| HS Code | 331716 |
| Density | 1.58 g/cm³ |
| Filler Content | 55% Glass/Mineral |
| Tensile Strength At Break | 180 MPa |
| Elongation At Break | 1.5% |
| Flexural Modulus | 12500 MPa |
| Flexural Strength | 250 MPa |
| Izod Impact Notched | 60 J/m |
| Heat Deflection Temperature At 1 82 Mpa | 160 °C |
| Water Absorption | 0.5% |
| Mold Shrinkage | 0.2% |
As an accredited Encom Polymers EnLon PX55MG Amorphous Nylon, 55% Glass Filled and Mineral Filled factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | EnLon PX55MG amorphous nylon (55% glass/mineral filled) is supplied in 25 kg net, heat-sealed, moisture-barrier bags, palletized for shipment. |
| Container Loading (20′ FCL) | Loading a 20-foot FCL of Encom Polymers EnLon PX55MG amorphous nylon, 55% glass and mineral filled, packaged securely for shipment. |
| Shipping | EnLon PX55MG ships as solid nylon pellets in sealed moisture-barrier bags or fiber drums. It is non-hazardous under U.S. DOT and international transport regulations, so standard ground freight applies. Keep containers sealed and dry to prevent moisture absorption during transit and storage. No special temperature controls required. |
| Storage | Store Enlon PX55MG in a cool, dry, well-ventilated area, tightly sealed in its original, clearly labeled container. Protect from moisture, direct sunlight, and excessive heat. Keep away from strong oxidizers, acids, and ignition sources. Avoid dust accumulation and floor-level storage to prevent water damage. Maintain stable temperatures to preserve material integrity and prevent degradation before processing. |
| Shelf Life | Store in original sealed container in a cool, dry area. Shelf life is indefinite if protected from moisture and contamination. |
Encom Polymers EnLon PX55MG amorphous nylon at 55% glass/mineral loading is specified for automotive forward-facing sensor mounting structures where dimensional stability clauses under IATF 16949:2016, clause 8.6.1.1, require documented stability across thermal cycling from 23 °C to 85 °C and through humidity exposure cycles. The compound is charged as 100 wt% neat pellet feed for first-generation parts; a black polyamide-carrier masterbatch is added at 1.0 wt% to 2.0 wt%, and post-industrial regrind from sprue and runner stock is capped at 15 wt% of total shot mass because camera-bracket mounting bosses commonly carry positional tolerances tighter than ±0.10 mm. Pre-drying is executed at 80 °C for 4 h in a desiccant dryer with supply dew point of -30 °C until residual moisture by Karl Fischer titration reads ≤0.10%. Injection molding is conducted on hydraulic machines between 1,800 kN and 4,000 kN clamp force, with nozzle melt temperature 265 °C to 285 °C and mold temperature 75 °C to 95 °C. The screw L/D is held at 20:1 to 24:1, compression ratio at 2.0:1 to 2.5:1, and back pressure at 1 MPa to 3 MPa to limit glass-fiber length reduction during plasticating. Compliance under REACH 1907/2006 and RoHS 2011/65/EU Annex II is verified by supplier declaration; tensile batch checks under ASTM D638-14 and flexural checks under ASTM D790-17 are used for incoming consistency, although published data for this specific configuration is limited. Amine-based mold release agents and flame retardant packages are avoided because free amines can accelerate nylon hydrolysis at melt temperature. Finished terminal parts include ADAS camera mounting brackets, radar sensor carriers, lidar housing base plates, and exterior mirror inner supports.
