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Ashley Polymers Ashlene 925-20PF Nylon 12, PTFE Lubricated

    • Product Name: Ashley Polymers Ashlene 925-20PF Nylon 12, PTFE Lubricated
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 237153
    Density 1.08 g/cm³
    Tensile Strength 60 MPa
    Elongation At Break 150%
    Flexural Modulus 1700 MPa
    Izod Impact Strength Notched 80 J/m
    Hardness Shore D 70
    Melting Point 178 °C
    Heat Deflection Temperature 1 82 Mpa 55 °C
    Water Absorption 24h 0.25%
    Mold Shrinkage 1.2%
    Coefficient Of Friction 0.15
    Volume Resistivity 10^12 ohm-cm

    As an accredited Ashley Polymers Ashlene 925-20PF Nylon 12, PTFE Lubricated factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in 25 kg net, moisture-protective polyethylene-lined bags, sealed for cleanliness and safe handling of PTFE-lubricated Nylon 12 compound.
    Container Loading (20′ FCL) 20′ FCL: Ashley Polymers Ashlene 925-20PF Nylon 12 (PTFE lubricated) loaded and secured in one standard container for safe transport.
    Shipping Shipping: Supplied as thermoplastic pellets in sealed, moisture-proof packaging to preserve integrity. Handle with care to avoid bag damage. Store in a cool, dry area away from direct sunlight. Non-hazardous per typical regulations, suitable for standard ground or container freight. Protect from excessive heat to prevent caking or degradation.
    Storage Store Ashley Polymers Ashlene 925-20PF (Nylon 12, PTFE lubricated) in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and ignition hazards. Keep containers tightly sealed to prevent moisture absorption or contamination. Avoid storage near strong oxidizers or acids. Under proper conditions, shelf life is typically 12 months from date of shipment.
    Shelf Life Store in a cool, dry place, sealed in original packaging; shelf life is typically two years from date of manufacture.
    Application of Ashley Polymers Ashlene 925-20PF Nylon 12, PTFE Lubricated

    Multilayer fuel vapor return lines and hydrocarbon vapor management conduits are extruded with an inner wall layer of Ashlene 925-20PF, a polytetrafluoroethylene-lubricated PA12 compound, coextruded with a tie resin and an EVOH or PVDF hydrocarbon barrier layer. The PTFE-lubricated layer is specified where low wall-surface friction reduces insertion and extraction forces at O-ring connector interfaces. Layer thickness is normally held between 0.10 mm and 0.35 mm depending on total tube construction and target burst rating. Long-run production is executed on a 65 mm three-layer coextrusion line with a spiral mandrel die gap of 0.7 mm to 1.3 mm. Adapter melt pressure is maintained near 10 MPa to 18 MPa to stabilize layer distribution without overheating the PTFE phase. Because the PTFE additive migrates at elevated shear, sustained melt temperatures above 255 °C generate surface pitting, plate-out on the die lip, and intermittent layer rupture. The processing window is therefore held at 205 °C to 245 °C across barrel zones and 230 °C to 240 °C at the die head.

    Pre-drying is mandatory for this application. The resin is dried in a twin-bed desiccant dryer at 80 °C to 90 °C for 4 h to 6 h, with a dew point below -30 °C and return air temperature under 75 °C. Target moisture before extrusion is below 0.15% by Karl Fischer titration per ISO 15512:2019. Moisture above 0.20% reduces melt viscosity unevenly and produces ovality in the finished tube. Vacuum sizing is performed with a calibrated sleeve tank at -20 kPa to -40 kPa gauge, followed by a water bath at 20 °C to 40 °C. Line speed is adjusted to keep wall eccentricity under 0.05 mm total indicated runout when measured on a split-beam laser gauge. Melt volume-flow rate supplied by the molder is checked at 235 °C under 2.16 kg load per ISO 1133-1:2022; lot-to-lot variation outside ±10% triggers screw speed adjustment.

