| HS Code | 901670 |
| Density | 1.06 g/cm³ |
| Tensile Modulus | 2400 MPa |
| Tensile Stress At Yield | 70 MPa |
| Tensile Strain At Yield | 5% |
| Elongation At Break | 50% |
| Charpy Impact 23 C | no break |
| Notched Charpy Impact 23 C | 11 kJ/m² |
| Glass Transition Temperature | 155 °C |
| Heat Deflection Temperature 1 8 Mpa | 115 °C |
| Heat Deflection Temperature 0 45 Mpa | 140 °C |
| Water Absorption 24h | 0.3% |
| Light Transmission | 90% |
As an accredited EMS-Grivory Grilamid TR 90 TL PAMACM12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | EMS-Grivory Grilamid TR 90 TL PAMACM12 transparent polyamide pellets supplied in 25 kg sealed multilayer bags, then palletized and stretch-wrapped. |
| Container Loading (20′ FCL) | 20′ FCL shipment of Grilamid TR 90 TL granules in sealed PE bags, palletized, secured, and moisture-protected for safe transport. |
| Shipping | Grilamid TR 90 TL (PAMACM12) ships as transparent polyamide granules in sealed, moisture-proof packaging to prevent water absorption and contamination. Keep dry, protected from heat and direct sunlight. Standard non-hazardous handling applies; avoid dust exposure and use proper labeling for safe transport. |
| Storage | Store Grilamid TR 90 TL in its original, unopened container in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and moisture. Keep the container tightly sealed to prevent water absorption. Avoid exposure to oxidizing agents. Under proper conditions, shelf life is typically several years. |
| Shelf Life | Shelf life is typically 2 years when stored in original, unopened packaging in a cool, dry environment. |
Direct-gated single-cavity moulding of ophthalmic frame fronts from 96.0–99.5 wt% EMS-Grivory Grilamid TR 90 TL PAMACM12, 0.2–1.5 wt% MACM12-carrier colour concentrate, and 0.3–0.8 wt% UV absorber masterbatch requires moisture to be reduced to ≤0.10% before plastication. The drying sequence is executed in a desiccant-bed dryer with -40 °C dew point at 80 °C for 4–6 h; if ambient relative humidity exceeds 60%, dried material is conveyed under dry nitrogen and accumulated for no more than 2 h before entering the feed throat. Melt temperature is held at 255–280 °C, mould temperature at 50–70 °C, holding pressure at 70–90 MPa, and cooling time between 25 s and 40 s for wall thicknesses of 2.5–4.0 mm. The gate is placed at the temple-barrel junction and uses a valve-gated hot runner with tip temperature ≥230 °C; direct edge gating at the lens rim is avoided because it creates anisotropic shrinkage along the rim axis and shifts the moulded lens opening beyond the ±0.2 mm tolerance required for lens mounting. After ejection, frame fronts are annealed at 120 °C for 2 h to reduce residual orientation as assessed by polariscope. Compliance documentation for optical retail includes ISO 12870:2016 for frame dimensional stability and mechanical durability, ANSI Z80.5-2019 for US market requirements, and EN 1811:2011+A1:2015 for nickel release. Ultraviolet ageing of pigmented grades is screened using ISO 105-B06:2020 with blue wool reference ≥6 at 100 h xenon exposure. Finished part categories include rimmed prescription frame fronts, shield-type sunglass frames, and replaceable temple arms for sports eyewear.
