender flanges, and vapour return line couplings.
Push-to-connect fittings and manifold blocks in commercial vehicle compressed air systems require dimensional stability after moisture uptake and impact resistance below -40 °C. Glass bead–filled PA12 is used at 100 wt% compound in these components; any blending with unreinforced PA12 regrind is kept below 15 wt% because dilution reduces the bead loading required to maintain tight bore roundness after 85 °C thermal ageing. Moulding parameters for valve bodies with wall sections between 2.0 mm and 6.0 mm include melt temperature 250–280 °C, tool temperature 70–100 °C, and holding pressure 400–800 bar to avoid sink marks around insert threads. The production line typically uses a closed-loop injection moulding machine with a clamp force of 800–1,500 kN for multi-cavity tools; premature mould release is avoided by maintaining a mould surface temperature above 70 °C to allow the bead-filled skin to develop full crystallinity. Regulatory compliance relies on SAE J844 for thermoplastic air brake tubing, ISO 7628-1 for air brake hose dimensions, and ISO 228-1 for threaded port interfaces. Finished part types include push-in fittings for 10 mm and 12 mm nylon tube, quick release couplings, ABS modulator valve bodies, and axle-mounted distribution blocks.
In engine-bay fluid sensor housings, the conditioned compound is selected for low creep under clamp load and resistance to hot diesel fuel, engine oil, and aqueous urea solution. Moulding is conducted with the compound at 100 % virgin ratio; metal terminal insert moulding often requires a surface primer on brass or stainless steel leads, while the polymer melt temperature is held between 250 °C and 270 °C to prevent local degradation in thin-walled sections below 1.5 mm. Glass bead loading provides isotropic shrinkage during insert moulding, typically 0.4–0.8 % in the flow and transverse directions after 48 h post-mould conditioning at 23 °C/50 % RH. Compliance for automotive electronic housings includes ISO 16750-3 for mechanical loads, ISO 20653 for ingress protection, and IEC 60068-2-30 for damp heat cyclic testing; electrical connector tests are conducted on the completed assembly per OEM specifications. Terminal parts are diesel fuel filter sensor housings, oil level sensor bodies, DEF tank level sensor bobbins, and transmission park-lock position sensor frames.
For EV battery cooling couplers and thermal management line connectors, the central processing limit is melt residence time in hot-runner systems. The bead-filled PA12 melt is held at 250–280 °C, and residence time exceeding 10 min leads to surface streaking and a measurable fall in weld-line burst strength; therefore hot-runner channels are designed for balanced flow lengths no longer than 80 mm from manifold to gate. The material is processed at 100 % compound without dilution, because the flat plate stiffness required for O-ring groove sealing depends on the as-supplied glass bead content; if post-industrial regrind is used, the ratio is limited to 10–15 wt% and only in non-sealing bosses. Injection moulding for couplers with an internal bore of 12–25 mm uses a two-stage injection speed profile with a fast fill of 80–120 mm/s and a short hold time of 4–6 s to reduce gate blush. Compliance is anchored to ISO 527-1 for tensile modulus, ISO 178 for flexural modulus, ISO 1133-1:2022 for melt volume-flow rate, and RoHS Directive 2011/65/EU; REACH Article 33 documentation is maintained for substances of very high concern. End products include battery cooling line quick connectors, coolant pump outlet adapters, cabin heater couplers, and thermal management manifold segments.
