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EMS-Grivory Grilamid TR 90 NZ Nylon 12, Dry

    • Product Name: EMS-Grivory Grilamid TR 90 NZ 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 215957
    Material Polyamide 12 (Nylon 12)
    Density Dry 1.06 g/cm³
    Tensile Modulus Dry 1600 MPa
    Tensile Yield Stress Dry 60 MPa
    Elongation At Break Dry 50%
    Charpy Notched Impact Strength 23 C Dry 10 kJ/m²
    Glass Transition Temperature 155°C
    Water Absorption 24 H 0.3%
    Refractive Index 1.566
    Visible Light Transmission 90%

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

    Packing & Storage
    Packing Supplied in 25 kg sealed, moisture-proof bags ensuring dry storage; keep tightly closed and protected from moisture.
    Container Loading (20′ FCL) 20′ FCL loaded with palletized, dry Grilamid TR 90 NZ Nylon 12, securely stowed and ventilated to prevent moisture damage.
    Shipping EMS-Grivory Grilamid TR 90 NZ Nylon 12 (dry) ships as a non-hazardous thermoplastic resin. It is moisture-sensitive, so use sealed, vapor-barrier packaging and avoid prolonged exposure to humidity. No special hazmat requirements apply; standard dry freight is suitable, with protection from rain and condensation during transit.
    Storage Store in a cool, dry place, ideally below 30°C (86°F). Keep the material in its original sealed packaging to prevent moisture absorption, which can degrade properties. Avoid exposure to direct sunlight, heat sources, and humidity. Use within a reasonable timeframe after opening, and reseal tightly to maintain dryness. Keep away from oxidizing agents and dust contamination.
    Shelf Life Shelf life is approximately 2 years when stored unopened, dry, and at room temperature in original packaging.
    Application of EMS-Grivory Grilamid TR 90 NZ Nylon 12, Dry

    Production-scale injection molding of spectacle fronts and temples from EMS-Grivory Grilamid TR 90 NZ, a dry-supplied transparent polyamide 12 grade, is governed by a narrow moisture-control envelope rather than a conventional pellet-to-part sequence. Manufacturer documentation and converter records position the dry-molded density at approximately 1.00 g/cm³ by ISO 1183-1:2019 and dry tensile modulus near 1,500–1,600 MPa by ISO 527-1:2019/ISO 527-2:2012. The plastication unit on commercial lines is normally a three-zone general-purpose screw with 22:1 to 25:1 L/D and 2:1 to 2.5:1 compression ratio, operating with a melt temperature of 240–270 °C, mold temperature of 70–90 °C, and screw back pressure held below 80 bar to limit shear overheating and free-radical generation. The as-supplied dry grade is conditioned below 0.10% residual moisture; once opened, bulk resin exposed to relative humidity above 60% for more than 30 min must be re-dried at 80 °C for 4–6 h in a desiccant dryer with -40 °C dew point. Hydrolysis from residual moisture produces silver streaking, viscosity drift, and reduced impact resistance in thin temple sections. The formulation at the press is typically 96–100 wt% virgin dry pellets, 1–3 wt% transparent polyamide-based color masterbatch, and 0.2–0.5 wt% external lubricant only where demolding torque increases; regrind usage above 20 wt% is avoided for optical-grade fronts because residence-time distribution broadens and haze formation becomes measurable. The downstream production process uses multi-cavity hot-runner tooling with valve-gated drops into polished A1 cavity surfaces, with gate positions biased toward temple lug intersections to move weld lines outside the central visual field. Terminal finished part types include prescription frame fronts, sun fronts, children’s frames, and shield-style frame components qualified under EN ISO 12870:2016 with particular attention to sweat resistance, dimensional recovery, and stress-cracking resistance.