Limiting wall thickness in terminal block bases molded from EnLon PX55MG is governed not by short-term tensile strength at 23 °C but by retention of clearance and creepage distances under IEC 60664-1:2020 after thermal shock and after the part reaches equilibrium moisture content. For sections below 1.5 mm, the addition of regrind is capped at 10 wt% because glass-fiber length reduction increases the coefficient of linear thermal expansion in the flow direction and can alter the surface resistivity of the molded dielectric. The formulation uses 100 wt% neat compound plus 0.5 wt% to 1.5 wt% of a halogen-free color masterbatch; no additional downstream flame retardant is added at the press, and the UL 94 rating must be taken from the published Yellow Card for the exact grade and thickness rather than inferred from comparable amorphous nylon compounds. Processing on an injection molding machine with a 20:1 to 24:1 L/D screw uses a melt temperature of 270 °C to 290 °C and a mold temperature of 80 °C to 95 °C; a shot cushion of 3 mm to 6 mm and a deceleration profile at the filling-to-packing switch prevent gate jetting. Gate placement is arranged so that weld lines do not cross current-carrying bushings, snap-fit retention features, or DIN rail mounting slots. IEC 60947-1:2007 provides the low-voltage switchgear context, while surface resistivity batch records use ASTM D257-14 and electric strength checks use IEC 60243-1:2013 where end-use dielectric tests are not substituted. Terminal components include PCB terminal block insulating bodies, busbar support plates, relay base housings, and distribution block carriers.
During continuous operation in end-suction centrifugal pump volutes, EnLon PX55MG is specified for sections above 3 mm wall thickness, where the 55% glass/mineral combination reduces differential shrinkage at the volute cutwater and around the stuffing box flange. Formulation addition practice for this hydraulic application uses 100 wt% virgin compound for impeller hubs and diffuser plates because pressure-bearing regions accept a regrind fraction no higher than 10 wt%; static volute casings with wall sections above 3 mm accept up to 30 wt% post-industrial regrind when sourced from a stable gate-runner stream. No additional glass or mineral is compounded at the downstream injection molder, because filler content above 55% would reduce melt flow and increase barrel wear without a corresponding gain in stiffness. The molders use nitrided or bimetallic barrels because glass and mineral fillers accelerate screw-flight wear; screw L/D is kept at 20:1 to 24:1, compression ratio at 2.0:1 to 2.5:1, nozzle melt temperature at 265 °C to 285 °C, and mold temperature at 70 °C to 90 °C. Gate thickness is specified at 0.8 times the adjacent wall section to prevent premature freeze and packing starvation at the impeller shroud. Dimensional checks follow ISO 2858 pump interface dimensions where applicable; tensile property records use ISO 527-2:2012, and RoHS 2011/65/EU plus REACH 1907/2006 are applied. Published hydrostatic creep data for this specific configuration is limited, so hydrostatic qualification is conducted on each tool rather than relying on extrapolated semi-crystalline polyamide values. End products are pump volutes, impeller blanks, diffuser plates, lantern rings, and pump end covers for industrial water circulation and booster systems.
Pneumatic valve base dimensional stability under cyclic actuation of 0.5 MPa to 1.0 MPa supply pressure is controlled by post-molding moisture conditioning of EnLon PX55MG rather than by tool shrinkage compensation alone. Formulation addition practice for this application uses 100 wt% virgin compound for mounting faces that must meet ISO 5599-1:2018 interface dimensions; if impact-modified amorphous nylon is added to reduce brittle fractures at threaded port edges, its proportion is held at ≤10 wt% to avoid excessive loss of compressive stiffness and dimensional fidelity. Additional internal mold release masterbatch is limited to 0.1 wt% to 0.3 wt% because excess lubricant can migrate to sealing surfaces and affect port leak tightness. Injection molding of high-flow valve bases uses sequentially valve-gated hot runners on clamp capacities from 1,200 kN to 2,500 kN; melt temperature is kept between 260 °C and 280 °C, and mold temperature is held at 85 °C to 95 °C. Cavity gas evacuation is set to 0.02 mm to 0.04 mm vent depth, and post-mold annealing at 120 °C for 2 h in a forced-air oven is used to relax molded-in stress before thread chasing. Standards cited include ISO 5599-1:2018 for five-port directional control valve mounting interfaces and IEC 60529 for ingress protection enclosure ratings. Terminal products include pneumatic solenoid valve bodies, ISO valve manifold bases, air preparation unit housings, and cylinder mounting adapters.
