| HS Code | 494709 |
| Density | 1.22 g/cm³ |
| Glass Fiber Content | 30% |
| Tensile Strength | 120 MPa |
| Elongation At Break | 3% |
| Flexural Modulus | 5500 MPa |
| Flexural Strength | 160 MPa |
| Izod Impact Notched | 8 kJ/m² |
| Heat Deflection Temperature 1 8 Mpa | 160 °C |
| Melting Temperature | 178 °C |
| Melt Temperature | 220-240 °C |
| Mold Temperature | 40-60 °C |
| Water Absorption 24h | 0.2% |
As an accredited Polyram PlusTek PD304G6YL55 Nylon 12 for Injection Molding, 30% Glass-fiber Reinforced factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polyram PlusTek PD304G6YL55 Nylon 12, 30% glass-fiber reinforced for injection molding, supplied in 25 kg sealed bags. |
| Container Loading (20′ FCL) | 20′ FCL shipment of Polyram PlusTek PD304G6YL55, glass-fiber reinforced Nylon 12 pellets, securely palletized and packed in dry containers. |
| Shipping | This product ships as 30% glass-fiber reinforced Nylon 12 resin in sealed moisture-barrier bags or drums, palletized for safe transport. It should be kept dry and away from heat sources. Standard non-hazardous freight applies. Ensure proper handling to prevent bag damage and moisture absorption during transit. |
| Storage | Store in sealed original packaging in a cool, dry, well-ventilated area away from direct sunlight and heat sources. Keep at temperatures below 30°C to prevent moisture absorption, which degrades Nylon 12. Reseal containers tightly after opening and use within one year to maintain performance and consistent injection molding results. |
| Shelf Life | Shelf life is typically 2 years when stored unopened in a cool, dry place, protected from moisture and UV exposure. |
Injection-molded quick connectors and bracket clips for gasoline vapor recovery lines are produced from Polyram PlusTek PD304G6YL55 because the PA12 matrix absorbs less moisture than PA6 and PA66. The material must be dried to below 0.10 % residual moisture using a desiccant hopper dryer at 80 °C for 4 h to 8 h before processing. If the drying time is shortened and the feed zone is exposed to ambient air with relative humidity above 60 %, hydrolysis at the melt temperature of 250 °C to 280 °C produces splay at the barb gates and reduces pressure retention after molding. The recommended mold temperature for these connectors is 60 °C to 90 °C; higher settings within this band improve weld-line coalescence in the undercut barb region but require longer cooling time. Glass-fiber orientation follows the flow path across the gate into the barb root. Where two melt fronts meet on the distal side of the barb, the 30 % fiber content restricts polymer chain entanglement across the knit line, reducing local tensile strength to roughly 60 % to 75 % of the bulk conditioned strength, depending on filling speed, mold temperature, and gate position. Single-gate layouts are generally preferred over twin-gate layouts for barbs subject to SAE J2044 pressure-decay and pull-out sequences. Burst performance for connectors in fuel vapor service is commonly proof-tested at 1.5× working pressure and leak-tested under SAE J2044 protocols after hot-fuel aging in Fuel C under ISO 1817 immersion. Published data for this specific Polyram grade under full SAE J2044 sequences are limited; a certificate of analysis and part-level validation should be obtained before series release.
