| HS Code | 908458 |
| Density | 1.23 g/cm³ |
| Tensile Strength Ultimate | 110 MPa |
| Elongation At Break | 2.0% |
| Flexural Modulus | 5.5 GPa |
| Flexural Strength | 160 MPa |
| Izod Impact Strength Notched | 75 J/m |
| Heat Deflection Temperature 1 8 Mpa | 170°C |
| Melting Point | 178°C |
| Water Absorption 24h | 0.25% |
| Mold Shrinkage | 0.003 mm/mm |
| Volume Resistivity | 1 x 10^14 ohm·cm |
| Dielectric Strength | 20 kV/mm |
As an accredited Ashley Polymers Ashlene D925LH-30G Nylon 12, 30% Glass Reinforced factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 25 kg net in polyethylene-lined kraft bags, palletized and stretch-wrapped, ensuring moisture protection and safe handling of nylon 12 compound. |
| Container Loading (20′ FCL) | Ashley Polymers Ashlene D925LH-30G in 20′ FCL: load palletized bags/cartons securely, evenly distributed, ensuring stability and protection during transit. |
| Shipping | Ship as non-hazardous plastic pellets in sealed moisture-resistant bags or drums. Avoid exposure to excessive heat, dust, and moisture. Keep upright, dry, and protected from damage. Standard freight handling applies; no special hazardous material declaration required for transportation under normal conditions. |
| Storage | Store in a cool, dry, well-ventilated area away from heat, open flames, and direct sunlight. Keep containers tightly sealed to prevent moisture absorption, which can affect processing. Protect pellets from physical damage and contamination. Avoid dust accumulation; use appropriate grounding. Maintain temperatures below 50°C (122°F) and follow manufacturer’s shelf-life recommendations. |
| Shelf Life | Store in sealed, dry containers away from moisture. Shelf life is typically two years from manufacture date under proper conditions. |
For gasoline and ethanol-blended fuel vapor line connectors, injection molding from Ashlene D925LH-30G takes advantage of the PA12 matrix water absorption near 0.25% in 24 h under ASTM D570 and the 30% glass fiber loading that reduces creep under radial clamp load. In low-permeation fuel quick-connect bodies, pre-drying in a desiccant dryer with a dew point of −40 °C to a residual moisture below 0.10% is mandatory; residual moisture above 0.15% at the feed throat causes hydrolysis during plastication, evidenced by silver streaks and a reduction in notched Izod impact below 6 kJ/m² when tested according to ISO 180/A. Barrel temperatures are profiled from 230 °C at the feed zone to 265 °C at the nozzle, with a maximum melt residence time of 10 min and screw rotation below 150 rpm to limit fiber attrition. A valve gate placed on the barb axis rather than on the side wall directs glass-fiber orientation along the pull-off direction, preventing a weld line at the retainer annulus where fuel pressure fluctuations of 0.5 MPa to 0.8 MPa occur during engine start-stop cycles. Mold temperature is maintained between 80 °C and 100 °C; the upper value reduces post-mold shrinkage to approximately 0.2% in the flow direction and 0.7% transverse, which is critical for maintaining connector-to-nylon tube interference fit after thermal aging at 125 °C for 1,000 h. Finished connectors are validated to SAE J2044 for quick-connect couplings in liquid fuel and vapor/emission systems, with additional leak testing at 0.35 MPa and pull-off force verification after fuel immersion in CE10 and CE85 at 55 °C for 96 h. The glass transition of PA12 near 45 °C to 50 °C means torque retention under the spring retainer at 85 °C depends on glass-fiber network density rather than matrix stiffness alone; stress relaxation occurs in the first 24 h of clamping but stabilizes after an initial 5% to 7% load drop. End products include fuel line quick-connector bodies, vapor canister retainer clips, and fuel rail spacers.