When regrind content exceeds 20 wt% in structural frames molded from EnLon PX55MG, notched Izod impact values under ASTM D256-10e1 begin to shift downward, while flexural modulus under ASTM D790-17 remains within 5% of virgin material in the same tool. The formulation addition limit for washing machine motor end covers is therefore set at 20 wt% to 30 wt% post-industrial regrind only when the wall section remains above 2.5 mm; for ribbed frames with snap-fit towers, the regrind fraction is reduced to 15 wt% to avoid brittle failures at ejection. If third-heat recycled compound is used, a polyamide-stabilized antioxidant masterbatch is added at 0.1 wt% to 0.3 wt% to offset thermo-oxidative degradation during repetitive melt processing. Relevant compliance is IEC 60335-1:2020, Clause 30.2, for resistance to ignition and spread of fire; applicable glow-wire terminal requirements depend on unattended appliance current and must be confirmed against the final part thickness. Injection molding is carried out on large hydraulic or toggle machines from 6,000 kN to 12,000 kN clamp force, using sequentially valve-gated hot runners to manage the long fill distance of base frames. Melt temperature is 270 °C to 285 °C, mold temperature is 70 °C to 85 °C, and cooling time is set according to the square of the dominant wall thickness rather than by a fixed timer. RoHS 2011/65/EU applies, and REACH 1907/2006 declarations are maintained for the compound. Terminal products include washing machine motor end covers, dishwasher sump supports, dryer fan housings, and appliance base frames.
Direct-gated industrial water meter bodies molded from EnLon PX55MG are more sensitive to gate blush and filler orientation at the boss-to-sidewall junction than to equilibrium water absorption at 23 °C. The formulation addition ratio for outdoor metering chambers uses 100 wt% virgin compound plus a UV-stabilized black masterbatch at 2.0 wt% to 2.5 wt%; regrind is limited to 15 wt% for pressure-containing walls and to 5 wt% for ultrasonic transducer mounting bosses where acoustic path alignment is critical. Potable water contact is outside the stated use of this compound unless the exact grade appears on an NSF/ANSI 61 listing; the material is instead specified for industrial metering and non-potable water circuits. Dimensional interfaces follow ISO 4064-1:2014 for water meter assemblies where applicable. Processing uses melt temperature from 260 °C to 285 °C and mold temperature from 80 °C to 95 °C; beryllium-copper cores or high-conductivity alloy inserts are used to maintain mold surface temperature variation within ±2 °C. Threaded inlet and outlet bosses are produced with unscrewing cores to avoid post-machining of the molded glass/mineral surface. Published data for long-term hydrostatic creep in this specific configuration is limited, so pressure cycling tests on actual molded bodies are required before field release. Terminal products include industrial water meter housings, ultrasonic flow meter bodies, irrigation controller enclosures, and submersible pump electrical junction boxes.
Competitive Encom Polymers EnLon PX55MG Amorphous Nylon, 55% Glass Filled and Mineral Filled prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618136850665
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Encom Polymers EnLon PX55MG is an amorphous nylon compound carrying a combined glass and mineral reinforcement fraction of 55% by weight. The reinforcement package is not a simple 55% glass-fibre loading; the mineral constituent reduces warp and lowers the coefficient of linear thermal expansion while the glass fibre contributes tensile and flexural stiffness. The matrix is a semi-aromatic amorphous copolyamide of the type used to suppress crystalline shrinkage and to provide a relatively high glass transition temperature compared with some conventional aliphatic polyamides. The grade is supplied for injection moulding of dimensionally critical structural parts where semi-crystalline PA66 or PA6 grades may show excessive differential shrinkage, moisture-induced growth, and post-mould warpage. Published physical property data for this specific configuration may be limited in open literature; lot-specific certificates of analysis and the Encom Polymers technical data sheet should be consulted before tooling release.