| Standard | Test method designation | Measured parameter | Application relevance |
|---|---|---|---|
| ISO 527-2 | Tensile specimen | Tensile modulus, strength, elongation | Structural brackets and snap-fit arms |
| ISO 178 | Three-point flexure | Flexural modulus | Pneumatic manifold plate stiffness |
| ISO 179-1/1eA | Notched Charpy impact | Impact resistance | Cold-impact sports and outdoor equipment |
| ISO 75-2 | Deflection temperature | HDT A and HDT B | Underhood thermal load assessment |
| ISO 62 | Water absorption | Moisture uptake | Dimensional stability in humid conditions |
| ISO 1817 | Liquid immersion | Mass change, swelling | Fuel, oil, and urea solution compatibility |
| ISO 294-4 | Plaque molding | Mold shrinkage | Tool cutting and cavity dimensioning |
Compressed air manifold plates and directional valve bodies molded from PD304G6YL55 require a balance of pressure containment, dimensional stability, and resistance to compressor oil mist. The material's flexural modulus, typically between 7,000 MPa and 8,500 MPa when tested to ISO 178, allows wall sections in the 3 mm to 6 mm range to carry 10 bar working pressure when the design safety factor is set at 4:1. Weld lines are the governing failure mode because the glass roving remains largely perpendicular to the knit line and does not cross the polymer interface. Mold flow analysis should position weld lines away from sealing lands and threaded brass inserts, or use sequential valve gating to collapse the knit front into an oversize flow tab that is removed after ejection. Mold temperature should not fall below 70 °C for these components; at 50 °C, the frozen skin layer thickens before the melt front rejoins, producing surface notches that reduce Charpy notched impact from approximately 12–15 kJ/m² to less than 8 kJ/m² when tested to ISO 179-1/1eA. Screw parameters are equally critical because excessive shear from a worn check ring can raise the melt temperature above 280 °C, causing discoloration, depolymerization, and a drop in melt viscosity that masks itself as improved fill but lowers load-bearing capacity in the air passage walls. End products include valve mounting plates and filter-regulator housings where creep under continuous pressure is more critical than short-term burst strength. Pneumatic systems designed under ISO 4414 require that such components be tested at the assembly level with the designated working fluid and pressure cycling profile.
Outdoor sensor housings and field bus connectors require a polymer shell that retains snap-fit engagement after repeated temperature-humidity cycles. PD304G6YL55 in these applications is typically processed with a melt temperature at the low end of the window, 245 °C to 260 °C, to preserve the yellow pigmentation and minimize thermal history. The mold surface is polished to SPI-B or SPI-A finish because the glass fibers leave a matte appearance that can hold dust and moisture. The coefficient of linear thermal expansion in the flow direction is about 30–40 × 10⁻⁶ K⁻¹, while transverse values can reach 80–100 × 10⁻⁶ K⁻¹ under ISO 11359-2. When the housing contains potted electronics, this anisotropy can generate shear stress on the encapsulant during thermal cycling from −40 °C to 85 °C. For that reason, housing ribs and screw bosses are gated so that the main flow direction follows the long dimension of the PCB pocket, not the narrow latch arms. A design review should compare the snap-fit deflection with the conditioned elongation at break of 4–6 %; if the latch root is located on a weld line, the effective elongation may fall below 2 %. The material is not inherently flame-retardant and should be specified only when the end-device standard permits UL 94 HB. For electrical properties, the comparative tracking index and dielectric strength should be taken from the supplier's UL yellow card; generic PA12 GF30 datasheets show dielectric strength in the range of 25–30 kV/mm under IEC 60243-1, but this value depends on specimen thickness and conditioning state.
Diesel fuel conditioning modules, oil separation plates, and low-pressure gear-pump rotors use PD304G6YL55 where metal replacement reduces weight and eliminates corrosion in oil-mist environments. The PA12 backbone shows low swelling in aliphatic hydrocarbons, mineral oils, diesel, and B20 biodiesel blends, as assessed by ISO 1817 immersion and associated mass-change measurements. A typical mass increase after 168 h in IRM 903 oil at 70 °C remains below 1 %, while the same part in concentrated formic acid or m-cresol would exhibit surface attack and stress cracking. Operational boundaries must exclude contact with strong mineral acids, phenols, and high-polar solvents above 50 °C; prolonged exposure to hot water above 80 °C may also reduce molecular weight through hydrolysis. Molding these thick-section plates requires a mold temperature of 80 °C to 100 °C and reduced injection velocity at the end of fill to minimize jetting. Fiber agglomeration at the gate is a known production defect when the nozzle bore is smaller than 4 mm; a direct sprue or a tab gate with a land length below 1.5 mm prevents glass separation from the melt front. The molded parts are often machined after annealing at 120 °C for 2 h to relax frozen-in orientation before flatness inspection on a granite surface plate. Without annealing, parts machined immediately after molding can warp by 0.3–0.5 % of the longest dimension over 72 h. Published data for this specific Polyram grade in continuous hot-oil service is limited; end users should validate with the specific fluid formulation and a safety factor appropriate for the pressure boundary.