At working pressures between 1.0 MPa and 1.6 MPa, industrial pneumatic distribution manifolds molded from Ashlene D925LH-30G operate in compressed-air networks where the polymer is exposed to residual compressor oil and water condensate meeting ISO 8573-1:2010 class 4 for water and class 5 for oil in non-critical plant air. The limiting variable governing burst pressure is not the tensile strength of the compound but the strength of the weld line created when separated melt fronts merge around a core pin or threaded insert. With 30% glass reinforcement, fibers orient parallel to the flow front at the weld plane; the resulting weld-line depth of 0.3 mm to 0.5 mm can reduce burst pressure by 20% to 30% compared with a weld-free plaque molded at the same conditions. To move the weld line outside the pressure envelope, the part is gated from the manifold hub center with a single submarine gate of 1.5 mm diameter, not from the port end. Multi-cavity hot-runner systems use sequential valve-gate opening with a delay of 0.8 s to 1.2 s so that flow fronts meet behind the main bore wall, not at the thread root where hoop stress concentrates. Melt temperature is held between 255 °C and 270 °C, mold temperature at 90 °C to 100 °C, and screw back pressure at 5 MPa to 8 MPa to disperse glass without excessive fiber length loss below 0.25 mm. A significant processing threshold exists: mold temperatures below 60 °C produce an amorphous skin that softens at 85 °C and permits creep of the threaded boss under sustained internal pressure of 1.2 MPa, while mold temperatures above 110 °C extend cycle time without a measurable additional burst strength and can cause PA12 to stick to uncoated cores. After molding, burst testing per ISO 14743:2004 for pneumatic fluid power push-in connectors is commonly applied, with acceptance at four times rated working pressure. End products include manifold blocks for directional control valves, filter-regulator-lubricator bodies, and push-to-connect air distribution modules.
For cable tray fasteners and terminal board support brackets molded from Ashlene D925LH-30G, pollution degree 3 environments under IEC 60664-1 impose tracking resistance and torque retention requirements where occasional condensation can produce conductive deposits. The comparative tracking index of this glass-filled PA12 is reported above 500 V under IEC 60112 solution A, which places it in material group II under IEC 60664-1 unless the specific lot tests above 600 V; creepage distance calculations must therefore use material group II tables rather than material group I. Torque retention after heat aging at 85 °C for 1,000 h is governed by the glass-fiber network, and a molded-in brass insert of M6 size is specified rather than cutting threads directly into the glass-filled polymer because thread roots create glass-fiber discontinuities that act as crack initiation sites under vibration. If direct thread forming is unavoidable, the boss hole diameter is kept at 0.7 to 0.8 times the screw major diameter and the engagement length is limited to 2.0 to 2.5 times the screw diameter to prevent radial cracking at installation torque above 4 N·m. The molding process uses a low-compression screw with an L/D ratio of 22:1 and a check ring designed for abrasive compounds; screw replacement intervals are shortened to 2,000 h to 3,000 h when running 30% glass-filled resin because barrel wear at the feed section increases clearance beyond 0.2 mm. Mold temperature is set at 80 °C to 90 °C; the lower value reduces flash but lowers surface resin thickness, producing glass-fiber protrusion at the surface that can reduce comparative tracking index by 100 V or more. UL 94 flame classification for this product class is typically HB at 0.75 mm; applications requiring V-0 must not use this grade unless an external flame-retardant package is specified and validated on actual molded parts. End products include heavy-duty cable tray fasteners, DIN rail adapter blocks, and terminal board mounting feet for electrical enclosures.