Mechanical property determination for this product class follows tensile testing to ISO 527-2:2012 or ASTM D638-14, flexural testing to ISO 178:2019 or ASTM D790-17, and heat deflection temperature to ISO 75-2:2013 method Af at 1.8 MPa. The high reinforcement loading requires specimen conditioning at 23 °C and 50% relative humidity only where moisture-dependent comparisons are being made; otherwise dry-as-moulded testing is preferred because amorphous nylon may absorb moisture that reduces modulus and strength. The density of heavily filled amorphous nylon compounds can exceed 1.5 g/cm³, but exact values vary with glass-to-mineral ratio and the presence of processing stabilizers.
| Property | Standard method | Condition |
|---|---|---|
| Tensile strength at break | ISO 527-2 | 1 mm/min, dry as moulded |
| Tensile modulus | ISO 527-2 | 1 mm/min |
| Flexural strength | ISO 178 | 2 mm/min |
| Flexural modulus | ASTM D790-17 | Procedure A, span-to-depth ratio 16:1 |
| Izod notched impact | ASTM D256-23 | Method A, specimen thickness 3.2 mm |
| Charpy unnotched impact | ISO 179-1/1eU | Edgewise, 4 J pendulum |
| Heat deflection temperature | ISO 75-2 | Method Af, 1.8 MPa, flatwise |
| Density | ISO 1183-1 | Method A, 23 °C |
| Mould shrinkage | ISO 294-4 | Plaque 60 mm x 60 mm x 2 mm |
| Water absorption | ISO 62 | 23 °C, immersion 24 h |
| Coefficient of linear thermal expansion | ISO 11359-2 | -40 °C to 150 °C |
| Melt volume-flow rate | ISO 1133-1 | 275 °C / 5 kg |
The glass-to-mineral ratio in PX55MG is not public in every datasheet, but the combined loading is fixed at 55% by weight. Glass fibre in a highly filled amorphous nylon increases tensile strength and flexural modulus but also raises melt viscosity and tool wear. Mineral filler contributes to compressive strength and flatness but may reduce notched impact strength. A higher total filler fraction also increases density and may lower the critical radius for notch sensitivity; design engineers should avoid sharp internal corners, especially near gate locations where frozen-in stress and glass fibre orientation concentrate. Rib-to-nominal-wall ratio should remain below 0.6:1 to prevent sink marks and differential orientation that can cause localized shrinkage differences. Weld lines in glass-filled grades typically retain only a fraction of the base tensile strength; placing the gate to move weld lines to low-stress regions improves part performance more than increasing part thickness.
When a component is transferred from a 33% glass-fibre-reinforced PA66 to EnLon PX55MG, the first difference is the reinforcement loading: 55% combined glass and mineral changes the modulus-to-density ratio and reduces the unreinforced matrix volume available for moisture uptake. In semi-crystalline PA66, post-mould crystallization continues for hours after ejection, causing shrinkage and warpage; an amorphous nylon matrix does not undergo the same crystalline rearrangement. The glass/mineral combination lowers anisotropic shrinkage relative to an all-glass compound at equal loading because the low-aspect-ratio mineral particles break up fibre orientation patterns. The trade-off is that all-glass compounds often retain higher tensile elongation and notched impact strength; the mineral phase in PX55MG improves flatness and thermal expansion characteristics but may reduce fracture toughness. Published data for this specific configuration is limited, but comparative moulding studies of glass/mineral-filled amorphous nylons consistently show lower warpage than equivalent glass-fibre-only versions when measured against ISO 294-4 plaques.