Corrugated cable conduits and harness clips made from this glass bead–filled PA12 are extruded or injection moulded at 100 % compound ratio; black 9225 pigmentation is already compounded into the resin, so downstream colour masterbatch addition is not required unless a custom colour specification overrides the as-supplied code. External pre-consumer conduit scrap is capped at 20 wt% to retain flexural modulus after 1,000 h of heat ageing at 125 °C. Extrusion conditions for corrugated conduit with an inner diameter between 10 mm and 40 mm use a single-screw extruder with a 30:1 L/D barrier screw, barrel temperatures from 220 °C at the feed throat to 260 °C at the die, and a corrugator vacuum of 0.6–0.8 bar. The glass beads raise melt viscosity, so screen packs are specified at 80–120 mesh and die land length is increased by 20–30 % relative to unreinforced PA12 to control die swell. Compliance is verified through UL 94 HB for flammability, REACH Article 33 for substances of very high concern, RoHS Directive 2011/65/EU for restricted heavy metals, and ISO 6722-1 for class B cable insulation compatibility in adjacent wiring. Terminal parts include convoluted cable conduits, split corrugated sleeving, harness mounting clips, and junction box cover frames.
Chemical dosing valve bodies and pump heads in water treatment systems are injection moulded from the conditioned compound at 100 % as delivered; if processors blend a small fraction of glass fibre reinforced PA12 to raise burst strength, the amount of this glass bead grade is maintained above 80 wt% of the total polymer charge to preserve isotropic dimensional change during 24 h water immersion. Moulding of parts with internal threads and O-ring grooves uses melt temperature 250–270 °C, mould temperature 60–90 °C, and a holding pressure profile decaying from 800 bar to 300 bar over 8–12 s to prevent sink marks around the sealing faces. The downstream process includes post-mould conditioning at 23 °C/50 % RH for 48–72 h before dimensional inspection. Compliance includes ISO 175 for chemical immersion, ISO 62 for water absorption, REACH, and RoHS Directive 2011/65/EU. Terminal parts are dosing pump heads, injection quill housings, pH sensor adapters, and chemical injection valve bodies.
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EMS-Grivory Grilamid L XE 4074 black 9225 is a polyamide 12 injection-molding compound filled with 40 wt% glass beads and supplied in black color number 9225. The EMS designation places the grade in the L polyamide 12 family; XE identifies glass bead reinforcement, and 4074 defines the filler and additive package. The term "Conditioned" is not a separate product variant but a moisture state. Specimens conditioned to ISO 1110 or stored at 23 °C/50 % RH under ISO 62 absorb water into the amorphous phase, lowering glass transition and modifying tensile, impact, and creep response relative to dry-as-molded specimens. Published EMS-Grivory technical data give a dry density of approximately 1.29 g/cm³ by ISO 1183-1, and molded shrinkage of approximately 0.6 % to 0.8 % for 2 mm plaques by ISO 294-4.
The filler geometry is analytically significant. Glass beads have an aspect ratio close to unity, so they do not orient strongly in the shear field during injection. Packing and cooling therefore dominate residual stress development rather than flow-induced fiber alignment. On production machines with clamp capacities from 80 t to 120 t and screw diameters from 25 mm to 35 mm, the grade molds with relatively low anisotropic shrinkage, but gate freeze time is shorter than unfilled PA12 because the bead-filled melt freezes quickly. Parts with wall thickness below 0.8 mm require high injection speed, typically above 200 mm/s, to avoid premature freeze-off; published process data for this specific thickness configuration is limited.
The lower bound is set by the PA12 crystalline melting point at 175–180 °C by ISO 11357-3. Feed zone settings below 220 °C may produce unmelted granules and glass bead agglomerates because effective melt viscosity is high. The upper bound is limited by amide bond oxidation. Barrel profiles from feed to nozzle are commonly set between 220 °C and 270 °C; melt temperatures above 280 °C cause visible yellowing and molecular weight loss. The use of glass beads rather than glass fibers reduces shear heating, but erosion of screw flights, check ring, and nozzle tip occurs because hard silica-based filler slides across metal surfaces. Screw peripheral speed is kept below 0.3 m/s; higher speeds do not typically degrade the melt first but accelerate wear, especially at the check ring.