| Application | Standard reference | Test condition | Acceptance criterion |
|---|---|---|---|
| Fuel line quick connectors | SAE J2044 | Leakage after CE10 immersion at 55 °C for 96 h | No leak at 0.35 MPa |
| Pneumatic manifolds | ISO 14743:2004 | Burst test on molded assembly | Burst ≥ 4× rated working pressure |
| Cable tray fasteners | IEC 60112, IEC 60664-1 | Tracking resistance on molded surface | CTI above 500 V, material group II |
| Ski touring binding housings | ISO 13992 | Cyclic torsion at −20 °C | Release torque stability after 500,000 cycles |
| Reusable surgical handles | ISO 17665-1:2006 | Steam sterilization at 134 °C | No cracking after 500 cycles |
Across the −30 °C to +50 °C service window, structural housings for ski touring bindings are injection molded from Ashlene D925LH-30G where the mechanical load path includes heel pins, toe wings, and release cams. Notched Izod impact values for this class of 30% glass-filled PA12 remain above 8 kJ/m² at −30 °C when the molded skin is resin-rich; if the melt temperature falls below 240 °C or the injection speed exceeds 150 mm/s, glass fibers migrate to the surface and the ductile-to-brittle transition shifts upward by 10 °C to 15 °C, causing brittle failure at the heel pin retention boss. The tool is designed with a fan gate of 2.5 mm thickness at the non-cosmetic rear face and with an overflow well at the toe wing tip to vent trapped air; gas entrapment at a melt front advancing from the rear gear rack to the front lobed cam produces microvoids that reduce fatigue life under cyclic torsion of 20 N·m to 40 N·m applied for 500,000 cycles. Load-bearing release components are tested to ISO 13992 for touring ski bindings, which requires torque release consistency after simulated service loading and environmental exposure at −20 °C and +50 °C; the glass-filled PA12 housing is not a substitute for metallic release springs but transfers load without creep at the binding mounting plane. A post-mold moisture treatment at 50% RH for 48 h is specified before assembly because dry-as-molded PA12 exhibits notched Izod values 2 kJ/m² to 3 kJ/m² lower at sub-zero temperature, and the moisture uptake restores ductility without shifting screw retention below 3 N·m. End products include heel housings, toe wing supports, and brake retention plates.
Because the lower amide group density of PA12 reduces equilibrium moisture uptake compared with PA66, reusable surgical instrument handles and non-patient-contact mounting brackets molded from Ashlene D925LH-30G are selected for repeated steam sterilization at 134 °C in a vacuum steam sterilizer validated under ISO 17665-1:2006. A heat-stabilized formulation is mandatory for this exposure; unstabilized 30% glass-filled PA12 develops surface microcracks at fiber end points after approximately 200 autoclave cycles, and the cracks propagate under repeated clamp loading of 15 N to 25 N applied to instrument handle grips. The molding process uses a reverse temperature profile with feed zone at 240 °C, compression zone at 250 °C, metering zone at 245 °C, and nozzle at 255 °C; the lower metering temperature reduces shear heating and preserves molecular weight, while the mold is held at 100 °C to maximize crystallinity and reduce post-sterilization dimensional shift. Parts are annealed after molding at 120 °C for 2 h in a nitrogen-purged oven to reduce molded-in stress below 5 MPa as evaluated by a solvent stress-crack test in n-propyl acetate; unannealed parts show dimensional movement of 0.3% to 0.5% after the first three autoclave cycles, which can compromise the snap-fit engagement of an instrument body. Biological evaluation of the finished device is performed according to ISO 10993-1:2018, with cytotoxicity testing per ISO 10993-5 and sensitization testing per ISO 10993-10 because glass fibers at the surface can release silane coupling agents during repeated steam exposure. End products include reusable laparoscopic handle shells, surgical light positioning brackets, and equipment housing clamps that do not enter the sterile field.
In downhole and subsea electrical connector shells, clamp spacers, and cable protection end fittings molded from Ashlene D925LH-30G, the environment includes produced water, aliphatic hydrocarbons, and occasional sour gas containing up to 2.0 mol% H₂S at service temperatures not exceeding 60 °C. The 30% glass reinforcement increases tensile strength to a range of 100 MPa to 120 MPa under ISO 527-2 and flexural modulus to 5,000 MPa to 6,000 MPa under ISO 178, allowing the replacement of machined acetal or unfilled PA12 in clamp spacers subject to crush loads of 8 kN to 12 kN. The processing window is narrow because glass fiber distribution in thick sections above 6 mm leads to center-plane glass depletion and anisotropic shrinkage; the solution is sequential overmolding of a shorter glass-fiber cap layer over a structural core rather than increasing melt temperature, which only accelerates polymer degradation and increases volatiles. Pre-drying at 80 °C for 4 h to 6 h is required, and the hopper must be blanketed with dry air at −30 °C dew point to prevent moisture re-absorption above 0.08% during extended molding runs. Compliance with rapid gas decompression testing is material-specific; for polymer components in subsea clamp applications, testing may follow ISO 23936-2:2011 or operator-specific procedures that require 15 decompression cycles from 15 MPa to 0.1 MPa at 60 °C without blistering or a loss of more than 10% in tensile elongation. If the end fitting is intended for sour service in upstream oil and gas, the polymer qualification may additionally reference NORSOK M-710 for non-metallic sealing materials, although published data for this specific 30% glass-filled PA12 in sour-service subsea hardware is limited and component-specific validation is required. End products include ROV grabber clamp spacers, subsea electrical connector alignment shells, and cable bend restrictor end collars for topside use.