Moisture exposure prior to moulding remains the most common source of batch-to-batch viscosity drift in amorphous nylon compounds. A desiccant dryer with a dew point no higher than -30 °C should reduce residual moisture below 0.10% by weight before processing. Drying at 80 °C to 90 °C for 4 h is common for heavily filled amorphous nylon; if ambient relative humidity exceeds 60%, hopper residence time and dry-air feed should be extended rather than relying on oven drying. A closed dry-air conveying system is recommended because regrind and virgin pellets can re-absorb surface moisture quickly. Injection barrels should use reverse or flat temperature profiles with rear zones at 250 °C to 270 °C, mid-zones at 265 °C to 280 °C, and nozzle at 270 °C to 285 °C. Melt residence time at full barrel temperature should remain below 8 min to avoid progressive chain scission, which appears as lower nozzle pressure and weak weld lines.
Mould shrinkage of a reinforced thermoplastic is not a single number; it depends on wall thickness, gate location, fibre orientation, packing pressure, and mould temperature. For a 55% glass/mineral-filled amorphous nylon, the mineral phase reduces orientation-dependent shrinkage by lowering anisotropy. A gate seal study with a cavity pressure transducer should be executed before production; hold pressure is adjusted until the gate freezes, then part weight is maximized without flash. Mould temperature between 80 °C and 120 °C is typical for amorphous nylon, with higher temperatures improving knit-line strength and surface finish but increasing thermal stress in deep draws. The coefficient of linear thermal expansion is measured by ISO 11359-2:2021, but the glass/mineral ratio may produce different expansion parallel and perpendicular to flow. Parts with strict flatness tolerances should use steel tooling with corner radii above 0.5 mm and generous venting to avoid gas burn marks.
In hot-water pump housings and glycol-contact valve bodies, the material's dimensional stability under hygrothermal load becomes a design variable. Candidate applications for glass/mineral-filled amorphous nylon include structural electrical housings, industrial sensor bodies, thermostat housings, oil-field connector shells, and pump volutes where creep under clamp load must remain low. Unlike PBT or PPS, amorphous nylon may provide a smoother mineral-filled surface at similar stiffness and lower warpage; however, continuous exposure to hot aqueous acids or strongly oxidizing media must be excluded. Long-term hydrolysis resistance can be screened by immersion in boiling water or a 50/50 glycol-water mixture for 1,000 h at 90 °C, with tensile strength retention measured to ASTM D543 or ISO 175:2010. Published data for this specific configuration is limited; end-use qualification is required for pressurized fluid contact.
If the application contains ethylene glycol-based coolant at temperatures above 110 °C, polyphthalamide or PPS may be selected instead of amorphous nylon, but PX55MG may remain suitable where the operating temperature is lower or where dimensional stability and cost per unit volume outweigh hydrolytic stability. The amorphous matrix generally has lower moisture absorption than PA66, which limits hygroscopic growth but does not eliminate it. Glass-filled amorphous nylon can still absorb enough moisture to reduce flexural modulus at saturation; design calculations should use wet-condition properties and not dry-as-moulded numbers. Stress crack resistance in coolant is influenced by internal stress from moulded-in orientation and by the presence of organic acid contaminants, which should be held below the concentration specified by the fluid supplier.
| Attribute | PX55MG glass/mineral amorphous nylon | All-glass 55% amorphous nylon | 33% glass-filled PA66 |
|---|---|---|---|
| Warp tendency in flat parts | Lower | Higher | Moderate to high |
| Anisotropic shrinkage | Reduced by mineral | Higher | High |
| Moisture-induced growth | Low to moderate | Low | Higher |
| Tensile strength retention at elevated temperature | High under dry heat | High | Moderate |
| Surface finish | Smoothed by mineral | Fibre-prominent | Moderate |
Rheological characterization for the moulding shop should use capillary rheometry per ISO 11443:2021 at 270 °C, 280 °C, and 290 °C, scanning shear rates from 100 s⁻¹ to 5,000 s⁻¹. Apparent shear viscosity will be higher than unfilled amorphous nylon and will shear-thin strongly due to glass fibre alignment. Gate sizing should follow short land lengths to avoid premature freeze-off; round or trapezoidal gates with diameter or hydraulic diameter above 1.5 mm are common for parts above 3 mm wall thickness. Hot runner systems should use externally heated manifolds with no dead spots, because the high filler content accelerates abrasive wear in valve pins and manifold channels. Screw and barrel surfaces should be treated for abrasion resistance, and the check ring should be inspected at intervals shorter than for unfilled nylon.
