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EMS-Grivory Grilamid® L 25 Z PA12-I

    • Product Name: EMS-Grivory Grilamid® L 25 Z PA12-I
    • 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 737671
    Material Polyamide 12 (PA12), impact modified
    Density 1.03 g/cm³
    Melting Point 178 °C
    Tensile Modulus 1700 MPa
    Tensile Stress At Yield 50 MPa
    Elongation At Break >50%
    Charpy Notched Impact Strength At 23 C No break
    Charpy Notched Impact Strength At 30 C 20 kJ/m²
    Shore D Hardness 65
    Heat Deflection Temperature 1 8 Mpa 50 °C
    Heat Deflection Temperature 0 45 Mpa 150 °C
    Water Absorption Saturation At 23 C 1.6%
    Moisture Absorption 23 C 50 Rh 0.7%

    As an accredited EMS-Grivory Grilamid® L 25 Z PA12-I factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing EMS-Grivory Grilamid® L 25 Z PA12-I is supplied as granules in sealed, moisture-protective 25 kg bags.
    Container Loading (20′ FCL) Grilamid® L 25 Z PA12-I granules packed in 25 kg bags, palletized, loaded standard into 20′ FCL for safe transport.
    Shipping Ship as non-hazardous plastic granules in sealed, moisture-proof packaging to prevent absorption. Keep dry, away from heat and direct sunlight. No special transport classification required. Avoid excessive stacking and handle gently to preserve bag integrity. Ensure warehouse ventilation and temperature control below 40°C.
    Storage Store in original sealed packaging in a cool, dry, well-ventilated area away from direct sunlight, heat, and moisture. Keep container tightly closed to prevent water absorption, which can affect processing and properties. Avoid exposure to excessive humidity or temperatures above 25°C. Use within recommended shelf life to maintain quality.
    Shelf Life Store in original sealed packaging, cool and dry. Shelf life is typically two years from production date.
    Application of EMS-Grivory Grilamid® L 25 Z PA12-I

    In diesel fuel return lines routed along chassis rails, low-temperature impact retention after road salt aerosol and fuel condensate exposure determines whether a line survives cold-soak assembly and field flexing. The compound is extruded with 100 wt% Grilamid L 25 Z PA12-I as the base resin; carbon black masterbatch is added at 2.0–4.0 wt% only when UV exposure on exposed frame sections is specified. No external plasticizer is introduced, because the impact-modification phase already shifts the ductile-to-brittle transition below -40 °C, validated by notched impact testing under ISO 179-1. Low-permeation fuel line assemblies align with SAE J2260, and burst-pressure retention is measured after 500 h fuel exposure according to the pressure/vacuum pulse methodology in ISO 19013-1. The downstream production process uses a 45 mm single-screw extruder with L/D 25–30 and barrier mixing elements; resin is pre-dried at 80 °C for 4–6 h to residual moisture below 0.10 wt%, and barrel zones are set from 200 °C at the feed throat to 240 °C at the die. On a 45 mm line, die pressure stabilizes only after the metering zone reaches 238–242 °C; below this range, surface melt fracture appears as shark-skin on 8 mm OD thin-wall tube. Vacuum sizing and a 60 °C water bath maintain 6–10 mm OD within ±0.05 mm at 1.0–1.5 mm wall. The terminal products are cut-to-length diesel fuel return tube assemblies supplied to commercial vehicle and off-highway engine manufacturers.

    Pneumatic actuation line requirements in high-cycle assembly cells

    High-cycle pneumatic actuators in semiconductor packaging and robotic assembly cells subject tubing to rapid decompression, repeated fitting insertion, and synthetic ester carryover from oil-mist-lubricated compressors. In this configuration, Grilamid L 25 Z PA12-I is formulated as the base resin at 95–98 wt% with a color and processing-stabilizer masterbatch at 2–5 wt%; no external plasticizer is added. Connections are designed to ISO 14743 push-in fitting geometry, and production lots are validated for leak-tightness at 1.5 times nominal working pressure after 1,000 insertion/withdrawal cycles. Dimensional stability is checked on a calibrated optical comparator because a variation of more than ±0.05 mm in outer diameter changes push-in seal retention force. The downstream process is single-screw tube extrusion on a 30 mm or 45 mm line with L/D 25–28; melt temperature is held at 220–245 °C and vacuum sizing is performed through a water bath at 50–70 °C. The material is pre-dried at 80 °C for 4–6 h to below 0.10 wt% moisture because residual moisture above this threshold generates inline voiding and reduces burst consistency. Finished product is coiled in 25 m or 50 m rings. Terminal products are pre-cut pneumatic tubing and coiled assemblies for end-of-arm tooling, high-cycle pick-and-place modules, and semiconductor packaging equipment.

