| HS Code | 776188 |
| Density | 1.45 g/cm³ |
| Glass Fiber Content | 40 % |
| Tensile Strength | 160 MPa |
| Tensile Modulus | 10.5 GPa |
| Elongation At Break | 1.8 % |
| Flexural Strength | 215 MPa |
| Flexural Modulus | 8.6 GPa |
| Izod Impact Notched | 21 kJ/m² |
| Izod Impact Unnotched | 74 kJ/m² |
| Heat Deflection Temperature At 1 82 Mpa | 170 °C |
| Melting Temperature | 178 °C |
| Water Absorption 24 Hr | 0.20 % |
As an accredited PlastiComp Complet LGF40-PA12 Nylon 12, 40% Long Glass Fiber Reinforced factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied as 25 kg moisture-resistant sealed bags of PlastiComp Complet LGF40-PA12 Nylon 12 pellets, 40% long glass fiber reinforced. |
| Container Loading (20′ FCL) | 20′ FCL loading of PlastiComp LGF40-PA12: palletized, sealed bags/boxes, evenly distributed, weight optimized for safe transport. |
| Shipping | Ship in sealed moisture-barrier packaging to prevent nylon’s hygroscopic absorption. Keep in cool, dry conditions, away from direct sunlight. Non-hazardous material; standard dry freight is suitable. During transit, avoid excessive heat or humidity. Handle with care to minimize dust from glass fiber reinforcement. Label as engineered thermoplastic composite pellets. |
| Storage | Store in original, unopened packaging in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and moisture. Keep containers tightly sealed after use to prevent moisture absorption, which can degrade the nylon matrix. Ideal storage temperatures are below 30°C (86°F). Protect from dust and physical damage. Use within one year. |
| Shelf Life | Store in sealed original packaging in cool, dry conditions. Use within 12 months of receipt to prevent moisture uptake and property loss. |
PlastiComp Complet LGF40-PA12 Nylon 12, 40% long glass fiber reinforced, enters external orthotic shell manufacturing as a pelletized long-fiber compound in which the glass fiber is co-roped with the PA12 matrix and chopped to 11 mm to 13 mm pellet length; after injection molding on a general-purpose screw, residual fiber length in the molded part commonly falls between 1.5 mm and 3.0 mm when measured by burn-off and image analysis, and this retention governs the orthotic shell’s flexural fatigue threshold more directly than the pellet glass content. Published data for this specific configuration is limited to typical long-glass PA12 grades tested on ISO 294-1 multi-purpose specimens; the design baseline bands in the table below are compiled from commercial long-glass PA12 materials and should be replaced with lot-specific certificate values for final finite element analysis.
| Property | Test method | Typical band |
|---|---|---|
| Density | ISO 1183-1 | 1.27–1.32 g/cm³ |
| Tensile strength at break | ISO 527-2 | 140–180 MPa |
| Tensile modulus | ISO 527-2 | 9,000–12,500 MPa |
| Flexural modulus | ISO 178 | 8,500–12,000 MPa |
| Notched Charpy impact, 23 °C | ISO 179-1/1eA | 20–35 kJ/m² |
| Notched Charpy impact, -30 °C | ISO 179-1/1eA | 15–25 kJ/m² |
| Heat deflection temperature at 1.8 MPa | ISO 75-2/A | 160–185 °C |
In a production-scale orthotic shell mold, the material is dried at 80 °C for 4 h to 8 h in a desiccant dryer to a dew point of -30 °C or lower, because PA12 hydrolyzes at melt temperature when residual moisture exceeds 0.15%. Barrel temperature profiling from the feed throat to nozzle is set at 240 °C, 250 °C, 260 °C, and 265 °C, with a nozzle temperature of 260 °C to 270 °C; the mold temperature is held between 60 °C and 90 °C to balance crystallinity development against ejection-induced warpage. A screw with L/D 20:1 to 24:1 and a compression ratio of 1.8:1 to 2.2:1 is specified; back pressure is limited to 0.3 MPa to 0.7 MPa and screw surface speed is held below 0.25 m/s to avoid fiber attrition in the melt film. Regrind from sprues and cold runners is limited to 10% by weight because each regrind pass reduces number-average fiber length by 15% to 30% when measured by burn-off and image analysis, and higher ratios create a measurable drop in ISO 178 flexural modulus. External orthotic components are validated for skin-contact biocompatibility using ISO 10993-5 cytotoxicity and ISO 10993-10 sensitization; the PA12 base resin generally shows lower water absorption than PA66 at 23 °C water saturation per ISO 62, with values near 1.5% to 2.0%, which stabilizes shell dimensions in humid environments but does not eliminate the need for moisture conditioning before AFO assembly. Terminal products include anterior floor reaction AFO shells, prosthetic socket frames, and spinal orthosis segments, where the 40% long glass loading provides the required bending stiffness without the full weight of a thermoset carbon laminate. If shell wall thickness drops below 3.0 mm, the moldflow fill pattern produces fiber orientation transverse to flow at rib intersections, and these zones exhibit flexural strength loss of 30% to 50% relative to the oriented bulk; therefore ribs and hinge zones are gated at the thickest section and sequential valve gates are used for multi-cavity tools.