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Ashley Polymers Ashlene D925LH-30G is specified as a 30% glass-fiber-reinforced polyamide 12 injection-molding compound in which chopped glass fiber is dispersed in a semi-crystalline nylon 12 matrix. The grade is evaluated where the low equilibrium moisture uptake of nylon 12 must be maintained while tensile and flexural stiffness are raised above unfilled PA12. Under ISO 62:2008 water-absorption testing at 23°C and 50% RH, unfilled nylon 12 typically reaches 0.7–1.0% moisture, whereas PA66 may reach 2.3–2.8%; the glass phase in D925LH-30G displaces polymer mass and reduces absolute moisture gain. The compound also exhibits lower mold shrinkage and higher melt viscosity than the unreinforced base resin. Pre-drying to below 0.10% moisture is required because residual water hydrolyzes the amide backbone during melting and can produce surface splay.
Mechanical data for 30% glass-reinforced PA12 fall broadly into these bands: dry-as-molded tensile strength of 100–120 MPa under ISO 527-2:2012, flexural modulus of 4.5–6.0 GPa under ISO 178:2019, and notched Izod impact of 10–15 kJ/m² under ISO 180/A. For unfilled PA12 the same tests typically yield 45–55 MPa tensile strength, 1.2–1.5 GPa flexural modulus, and lower elongation at break. The values shift when specimens are conditioned to equilibrium moisture; tensile strength can decline by 10–20% relative to dry-as-molded data because water plasticizes the amide phase. For finite-element input, lot-specific certificates should replace generic averages.
In a molded part with flow-induced fiber orientation, moisture-driven growth is anisotropic. Because the skin orients fibers in the flow direction, the part expands more transversely than along the flow when moisture content increases from dry to equilibrium. In a 50% RH service environment, a 100 mm transverse dimension can grow 0.1–0.2% relative to the flow direction. This amount is small compared with PA66-GF30, which may show 0.4–0.7% growth under the same conditioning. The practical consequence is that a pneumatic fitting with an engagement diameter of 20 mm can retain tighter clearance control across seasonal humidity shifts.
The glass fibers align partially with the melt-flow direction during filling. In the flow direction, linear mold shrinkage under ISO 294-4 is held to 0.2–0.5%, while transverse shrinkage remains at 0.4–0.7%. For unfilled PA12, shrinkage is more isotropic and typically falls between 0.7% and 1.2%. The same flow-induced orientation lowers the coefficient of linear thermal expansion in the flow direction to 30–40 ppm/K per ISO 11359-2, compared with 120–150 ppm/K for neat PA12. When two melt fronts meet, the fibers do not cross the weld plane. Notched impact strength measured with ISO 180/A specimens can be 10–15 kJ/m² in a single-gated molding but may fall to less than half that value at a weld line. Gate location should place weld lines away from pressure-loaded hoop paths or snap-fit roots.
Drying is performed in a desiccant dryer with a supply-air dew point at or below -30°C. A hopper residence time of 4–6 h at 80°C is suitable for granule moisture reduction to 0.10%; if ambient relative humidity exceeds 60%, extension to 8 h or use of a closed hopper loader with nitrogen purge reduces moisture regain. Residual moisture can be checked by ISO 15512:2008 before startup. The melt cylinder on a reciprocating-screw injection machine should be profiled from approximately 220°C in the feed zone to 250°C at the nozzle. A mold temperature between 40°C and 80°C is commonly used; lower mold temperatures can freeze an unfilled skin before fiber-containing core layers orient, while higher mold temperatures improve crystallinity at the expense of cycle time. Melt residence time above 10 min should be avoided because the PA12 backbone can undergo thermal-oxidative chain scission even with heat stabilization. Screw back pressure of 0.3–0.7 MPa and screw surface speed not exceeding 0.2 m/s are typical starting points for limiting fiber attrition; injection velocity is set by filling-pressure curves rather than by fixed timer values.