    Why Is Impact-Modified PA12 Retained When Brake Coil Tubing Is Cold-Soaked Below -40 °C?

    Heavy commercial vehicle air brake coils are repeatedly flexed during coupling and uncoupling, and the tube surface is exposed to road de-icing salts, diesel spray, and ultraviolet radiation in northern service. The compound is processed at 100 wt% Grilamid L 25 Z PA12-I with an ultraviolet-stabilized black masterbatch at 2.0–3.5 wt% for the outer layer; the bore remains unfilled to maintain smooth airflow and avoid particulate release into brake circuits. Performance is evaluated under SAE J844 for air brake tubing, and cold-flexibility plus burst tests are conducted after conditioning at -40 °C for 4 h. The extrusion process uses a 50 mm grooved-feed single-screw extruder with L/D 30 and a screw designed for high-viscosity polyamide; barrel temperatures run from 210 °C at the feed zone to 235 °C at the die, and the vacuum-sized tube is heat-set at 120 °C for 30 min to suppress recoil memory during uncoiling. Field observation on a 50 mm line shows that maintaining the compression zone at 220–230 °C is critical; excursions above 235 °C lower melt viscosity enough to produce wall-thickness variation at the coiling stage. Terminal products include straight air brake tubing and coiled assemblies in 8 mm, 10 mm, and 12 mm OD with push-in or compression fittings.

    Processing parameterSet rangeUnitEquipment note
    Predrying temperature80°C4–8 h to residual moisture ≤ 0.10 wt%
    Feed zone200–220°CSingle-screw barrier section
    Compression zone220–230°CModerate shear mixing
    Metering zone230–245°CStable die pressure required
    Die head230–240°CMinimum residence time
    Vacuum sizing water bath50–70°COD tolerance ±0.05 mm
    Heat-set annealing120°C30 min for coil memory
    Injection mold temperature40–80°COptional overmolding

    When ethylene glycol-water coolant circulates at 85 °C through battery pack cold plates, the tube wall is simultaneously exposed to electrochemical potential differences at quick-connect interfaces, thermal oxidation, and flexural stress from pack expansion. Grilamid L 25 Z PA12-I is employed as the base resin at 100 wt% with a hydrolysis-resistant stabilization package added at 0.5–1.5 wt%; conductive carbon black is excluded unless static dissipation is explicitly required because it shifts elongation at break and increases weld-line sensitivity in heat-bent sections. Industry validation for such thermal management lines is governed by OEM-specific coolant system specifications derived from REACH and RoHS Directive 2011/65/EU restrictions, with mechanical property retention tested under ASTM D638-14 after 1,000 h at 125 °C in 50/50 ethylene glycol/water, and low-temperature impact checked after -40 °C conditioning. The downstream production process begins with pre-drying at 80 °C for 5–8 h to below 0.08 wt% moisture, followed by extrusion at 220–250 °C into straight sections that are heat-bent into three-dimensional coolant routing on a 160 °C forming fixture. Wall thickness is maintained at 1.0–1.5 mm, and OD is held to ±0.05 mm for quick-connect sealing. Terminal products are formed battery pack coolant line assemblies with quick-connector ends for electric vehicle thermal management.

    When cable protection conduits are subjected to stone impingement and engine compartment ozone

    Under-hood and off-road cable protection conduits absorb stone impingement, diesel aerosol, hot oil mist, and ultraviolet radiation while shielding wire harnesses from abrasion. The impact-modified PA12 compound is run at 90–95 wt% Grilamid L 25 Z PA12-I with a stabilizer and color masterbatch at 5–10 wt% for extended outdoor exposure; if a flame-retardant variant is required, published data for this specific impact-modified grade are limited and must be confirmed by melt-flow stability and smoke-density screening, because halogenated additives can shift extrusion viscosity and promote die-lip deposit formation. Compliance for the finished conduit assembly is assessed under RoHS Directive 2011/65/EU and REACH SVHC restrictions, with flammability classed under UL 94 HB unless a validated flame-retardant formulation has been used. Weathering and heat-aging are tested under ISO 4892-2 and ISO 188 at 100 °C for 500 h; visual crazing and surface cracking are used as failure criteria. The downstream process is profile extrusion on a 60 mm single-screw extruder with corrugator blocks maintained at 40–60 °C; melt temperature is 230–250 °C and the resin is pre-dried to 0.10 wt% moisture. The extruded profile is slit or left unslit and wound into reels. Terminal products are corrugated cable protection tubes for agricultural, construction, and mining harness assemblies.

