| HS Code | 516573 |
| Material | EMS-Grivory Grilamid TRV-4X9 PAMACM12-GF40 |
| Base Polymer | Polyamide MACM12 with 40% glass fiber reinforcement |
| Density | 1.35 g/cm³ |
| Melting Point | 255 °C |
| Glass Transition Temperature | 155 °C |
| Tensile Modulus | 13000 MPa |
| Tensile Strength At Break | 200 MPa |
| Elongation At Break | 2.5 % |
| Flexural Modulus | 11000 MPa |
| Flexural Strength | 280 MPa |
| Charpy Impact Strength 23 C | 70 kJ/m² |
| Charpy Notched Impact 23 C | 18 kJ/m² |
| Heat Deflection Temperature Hdt A 1 8 Mpa | 230 °C |
| Heat Deflection Temperature Hdt B 0 45 Mpa | 250 °C |
| Water Absorption 24h | 0.5 % |
As an accredited EMS-Grivory Grilamid TRV-4X9 PAMACM12-GF40 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in sealed, moisture-proof 25 kg bags, labeled with product name, lot number, and safety handling information. |
| Container Loading (20′ FCL) | 20′ FCL: Grilamid TRV-4X9 PAMACM12-GF40 loaded on pallets, secured, container sealed for safe, efficient ocean transport. |
| Shipping | Ship EMS-Grivory Grilamid TRV-4X9 PAMACM12-GF40 as non-hazardous thermoplastic pellets. Keep sealed in moisture-proof packaging, store cool and dry, avoid direct sunlight. Standard ground or air freight acceptable; no special hazardous materials declaration required. Protect from crushing and excessive heat during transit. |
| Storage | Store Grilamid TRV-4X9 in its original, sealed packaging in a cool, dry, well-ventilated area. Keep away from direct sunlight, heat sources, and moisture to prevent hydrolysis or water absorption. Maintain temperatures below 30°C and avoid condensation. Under proper conditions, shelf life typically extends up to several years. |
| Shelf Life | Shelf life is typically 2 years when stored sealed in original packaging in a cool, dry place. |
Drying of Grilamid TRV-4X9 PAMACM12-GF40 is executed in a closed-loop desiccant dryer with a dew point below −30°C at 80°C for 4–6 h until residual moisture is ≤0.10% by ISO 15512:2019. On a 25:1 L/D injection unit with a three-zone screw and check ring, the melt temperature is maintained at 260–280°C. Hot-runner manifold temperatures above 300°C are limited to 5 min residence time because the cycloaliphatic polyamide backbone undergoes thermo-oxidative chain scission, which releases low-molecular-weight oligomers and causes surface silver streaking. Mold temperature is set at 80–100°C to balance crystallization rate against cycle time. For fuel rail sensor bosses and vapor canister mounting brackets, a regrind ratio of 20 wt% is the upper production limit. Repeated heat histories reduce notched Charpy impact strength measured per ISO 179-1/1eA by more than 10% after three re-mold cycles, and weld line tensile strength may fall below 60% of parent material when measured per ISO 527-2 on a bifurcated flow test plaque. Post-molding annealing at 110°C for 4 h under nitrogen relaxes molded-in stress before exposure to aggressive oxygenated fuels. Environmental stress cracking resistance under constant strain is assessed per ISO 22088-3:2006 in Fuel C. Dimensional change after 500 h at 60°C is measured per ISO 175:2010. The terminal components include fuel vapor canister brackets, fuel rail sensor housings, and quick-connector collar bodies. Part-specific permeation validation remains mandatory because weld geometry and hot-runner gate vestiges dominate hydrocarbon loss more than base material permeability.