In luer-activated fluid circuits, connector bodies injection moulded from 99.0–99.5 wt% neat Grilamid TR 90 TL PAMACM12 and 0.5–1.0 wt% MACM12-compatible silicone lubricant masterbatch are used where polycarbonate develops environmental stress-cracking networks at thread roots under 0.2–0.4% outer-fibre strain when exposed to lipid emulsions. The moulding is run on an electric reciprocating-screw machine with 24 mm screw and 22:1 L/D ratio; melt temperature is controlled at 260–280 °C, mould temperature at 60–80 °C, injection speed at 80–120 mm/s, and switch-over from velocity to pressure occurs at 600–800 bar cavity pressure measured at the last filling point. Cavity-pressure monitoring is documented for every shot under ISO 13485:2016 production controls. Cleaning, assembly, and packaging are performed in an ISO 14644-1 Class 7 cleanroom with controlled humidity ≤45% RH. Pre-drying is fixed at 80 °C for 4 h, with moisture verification by Karl Fischer titration below 0.10%. The material batch must have test data from ISO 10993-5:2009 cytotoxicity, ISO 10993-10:2010 sensitisation and irritation, and USP <88> Class VI biological reactivity, with application-specific evaluation under ISO 10993-1:2018; dimensional compatibility of small-bore connectors follows ISO 80369-7:2016 to reduce misconnection risk. For steam autoclave, repeated exposure at 121 °C for 20 min is not recommended beyond 50 cycles without optical re-validation according to ASTM D1003-21. Terminal parts are transparent luer lock connectors, stopcock bodies, and quick-disconnect couplings used in renal dialysis, enteral feeding, and diagnostic fluid management lines.
For fragrance pump collars and lipstick sleeves, transparent cosmetic closures are produced from 98.0–99.0 wt% Grilamid TR 90 TL PAMACM12, 0.5–1.5 wt% MACM12-carrier pigment masterbatch, and 0.1–0.5 wt% non-migratory mould-release concentrate. Threaded areas must remain free of stress-cracking zones after filling with ethanol-water fragrance systems. The preform route uses a two-stage injection blow moulding cell with preform melt temperature 260–285 °C, blow mould temperature 40–60 °C, and blow pressure 8–12 bar; the injection mould cavity surface is polished to SPI A-1 diamond finish to preserve total luminous transmittance above 90% on a 2.0 mm plaque measured according to ASTM D1003-21. For single-stage injection moulded caps with collapsible core thread forming, mould temperature is set at 50–60 °C, holding pressure at 60–80 MPa, and cooling time at 15–25 s. Drying is performed at 80 °C for 4 h; regrind from identically pigmented sprue and runners may be reintroduced up to 15 wt% only after drying, while cross-contamination with PE or EVA carrier masterbatch is prohibited because carrier incompatibility increases haze by more than 2% at 1.0 wt% addition. Heavy metal content is controlled under 94/62/EC packaging requirements and the US TPCH model legislation with combined lead, cadmium, mercury, and hexavalent chromium below 100 ppm. Fragrance compatibility is screened by immersion in 50/50 v/v ethanol-water at 40 °C for 14 d, followed by visual inspection under ISO 22715:2006 surface-defect criteria. Finished product types include fragrance pump collars, lipstick tube sleeves, mascara cap shells, and compact case lids for cosmetic packaging lines.
