| HS Code | 193106 |
| Filler Content | 23% Glass Fiber |
| Density | 1.17 g/cm³ |
| Melting Point | 185 °C |
| Glass Transition Temperature | 45 °C |
| Tensile Modulus | 5.4 GPa |
| Tensile Strength At Break | 95 MPa |
| Elongation At Break | 5% |
| Flexural Modulus | 4.7 GPa |
| Flexural Strength | 130 MPa |
| Notched Izod Impact Strength | 4.5 kJ/m² |
| Heat Deflection Temperature At 1 8 Mpa | 160 °C |
| Vicat Softening Temperature | 173 °C |
| Water Absorption At Saturation | 1.0% |
As an accredited Arkema Rilsan BZM 23 G9 Nylon 11, 23% Glass Fiber Filled factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Arkema Rilsan BZM 23 G9 Nylon 11 is packaged in 25 kg polyethylene-lined paper bags as free-flowing pellets. |
| Container Loading (20′ FCL) | One 20-foot FCL container loaded with Arkema Rilsan BZM 23 G9 Nylon 11, 23% glass fiber filled resin, securely packed for transport. |
| Shipping | Ship as non-hazardous polymer resin in sealed, moisture-proof bags or drums. Avoid prolonged UV exposure and high humidity. Keep pallets dry, secured, and protected from punctures. Use standard dry van containers. Label with product name and lot number. Store below 30°C, away from heat sources. |
| Storage | Store Rilsan BZM 23 G9 in its original, sealed container in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and oxidizing agents. Keep the container tightly closed to prevent moisture absorption, which can degrade the nylon 11 resin. Recommended storage temperature is below 50°C. Keep away from ignition sources. |
| Shelf Life | Shelf life is typically 2 years when stored unopened in original, sealed packaging in a cool, dry place away from moisture. |
In automotive evaporative emission systems, injection-moulded flanges and canister bodies produced from Rilsan BZM 23 G9 are specified for fuel pump retainers, EVAP canister flanges, and fuel filter housings where Fuel C immersion and vapour cycling create combined dimensional and mechanical demands. The compound as supplied contains 23% by weight short glass fibre distributed in a PA11 matrix; the glass fraction reduces mould shrinkage to a published range of 0.2–0.5% in the flow direction and 0.5–1.0% transverse, enabling a 180 mm sealing face to remain within a 0.15 mm flatness tolerance after 1,000 h of cyclic exposure to Fuel C per SAE J1645. Drying before melt processing is mandatory: residual moisture must be below 0.08% by weight after 4–6 h at 80°C in a desiccant dryer with a dew point of -40°C or lower. A barrel profile from 250°C rear to 270°C front and nozzle at 265°C is used, with a mould temperature of 70–80°C; below 60°C mould temperature, the glass-rich skin freezes before pack out and sealing-face flatness shifts upward. Hold pressure is maintained at 50–70 MPa for 6–10 s, followed by 20–30 s cooling. Gate location must place the last filling point away from the sealing land because the weld line formed by opposing glass-flow fronts can retain as little as 50–70% of the unwelded tensile strength under ISO 527-2. Tensile modulus in the conditioned state is typically in the 5,000–6,000 MPa range, while elongation at break remains above 3%, sufficient for snap-fit retainers that must not crack after -40°C impact tests per ISO 16750-4. Regrind addition up to 20 wt% is accepted for non-appearance regions only when the pellet moisture is re-controlled to the same 0.08% threshold and the glass content is verified after re-blending.
| Component class | Wall thickness | Melt temperature | Mould temperature | Hold pressure | Residual moisture |
|---|---|---|---|---|---|
| Thin-wall connector body | 0.8–1.5 mm | 270–280°C | 80–90°C | 60–80 MPa | ≤0.08% |
| Medium-wall fuel flange | 2–4 mm | 260–270°C | 70–80°C | 50–70 MPa | ≤0.08% |
| Thick-wall offshore clamp | >6 mm | 250–260°C | 60–70°C | 40–60 MPa | ≤0.06% |
Outdoor telemetry boxes, ultrasonic sensor bodies, and electric vehicle charging port housings exploit the low moisture uptake of Rilsan BZM 23 G9 relative to PA66 GF30, because dimensional change after 24 h water immersion per ISO 62 is under 1.0% and equilibrium moisture uptake at 50% RH remains below 1.5% for most wall thicknesses below 3 mm. The 23% glass fibre reinforcement produces a tensile modulus close to 5,500 MPa and a heat deflection temperature of 150–170°C under ISO 75-2/Af, allowing the material to pass short-term peak temperatures near 160°C during selective wave soldering or hot-plate welding of inserts. The melt viscosity of the glass-filled grade demands a reciprocating screw with a 20:1–25:1 L/D ratio and a compression ratio of 2.0:1–2.4:1; back pressure is set at 0.5–1.0 MPa to homogenise fibre distribution without generating enough shear to reduce fibre length below 0.3 mm. For thin-wall connector bodies between 0.8 mm and 1.5 mm, injection velocity is set from 80 mm/s to 120 mm/s, and the mould temperature is held at 80–90°C to ensure fibre wet-out at the surface, which reduces surface glass protrusion and improves comparative tracking index stability under IEC 60112. Because PA11 contains no halogens, the compound normally meets UL 94 HB and RoHS Directive 2011/65/EU threshold requirements, with Lot 4 phthalate restrictions checked on a batch basis. Insulation resistance after 1,000 h at 85°C/85% RH per IEC 60068-2-78 should be verified on the final housing geometry, not on a standard plaque, because surface contamination and mould release can produce leakage paths that are not captured by the material datasheet.