    The principal process conflict in optical-grade frame molding is balancing packing pressure against orientation stress. Hold pressure in the 600–900 bar hydraulic-intensification range is required to control sink marks along thick brow and temple arms, but excessive packing induces frozen-in orientation that appears as stress fringes when inspected by polariscope. Production lots are commonly screened by polarized-light imaging for stress-induced birefringence; acceptance thresholds must be derived from optical distortion requirements and cannot be transferred across part geometries. Published data for this specific grade’s stress birefringence as a function of hold pressure is limited, and converter validation should include spiral-flow and pressure-retention studies on the intended tooling to avoid gate-freeze inconsistency and orientation-induced dimensional recovery after 48 h at 50 °C.

    Processing-window reference for selected downstream molding categories
    Downstream sectorDrying threshold and required equipmentMelt temperatureMold temperatureSpecial processing constraint
    Spectacle frames≤0.10% moisture; desiccant dryer at 80 °C/-40 °C240–270 °C70–90 °CRegrind ≤20 wt%; polariscope inspection
    Medical housings≤0.10% moisture; closed hopper dryer240–265 °C70–90 °CISO 14644-1:2015 Class 8 cleanroom
    Automotive optical covers≤0.08% moisture; dew point -40 °C250–270 °C80–100 °CNo IR absorber above 0.01 wt%
    Cosmetic closures≤0.10% moisture; desiccant dryer240–265 °C60–80 °CInjection velocity >120 mm/s
    Protective eyewear≤0.10% moisture; desiccant dryer245–265 °C70–90 °CPost-mold plasma treatment before coating
    Filter housings≤0.08% moisture; desiccant dryer250–270 °C80–100 °CThick-wall pack-and-hold until gate freeze

    What limits repeated steam autoclave use in transparent polyamide 12 medical housings?

    Steam sterilization at 121 °C for 15 min or 134 °C for 3 min is the defining threshold for transparent reusable medical housings, because moisture ingress and transient thermal expansion occur simultaneously. For EMS-Grivory Grilamid TR 90 NZ, the processing formulation is generally 100 wt% virgin dry resin, with 0.5–2.0 wt% masterbatch only where color coding is required and 0.2–0.6 wt% processing stabilizer added by the compounder; impact modifiers are omitted where lens-like transparency is required. The downstream manufacturing route is cleanroom injection molding under ISO 14644-1:2015 Class 8 or better, using closed hopper dryers, positive-pressure laminar-flow conveyance, and polished mold surfaces to reduce particulate contamination. Typical melt temperature is 240–265 °C, mold temperature is 70–90 °C, and screw speed is trimmed to avoid splay at thin window sections. Terminal finished products include clear surgical instrument housings, diagnostic device covers, irrigation control bodies and fluid connectors. Quality and regulatory alignment requires ISO 13485:2016, with biological evaluation per ISO 10993-1:2018 and cytotoxicity screening per ISO 10993-5:2009; where the article may fall under food-contact pathways, converters additionally screen against FDA 21 CFR 177.1500 and Regulation (EU) No 10/2011.

    The primary operational boundary is cumulative moist-heat exposure. Absorbed water plasticises the amorphous polyamide network, lowers the glass-transition-dominated service temperature, and shifts dimensions during cooling; repeated autoclaving can produce surface haze and microcracking at metal inserts or weld lines. Published data for this specific grade under repeated 134 °C autoclave cycling is limited, so suppliers do not permit material-level substitution for device-specific validation under ISO 17665-1. Molded parts with wall sections above 3.0 mm or internal threaded inserts require post-molding stress relief and dimensional checks after 5 and 10 cycles. Hot-water pre-cleaning above 80 °C is a known incompatibility for insert-bearing housings because differential thermal expansion and interfacial moisture uptake can initiate radial cracks around metal bosses.