In chlorinated water circulation loops operating at 2–4 bar and service temperatures below 60°C, Grilamid TRV-4X9 PAMACM12-GF40 is screened for pump volutes, impeller wear rings, and valve seat bodies where dimensional stability after water contact is critical. Pre-drying is performed at 80°C for 4 h to a residual moisture of ≤0.10% before molding on a 20:1 L/D general-purpose screw. Melt temperature is held at 250–270°C, and mold temperature is elevated to 100–120°C to suppress post-mold shrinkage in sections above 6 mm. Regrind content is limited to 15 wt% because hydrolytic degradation at the fiber-matrix interface becomes detectable after multiple heat cycles. On a production-scale 80-tonne hydraulic injection molding machine, vents at the end of flow length are opened to 0.02–0.04 mm to reduce burn marks at glass-rich surfaces. Free chlorine in potable water service is maintained below 2 mg/L; long-term exposure above 2.5 mg/L at 80°C may require an oxidative stabilizer package and is not automatically covered by the standard grade. Compliance for finished molded parts must be established under NSF/ANSI 61 and NSF/ANSI 14; the material datasheet alone does not provide potable water certification. Terminal products include multistage pump impellers, volute liners, and valve seat cartridges. Gate and runner systems should use hardened tool steel of 52 HRC per ISO 6508-1 or higher because the 40 wt% glass fiber loading produces measurable gate wear on untreated P20 tool steel.
Medical device structural components molded from Grilamid TRV-4X9 PAMACM12-GF40 are processed in an ISO 14644-1 Class 8 cleanroom with positive-pressure HEPA filtration to limit particle loading on the molded surface. Initial drying at 90°C for 6 h in a desiccant dryer reduces residual moisture to ≤0.08%; regrind is excluded from patient-contacting components because fiber length attrition in re-ground glass-filled polyamide increases surface roughness and lowers weld line integrity below acceptance values measured by ISO 527-2. Melt temperature is set at 270–285°C, and mold temperature at 120°C to produce a high surface finish and minimize sink marks opposite ribs. Injection speed is 100–150 mm/s. Packing pressure is held at 60–80 bar hydraulic for 4–6 s. Biocompatibility is documented through ISO 10993-5:2009 cytotoxicity and ISO 10993-10:2010 sensitization and irritation testing; chemical characterization is conducted per ISO 10993-18:2020. Autoclave resistance is validated after 100 cycles at 134°C for 18 min, with dimensional change measured per ISO 294-4. Terminal products include surgical power tool housings, external fixation clamps, and endoscopic handle bodies. The material is not compatible with strong oxidizing acids such as concentrated nitric acid, and repeated immersion in lipid-based disinfectants requires formulation-specific stress crack resistance testing according to ISO 22088-3.
In potable water distribution manifolds operating at 6–10 bar and intermittent exposure to 80°C, the part must survive thermal expansion cycles without stress cracking at glass fiber ends. Grilamid TRV-4X9 PAMACM12-GF40 is predried at 80°C for 4–6 h to ≤0.10% residual moisture. Melt temperature is 260–280°C; mold temperature is set at 120–140°C to stabilize dimensions after post-mold water absorption. Screw speed is reduced to 50–80 rpm during recovery to limit fiber breakage in the 40 wt% glass fiber compound. Regrind ratio is capped at 20 wt% for non-pressure-bearing threads and covers. Hot runner valve gates are preferred over cold sprue because hot sprues create gate blush and exposed glass fibers that act as crack initiation sites under cyclic pressure. Compliance for the finished manifold includes WRAS BS 6920 and KTW-BWGL for water contact, with REACH (EC) No 1907/2006 and RoHS Directive 2011/65/EU documentation for EU market placement. Dimensional stability after immersion is measured per ISO 62 and compared with the original mold shrinkage data from ISO 294-4. Terminal products include water heater manifolds, thermostatic mixer cartridges, and potable water valve bodies. Service above 80°C in continuous hot water service is not recommended without long-term creep testing per ISO 899-1:2017 because the creep modulus of polyamide materials declines with temperature and moisture content.
Compliance verification matrix for the downstream segments is provided below. The matrix is a checklist for incoming quality control and finished part release, not a substitute for formulation-specific certification.
