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EMS-Grivory Grilamid TR 90 TL Nylon 12, Impact Modified, Dry

    • Product Name: EMS-Grivory Grilamid TR 90 TL Nylon 12, Impact Modified, Dry
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 846396
    Density 1.04 g/cm³
    Water Absorption 24h At 23 C 0.3 %
    Tensile Modulus Dry 1800 MPa
    Tensile Yield Stress Dry 50 MPa
    Tensile Yield Strain Dry 4 %
    Nominal Strain At Break Dry 120 %
    Flexural Modulus Dry 1700 MPa
    Charpy Impact Strength 23 C No break
    Charpy Notched Impact Strength 23 C 35 kJ/m²
    Izod Notched Impact Strength 23 C 30 kJ/m²
    Heat Deflection Temperature 1 80 Mpa 110 °C
    Glass Transition Temperature 140 °C

    As an accredited EMS-Grivory Grilamid TR 90 TL Nylon 12, Impact Modified, Dry factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Available in 25 kg sealed, moisture-proof bags, preserving the dry, impact-modified Grilamid TR 90 TL nylon 12 pellets.
    Container Loading (20′ FCL) 20′ FCL loaded with dry nylon 12 impact-modified pellets, packed in sealed bags, secured safely for transport.
    Shipping This material ships as impact-modified nylon 12 pellets in sealed, moisture-resistant packaging. Keep containers tightly closed to prevent moisture absorption. Store in a cool, dry area away from heat and ignition sources. Standard industrial handling applies. No special shipping classification for dry polymer. Ensure proper labeling and documentation.
    Storage Store Grilamid TR 90 TL in its original, tightly sealed container in a cool, dry area away from direct sunlight and heat sources. Keep the resin protected from moisture absorption, as humidity degrades processing quality. After opening, purge with dry air or reseal immediately. Use within the manufacturer’s stated shelf life.
    Shelf Life Provided proper storage conditions, the shelf life is typically indefinite, but should be used within 2 years.
    Application of EMS-Grivory Grilamid TR 90 TL Nylon 12, Impact Modified, Dry

    Injection moulding of corrective optical frame fronts from Grilamid TR 90 TL is run on 60–120 t hydraulic toggle presses with 22–35 mm diameter plasticating screws and L/D 18:1–22:1. The dry-as-supplied pellets are transferred from moisture-barrier packaging into a dehumidifying hopper dryer set at 80–90°C with a dew point below −30°C; when ambient relative humidity exceeds 60%, re-drying for 4–6 h is mandatory because the impact-modified polyamide hydrolyses during plastication above 240°C. Residual moisture above 0.10 wt% is measured by ISO 15512:2019 and manifests as splay, silver streaks, or gate blush. The melt temperature window is 240–270°C at the nozzle, and nozzle temperature is kept below 280°C to avoid yellowing; melt residence time above 260°C should not exceed 5 min. Mould temperature is maintained at 50–80°C with pressurised water units using turbulent flow; below 50°C the gate freezes before packing is complete, leaving sink marks at temple-arm bosses and bridge curvature deformation. Impact-modified TL grades retain a notched Charpy impact above 10 kJ/m² at 23°C when tested per ISO 179-1/1eA:2010. At wall thicknesses below 1.2 mm, the hinge boss inner radius is kept above 0.5 mm because sharp corners produce stress concentration during hinge insertion. Hinge insertion is performed after a 4 h stress-relief anneal at 60°C in a circulating air oven; unannealed frames show higher crack occurrence in 0.8 mm temple arms when metal hinge barbs are press-fitted. The density of 1.00 g/cm³ is determined by ISO 1183-1:2019, and optical transmittance above 90% at 2 mm thickness is measured by ASTM D1003-21; maintaining these values requires a melt cushion of 3–6 mm. Compliance for finished frames references ISO 12870:2016 clause 5.2 for dimensional stability and clause 5.6 for nickel release; perspiration resistance is screened under ISO 175:2010 at 37°C for 24 h with artificial perspiration. Blend additions of amine-based impact modifiers or amine-slaked hindered amine stabilizers are incompatible; they cause gel specks and localised molecular weight degradation in hot-runner manifolds.