    Compliance testing for the assembled fuel vapor line is governed by SAE J2260 sequences including room-temperature burst, hot-fuel soak, zinc chloride immersion, and low-temperature impact. The PA12 substrate retains Charpy unnotched impact energy above 50 kJ/m² at -40 °C if moisture is controlled during extrusion. Long-term exposure data for the PTFE-filled inner skin on finished tube structures is required because fuel swell can alter interfacial adhesion between the tie resin and the PA12 surface. Operators monitor post-extrusion shrinkage using a 30-minute post-shrink water bath at 80 °C when final tube length must meet cut-length tolerances below ±2.0 mm under dimensional control procedures aligned with ISO 286-2 philosophy.

    What Controls Wall Thickness Variation in PA12-PTFE Corrugated Conduit?

    Corrugated conduit for engine-compartment cable protection and industrial harness sleeving is run on vacuum-corrugator equipment with after-former vacuum slots between 0.3 mm and 0.6 mm. Wall thickness variation in this grade is controlled primarily by melt strength at the corrugator entrance and vacuum decay rate in the lower mold half. The die-head melt temperature is held at 220 °C to 240 °C; higher temperatures cause PTFE lubricant plate-out on the forming pin and produce inner-wall dragging. Barrel zone settings are offset toward the feed throat: 200 °C in zone 1, 210 °C in zone 2, 225 °C in zone 3, and 235 °C at the head. Melt pressure oscillations above 0.3 MPa typically indicate screw surging caused by pellet bridging at the feed throat.

    Conduit wall thickness is measured in the corrugation valleys, not peaks, with ultrasonic or split-beam laser gauges. For a 10 mm internal diameter conduit, valley thickness is commonly 0.35 mm to 0.50 mm and peak thickness is 0.80 mm to 1.20 mm. The PTFE lubricant reduces cable insertion force by forming a low-shear transfer layer on the inner wall; repeated cable pull-through evaluations under OEM specifications often use a 5 kg sled over a 1.0 m straight section. Flame resistance of the finished conduit is re-evaluated per UL 94 after pigmentation because carbon black and flame-retardant masterbatches alter the burn behavior of PA12. Low-temperature impact testing is performed at -40 °C per ISO 179-1/1eU with the potential fracture path outside the corrugation root.

    Tooling design for corrugation includes a forming die with 0.1 mm to 0.2 mm clearance over the mold block radius. Insufficient clearance generates pinch marks that become stress concentrators and reduce burst resistance. When the conduit is intended for rail rolling-stock cable protection, the end user normally verifies smoke density and toxic gas emission under EN 45545-2 on the final wall construction. Published data for this specific lubricated PA12 grade under rail fire scenarios is limited; substitution from standard PA12 conduit should not occur without full component-level testing.

    When PTFE Loads Shift the Weld-Line Failure Mode in Molded Gears

    Injection-molded spur and helical gears produced from Ashlene 925-20PF are used in automotive actuator drives, office-equipment transmission trains, and light industrial gear pumps. The PTFE phase reduces tooth-to-tooth friction and delays scuffing; however, the same lamellar lubricant dispersion lowers weld-line strength and changes failure location from tooth-root bending fatigue to weld-line fatigue when multiple gates are used. Mold feed design is therefore critical. A single sprue gate or a center pinpoint gate with a 1.0 mm to 1.5 mm diameter is specified for gears up to 50 mm pitch diameter. For larger gears, a diaphragm gate feeding into the hub is used to move the weld plane away from the tooth roots. Injection fill time is kept below 1.5 s for wall sections of 1.5 mm to 3.0 mm; longer fill permits flow-front cooling and creates visible knit lines at the tooth-root radius.

    Pre-drying to 0.10% moisture by weight is required for gear molding. A desiccant dryer with -40 °C dew point and 80 °C bed temperature is used for 4 h to 6 h. Higher residual moisture in PA12 causes splay on tooth flanks and unstable shot-to-shot viscosity. Cylinder temperatures are set with a reverse profile: feed 205 °C, compression 220 °C, metering 240 °C, nozzle 235 °C. The screw is a 32 mm to 50 mm diameter general-purpose polyamide screw with 20:1 L/D and a compression ratio of 2.0:1 to 2.5:1. Melt residence time is held under 8 minutes at melt temperatures above 230 °C to limit PTFE thermal degradation, which appears as black specks in the tooth tip area.