Because dilute sodium hypochlorite residuals attack acetal bushings and generate brittle POM failures in municipal water treatment skids, fixed-displacement diaphragm pump volutes and injector bodies are switched to Rilsan BZM 23 G9 where 0.5–2.0 ppm free chlorine residuals at 20–40°C create oxidative stress. In 10% sodium hypochlorite at 40°C for 28 days under ISO 175, the material typically shows mass change below 0.5% and tensile strength retention above 90%, but concentrated hypochlorite above 12% at temperatures above 50°C is an operational boundary because oxidative surface microcracking and notch sensitivity increase with glass-fibre orientation. The 23% short glass loading raises burst pressure of a 3 mm wall pump volute to approximately 20–25 bar at 23°C, and the fibre network reduces creep under cyclical pressure spikes from 0–10 bar at 60°C. Moulding practice for these parts uses a 20:1 L/D screw with a compression ratio of 2.2:1, screw speed below 150 rpm to limit fibre attrition, and melt temperature from 250°C to 270°C. Fibre length retention above 0.4 mm is the critical quality variable; excessive screw speed or back pressure above 1.5 MPa can shorten number-average fibre length and reduce notched Charpy impact from the typical 10–15 kJ/m² range toward 8 kJ/m² under ISO 179/1eA. The finished valve body and pump casing are often post-conditioned in 80°C water for 24 h before dimensional inspection, because PA11 reaches most of its service moisture growth of 0.1–0.3% within the first 48 h and this step prevents later seal-groove shifting in service. Incompatible service fluids include strong mineral acids at pH below 2 at elevated temperature, phenolic process streams, and concentrated oxidising acids; published data for this specific grade in such environments is limited and end-use qualification is required.
Above the waterline on offshore production platforms, junction-box retention brackets, cable cleats, and bend-stiffener retainer collars are moulded from Rilsan BZM 23 G9 because salt spray, UV, and constant wind pressure impose combined creep and corrosion demands that unfilled PA11 cannot meet. The glass fibre phase raises flexural modulus under ISO 178 to 4,500–5,500 MPa and holds creep under 20 MPa at 60°C to a lower strain than unfilled PA11, while the PA11 matrix resists hydrolysis better than PA6 or PA66 in continuous 3.5% NaCl exposure per ISO 175 at 40°C for 28 days, with tensile strength retention above 85%. Natural unpigmented grades are restricted to short-term outdoor exposure or must be painted because UV radiation under ISO 4892-2 can oxidise a surface layer of 0.03–0.05 mm after 1,000 h; black UV-stabilised variants are preferred for continuous service above 60 months. Thick-section clamps above 6 mm require a reduced cooling rate and a mould temperature of 60–70°C, with pack pressure sustained for 15–20 s and post-mould annealing at 120°C for 2 h to suppress residual stress cracking at -20°C under ISO 179/1eA notched impact testing. The terminal clamp geometry includes integrated nut pockets and is specified to retain 1.5 kN on a steel bolt boss without cracking; the boss diameter must be at least 2.5 times the thread diameter to prevent glass-fibre induced stress concentration at the thread root. Because the material is not flame retardant in this unmodified form, enclosures requiring IEC 60079-7 increased safety for hazardous areas need additional design measures or a flame-retardant variant.