In a hydraulically clamped machine producing a housing with 120-tonne clamp force and a 40 mm screw of 20:1 L/D, the high filler loading may increase melt pressure at the nozzle above 120 MPa. The exact pressure depends on flow length and wall thickness. Cavity pressure sensors should be specified at the end of fill and near the gate to monitor packing. Hold pressure should be set to reach 60–80 MPa at the gate sensor, but not so high that the part sticks or flashes. Back pressure in the injection unit is usually held between 0.5 MPa and 1.5 MPa to homogenize the melt without excessive fibre breakage; screw rotation speed should be limited to 50–100 min⁻¹ for a medium-diameter screw to reduce fibre attrition. A shut-off nozzle is necessary when the barrel remains hot between cycles to prevent drool and moisture uptake in the melt stream.
Tool steel selection should account for the abrasive nature of 55% glass/mineral-filled amorphous nylon. Core pins and slides in production with this compound require higher hardness or surface coatings to maintain roundness and shut-off integrity. Venting channels should be 0.01 mm to 0.02 mm deep for the first 1 mm of passage, then widen to full runner depth; inadequate venting results in diesel burn marks at the end of fill in blind pockets. Draft angles above 0.5° are generally needed for textured sidewalls, and ejector area should be increased when ribs or bosses are added due to higher shrinkage forces on core pins. When a tool is transferred from an unfilled nylon or a 33% glass grade to a 55% glass/mineral grade, rebalancing the runner system may be necessary because the higher viscosity and filler packing can shift the last-fill location.
All-glass 55% amorphous nylon compounds are a natural alternative when tensile strength is the primary requirement. However, all-glass versions often produce greater anisotropic shrinkage, higher warpage, and a more fibrous surface appearance. The mineral modification in PX55MG trades a modest reduction in flexural strength and impact for more uniform shrinkage and better flatness. Against a 50% mineral-filled amorphous nylon, the PX55MG's glass fibre fraction improves tensile and flexural modulus, while the mineral still controls warpage. Against a semi-crystalline PPA with similar heat deflection, the amorphous nylon may offer lower moisture absorption and easier mould flatness, but PPA generally retains better hydrolytic stability in aggressive coolant and hot water environments.
Moisture analysis may be performed by Karl Fischer titration at 180 °C headspace or by a thermogravimetric moisture balance. Residual moisture above 0.15% is known to produce splay and degradation in amorphous nylon at high barrel temperatures. In a production environment, the use of hopper dryers with insufficient airflow can leave the centre of the hopper wet while the walls are dry; hopper capacity should allow at least 4 h of material residence when drying at 80 °C. For throughputs above 20 kg/h, a desiccant wheel dryer with a regenerated desiccant bed and closed-loop conveying is standard.
Regulatory documentation should confirm compliance with RoHS 2011/65/EU and REACH 1907/2006/EC SVHC restrictions. The material is not implicitly qualified for food-contact or medical devices; any citation to FDA 21 CFR or ISO 10993 must be obtained from Encom Polymers for the specific lot and compound formulation. Flammability classification under UL 94 is not assumed unless a yellow card exists for the exact grade and colour. Post-consumer recyclate or unspecified regrind should not be substituted without mechanical property verification to ISO 527-2 and ISO 179-1. Laser marking and adhesive bonding performance vary with mineral content and surface polarity; adhesive bonding can be evaluated by lap shear testing to ISO 4587 or ASTM D3163, and laser mark contrast should be verified on production-textured surfaces rather than polished plaques.