    Subsea unbonded flexible risers impose a combination of hydrostatic collapse resistance, methanol-assisted aging, and retained ductility in sour gas service. In this application, Grilamid L 25 Z PA12-I is extruded as the internal pressure sheath from 100 wt% base resin with a processing stabilizer package below 1.0 wt%; no fillers are introduced because filler particles can act as nucleation sites for microvoids when the sheath is exposed to methanol and carbon dioxide at 60 °C. Industry compliance for flexible pipe polymer sheathing is governed by API Spec 17J and ISO 13628-2, with chemical resistance screening under ISO 22088 environmental stress cracking and retained elongation after aging. The liner is produced on a heavy-duty single-screw extruder with 25–30 L/D, barrel temperatures 210–250 °C, and melt temperature controlled to 240 °C maximum; the resin is pre-dried to 0.05 wt% moisture in a closed desiccant hopper because the high-viscosity grade absorbs moisture and can hydrolyze in the melt. The extrudate is applied over a stainless steel carcass and cooled in controlled stages to reduce residual stress and shrink voids; thickness is maintained between 5 mm and 12 mm. Terminal products are unbonded flexible flowlines and risers for subsea oil and gas production and gas lift.

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    Certification & Compliance
    More Introduction

    EMS-Grivory Grilamid® L 25 Z is an unreinforced impact-modified polyamide 12 injection-moulding grade identified under ISO 1874-1 as PA12-I. The product is supplied as cylindrical granules and is specified for high-flow injection moulding of thin-wall technical components. Manufacturer-published property values include an ISO 1183-1 density of 1.01 g/cm³, an ISO 11357-1/-2 melting peak of 178°C, and an ISO 62 moisture uptake of 0.7% at 23°C/50% RH. The melt volume-flow rate is determined under ISO 1133-1 at 275°C/5.0 kg; product-specific values in the current EMS technical datasheet should be used for gate sizing, because impact-modified PA12-I grades in this viscosity class typically span 15–30 cm³/10 min. The combination of a PA12 backbone with impact modification shifts the ductile-brittle transition below 0°C while maintaining a moisture absorption roughly one-third that of PA6 and PA66. The grade is therefore used in connectors, clips, pneumatic couplings, cable ties, and housings in which dimensional stability under humid air and resistance to aliphatic hydrocarbons are required simultaneously. It is not a structural high-modulus material; ISO 527-1/-2 tensile modulus remains below 2000 MPa, and continuous load-bearing functions should be transferred to reinforced PA12 grades unless creep testing under defined load and temperature has been completed.

    What Distinguishes Grilamid® L 25 Z from Unmodified PA12 Grades?

    Impact modification alters the mechanical failure envelope while leaving the base PA12 chemical resistance largely intact. Under ISO 179-1/1eA notched Charpy testing, the impact-modified grade retains a meaningful fraction of its ambient impact energy at −30°C, whereas unmodified low-viscosity PA12 grades typically fall below 5 kJ/m² in the same specimen geometry. The low-temperature response is obtained at the cost of a 10–15% reduction in tensile modulus relative to unmodified high-flow PA12; published ISO 527-1/-2 values for the impact-modified composition lie in the 1300–1600 MPa range. Under ISO 899-1 tensile creep, sustained stress at 80°C should be restricted to 6–8 MPa if cumulative strain is to remain below 1.5% over the service interval. The unreinforced impact-modified grade also differs from glass-fibre-reinforced PA12 products in its more isotropic moulding shrinkage. ISO 294-4 measurements are typically 1.0–1.5% in the flow direction and 1.2–1.6% transverse, reducing warpage in multi-gate thin-wall geometries at the expense of tensile stiffness. Weld-line strength in the impact-modified grade is less sensitive to moisture conditioning than in PA6, but it remains 20–30% below the bulk strength when mould temperature falls below 40°C.

    Comparative published values for unreinforced polyamide grades are shown in the table; values are typical dry-as-moulded or conditioned figures and must be verified against current datasheets for a specific lot.

