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EMS-Grivory Grilamid TR 55 Nylon 12, Dry

    • Product Name: EMS-Grivory Grilamid TR 55 Nylon 12, 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 664160
    Density 1.06 g/cm³
    Tensile Modulus 2200 MPa
    Yield Stress 60 MPa
    Nominal Strain At Break >50%
    Charpy Impact Strength Notched 11 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 135 °C
    Heat Deflection Temperature 1 80 Mpa 105 °C
    Glass Transition Temperature 155 °C
    Water Absorption Saturation 1.5%
    Moisture Absorption Equilibrium 23 C 50 Rh 0.5%

    As an accredited EMS-Grivory Grilamid TR 55 Nylon 12, Dry factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged as 25 kg net in sealed moisture-proof polyethylene-lined kraft bags, palletized and stretch-wrapped for dry storage.
    Container Loading (20′ FCL) 20-foot full container load of dry EMS-Grivory Grilamid TR 55 Nylon 12 granules, securely packed and shipped.
    Shipping Ship EMS-Grivory Grilamid TR 55 Nylon 12 in sealed, moisture-barrier packaging to preserve its dry state. Avoid prolonged exposure to humidity, extreme heat, or direct sunlight. Transport at ambient temperature in dry, ventilated conditions. Standard non-hazardous handling applies, with secure stacking to prevent bag or drum damage during transit.
    Storage Store in a cool, dry area away from direct sunlight and heat sources. Keep the material in its original, unopened packaging to prevent moisture absorption, which can degrade properties. Avoid exposure to UV radiation and humidity. Ensure good ventilation and handle with clean, dry equipment to maintain optimal processing performance.
    Shelf Life Shelf life is indefinite when stored dry, sealed, and protected from moisture; keep containers tightly closed.
    Application of EMS-Grivory Grilamid TR 55 Nylon 12, Dry

    Where low-pressure chemical skids replace annealed borosilicate sight glass with an injection-moulded transparent polyamide, Grilamid TR 55 dry is processed at a melt temperature of 250 °C to 270 °C and a mould surface temperature of 60 °C to 80 °C. The resin is amorphous and therefore does not develop crystalline spherulite haze in thick sections; however, the absence of crystallinity reduces resistance to hot aromatic solvents and strongly oxidizing aqueous acids. Pre-drying in a desiccant dryer with a dew point below -30 °C at 80 °C for 6 h is required once the sealed liner has remained open for more than 30 min at relative humidity above 60%, because residual moisture above 0.1 wt% produces splay, silver streaks, and gate-area clouding. For a filter bowl with wall stock between 2.5 mm and 3.5 mm, a peripheral edge gate is preferable to a central diaphragm gate; the central gate orientation generates a circular weld line at the core pin and a local pressure drop that produces stress whitening under 0.4 MPa hydrostatic testing. Sequential valve-gate control on multi-cavity tooling reduces shot-to-shot cavity imbalance below 0.5%, but published data for this specific configuration is limited. The finished transparent housing is annealed at 80 °C for 2 h to reduce moulded-in stress before thread cutting and hydrostatic verification according to ISO 22088-2 for environmental stress cracking in detergent solutions.

    What Limits Wall Thickness Reduction in Overmoulded Luer Hubs?

    Thin-wall female Luer hubs produced from Grilamid TR 55 dry encounter a processing conflict between filling pressure and the dimensional tolerance band of ISO 80369-7. Below 1.0 mm nominal wall stock, the shear-heated melt front can degrade in the hot runner gate, producing yellow particles that fail visual inspection after steam sterilization at 121 °C for 15 min. The material is therefore processed at the lower end of the melt temperature window, between 250 °C and 260 °C, with a cold runner and tunnel gate on the outer taper rather than a hot runner drop on the sealing face. For insert-moulded stainless steel cannulas, the gate is placed at the hub base to avoid weld lines on the 6% Luer taper. Residual moisture before moulding is kept below 0.08 wt% by drying at 80 °C for 8 h in a dry-air system with a return-air dew point below -35 °C. The mould surface is held at 65 °C, and the melt cushion is limited to 3 mm to avoid uncontrolled decompression at the screw tip. Cytotoxicity is evaluated under ISO 10993-5:2009 using MEM elution on as-moulded and autoclaved specimens aged in saline at 70 °C for 24 h. Grilamid TR 55 dry is not supplied sterile and is not validated for implant contact; only short-term medical device contact is supported by the resin manufacturer. Published data for repeated extended autoclave cycling on this specific amorphous PA 12 grade is limited, so end-use validation must include optical transmission and leak testing after the worst-case number of reprocessing cycles.

