| HS Code | 384721 |
| Density | 1.35 - 1.36 g/cm³ |
| Water Absorption 24 Hr | 0.20 - 0.25 % |
| Tensile Strength Ultimate | 140 - 150 MPa |
| Tensile Modulus | 10.5 - 12.5 GPa |
| Elongation At Break | 1.5 - 2.5 % |
| Flexural Modulus | 8.5 - 10.0 GPa |
| Flexural Strength | 180 - 200 MPa |
| Izod Impact Notched | 70 - 90 J/m |
| Melting Point | 183 - 190 °C |
| Heat Deflection Temperature 0 46 Mpa | 185 - 190 °C |
| Heat Deflection Temperature 1 8 Mpa | 170 - 180 °C |
| Linear Mold Shrinkage | 0.0010 - 0.0030 cm/cm |
| Volume Resistivity | 1.0e12 - 1.0e14 ohm·cm |
| Thermal Conductivity | 0.30 - 0.35 W/(m·K) |
As an accredited Overview of materials for Nylon 11 with 40% Glass Fiber Filler factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Moisture-resistant sealed polyethylene-lined kraft bags, each containing 25 kilograms of Nylon 11 with 40% glass fiber filler, ensure dry storage. |
| Container Loading (20′ FCL) | 20′ FCL: palletized bags of Nylon 11/40% glass fiber, secured, moisture-protected, weight within container limits. |
| Shipping | Ship as sealed moisture-proof bags or drums to prevent water absorption. Store in a cool, dry area away from heat sources. Avoid dust from glass fibers; use gloves and eye protection during handling. Ensure secure labeling and compliance with standard thermoplastic shipping regulations. |
| Storage | Store Nylon 11 with 40% glass fiber filler in a cool, dry environment, ideally below 30°C (86°F), inside sealed, moisture-proof containers to prevent hygroscopic moisture absorption. Keep away from direct sunlight, UV sources, and excessive heat. Avoid stacking heavy loads to prevent deformation. Use within recommended shelf life to maintain mechanical properties. |
| Shelf Life | Shelf life is indefinite when stored in a cool, dry place, protected from moisture, sunlight, and contamination. |
Engine-side fuel quick connectors molded from GF40 PA11 are required to survive cyclic pressure pulses between 0.4 MPa and 0.6 MPa at fuel temperatures peaking at 80°C while immersed in oxygenated methanol-gasoline blends; this is the zone where weld-line embrittlement appears because methanol diffusion follows the oriented fiber bundles and disrupts hydrogen bonding in the amorphous regions adjacent to the knit line. Compliance for the automotive fuel-system application is evaluated under SAE J2044 for quick-connect joint performance, SAE J2260 for thermoplastic tubing and connector material requirements, and ISO 19013-2 for sequential exposure testing in fuel components, supplemented by ASTM D638-14 tensile property verification on type I specimens cut across the weld plane. Production batches are adjusted by blending 60-70 parts of GF40 PA11 with 30-40 parts of unreinforced plasticized PA11 to bring actual glass content to 24-28 wt% and restore cross-weld elongation at break above 5%; this addition ratio shifts flexural modulus to roughly 55-65% of the fully loaded compound but preserves fuel permeation resistance in the thin-wall barb region. Drying before molding is executed at 100°C for 4 h with a dehumidifying dryer achieving a dew point of -40°C, because residual moisture above 0.08% causes surface splays and reduces weld strength. The hot-runner tool uses two valve-gated cavities and a nozzle tip temperature of 260°C; barrel profile is 240-255°C from throat to nozzle, and the mold is held at 80-90°C to promote interfacial crystallization across the knit line. A post-mold annealing operation at 130°C for 2 h in nitrogen is applied to relax fiber orientation stress, which otherwise raises crack propagation when the barb is pressed over a steel tube end. The operational boundary for this application is defined by methanol concentration: exposure to fuels exceeding 85% methanol at temperatures above 60°C is outside validated long-term service data for this specific glass-filled configuration. Terminal products include fuel line quick connectors, evaporative emission port connectors, and tank check valve bodies.