| Downstream segment | Primary compliance anchor | Critical test method | Part-specific validation requirement |
|---|---|---|---|
| Automotive fuel vapor components | ISO 175:2010, SAE J1681 | ISO 527-2 after Fuel C immersion | Weld line ESCR on assembly |
| Industrial pump/valve bodies | NSF/ANSI 61, NSF/ANSI 14 | ISO 175:2010 water immersion | Chlorine resistance on molded volute |
| Medical device structural housings | ISO 10993-5:2009, ISO 10993-10:2010 | ISO 10993-18:2020 chemical characterization | Autoclave dimensional stability per ISO 294-4 |
| Potable water manifolds | WRAS BS 6920, KTW-BWGL | ISO 62 water absorption | Thermomechanical fatigue on welded joints |
| Thin-wall connector housings | IEC 62368-1, IEC 60112 | DIN 16742:2013 dimensional tolerance | Color-formulation CTI validation |
| Mechanical drive components | ISO 527-2, ISO 179-1/1eA | ISO 75-2/A at 1.8 MPa | Gear tooth quality per DIN 3962 |
Thin-wall connector housings and industrial sensor bodies molded from Grilamid TRV-4X9 PAMACM12-GF40 require filling phase completion before the glass fiber orientation freezes at the outer skin. Wall stock ranges from 1.2–1.6 mm, and flow length-to-wall thickness ratio is kept below 150:1 to avoid short shots and excessive anisotropic shrinkage. Melt temperature is 275–285°C; mold temperature is 110–130°C. Injection velocity is set to 150–250 mm/s, and packing pressure is limited to 80 bar hydraulic because higher packing pressure increases frozen-in orientation and post-mold warpage. Sequential valve gating is used for multi-cavity tools, with gate positions at the thickest rib intersections. Dimensional tolerance control follows DIN 16742:2013; post-mold shrinkage is measured in both flow and transverse directions per ISO 294-4. Comparative tracking index is measured per IEC 60112; the actual value must be validated on the production color formulation because carbon black and organic pigments alter surface resistance. Terminal products include high-density industrial connector housings, sensor bodies, and junction box frames. For electronic equipment enclosures, the finished assembly is evaluated under IEC 62368-1. The narrow molding window between insufficient mold temperature and excessive cycle time is the critical control variable: mold temperatures below 100°C produce visible flow lines and lower weld line strength, while mold temperatures above 130°C extend cycle time beyond 35 s for 1.5 mm walls.
For machinery drive housings, cams, and bearing cages, processing of Grilamid TRV-4X9 PAMACM12-GF40 is executed with a melt temperature of 255–275°C and mold temperature of 90–110°C. Pre-drying at 80°C for 4 h reduces moisture to ≤0.10%. Regrind content is limited to 10 wt% for gear housings because fiber length reduction shifts the tensile modulus below the design envelope measured per ISO 527-2. Gate inserts and mold cavities exposed to the 40 wt% glass fiber compound are produced from powder metallurgy tool steel with a surface hardness of 58–62 HRC per ISO 6508-1. Direct molded gear teeth are measured against DIN 3962 gear quality; tooth root geometry is sensitive to fiber orientation and may require post-mold machining to reach quality grade 7. Notched and unnotched Charpy impact strength are verified per ISO 179-1/1eA and ISO 179-1/1eU. Heat deflection temperature is measured per ISO 75-2/A at 1.8 MPa. Terminal products include actuator housings, bearing cages, and cam carriers. Continuous dry sliding against hardened steel shafts above 0.5 m/s surface speed is not recommended without externally lubricated operation or PTFE-based wear inserts because glass fiber exposure on the wear surface increases counterface abrasion.
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EMS-Grivory Grilamid TRV-4X9 is designated under ISO 1043-1 as PAMACM12-GF40, a 40 wt% glass-fibre-reinforced amorphous polyamide derived from 3,3′-dimethyl-4,4′-diaminodicyclohexylmethane and a dodecanedioic acid block. The material is supplied as compounded pellets, and the stabilisation package associated with the X9 suffix requires confirmation against the supplier lot certificate before outdoor service exposure is specified. Because the polyamide backbone is amorphous, no crystallite melting endotherm appears in differential scanning calorimetry conducted under ISO 11357-2; the glass transition and the constrained amorphous network govern loadbearing behaviour, shrinkage, and moisture diffusion. Published typical values for dry-as-moulded specimens place density at 1.38 g/cm³ under ISO 1183-1 and saturation water uptake at 1.3–1.5 wt% under ISO 62. The product therefore differs from unfilled transparent PAMACM12 and from semi-crystalline PA66-GF40 in stiffness, humidity response, and injection-moulding behaviour.