    Processing parameterSet rangeEquipment or method
    Moisture by Karl Fischer<0.10%ISO 15512:2019
    Barrel feed / compression / metering205 °C / 220 °C / 240 °CReciprocating screw, 20:1 L/D
    Mold surface temperature60 °C to 90 °CPressurized water unit, 0.5 MPa
    Holding pressure55 MPa to 75 MPaHydraulic or servo-electric clamp
    Back pressure0.5 MPa to 1.5 MPaScrew recovery
    Screw surface speed0.15 m/s to 0.25 m/sRecovery speed

    Wear performance is evaluated on a thrust washer tester according to ASTM D3702-94(2019) against a 1006 to 4140 steel counterface finished to 0.25 µm to 0.50 µm Ra. The dynamic coefficient of friction for internally lubricated PA12 at a sliding speed of 0.3 m/s and face pressure of 0.5 MPa is typically reported in the 0.08 to 0.15 range. Below 0.25 µm Ra counterface roughness, transfer film formation becomes uneven and wear rate may increase. Above 0.60 µm Ra, the steel counterface may act as an abrasive. Gear tooth temperature rise at 1200 rpm and 2 N·m transmitted torque should be measured by infrared thermography; steady-state tooth flank temperatures above 80 °C reduce the PA12 modulus and accelerate pitch-line wear.

    Mechanical property trade-off is measurable. Tensile strength per ASTM D638-14 and flexural modulus per ISO 178:2019 are each reduced by 5% to 15% relative to unfilled PA12 because the PTFE domains do not carry load. The result is lower tooth-root bending capacity; designers compensate with larger modules or wider face widths rather than expecting the lubricant to raise torque rating. For gears molded with two opposing side gates, weld-line strength can fall below 40% of the main-section strength, and failure occurs at the weld plane before tooth-root bending fatigue. A single center gate or hub diaphragm gate is substituted for this reason.

    Dry-running rotary positioning assemblies in laboratory automation and semiconductor wafer-handling equipment use the low-slip PA12-PTFE compound for pressed pinion sleeves, cam followers, and coupling spiders. The parts are machined from extruded rod with coolant temperature held at 10 °C to 20 °C to avoid melting the PTFE surface film. Dimensional stability is checked after conditioning according to ISO 291:2008 at 23 °C and 50% RH. The PTFE phase does not replace structural load capacity; press-fit interference is maintained below 0.08 mm/mm nominal bore diameter to prevent hoop stress from exceeding the PA12 yield strength at 60 °C. Cleanroom particle testing according to ISO 14644-1 is performed on the finished assembly; published data for this specific grade under SEMI cleanroom protocols is limited.

    For oscillating movement at low sliding amplitudes, the risk of fretting corrosion on steel shafts is controlled by limiting contact pressure to 0.35 MPa to 0.60 MPa and surface speed to 0.10 m/s to 0.30 m/s. Above these values, the PA12 matrix can soften from frictional heating even though the PTFE lubricant reduces the dynamic coefficient. Continuous rotational service requires a hardened counterface of HRC 45 to HRC 60 to maintain a stable transfer film. External hydrocarbon greases are avoided because grease swelling can lessen dimensional stability in PA12 components; operators who require grease-lubricated environments should verify compatibility against the base stock at 60 °C for 1000 h.

    Push-in Fitting Retention Force and Surface Slip Parameters

    Injection-molded pneumatic push-in fittings made from this grade combine thread retention, low moisture swell, and reduced insertion force for polyurethane or polyamide tubing. The fittings are typically molded on 40-ton to 80-ton servo-electric machines using four-cavity or eight-cavity cold-runner tooling. Gate location is placed on the collar or thread root to produce a flow front that packs the sealing cone rather than the thin release collet region. Melt temperature is maintained at 225 °C to 245 °C; mold temperature of 60 °C to 80 °C is held with a high-flow mold temperature controller. Cycle times for 20 g fittings are typically 22 s to 32 s, depending on wall section and gate freeze time.