Ski touring binding plates, bicycle hydraulic brake lever bodies, and climbing fall-protection backplates exploit the high specific stiffness of PD304G6YL55 at subzero temperatures. The material's Charpy notched impact at −30 °C remains in the range of 8–12 kJ/m² for a well-molded specimen, while many short-glass engineering polymers show a sharper ductile-to-brittle transition. In lever bodies, the gate is placed at the pivot boss, and the flow path is deliberately lengthened along the lever blade axis so that glass fibers align with the bending load path. Transverse reorientation is discouraged because a side gate at the blade edge shortens the flow length and creates a high-stress skin layer perpendicular to the lever axis. Molding trials with two-cavity tools show that cavity-to-cavity weight variation must be kept below 0.3 %; above this threshold, the thinner cavity exhibits more fiber orientation in the skin and a different impact response. The surface is then overmolded or coated because the yellow color is not a cosmetic match for all brands, and the glass fibers can abrade against soft elastomer grips. If the part is painted, the mold release agent must be fully removed and the surface roughened to 0.8–1.2 µm Ra to achieve adhesion; no primer or silane treatment should be assumed without adhesion testing. Finished components are retained by screws into brass inserts, and the insert bosses are designed with a hoop stress margin based on the conditioned tensile strength of 100–120 MPa when measured to ISO 527-2. Ultrasonic insertion is preferred over heat-staking to avoid localized re-melting of the glass-filled matrix around the insert knurl.
Across industrial machinery guarding and conveyor bracketry, PD304G6YL55 replaces painted steel components where high humidity and incidental cutting fluids cause corrosion. Structural posts, guide rails, and sensor mounts are molded with walls of 5 mm to 8 mm and use molded-in ribs rather than flat plate geometries because the flexural modulus drops when fiber orientation is randomized by complex flow around ribs. The part designer should specify a draft angle of 0.5° to 1° on textured surfaces to prevent ejection drag marks; the glass fibers increase friction against the cavity steel and can generate white stress marks when the part is pulled from an unpolished sidewall. Injection pressure at transfer should be limited to 80–120 MPa specific injection pressure depending on the flow length-to-wall thickness ratio. For a flow length of 150 mm and a wall of 3 mm, the ratio is 50:1 and the required pressure is near the upper end of that band. Process engineers monitor the cushion at 2–4 mm and screw decompression at 2–3 mm to avoid drooling from the nozzle during part removal. Shrinkage in the flow direction is approximately 0.2–0.4 %, while shrinkage in the transverse direction is 0.6–0.9 % by ISO 294-4, so the tool maker must cut the cavity as an anisotropic steel-safe allowance rather than a uniform scale factor. In service, cutting fluid compatibility should be confirmed by ISO 175 immersion for 168 h; most water-miscible machining coolants at 5 % concentration do not reduce tensile strength beyond 10 %, but chlorinated solvents and aggressive degreasers must be excluded from cleaning procedures.