    What Limits Lipid and Autoclave Performance in Transparent Fluid Management Connectors?

    Transparent male/female Luer connectors, access ports and syringe funnels are shot on 30–80 t hybrid injection moulding machines with 18–25 mm screws; for shot weights below 30 g, screw L/D is reduced to 18:1 to avoid prolonged residence time. The process conflict is the narrow window between transparency and impact strength: melt temperature below 240°C leaves haze bands at weld lines caused by the TL impact modifier, while melt temperature above 270°C increases yellowing. Weld lines formed by core pins in through-lumen connectors are tensile tested on split-lumen specimens per ISO 527-2:2012; values below 40 MPa indicate insufficient packing or cold mould walls. Residual stress from unbalanced filling leads to environmental stress cracking after exposure to lipid emulsions, evaluated by the bent-strip method under ISO 22088-3:2003 at 1% strain for 24 h in 20% lipid solution at 37°C. Equilibrium moisture uptake at 23°C and 50% RH is determined per ISO 62:2008 and generally remains below 2.0 wt%; continuous immersion in 37°C deionised water can raise uptake above 5 wt%, producing measurable lumen expansion if parts are not conditioned prior to joining with flexible PVC tubing. Repeated autoclaving at 121°C for 30 min under EN 285:2015 causes progressive yellowing; after 50 cycles, notched impact measured per ISO 179-1/1eA:2010 in sections thinner than 1.0 mm can fall by more than 20%, which is an operational boundary for reusable devices. Biocompatibility for patient-contacting use is established under ISO 10993-1:2018, with cytotoxicity per ISO 10993-5:2009 and irritation per ISO 10993-23:2021; the dry impact-modified formulation is not supplied as a claim-free medical grade. Glutaraldehyde-based cleaning solutions above 2% for more than 60 min are not recommended because carbonyl attack frosts the surface and initiates microcracks at weld lines. Production failure modes include collar cracking after autoclaving when core pin draft angles are below 0.5°; for lumen lengths above 15 mm, draft angles of 0.5–1.0° are used to reduce demoulding stress concentration at the collar base.

    Insert Moulding of Threaded Bosses and Metal-Reinforced Head-Worn Device Structures

    Within automatic moulding cells for head-worn devices, threaded brass or stainless steel bosses are insert-loaded into tool cavities and overmoulded with Grilamid TR 90 TL. The main process discrepancy is thermal expansion mismatch: steel inserts preheated to 80–100°C are required when insert wall thickness exceeds 2.0 mm; ambient inserts produce hoop stress and radial cracks at knurl tips within 24 h at 23°C and 60% RH. Melt is injected at 250–265°C through a heated sprue bushing with a hot-tip temperature of 260°C; packing pressure is held at 60–80 MPa hydraulic for 3–5 s until gate freeze. Mould temperature for insert-bearing cavities is 60–80°C, approximately 10°C higher than for unsupported thin-wall covers. A 10 mm steel insert produces a sink mark depth of 0.03–0.06 mm opposite the flat boss face when a single-stage packing profile is used; a two-stage profile of 70 MPa for 2 s followed by 40 MPa for 4 s eliminates the defect. Screw pull-out force is measured at 25 mm/min; values above 800 N for an M2 brass knurl insert in a 4 mm thick boss require an insert diameter of at least 5.5 mm and a remaining boss wall of 1.5 mm. Adhesion is mechanical only; the insert must be free of mineral oil because oil contamination causes local burn marks and loss of transparency at the knurl. Hardened steel inserts with 0.8 µm Ra surface roughness provide reproducible extraction on the moulding line, while aluminium inserts are avoided due to accelerated wear and heat-sink inconsistency. For eyewear end-products, ISO 12870:2016 clause 5.6 applies to nickel release; for non-eyewear head-worn products, REACH 1907/2006 Annex XVII entry 27 remains the nickel restriction reference.