Mold temperature is the second critical variable. At 40 °C, a quenched amorphous skin forms quickly and can restrict packing in thin sections; at 80–90 °C, skin thickness is reduced and pressure transmission improves. Hold pressure is typically 50–80 MPa, with packing time of 2–4 s/mm wall thickness. Cooling time for a 3 mm wall is approximately 15–25 s; glass beads increase thermal conductivity relative to unfilled PA12, but the exact reduction in cooling time depends on mold steel, coolant temperature, and part geometry. Hot-runner valve gates are preferred over small open gate tips; gate diameter should be at least 1.5 mm to prevent bead jamming and excessive gate shear. On production-scale injection molding lines, the most common failure mode is not melt degradation but gate blush and surface roughness caused by glass beads migrating to the surface during high-speed injection. Reducing injection velocity below 100 mm/s for large gates and increasing mold temperature to 80 °C often reduces surface defects. Another observed effect is check ring leakage when the screw and barrel wear; this causes shot weight variation above 0.3 %. Replacement intervals for bimetallic screw and barrel assemblies are shorter than for unfilled PA12 because the glass beads are abrasive.
PA12 absorbs moisture more slowly than PA6 or PA66 because of its longer aliphatic chain and lower amide group density. Nevertheless, pellet surface moisture at processing can cause hydrolysis and splay. EMS processing documentation for polyamide 12 grades recommends pre-drying at 80 °C for 4–6 h in a desiccant dryer with a dew point below -20 °C after storage in open containers for more than 30 min at 23 °C/50 % RH. Residual moisture at the machine feed throat above 0.10 % by weight is associated with viscosity reduction and notched impact loss. A hot-air hopper dryer alone is insufficient when ambient relative humidity exceeds 60 %; desiccant drying is required.
The dry-as-molded state is not stable in service. After ejection, specimens and parts take up water from humid air. At 23 °C/50 % RH, a 3 mm thick plaque approaches equilibrium moisture content on a timescale of weeks, not hours, because moisture diffusion in PA12 follows Fickian kinetics with concentration-dependent diffusivity. Accelerated conditioning under ISO 1110 at 70 °C/62 % RH accelerates this. Water in the amorphous phase acts as a plasticizer; the glass transition temperature of dry PA12 is near 50–60 °C by ISO 11357-2, but in the conditioned state it can fall below 0 °C. This shift explains why conditioned tensile modulus and yield stress are lower, while elongation at yield and notched impact rise.
The mechanical response of this grade is dominated by the glass bead interphase and the plasticized matrix. In dry specimens, the matrix is stiff and relatively brittle under tensile deformation; in conditioned specimens, the matrix yields more readily, so tensile modulus declines from approximately 3500 MPa to 2500 MPa by ISO 527-1/-2. Tensile stress at yield drops from approximately 50 MPa to 34 MPa, while tensile strain at yield increases from about 5 % to 14 %. The glass beads themselves are rigid and do not absorb moisture; the property shift arises from the matrix. Notched Charpy impact at 23 °C by ISO 179-1/1eA increases from about 5 kJ/m² dry to 7 kJ/m² conditioned. At -30 °C, the conditioned gain is smaller because matrix mobility is reduced.
| Property | Test standard | Dry | Conditioned |
|---|---|---|---|
| Density | ISO 1183-1 | 1.29 g/cm³ | Not applicable |
| Tensile modulus | ISO 527-1/-2 | 3500 MPa | 2500 MPa |
| Tensile stress at yield | ISO 527-1/-2 | 50 MPa | 34 MPa |
| Tensile strain at yield | ISO 527-1/-2 | 5 % | 14 % |
| Charpy notched impact, 23 °C | ISO 179-1/1eA | 5 kJ/m² | 7 kJ/m² |
| Charpy notched impact, -30 °C | ISO 179-1/1eA | 4 kJ/m² | 4.5 kJ/m² |
| Heat deflection temperature, 1.80 MPa | ISO 75-2/A | 100 °C | Not typically published |
| Heat deflection temperature, 0.45 MPa | ISO 75-2/B | 145 °C | Not typically published |
Differences from unfilled PA12 are most visible in stiffness and dimensional stability. Unfilled PA12 has a dry tensile modulus near 1400–1600 MPa by ISO 527-1/-2; the glass bead-filled grade raises this to approximately 3500 MPa. However, the same filler reduces notched impact and may reduce weld-line strength because beads concentrate stress at the interphase. Flow-weld lines in glass bead-filled grades show strength retention of roughly 50–70 % of bulk yield, depending on melt temperature and mold temperature; published data for this specific color and conditioning state is limited.