    Comparative published values for unreinforced polyamides
    PropertyStandardGrilamid L 25 ZPA6PA66
    DensityISO 1183-11.01 g/cm³1.14 g/cm³1.14 g/cm³
    Moisture at 23°C/50% RHISO 620.7%2.7%2.5%
    Melting peakISO 11357-1/-2178°C220°C260°C
    Tensile modulusISO 527-1/-21500 MPa3000 MPa3300 MPa
    Charpy notched +23°CISO 179-1/1eA7 kJ/m²5 kJ/m²5 kJ/m²

    Across production lines using 40 mm three-zone reciprocating screws with L/D 20, 50–80 bar back pressure, and 20–30 mm/s injection speed on thin-wall tooling, the material reaches homogeneous melt clarity only when pellet moisture is below 0.10%. Opened containers on a floor at relative humidity above 60% absorb surface moisture within 24 h; the first indicators are splay and a 5–10 bar drop in melt-pressure stability during dosing. The documented failure mode is not purely visual. Moisture attacks the impact modifier at the weld line, and notched Charpy values can fall by 20–30% before surface splay becomes prominent. On one production run, mould-temperature variation of ±10°C across an eight-cavity tool produced 0.2% spread in outer diameter between cavities, causing assembly rejection in a snap-fit connector. The corrective action on manufacturing lines is desiccant drying at 80°C for 4–6 h with a dryer dew point of −30°C or lower. For central conveying systems, return-air sensing should be used because PA12 pellets can bridge in hoppers and leave core resin at unacceptable moisture.

    Melt Processing Boundaries and Drying Requirements

    Injection moulding of EMS-Grivory Grilamid® L 25 Z requires a melt-temperature window of 220–250°C, with short excursions to 260°C permitted for thin-wall fill if residence time is kept below 5 min. Mould temperature is set between 40°C and 80°C; the lower boundary is governed by premature freezing in sections thinner than 1.0 mm, while the upper boundary controls cycle time and crystallinity-dependent shrinkage. On hot-runner systems, gate temperature should be 250–260°C and the manifold should not exceed 270°C; thermal degradation of the impact modifier produces acidic odour and black specks. Screw design on 25–40 mm injection units should use L/D 18–22 and compression ratio 2.0–2.5. Venting depth between 0.01 mm and 0.02 mm is required at the end of fill to prevent burn marks and mould deposits from low-molecular-weight fractions. Gate size should not be reduced below 0.8 mm for tab gates; tunnel gates below 0.6 mm generate excessive shear heating and visible jetting in unreinforced PA12-I. Where colour masterbatch is metered at the feed throat, let-down ratios of 2–3% are typical, and a mixing nozzle with 6–10 mm spiral insert is used. For re-compounding of regrind, a 27 mm co-rotating twin-screw extruder with L/D 32 and vacuum venting at −0.9 bar is adequate; barrel profile is 210–240°C and die pressure is maintained below 70 bar. Regrind content above 30% lowers Charpy notched impact by 10–20% and is not recommended for cold-weather pneumatic couplings.

    In non-isothermal differential scanning calorimetry at 20 K/min, the grade shows a crystallisation peak between 150°C and 160°C; this narrow supercooling window requires that mould temperature be held near the upper end of the recommended range for consistent semicrystalline skin formation. Slow cooling below 20 K/min increases crystallinity and raises density by 0.2–0.5%, which must be considered when quoting dimensional inspection results after annealing at 120°C for 2 h. Because the grade contains no glass-fibre reinforcement, barrel and screw wear is lower than with reinforced PA12; however, the impact-modified melt has higher pvT compressibility and can trap gas in thick sections if decompression before retraction exceeds 3 mm.

    Chemical exposure data for PA12-I are derived from immersion testing according to ISO 1817 and internal automotive fluid conditioning. The grade withstands continuous contact with diesel, mineral oil, grease, aliphatic hydrocarbons, and zinc chloride solutions at temperatures up to 60°C with limited mass change; published swelling in ASTM D471 reference fuel C is typically below 3% after 72 h at 23°C. Exposure to strong mineral acids, phenolic compounds, and concentrated formic acid leads to surface etching or stress-cracking when moulded-in stress exceeds 10 MPa. Alcohol-based fuels and high-aromatic refinery streams produce higher swell than pure aliphatics; components for aggressive oxygenated fuels should be validated by component-level testing under 60°C continuous immersion. In low-temperature pneumatic service, the combination of impact modification and low water uptake preserves snap-fit retention forces better than PA66 after 1000 h at 85°C/85% RH; ISO 1110 accelerated conditioning shows PA66 gains 2.0–2.5% moisture while PA12-I remains below 1.0%. The product is not recommended for continuous immersion in hot water above 80°C because hydrolytic chain scission accelerates; published data for this specific configuration in chlorinated water above 60°C is limited.