    Compliance checklist matrix for selected downstream sectors
    Downstream sectorRegulatory or quality anchorStandard designationValidation focus
    Spectacle framesOphthalmic spectacle frame testingEN ISO 12870:2016Dimensional recovery, sweat resistance
    Medical housingsBiological evaluation and QMSISO 10993-1:2018, ISO 13485:2016Sterilization cycles, cleanroom molding
    Automotive optical coversEnvironmental simulation and foggingISO 16750-4:2010, DIN 75201:2011Optical transmission, laser welding
    Cosmetic closuresCosmetic packaging and chemical resistanceRegulation (EC) No 1223/2009, ASTM D543Stress-crack screening
    Protective eyewearPersonal protective equipmentEN 166:2001, Regulation (EU) 2016/425Impact, UV exposure
    Filter housingsFood-contact and drinking-water plasticsFDA 21 CFR 177.1500, NSF/ANSI 61Migration, burst pressure

    Automotive lidar and camera cover resin: moisture uptake, laser weldability, and fogging resistance

    Two-shot assembly of automotive optical sensor modules imposes simultaneous requirements on a transparent cover resin: near-infrared transmission, resistance to windshield-washer fluid and road-salt splash, and low birefringence after thermal cycling. In this sector, the addition ratio for a clear cover is 100 wt% virgin EMS-Grivory Grilamid TR 90 NZ, because any near-infrared absorber, including many black masterbatches, is excluded above 0.01 wt% to preserve transmission at diode wavelengths around 850–1,060 nm. Where a UV-capping or color function is specified, 0.3–0.8 wt% UV stabilizer and 1–2 wt% color masterbatch are added with spectrophotometric verification of transmission. Where masterbatches are used, converters typically purchase concentrates compounded on L/D 40:1 co-rotating twin-screw extruders, because single-screw dilution at the press cannot guarantee sufficient dispersion. The downstream process is typically single- or two-cavity injection molding with high-pressure closure and sequential valve gating to minimize orientation birefringence; mold temperature is held at 80–100 °C and melt temperature at 250–270 °C. Terminal finished product types include camera module covers, lidar windows, sensor bezels and transparent front covers for driver-monitoring systems. Component qualification usually includes environmental cycling per ISO 16750-4:2010, xenon-arc aging per ISO 4892-2:2013, and fogging assessment per DIN 75201:2011. The main process conflict is packing-pressure control: insufficient packing leaves sink over bosses, while excessive packing creates stress birefringence that can distort optical signals. Published data on transmission stability after 1,000 h of xenon aging for this exact grade is limited, so module-level validation with production coatings is mandatory.

    When ester-rich cosmetic formulations contact transparent polyamide closures

    Packaging converters frequently qualify EMS-Grivory Grilamid TR 90 NZ for fragrance caps, cream jar covers, lipstick components and transparent over-caps because its low equilibrium moisture uptake reduces dimensional change in humid bathroom environments; supplier water-absorption data are generated under ISO 62:2008. The limiting technical criterion is environmental stress-crack resistance, not mechanical strength. The formulation at the press is typically 98–100 wt% virgin dry pellets, 1–2 wt% cosmetic-grade color masterbatch, and 0.2–0.5 wt% internal release agent only where severe ejection geometry demands it. The downstream process is thin-wall injection molding with screw diameters of 25–35 mm, melt temperature 240–265 °C, mold temperature 60–80 °C, and injection velocities above 120 mm/s to fill thin clamshell sections before freeze-off. Terminal finished products include transparent packaging closures, collar components, over-caps and decorative outer shells. Regulatory screening for the packaged article is governed by Regulation (EC) No 1223/2009 and REACH Annex XVII; where food-contact use is possible, converters also screen under Regulation (EU) No 10/2011 and FDA 21 CFR 177.1500. The dominant failure mode is stress cracking in high-aromatic fragrance oils and aggressive ester solvents, which demands static-strain testing under ASTM D543 with the actual formulation at 40–50 °C for 72 h. Sharp threads and undercuts concentrate stress and should be avoided or prototyped before tool steel is cut. Published data for this specific configuration is limited, especially for migration kinetics of low-molar-mass colorants under extended contact.

