| HS Code | 534856 |
| Density | 1.06 g/cm³ |
| Tensile Modulus | 2100 MPa |
| Yield Stress | 60 MPa |
| Yield Strain | 4% |
| Strain At Break | >50% |
| Charpy Impact Notched 23 C | 5 kJ/m² |
| Charpy Impact Unnotched 23 C | No break |
| Glass Transition Temperature | 160 °C |
| Heat Deflection Temperature 0 45 Mpa | 135 °C |
| Heat Deflection Temperature 1 8 Mpa | 125 °C |
| Water Absorption 24h 23 C | 0.3% |
| Refractive Index | 1.566 |
As an accredited EMS-Grivory Grilamid® TR 55 PA12/MACMI factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 25 kg sealed moisture-barrier bags of Grilamid® TR 55 PA12/MACMI pellets, packaged for safe transport and dry storage. |
| Container Loading (20′ FCL) | 20′ FCL: palletized bags of Grilamid TR 55 loaded securely, protected from moisture, ventilated, for safe ocean transport. |
| Shipping | Grilamid® TR 55 is shipped as solid granules in sealed, moisture-proof bags or drums to prevent moisture absorption. Transport is non-hazardous under normal conditions, though keep dry, avoid excessive heat, and store in ventilated areas. Ensure containers are intact to maintain product purity during transit. |
| Storage | Store in original, tightly sealed containers in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and moisture. Keep at room temperature (20–25°C) to prevent degradation. Avoid exposure to humidity, as polyamides absorb water. Ensure no cross-contamination with other materials. Properly label and protect from mechanical damage. |
| Shelf Life | Store dry, cool, and in original sealed packaging to prevent moisture uptake; shelf life is typically 2–3 years. |
Transparent Luer-actuated stopcock bodies and extension-line connectors moulded from Grilamid® TR 55 are produced in cleanroom-classified injection suites under ISO 14644-1 Class 8 because the amorphous PA12/MACMI backbone hydrolyses when melt moisture exceeds 0.10%, generating splay on tapered sealing surfaces and reducing weld-line elongation at the intersection of three fluid channels. Before moulding, the granulate is dried in a desiccant-bed dryer at 80°C for 4–6 h until the residual moisture measured by Karl Fischer titration is below 0.08%; the drying hopper maintains a dew point of at most -30°C and a return-air temperature of 80°C. The needle-valve orifice is sized to a gate-to-wall thickness ratio of 0.8:1 at each Luer taper. Melt is injected at a nozzle set point of 250–270°C through a hot-runner system with separately controlled needle-valve gates for bodies of 0.8–1.2 mm nominal wall thickness, and the mould temperature is held at 80–90°C to minimise frozen-in orientation that would otherwise appear as photoelastic stress fringes at the Luer taper. Clamp force on a 50 t all-electric machine is selected so that cavity pressure at the gate does not exceed 600 bar before switchover at 95% cushion volume. The finished parts are assembled without solvent bonding because the resin resists stress cracking in contact with isotonic saline, lipid emulsions, and alcohol-based disinfectant wipes; biocompatibility is reviewed under ISO 10993-5 for cytotoxicity, ISO 10993-10 for sensitisation and irritation, and the resin is additionally evaluated against USP <88> Class VI for systemic injection, intracutaneous reactivity, and implantation. Gamma sterilisation at 25–50 kGy and ethylene oxide exposure at 55°C with a 6 h post-sterilisation degassing step are typical terminal processes; lots exceeding 50 kGy are retained for yellowness-index comparison under ISO 14782. Terminal products include male and female Luer lock collars, three-way stopcocks, and latching extension connectors used in infusion and enteral tubing sets. The visual clarity of the moulded body permits air-bubble detection during priming, and the absence of a crystalline melting plateau avoids the haze band that semi-crystalline polyamides develop in thick bosses.