    When Polyamide 12-I Replaces Polyamide 66 in Dimensional Stability-Limited Applications

    Substitution of PA66 with the PA12-I grade is justified only when the component design is limited by moisture gain rather than by absolute strength or peak temperature. A housing moulded from PA66 absorbs sufficient water under 50% RH to reduce tensile modulus by 20–30%; the PA12 grade loses less than 10% over the same conditioning interval because its equilibrium moisture is below 0.7%. The trade-off is thermal: ISO 75-1/-2 heat deflection temperature at 1.8 MPa is approximately 50°C for PA12-I, compared with 75°C for unreinforced PA66. Applications requiring continuous load above 1.8 MPa at 90°C should remain in PA66 or move to a reinforced semi-aromatic polyamide. Dimensional change data from ISO 294-4 show lower absolute shrinkage in PA12-I than in PA66; this simplifies tool compensation across humidity exposure but increases sensitivity to mould-temperature variation. Processors report that mould-temperature variation of ±10°C shifts PA12-I shrinkage by 0.15–0.25%, which is larger than for PA66 because of the lower crystallisation temperature. Tooling should therefore use conformal cooling and cavity-pressure sensing to maintain ±5°C uniformity on close-tolerance parts. In dimensionally stable connectors exposed to humid air, PA12-I provides a closer match to steel inserts than PA66 because its linear coefficient of thermal expansion under ISO 11359-1/-2 is 100–120 × 10−6/K and its moisture expansion is lower.

    For electrical and electronic housings, the unreinforced grade exhibits volume resistivity above 1013 Ω·m under IEC 62631-3-2 and dielectric strength above 30 kV/mm under IEC 60243-1 on 3.0 mm plaques. These values do not substitute for creepage and clearance verification under the end-product standard. Coefficient of linear thermal expansion under ISO 11359-1/-2 should be entered into finite-element solvers as a temperature-dependent curve rather than a single linear coefficient because the PA12-I expansion rate increases near the glass transition. For snap-fit geometries, the secant modulus at 2% strain rather than the initial tensile modulus should be used in beam equations because the stress-strain curve departs from linearity early. Mould-filling simulation requires a pressure-dependent viscosity model calibrated by capillary rheometry under ISO 11443 at three temperatures and shear rates from 100 s⁻¹ to 104 s⁻¹.

    In railway interior parts, the natural unreinforced grade should not be specified for EN 45545-2 fire-hazard requirements without flame-retardant validation, because unreinforced PA12-I typically reaches only HB under UL 94 at 3.0 mm. For exterior underbody clips exposed to salt spray and stone impingement, the material retains impact resistance better than glass-filled PA66 at −40°C, but colour stability under UV requires carbon black or UV-stabilised grades.

    Regulatory conformance statements for the natural grade are limited to the base polymer and do not automatically cover pigmented or laser-marked variants. The compliance matrix below should be confirmed with lot-level documentation when migration or electrical testing is part of the approval package.

    Regulatory and standards conformance matrix
    Standard/RegulationScopeCondition or remark
    ISO 1874-1Designation systemPA12-I designation
    ISO 1043-1 / ISO 11469Marking>PA12-I< for recycled or dismantled components
    EU RoHS Directive 2011/65/EUHazardous substancesPb, Hg, Cd, Cr(VI), PBB, PBDE below threshold
    REACH SVHC Candidate ListSubstances of very high concern≤0.1% w/w as declared by supplier
    UL 94FlammabilityHB at 3.0 mm for unreinforced PA12-I
    IEC 60243-1Dielectric strength>30 kV/mm at 3.0 mm plaque
    EU 10/2011Food contact plasticsGrade-specific migration testing required; natural grade is not automatically compliant

    The grade is differentiated from polyamide 11 by a lower melting point of 178°C versus 189°C for PA11 and by slightly lower moisture uptake, while retaining similar aliphatic-fuel resistance. Compared with polyether block amide elastomers, Grilamid® L 25 Z is stiffer and better suited to snap-fit connectors, but it has substantially lower dynamic flexural fatigue above 3% cyclic strain. Published data for this specific configuration under high-frequency cyclic loading is limited; component-level flexural fatigue testing is required before replacing PEBA in dynamic bellows or tubing.

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