    Across high-altitude ski and cycling applications, impact loading, ultraviolet irradiance in the 280–400 nm band, and thermal swings from -20 °C to 40 °C push protective-equipment frames toward low-mass, metal-free designs; EMS-Grivory Grilamid TR 90 NZ is selected for goggle frames, visor frames, and side-shield components where toughness must be retained without metal inserts. The addition ratio for protective-equipment molding is 96–100 wt% virgin resin, 1–3 wt% color masterbatch, and 0.5–1.0 wt% hindered amine light stabilizer concentrate; anti-fog and hard-coat functionality is applied post-molding through plasma pre-treatment and dip coating rather than compounded into the pellet. The downstream production process is injection molding with polished cavity surfaces and valve-gated hot or cold runner systems, melt temperature 245–265 °C, and mold temperature 70–90 °C. Terminal finished products include ski goggles, visor frames, and protective eyewear components certified under EN 166:2001 where the complete article falls under Regulation (EU) 2016/425. The critical processing issue is anisotropic shrinkage at wall-thickness transitions above 2.5:1, which can generate warp sufficient to compromise lens retention. Published data on coating adhesion after plasma treatment for this specific grade is limited, so coaters must validate wetting and peel adhesion on textured cavity surfaces.

    Clear filter housings expose fracture, chemical compatibility, and dimensional stability trade-offs

    Transparent filter bowls, sight glasses, and flow-monitoring housings molded from EMS-Grivory Grilamid TR 90 NZ require a balance among clarity, pressure resistance, and chemical compatibility in metering and dispensing systems. The formulation addition ratio is 100 wt% virgin dry resin where clarity is non-negotiable; 5–10 wt% impact modifier can be added for larger industrial housings, but this reduces light transmission and increases haze, so it is generally restricted to applications where transparency is secondary. The downstream production process is thick-wall injection molding with conformal cooling channels, melt temperature 250–270 °C, mold temperature 80–100 °C, and pack-and-hold pressure maintained until gate freeze to eliminate internal voids. Terminal finished product types include clear filter bowls for compressed-air service, water-filter housings, chemical-level sight glasses and flow-meter bodies. Applicable compliance screening includes FDA 21 CFR 177.1500 for nylon resins in food-contact use, Regulation (EU) No 10/2011 for plastic food-contact migration, and NSF/ANSI 61 for potable-water components where certification is required. The central processing conflict is that high mold temperature improves transparency and reduces residual stress but extends cycle time and increases post-mold shrinkage. Chemical compatibility is acceptable for aliphatic hydrocarbons, lubricating oils and dilute neutral salts; concentrated acids, phenols, and hot water above 80 °C are known incompatibilities. Published data for burst-pressure retention after prolonged methanol exposure is limited, so converters should validate usable pressure ratings at 60 °C and 95% RH with the final insert and seal stack.

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    Certification & Compliance
    More Introduction

    EMS-Grivory Grilamid TR 90 NZ Nylon 12, Dry is a natural, unreinforced transparent polyamide supplied in a dry moisture state. The designation places the material within the PA12 chemical family, although the amorphous morphology separates it from conventional semicrystalline Nylon 12. Because the polymer backbone is formulated to suppress spherulitic crystallisation, moulded sections retain optical clarity at thicknesses up to approximately 2.0 mm, depending on thermal history and mould surface replication. Published datasheets indicate a density of 1.00 g/cm³ under ISO 1183-1:2019; this is lower than many transparent engineering polymers such as polycarbonate and permits lightweight optical frames and transparent clips where mass reduction is a design requirement. The “Dry” designation refers to the as-supplied moisture condition required for consistent melt processing; it does not imply indefinite moisture stability after opening. The grade is intended for injection moulding and extrusion of profiles, tubes, and films in which a combination of transparency, chemical resistance, and toughness is required.

    Compared with true crystalline Nylon 12, the product is differentiated by the absence of a melting endotherm and by its isotropic light transmission. Conventional Nylon 12 solidifies from a melt into spherulites that scatter visible light; TR 90 NZ retains a rigid amorphous network that does not develop large-scale crystallinity. This distinction changes processing, because no crystallisation plateau is available to hold part dimensions during the cooling phase, and it changes service behaviour, because upper-use temperature is defined by heat deflection and Vicat softening rather than by a crystalline melt temperature.