    Silicone release agents are excluded from optical sensor housing production with Grilamid TR 55 dry because silicone migration lowers surface energy and changes the reflected-light signature measured by the sensor element. The tool cavity is polished to SPI A-1 finish and vented with peripheral channels 0.015 mm deep to avoid gas burn at the melt front. Melt temperature is set at 255 °C to 265 °C and the shot volume is kept below 70% of barrel capacity to limit residence time. A reverse-taper check ring and screw L/D of 20:1 maintain a homogeneous melt without high shear. Regrind is limited to 15 wt% and only from clean start-up purgings because dust contamination produces black specks visible at 10× magnification. Moulded housings for laser-scattered light sensors are annealed at 80 °C for 1.5 h and then tested for internal haze after 24 h storage at 23 °C and 50% relative humidity. Dimensional stability during temperature cycling from -20 °C to 70 °C is assessed according to IEC 60068-2-14, with no distortion above 0.05 mm at the window plane. The unfilled amorphous PA 12 cannot match glass fibre reinforced PBT in flexural modulus; this boundary must be considered in long unsupported spans.

    When Coolant Level Indicators Replace PA6-GF30 in Glycol Circuits

    When an OEM replaces a filled PA6-GF30 coolant level indicator with an unfilled transparent polyamide, the loss of stiffness cannot be compensated by simple wall thickening alone because the amorphous PA 12 grade has a lower compressive modulus and a different stress relaxation profile. Grilamid TR 55 dry is dried to 0.08 wt% residual moisture and moulded at a melt temperature of 260 °C to 270 °C with a mould surface at 70 °C. For a 40 mm diameter indicator body with 2.8 mm wall stock, the gate is placed on the non-appearance side and sequential overmoulding of the sealing boss is avoided because a secondary interface creates a hydrolysis path under sustained contact with a 50/50 water-ethylene glycol mixture at 95 °C. The screw design uses a low-shear barrier profile and the back pressure is held below 5 MPa to minimize thermal history. The final body is annealed at 90 °C for 2 h to reduce hoop stress around the threaded boss before pressure cycling from 0.1 MPa to 0.5 MPa at 1 Hz for 100,000 cycles. Hydrolysis resistance is evaluated by exposure in a pressurised autoclave at 121 °C for 100 h followed by tensile impact testing under ISO 527-2; the acceptable shift is defined by the OEM rather than a universal numeric requirement. Grilamid TR 55 dry is not a drop-in replacement for glass reinforced polyamide in mounting brackets; metal-to-polymer joint design must be re-validated for thread pull-out and creep at the 80 °C continuous service boundary. Published data for this specific glycol circuit configuration is limited, so prototype testing on production-scale moulding cells is required.

    Water Jet Flow-Meter Transparent Chambers and NSF/ANSI 61 End-Use Limits

    Transparent impeller housings for potable water flow meters rely on the low moisture-induced dimensional change of amorphous PA 12 relative to PA6, but incorporation of an NSF/ANSI 61 certification is lot-specific and cannot be assumed from the base resin declaration. The chamber is moulded with a collapsible core to produce a 1.6 mm side wall and an ACME thread at the inlet boss; the melt temperature is limited to 255 °C because water contact applications demand minimal thermal degradation by-products. Drying follows the same 80 °C / 6 h desiccant profile to 0.08 wt% residual moisture, and the hopper is purged with dry nitrogen to avoid moisture regain during long production runs. The gate is a fan gate on the outlet boss, positioned to avoid flow marks across the impeller viewing window. After moulding, the chamber is pressure-tested at 1.5 MPa for 10 s with no permanent deformation above 0.03 mm measured on the outer diameter. Long-term water exposure at 60 °C is evaluated under ISO 62 for water absorption and under ISO 527-2 for tensile property retention after 1,000 h. The use of external lubricants is avoided because silicone or ester films can release into the potable water and alter disinfection by-product profiles. A compliance matrix for the material in fluid-contact segments is given in the following table.