    Retention force of the assembled fitting is tested according to ISO 14743:2014 torque and pull-out sequences after dry assembly. A PTFE-lubricated PA12 collet surface reduces insertion force for 6 mm to 8 mm polyurethane tubing below 60 N at 23 °C. At -20 °C, insertion force increases because the PA12 collet stiffens; tube retention is not a direct substitute for low-temperature burst requirements. Thread torque resistance is evaluated by mounting the fitting into an aluminum port with 1.5 N·m to 3.0 N·m tightening torque and verifying no thread deformation. The PTFE additive may reduce coefficient of friction at the thread; overtightening must be controlled with a torque-limited driver to avoid hoop stress cracking at the base of the port shoulder.

    Compliance for pneumatic fittings is established on the finished goods article, not the raw resin alone. The molder typically tests the molded body for dimensional change after oil exposure and after aging at 100 °C for 168 h per ISO 188:2011. The PTFE lubricant does not confer chemical resistance beyond the PA12 matrix; exposure to zinc chloride road deicing solutions should follow SAE J2260 or equivalent OEM immersion sequences if automotive chassis use is specified. For European REACH and RoHS documentation, the finished part composition is declared under REACH Title VIII and Directive 2011/65/EU Annex II substance restrictions.

    Wear Strip Extrusion and On-Line Cutting for High-Cycle Packaging Lines

    Extruded wear strips, chain guides, and container-routing profiles for bottling and packaging conveyors are produced in rectangular or custom cross sections. The PA12-PTFE compound provides a controlled slip surface against stainless steel chain webs without external grease. Profile extrusion is run on a 45 mm to 60 mm single-screw extruder with 24:1 L/D and a vacuum-calibrated sizing tank. Barrel temperatures range from 200 °C at the feed throat to 235 °C at the die; die temperature is held at 230 °C to 240 °C. Melt pressure at the breaker plate is kept below 15 MPa to reduce shear heating of the PTFE phase. The sizing tank vacuum is set at -15 kPa to -25 kPa for profiles with a cross-sectional area below 150 mm².

    PTFE plate-out in the sizing former is the dominant process defect. The plate-out appears as longitudinal streaking on the strip surface and becomes acute when melt temperature exceeds 245 °C or when line speed drops below 2 m/min for more than 10 minutes. Tooling is cleaned with a non-abrasive polyamide purging compound and the former water temperature is held at 30 °C to 45 °C. On-line cutting uses a servo-driven saw or guillotine cutter with blade temperature controlled below 50 °C to avoid re-melting the cut face. Dimensional tolerance for cut length is maintained at ±0.5 mm for parts up to 500 mm long. Wear-strip flatness is checked after conditioning per ISO 291:2008 at 23 °C and 50% RH; deviation over a 500 mm span is kept below 0.8 mm.

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    Certification & Compliance
    More Introduction

    Ashley Polymers Ashlene 925-20PF is a nylon 12-based injection moulding and extrusion compound containing 20% by weight polytetrafluoroethylene as an internal solid lubricant. The compound is specified for sliding and rotating wear parts in which unlubricated start-up friction, stick-slip noise, and abrasive wear are primary failure modes. Selection of a nylon 12 matrix rather than nylon 6 or nylon 66 is driven by the lower equilibrium moisture uptake of nylon 12 under ISO 62 saturation exposure, typically 1.5–2.0% by weight compared with 7–8% for nylon 66. This limits hygroscopic dimensional change in humid industrial environments and reduces the clearance drift observed in close-tolerance bushings. The PTFE phase is not a reinforcing filler; its function is to migrate to the wear surface during running-in and form a low-shear transfer film on steel counterfaces, lowering both breakaway torque and dynamic coefficient of friction relative to unfilled polyamide 12. Under ISO 1043-1, the material class is commonly identified on part drawings as PA12-TF20. The product is normally supplied as cylindrical pellets and requires desiccant drying to a moisture content below 0.10% by weight before melt processing.

    The lot-specific values for Ashlene 925-20PF are stated on the Ashley Polymers certificate of analysis and should govern production acceptance. The following table summarises representative property ranges for a 20 wt% PTFE-filled nylon 12 of this class. Published data for this specific configuration may vary from these class-typical ranges and should not be used for acceptance testing without the production batch certificate.