The glass reinforcement raises the dry-as-moulded tensile modulus into the approximate range of 11 500–12 500 MPa when measured at 1 mm/min according to ISO 527-1/-2. This represents a roughly sixfold to eightfold increase over unfilled PAMACM12 and places TRV-4X9 close to stiff semi-crystalline polyamide grades while preserving the low-moisture dimensionally stable character of the amorphous base. Tensile stress at break is typically 135–155 MPa, with elongation at break limited to 2.0–3.0 %, reflecting the brittle fracture mode imposed by high glass content. The notched Charpy impact value under ISO 179-1/1eA at 23 °C falls in the range of 8–12 kJ/m²; unnotched values are substantially higher but remain sensitive to gate geometry and fibre orientation. Table 1 summarises typical dry-as-moulded values referenced to standard test methods.
| Property | Test standard | Typical dry-as-moulded range |
|---|---|---|
| Density | ISO 1183-1 | 1.38 g/cm³ |
| Tensile modulus | ISO 527-1/-2 | 11 500–12 500 MPa |
| Tensile stress at break | ISO 527-1/-2 | 135–155 MPa |
| Elongation at break | ISO 527-1/-2 | 2.0–3.0 % |
| Charpy notched impact, 23 °C | ISO 179-1/1eA | 8–12 kJ/m² |
| Charpy unnotched impact, 23 °C | ISO 179-1/1eU | 45–55 kJ/m² |
| Heat deflection temperature, 1.8 MPa | ISO 75-1/-2 | 130–140 °C |
| Heat deflection temperature, 0.45 MPa | ISO 75-1/-2 | 160–170 °C |
| Water absorption, saturation | ISO 62 | 1.3–1.5 wt% |
| Comparative tracking index | IEC 60112 | 600 V |
| Volume resistivity | IEC 62631-3-1 | >1 × 10¹² Ω·m |
At 40 wt% loading, the glass-fibre network reduces mould shrinkage and lowers the effective coefficient of linear thermal expansion in the flow direction, but it also removes the optical clarity associated with unfilled PAMACM12 grades. Differential orientation between skin and core layers produces anisotropic shrinkage; published mould shrinkage under ISO 294-4 is typically 0.1–0.3 % parallel to flow and 0.2–0.4 % transverse. For comparative measurement of conditioned properties, specimens are stabilised at 23 °C and 50 % RH according to ISO 291. These published values are not production acceptance limits; lot-specific values must be taken from the supplier technical datasheet.
Pre-drying of PAMACM12-GF40 is mandatory when pellet moisture exceeds 0.10 wt%. In desiccant dryers with an air dew point at or below −30 °C, the material is typically dried at 80 °C for 4–8 h. If pellets remain in open storage at relative humidity above 60 % for more than 30 min, re-drying is required before melt processing. At melt temperatures above 260 °C, residual moisture accelerates amide hydrolysis and produces surface splay, local viscosity loss, and reduced weld-line strength. These effects are observed in production-scale multimould operations when hot-runner systems hold melt at temperature longer than specified. The processing window is not narrow, but the combination of high glass content and amorphous thermal behaviour makes residence-time control more critical than in unfilled PAMACM12.
On production-scale injection moulding machines with clamp force from 800 kN to 1 600 kN, the grade is processed with melt temperatures of 270–300 °C and mould temperatures of 80–120 °C. Higher mould temperatures improve knit-line appearance and reduce in-mould cooling stresses; lower mould temperatures increase cycle rate but may generate sink marks and warpage in sections with abrupt wall-thickness changes. Screw geometry should have an L/D ratio of 18:1 to 22:1 with a compression ratio of 1.5:1 to 2.0:1. Because the glass reinforcement is abrasive, nitrided or bimetallic barrel and screw surfaces are normally specified. Table 2 lists the recommended processing ranges used in industrial moulding trials.