The shift to 800 V DC battery system architectures has changed the requirements for molded nonconductive supports from simple electrical insulation to combined creepage control, thermal stability at 150°C, and strict tracking resistance. GF40 PA11 is selected for these carriers because its saturated-moisture uptake of approximately 0.8 wt% under ISO 62 at 23°C is lower than that of PA6 and PA66 glass-filled grades, reducing dimensional change during humidity cycling. Compliance is assessed under IEC 60664-1 for pollution degree 3 creepage and clearance coordination, IEC 60112 for comparative tracking index with solution A, UL 94 vertical burn at 3.0 mm for flame class, and IEC 60243-1 for breakdown strength of 3 mm plaques, with reported values between 18 kV/mm and 25 kV/mm in molded plaques. The compound is processed without flame-retardant modification at the 40 wt% glass loading, with a heat stabilizer addition of 0.2-0.5 wt%; this loading is not reduced for creepage-critical parts because lower glass content moves thermal deflection under ISO 75-2 method A from the 170-185°C band toward the unfilled PA11 value. Injection molding is carried out on a 120-tonne hydraulic press with a 20:1 L/D screw; melt temperature is 250-265°C, mold temperature 70-90°C, and cavity pressure sensors maintain 65 MPa packing for 8 s until gate freeze. Tooling uses a hot manifold with natural-balanced runner layout; dead spots in the manifold are eliminated because residence time beyond 7 min causes visible browning at the gate entrance, and surface bloom occurs when mold release additive exceeds 1.5 wt%. Terminal products include high-voltage busbar supports, charging inlet housings, and disconnect switch bodies.
Cast metal impellers in sodium hydroxide service fail predominantly at the shaft-keyway crevice because chlorinated brine wetting alternates with atmospheric drying, promoting crevice corrosion that cannot be addressed by coating systems. 40 wt% glass-filled PA11 is substituted in end-suction chemical process pumps for rotating and wear components where the pH range of 2-12 excludes unfilled thermoplastics and where glass-filled PP is ruled out by temperature excursions to 80°C in suction lines. Chemical resistance is characterized according to ISO 175 immersion tests in 30 wt% sodium hydroxide at 80°C for 1,000 h, with tensile strength retention exceeding 80% relative to unexposed reference specimens when tested under ISO 527-2 type 1A; additional screening follows ASTM D543 for chemical reagent exposure and ISO 5199 for design and hydraulic performance classification. The formulation is used at the full 40 wt% fiber loading without plasticizer dilution, but regrind is restricted to a maximum of 20 wt% because each regrind pass reduces average fiber length from approximately 350 µm to below 200 µm and lowers notched Charpy impact by 25-35%. Large impeller bodies are molded with a three-plate mold and two hydraulic valve gates to shift the weld plane from the blade leading edge to the hub core; melt temperature is 260-275°C, mold temperature 80-100°C, and holding pressure is set at 50-70 MPa with a gate seal time of 10-14 s. Post-mold annealing at 150°C for 1 h is applied before dynamic balancing on a two-plane balancing machine to reduce later creep at the impeller bore under shaft clamp loads. Operational limits apply when chlorine dioxide is present: continuous exposure beyond 2 ppm at 80°C in moist gas can hydrolyze the PA11 surface and reduce tensile strength by 10-15%, although published data for this specific configuration is limited. Terminal products include impellers, volute casings, stuffing box wear rings, and baffle plates.
Automated drone arm injection cells running GF40 PA11 operate with mold temperatures held at 65-85°C because reduced mold temperature freezes glass fibers at the wall before packing pressure can compensate for the 0.8-1.2% volumetric shrinkage of the crystalline PA11 matrix. The resulting parts carry a fiber-rich skin layer of 0.2-0.4 mm that raises flexural modulus under ISO 178 to the 8,500-10,000 MPa range, while core-zone Charpy notched impact under ISO 179-1/1eA at 23°C falls between 10 kJ/m² and 13 kJ/m². Compliance for load-bearing bicycle pedal bodies adheres to ISO 4210-2 for sharp-edge and impact requirements, with material lot release tested under ISO 527-2 and ISO 179-1/1eA; drone enclosures are validated against internal fatigue protocols of 5 Hz, 500,000 cycles at maximum design bending moment because no harmonized material standard applies to that category. The compound is fed directly at 40 wt% glass content, but up to 10-15 wt% of an impact-modified PA11 is added when pedal body cold-crack requirements below -20°C are specified; that blend lowers flexural modulus by roughly 20% and requires re-qualification of mold shrinkage allowances. Production uses a 2-4 cavity tool on an 80-100 tonne electric injection press; pre-drying at 80-90°C for 5 h to 0.15% residual moisture, barrel profile 250-265°C, mold 65-85°C, and cycle time of 35-45 s for 3 mm wall sections. Terminal products include drone arm shells, bicycle pedal bodies, and ski touring binding levers.