Industrial pneumatic distribution blocks, push-to-connect fitting bodies, and solenoid mounting manifolds use the compound where compressor oil carryover and high humidity rule out PA66 GF30 due to its greater moisture stiffness loss. Under equilibrium moisture at 50% RH and 23°C, PA11 GF23 retains approximately 90% of dry flexural modulus, whereas PA66 GF30 may retain only 60–70% under comparable conditions according to comparative ISO 527-2 data; this differential is the design basis for using the material in 16 bar circuits at 65°C and 80% RH. The 23% glass fibre loading supplies enough hoop stiffness to limit diametral expansion in a 2.5–4.0 mm wall manifold to below 0.2% under the same pressure-temperature envelope. The tool is sized with 0.3% flow-direction and 0.6% transverse shrink compensation for a typical 4-cavity hot runner system; valve gates are preferred over open hot tips because the glass-filled melt string can freeze and crack at the gate. Melt temperature is set at 265–275°C, mould at 65°C, injection velocity 60–90 mm/s, and screw decompression at 2–3 mm to prevent drool from the hot runner. After moulding, threads are chase-tapped or formed by unscrewing cores with silicone-free lubricant, since external silicone can impair ultrasonic weld strength. Leak tightness of finished manifold bodies is tested at 24 bar for 30 s under air or water, corresponding to 1.5 times the 16 bar nominal working pressure. Service limitations include continuous contact with ester-based compressor oils above 70°C, which can soften the PA11 matrix, and the use of strong alkaline cleaning baths above pH 12 at elevated temperature.
| Application | Stress condition | Test standard | Acceptance criterion |
|---|---|---|---|
| Fuel vapour flange | Fuel C cyclic, -40°C to 80°C | SAE J1645, ISO 16750-4 | Tensile retention >80%, flatness ≤0.15 mm |
| Electrical enclosure | 85°C/85% RH, 1,000 h | IEC 60068-2-78, IEC 60112 | Insulation resistance stable, CTI ≥600 V |
| Chemical pump volute | 10% NaClO, 40°C, 28 days | ISO 175 | Mass change <0.5%, tensile retention >90% |
| Offshore top-side clamp | 3.5% NaCl, 40°C, 1,000 h | ISO 175, ISO 4892-2 | Tensile retention >85%, surface oxidation <0.05 mm |
| Compressed air manifold | 16 bar at 65°C, 80% RH | ISO 527-2, leak test | Diametral expansion <0.2% |
Cyclic flexural loading at -20°C differentiates Rilsan BZM 23 G9 from PA6 GF30 in alpine touring binding toe plates, mountain bike chainring guards, and climbing ascender frames where low-temperature ductility and long-term creep resistance are tested side by side. Notched Charpy impact at -30°C under ISO 179/1eA remains in the 8–12 kJ/m² range, while flexural modulus under ISO 178 reaches 4,500–5,500 MPa, which limits deflection in a 4 mm thick binding plate under 1 kN cyclic load to below 0.2 mm over 5,000 cycles in laboratory fixtures. The semi-ductile failure mode reduces the brittle fracture risk in snap hooks, rope guides, and drone armatures that must pass cold-soak impact after IEC 60068-2-1 storage at -40°C for 4 h. Moulding of structural inserts from this compound is performed with injection velocity of 100–150 mm/s to fill before the glass-rich skin freezes, while melt temperature is capped at 280°C because higher settings accelerate thermal degradation and yellowing in natural grades. A mould temperature of 80°C improves surface finish and shortens gate freeze time by 10–15% but increases transverse post-mould shrinkage by approximately 0.1 percentage point, so dimensional checks on the fully crystallised part are taken after 24 h at 23°C and 50% RH. Overmoulding with unfilled PA11 is feasible because the polymer backbone is identical, but the glass-filled substrate must be preheated to 80°C before the second shot to prevent a weak interface at the glass-rich surface. Published data on overmould bond strength for this specific grade is limited; lap shear specimens should be tested per ISO 527-2 on each tool rebuild.
Competitive Arkema Rilsan BZM 23 G9 Nylon 11, 23% Glass Fiber Filled 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!
Arkema Rilsan BZM 23 G9 is a 23% glass-fiber-reinforced polyamide 11 injection-molding compound supplied in black pellet form. The base resin is synthesized from 11-aminoundecanoic acid, yielding a long-chain aliphatic polyamide that exhibits lower equilibrium moisture uptake than PA6 and PA66 when conditioned at 23 °C and 50% relative humidity under ISO 62. The grade is distinguished within the Rilsan PA11 portfolio by its glass fiber mass fraction, which is quoted as 23% by weight. This loading shifts the mechanical response from ductile yielding to semi-brittle fracture under tensile loading and raises the heat deflection temperature under load to a typical band of 145–165 °C at 1.80 MPa when tested according to ISO 75-2/A. The compound is used for injection-molded components requiring hydrocarbon resistance, low moisture-driven dimensional change, and improved stiffness relative to unfilled PA11. Published data for continuous high-temperature service above 150 °C in oxidative environments is limited, and operating boundaries must be validated against the specific aggressive medium.