    Cleaning-in-place validation for transparent beverage dispensing manifolds exposes the moulded components to alternating 0.5% sodium hydroxide at 60°C, 50–200 mg/L free chlorine at 25°C, and citric acid descaling at 70°C. The dry impact-modified PA 12 grade shows lower stress-cracking than polycarbonate in this environment, but only if gate-vestige regions are smooth; a raised valve pin vestige of 0.2 mm acts as a crack initiator and losses occur after 300–500 cycles. Moulding is performed on 100–180 t electric toggle machines using sequential valve gating; the first gate is placed at the central bore and the second gate at the outer flange to prevent gas traps. Melt temperature is 245–265°C and mould temperature is 70°C; the higher cavity surface temperature improves packing and lowers free volume at the gate region. Internal-pressure hydrostatic strength of the assembled fluid-handling component is evaluated under ISO 9080:2012 when the part is categorised as pressure-retaining; published data for this specific configuration in chlorinated water at 60°C is limited, so end-user protocols specify a burst pressure of at least nominal operating pressure. The material does not carry a blanket food-contact statement; compliance with EU 10/2011 for repeated contact would require migration testing with aqueous and fatty simulants according to EN 1186-2:2022 at the intended time-temperature condition. Silicone gaskets are platinum-cured to avoid peroxide residues; bonding to the moulded surface uses atmospheric plasma at a nozzle speed of 50 mm/s, and open time before silicone dispensing is kept below 4 h to avoid hydrophobic recovery.

    When Cold Impact and Optical Clarity Are Specified Together for Sports Equipment

    At service temperatures down to −20°C, impact-modified transparent polyamide components such as binding windows, side plates and brake lever windows are moulded with wall thicknesses of 1.5–3.0 mm. The TL grade retains ductile failure at low temperature when tested per ISO 179-1/1eA:2010 at −30°C; however, optical transmission measured by ASTM D1003-21 can decline if the melt is overheated to reduce flow resistance. Moulding of a 2.0 mm wall sports component with a flow path length of 120 mm requires a melt temperature of 260°C and sufficient injection velocity to prevent premature freeze-off, but excessive velocity creates gate-area surface ripple that reduces transmission by 2–5%. Cavity surface temperature below 60°C leads to incomplete wetting and micro-voids visible under cross-polarized light; therefore, the tool is designed with conformal cooling channels and supplied with water at 60–80°C. The main processing conflict is that low-temperature impact performance is sensitive to moisture after moulding; conditioning at 23°C and 50% RH for 24–48 h before cold impact testing is necessary because moisture acts as a plasticizer and shifts the ductile-brittle transition upward. Impact-modified TL is not suited to continuous service above 90°C, where dimensional stability and optical clarity can drift; the grade is not a replacement for transparent polyamide grades with higher aromatic content. Production-scale scrap in this sector arises from gate blush and surface ripple when hot-runner tips are set above 280°C, and the hot-runner tip should be maintained at 250–260°C to avoid both cold-slug lines and thermal degradation.

    For simple non-optical snap-fit cable clips and bracket covers in rail interiors, the material is processed without gas counterpressure; the only critical processing requirement is to maintain moisture below 0.10 wt% before plastication. Drying at 80°C for 4–6 h is sufficient when the sealed bag has been opened for longer than 2 h at ambient humidity above 50% RH.

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    Certification & Compliance
    More Introduction

    EMS-GRIVORY GRILAMID TR 90 TL is an impact-modified transparent polyamide 12 injection moulding grade supplied in the dry state. The designation combines an amorphous cycloaliphatic/aliphatic polyamide 12 backbone, a discrete toughening phase, and the TL package; the material remains optically clear because the amorphous backbone suppresses spherulitic light scattering, while the impact modifier shifts low-temperature crack initiation toward shear yielding. Dry-state test data are obtained on specimens whose moisture content is below 0.06 wt% and are reported under the relevant ISO mechanical testing atmospheres. Density is 1.00 g/cm³ when measured to ISO 1183, placing it below polycarbonate and PMMA and directly affecting mass-sensitive transparent parts. Principal uses include spectacle frames, sports eyewear, transparent clips, visor components, and thin-wall brackets for which ductility, low density, and chemical-stress-cracking resistance are specified alongside transparency.