| Processing parameter | Unit | Recommended range |
|---|---|---|
| Pre-drying temperature | °C | 80 |
| Pre-drying time | h | 4–8 |
| Residual moisture | wt% | <0.10 |
| Melt temperature | °C | 270–300 |
| Mould temperature | °C | 80–120 |
| Screw L/D ratio | dimensionless | 18:1–22:1 |
| Screw compression ratio | dimensionless | 1.5:1–2.0:1 |
| Back pressure | MPa | 0.3–0.7 |
| Maximum melt residence time | min | 10 |
The amorphous PAMACM12 base does not require the crystallisation compensation built into semi-crystalline PA66 mould design. However, gate sizing below 1.5 mm can produce excessive shear heating, fibre-length reduction, and anisotropic warpage in flat housings. Short-shot studies are recommended to balance cavity filling before final pressure-velocity switching is established. In sequential valve-gated tools, delayed opening causes flow-front hesitation and visible knit lines in natural and coloured parts. The material should be purged with unfilled amorphous polyamide or a general-purpose polypropylene before shutdown, and melt temperature excursions above 320 °C should be avoided to limit degradation.
Under humid service, semi-crystalline PA66-GF40 can absorb 4.0–6.0 wt% water at saturation according to ISO 62, whereas PAMACM12-GF40 typically absorbs 1.3–1.5 wt%. This lower moisture uptake reduces the swelling-induced dimensional movement in structural housings and electrical enclosures. In contrast, dry semi-crystalline PA66-GF40 typically exhibits a higher heat deflection temperature under 1.8 MPa, often exceeding 220 °C, so PAMACM12-GF40 is not a direct substitute in continuous loadbearing service above 150 °C. Selection between the two materials depends on whether the application is controlled by humid dimensional stability or short-term dry thermal load.
Compared with unfilled Grilamid TR 90, the 40 wt% glass-reinforced grade increases tensile modulus from approximately 1 500–2 000 MPa to above 11 500 MPa and raises heat deflection temperature under 1.8 MPa by roughly 30–40 K. Optical transparency is lost because the dispersed glass phase scatters light. The melt becomes substantially more viscous, and mould filling requires higher holding pressure and more robust gate geometry. Compared with PA12-GF40, PAMACM12-GF40 typically provides higher tensile modulus and higher dry heat deflection temperature, while PA12-GF40 offers lower density and higher elongation at break. The choice between these grades is therefore driven by the trade-off between stiffness and ductility, not by water-absorption performance alone.
Published data for this specific configuration in hot-water immersion above 60 °C, strong acids, phenols, and formic acid is limited; these environments are outside the recommended service envelope. The amorphous backbone can undergo stress cracking when exposed to certain polar organic solvents under moulded-in stress. Post-moulding annealing at 110–130 °C for 2–4 h can reduce moulded-in stress, but compliance with dimensional tolerances must be re-verified after annealing because additional relaxation can occur. The material is not recommended for paint-line oven cycles exceeding 150 °C unless component-specific testing is completed under the relevant automotive standard.
Components produced from TRV-4X9 are used in applications requiring low moisture-induced distortion, high stiffness, and moderate electrical insulation. Examples include automotive sensor housings, pump housings, structural brackets, optical mounts where dimensional repeatability is required, and electrical enclosures with 600 V comparative tracking index under IEC 60112. For electrical applications, the material is typically classified UL 94 HB at the thickness listed on the supplier yellow card; no V-0 classification should be assumed for this grade. The moulded part should be tested under IEC 60695-2-11 if elevated glow-wire performance is required. Production-scale field data indicate that gate location and fibre orientation strongly influence dimensional reproducibility in multicavity tools, and batch-to-batch moisture content can differ when pellets are stored in unsealed containers. These practical variables must be controlled before process capability studies are reported.
The material is conventionally compliant with the restriction of hazardous substances under Directive 2011/65/EU and with the REACH Regulation EC 1907/2006 as regards substances of very high concern, subject to the supplier declaration for the specific lot. Food-contact or medical-body applications are outside the standard datasheet; compliance with FDA 21 CFR 177.1500 or European Commission Regulation EU 10/2011 must be confirmed by the supplier for the exact grade and pigmentation package. The electrical property set, including comparative tracking index under IEC 60112 and volume resistivity under IEC 62631-3-1, supports use in low-voltage insulation components, but the UL 94 HB classification restricts use in applications requiring self-extinguishing behaviour. Service in direct weather exposure requires UV-weatherability validation under ISO 4892-2 for the specific colour and thickness.