| Parameter | Target | Reference equipment / method |
|---|---|---|
| Residual moisture after drying | ≤0.08% by weight | Karl Fischer titration |
| Drying air dew point | ≤-30°C | Desiccant dryer with dew-point monitor |
| Melt temperature at nozzle | 250–270°C | Injection-moulder thermocouple |
| Mould temperature | 80–90°C | Pressurised water temperature control unit |
| Screw L/D ratio | 20:1–25:1 | All-electric reciprocating screw |
| Switchover position | 95% cushion volume | Machine controller |
| Back pressure | 30–50 bar | Hydraulic or electric drive |
In positive-displacement flow-meter taper bodies moulded from Grilamid® TR 55, gate haze is observed when the gate diameter is smaller than half the wall thickness at the inlet boss, creating shear heating above 300°C in the amorphous melt. The taper body is designed with a gate land length of 0.8–1.0 mm and a gate diameter of 1.5–2.0 mm, while the flow path from the cold runner is kept below 60 mm measured from sprue bush to the farthest fill point to avoid premature solidification. Dimensional acceptance follows ISO 294-4 for shrinkage determination and ISO 1101 for geometrical tolerancing; the as-moulded taper angle is held to a profile tolerance of 0.03 mm over a 25 mm axial length. Because moisture uptake above 0.3% enlarges the bore diameter, post-mould conditioning is performed at 23°C and 50% RH for 48 h before final calibration. Published component-specific shrinkage data for complex taper geometries are limited; in the absence of such data, short-shot progression on a pilot tool is used to set the holding-pressure profile. The melt temperature is set at 260–280°C and the mould temperature at 75–85°C; screw speed is limited to 80 rpm and back pressure to 30–50 bar to restrict shear heating. Clean run regrind from sprue and cold-runner material is allowed at a maximum of 20 wt% only when the regrind is dried separately and inspected for dust, because particulates act as haze nuclei in transparent optical bodies. The terminal product is a transparent taper tube for rotameter-type flow meters, chemical dosing sight glasses, and low-pressure hydraulic flow indicators. Repeated exposure to strong acids or strong bases is not recommended without immersion testing under ISO 175 and stress-cracking assessment under ISO 22088-3.
In diesel fuel-filter sight bowls and tank-level inspection windows, Grilamid® TR 55 is specified because its amorphous morphology retains luminous transmittance after contact with fatty-acid methyl ester blends, low-sulphur diesel, and standard hydraulic oils at exposure temperatures not exceeding 80°C in continuous service. The bowl is moulded as a single-walled component of 3.0–5.0 mm thickness on a hydraulic machine with a 120 t clamp unit, using a cold-runner sprue-to-bowl diameter ratio of 1.5:1 and a valve-gate position offset from the bowl axis to prevent side-loading of the core. The mould temperature is maintained at 70–80°C with a tolerance of ±3°C across the cavity, because asymmetric cooling produces birefringence rings that become visible under polarised inspection after fuel immersion. Regrind from sprues is limited to 15 wt%; higher fractions reduce surface gloss on the sealing bead and increase the probability of pinhole leakage at the O-ring seat. Material conformity for automotive fuel exposure is reviewed against SAE J2260 for nonmetallic fuel-system tubing where the design falls within that specification, and the finished assembly is validated by the end user under ISO 16750-4 thermal cycling and ISO 175 chemical immersion for diesel and biodiesel blends. The terminal product range includes fuel-filter bowls, inspection windows on fuel priming pumps, and level glasses for hydraulic reservoirs. Continuous service above 100°C is not recommended for this grade without component-specific creep and extraction testing, because the glass-transition-dominated modulus decay reduces sealing force retention in hot-oil environments.
Moulded sight glasses for drinking-water filter sumps and flow-monitoring cells are dry-blended without external lubricants because migration of metallic stearates into the water-contact layer would require additional leachate correction under BS 6920 and the German KTW-BWGL guideline. The granulate is processed at a melt temperature of 260–280°C and a mould temperature of 75–85°C; the screw is a low-shear barrier design with a compression ratio of 2.5:1 and a mixing zone no longer than 4 L/D to avoid excessive thermal history. Injection speed is set to achieve a flow-front velocity of 150–200 mm/s through the sight-glass window, and holding pressure is stepped from 700 bar for 2 s to 350 bar for 5 s before cooling to prevent sink marks at the boss. After demoulding, the parts are conditioned at 23°C and 50% RH for 48 h before dimensional inspection because the equilibrium moisture content for thin sections shifts the outer diameter by up to 0.3%. Odour and flavour testing for drinking-water suitability is performed according to EN 1622, cold-water extraction follows EN 12873-1, and surface analysis for leachable organic carbon is conducted under the local water-authority protocol. Terminal products include transparent filter sump lids, ultraviolet-reactor inspection ports, and flow indicators in point-of-use water treatment appliances. The grade must not be exposed to strong oxidising disinfectants at elevated concentrations, particularly ozone above 0.5 ppm continuous, unless the end user confirms long-term crack resistance under ISO 22088-3 with the specific water matrix.