| Downstream sector | Primary compliance standard | Key test method | Critical numerical condition |
|---|---|---|---|
| Ophthalmic frames | ISO 12870:2016; ANSI Z80.5-2019; EN 1811:2011+A1:2015 | ISO 105-B06:2020 | Moisture ≤0.10%; melt 255–280 °C |
| Medical connectors | ISO 10993-1:2018; ISO 80369-7:2016; USP <88> | ASTM D1003-21 | Moisture ≤0.10%; autoclave 121 °C |
| Cosmetic packaging | 94/62/EC; US TPCH | ISO 22715:2006 | Haze increase ≤2%; combined metals <100 ppm |
| Dairy sight tubes | FDA 21 CFR 177.1500; EU 10/2011; 3-A Sanitary Standards | ISO 13468-1:2019; ASTM D1003-21 | Migration 10 mg/dm²; CIP 100 cycles |
| Water filter bowls | NSF/ANSI 61; KTW-BWGL; BS 6920-1:2014 | ISO 527-2:2012 | Burst test 24 bar; free chlorine 0.5–1.0 mg/L |
| Automotive HVAC lenses | IATF 16949:2016; VDA 275:1994; ISO 3795:1989 | ISO 105-B06:2020 | Fogging 100 °C/16 h; burn rate <100 mm/min |
Across dairy level indication circuits, transparent level tubes and sight-glass bodies machined from 100 wt% virgin Grilamid TR 90 TL PAMACM12 are inserted where the contacting media alternate between raw milk at 4 °C, hot water rinse at 60–80 °C, 0.5–1.0 wt% sodium hydroxide CIP solution at 70–85 °C, and 1.0–2.0 wt% nitric acid descaler at 60–70 °C. The critical degradation vector is not chemical dissolution but water absorption, which reduces the glass transition temperature of the penetrated surface and produces haze in thick sections after repeated thermal cycling. Equilibrium water uptake measured according to ISO 62:2008 reaches approximately 3.5–4.5 wt% after 14 d immersion at 60 °C; when the part returns to 20 °C, absorbed water remains in the amide network and creates a reversible plasticising effect, but if the wet part is immediately heated above 80 °C, surface microvoiding can occur. Published data for this specific grade under repeated caustic CIP cycles is limited, so processors must validate optical transmission and haze using ISO 13468-1:2019 and ASTM D1003-21 on 2.0 mm moulded plaques before and after 100 CIP cycles. Food-contact compliance is documented under FDA 21 CFR 177.1500 for polyamide resins, EU 10/2011 overall migration with 10 mg/dm² maximum, and 3-A Sanitary Standards for cleanability of fluid-contact surfaces. For thick-walled blanks of 6–12 mm, injection moulding is performed with a low-shear 20:1 L/D screw at melt temperature 250–270 °C, mould temperature 50–60 °C, holding pressure 60–80 MPa, and cooling time 30–60 s; moulded blanks are annealed at 120 °C for 2 h under nitrogen to relax orientation. Threads and sealing faces are subsequently CNC-machined and polished to remove moulded skin so that the optical surface is not dependent on cavity-surface replication. Terminal part types include transparent level indicator tubes for balance tanks, sight-glass discs for positive-displacement filler monitoring, and inline observation sleeves for pasteuriser recirculation loops.
After hydrostatic testing of point-of-use filter bowls injection moulded from 97.0–98.0 wt% Grilamid TR 90 TL PAMACM12, 1.0–2.0 wt% hindered-phenol antioxidant masterbatch, and 0.5–1.0 wt% processing aid, the assemblies are qualified at 24 bar at 20 °C for 5 min, corresponding to a 3.0 safety factor over the 8.0 bar maximum rated operating pressure. The base-centre gate is used to force the melt front upward and eliminate weld lines at the threaded neck; where a side gate cannot be avoided, mould temperature is raised to 70 °C and packing time is extended to 15–20 s to raise knit-line tensile strength to 70–80% of parent material measured on welded plate specimens according to ISO 527-2:2012. Injection moulding uses melt temperature 255–275 °C, mould temperature 50–60 °C, screw L/D 20:1, and cooling time 35–60 s depending on wall thickness from 2.5 mm to 5.0 mm. The resin is dried at 80 °C for 4–6 h to ≤0.10% moisture; if the bowl is assembled with an acrylic sight window, adhesive selection must avoid amine-based curatives that can attack the polyamide surface and produce microcracking at the lip seal. Potable-water suitability is documented under NSF/ANSI 61 for chemical extractables, KTW-BWGL for German Federal Environment Agency assessment, BS 6920-1:2014 for UK water fittings, and AS/NZS 4020:2018 for Australian and New Zealand product contact. Oxidative resistance is evaluated by immersion in 0.5–1.0 mg/L free chlorine at pH 6–8 and 23 °C for 1000 h; continuous service above 2.0 mg/L total chlorine is not recommended without end-use validation because polyamide surface degradation can initiate at gasket grooves. Terminal finished product types are clear sediment filter bowls, reverse-osmosis prefilter housings, and transparent bypass loop indicators for residential and food-service water treatment equipment.