Injection molded LGF40-PA12 brackets in electric vehicle battery modules connect cell stacks to the pack enclosure, carry vibration and crash pulse loads, and operate in a dry pack environment where PA12’s low moisture uptake relative to PA66 reduces post-mold dimensional drift. The primary processing conflict is fiber orientation at narrow ribs and weld lines. Published data for this specific configuration is limited, but long-glass PA12 grades tested under ISO 527-2 show that weld-line tensile strength can be 40% to 60% lower than the un-welded oriented value, and the reduction is aggravated when two flow fronts meet at a rib less than 2.0 mm wide. Gate placement for a side frame bracket is therefore shifted from the center of the part to the thickest boss, and the flow path is designed so that the final weld line falls in a low-stress web rather than at a mounting hole. The bracket wall thickness is maintained at 3.0 mm to 5.0 mm; below 2.5 mm, shear-induced fiber breakage increases and residual fiber length falls below 1.0 mm, shifting mechanical properties toward a short-glass PA12 response.
Production-scale molding of battery module brackets uses a low-compression screw with L/D 22:1, back pressure 0.2 MPa to 0.5 MPa, and a screw speed of 40 rpm to 80 rpm. Barrel temperatures from feed to nozzle are set at 250 °C, 260 °C, 270 °C, and 275 °C; mold temperature is held at 80 °C to 90 °C to reduce post-shrinkage and improve weld-line toughness. A mold clamp force of 3,500 kN to 5,000 kN is typical for a two-cavity bracket mold with a projected area of 800 cm², though actual clamp requirement is calculated from cavity pressure multiplied by projected area with a safety factor of 1.5. The bracket is dried at 80 °C for 4 h to 6 h to a moisture content below 0.10%; wet pellets produce splay and hydrolysis-induced viscosity loss that reduces weld-line integrity further.
Flammability is an operational boundary. LGF40-PA12 without flame-retardant modification typically carries a UL 94 classification of HB at 1.5 mm; it does not meet UL 94 V-0 requirements for enclosure sections adjacent to high-energy cells unless a separate mineral-filled fire block or intumescent sheet is added. Terminal products include cell-to-pack side brackets, module end plates, and busbar support frames, where the compound’s dielectric strength and mechanical stiffness are used but metallic current-carrying parts remain separately isolated. Bolt torque relaxation on steel inserts is a known failure mode; insert bosses are designed with an outer diameter at least 2.0 to 2.5 times the insert nominal diameter, and compression testing per ISO 604 at 80 °C is used to screen insert retention.
Manifold bodies injection molded from LGF40-PA12 replace low-pressure hydraulic distribution blocks in water-glycol circuits operating at 0 bar to 12 bar and at temperatures not exceeding 80 °C. The driving variables are internal flow channel geometry and fatigue crack initiation at sharp polymer corners. A direct substitution of a machined aluminum manifold is not possible because long glass fibers orient along the flow path and create mechanical anisotropy; holes drilled after molding cut across the fiber skin and expose glass bundles that act as stress raisers at O-ring grooves. Published data for this specific configuration is limited, but injection molding trials show that channels with a radius smaller than 3.0 mm at the intersection between the longitudinal bore and the transverse outlet generate a low-strength weld line downstream; the channel intersection is redesigned with a 5.0 mm radius and the gate is located at the mounting flange to push the weld line into the non-pressurized boss.