| Application segment | Standard or regulation | Test purpose |
|---|---|---|
| Medical Luer connectors | ISO 10993-5, ISO 10993-10, USP <88> Class VI | Cytotoxicity, sensitisation, systemic toxicity |
| Flow-meter tapers | ISO 294-4, ISO 1101 | Shrinkage measurement, geometrical tolerancing |
| Automotive sight bowls | SAE J2260, ISO 16750-4, ISO 175 | Fuel-system material conformance, thermal cycling, chemical immersion |
| Potable-water sight glasses | KTW-BWGL, BS 6920, EN 1622, EN 12873-1 | Leachate, odour/flavour, extraction |
| Cosmetic packaging | Regulation (EC) No 1223/2009, EU 10/2011, 21 CFR 177.1500(b) | Finished goods safety, migration, resin compliance |
| Hand sanitiser reservoirs | ISO 175, ISO 22088-3 | Chemical immersion, environmental stress cracking |
Because lipophilic lotions and alcohol-rich toners contain plasticising fractions that haze acrylic and stress-crack polycarbonate, thick-wall cosmetic jars are injection-blow moulded from Grilamid® TR 55 to maintain transparency after twelve-week accelerated contact with a model emulsion of 60 wt% ethanol and 20 wt% caprylic/capric triglyceride at 40°C. The preform is injection moulded with a core-to-cavity thickness ratio of 1:1.6 to control wall distribution in the blow station, and the preform body is heated to 105–115°C using quartz IR lamps before stretch-blow orientation. Because the resin is amorphous, the blowing window is narrower than that of PET; a temperature deviation of ±5°C at the preform inner wall is sufficient to produce local haze bands at the jar shoulder. The blow mould is polished to SPI A1 surface finish and maintained at 30–40°C under vacuum to prevent surface micro-roughening. Cosmetic packaging conformity is assessed under Regulation (EC) No 1223/2009 for finished goods, while migration evaluation follows EU Regulation (EC) No 10/2011 for food-contact analogies and, where the component is used in dual-use packaging, 21 CFR 177.1500(b) for polyamide resins. Terminal products include multi-wall jars, overcap shells, and transparent airless dispenser housings. Lot-to-lot haze is controlled by measuring total luminous transmittance in the moulded wall according to ISO 13468-1 and yellowness index according to ISO 14782. The material should not be filled above 60°C with pure solvent-based formulations unless the manufacturer verifies that the specific solvent does not swell the amorphous phase beyond the permissible dimensional change.
Hand sanitiser dispenser reservoirs and pump bodies moulded from Grilamid® TR 55 resist environmental stress cracking when the reservoir wall is exposed to ethanol concentrations between 60% and 80% by volume at room temperature, provided the internal weld line is relocated away from the threaded neck by means of a sequential valve-gate programme. The reservoir is filled through a neck with an internal thread of M24 x 3 and an undercut ratio of 0.8% of the major diameter, which requires a collapsible core or unscrewing mechanism. Melt is injected at 255–275°C into a mould held at 70–85°C, and the holding phase is segmented into three steps: 900 bar for 0.8 s, 550 bar for 2.5 s, and 200 bar until gate freeze. Screw speed is limited to 80 rpm because shear heating in the plastication zone can exceed 300°C, causing yellowing that is quantified by ISO 14782. The terminal product is a transparent, break-resistant reservoir that allows visible fill level monitoring in high-traffic dispensing stations. The material is assessed for chemical compatibility using ISO 175 immersion in ethanol/water mixtures, and for stress cracking resistance under ISO 22088-3 bent-strip methodology with the specific sanitising formulation. The user must verify that the formulation does not contain high levels of alkyl quaternary ammonium compounds or concentrated hydrogen peroxide above 1.0 wt%, because these aggressive oxidative species can initiate microcracking over repeated exposure cycles.
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EMS-Grivory Grilamid® TR 55 is an amorphous transparent copolyamide belonging to the PA12/MACMI family under ISO 1874-1. It combines a laurolactam-derived polyamide 12 backbone with a bulky comonomer that inhibits crystallisation, resulting in a clear, low-density thermoplastic with no defined crystalline melting point. Dry-as-moulded density is approximately 1.02 g/cm³ by ISO 1183, the glass transition temperature is near 155 °C by ISO 11357-2, and water absorption at saturation is approximately 3.0 % by ISO 62. The grade is specified for injection moulding and limited extrusion. Typical applications include transparent filter housings, cosmetic closures, medical device components, automotive sensor covers, and industrial sight glasses where optical clarity must be maintained in contact with oils, greases, aqueous media, and cleaning agents. In comparison with semicrystalline PA12, the material exhibits more isotropic mould shrinkage, lower haze, and a glass transition instead of a melting endotherm; in comparison with polycarbonate and polymethyl methacrylate, it offers lower density and a different chemical resistance profile.