To maintain legibility of backlit graphics after prolonged sunlight exposure, thin-wall transparent lenses for automotive HVAC control interfaces are moulded from 98.0–99.3 wt% Grilamid TR 90 TL PAMACM12, 0.5–1.5 wt% neutral-smoke tint masterbatch, and 0.2–0.5 wt% UV absorber masterbatch. The process uses a sequential valve-gate hot runner with two or four drop points to prevent gas traps in lenses with 1.2–2.0 mm wall thickness; gate opening is delayed by 0.2–0.5 s to allow the first flow front to reach the next gate position. Melt temperature is set at 260–285 °C, mould temperature at 70–80 °C, filling speed at 60–100 mm/s, and holding pressure at 40–60 MPa for 5–10 s; the switch-over is controlled by screw position at 95% of filling volume. Mould surfaces are polished to SPI A-1 diamond and the tool is designed with 0.5–1.0° draft on ribs to reduce ejection marks. Pre-drying is performed at 80 °C for 4 h with dew point -40 °C. Automotive interior compliance is documented under IATF 16949:2016 production part approval, VDA 275:1994 fogging with test condition 100 °C/16 h, ISO 3795:1989 flammability with burn rate not exceeding 100 mm/min, and ISO 105-B06:2020 artificial weathering for lightfastness. Odour evaluation is conducted under VDA 270 at 80 °C for 2 h; specification limits are defined by the individual OEM. The amorphous polyamide is not combined with semi-crystalline polyamide regrind because differing solidification rates generate visible gate blush and inconsistent shrinkage. Finished part geometries are climate-control display lenses, gear-selector indicator windows, steering-wheel scroll optical lenses, and interior ambient-light diffuser covers.
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EMS-Grivory Grilamid TR 90 TL is a transparent amorphous polyamide supplied under the PAMACM12 chemical descriptor. The polymer is produced by polycondensation of bis(3-methyl-4-aminocyclohexyl)methane with dodecanedioic acid and exhibits no measurable melting endotherm when analysed by ISO 11357-3. The amorphous morphology permits visible-light transmission and isotropic shrinkage in injection-moulded components. The TL suffix identifies a specific internally lubricated, tribologically modified system relative to standard Grilamid TR 90. Dry density at 23°C is approximately 1.00 g/cm³ by ISO 1183-1. The resin is intended for lightweight transparent parts requiring impact resistance, chemical resistance and dimensional stability in contact with skin lipids, cosmetic formulations and aliphatic hydrocarbons.
Because the polymer is amorphous, melt solidification is controlled by glass transition and frozen orientation rather than crystallisation kinetics. This has direct consequences for tool design: shrinkage is low and isotropic, but residual stress can reduce optical quality if mould temperature or packing pressure is insufficient. The following processing limits are derived from standard EMS polyamide processing guidance and production-scale injection moulding practice; grade-specific values should be confirmed against the current technical datasheet.
The critical variables are moisture content, melt temperature, residence time and mould surface temperature. Feedstock should be dried to below 0.10 wt% residual moisture as measured by ISO 15512 Method B. A closed-loop desiccant dryer with a dew point below -40°C and an air temperature of 80°C for 4–6 h is normally adequate. Nozzle melt temperature is held between 250°C and 280°C. Above 300°C, thermal-oxidative chain scission accelerates yellowing; below 240°C, high melt viscosity can generate flow lines and gate blush. Mould temperature is set between 40°C and 80°C. Low mould temperatures shorten cycle time but may freeze orientation; high mould temperatures reduce residual stress and improve stress-optical behaviour at the expense of longer cooling time.