Selective catalytic reduction fluid handling uses injection-molded quick connectors, clips, and urea tank level-sensor bosses made from PD304G6YL55. The polymer must resist 32.5 % urea solution as defined in ISO 22241 over a temperature window from −40 °C to 80 °C. Because urea solution freezes at approximately −11 °C, the connector must tolerate the expansion of freezing solution, making a flexible PA12 matrix more suitable than a highly crosslinked thermoset. Wall sections around the sealing face are kept below 4 mm to reduce core shift and sink, and the seal retention groove is vented to avoid trapped gas that would otherwise blister during fill. The gate is placed outside the groove so that glass fibers do not abrade the O-ring seat during assembly. After molding, parts are annealed at 100 °C in a circulating air oven for 2 h and then conditioned at 23 °C and 50 % RH for 24 h before dimensional audit. The sealing groove diameter is measured with a coordinate measuring machine at multiple points because ovality greater than 0.1 mm can cause leakage during low-temperature pressure cycling. A production concern is cross-contamination from other PA66 or PP materials in the same drying hopper; PA66 pellets require higher drying temperatures and can cause unmelted particles in the PA12 matrix, while PP contamination produces delamination and poor weld strength. Dedicated drying and material handling lines are required. The connector is then tested in the finished assembly under ISO 22241-compliant urea solution for dimensional stability and pressure retention; published data for this specific grade under continuous ISO 22241 immersion is limited, so a part-level validation sequence with the actual freeze-thaw profile is mandatory.
Competitive Polyram PlusTek PD304G6YL55 Nylon 12 for Injection Molding, 30% Glass-fiber Reinforced prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8615365186327
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Polyram PlusTek PD304G6YL55 is a polyamide 12 injection-molding compound reinforced with 30% by weight short glass fiber. The designation PD304 identifies the PlusTek PA12 series; G6 denotes a nominal glass-fiber content of 30% by mass, and YL55 denotes the yellow colour code. Under ISO 1043-1, the generic family designation is PA12-GF30. This product is normally specified where a nylon component must combine lower moisture uptake than PA6-GF30 or PA66-GF30, low-temperature impact resistance, resistance to aliphatic hydrocarbons, and post-mould dimensional stability. Published product-specific numerical data for PD304G6YL55 is limited in public technical literature; engineering-grade selection should therefore rely on supplier certificate-of-analysis values and lot-specific moulding evaluations. The following sections provide the processing boundaries, comparative property envelope, service limitations, and specification-verification logic for this class of compound.
Predrying is the first operational boundary. The polyamide 12 matrix absorbs atmospheric moisture, and residual moisture above 0.10% by weight at melt processing can produce hydrolysis at barrel residence temperatures above 240 °C. For a 30% glass-filled PA12 grade, a desiccant-bed dryer with a dew point of −30 °C or lower, a hopper inlet air temperature of 80 °C, and a residence time of 4 h to 6 h is the standard starting condition. Closed-loop conveying from dryer to feed throat is required where ambient relative humidity exceeds 60%. In production-scale injection molding, insufficient dryer airflow or hopper residence time below 4 h is a common batch-start defect source because moisture-laden granules near the feed throat are not fully regenerated.
Melt temperature at the nozzle should be maintained between 240 °C and 270 °C. Local melt temperatures above 280 °C or residence times longer than 8 min can induce thermal-oxidative degradation, which appears as yellow-brown discoloration and reduced notched impact strength. Because the compound contains 30% by mass glass fiber, screw wear is accelerated; bimetallic barrels, hardened check rings, and wear-resistant screw tips are specified on production machines. A general-purpose three-zone screw with an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.5:1 to 3.0:1 is adequate for short glass fiber, but a low-shear metering profile reduces fiber attrition. On presses with clamp forces from 800 kN to 1,600 kN, the practical throughput for PA12-GF30 can be limited by drying capacity rather than plasticating capacity.
Mould temperature between 60 °C and 80 °C is recommended. Below 40 °C, crystallinity development is incomplete and post-mould dimensional movement increases. Above 100 °C, cycle time is extended without proportional property benefit. Back pressure of 0.3 MPa to 0.7 MPa assists melt homogeneity; back pressure above 1.0 MPa may lower residual fiber length. Injection velocity should be medium to high for thin-walled parts; low injection speed can create weld-line weakness. A production failure mode specific to glass-filled grades is loss of screw cushion due to check-ring wear. Cushion variation exceeding 1 mm over a 20-shot window indicates non-return valve leakage, producing inconsistent packing pressure, sink marks, and variable part mass.