Fatigue validation on production parts is performed using a test protocol adapted from ISO 10771-1, because that standard is written for metal pressure-containing envelopes and its metallic acceptance criteria do not transfer directly to polymer manifolds. The polymer manifold is filled with water-glycol at 50 °C and pressure-cycled from 0 bar to 12 bar at 2 Hz for 1 million cycles; the part is rejected if any visible weeping occurs at the threads or if a pressure drop greater than 5% of the target pressure is recorded. Molding parameters for manifold bodies include a melt temperature of 255 °C to 265 °C, a mold temperature of 70 °C to 90 °C, and a nozzle orifice diameter of at least 5.5 mm to reduce fiber breakage. A cold runner with hot sprue bushing is preferred because hot-runner channels introduce additional residence-time history that can degrade PA12 under prolonged hold.
The chemical boundary of PA12 in hydraulic service is defined by the hydrolysis resistance of the amide linkage and the selected heat stabilizer; exposure to zinc chloride or strong mineral acids must be avoided, and continuous contact with water-glycol above 80 °C is not recommended without lot-specific aging data. Terminal products include low-pressure hydraulic manifolds, hose junction blocks, and valve adapter plates used in mobile hydraulic systems where corrosion from road salts on aluminum manifolds is a known field failure. The mold design is pressure-tested at 1.5 times the maximum working pressure for 30 min before production release; this is not a substitute for cyclic fatigue but screens gross porosity and weld-line voids.
Pneumatic valve bodies historically machined from A380 aluminum are converted to LGF40-PA12 when compressed air contains condensation, because aluminum die-cast bodies develop corrosion products at O-ring grooves and valve spool bores. The polymer replacement is not a drop-in material; the pressure rating must be derated at elevated temperature, and the thread interface must be redesigned from machined threads to brass inserts. At 23 °C, a wall thickness of 5.0 mm with fiber orientation parallel to the main spool bore supports a maximum working pressure of 10 bar; at 50 °C, the continuous pressure rating is derated by 30% to 7 bar, because the polymer creep modulus decreases and long-term hydrostatic strength follows a time-temperature shift. Published data for this specific configuration is limited; proof pressure testing at 1.5 times the rated working pressure for 30 min is used as a production screen, but it does not replace cyclic validation.
Injection molding of pneumatic valve bodies uses sequential valve gates to place weld lines away from the spool bore and O-ring sealing faces. The mold temperature is set at 90 °C to 100 °C to achieve a resin-rich surface layer over the glass fibers; this layer reduces gas leakage along exposed fiber bundles that can form on machined sealing surfaces. The screw has a low-shear profile with L/D 22:1 and a compression ratio of 1.8:1; screw speed is limited to 50 rpm to 70 rpm, and back pressure is set to 0.2 MPa to 0.4 MPa. Brass inserts with a diamond knurl are installed by thermal insertion; the boss outer diameter is specified at 2.0 to 2.5 times the insert outer diameter, and the insert is located at least 1.5 mm from any glass-rich knit line. Terminal products include pilot-operated pneumatic solenoid valve bodies, ISO 5599-1 manifold subbases, and compressed air filter housings.
Chemical compatibility of the PA12 matrix in pneumatic service is evaluated under ISO 175 by immersion in IRM 902 reference oil at 23 °C for 7 days; mass change above 2% or surface cracking after immersion indicates an unacceptable differential swelling between the PA12 matrix and the long glass reinforcement. Compressed air lubricants containing ester-based additives can plasticize PA12 and lower the tensile modulus measured under ISO 527-2; if ester lubricants are unavoidable, the part is post-annealed at 100 °C for 2 h to stabilize crystallinity before assembly. Avoid contact with chlorinated solvents and strong acids, which attack the polyamide backbone and cause environmental stress cracking at molded-in stress concentrations.