Compared with short glass fiber reinforced PA12, the glass bead grade provides lower tensile modulus and strength but lower anisotropic shrinkage. A short glass fiber PA12 may show flow shrinkage below 0.2 % and transverse shrinkage above 1.0 % in 2 mm plaques; this difference drives warpage. The glass bead grade keeps flow and transverse shrinkage within 0.2 percentage points, enabling flat parts with dimensional tolerances below 0.05 mm/mm in some gated geometries. This is the main technical rationale for selecting XE 4074 over a fiber grade: not maximum mechanical strength, but predictable geometry.
Capillary rheometry for glass bead-filled PA12 shows pronounced shear thinning above 100 s⁻¹. The beads increase low-shear viscosity but contribute negligible melt elasticity because of spherical shape. In mold-filling simulation, a Cross-WLF or Herschel-Bulkley viscosity model calibrated from capillary data is needed; generic unfilled PA12 coefficients underpredict fill pressure in gates where shear rates exceed 10,000 s⁻¹. Published capillary viscosity data for this exact grade and color is limited; processing simulations should use material data from the EMS-Grivory database or direct capillary testing.
Creep data for glass bead-filled PA12 are more limited than short-term tensile data. Bead-filled grades generally show lower creep resistance than glass fiber grades at the same filler weight fraction because spherical particles do not bridge cracks or retain orientation. Under sustained loads above 20 MPa at 23 °C, creep strain can accumulate progressively; design calculations should use creep modulus from ISO 899-1 or supplier-generated isochronous stress-strain curves, not short-term tensile modulus. Fatigue performance under cyclic loading is sensitive to weld lines, surface roughness, and moisture. Published fatigue data for this specific glass bead-filled PA12 configuration is limited; designers should not extrapolate from unfilled PA12 or glass fiber PA12.
PA12 itself has one of the lowest water absorption values among common polyamides, near 1.2–1.5 % saturation in water at 23 °C by ISO 62. The glass bead filler reduces the matrix fraction and therefore tends to lower total water uptake proportionally. Resistance to automotive fuels, oils, greases, and salt spray is generally strong for PA12, but continuous exposure to hot glycol, methanol, or strong acids should be evaluated against the EMS chemical resistance list for Grilamid L grades. No universal compatibility statement applies; stress-cracking resistance depends on chemical concentration, temperature, and molded-in stress.
EMS-Grivory material data sheets for this grade typically reference classification under ISO 1043-1, ISO 1874-1, and marking under ISO 11469. RoHS and REACH statements are declared on the supplier lot-specific certification; users should verify the black 9225 colorant package for food-contact or medical suitability because pigmented variants may not carry identical regulatory status to natural resin. The material should not be processed with regrind above 30 % without remixing and impact verification. Processing regrind above 30 % may reduce Charpy notched impact and increase variability; published data for this specific grade is limited. The recommended practice is to limit regrind to 20–30 % and keep hopper residence time below 30 min in humid environments.
The grade is suited to molded parts such as sensor housings, solenoid valve bodies, cable clips, and pneumatic manifolds where dimensional stability and moderate stiffness are required over a temperature range from -40 °C to 80 °C. In such parts, the design should avoid thin sections below 0.8 mm, sharp internal corners below 0.5 mm radius, and hot-weld lines in tensile load paths. If continuous operating temperature exceeds 90 °C or if the part is exposed to hot air for more than 1000 h, oxidative embrittlement of PA12 becomes a design constraint and an antioxidant-stabilized grade or alternative material should be considered.