Regrind can be incorporated at proportions up to 25% in some production environments, but each pass reduces average glass-fiber length and narrows the tensile-strength distribution. Fiber-length reduction from granulating and remelting can lower tensile strength by 5–10% at 25% regrind content when compared with virgin material under ISO 527-2; published data for this specific formulation are limited. If regrind is used, the ratio should be held constant to prevent mechanical-property batch-to-batch variation.
Production-scale molding of glass-reinforced PA12 requires wear-resistant screw and barrel surfaces because E-glass fibers are abrasive. Nitrided or bimetallic barrels and hardened check rings are specified to avoid screw recovery time drift. When check-ring seats wear, cushion position becomes unstable and shot-weight variance can exceed 0.5% in thin-wall connectors. Screw clearance against the barrel inner diameter should be measured periodically because increased clearance reduces melt temperature control and increases fiber attrition.
| Property | Test method | Unfilled PA12 | PA12 GF30 | PA66 GF30 |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.01–1.03 g/cm³ | 1.22–1.25 g/cm³ | 1.35–1.40 g/cm³ |
| Tensile strength, dry | ISO 527-2:2012 | 45–55 MPa | 100–120 MPa | 150–180 MPa |
| Flexural modulus | ISO 178:2019 | 1.2–1.5 GPa | 4.5–6.0 GPa | 7.0–9.0 GPa |
| Water absorption, 24 h | ISO 62:2008 | 0.2–0.3% | 0.1–0.2% | 0.7–0.9% |
| CLTE, flow direction | ISO 11359-2 | 120–150 ppm/K | 30–40 ppm/K | 25–35 ppm/K |
| Deflection temperature, 1.8 MPa | ISO 75-2 | 50–60°C | 150–170°C | 230–250°C |
Values in the table are representative published ranges for the material class; the specific lot certificate for Ashlene D925LH-30G governs final design input.
Nylon 12 is less susceptible than PA66 to stress cracking by zinc chloride solutions, which are produced when road salt contacts galvanized surfaces. This characteristic is relevant for fuel connectors, quick-connect fittings, and underbody clips exposed to winter deicing salts. Glass reinforcement lowers the elongation necessary to initiate a crack, but the PA12 matrix still provides a wider processing and service window than PA66 in zinc chloride environments. At low temperatures, PA12 retains ductility at -40°C more reliably than many PA66 compounds; however, sharp weld lines and notches can shift failure to brittle mode even in PA12. For parts subjected to subzero impact, testing should be carried out on molded plaques or actual components rather than relying only on ISO 180/A laboratory data.
The density of D925LH-30G is lower than PA66-GF30: 1.22–1.25 g/cm³ compared with 1.35–1.40 g/cm³ for a 30% glass-reinforced PA66 compound under ISO 1183-1:2019. This difference can reduce part mass by approximately 10% on identical geometry. Dry tensile strength of PA66-GF30 is typically higher, but moisture absorption narrows the difference after conditioning. Deflection temperature under 1.8 MPa load for PA12-GF30 is generally between 150°C and 170°C, while PA66-GF30 is often above 230°C; therefore D925LH-30G is not a direct substitute in applications requiring continuous high-temperature retention. Compared with PBT-GF30, PA12-GF30 typically provides higher elongation at break and better zinc chloride resistance, while PBT-GF30 often provides higher flexural modulus and lower moisture uptake under ISO 62:2008. Each substitution should be verified by comparative molding trials rather than by data-sheet equivalence.