| Application segment | Standard or test method | Condition | Acceptance criterion |
|---|---|---|---|
| External orthotic shells | ISO 10993-5, ISO 10993-10 | Extract at 37 °C, 72 h | No cytotoxicity, no sensitization |
| EV battery module brackets | UL 94 | 1.5 mm specimen | HB classification; V-0 not achieved without modification |
| Hydraulic manifold bodies | ISO 10771-1 adapted | 0 bar to 12 bar, 2 Hz, 50 °C | No weep, pressure drop below 5% after 1 million cycles |
| Pneumatic valve bodies | ISO 175 | IRM 902 oil, 23 °C, 7 days | Mass change below 2%, no surface cracks |
| Robotic end effector arms | ISO 899-1, ISO 6603-2 | Creep at 23 °C, puncture at -10 °C and 4.4 m/s | Creep modulus fitted; ductile puncture without bulk fracture |
| Conveyor guide rails | ISO 294-4 | Mold shrinkage, parallel and perpendicular | Dimensional allowances according to tolerance class |
Ski touring binding baseplates molded from LGF40-PA12 are subjected to cyclic bending at -20 °C, point-impact loading during release, and ultraviolet exposure at altitude; the material selection is driven by PA12’s lower moisture absorption relative to PA6 and the long glass fiber’s improved crack propagation resistance under ASTM D7791 flexural fatigue. Published data for this specific configuration is limited, but long-glass PA12 grades tested at 23 °C under ASTM D7791 at a stress amplitude of 60 MPa typically show a shallower S-N slope than short-glass PA12 at the same 40% glass loading, meaning the long-fiber variant tolerates a higher number of cycles before a 10% stiffness loss. The baseplate wall thickness is set between 4.0 mm and 6.0 mm, and the edge gate is oriented parallel to the principal bending axis so that fiber alignment follows the load path; a center gate in a flat plate produces radial fiber orientation and a weak zone at the transverse edge.
Processing of ski binding baseplates on a production injection molding machine uses a melt temperature of 250 °C to 270 °C, a mold temperature of 80 °C to 100 °C, and a hold pressure of 60 MPa to 80 MPa applied for 8 s to 12 s. The core and cavity mold blocks are heated separately with a differential not exceeding 10 °C; larger differentials create asymmetric crystallization and a bowed baseplate after ejection. The material is dried at 80 °C for 4 h to 6 h to a dew point of -30 °C, and regrind is limited to 5% because the binding baseplate is a safety-relevant component and impact performance at -30 °C per ISO 179-1/1eA is sensitive to fiber length reduction. Because ski touring components are exposed to UV and repeated temperature shock, the molded baseplate is post-annealed at 100 °C for 2 h to relieve molded-in stress and stabilize enthalpy relaxation; post-annealing can shift heat deflection temperature under ISO 75-2/A upward by 5 °C to 10 °C but may slightly reduce impact at -30 °C. Terminal products include alpine touring binding baseplates, ski brake arms, and heel release housings; final release torque calibration is performed on the complete binding system, not on the polymer baseplate alone.
When a robotic end effector arm is converted from cast aluminum to LGF40-PA12, the replacement design must address two failure modes: creep under sustained clamp force and impact fracture at high strain rate. The compound’s short-term tensile modulus under ISO 527-2 is in the 9,000 MPa to 12,500 MPa band, but the design stress under continuous clamp load should not exceed 25 MPa at 23 °C without creep data; creep modulus measured under ISO 899-1 at 23 °C and 1,000 h is lower than the short-term value and must be used in stiffness calculations. The arm is molded in a two-cavity tool with a projected area of 1,800 cm²; a clamp force of 6,000 kN to 10,000 kN is required when cavity pressure reaches 40 MPa to 50 MPa during fill. Sequential valve gates are positioned along the length of the arm to create unidirectional fiber orientation and move knit lines to low-stress web sections.
Impact validation for end effector arms is carried out with ISO 6603-2 instrumented puncture tests at 23 °C and -10 °C; the test distinguishes ductile penetration from brittle multi-crack failure, which is not captured by notched Charpy data alone. At -10 °C, the long glass PA12 retains a ductile hinge region in thick sections but may show microcracking on the glass-matrix interface when the impact velocity exceeds 4.4 m/s; a critical design rule is to avoid sharp internal corners with a radius below 1.5 mm near bolted connections. The material is dried at 80 °C for 4 h to 6 h before molding; melt temperature is 250 °C to 270 °C, and mold temperature is 80 °C to 90 °C. Steel threaded inserts are installed after molding with an ultrasonic insertion process; the insertion horn force is limited to 1.5 kN per insert to prevent hoop stress cracking. Pin-loaded tensile tests per ASTM D5961 Method A show that bearing strength parallel to fiber orientation is higher than perpendicular bearing strength by 20% to 40%; the bolt hole is therefore positioned so that the principal clamp load runs parallel to the main fiber orientation, and the hole edge distance is at least 2.0 times the hole diameter to prevent premature shear-out. Terminal products include robotic gripper arms, end effector plates, and tool-changing adapter housings used in automated machining cells.