The glass fiber is incorporated as chopped strands with a nominal length of approximately 3.0 mm before compounding. After passing through a co-rotating twin-screw extruder with an L/D ratio of 36:1 to 44:1, the residual fiber length in the pellet is generally reduced to 250–450 µm because of shear-induced filament fracture. This reduction must be accounted for in mechanical property predictions because short-fiber reinforcement models based on nominal as-supplied fiber length overestimate stiffness retention in molded parts. The polymer matrix is a polyamide 11, meaning the amide group density is lower than in short-chain polyamides; this is the structural basis for the moisture absorption figure of 0.16–0.25% after 24 h immersion at 23 °C under ISO 62. The glass transition temperature of dry PA11 is approximately 40–50 °C, but the compound is typically used above that temperature in the dry-as-molded state where the glass-reinforced modulus remains determined primarily by fiber efficiency and matrix crystallinity.
| Property | Test method | Typical band | Unit |
|---|---|---|---|
| Density | ISO 1183-1 | 1.19–1.23 | g/cm³ |
| Tensile modulus | ISO 527-2/1A | 4,800–5,600 | MPa |
| Tensile strength at break | ISO 527-2/1A | 85–105 | MPa |
| Elongation at break | ISO 527-2/1A | 2.5–4.5 | % |
| Flexural modulus | ISO 178 | 4,200–5,000 | MPa |
| Notched Charpy impact strength | ISO 179/1eA | 7–12 | kJ/m² |
| Heat deflection temperature at 1.80 MPa | ISO 75-2/A | 145–165 | °C |
| Melting peak temperature | ISO 11357-3 | 186–192 | °C |
| Water absorption after 24 h at 23 °C | ISO 62 | 0.16–0.25 | % |
| Mold shrinkage, parallel | ISO 294-4 | 0.2–0.5 | % |
| Coefficient of linear thermal expansion, parallel | ISO 11359-2 | 3.0–4.5 × 10⁻⁵ | K⁻¹ |
Property consistency in molded parts depends on flow-induced fiber orientation. In a tensile-bar cavity with a 2.0 mm wall thickness, longitudinal fiber alignment in the skin layer produces a tensile modulus commonly near the upper end of the band, while cross-flow orientations in large flat surfaces can reduce the effective modulus by 10–20% relative to the datasheet value. Design calculations should therefore use orientation-dependent moduli generated from mold-filling simulation rather than a single isotropic modulus. The notched Charpy value is also affected by gate location: specimens cut at weld lines can fall below 6 kJ/m² even when the bulk value is above 10 kJ/m², reinforcing the need for destructive part-level validation.
Melt processing starts with desiccant drying to a residual moisture level below 0.10% by weight. Typical drying conditions of 80–90 °C for 4–6 h in a dry-air dryer with a dew point below −30 °C are sufficient for initial moisture levels below 0.20%. The melt temperature at the nozzle should be maintained within 250–280 °C for thin-wall sections; lower settings between 240 °C and 260 °C may reduce thermal degradation in thick sections but raise injection pressure. Mold surface temperatures in the range 40–80 °C are required to obtain reproducible crystallinity and dimensional stability. Gate dimensions should be enlarged relative to unfilled PA11 by approximately 25% to accommodate the increased viscosity and reduce gate-freeze restrictions. On production-scale injection molding machines with clamp forces from 80 t to 250 t, screw recovery times are typically 15–35% longer than for unfilled PA11 at the same shot size due to filler-induced viscosity increase and reduced bulk density.
Shrinkage is anisotropic because of the reinforcing fiber. In the flow direction, mold shrinkage is typically near the lower end of the band, while transverse shrinkage can approach 0.4–0.5%, producing differential movement in multi-gated parts. Cavities with wall-thickness transitions greater than 1.5 mm or abrupt gate-area restrictions can generate warpage that cannot be corrected by packing pressure alone. Cooling design should maintain cavity surface temperature variation below 10 °C across the part to avoid non-uniform crystallization and stress accumulation.