Suppression of crystallisation arises from the irregular repeat-unit geometry introduced by the MACMI comonomer. The amorphous phase lacks long-range three-dimensional order, so solidification is controlled by vitrification at the glass transition rather than by spherulite growth. Differential scanning calorimetry according to ISO 11357-3 therefore shows a distinct glass transition and no melting endotherm before decomposition. The absence of crystallites reduces light scattering at grain boundaries and produces transmission values of approximately 90 % at 3 mm thickness when measured by ASTM D1003. Dimensional change is also more isotropic than that of semicrystalline polyamides; the coefficient of linear thermal expansion is typically in the range 80–100 × 10−6 K−1 by ISO 11359-2. The aliphatic PA12 block contributes lower equilibrium moisture uptake than PA6 or PA66, while the bulky comonomer stiffens the chain and raises the glass transition relative to pure amorphous PA12. This architecture explains the product’s balance of clarity, chemical resistance, and processing flow.
In semicrystalline PA12, the crystalline phase restricts molecular motion above the glass transition and masks some early oxidative chain scission during melt processing. Grilamid® TR 55 has no such crystalline network; viscosity loss, yellowing, and evolution of low-molecular-weight volatile species become visible more rapidly when barrel holds are excessive. Processing guides therefore set the melt temperature window at 250–280 °C and recommend the lower half of the window for natural grades and the upper half only for thin-wall sections below 0.8 mm. Hot-runner systems with poorly balanced melt channels produce longer residence-time distributions in outer cavities; field observations on multi-cavity tools indicate that asymmetric filling becomes visible as optical birefringence and gate blush before short shots appear. Screw geometry should use a general-purpose three-zone screw with L/D between 20:1 and 25:1 and a compression ratio of 2.0:1–2.5:1. Excessive shear from small-diameter hot-runner drops or undersized valve-gate orifices is avoided because shear heating raises local melt temperature above the degradation threshold even when barrel setpoints remain within specification. Melt cushion should be constant, typically 2–4 mm, and screw retraction should not introduce air into the melt stream.
Drying is mandatory before injection moulding or extrusion. Moisture in PA12/MACMI reduces molecular weight during melt processing through hydrolysis, producing splay, silver streaks, reduced tensile strain at break, gate drool, and lot-to-lot inconsistency in transparency. A desiccant dryer with a dew point of −30 °C or lower is specified; drying at 80 °C for 4–8 hours from sealed bags reduces moisture below 0.10 %, as verified by Karl Fischer titration or an equivalent moisture analyser. Storage at relative humidity above 60 % for more than 4 hours after drying requires re-drying, because moisture regain in amorphous PA12/MACMI is faster than in semicrystalline PA12 due to greater free volume. The same limitation applies to regrind. Dried regrind should be used within 2 hours when exposed to ambient plant conditions at 23 °C and 50 % RH, or re-dried at the same conditions before processing. Uncontrolled moisture is the most common cause of optical defects in transparent polyamide mouldings produced on equipment originally validated for opaque PA12.
Melt temperature at the nozzle should be profiled from rear to front, with rear zones at 240–260 °C, compression and metering zones at 260–280 °C, and nozzle at 270–280 °C. Mould temperature is set between 40 °C and 80 °C; higher mould temperatures reduce residual stress and improve surface replication but extend cooling time. Injection velocity should follow a short rapid fill to 95–98 % of cavity volume, then reduced velocity during hold to avoid jetting and burning at the end of fill. Packing pressure is typically 60–80 % of the first-stage injection pressure and must be maintained until the gate freezes. Clamp force requirements are approximately 0.5–0.8 kN/cm² of projected area for unfilled transparent grades. Shrinkage values in the flow and transverse directions are close; published data under ISO 294-4 indicate total mould shrinkage of approximately 0.5–0.8 %, with anisotropy below 0.1 percentage points in properly balanced tools. Valve-gated hot-runner systems should be validated for colour stability at the gate, because elevated shear rates in the gate orifice can generate discolouration that is not present in cold-runner prototypes. For thick sections above 3 mm, holding time must be extended until the core reaches 80 °C or below to prevent sink marks and vacuum voids.