    SegmentStandard or methodVerification condition
    Potable water contactNSF/ANSI 61Certification on commercial lot, not base resin
    Food contactFDA 21 CFR 177.1500Nylon resin specifications, extractives
    Medical LuerISO 80369-7Dimensional gauge after ageing
    CytotoxicityISO 10993-5:2009MEM elution
    Chemical process transparencyASTM D1003Haze / light transmittance, 2 mm plaque
    Environmental stress crackingISO 22088-2Bent strip in detergent solution

    Cosmetic Packaging Gate Vestige Standards Vary by Wall Stock

    For thick-walled transparent closures, the gate vestige on the visible surface is controlled by wall-stock-dependent tooling practices rather than a uniform standard. In a 4.0 mm refillable lipstick mechanism collar, a valve-gated hot runner is used because the larger gate diameter reduces shear heating and gate blush; the nozzle tip temperature is held within ±3 °C of the 260 °C melt set point. The material is processed from sealed drying carts to avoid moisture uptake in the cleanroom. A 2 wt% polyamide-12 carrier masterbatch is let down for tinted transparent variants, while polyolefin carrier masterbatch is excluded because it creates interfacial haze. Dimensional testing after 48 h conditioning at 23 °C and 50% RH uses ISO 294-4 shrinkage plaques and non-contact optical gauging.

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    Certification & Compliance
    More Introduction

    EMS-Grivory Grilamid TR 55 is a transparent polyamide 12 injection-moulding compound supplied and tested in the dry-as-moulded condition. The grade designation TR 55 identifies an unfilled transparent polyamide within the Grilamid TR family; “Dry” indicates that the mechanical and thermal values in the supplier’s technical documentation are generated on specimens stored under dry conditions and not on moisture-conditioned test bars. The polymer backbone is built around C12 aliphatic/cycloaliphatic units, giving a transparent moulded part with a density of 1.06 g/cm³ measured according to ISO 1183-1. The material is therefore outside the standard semicrystalline PA12 segment: the solid-state optical clarity places it in the transparent-polyamide class, while the PA12 chemistry contributes lower water uptake than typical PA6 or PA66 transparent formulations. The dry condition is relevant because polyamide properties shift after equilibrium moisture uptake; design calculations based on dry-as-moulded data must account for service humidity.

    Property values obtained under ISO 527-2, ISO 179-1 and ISO 75-2

    The following values are typical dry-moulded data from EMS-Grivory grade documentation, not specification minima. Lot-specific certificates of analysis should be used for production release.

    PropertyMethodUnitDry value
    DensityISO 1183-1g/cm³1.06
    Water absorption, saturation in water at 23 °CISO 62%3.5
    Water absorption, equilibrium at 23 °C and 50 % RHISO 62%1.0
    Tensile modulusISO 527-1/-2MPa1600
    Tensile yield stressISO 527-1/-2MPa45
    Tensile yield strainISO 527-1/-2%5
    Nominal strain at breakISO 527-1/-2%>50
    Notched Charpy impact at 23 °CISO 179-1/1eAkJ/m²10
    Notched Charpy impact at −30 °CISO 179-1/1eAkJ/m²7
    Ball indentation hardnessISO 2039-1MPa100
    Heat deflection temperature, 1.8 MPaISO 75-2°C100
    Heat deflection temperature, 0.45 MPaISO 75-2°C140
    Vicat softening temperature, VST/A50ISO 306°C135
    Coefficient of linear thermal expansion, 23–55 °CISO 11359-210-4/K1.2
    Light transmission at 2 mmISO 13468-2%88
    Flammability at 1.6 mmUL 94classHB

    The tensile modulus of 1600 MPa and tensile yield stress of 45 MPa define a stiff but ductile response in the dry state. The nominal strain at break above 50% indicates that short-term tensile overload is more likely to produce yielding than immediate brittle fracture at room temperature. The notched Charpy value of 10 kJ/m² at 23 °C is relevant for transparent components with stress concentrations such as threaded inserts, snap-fit arms, and fluid-port bosses. Moisture conditioning will reduce tensile modulus and yield stress while generally raising impact energy; conditioned data should be requested when the application operates continuously above 50 % RH.

    What happens if the pellet is moulded without a dew-point-controlled drying step?