On a production-scale injection moulding cell using a 25 mm diameter, 20:1 L/D three-zone screw, melt residence time above 10 min at processing temperature may produce visible yellowing in sections thicker than 3 mm. Hot-runner drops should be individually heated, and cold-runner sprue bushes should be sized for early gate freeze at mould temperatures below 50°C. Injection speed should be profiled rather than constant; a fast initial fill to 95% of shot volume followed by slower packing reduces jetting and gate blush in gates below 0.8 mm diameter. Holding pressure is best established by part weight stabilisation or cavity pressure measurement. Typical hydraulic holding pressures for thin-wall parts range from 50 MPa to 70 MPa, but cavity pressure sensors sampled at 1 kHz provide better short-shot and flash detection than machine pressure. Mould shrinkage is usually 0.4–0.6% by ISO 294-4 depending on wall thickness and mould temperature.
| Parameter | Recommended range or value | Standard or method |
|---|---|---|
| Residual moisture | <0.10 wt% | ISO 15512 Method B |
| Drying temperature | 80°C | Desiccant dryer |
| Drying time | 4–6 h | Closed-loop air |
| Melt temperature | 250–280°C | Nozzle |
| Mould temperature | 40–80°C | Thermocouple probe |
| Back pressure | 3–8 MPa | Hydraulic pressure |
| Screw peripheral speed | <0.3 m/s | From screw diameter and rpm |
| Mould shrinkage | 0.4–0.6% | ISO 294-4 |
For optical mouldings, transmitted haze and specular gloss are sensitive to screw recovery speed and hot-runner temperature distribution. Moisture above 0.10 wt% causes hydrolysis at melt temperature; the resulting molecular weight reduction may appear as silver streaks, splay and loss of notched impact rather than immediately visible black specks. Relative viscosity by ISO 307 can be measured before and after processing; a decrease of more than 5% indicates unacceptable degradation. Regrind from sprues and runners may be re-used for non-optical or dark-coloured parts if re-dried, but repeated heat histories increase yellowness and reduce notched impact. For clear parts, regrind content above 20 wt% is generally avoided unless validated by optical and mechanical testing. Parts requiring low residual stress may be annealed at 80–100°C for 1–2 h under nitrogen or dry air, but oxygen-containing ovens can increase yellowing.
| Property | Standard | Unit | Typical value |
|---|---|---|---|
| Density | ISO 1183-1 | g/cm³ | 1.00 |
| Tensile modulus, dry | ISO 527-1/-2 | MPa | 1600 |
| Tensile stress at yield, dry | ISO 527-1/-2 | MPa | 60 |
| Elongation at yield, dry | ISO 527-1/-2 | % | 6 |
| Nominal elongation at break, dry | ISO 527-1/-2 | % | >50 |
| Notched Charpy impact, dry, 23°C | ISO 179/1eA | kJ/m² | 8–11 |
| Heat deflection temperature, 1.8 MPa | ISO 75-1/-2 | °C | 90 |
| Vicat softening temperature, B50 | ISO 306 | °C | 145 |
| Total luminous transmittance, 2 mm | ISO 13468-1 | % | 92 |
| Water absorption at saturation, 23°C | ISO 62 | % | 1.5 |
| Mould shrinkage | ISO 294-4 | % | 0.4–0.6 |
The optical and mechanical values above are representative of the TR 90 family in the dry moulded state; the internal lubricant in the TL grade may slightly reduce tensile yield stress and notched impact relative to unmodified TR 90 because the additive phase is not load-bearing. Absorbed water acts as a plasticiser and increases notched impact energy but reduces modulus and glass transition. At 23°C and 50% relative humidity, the moisture content equilibrates near 1.0–1.5%, and tensile modulus may fall from 1600 MPa to approximately 1100–1300 MPa. These shifts are reversible on drying but must be included in snap-fit calculations. If dry as-moulded modulus is used without moisture correction, predicted snap-fit insertion force can be overestimated by more than 20%. The Vicat B50 value of 145°C should not be interpreted as a continuous upper limit; long-term thermal ageing must be evaluated by ISO 2578 or a product-specific heat-ageing programme.