Post-mold dimensional movement in GF40 PA11 instrument bodies continues for 24-48 h at ambient because the crystalline fraction formed during cooling does not reach equilibrium volume until the part passes through a final anneal; this is the primary process conflict for reusable life-science equipment that must fit into instrument nests after steam sterilization. Compliance for a non-invasive medical device housing is tested under ISO 10993-5 for cytotoxicity and USP <88> Class VI extraction for patient-contact polymers, with terminal sterilization validated under ISO 17665-1 in a saturated steam cycle at 121°C for 30 min. The filler loading is maintained at 40 wt% glass fiber, and a 5-10 wt% barium sulfate radiopacifier may be compounded in when fluoroscopic visibility is required; the radiopacifier addition reduces weld strength by approximately 15%, so weld lines are positioned away from latch bosses. Processing begins with an injection molded blank on a 90-tonne hydraulic press using melt temperature 250-270°C and mold temperature 60-80°C; after demolding, the blank is annealed at 150°C for 2 h in dry nitrogen, then critical bores and latch recesses are CNC machined to maintain ±0.05 mm true position tolerances that would be lost if machining preceded the anneal. Repeated autoclave cycling beyond 200 cycles at 121°C is not covered by published mechanical data for this specific configuration; surface hydrolysis increases with saturated steam exposure and can lower tensile strength by 10-15% after 300 cycles in unfilled PA11 reference studies, though filled-grade data remain scarce. Terminal products include reusable surgical instrument handle bodies, sterilization tray standoffs, and equipment housing panels.
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Polyamide 11 with 40% by mass E-glass fiber filler is a high-stiffness, semi-crystalline thermoplastic compound classified generically as PA11,GF40 under ISO 16396-1. The matrix is synthesised through polycondensation of 11-aminoundecanoic acid derived from castor oil, while the reinforcement consists of silane-sized E-glass fibres with filament diameters commonly between 10 µm and 17 µm. Commercial injection-moulding grades are supplied in pellet form with pellet moisture specified below 0.05 % by mass when measured by ISO 15512:2019 Karl Fischer coulometry. Typical isotropic specimen data consolidated from technical datasheets place density at 1.38–1.42 g/cm³ per ISO 1183-1, tensile modulus at 8,500–10,500 MPa per ISO 527-2, tensile strength at break at 120–150 MPa, elongation at break at 2.5–4.5 %, flexural modulus at 7,500–9,500 MPa per ISO 178, and notched Charpy impact at 8–14 kJ/m² per ISO 179-1/1eA. Heat deflection temperature under 1.8 MPa loading according to ISO 75-2 Method A is commonly reported between 165 °C and 180 °C. Melt volume-flow rate at 235 °C with 2.16 kg load is typically 4–12 cm³/10 min per ISO 1133-1, although glass-filled grades show pronounced dependence on residence time and shear history.
Processing of PA11-GF40 is bounded by moisture control, residence time, shear exposure, and fiber-orientation management. Pre-drying in a desiccant dryer at 80 °C for 4–6 h to a final moisture content below 0.05 % by mass is required when relative humidity exceeds 60 %. Hydrolysis reduces molecular weight; a moisture level above 0.10 % can reduce tensile strength by 5–10 % and produce silver streaks on moulded surfaces. Injection moulding uses a reciprocating screw with a length-to-diameter ratio of 20:1 to 24:1, a non-return valve, and nozzle melt temperature between 240 °C and 270 °C. Barrel zones are profiled from 230 °C at the feed throat to 260 °C at the metering zone. Mould temperature is held between 60 °C and 100 °C to control crystallinity and surface finish. Back pressure of 0.5–1.5 MPa and injection speeds of 30–100 mm/s are common. High screw speeds above 150 rpm intensify fiber attrition; initial fiber length of 3.0–4.5 mm can fall to 200–400 µm after compounding and moulding. This attrition changes modulus less than tensile strength but strongly affects anisotropy and weld-line integrity. On production-scale compounding lines using co-rotating twin-screw extruders with L/D 36:1 to 44:1, glass fiber is side-fed downstream after polymer melting; if side-feed zone melt temperature exceeds 280 °C, silane sizing degrades, producing discolouration and reduced interfacial adhesion. Vacuum devolatilisation at -0.08 MPa gauge is used to remove volatiles. Weld-line tensile strength retention in glass-filled polyamides is commonly 40–60 % of the parent material, so gate and vent locations must be positioned to move weld lines away from pressure boundaries and snap-fit features.
In service, PA11-GF40 appears in secondary structural components where lower equilibrium moisture uptake is required than PA6-GF40. Documented application areas include fuel-system brackets, quick-connector bodies, pneumatic manifolds, cable conduits, pump housings, and industrial fluid-contact components exposed to diesel, biodiesel, methanol-blended gasoline, and hydraulic oils. Performance under short-term road-salt exposure is characterised by lower amide density than PA66-GF40, which reduces plasticisation and dimensional change. Qualification practice uses salt-spray testing according to ISO 9227 or SAE J2334 and thermal shock profiles according to ISO 16750-4. In compressed-air systems, the compound maintains dimensional stability at intermittent operating temperatures up to 120 °C, but continuous exposure above 140 °C in air requires oxidation stabilisation. Published data for potable-water approvals of this specific glass-filled configuration is limited; water-contact compliance must be evaluated on the formulated grade.