Table 1 lists representative dry-as-moulded values obtained from publicly available product data and standardised laboratory specimens. Values are not lot-specific guarantees and must be confirmed for each production batch, colour, and post-treatment.
| Property | Unit | Test method | Typical dry value |
|---|---|---|---|
| Density | g/cm³ | ISO 1183 | 1.02 |
| Tensile modulus | MPa | ISO 527-1/-2 | 1700 |
| Yield stress | MPa | ISO 527-1/-2 | 50 |
| Nominal strain at break | % | ISO 527-1/-2 | >50 |
| Charpy notched impact, 23 °C | kJ/m² | ISO 179/1eA | 18 |
| Glass transition temperature | °C | ISO 11357-2 | 155 |
| Vicat softening temperature B50 | °C | ISO 306 | 145 |
| Water absorption, saturation | % | ISO 62 | 3.0 |
| Light transmission, 3 mm plaque | % | ASTM D1003 | 90 |
| Haze, 3 mm plaque | % | ASTM D1003 | <3 |
Table 2 summarises the principal processing envelope described above.
| Parameter | Unit | Range or target | Reference |
|---|---|---|---|
| Drying temperature | °C | 80 | Desiccant dryer |
| Drying time, sealed bag | h | 4–8 | Manufacturer processing guide |
| Maximum retained moisture | % | <0.10 | Karl Fischer titration |
| Melt temperature, nozzle | °C | 250–280 | Validated injection window |
| Mould temperature | °C | 40–80 | Validated injection window |
| Clamp force | kN/cm² | 0.5–0.8 | Projected area |
| Holding pressure | % of injection pressure | 60–80 | Gate-seal requirement |
| Total mould shrinkage | % | 0.5–0.8 | ISO 294-4 |
Grilamid® TR 90 is another amorphous PA12/MACMI grade with higher notched impact strength in published ISO 179/1eA data; TR 55 is selected when easier melt flow in thin-wall tools is required. The two grades differ mainly in molar mass distribution and viscosity curve, not in chemical family. Compared with semicrystalline PA12, TR 55 has no crystalline melting plateau, lower tensile modulus decay above the glass transition, and higher optical clarity. Compared with aromatic transparent polyamides based on PA6I/6T or PAMACM12, the PA12/MACMI structure provides lower density and generally lower water uptake, but it has a lower continuous-use temperature ceiling because the glass transition is below that of some high-Tg amorphous polyamides. Glass-reinforced transparent polyamides sacrifice contact clarity because fibre-matrix refractive index differences are large; TR 55 is unfilled and retains true light transmission. Direct comparison of TR 55 with other EMS grades should use the same test specimen geometry and conditioning state; published data for this specific configuration is limited where fillers, colourants, and processing thermal history differ.
Chemical resistance testing is typically performed using immersion or bent-strip methods according to ISO 175 and ISO 22088-3. The material resists aliphatic hydrocarbons, oils, greases, dilute aqueous salt solutions, and many alcohol-based cleaners at room temperature. Environmental stress cracking resistance in isopropanol and ethanol is superior to polycarbonate under the same test configuration, but published data for this specific configuration is limited because stress-crack initiation depends on moulded-in stress, gate location, and contact time. Strong acids, oxidising media, and phenolic compounds are not recommended; aqueous service above 80 °C is outside the typical design envelope for unfilled amorphous PA12/MACMI. For fluid-handling applications, long-term chemical compatibility must be tested in the finished part at service temperature and stress.
In medical device applications, selected transparent grades are used in luer fittings, filter housings, and diagnostic components. Biocompatibility data are lot- and supplier-specific; manufacturers may supply cytotoxicity test data according to ISO 10993-5, but this does not replace finished-device validation under ISO 10993-1. Food-contact status is grade-specific and may be based on FDA 21 CFR 177.1500 or EU Regulation 10/2011; current certificates of compliance must be obtained from the compounder before commercial use. In automotive optical systems, the material may be used for interior sensor lenses and transparent covers where chemical resistance to automotive interior cleaners and dimensional stability under 85 °C hot-air exposure are required. In industrial sight glasses and filter bowls, the combination of clarity, low density, and resistance to aliphatic oils replaces glass-reinforced PA12 where weight or impact toughness are governing constraints. Processors should validate colour stability and transmission after each regeneration cycle; regrind levels above 20 wt% are not recommended for optical parts unless re-qualified.