Compared with unmodified Grilamid TR 90, the TL grade contains a non-blooming internal lubricant system intended to reduce friction and improve ejection. Dry sliding contact in articulated eyewear hinges or snap-fit brackets benefits from the additive, although published coefficient-of-friction data for this specific configuration is limited. Tribological verification should therefore be performed by pin-on-disc testing according to ISO 7148 or linear reciprocating wear according to ASTM G133 using plaques moulded under production-representative conditions. Compared with semi-crystalline PA12, TR 90 TL retains optical clarity because the amorphous structure lacks crystallites that scatter light, but this same structure can increase sensitivity to polar organic solvents and alcohols relative to high-crystallinity PA12. Compared with bisphenol-A polycarbonate, the polyamide offers lower density and lower melt processing temperature, but lower tensile modulus and higher moisture uptake. Compared with PMMA, TR 90 TL provides higher notched impact strength and better resistance to stress cracking in alkane-based formulations, but lower surface hardness and lower tensile modulus. Unfilled polycarbonate typically has a density of 1.20 g/cm³ and a tensile modulus near 2400 MPa, while PMMA typically has a density of 1.19 g/cm³ and a tensile modulus near 3300 MPa; these comparative values are not grade-specific and are supplied only for engineering context.
Chemical compatibility should be tested by immersion under ISO 175 or ASTM D543. The resin is generally resistant to non-polar aliphatic hydrocarbons, mineral oils, greases and dilute aqueous salt solutions, but it is attacked by strong acids, oxidising agents and some chlorinated solvents. Stress-cracking resistance is strongly geometry-dependent; highly stressed transparent mouldings should avoid sharp internal radii and should be annealed or moulded against hot tool surfaces. Dry blending with amine-based stabilisers or certain copper halide packages may cause discoloration or viscosity shifts and should be avoided unless validated by the compounder. For food-contact applications, nylon resins such as PAMACM12 may fall under FDA 21 CFR 177.1500, but the final article must satisfy applicable migration limits and conditions of use. REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU documentation is available from the resin supplier. Medical device use is not covered by a generic approval; cytotoxicity, sensitisation and irritation testing under ISO 10993-5 and ISO 10993-10 must be completed on the final sterilised component. For eyewear applications, frame-level requirements may include EN ISO 12870, while optical transmittance is measured by ISO 13468-1 and haze by ASTM D1003.
The internal lubricant in TR 90 TL lowers the tendency for audible squeak and surface scuffing in low-load, low-speed dry sliding contacts. The additive is dispersed without creating the refractive-index inhomogeneity associated with glass-fibre or graphite fillers, so optical clarity is preserved. The system is not a substitute for POM or PEEK in high-load gears, high-speed wear surfaces, or continuous tribological service. At elevated pressure-velocity conditions, the wear rate accelerates and must be evaluated against semi-crystalline tribocompounds. The utility of TR 90 TL in sliding contacts is therefore limited to intermittent or lightly loaded movement, such as spectacle hinges, detents and snap-fit closures. For applications involving continuous load, external lubrication or a more wear-resistant engineering polymer should be selected. The low-friction modification also assists demoulding, which can reduce ejection force and surface defects in polished transparent tools, but tool release angles should still follow standard polyamide practice.
Typical application examples include lightweight spectacle frames, sports eyewear, transparent fluid-handling housings and non-implant medical equipment components. The density of 1.00 g/cm³ reduces part weight compared with polycarbonate and PMMA. Resistance to sebum and skin oil supports use without paint or clear coats; however, sunscreen formulations vary and may contain solvents that require specific immersion testing. Hard coating may be applied for scratch resistance, but adhesion should be checked by cross-cut testing according to ISO 2409 after moisture conditioning. Moulded hinges and snap-fit closures can use the TL lubricant for improved action; designs should maintain generous radii and avoid high assembly strain because absorbed moisture and cosmetic agents can reduce stress-cracking resistance over time.