Mould-filling simulation requires orthotropic material cards because fiber orientation creates significant stiffness anisotropy. Flow-direction tensile modulus may reach 8,500–10,500 MPa, while cross-flow modulus can fall to 5,000–6,500 MPa and thickness-direction modulus to 3,000–4,000 MPa. The flow-to-cross-flow modulus ratio commonly lies between 1.5:1 and 2.0:1. Finite-element models should use fiber-orientation tensor data generated from injection-moulding simulation and composite stiffness models such as Halpin-Tsai or Tandon-Weng. Stress-strain response should be captured at -40 °C, 23 °C, and 80 °C because PA11-GF40 exhibits nonlinear strain-rate dependence. The creep modulus at 1,000 h and 23 °C is typically 55–70 % of the short-term tensile modulus; published data for this specific configuration is limited.
| Property and test method | PA11-GF40 | PA6-GF40 | PA12-GF40 | PBT-GF30 |
|---|---|---|---|---|
| Density, ISO 1183-1 | 1.38–1.42 g/cm³ | 1.45–1.50 g/cm³ | 1.35–1.40 g/cm³ | 1.51–1.55 g/cm³ |
| Equilibrium moisture at 23 °C, 50 % RH, ISO 62 | 0.7–1.0 % | 2.3–2.8 % | 0.6–0.9 % | 0.2–0.4 % |
| Tensile modulus, dry-as-moulded, ISO 527-2 | 8,500–10,500 MPa | 10,000–12,500 MPa | 7,500–9,500 MPa | 9,000–11,000 MPa |
| Tensile strength at break, ISO 527-2 | 120–150 MPa | 160–190 MPa | 105–135 MPa | 120–140 MPa |
| Heat deflection temperature, 1.8 MPa, ISO 75-2/A | 165–180 °C | 190–205 °C | 150–170 °C | 200–210 °C |
| Notched Izod, 23 °C, ISO 180/1A | 8–14 kJ/m² | 9–15 kJ/m² | 8–13 kJ/m² | 7–10 kJ/m² |
Compared with PA6-GF40, PA11-GF40 has lower density and lower equilibrium moisture uptake, but lower dry tensile strength and lower heat deflection temperature. Compared with PA12-GF40, the 40% PA11 compound typically exhibits somewhat higher dry stiffness at equivalent conditioning, although property envelopes overlap across suppliers. Compared with PBT-GF30, PA11-GF40 has lower density and better resistance to hot aqueous fluids, but lower dimensional stability at elevated temperature. The selection boundary is not uniform because datasheet values depend on glass sizing chemistry, stabiliser package, fiber length distribution, and mould-flow orientation. Procurement specifications should therefore verify glass content by ISO 3451-1 ash residue with acceptance limits of 38–42 %, fiber length distribution by optical microscopy, and moisture content by ISO 15512.
In acidic and saline service, PA11-GF40 resists aliphatic hydrocarbons, chlorinated solvents, fuels, oils, and neutral salts, but undergoes degradation in strong mineral acids, phenol, and cresol. At 40% glass loading, the chemical resistance of the matrix is unaffected by the filler except where the fiber sizing is hydrolytically unstable. Coolant exposure in ethylene glycol at 130 °C should be verified by ISO 22088-2 or ISO 22088-3 stress-cracking tests because glass-filled PA11 can fail by environmental stress cracking at weld lines or flow fronts. Continuous immersion in hot water above 80 °C is not recommended without hydrolysis stabilisers because molecular weight loss reduces tensile strength. Zinc chloride road salts are less aggressive than with PA66-GF40, but concentrated calcium chloride brines can still produce surface pitting. Under sustained load, design calculations should account for creep modulus reduction and moisture-conditioned strength loss rather than relying on dry-as-moulded short-term values.
| Regulatory or application domain | Reference designation or test method | Typical condition or limit |
|---|---|---|
| Flammability | UL 94 | Ratings from HB to V-2 depending on stabiliser package; UL Yellow Card required for final part thickness |
| RoHS recast | Directive 2011/65/EU Annex II | Pb below 0.1 % by weight, Cd below 0.01 %, no PBB or PBDE above threshold |
| REACH SVHC | Regulation (EC) No 1907/2006 | Candidate-list substance content below 0.1 % by article mass |
| Food contact | FDA 21 CFR 177.1500; EU 10/2011 | Compliance applies to specific formulated grades; glass fiber and sizing require separate evaluation |
| Automotive fluid handling | ISO 6722; ISO 16750-4 | Temperature class up to 120 °C intermittent; fluid compatibility must be confirmed under defined test fuels |
| Water contact | NSF/ANSI 61 or AS/NZS 4020 | Published data for this specific configuration is limited; formulation-specific testing required |