    Moisture uptake in the feedstock is the first processing boundary. At saturation in 23°C water, a polyamide 12 system of this class absorbs approximately 1.5 wt% water, but at 23°C/50% RH equilibrium it is nearer 0.5 wt% according to ISO 62. These values are low relative to PA6 and PA66, but they are sufficient to alter melt viscosity, dimensional stability, and impact response if the dry condition is not restored before moulding. A closed-loop desiccant dryer with a dew point of -30°C, an air temperature of 80°C, and a residence time of 4–6 h reduces residual moisture to below 0.06 wt%. On production lines using hopper-loading equipment, the hopper should be purged with dry air when ambient relative humidity exceeds 60%, because conditioned resin loaded into a hot dryer in thick layers can retain moisture pockets. Failure is visible as surface splay on thick sections, but the non-visible damage is hydrolytic chain scission at processing temperature, which reduces notched impact strength and invalidates the dry-state mechanical envelope.

    What does “dry” signify for TR 90 TL in injection moulding?

    “Dry” in the GRILAMID TR 90 TL datasheet does not mean zero water; it identifies a moulding feedstock state in which residual moisture is low enough to prevent hydrolytic degradation during plastication. The recommended maximum is 0.06 wt%, determined by Karl Fischer titration to ISO 15512 or by a calibrated on-line moisture analyser. The dryer residence time is bounded at the lower end by the diffusion coefficient of water through the pellet and at the upper end by oxidative discoloration. The moulder should not use an oven-drying step for more than 8 h unless the oven has a dry-air purge, because hot air alone at high humidity can cause surface oxidation and yellowing of transparent amorphous polyamide. When a barrel zone exceeds 260°C, degradation accelerates, and the melt becomes suspect for colour shift and notched Charpy loss. The dry-state mechanical certificate is therefore a processing specification, not merely a conditioning label.

    PropertyTest methodDry-state typical valueRelevance for part design
    DensityISO 11831.00 g/cm³Low mass in spectacle frames and clips
    Water absorption, equilibrium 23°C/50% RHISO 620.5 wt%Dimensional shift expected in humid service
    Water absorption, saturation 23°CISO 621.5 wt%Upper bound for wet-condition design
    Tensile modulusISO 527-1/-21200 MPaLower stiffness than semi-crystalline PA12
    Yield stressISO 527-1/-245 MPaSnap-fit insertion and bending load limit
    Nominal strain at breakISO 527-1/-2>50%Ductile failure in overload
    Charpy notched impact, 23°CISO 179/1eA12 kJ/m²Release criterion and ambient impact
    Charpy notched impact, -30°CISO 179/1eA8 kJ/m²Low-temperature frame durability
    Vicat softening temperature, B50ISO 306100°CShort-term heat contact limit
    Heat deflection temperature, 1.8 MPaISO 75-1/-280°CContinuous load-bearing ceiling
    Coefficient of linear thermal expansion, 23–55°CISO 11359-1/-2100 × 10⁻⁶ K⁻¹Metal-polymer fit in inserted parts
    Light transmittance, 2 mmISO 1346889%Optical clarity requirement
    Haze, 2 mmASTM D1003<1%Transparency in polished cavities
    Mould shrinkage, parallel/normalISO 294-40.5–0.7%Nearly isotropic tool compensation

    On a three-zone hydraulic injection moulding machine with a screw L/D ratio between 18:1 and 22:1, the melt temperature for TR 90 TL is normally maintained between 240°C and 260°C. Mould temperature should be kept at 40–60°C. The lower mould temperature is a deliberate process choice: raising it above 70°C can produce surface haze through relaxation effects in the amorphous transparent layer. Back pressure is set between 30 bar and 60 bar, and screw surface speed is limited to 50–100 min⁻¹ to avoid shear heating above the set melt temperature. Injection speed is moderate to high, but not so high that gate blush appears at tunnel gates; full-round or trapezoidal runners with cold slug wells are preferred. A residual hold pressure of 400–800 bar is selected based on gate freezing time, which is shorter than semi-crystalline PA12 because the amorphous phase does not exhibit a sharp crystallisation plateau. Mould shrinkage after 24 h is typically 0.5–0.7% in both flow and transverse directions when measured to ISO 294-4, giving nearly isotropic dimensional behaviour that simplifies frame hinge snap-fit tolerances.