Compounding of a PA12-GF30 grade is normally performed on a co-rotating intermeshing twin-screw extruder with an L/D ratio between 40:1 and 48:1 and side feeding of glass fiber downstream of the polymer feed. This sequencing preserves fiber length by minimizing full-melt residence time. Moulded-part fiber-length distribution after plastication is generally lower than the pellet distribution; number-average fiber lengths of 200 µm to 400 µm are common for injection-moulded short-glass polyamides. Glass content can be verified by ash according to ISO 3451-1, and moisture content can be measured by ISO 15512.
Because supplier-published product-specific data for PD304G6YL55 is limited, the comparative envelope below uses representative values reported for commercial PA12-GF30, PA66-GF30, and unfilled PA12 injection-moulding grades. These ranges are not lot-specific specifications.
| Property | PA12-GF30 | PA66-GF30 | Unfilled PA12 | Test method |
|---|---|---|---|---|
| Density | 1.22–1.28 g/cm³ | 1.35–1.41 g/cm³ | 1.01–1.03 g/cm³ | ISO 1183-1 |
| Tensile modulus | 6,000–8,500 MPa | 9,000–12,000 MPa | 1,400–1,600 MPa | ISO 527-2 |
| Tensile strength at break | 105–135 MPa | 150–190 MPa | 40–55 MPa | ISO 527-2 |
| Flexural modulus | 5,500–7,500 MPa | 8,000–11,000 MPa | 1,100–1,400 MPa | ISO 178 |
| Charpy notched impact, 23 °C | 8–14 kJ/m² | 10–15 kJ/m² | 6–12 kJ/m² | ISO 179-1/1eA |
| HDT at 1.8 MPa | 160–180 °C | 245–255 °C | 50–60 °C | ISO 75-2 |
| CLTE, flow direction | 30–50 µm/(m·K) | 25–40 µm/(m·K) | 100–120 µm/(m·K) | ISO 11359-2 |
| Equilibrium moisture at 23 °C/50% RH | 0.5–0.8% | 1.2–1.7% | 0.5–0.8% | ISO 62 |
These values identify the main differences among product classes. PA12-GF30 does not equal the load-bearing stiffness of PA66-GF30, but it displays roughly half the equilibrium moisture sorption at 23 °C and 50% RH. Lower moisture uptake reduces hygroscopic dimensional change and preserves a larger fraction of dry-as-moulded stiffness in humid service. The glass-fiber reinforcement also reduces coefficient of linear thermal expansion to approximately one-third that of unfilled PA12.
Polyamide 12 contains fewer amide groups per unit chain length than PA6 or PA66. The equilibrium moisture uptake at 23 °C and 50% RH for a 30% glass-filled PA12 is approximately 0.5% to 0.8%, whereas PA66-GF30 typically absorbs 1.2% to 1.7% and PA6-GF30 can absorb 1.3% to 1.8%. The practical consequence is that PD304G6YL55 components retain tighter post-mould tolerances in ventilated enclosures, air-conditioned interiors, and outdoor shelter applications where humidity cycles. A glass-fiber loading of 30% by weight also suppresses the absolute swelling magnitude compared with unfilled PA12 because the inorganic fiber phase does not expand with moisture. Under immersion at 23 °C in water, reported saturation moisture uptake for PA12-GF30 is commonly 1.5% to 2.5% according to ISO 62, though product-specific data for PD304G6YL55 is limited.
Design for injection molding must account for anisotropic shrinkage. Mould shrinkage of short-glass reinforced PA12 is typically 0.2% to 0.5% parallel to flow and 0.5% to 1.0% perpendicular to flow when measured according to ISO 294-4. This difference requires gate placement that avoids asymmetric fiber orientation across sealing faces. In production trials, tensile specimens cut transverse to flow may show 20% to 30% lower strength than flow-direction specimens; published data for PD304G6YL55 in transverse orientation is limited. Tooling should be sized using supplier-specific shrinkage data for the selected wall thickness and gating configuration.