At knit lines, fiber orientation perpendicular to the flow front reduces tensile strength by 20–40% relative to the bulk value measured on ISO 527-2/1A specimens. Because the matrix is PA11, the notch sensitivity of the compound is lower than that of glass-filled PA66 in notched Charpy testing, but weld-line regions remain the limiting design feature. Tensile elongation at break falls below 5%, so ribbed parts should avoid abrupt transitions with radii below 0.5 mm. Failure under impact in dry-as-molded parts occurs by fiber pull-out and matrix microcracking, whereas moisture-conditioned parts shift to more ductile matrix deformation. The practical strain limit for long-term creep-loaded parts is approximately 0.8–1.2% when assessed under ISO 899-1 at 23 °C; creep rupture data at elevated temperature above 100 °C in polar fluids is limited.
Chemical compatibility is influenced by the PA11 matrix rather than the glass reinforcement. The compound withstands aliphatic hydrocarbons, diesel fuel, lubricating oils, and zinc chloride brine at moderate temperatures, but the glass fiber increases surface wicking along fiber-matrix interfaces, making the material more sensitive to strong aqueous acids and oxidizing media than unfilled PA11. Long-term immersion in hot water above 80 °C can hydrolytically degrade the polyamide 11 matrix; the rate is lower than for PA66 at equivalent temperature, but pressure-bearing components should be derated by at least 30% when operating continuously in water-glycol mixtures above 60 °C. The compound is not recommended for contact with phenols, concentrated sulfuric acid, or chlorinated solvents under stress, because environmental stress cracking can occur. Regulatory documentation commonly references REACH and RoHS compliance; specific food-contact suitability must be verified against the grade’s manufacturer certification and the intended use conditions under FDA 21 CFR 177.1500 or corresponding regional regulations.
Replacing unfilled PA11 with Rilsan BZM 23 G9 is technically justified when the design stress requires tensile modulus above 4,000 MPa and the allowable creep strain in service is below 1.0%. The glass-filled grade raises heat deflection temperature from approximately 55–60 °C to 145–165 °C at 1.80 MPa, allowing structural components to survive paint-bake cycles and under-hood thermal loads without gross distortion. However, the reinforcement reduces elongation at break from greater than 100% for unreinforced PA11 to below 5%, so snap-fit geometries designed for high arm deflection must be re-evaluated. The coefficient of linear thermal expansion falls by roughly 40–60% in the flow direction relative to unfilled PA11, reducing differential stress in metal-overmolded assemblies. Where the application depends on impact energy absorption rather than stiffness, unfilled or impact-modified PA11 grades provide higher notched Charpy values, often exceeding 20 kJ/m², compared with the 7–12 kJ/m² band of the glass-filled grade.
Comparative data for glass-fiber-reinforced polyamides illustrate the positioning of Rilsan BZM 23 G9. PA66 with 23% glass typically offers higher dry modulus and higher heat deflection temperature, but its saturated moisture uptake can exceed 2.0% and its density is approximately 1.30 g/cm³, roughly 6–8% higher than PA11-GF23. PA12 with similar glass loading shows lower moisture uptake but typically lower tensile strength retention at temperatures above 120 °C. Unfilled PA11 grades retain higher ductility and chemical resistance but provide insufficient modulus for dimensionally constrained parts. These differences arise from amide group density, chain length, and the resulting hydrogen-bonding capacity of the matrix; glass-fiber content alone does not predict performance.
Because the 23% glass fiber loading raises melt viscosity, the maximum residence time at melt temperature should not exceed 10 min at 280 °C; longer residence times produce visible surface silvering and measurable loss in notched Charpy impact strength. In hot-runner systems, the manifold and drops should be sized for shear rates below 40,000 s⁻¹ to limit fiber attrition and local temperature overshoot. Experience from production-scale molding with a 120 t machine using a 35 mm screw diameter and 20:1 L/D plastication unit indicates that a cushion of 3–6 mm and a back pressure of 2–5 MPa reduce shot-to-shot density variation below 0.3%. Fiber orientation in the skin layer follows the filling direction, while the core layer becomes transverse to flow in thick sections, producing anisotropic shrinkage that must be captured in mold design. Draft angles below 0.5° increase ejection force and may produce microcracking around rib roots in high-volume production.
Production experience with automotive connectors and fluid-system housings indicates that molded parts in Rilsan BZM 23 G9 retain dimensional stability after repeated thermal cycling between −40 °C and 125 °C when the design eliminates sharp internal corners and maintains a maximum wall-thickness variation of 1.5 mm. For applications involving continuous exposure to hot diesel fuel above 90 °C, published long-term data for this specific configuration is limited, so component validation under ISO 22088-3 environmental stress cracking is required. The presence of glass fiber at the surface may increase wear on mating polymer components with hardness below HRC 20; in such cases the contact partner should be hardened or replaced with a non-abrasive grade. These constraints define the operational boundary of the product rather than a limitation of the PA11 matrix alone.