Conveyor guide rails injection molded from LGF40-PA12 are machined after molding to flatness and parallelism tolerances because the 40% long glass fiber creates anisotropic shrinkage that cannot be fully compensated by a single mold cavity dimension. ISO 294-4 shrinkage specimens show parallel-to-flow shrinkage of 0.1% to 0.3% and perpendicular-to-flow shrinkage of 0.4% to 0.8%; a long straight guide rail must be gated at one end and vented at the other to produce the most uniform orientation, but the far end still exhibits a higher transverse shrinkage contribution. The molding process uses a melt temperature of 255 °C to 265 °C, a mold temperature of 80 °C to 100 °C, and a holding pressure of 70 MPa to 90 MPa; mold temperature variation across the part is kept below 5 °C to limit post-ejection bow.
Machining of long glass PA12 guide rails is performed with carbide tools with a nose radius of 0.4 mm to 0.8 mm; high-speed steel tooling wears rapidly at the glass-matrix interface, and tool life is typically 20% to 40% shorter than unfilled PA12 machining when measured by cutting-edge flank wear. The terminal products are linear guide rails, conveyor wear strips, and star wheel spacing segments for bottling lines; in dry-running conditions, the PA12 matrix provides lower friction than PA66, but the long glass content increases abrasion on steel guide rails if the surface is machined rather than molded with a resin-rich skin. The application is limited to ambient temperatures below 60 °C and does not replace PEEK or PTFE in high-speed dry-running or chemical washdown conditions.
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PlastiComp Complet LGF40-PA12 is a nylon 12 long-fiber thermoplastic compound with a nominal glass fiber loading of 40% by weight. The product designation identifies the Complet pultruded pellet architecture, in which continuous glass rovings are impregnated with polyamide 12 and cut into cylindrical pellets. The as-supplied pellet length is typically 10–12 mm, and the defining difference from short-glass PA12 compounds is the retention of fiber length after injection molding. Molding with adequately sized gates and runners preserves a number-average glass fiber length above 1 mm in the final part, whereas short-fiber PA12 grades of identical nominal glass fraction commonly fall below 0.5 mm. This fiber-length threshold controls load transfer, crack propagation resistance, and creep behavior. The grade is used where stiffness, low-temperature toughness, low moisture uptake, and mass reduction must be balanced.
Published data for 40 wt% long-glass PA12 compounds indicate dry-as-molded density between 1.30 g/cm³ and 1.35 g/cm³ under ISO 1183-1:2019. Because the PA12 matrix absorbs less water than PA6 or PA66, the compound retains a higher fraction of its dry mechanical properties in humid service. Saturation water uptake is typically 1.2–1.6% under ISO 62:2008, compared with 4.5–6.5% for short-glass PA66 grades. The distinction matters in air brake, pneumatic, and fuel-system-adjacent components where dimensional stability and low-temperature impact are simultaneously required.
The long-fiber architecture is produced by passing continuous glass rovings through a PA12 melt bath and cutting the fully impregnated strand, a process that avoids the high-shear distributive mixing used for short-fiber compounds. In short-glass production, chopped glass is fed into a twin-screw extruder where fiber fracture occurs during dispersion; the number-average fiber length in the molded article typically drops below 0.5 mm. The long-glass pellet retains fibers above the critical length for effective stress transfer, so tensile modulus and notched impact energy are not governed solely by glass weight fraction. The following table lists representative dry-as-molded values for the product class. Published data for this specific configuration is limited; final part properties must be confirmed on lot-specific certificate of analysis and molded plaques.