    Failure analysis on moulded spectacle frames indicates that the impact-modified grade changes the practical failure mode from hinge boss cracking to ductile bending at low temperatures. The Charpy notched value at 23°C under ISO 179/1eA is used for material release, but the more relevant test for a frame side arm is multi-axial impact response. The TL grade reduces brittle crack propagation at gate freeze-off regions and in flow-weld lines. Weld-line strength is still lower than bulk strength and should be assessed by simulation or by drop-weight test to ASTM D3763. Repeated flexing durability is better than PMMA and comparable to polycarbonate in thin sections, but published data for this specific configuration is limited for very high cycle fatigue above 10⁵ flex cycles. Components under continual load in hot climates should use conditioned modulus rather than dry-state modulus, because absorbed water lowers the glass transition of the amorphous polyamide matrix.

    When TR 90 TL replaces polycarbonate or PMMA in transparent thin-walled components

    Polycarbonate and PMMA are the usual incumbent materials for transparent consumer and industrial components, but they impose different trade-offs. At 1.00 g/cm³, TR 90 TL is approximately 17% lower in density than polycarbonate at 1.20 g/cm³ and approximately 16% lower in density than PMMA at 1.19 g/cm³; for a frame front of identical volume this mass saving is achieved without reducing wall thickness. Polycarbonate is susceptible to environmental stress cracking when residual stress and external chemical exposure combine, particularly with alcohol-based cosmetics and plasticisers. The polyamide 12 backbone of TR 90 TL is generally less affected by these mixtures, although each formulation must be checked against the specific solvent mixture. PMMA offers higher surface hardness and clarity but has low impact strength and cannot sustain snap-fit assembly in thin sections; TR 90 TL is used where flexural ductility and repeated assembly are required, while an anti-scratch coating compensates for the lower surface hardness of transparent polyamide. The heat deflection temperature of TR 90 TL under ISO 75-1/-2 at 1.8 MPa is below that of polycarbonate; continuous load-bearing service above 80°C should not be assumed without conditioned HDT measurement and creep testing under the application load.

    Compared with semi-crystalline PA12, the amorphous TR 90 TL does not develop a crystalline melting peak. The process window therefore does not require a crystallisation plateau, and mould temperature can be lower. This difference removes the anisotropic shrinkage associated with lamellar growth but also lowers tensile modulus and solvent resistance in certain aggressive media. Compared with standard transparent TR 90, the TL impact modification reduces stiffness and increases multi-axial ductility; downgauging of load-bearing frames should therefore be recalculated using the TL modulus. For applications requiring higher surface hardness, a coated transparent polyamide or an alternative transparent polymer is preferred unless the ductility of TR 90 TL is decisive.

    Chemical compatibility boundaries for the moulder are defined by the polyamide linkage. Strong mineral acids, concentrated formic acid, and some chlorinated solvents attack the amide group or cause stress cracking; these media should be avoided in production cleaning and end-use exposure. The material is not formulated for continuous hot-water or steam-sterilisation service. In controlled manufacturing, the lot-specific certificate should list melt volume-flow rate under ISO 1133-1, residual moisture by ISO 15512, and notched Charpy impact by ISO 179/1eA; this traceable data set links the moulded result to the dry-state datasheet. Batch-to-batch variation on production injection lines is usually observed as a shift in fill time and part gloss when dryer dew point is not maintained; the correction is re-drying, not an upward adjustment of barrel temperature. Suitability for a particular transparent part must be established by end-use testing under the relevant part-level standard, not by extrapolation from a single material property table.

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