    What Limits Drying and Melt Handling for Transparent PA12?

    The critical processing boundary for the dry grade is not melting point but moisture control and amorphous melt solidification. Residual moisture above 0.10% by weight is considered the upper limit for melt processing because hydrolysis of the polyamide backbone can reduce molecular weight, generate volatile degradation products, and produce silver streaks at the surface of transparent parts. Desiccant-bed drying at 80°C to 100°C for 4 h to 12 h is specified by processors to reach the required moisture threshold; the exact time depends on initial water content, pellet geometry, and the dew point of the drying air. A dew point at or below -30°C is commonly maintained to ensure the partial vapour pressure gradient removes water from the amorphous polyamide granules.

    After drying, the material should be conveyed in closed, dry-air-purged lines because re-adsorption in an unprotected machine hopper can exceed 0.02% within 30 min under ambient relative humidity above 60%. On production lines, this re-uptake is controlled with hopper dryers at the feed throat or with automated vacuum loading from a central drying cell. Batch-to-batch variance is normally managed by verifying moisture content with a halogen loss-on-drying analyser or Karl Fischer titration before start-up; if measured moisture exceeds 0.12%, the production lot is returned to the dryer.

    Plasticising equipment for the material benefits from a low-compression screw with a polished surface to reduce dead spots. Screw L/D ratios between 20:1 and 24:1 are typical for polyamide processing, and back pressure is maintained below 100 bar to avoid excessive shear heating. Barrel temperature profiles are set from feed to nozzle between 240°C and 280°C, with melt temperature measured directly by an immersion probe rather than inferred from barrel set points. When running in multi-cavity hot-runner tools, thermocouple placement and gate balance are critical because the amorphous melt does not have a latent heat of crystallisation to buffer solidification; gate freeze-off occurs quickly, and local viscosity differences are visible as optical unevenness.

    Comparative Position Against Semicrystalline PA12 and Amorphous Copolyamides

    Grilamid TR 90 NZ is not a glass-reinforced grade; the absence of fibre enables isotropic shrinkage but reduces tensile modulus relative to short-glass polyamides. Semicrystalline Nylon 12, by contrast, develops spherulitic structures that scatter visible light and produce an opaque appearance in natural tones. The density of semicrystalline PA12 is generally around 1.01 g/cm³, while the transparent amorphous grade is specified near 1.00 g/cm³; this difference, though small, becomes material in mass-sensitive applications such as temple arms and optical front frames.

    Typical semicrystalline Nylon 12 has a melting range near 175°C to 180°C; Grilamid TR 90 NZ has no melting endotherm and is instead characterised by an HDT/A value near 110°C to 115°C under ISO 75-1/-2:2020 and a Vicat softening temperature near 145°C under ISO 306:2022. These thermal properties mean the amorphous grade is not suitable for continuous load-bearing service above its Vicat softening point, and designers should verify the specific HDT class under the relevant applied stress rather than relying on melt temperature references used for semicrystalline PA12.

    PropertyTest methodRepresentative dry-state value
    DensityISO 1183-1:20191.00 g/cm³
    Tensile modulusISO 527-1/-2:20121600 MPa
    Tensile stress at yieldISO 527-1/-2:201260 MPa
    Nominal tensile strain at breakISO 527-1/-2:2012>50%
    Charpy notched impact strength, 23°CISO 179-1/1eA:20107–8 kJ/m²
    HDT/A at 1.8 MPaISO 75-1/-2:2020110–115°C
    Vicat softening temperature B50ISO 306:2022145°C
    Water absorption 23°C/50% RHISO 62:20081.5%

    The table values represent the dry state; conditioned values under 23°C and 50% RH show a shift in tensile modulus and yield stress toward lower values as absorbed moisture plasticises the amorphous network. The magnitude of that shift should be measured on moulded plaques using ISO 291:2008 conditioning rather than extrapolated from the dry property set, because part thickness and thermal history affect moisture uptake rate.