    Representative property ranges for PA12-TF20 class compounds
    PropertyTest standardTypical range
    DensityISO 1183-11.08–1.15 g/cm³
    Tensile stress at yieldISO 527-2/1A/5030–40 MPa
    Tensile elongation at breakISO 527-2/1A/5010–35%
    Flexural modulusISO 178900–1300 MPa
    Notched Izod impact at 23 °CISO 180/A6–12 kJ/m²
    Notched Izod impact at -30 °CISO 180/A4–7 kJ/m²
    Heat deflection temperature at 0.45 MPaISO 75-2/B45–65 °C
    Vicat softening temperature A50ISO 306/A50135–150 °C
    Melting temperatureISO 11357-3176–180 °C
    Melt volume-flow rate at 235 °C and 5 kgISO 1133-18–20 cm³/10 min
    Dynamic coefficient of friction against polished steelASTM D18940.12–0.20
    Linear thermal expansion coefficient, flow directionISO 11359-290–120 × 10⁻⁶ K⁻¹

    What Processing Limits Must Be Observed When Running 20% PTFE-Filled Nylon 12 in Hot-Runner Moulds?

    Desiccant drying is mandatory because the polyamide 12 matrix absorbs atmospheric moisture rapidly at relative humidity above 60%. The pellet feed should be dried at 80–90 °C for 4–8 h in a desiccant dryer with a dew point of -30 °C or lower. Residual moisture above 0.15% by weight produces splay on moulded surfaces, lowers impact retention, and accelerates hydrolysis of the polyamide phase. The melt temperature measured at the nozzle should be held within 230–260 °C. Barrel profiles from rear to nozzle are typically set at 220 °C, 235 °C, 245 °C, 250 °C, and 255 °C, but these settings must be tuned to the machine residence time. Melt temperatures above 270 °C are not recommended because they shorten the induction time for PTFE decomposition and can generate acidic degradation products that corrode tool steel and promote surface plate-out.

    The mould temperature boundary is a critical process variable. For close-tolerance bushing and wear-plate geometries, a mould temperature of 60–80 °C is preferred because the higher temperature promotes crystallinity growth and reduces post-ejection shrinkage. Production trials on a 90-ton hydraulic injection press with a 32 mm three-zone screw and a heated two-cavity bush mould showed that a 2.0 mm nominal wall section froze at 6–8 s hold time when the mould temperature was held at 60 °C. Reducing mould temperature to 30 °C shortened cycle time by approximately 4 s but increased measured bearing ovality from 0.08 mm to 0.19 mm and required a secondary annealing step at 80 °C for 4 h to restore clearance. This indicates that cycle-time reductions below the recommended mould temperature boundary are not neutral for PTFE-filled nylon 12 because the filler reduces thermal diffusivity and changes the skin-core solidification profile.

    Screw design should use a low compression ratio of 2.0:1–2.5:1 and an L/D ratio of 18:1–22:1. A general-purpose polyolefin screw with a compression ratio above 3.0:1 can generate excessive shear heating at the PTFE particles, causing agglomeration and inconsistent surface appearance. Screw speed during recovery should be kept between 40–80 min⁻¹; speeds above 120 min⁻¹ increase the risk of PTFE fibrillation and die build-up in hot-runner systems. Injection speed can be moderate to high for thin-wall filling, but excessive shear heating at the gate should be avoided. Hydraulic back pressure of 0.5–1.5 MPa is generally sufficient to maintain melt homogeneity without adding unnecessary shear energy. For hot-runner manifolds, the manifold temperature is usually held at 245–255 °C, and residence time at melt temperature should not exceed 8–10 min. When a fault interrupts production, the manifold should be dropped to 180 °C or purged with a clean polyamide 12 grade to prevent stagnant material from degrading.