    Polyamide 12 absorbs moisture from ambient air, and the equilibrium water content at 23 °C and 50 % RH is close to 1.0 wt%. This is approximately one order of magnitude above the recommended process moisture limit of <0.10 wt%. Hydrolytic degradation occurs when wet pellets are melted in the barrel at 220–250 °C, reducing molecular weight and causing surface splay, bubble formation, loss of notched impact strength, and inconsistent optical clarity. Drying should be performed in a closed-loop desiccant dryer with a return-air dew point of −30 °C or lower. A drying temperature of 80 °C for 4–6 h is typical for cold or moderately pre-dried pellets; longer residence may be needed if sacks have been opened under high humidity. Above 90 °C, prolonged drying can produce discoloration and should be avoided.

    Moisture content should be verified by ISO 15512 or an equivalent calibrated method before start-up. Production-scale dryers should be sized so that hopper residence time matches throughput and the pellet bed is not short-circuited. The material should not be left in a heated hopper overnight without dry-air purge. In campaigns where ambient relative humidity exceeds 60 %, pre-drying is mandatory even for new packaging because condensation on cold pellet surfaces can be transferred into the feed throat.

    For injection moulding, a melt temperature range of 220–250 °C is applied. The barrel profile is generally flat to slightly rising, and the mould temperature is maintained between 50 °C and 80 °C. The lower mould-temperature range may be used for fast cycle times with thin-walled optical parts, but surface ripple and flow-line visibility should be monitored. Hot-runner systems require independent temperature control within the same melt-temperature window, and residence time at temperature should be minimized. A conventional polyamide screw with effective L/D of 20–25 and low compression is acceptable for unfilled transparent grade. Back pressure should be sufficient to homogenize the melt without excessive shear heating, particularly in 12–18 mm light-cavity tooling where melt-temperature overshoot can produce local yellowing.

    When chemical resistance and transparency are specified for fluid-handling equipment

    Grilamid TR 55 is used where a transparent part must remain clear during intermittent contact with aliphatic hydrocarbons, mineral oils, greases, and diesel fuel. The PA12-based structure provides a different stress-cracking mechanism than polycarbonate, which is prone to environmental stress cracking in the presence of oil, grease, and polar hydrocarbons. Components such as sight-glass covers, filter bowls, oil-level indicators, and fluid-reservoir windows are therefore evaluated under ISO 2812 immersion protocols rather than by visual inspection alone. Published data for specific end-use fuel blends or aggressive additives is limited; immersion testing in the actual fluid at the maximum service temperature is required.

    The material is not specified for continuous service with strong acids, oxidizing media, chlorinated solvents, or steam above 60 °C without end-use testing. Applications involving hot-water exposure, glycol-water mixtures, or brake fluid should be qualified with conditioned mechanical data and dimensional change measurements because absorbed moisture and polar fluids shift both stiffness and part dimensions. Metal inserts and bearing surfaces require tolerance stacks that allow for the moisture-related dimensional movement typical of polyamides.

    Distinctions from semicrystalline PA12 and polycarbonate alternatives

    Standard semicrystalline PA12 grades are optically opaque or translucent because of crystallite scattering. Grilamid TR 55 retains the PA12 chemical resistance profile but is formulated to suppress crystallinity sufficiently for light transmission of 88% at 2 mm. The density of 1.06 g/cm³ is lower than that of polycarbonate at approximately 1.20 g/cm³, but higher than standard semicrystalline PA12 at approximately 1.01 g/cm³. The heat deflection temperature under 1.8 MPa of 100 °C is below typical glass-reinforced PA12 and below many polycarbonate grades, so the grade is not selected for high-temperature optical glazing.

    Compared with polycarbonate, Grilamid TR 55 is specified where aliphatic fuel and oil resistance under stress is the primary failure mode. Compared with impact-modified PMMA, the polyamide grade offers higher notched impact resistance and better resistance to solvent stress cracking, but lower surface hardness and lower modulus. Within the EMS-Grivory transparent polyamide range, grades such as TR 90 are available where higher heat deflection is required; the appropriate choice is determined by the combination of service temperature, chemical exposure, and impact loading. Processing conditions for TR 55 remain within the standard polyamide window, but the transparent dry-moulded condition requires tighter melt-temperature and moisture control than semicrystalline PA12 extrusion or injection grades.

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