PA12-GF30 is frequently selected for fuel-system clips, diesel exhaust fluid connectors, pneumatic tubing couplings, pump components, cable glands, and industrial housings because the polyamide 12 backbone resists aliphatic hydrocarbons, mineral oils, diesel fuel, greases, and many neutral salt solutions. Compared with PBT-GF30, PA12-GF30 generally provides better resistance to alkaline media and superior low-temperature impact; PBT-GF30 provides faster crystallization and lower moisture uptake but may embrittle in hot moist alkaline environments. Compared with PPS-GF40, PA12-GF30 offers higher elongation at break and lower melt temperature, but PPS-GF40 is more suited to continuous-use temperatures above 180 °C.
Resistance can be evaluated by ISO 175 immersion at defined temperatures, with property retention measured before and after exposure by ISO 527-2 or ISO 179-1/1eA. The PA12 chain does not swell heavily in diesel, heptane, or mineral oil at ambient temperature, making the glass-reinforced grade suitable for hydrocarbon contact. However, PD304G6YL55 should not be specified for continuous immersion in strong mineral acids below pH 2, concentrated formic acid, aqueous phenol, or chlorinated solvents at elevated temperature because these media attack polyamide chains or promote environmental stress cracking. Continuous exposure to hot water above 80 °C under pressure can also hydrolyze the matrix over extended service life; this is a known boundary for all PA12 grades, including glass-filled variants.
Low-temperature performance is a key difference from PA66-GF30. PA12 maintains lower brittle-point behaviour than PA66, and a 30% glass-filled PA12 typically retains notched Charpy impact of 5 kJ/m² to 9 kJ/m² at −30 °C. This makes PD304G6YL55 a candidate for snap-fit connectors and mounting clips exposed to cold-arctic or high-altitude environments, provided the part design avoids sharp corners that concentrate moulded-in glass-fiber stress.
The generic ISO designation is PA12-GF30 under ISO 1043-1. Injection-moulding grades are often supplied with certificates of analysis against ISO 1133-1 melt volume-flow rate and ISO 3451-1 glass content. PD304G6YL55 is subject to supplier declarations under REACH Regulation EC No 1907/2006 Article 33 and RoHS Directive 2011/65/EU Annex II; no grade-specific SVHC statement should be inferred without reviewing the current safety data sheet. FDA 21 CFR 177.1500 may be relevant for polyamide 12 resins in repeat-use food-contact articles, but the specific compound with glass fiber and colourants requires supplier certification and migration testing under the intended conditions of use. UL 94 Yellow Card data should be consulted for thickness-dependent flammability classification.
| Reference | Application to PD304G6YL55 | Verification source |
|---|---|---|
| ISO 1043-1 | Generic designation PA12-GF30 | Supplier technical data sheet |
| REACH EC No 1907/2006, Article 33 | SVHC declaration for articles | Safety data sheet or supplier declaration |
| RoHS Directive 2011/65/EU, Annex II | Restricted substances in electrical and electronic equipment | Supplier declaration |
| FDA 21 CFR 177.1500 | Potential food-contact suitability for nylon resins | Grade-specific certification required |
| UL 94 | Thickness-dependent flammability classification | UL Yellow Card for exact grade and colour |
| ISO 3451-1 | Glass content of 30% by mass | Certificate of analysis |
| ISO 15512 | Residual moisture before moulding | In-process or supplier certificate |
The selection of PD304G6YL55 against PA6-GF30, PA66-GF30, PBT-GF30, or unfilled PA12 should be made on the basis of the service environment, tolerance window under humidity, chemical exposure, and moulding-process capability. Where dry-as-moulded stiffness dominates, PA66-GF30 may offer higher modulus. Where low moisture absorption, cold-impact resistance, and hydrocarbon contact control the specification, the PA12-GF30 configuration of PD304G6YL55 is the appropriate reference point.