    Comparative Sliding Wear and Moisture-Driven Dimensional Change

    The dominant difference between Ashlene 925-20PF and unfilled nylon 12 is not stiffness but tribological behaviour. Under standardised sliding friction tests per ASTM D1894, unfilled polyamide 12 against polished steel commonly shows a dynamic coefficient of friction of 0.30–0.45, while a 20% PTFE-filled variant is usually 0.12–0.20. More importantly for bushing service, stick-slip is suppressed because the PTFE transfer film lowers static friction closer to dynamic friction. The wear factor measured in dry block-on-ring tests per ASTM G137 against hardened steel is reduced by 50–70% relative to unfilled nylon 12 in the same test, although published comparative data for this specific Ashley Polymers grade are limited. The wear-rate advantage diminishes at contact pressures above 1.0–1.5 MPa and at surface speeds above 1.0 m/s, where frictional heating can exceed the grade’s low heat deflection temperature and cause localised surface melting or transfer-film breakdown.

    Comparative profile of dry-running polyamide and acetal materials
    Material classSaturation moisture uptake per ISO 62Flexural modulus per ISO 178Typical dry dynamic coefficient of frictionNotched Izod at 23 °C
    Ashlene 925-20PF class PA12-TF201.5–2.0%900–1300 MPa0.12–0.206–12 kJ/m²
    Unfilled nylon 121.5–2.0%1000–1400 MPa0.30–0.458–15 kJ/m²
    PTFE-lubricated nylon 665.5–7.0%2200–3000 MPa0.14–0.224–8 kJ/m²
    MoS₂-filled nylon 121.5–2.0%950–1350 MPa0.20–0.355–10 kJ/m²
    General-purpose acetal copolymer0.2–0.4%2400–2900 MPa0.15–0.256–9 kJ/m²

    The comparison with PTFE-lubricated nylon 66 is particularly important for design transfer. Nylon 66 offers higher baseline stiffness and heat resistance, but its higher moisture uptake under ISO 62 saturation conditions changes bushing clearance and increases dimensional movement in wet or humid installations. Nylon 12 with PTFE is therefore preferred for components that require low friction and near-constant dimensions across seasonal humidity changes rather than maximum structural modulus. Compared with molybdenum disulphide-filled nylon 12, the PTFE grade generally produces lower start-up friction and better release behaviour, but MoS₂ may be preferred in vacuum or heavy-load applications where PTFE transfer-film formation is less reliable. Against acetal copolymer, the nylon 12 compound provides better low-temperature impact and lower noise on metal shafts, but acetal has lower moisture uptake and better dimensional stability at equilibrium; acetal also does not require pre-drying, while nylon 12 PTFE does require moisture control before moulding.

    When the 925-20PF Replaces Unfilled Nylon 12 in Dry-Running Bushings

    The grade is used in industrial wear pads, conveyor guide rails, sliding bearings, cams, rollers, collars, and positioning elements in packaging and material-handling equipment. It is also applied in non-structural automotive adjustment mechanisms where intermittent sliding motion and low noise are required. Because the PTFE filler is a solid lubricant rather than a plasticizer, the compound retains most of the short-term mechanical strength of the nylon 12 matrix but should not be specified for heavily loaded structural components. Continuous service in dry bushing applications should be limited to contact pressures below 0.5–1.0 MPa and surface speeds below 1.0 m/s, corresponding to a continuous PV limit of roughly 0.10–0.20 MPa·m/s depending on counterface finish and ambient temperature. Higher PV values require internal lubrication, external grease, or a counterface material with superior heat removal.

    The operational boundaries of the compound are defined by its polyamide 12 matrix. Continuous service above 90 °C under load is not recommended, and intermittent exposure should not exceed 120 °C. The grade is not suitable for contact with strong mineral acids, oxidising acids, or aqueous zinc chloride solutions, which attack polyamide 12. Food-contact suitability must be confirmed separately against FDA 21 CFR 177.1500 for polyamide and 21 CFR 177.1550 for PTFE, but this grade is not commonly marketed with food-contact certification. In sliding-bearing replacement of unfilled nylon 12, the PTFE-filled product reduces start-up noise and allows the same bush to operate without external grease under mild dry sliding conditions; however, the designer must accept a slight reduction in tensile yield strength and should monitor wear depth because the transfer film can be removed by aggressive cleaning solvents or by prolonged exposure to high-speed sliding without lubrication. The practical end-of-life indicator is not visual surface damage but measured radial wear exceeding 0.25 mm in standard bushing designs.

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