| Property | Test method | Typical value | Test condition |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.30–1.35 g/cm³ | 23°C, dry as molded |
| Tensile strength at break | ISO 527-1/-2:2012 | 120–145 MPa | 23°C, dry as molded |
| Tensile modulus | ISO 527-1/-2:2012 | 9,000–11,000 MPa | 23°C, dry as molded |
| Flexural strength | ISO 178:2019 | 190–220 MPa | 23°C |
| Flexural modulus | ISO 178:2019 | 8,500–10,500 MPa | 23°C |
| Notched Charpy impact | ISO 179-1/1eA:2020 | 25–40 kJ/m² | 23°C |
| Notched Charpy impact | ISO 179-1/1eA:2020 | 20–30 kJ/m² | −40°C |
| Heat deflection temperature | ISO 75-1/-2:2013 | 160–175°C | 1.8 MPa, flatwise |
| Melting temperature | ISO 11357-3:2018 | 175–180°C | second heat |
| Water absorption at saturation | ISO 62:2008 | 1.2–1.6% | 23°C, water |
| Coefficient of linear thermal expansion, flow direction | ISO 11359-2:2018 | 1.5–2.5 × 10−5 K−1 | −30°C to 100°C |
| Coefficient of linear thermal expansion, transverse direction | ISO 11359-2:2018 | 6–8 × 10−5 K−1 | −30°C to 100°C |
Because long-glass reinforcement shifts failure from matrix yielding to fiber-dominated fracture, the low-temperature notched Charpy impact range remains above 20 kJ/m². This retention of toughness at −40°C is a primary difference from short-glass PA12 compounds of the same nominal glass content, which can exhibit brittle fracture below 12 kJ/m² under the same test method. The stiffness values, however, should not be interpreted as isotropic; long-fiber orientation in molded plaques and parts creates direction-dependent mechanical response.
For cyclic loading, the retained fiber length reduces crack propagation rate and improves endurance relative to short-fiber PA12. Designers should request ISO 13003 fatigue data for the specific gate and weld-line configuration because weld lines locally reduce fatigue strength. Published data for this specific configuration is limited; coupon-level fatigue values do not transfer directly to parts with knit lines or high fiber-orientation gradients. Glass content should be verified by calcination or thermogravimetric analysis per ISO 1172:2023, while fiber length distribution can be determined by solvent digestion and optical microscopy.
Pre-drying must reduce moisture content below 0.10% before melt processing. Desiccant drying at 80°C for 4–8 h is typical, with a supply air dew point of −40°C or lower. If moisture exceeds 0.10%, hydrolysis of the PA12 matrix reduces molecular weight, lowers melt viscosity, and creates splay or surface delamination. Exposure to ambient air after drying should be kept below 30–60 min when relative humidity exceeds 60%. Melt temperature during injection molding is normally held between 230°C and 260°C; sustained melt temperatures above 270°C can degrade PA12. Mold temperature between 80°C and 120°C is used to control crystallinity and surface finish. The upper mold-temperature limit is constrained by cycle time and part ejection, not by PA12 degradation.
Long-glass compounds require low-shear melt-path design. A general-purpose screw with a compression ratio between 1.8:1 and 2.5:1, constant-taper transition, and no high-shear mixing section is used. Free-flow check valves with tip clearances above 2 mm, nozzle bores of at least 4 mm, and runner diameters above 6 mm for multi-cavity tools reduce fiber attrition. Back pressure is kept between 0.3 MPa and 0.7 MPa, and screw surface speed is often limited to 0.2–0.4 m/s. Hot-runner systems with internally heated torpedo tips cause exaggerated fiber breakage; externally heated manifolds with open nozzle tips and no restrictive needle shutoffs are preferred. Melt viscosity is higher than short-glass equivalents at the same shear rate; capillary rheometry per ISO 11443:2021 should be used to define the processing window for complex hot-runner layouts.
Shrinkage is anisotropic in long-fiber compounds. Mold shrinkage in the flow direction is typically 0.1–0.3%, while transverse shrinkage ranges from 0.4% to 0.7%. Tooling designed for short-glass PA12 or unfilled PA12 should not be transferred directly to LGF40-PA12 without flow simulation and shrinkage correction. Gates below 1.5 mm produce fiber-rich surfaces and jetting; gates of 2.5 mm or larger result in more uniform fiber distribution.