    Optical frame production uses the material as a front-frame resin in multi-cavity tools with hydraulically sequenced valve gates to balance filling across left and right rim sections, bridge, and temple hinges. Processing reports from tooling shops indicate cavity filling pressures in the 400 bar to 800 bar range reduce sink marks and gas entrapment, but published data for this exact configuration is limited. After ejection, frames are conditioned in a controlled atmosphere to stabilise dimensions before lens insertion. Because the dry grade takes up moisture and undergoes slight dimensional expansion, unannealed parts measured immediately after demoulding may fail final inspection if the acceptance protocol assumes equilibrium moisture content.

    In automotive clips and fluid connectors, the material is selected for aliphatic hydrocarbon resistance and for greater transparency than semicrystalline PA12. However, the amorphous morphology alters the environmental stress cracking response in alcohol- or glycol-containing media; end-use qualification should follow ISO 22088-2:2006 or a defined OEM test specification. Prolonged exposure to strong acids, phenolic solvents, or high concentrations of certain glycol ethers can soften the surface and reduce retention force in snap-fit designs. Processors therefore avoid combining the dry grade with amines or metal stearates that can catalyse degradation at processing temperatures; published chemical compatibility tables for semicrystalline PA12 do not automatically transfer to the amorphous grade.

    When Thin-Wall Optical Tooling Requires Viscosity Control

    Thin-wall flow behaviour is governed by melt viscosity and fast amorphous solidification. For melt volume-flow rate measurement under ISO 1133-1:2022, the grade is commonly tested at 275°C and 5 kg; processors report MVR between 15 cm³/10 min and 25 cm³/10 min for similar transparent polyamide grades, but the exact value should be read from the supplier’s lot certificate. At wall thicknesses below 1.2 mm, the frozen layer can reach 0.2 mm before complete filling if injection speed is too low; the moulding process therefore uses high injection speeds and short boost times, with switch-over set by screw position rather than injection time.

    Mould temperature is maintained between 60°C and 90°C to delay surface freeze and replicate polish. Below 40°C, the highly polished cavity may cause premature solidification and visible flow lines. Above 100°C, cycle time increases without proportional gains in surface finish, and ejection may degrade due to reduced rigidity at demoulding. For curved optical front frames, differential cooling between the convex rim and thicker temple hinge can induce warpage; cooling channels with separate manifold temperatures are used, but published generic guidelines for this grade require confirmation on the specific tool.

    Regrind use in transparent parts is permitted only at low addition levels because repeated melt processing intensifies yellowing and reduces surface quality. Typical process guidance restricts regrind to 20% by weight when transparency and notched impact retention are critical; published data for this specific grade is limited and the regrind fraction should be validated on the actual cavity set. For high-clarity lenses and front frames, even lower regrind levels may be necessary to avoid visible specks from degraded material.

    The natural NZ designation identifies an unreinforced and unmodified formulation; no fibrous reinforcement, mineral filler, or flame-retardant package is present. In applications requiring outdoor weathering, the base grade should be evaluated with appropriate UV screening because unprotected transparent polyamides can yellow after extended terrestrial UV exposure. The dry state does not imply the presence of an internal lubricant or mould-release additive; converters often specify the supplier’s stabilised variant where UV performance is required. Published data for this exact formulation under long-term outdoor weathering is limited, and accelerated testing under ISO 4892-2:2013 remains necessary before external component qualification.

    Relative to polycarbonate, the PA12-based transparent polyamide offers higher chemical resistance to oils and alcohols but lower modulus and higher water absorption; relative to polymethyl methacrylate, it offers better impact toughness but lower surface hardness and reduced optical clarity. Unlike polysulfone, it does not need the same drying temperatures and may be processed at lower melt temperatures, but its upper-use temperature is also lower. These trade-offs are evaluated with the part geometry and exposure medium; no single resin occupies the same density, toughness, and transparency envelope without some compromise in dimensional stability or chemical resistance.

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