Within the Ashlene polyamide 12 portfolio, the 30% glass-reinforced D925LH-30G differs from unfilled and impact-modified grades primarily in tensile modulus, shrinkage, and flow length. Unfilled PA12 is often selected for flexible tube and clip applications where high elongation is required; D925LH-30G is selected when the same chemical resistance must be retained with higher hoop strength. Impact-modified PA12 grades may show higher notched impact at low temperature but lower tensile strength and lower deflection temperature under load. The specific “LH” markings should be confirmed against the supplier’s product documentation because lubricant and heat-stabilization packages influence melt stability and mold deposit rates.
Sustained contact with strong mineral acids, phenolic compounds, and certain chlorinated solvents can attack nylon 12. Glass reinforcement does not provide a barrier function; it can accelerate wicking along fiber-matrix interfaces if the polymer matrix is chemically degraded. Continuous exposure to hot aqueous ethylene-glycol mixtures above 80°C is outside the conservative service window for pressurized glass-reinforced PA12 components because hydrolysis can reduce tensile strength after 1,000–3,000 h depending on temperature and glycol concentration. Fuel immersion testing is often performed in ASTM Reference Fuel C at 60°C for 500 h; published data for D925LH-30G under this exact condition are limited, so component-level validation is required for fuel-contact applications.
For continuously loaded parts at 23°C, glass reinforcement increases creep resistance compared with unfilled PA12, but the compound remains a short-glass thermoplastic, not a structural metal substitute. Creep testing under ISO 899-1:2003 should be performed on specimens molded with the same gate orientation as production parts because fiber alignment changes the creep response. Published creep data for this exact grade are limited, so design stress should be derived from orientation-matched testing rather than from short-term tensile data.
Components molded from 30% glass-filled PA12 are used in pneumatic quick-connect fittings evaluated under ISO 14743 and in automotive fuel-system quick connectors evaluated under SAE J2044. These are assembly-level tests; material selection is necessary but not sufficient for compliance. For fuel-contact parts, long-term exposure to fuel, heat aging, and road-salt solutions are combined in qualification matrices. Published data for D925LH-30G in these exact assembly configurations are limited, so prototype testing on production tooling is required. For pressure-containing components with wall stock of 2–3 mm, short-shot-based fill studies should be used to establish the injection speed that fills the cavity without jetting. The projected area clamp-force requirement is often estimated at 3–5 kN/cm² for reinforced semi-crystalline materials, but thin-wall parts and glass-induced viscosity may require a higher figure. Tool deformation must be checked because the higher modulus of the glass-filled melt does not prevent flash if clamp force is insufficient.
Incoming QC for this compound should include melt flow rate under ISO 1133-1:2022, ash content under ISO 3451-1:2019, and moisture content under ISO 15512:2008. A glass content of 30% by weight corresponds to an ash content near 30% after combustion; variation beyond ±2% can shift tensile strength and mold shrinkage. Melt flow rate is process-dependent and not a specification in itself, but batch-to-batch drift outside a ±10% band relative to the supplier reference can indicate fiber-length or molecular-weight changes.
| Area | Reference | Typical requirement | Verification |
|---|---|---|---|
| Moisture before molding | ISO 15512:2008 | <0.10% | Lot-specific |
| Flammability at 1.5 mm | IEC 60695-11-10 | HB typical | Component test |
| RoHS restrictions | EU 2011/65/EU | ≤0.1% homogeneous material for lead, mercury, hexavalent chromium, PBB, PBDE | Supplier declaration |
| REACH SVHC | EC 1907/2006 | <0.1% w/w per SVHC | Supplier statement |
| Fuel-system component | SAE J2044 | Assembly-level pull-off, pressure, fuel exposure | Production-tool validation |
| Pneumatic fitting | ISO 14743 | Leakage and burst at specified pressure | Assembly-level |
Operational boundaries must be defined by specific part geometry and chemical environment. D925LH-30G should not be specified as a direct replacement for PA66-GF30 in applications that see continuous use above 180°C because the PA12 matrix softens well below that temperature. It should not be used with strong mineral acids, phenols, or oxidizing agents that attack the amide linkage. If part surfaces are exposed to ultraviolet radiation for outdoor service, a UV-stabilized formulation or coating may be required; the base glass-reinforced PA12 grade is not inherently UV-stable. Published data for this specific grade under exterior weathering are limited.