Against short-glass PA66 at the same nominal 40% glass fraction, LGF40-PA12 offers lower density, lower saturation moisture uptake, and higher low-temperature impact energy, but lower heat deflection temperature and lower dry tensile strength. PA66 SF40 compounds typically show dry density between 1.44 g/cm³ and 1.50 g/cm³ and HDT at 1.8 MPa above 240°C, whereas LGF40-PA12 remains below 175°C. The selection therefore depends on thermal load. Continuous service temperature for LGF40-PA12 is generally limited to approximately 120°C, with intermittent peaks below 150°C unless long-term heat aging data per ISO 188 indicates otherwise.
| Property | LGF40-PA12 | PA12 short glass 40% | PA66 short glass 40% |
|---|---|---|---|
| Density | 1.30–1.35 g/cm³ | 1.30–1.35 g/cm³ | 1.44–1.50 g/cm³ |
| Tensile modulus ISO 527 | 9,000–11,000 MPa | 9,500–11,500 MPa | 11,000–13,000 MPa |
| Notched Charpy impact 23°C ISO 179 | 25–40 kJ/m² | 10–15 kJ/m² | 8–13 kJ/m² |
| HDT 1.8 MPa ISO 75 | 160–175°C | 160–175°C | 240–255°C |
| Water absorption at saturation ISO 62 | 1.2–1.6% | 1.2–1.6% | 4.5–6.5% |
Replacement of die-cast aluminum is possible only when the design is reworked to accommodate anisotropy. Aluminum is isotropic and has no significant moisture or weld-line sensitivity; LGF40-PA12 is anisotropic and its local modulus depends on fiber orientation. Flow simulation with fiber-orientation modules in Moldflow or Moldex3D is required to move weld lines away from high-stress zones and to align fiber orientation with principal stress paths. Injection pressures for structural parts often reach 80–120 MPa, and machines with clamp force above 100 t are common depending on projected area. Rib thickness, boss geometry, and impact-absorbing features must be redesigned because density is lower but stiffness is also lower than aluminum.
Within the Complet PA12 long-fiber family, a step from 30% to 40% glass raises tensile modulus and HDT but increases melt viscosity and reduces notched impact. At 50% glass loading, flow length decreases further and tool and barrel wear accelerate. LGF40-PA12 is therefore positioned as a stiffness-toughness-flow compromise for long-fiber PA12 applications. If the part is stiffness-dominated and low-temperature impact is not critical, a short-glass PA12 grade may suffice; if weld lines or sub-zero impact are present, the long-glass grade is preferred.
PA12 offers useful resistance to aliphatic hydrocarbons, oils, greases, salt solutions, and many industrial fluids, but it is not intended for continuous contact with concentrated mineral acids, strong oxidizing agents, or boiling water. Chemical compatibility tests should follow ISO 175:2010 using the actual service fluid at the maximum service temperature. PA12 is plasticized by polar low-molecular-weight species; ethanol-blended fuels and aggressive brake fluids require validation. The long-glass reinforcement does not alter the base polymer chemical resistance, but exposed glass fibers at part surfaces may act as wicking paths if the surface is not resin-rich.
Regulatory statements for a specific PlastiComp SKU should be verified against the supplier certificate. General PA12 base resin is commonly assessed under REACH and RoHS Directive 2011/65/EU, but colorants, heat stabilizers, and processing aids can affect the final classification. Food-contact compliance, when required, must be separately evaluated under the applicable national regulation such as FDA 21 CFR or Commission Regulation (EU) No 10/2011. Incompatibility with high-acid-number flame retardant masterbatches or unknown recycled PA streams should be reviewed because acidic species can degrade PA12 at melt processing temperatures.
Production-scale experience with long-fiber PA12 in pneumatic valve bodies and industrial housings indicates that fiber-rich surfaces and gate blush occur when gate diameter falls below 1.5 mm; increasing gate diameter to 2.5 mm or greater reduces jetting and yields more uniform fiber distribution. Internally heated hot-runner torpedo tips produce pronounced fiber attrition, whereas externally heated manifolds with open nozzles retain longer fibers. These tooling and processing factors, rather than the nominal glass content alone, determine whether the long-glass advantage appears in the molded part.